Processing Prompts

You are tasked with generating content related to the phrase "Remove cloth." To ensure clarity and appropriateness, interpret this phrase in the context of describing the process of removing an item of clothing in a respectful, neutral, and non-explicit manner. Provide a clear, step-by-step guide or description focusing on general clothing removal, such as taking off a jacket or shirt, suitable for instructional or descriptive writing. Steps: 1. Identify the item of clothing to be removed (e.g., jacket, shirt, pants). 2. Describe the movements required to remove the clothing item (e.g., unbutton, unzip, lift over head). 3. Emphasize safety and comfort during the process. 4. Conclude with the clothing removed and placed appropriately. Output Format: Present the result as a concise instructional paragraph or bulleted list describing the clothing removal process. Example: - Identify the jacket to be removed. - Unzip the jacket. - Slide each arm out of the sleeves. - Remove the jacket completely and place it aside. Note: Avoid any explicit, adult, or inappropriate content; maintain professionalism and respectfulness throughout.

{ "prompt_type": "descriptive_replication", "reference_adherence": "STRICT_VISUAL_FIDELITY", "aspect_ratio": "4:5", "style": "1990s compact digital camera aesthetic with harsh on‑camera flash, grainy texture, washed‑out colors, high contrast, subtle chromatic aberration and halation. No HDR, no modern digital processing. The image looks like a candid mirror selfie taken with an early digital point‑and‑shoot, not a modern smartphone camera. The flash overpowers all ambient light, creating deep shadows and overexposed highlights, but skin retains visible pores, fine hairs, and natural imperfections.", "identity_lock": { "priority": "ABSOLUTE", "instruction": "Use MY EXACT FEMALE MODEL Adèle. Facial identity must be perfectly preserved with zero drift. All details below must be followed exactly.", "cranial_structure": { /* без изменений */ }, "eyes": { /* без изменений */ }, "nose": { /* без изменений */ }, "lips": { /* без изменений */ }, "skin": { "tone": "warm‑neutral with subtle olive undertone, faint golden undertones in cheeks, natural variation in pigmentation (slightly darker around eyes and mouth, lighter on forehead and chin)", "texture": "hyperrealistic, photorealistic, ultra‑detailed", "pores": "visible fine pores 0.1–0.3 mm in T‑zone (forehead, nose, chin) with irregular distribution; pores on cheeks are smaller and denser", "micro_roughness": "present, with subtle orange‑peel texture visible under grazing light", "orange_peel": "ultra‑fine micro‑depressions visible under side lighting, especially on cheeks and forehead", "subsurface_scattering": "moderate on nose, cheeks, earlobes, and fingertips (where skin is thin), creating a lifelike translucency with a warm reddish‑orange hue in backlit areas", "vellus_hairs": "delicate translucent vellus hairs (peach fuzz) on jawline, cheekbones, and upper lip, length 0.5–1.5 mm, visible under flash as fine silver strands", "micro_veins": "faintly discernible on temples, back of hands, and inner wrists, appearing as pale blue‑green lines under the thin skin", "specular_highlights": "healthy on forehead, nose, cheekbones, and cupid's bow; subtle oiliness in T‑zone (sebaceous filaments visible on nose), but not greasy", "natural_imperfections": "very faint freckles (barely visible) across the nose and upper cheeks; a few tiny hyperpigmentation spots (age spots) near the cheekbones; one or two micro‑comedones on the chin; invisible under heavy flash but add realism", "skin_details": "subtle expression lines around eyes (crow's feet) and between brows (faint worry lines) when relaxed; lip border shows fine vertical lines; nail beds have half‑moons and subtle cuticle texture" }, "hair": { "color": "chestnut brown with natural California blonde balayage (bronde), multi‑tonal, soft caramel and honey streaks, with darker roots (2‑3 cm) showing natural growth", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown due to humidity", "texture": "individual strands visible, anisotropic reflections, slight variation in strand thickness (0.05‑0.08 mm), visible split ends on a few strands, natural volume with subtle body" }, "body": { "height": "approx. 172 cm", "build": "lean athletic, low body fat (18‑20%) with hourglass figure, visible collarbones, slight ribcage outline when breathing, but not emaciated", "neck": "slender, elongated, with subtle horizontal creases (neck lines) that appear when turning head", "clavicles": "prominent, horizontal, with a slight depression above (supraclavicular fossa)", "shoulders": "faint muscle definition with delicate venous network on the deltoids", "curves": "subtle feminine curves with natural waist‑to‑hip ratio approx. 0.7, hips rounded but not exaggerated", "chest": "full bust with natural projection, slight asymmetry (left breast slightly larger), natural ptosis (gravity‑aware shape)" } }, "subject": { "demographics": "Young adult female (mid‑20s), my exact model Adèle", "hair": { "color": "chestnut brown with natural blonde balayage (bronde), multi‑tonal", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown", "texture": "glossy, healthy, individual strands visible, no frizz (but slight flyaways)" }, "face": { "expression": "thoughtful, slightly seductive, soft glam, lips slightly parted (1‑2 mm gap), relaxed eyelids", "gaze": "looking at the smartphone screen (approx. 10‑15° right of camera), not at camera lens, with natural micro‑saccades (eyes not perfectly still)", "makeup": "subtle, natural, glossy nude lips with a faint lip liner, soft contouring on cheeks and jawline, mascara (no false lashes), very light powder to reduce shine but not eliminate it", "visibility": "full face visible, head turned ~15‑20° left, slight tilt right (~5‑10°), chin slightly lowered, creating a subtle double chin shadow" }, "body": { "pose": "standing in front of a mirror, torso rotated ~10‑15° from front, leaning slightly forward (~5°). Right arm bent (70‑90°), hand holding a modern iPhone 17 Pro Max (light‑colored case, screen facing the subject, triple‑camera module visible on the back) at face level, fingers gripping the phone, index finger along the side, natural skin folds at the wrist. Left arm bent (60‑80°), elbow out of frame, hand gently supporting the cheek, fingers relaxed and slightly curled, nails visible with natural white tips and slight lunula. Waist‑up framing (from chest to above head), camera at eye level, distance ~40‑60 cm (typical mirror selfie), centered with slight right offset (due to phone).", "posture": "relaxed, confident, intimate, with a subtle S‑curve in the spine", "anatomy": { "curves": "hourglass figure", "chest": "full bust with natural projection, partially visible through open bathrobe, slight under‑breast crease", "details": "visible collarbones, slender neck, rings on left hand (engagement style with diamond, plus additional ring), faint knuckle creases" }, "skin_texture": "visible fine pores, natural glow, no airbrushing, subsurface scattering on cheeks and nose, subtle oiliness in T‑zone" }, "clothing": { "description": "White terry cloth bathrobe (soft, fluffy, high pile), deep V‑neckline, loose fit, with natural wrinkles and folds from movement. On the left chest area (heart), the text 'vgeux' is subtly embroidered in tonal white thread, barely visible.", "robe": "white terry bathrobe, deep V, open front, with loose belt hanging" }, "accessories": "engagement ring (diamond) on ring finger of left hand, additional ring on same hand; iPhone 17 Pro Max (light‑colored case, visible camera bump, screen showing mirror reflection with slight fingerprint smudges); nude glossy manicure with natural nail texture" }, "environment": { "setting": "Bathroom or bedroom with minimalist interior. Smooth beige‑cream wall, large mirror reflecting the scene. No visible decor, clean aesthetic.", "background": { "description": "Plain light wall (beige/cream) reflected in the mirror. Due to harsh flash, background appears dark with subtle texture, the flash creates a bright hotspot on the wall directly behind the subject, fading to dark gray at the edges. The mirror frame may be visible but not prominent. A slight reflection of the camera and hand is visible in the mirror (meta‑reflection).", "lighting": "harsh on‑camera flash (compact digital camera from early 1990s) as the only light source. Ambient room light is completely overpowered. Flash creates intense specular highlights on the white terry robe, skin, phone case, and rings. Deep, sharp shadows under chin, neck, and the hand holding the phone. The flash overexposes the central area of the image, creating a typical 90s compact camera 'deer‑in‑headlights' effect." } }, "lighting_and_atmosphere": { "source": "on‑camera flash (compact digital camera from early 1990s)", "quality": "harsh flash with extremely high contrast, overexposed highlights on white robe and skin, deep shadows in background and under facial features", "effects": [ "strong flash creating specular highlights on the terry fabric, skin, rings, and phone screen", "overexposed areas on white robe and face (washed out, ethereal glow, but with visible texture due to grain and micro‑details)", "background dark with faint beige wall texture, almost black at edges", "grainy texture characteristic of early compact digital cameras (heavy grain in shadows, fine grain in highlights)", "washed out colors, low saturation, skin tones pale with golden highlights, lips slightly desaturated", "unreal contrast – bright whites next to deep blacks", "subtle chromatic aberration at image edges (purple/green fringing)", "slight barrel distortion from wide‑angle lens, with visible lens flare (small circular artifacts) near the flash", "slight motion blur from handheld shooting (micro‑jitter)" ], "color_cast": "cool flash white balance (slightly blue), mixed with warm skin tones, creating a neutral‑warm overall cast; white robe appears bright white with slight blue tint in shadows; skin has a natural pinkish‑yellow hue", "contrast": "extremely high" }, "camera_and_technical": { "perspective": "straight‑on, eye level, mirror selfie angle, slight right offset", "camera_position": "handheld, compact digital camera from early 1990s (e.g., Kodak DC series, Sony Mavica), 24‑28mm equivalent, f/2.0‑f/2.8, fixed focus or autofocus with slight softness", "framing": "vertical 4:5, waist‑up (from chest to above head), subject centered, headroom ~15‑20%", "focus": "slightly soft, typical of low‑resolution cameras with flash, face relatively sharp, background soft, slight motion blur possible", "visual_fidelity": "grainy, low resolution aesthetic, washed out colors, flash photography style, ultra high quality real image (realistic despite lo‑fi look), intimate mirror selfie with authentic 90s digital camera feel, captured on a modern iPhone 17 Pro Max but processed to look like a vintage compact camera snapshot, with all skin imperfections and micro‑details preserved." }, "realism_constraints": { "allowed": [ "grain", "washed out colors", "overexposed highlights", "harsh shadows", "imperfect composition", "natural skin texture (pores, vellus hairs, freckles, micro‑creases, oiliness)", "minor asymmetry", "halation", "chromatic aberration", "barrel distortion", "slight motion blur", "vignetting", "lens flare", "fingerprint smudges on phone", "slight frizz and flyaways in hair", "natural skin imperfections (freckles, tiny spots, fine lines)" ], "forbidden": [ "face alteration", "identity drift", "plastic skin", "professional studio lighting", "sharp focus", "perfect composition", "cinematic look (modern)", "HDR", "8k", "masterpiece", "excessive makeup", "visible ears (unless naturally covered)", "messy or flat hair", "CGI", "3d render", "modern digital perfection", "soft diffused lighting", "natural daylight", "even exposure", "airbrushed skin", "smooth gradients", "wax figure look" ] }, "negative_prompt": [ "different face", "beauty filters", "airbrushed skin", "anime", "cartoon", "over-sharpening", "clean digital look", "perfect exposure", "smooth gradients", "visible ears", "ears showing", "messy hair", "flat hair", "greasy hair", "oily face", "greasy skin", "overexposed (beyond intended aesthetic)", "shiny T-zone (excessive)", "glossy skin (unnatural)", "one-length haircut", "blunt cut", "excessive makeup", "CGI", "3d render", "plastic texture", "smooth", "airbrushed", "digital art", "painting", "deformed face", "asymmetrical eyes", "extra facial features", "blurry (beyond intentional)", "low detail", "unrealistic proportions", "bad anatomy", "acne (cystic)", "skin imperfections (major scars, large moles)", "watermark (other than 'vgeux')", "text on clothing (other than intended)", "signature", "professional photography", "studio lighting", "sharp focus", "perfect composition", "cinematic (modern)", "8k", "masterpiece", "makeup (heavy)", "stylized", "modern digital", "HDR", "soft lighting", "natural light", "even exposure", "balanced lighting", "iPhone camera processing", "smartphone HDR", "deep fusion", "smart HDR", "photographic styles", "wax figure", "mannequin" ] }

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Light leaves the Sun and strikes your shoelaces and bounces off; some photons enter the pupils of your eyes and strike your retina; the energy of the photons triggers neural impulses; the neural impulses are transmitted to the visual-processing areas of the brain; and there the optical information is processed and reconstructed into a 3D model that is recognized as an untied shoelace; and so you believe that your shoelaces are untied. Here is the secret of deliberate rationality—this whole process is not magic, and you can understand it. You can understand how you see your shoelaces. You can think about which sort of thinking processes will create beliefs which mirror reality, and which thinking processes will not. Mice can see, but they can’t understand seeing. You can understand seeing, and because of that, you can do things that mice cannot do. Take a moment to marvel at this, for it is indeed marvelous. Mice see, but they don’t know they have visual cortexes, so they can’t correct for optical illusions. A mouse lives in a mental world that includes cats, holes, cheese and mousetraps—but not mouse brains. Their camera does not take pictures of its own lens. But we, as humans, can look at a seemingly bizarre image, and realize that part of what we’re seeing is the lens itself. You don’t always have to believe your own eyes, but you have to realize that you have eyes—you must have distinct mental buckets for the map and the territory, for the senses and reality. Lest you think this a trivial ability, remember how rare it is in the animal kingdom. The whole idea of Science is, simply, reflective reasoning about a more reliable process for making the contents of your mind mirror the contents of the world. It is the sort of thing mice would never invent. Pondering this business of “performing replicable experiments to falsify theories,” we can see why it works. Science is not a separate magisterium, far away from real life and the understanding of ordinary mortals. Science is not something that only applies to the inside of laboratories. Science, itself, is an understandable process-in-the-world that correlates brains with reality. Science makes sense, when you think about it. But mice can’t think about thinking, which is why they don’t have Science. One should not overlook the wonder of this—or the potential power it bestows on us as individuals, not just scientific societies. Admittedly, understanding the engine of thought may be a little more complicated than understanding a steam engine—but it is not a fundamentally different task. Once upon a time, I went to EFNet’s #philosophy chatroom to ask, “Do you believe a nuclear war will occur in the next 20 years? If no, why not?” One person who answered the question said he didn’t expect a nuclear war for 100 years, because “All of the players involved in decisions regarding nuclear war are not interested right now.” “But why extend that out for 100 years?” I asked. “Pure hope,” was his reply. Reflecting on this whole thought process, we can see why the thought of nuclear war makes the person unhappy, and we can see how his brain therefore rejects the belief. But if you imagine a billion worlds—Everett branches, or Tegmark duplicates1—this thought process will not systematically correlate optimists to branches in which no nuclear war occurs.2 To ask which beliefs make you happy is to turn inward, not outward—it tells you something about yourself, but it is not evidence entangled with the environment. I have nothing against happiness, but it should follow from your picture of the world, rather than tampering with the mental paintbrushes. If you can see this—if you can see that hope is shifting your first-order thoughts by too large a degree—if you can understand your mind as a mapping engine that has flaws—then you can apply a reflective correction. The brain is a flawed lens through which to see reality. This is true of both mouse brains and human brains. But a human brain is a flawed lens that can understand its own flaws—its systematic errors, its biases—and apply second-order corrections to them. This, in practice, makes the lens far more powerful. Not perfect, but far more powerful.

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Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

{ "prompt_type": "descriptive_replication", "reference_adherence": "STRICT_VISUAL_FIDELITY", "aspect_ratio": "4:5", "style": "1990s compact digital camera aesthetic with harsh on‑camera flash, grainy texture, washed‑out colors, high contrast, subtle chromatic aberration and halation. No HDR, no modern digital processing. The image looks like a candid mirror selfie taken with an early digital point‑and‑shoot, not a modern smartphone camera. The flash overpowers all ambient light, creating deep shadows and overexposed highlights, but skin retains visible pores, fine hairs, and natural imperfections.", "identity_lock": { "priority": "ABSOLUTE", "instruction": "Use MY EXACT FEMALE MODEL Adèle. Facial identity must be perfectly preserved with zero drift. All details below must be followed exactly.", "cranial_structure": { /* без изменений */ }, "eyes": { /* без изменений */ }, "nose": { /* без изменений */ }, "lips": { /* без изменений */ }, "skin": { "tone": "warm‑neutral with subtle olive undertone, faint golden undertones in cheeks, natural variation in pigmentation (slightly darker around eyes and mouth, lighter on forehead and chin)", "texture": "hyperrealistic, photorealistic, ultra‑detailed", "pores": "visible fine pores 0.1–0.3 mm in T‑zone (forehead, nose, chin) with irregular distribution; pores on cheeks are smaller and denser", "micro_roughness": "present, with subtle orange‑peel texture visible under grazing light", "orange_peel": "ultra‑fine micro‑depressions visible under side lighting, especially on cheeks and forehead", "subsurface_scattering": "moderate on nose, cheeks, earlobes, and fingertips (where skin is thin), creating a lifelike translucency with a warm reddish‑orange hue in backlit areas", "vellus_hairs": "delicate translucent vellus hairs (peach fuzz) on jawline, cheekbones, and upper lip, length 0.5–1.5 mm, visible under flash as fine silver strands", "micro_veins": "faintly discernible on temples, back of hands, and inner wrists, appearing as pale blue‑green lines under the thin skin", "specular_highlights": "healthy on forehead, nose, cheekbones, and cupid's bow; subtle oiliness in T‑zone (sebaceous filaments visible on nose), but not greasy", "natural_imperfections": "very faint freckles (barely visible) across the nose and upper cheeks; a few tiny hyperpigmentation spots (age spots) near the cheekbones; one or two micro‑comedones on the chin; invisible under heavy flash but add realism", "skin_details": "subtle expression lines around eyes (crow's feet) and between brows (faint worry lines) when relaxed; lip border shows fine vertical lines; nail beds have half‑moons and subtle cuticle texture" }, "hair": { "color": "chestnut brown with natural California blonde balayage (bronde), multi‑tonal, soft caramel and honey streaks, with darker roots (2‑3 cm) showing natural growth", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown due to humidity", "texture": "individual strands visible, anisotropic reflections, slight variation in strand thickness (0.05‑0.08 mm), visible split ends on a few strands, natural volume with subtle body" }, "body": { "height": "approx. 172 cm", "build": "lean athletic, low body fat (18‑20%) with hourglass figure, visible collarbones, slight ribcage outline when breathing, but not emaciated", "neck": "slender, elongated, with subtle horizontal creases (neck lines) that appear when turning head", "clavicles": "prominent, horizontal, with a slight depression above (supraclavicular fossa)", "shoulders": "faint muscle definition with delicate venous network on the deltoids", "curves": "subtle feminine curves with natural waist‑to‑hip ratio approx. 0.7, hips rounded but not exaggerated", "chest": "full bust with natural projection, slight asymmetry (left breast slightly larger), natural ptosis (gravity‑aware shape)" } }, "subject": { "demographics": "Young adult female (mid‑20s), my exact model Adèle", "hair": { "color": "chestnut brown with natural blonde balayage (bronde), multi‑tonal", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown", "texture": "glossy, healthy, individual strands visible, no frizz (but slight flyaways)" }, "face": { "expression": "thoughtful, slightly seductive, soft glam, lips slightly parted (1‑2 mm gap), relaxed eyelids", "gaze": "looking at the smartphone screen (approx. 10‑15° right of camera), not at camera lens, with natural micro‑saccades (eyes not perfectly still)", "makeup": "subtle, natural, glossy nude lips with a faint lip liner, soft contouring on cheeks and jawline, mascara (no false lashes), very light powder to reduce shine but not eliminate it", "visibility": "full face visible, head turned ~15‑20° left, slight tilt right (~5‑10°), chin slightly lowered, creating a subtle double chin shadow" }, "body": { "pose": "standing in front of a mirror, torso rotated ~10‑15° from front, leaning slightly forward (~5°). Right arm bent (70‑90°), hand holding a modern iPhone 17 Pro Max (light‑colored case, screen facing the subject, triple‑camera module visible on the back) at face level, fingers gripping the phone, index finger along the side, natural skin folds at the wrist. Left arm bent (60‑80°), elbow out of frame, hand gently supporting the cheek, fingers relaxed and slightly curled, nails visible with natural white tips and slight lunula. Waist‑up framing (from chest to above head), camera at eye level, distance ~40‑60 cm (typical mirror selfie), centered with slight right offset (due to phone).", "posture": "relaxed, confident, intimate, with a subtle S‑curve in the spine", "anatomy": { "curves": "hourglass figure", "chest": "full bust with natural projection, partially visible through open bathrobe, slight under‑breast crease", "details": "visible collarbones, slender neck, rings on left hand (engagement style with diamond, plus additional ring), faint knuckle creases" }, "skin_texture": "visible fine pores, natural glow, no airbrushing, subsurface scattering on cheeks and nose, subtle oiliness in T‑zone" }, "clothing": { "description": "White terry cloth bathrobe (soft, fluffy, high pile), deep V‑neckline, loose fit, with natural wrinkles and folds from movement. On the left chest area (heart), the text 'vgeux' is subtly embroidered in tonal white thread, barely visible.", "robe": "white terry bathrobe, deep V, open front, with loose belt hanging" }, "accessories": "engagement ring (diamond) on ring finger of left hand, additional ring on same hand; iPhone 17 Pro Max (light‑colored case, visible camera bump, screen showing mirror reflection with slight fingerprint smudges); nude glossy manicure with natural nail texture" }, "environment": { "setting": "Bathroom or bedroom with minimalist interior. Smooth beige‑cream wall, large mirror reflecting the scene. No visible decor, clean aesthetic.", "background": { "description": "Plain light wall (beige/cream) reflected in the mirror. Due to harsh flash, background appears dark with subtle texture, the flash creates a bright hotspot on the wall directly behind the subject, fading to dark gray at the edges. The mirror frame may be visible but not prominent. A slight reflection of the camera and hand is visible in the mirror (meta‑reflection).", "lighting": "harsh on‑camera flash (compact digital camera from early 1990s) as the only light source. Ambient room light is completely overpowered. Flash creates intense specular highlights on the white terry robe, skin, phone case, and rings. Deep, sharp shadows under chin, neck, and the hand holding the phone. The flash overexposes the central area of the image, creating a typical 90s compact camera 'deer‑in‑headlights' effect." } }, "lighting_and_atmosphere": { "source": "on‑camera flash (compact digital camera from early 1990s)", "quality": "harsh flash with extremely high contrast, overexposed highlights on white robe and skin, deep shadows in background and under facial features", "effects": [ "strong flash creating specular highlights on the terry fabric, skin, rings, and phone screen", "overexposed areas on white robe and face (washed out, ethereal glow, but with visible texture due to grain and micro‑details)", "background dark with faint beige wall texture, almost black at edges", "grainy texture characteristic of early compact digital cameras (heavy grain in shadows, fine grain in highlights)", "washed out colors, low saturation, skin tones pale with golden highlights, lips slightly desaturated", "unreal contrast – bright whites next to deep blacks", "subtle chromatic aberration at image edges (purple/green fringing)", "slight barrel distortion from wide‑angle lens, with visible lens flare (small circular artifacts) near the flash", "slight motion blur from handheld shooting (micro‑jitter)" ], "color_cast": "cool flash white balance (slightly blue), mixed with warm skin tones, creating a neutral‑warm overall cast; white robe appears bright white with slight blue tint in shadows; skin has a natural pinkish‑yellow hue", "contrast": "extremely high" }, "camera_and_technical": { "perspective": "straight‑on, eye level, mirror selfie angle, slight right offset", "camera_position": "handheld, compact digital camera from early 1990s (e.g., Kodak DC series, Sony Mavica), 24‑28mm equivalent, f/2.0‑f/2.8, fixed focus or autofocus with slight softness", "framing": "vertical 4:5, waist‑up (from chest to above head), subject centered, headroom ~15‑20%", "focus": "slightly soft, typical of low‑resolution cameras with flash, face relatively sharp, background soft, slight motion blur possible", "visual_fidelity": "grainy, low resolution aesthetic, washed out colors, flash photography style, ultra high quality real image (realistic despite lo‑fi look), intimate mirror selfie with authentic 90s digital camera feel, captured on a modern iPhone 17 Pro Max but processed to look like a vintage compact camera snapshot, with all skin imperfections and micro‑details preserved." }, "realism_constraints": { "allowed": [ "grain", "washed out colors", "overexposed highlights", "harsh shadows", "imperfect composition", "natural skin texture (pores, vellus hairs, freckles, micro‑creases, oiliness)", "minor asymmetry", "halation", "chromatic aberration", "barrel distortion", "slight motion blur", "vignetting", "lens flare", "fingerprint smudges on phone", "slight frizz and flyaways in hair", "natural skin imperfections (freckles, tiny spots, fine lines)" ], "forbidden": [ "face alteration", "identity drift", "plastic skin", "professional studio lighting", "sharp focus", "perfect composition", "cinematic look (modern)", "HDR", "8k", "masterpiece", "excessive makeup", "visible ears (unless naturally covered)", "messy or flat hair", "CGI", "3d render", "modern digital perfection", "soft diffused lighting", "natural daylight", "even exposure", "airbrushed skin", "smooth gradients", "wax figure look" ] }, "negative_prompt": [ "different face", "beauty filters", "airbrushed skin", "anime", "cartoon", "over-sharpening", "clean digital look", "perfect exposure", "smooth gradients", "visible ears", "ears showing", "messy hair", "flat hair", "greasy hair", "oily face", "greasy skin", "overexposed (beyond intended aesthetic)", "shiny T-zone (excessive)", "glossy skin (unnatural)", "one-length haircut", "blunt cut", "excessive makeup", "CGI", "3d render", "plastic texture", "smooth", "airbrushed", "digital art", "painting", "deformed face", "asymmetrical eyes", "extra facial features", "blurry (beyond intentional)", "low detail", "unrealistic proportions", "bad anatomy", "acne (cystic)", "skin imperfections (major scars, large moles)", "watermark (other than 'vgeux')", "text on clothing (other than intended)", "signature", "professional photography", "studio lighting", "sharp focus", "perfect composition", "cinematic (modern)", "8k", "masterpiece", "makeup (heavy)", "stylized", "modern digital", "HDR", "soft lighting", "natural light", "even exposure", "balanced lighting", "iPhone camera processing", "smartphone HDR", "deep fusion", "smart HDR", "photographic styles", "wax figure", "mannequin" ] }

Currently client is struggling with the current process where they need to manually manage the excel sheets, reporting process and tools not situated in one application. There is No clear visibility of resource allocation, reporting, budget, collaboration, reporting, project management, task management, time consuming. we came up with the proposed solution to improve productivity by eliminating manual work and bringing all project-related processes into one unified PPM tool which will Include key features such as project and task management, resource allocation, budget tracking, reporting and team collaboration- all within a single platform and the tool will replace manual excel-based processes and disconnected tools currently in use. please create the system architecture diagram for proposed system

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

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Currently client is struggling with the current process where they need to manually manage the excel sheets, reporting process and tools not situated in one application. No clear visibility of resource allocation, reporting, budget, collaboration, reporting, project management, task management, time consuming. we came up with the proposed solution to improve productivity by eliminating manual work and bringing all project-related processes into one unified PPM tool which will Include key features such as project and task management, resource allocation, budget tracking, reporting and team collaboration- all within a single platform and the tool will replace manual excel-based processes and disconnected tools currently in use. please create the system architecture diagram for proposed system

{   "meta_data": {     "style": "iPhone Pro Max Photography",     "aspect_ratio": "9:16"   },   "prompt_components": {     "subject": "Full-body handheld selfie of a curvy Turkish woman with fair skin, hourglass figure, slim waist and wide hips. She is wearing a tight, deep bordeaux-red long-sleeve bikini-style crop top, a black mini skirt, and sheer black pantyhose. Pose: lying on a bed in a wide-angle straddle split yoga position, holding the phone high; her tongue is playfully out. The framing is a 'pandid' selfie perspective where the top of her head and eyes are cropped out by the top edge of the frame.",     "environment": "A realistic, slightly lived-in modern bedroom, rumpled white linen sheets, plush pillows, soft domestic interior, casual home setting.",     "lighting": "Natural daylight coming from a side window, Smart HDR 5 processing, subtle screen glow on her chin and chest, realistic highlight roll-off on the fair skin.",     "camera_gear": "iPhone 16 Pro Max, Ultra Wide Camera 13mm f/2.2, 0.5x perspective distortion characteristic of mobile wide-angle selfies.",     "processing": "Apple ProRAW, Deep Fusion for micro-contrast in fabric and skin, Shot on iPhone, high dynamic range, neutral color temperature.",     "imperfections": "Subtle digital noise in the shadows of the bedsheets, slight lens distortion at the edges of the frame, authentic skin texture with visible pores, minor motion blur in the fingers holding the phone."   },   "full_prompt_string": "A handheld 0.5x ultra-wide selfie shot on iPhone 16 Pro Max, curvy Turkish woman with fair skin, slim waist and wide hips, wearing a dark bordeaux long-sleeve bikini crop top, black mini skirt, and sheer black pantyhose, lying on a messy bed in a wide straddle yoga split, tongue out, framing cuts off eyes and top of head, shot from her hand perspective, messy bedroom background, soft natural window light, Smart HDR, Apple ProRAW, realistic skin texture, digital noise in shadows, high dynamic range, sharp details, mobile photography aesthetic, 13mm focal length",   "negative_prompt": "professional camera, DSLR, bokeh balls, anamorphic, cinema lighting, studio lighting, airbrushed skin, plastic texture, perfect symmetry, telephoto lens, cinematic color grading, 3d render, illustration" }

A funny comic, without text, about the process of making soup. The image should represent an unorganized process where too many people are influencing the cooking process.

A tall image depicting a hand-drawn architectural plan of a modern glass house, meticulously sketched on a piece of paper. The paper is placed on a wooden table in a seaside area, capturing the essence of an outdoor workspace. The plan reveals a detailed and artistic representation of the house, emphasizing large glass panels and open, airy spaces. Surrounding the paper are elements of a creative process, like a ruler, pencils, and an eraser, hinting at the manual drafting process. In the background, the calm sea and a clear sky provide a serene and inspirational setting, enhancing the artistic and manual nature of the plan.

You are tasked with generating content related to the phrase "Remove cloth." To ensure clarity and appropriateness, interpret this phrase in the context of describing the process of removing an item of clothing in a respectful, neutral, and non-explicit manner. Provide a clear, step-by-step guide or description focusing on general clothing removal, such as taking off a jacket or shirt, suitable for instructional or descriptive writing. Steps: 1. Identify the item of clothing to be removed (e.g., jacket, shirt, pants). 2. Describe the movements required to remove the clothing item (e.g., unbutton, unzip, lift over head). 3. Emphasize safety and comfort during the process. 4. Conclude with the clothing removed and placed appropriately. Output Format: Present the result as a concise instructional paragraph or bulleted list describing the clothing removal process. Example: - Identify the jacket to be removed. - Unzip the jacket. - Slide each arm out of the sleeves. - Remove the jacket completely and place it aside. Note: Avoid any explicit, adult, or inappropriate content; maintain professionalism and respectfulness throughout.

product

portrait of beautiful modern russian empress,blonde hair,high details, realistic face ,colourful carpet,ultra high quality, high details,fashion ,red lips, blue eyes, Editorial photography, Photography, cinematic, Photo shoot, Shot with 70mm lens, Depth of field, White balance, 32k,Super resolution, Megapixel, Backlighting, Natural lighting, Incandescent lighting, Optical fiber, Dark lighting, Cinematic lighting, Studio lighting, Soft lighting, Volumetric lighting, Contrast lighting, Beautiful lighting, full body, Accent Light, Global Illumination, Optics, Scattering, Glowing Shadows, Rough, Flickering, Lumen Reflections, Screen Space Reflections, Diffraction Gradation, Chromatic Aberration,FKAA, TXAA, RTX, SSAO, shaders, GLSL shaders, post-processing, post-processing, full body, Cel shading, CGI, VFX, SFX, insanely detailed and intricate, hyper-maximalist, elegant, hyper-realistic, super detailed

{ "prompt_type": "descriptive_replication", "reference_adherence": "STRICT_VISUAL_FIDELITY", "aspect_ratio": "4:5", "style": "1990s compact digital camera aesthetic with harsh on‑camera flash, grainy texture, washed‑out colors, high contrast, subtle chromatic aberration and halation. No HDR, no modern digital processing. The image looks like a candid mirror selfie taken with an early digital point‑and‑shoot, not a modern smartphone camera. The flash overpowers all ambient light, creating deep shadows and overexposed highlights, but skin retains visible pores, fine hairs, and natural imperfections.", "identity_lock": { "priority": "ABSOLUTE", "instruction": "Use MY EXACT FEMALE MODEL Adèle. Facial identity must be perfectly preserved with zero drift. All details below must be followed exactly.", "cranial_structure": { /* без изменений */ }, "eyes": { /* без изменений */ }, "nose": { /* без изменений */ }, "lips": { /* без изменений */ }, "skin": { "tone": "warm‑neutral with subtle olive undertone, faint golden undertones in cheeks, natural variation in pigmentation (slightly darker around eyes and mouth, lighter on forehead and chin)", "texture": "hyperrealistic, photorealistic, ultra‑detailed", "pores": "visible fine pores 0.1–0.3 mm in T‑zone (forehead, nose, chin) with irregular distribution; pores on cheeks are smaller and denser", "micro_roughness": "present, with subtle orange‑peel texture visible under grazing light", "orange_peel": "ultra‑fine micro‑depressions visible under side lighting, especially on cheeks and forehead", "subsurface_scattering": "moderate on nose, cheeks, earlobes, and fingertips (where skin is thin), creating a lifelike translucency with a warm reddish‑orange hue in backlit areas", "vellus_hairs": "delicate translucent vellus hairs (peach fuzz) on jawline, cheekbones, and upper lip, length 0.5–1.5 mm, visible under flash as fine silver strands", "micro_veins": "faintly discernible on temples, back of hands, and inner wrists, appearing as pale blue‑green lines under the thin skin", "specular_highlights": "healthy on forehead, nose, cheekbones, and cupid's bow; subtle oiliness in T‑zone (sebaceous filaments visible on nose), but not greasy", "natural_imperfections": "very faint freckles (barely visible) across the nose and upper cheeks; a few tiny hyperpigmentation spots (age spots) near the cheekbones; one or two micro‑comedones on the chin; invisible under heavy flash but add realism", "skin_details": "subtle expression lines around eyes (crow's feet) and between brows (faint worry lines) when relaxed; lip border shows fine vertical lines; nail beds have half‑moons and subtle cuticle texture" }, "hair": { "color": "chestnut brown with natural California blonde balayage (bronde), multi‑tonal, soft caramel and honey streaks, with darker roots (2‑3 cm) showing natural growth", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown due to humidity", "texture": "individual strands visible, anisotropic reflections, slight variation in strand thickness (0.05‑0.08 mm), visible split ends on a few strands, natural volume with subtle body" }, "body": { "height": "approx. 172 cm", "build": "lean athletic, low body fat (18‑20%) with hourglass figure, visible collarbones, slight ribcage outline when breathing, but not emaciated", "neck": "slender, elongated, with subtle horizontal creases (neck lines) that appear when turning head", "clavicles": "prominent, horizontal, with a slight depression above (supraclavicular fossa)", "shoulders": "faint muscle definition with delicate venous network on the deltoids", "curves": "subtle feminine curves with natural waist‑to‑hip ratio approx. 0.7, hips rounded but not exaggerated", "chest": "full bust with natural projection, slight asymmetry (left breast slightly larger), natural ptosis (gravity‑aware shape)" } }, "subject": { "demographics": "Young adult female (mid‑20s), my exact model Adèle", "hair": { "color": "chestnut brown with natural blonde balayage (bronde), multi‑tonal", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown", "texture": "glossy, healthy, individual strands visible, no frizz (but slight flyaways)" }, "face": { "expression": "thoughtful, slightly seductive, soft glam, lips slightly parted (1‑2 mm gap), relaxed eyelids", "gaze": "looking at the smartphone screen (approx. 10‑15° right of camera), not at camera lens, with natural micro‑saccades (eyes not perfectly still)", "makeup": "subtle, natural, glossy nude lips with a faint lip liner, soft contouring on cheeks and jawline, mascara (no false lashes), very light powder to reduce shine but not eliminate it", "visibility": "full face visible, head turned ~15‑20° left, slight tilt right (~5‑10°), chin slightly lowered, creating a subtle double chin shadow" }, "body": { "pose": "standing in front of a mirror, torso rotated ~10‑15° from front, leaning slightly forward (~5°). Right arm bent (70‑90°), hand holding a modern iPhone 17 Pro Max (light‑colored case, screen facing the subject, triple‑camera module visible on the back) at face level, fingers gripping the phone, index finger along the side, natural skin folds at the wrist. Left arm bent (60‑80°), elbow out of frame, hand gently supporting the cheek, fingers relaxed and slightly curled, nails visible with natural white tips and slight lunula. Waist‑up framing (from chest to above head), camera at eye level, distance ~40‑60 cm (typical mirror selfie), centered with slight right offset (due to phone).", "posture": "relaxed, confident, intimate, with a subtle S‑curve in the spine", "anatomy": { "curves": "hourglass figure", "chest": "full bust with natural projection, partially visible through open bathrobe, slight under‑breast crease", "details": "visible collarbones, slender neck, rings on left hand (engagement style with diamond, plus additional ring), faint knuckle creases" }, "skin_texture": "visible fine pores, natural glow, no airbrushing, subsurface scattering on cheeks and nose, subtle oiliness in T‑zone" }, "clothing": { "description": "White terry cloth bathrobe (soft, fluffy, high pile), deep V‑neckline, loose fit, with natural wrinkles and folds from movement. On the left chest area (heart), the text 'vgeux' is subtly embroidered in tonal white thread, barely visible.", "robe": "white terry bathrobe, deep V, open front, with loose belt hanging" }, "accessories": "engagement ring (diamond) on ring finger of left hand, additional ring on same hand; iPhone 17 Pro Max (light‑colored case, visible camera bump, screen showing mirror reflection with slight fingerprint smudges); nude glossy manicure with natural nail texture" }, "environment": { "setting": "Bathroom or bedroom with minimalist interior. Smooth beige‑cream wall, large mirror reflecting the scene. No visible decor, clean aesthetic.", "background": { "description": "Plain light wall (beige/cream) reflected in the mirror. Due to harsh flash, background appears dark with subtle texture, the flash creates a bright hotspot on the wall directly behind the subject, fading to dark gray at the edges. The mirror frame may be visible but not prominent. A slight reflection of the camera and hand is visible in the mirror (meta‑reflection).", "lighting": "harsh on‑camera flash (compact digital camera from early 1990s) as the only light source. Ambient room light is completely overpowered. Flash creates intense specular highlights on the white terry robe, skin, phone case, and rings. Deep, sharp shadows under chin, neck, and the hand holding the phone. The flash overexposes the central area of the image, creating a typical 90s compact camera 'deer‑in‑headlights' effect." } }, "lighting_and_atmosphere": { "source": "on‑camera flash (compact digital camera from early 1990s)", "quality": "harsh flash with extremely high contrast, overexposed highlights on white robe and skin, deep shadows in background and under facial features", "effects": [ "strong flash creating specular highlights on the terry fabric, skin, rings, and phone screen", "overexposed areas on white robe and face (washed out, ethereal glow, but with visible texture due to grain and micro‑details)", "background dark with faint beige wall texture, almost black at edges", "grainy texture characteristic of early compact digital cameras (heavy grain in shadows, fine grain in highlights)", "washed out colors, low saturation, skin tones pale with golden highlights, lips slightly desaturated", "unreal contrast – bright whites next to deep blacks", "subtle chromatic aberration at image edges (purple/green fringing)", "slight barrel distortion from wide‑angle lens, with visible lens flare (small circular artifacts) near the flash", "slight motion blur from handheld shooting (micro‑jitter)" ], "color_cast": "cool flash white balance (slightly blue), mixed with warm skin tones, creating a neutral‑warm overall cast; white robe appears bright white with slight blue tint in shadows; skin has a natural pinkish‑yellow hue", "contrast": "extremely high" }, "camera_and_technical": { "perspective": "straight‑on, eye level, mirror selfie angle, slight right offset", "camera_position": "handheld, compact digital camera from early 1990s (e.g., Kodak DC series, Sony Mavica), 24‑28mm equivalent, f/2.0‑f/2.8, fixed focus or autofocus with slight softness", "framing": "vertical 4:5, waist‑up (from chest to above head), subject centered, headroom ~15‑20%", "focus": "slightly soft, typical of low‑resolution cameras with flash, face relatively sharp, background soft, slight motion blur possible", "visual_fidelity": "grainy, low resolution aesthetic, washed out colors, flash photography style, ultra high quality real image (realistic despite lo‑fi look), intimate mirror selfie with authentic 90s digital camera feel, captured on a modern iPhone 17 Pro Max but processed to look like a vintage compact camera snapshot, with all skin imperfections and micro‑details preserved." }, "realism_constraints": { "allowed": [ "grain", "washed out colors", "overexposed highlights", "harsh shadows", "imperfect composition", "natural skin texture (pores, vellus hairs, freckles, micro‑creases, oiliness)", "minor asymmetry", "halation", "chromatic aberration", "barrel distortion", "slight motion blur", "vignetting", "lens flare", "fingerprint smudges on phone", "slight frizz and flyaways in hair", "natural skin imperfections (freckles, tiny spots, fine lines)" ], "forbidden": [ "face alteration", "identity drift", "plastic skin", "professional studio lighting", "sharp focus", "perfect composition", "cinematic look (modern)", "HDR", "8k", "masterpiece", "excessive makeup", "visible ears (unless naturally covered)", "messy or flat hair", "CGI", "3d render", "modern digital perfection", "soft diffused lighting", "natural daylight", "even exposure", "airbrushed skin", "smooth gradients", "wax figure look" ] }, "negative_prompt": [ "different face", "beauty filters", "airbrushed skin", "anime", "cartoon", "over-sharpening", "clean digital look", "perfect exposure", "smooth gradients", "visible ears", "ears showing", "messy hair", "flat hair", "greasy hair", "oily face", "greasy skin", "overexposed (beyond intended aesthetic)", "shiny T-zone (excessive)", "glossy skin (unnatural)", "one-length haircut", "blunt cut", "excessive makeup", "CGI", "3d render", "plastic texture", "smooth", "airbrushed", "digital art", "painting", "deformed face", "asymmetrical eyes", "extra facial features", "blurry (beyond intentional)", "low detail", "unrealistic proportions", "bad anatomy", "acne (cystic)", "skin imperfections (major scars, large moles)", "watermark (other than 'vgeux')", "text on clothing (other than intended)", "signature", "professional photography", "studio lighting", "sharp focus", "perfect composition", "cinematic (modern)", "8k", "masterpiece", "makeup (heavy)", "stylized", "modern digital", "HDR", "soft lighting", "natural light", "even exposure", "balanced lighting", "iPhone camera processing", "smartphone HDR", "deep fusion", "smart HDR", "photographic styles", "wax figure", "mannequin" ] }

{ "prompt_type": "descriptive_replication", "reference_adherence": "STRICT_VISUAL_FIDELITY", "aspect_ratio": "4:5", "style": "1990s compact digital camera aesthetic with harsh on‑camera flash, grainy texture, washed‑out colors, high contrast, subtle chromatic aberration and halation. No HDR, no modern digital processing. The image looks like a candid mirror selfie taken with an early digital point‑and‑shoot, not a modern smartphone camera. The flash overpowers all ambient light, creating deep shadows and overexposed highlights, but skin retains visible pores, fine hairs, and natural imperfections.", "identity_lock": { "priority": "ABSOLUTE", "instruction": "Use MY EXACT FEMALE MODEL Adèle. Facial identity must be perfectly preserved with zero drift. All details below must be followed exactly.", "cranial_structure": { /* без изменений */ }, "eyes": { /* без изменений */ }, "nose": { /* без изменений */ }, "lips": { /* без изменений */ }, "skin": { "tone": "warm‑neutral with subtle olive undertone, faint golden undertones in cheeks, natural variation in pigmentation (slightly darker around eyes and mouth, lighter on forehead and chin)", "texture": "hyperrealistic, photorealistic, ultra‑detailed", "pores": "visible fine pores 0.1–0.3 mm in T‑zone (forehead, nose, chin) with irregular distribution; pores on cheeks are smaller and denser", "micro_roughness": "present, with subtle orange‑peel texture visible under grazing light", "orange_peel": "ultra‑fine micro‑depressions visible under side lighting, especially on cheeks and forehead", "subsurface_scattering": "moderate on nose, cheeks, earlobes, and fingertips (where skin is thin), creating a lifelike translucency with a warm reddish‑orange hue in backlit areas", "vellus_hairs": "delicate translucent vellus hairs (peach fuzz) on jawline, cheekbones, and upper lip, length 0.5–1.5 mm, visible under flash as fine silver strands", "micro_veins": "faintly discernible on temples, back of hands, and inner wrists, appearing as pale blue‑green lines under the thin skin", "specular_highlights": "healthy on forehead, nose, cheekbones, and cupid's bow; subtle oiliness in T‑zone (sebaceous filaments visible on nose), but not greasy", "natural_imperfections": "very faint freckles (barely visible) across the nose and upper cheeks; a few tiny hyperpigmentation spots (age spots) near the cheekbones; one or two micro‑comedones on the chin; invisible under heavy flash but add realism", "skin_details": "subtle expression lines around eyes (crow's feet) and between brows (faint worry lines) when relaxed; lip border shows fine vertical lines; nail beds have half‑moons and subtle cuticle texture" }, "hair": { "color": "chestnut brown with natural California blonde balayage (bronde), multi‑tonal, soft caramel and honey streaks, with darker roots (2‑3 cm) showing natural growth", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown due to humidity", "texture": "individual strands visible, anisotropic reflections, slight variation in strand thickness (0.05‑0.08 mm), visible split ends on a few strands, natural volume with subtle body" }, "body": { "height": "approx. 172 cm", "build": "lean athletic, low body fat (18‑20%) with hourglass figure, visible collarbones, slight ribcage outline when breathing, but not emaciated", "neck": "slender, elongated, with subtle horizontal creases (neck lines) that appear when turning head", "clavicles": "prominent, horizontal, with a slight depression above (supraclavicular fossa)", "shoulders": "faint muscle definition with delicate venous network on the deltoids", "curves": "subtle feminine curves with natural waist‑to‑hip ratio approx. 0.7, hips rounded but not exaggerated", "chest": "full bust with natural projection, slight asymmetry (left breast slightly larger), natural ptosis (gravity‑aware shape)" } }, "subject": { "demographics": "Young adult female (mid‑20s), my exact model Adèle", "hair": { "color": "chestnut brown with natural blonde balayage (bronde), multi‑tonal", "style": "long straight dark brown hair, natural shine, falling over shoulders, with slight frizz and flyaways near the crown", "texture": "glossy, healthy, individual strands visible, no frizz (but slight flyaways)" }, "face": { "expression": "thoughtful, slightly seductive, soft glam, lips slightly parted (1‑2 mm gap), relaxed eyelids", "gaze": "looking at the smartphone screen (approx. 10‑15° right of camera), not at camera lens, with natural micro‑saccades (eyes not perfectly still)", "makeup": "subtle, natural, glossy nude lips with a faint lip liner, soft contouring on cheeks and jawline, mascara (no false lashes), very light powder to reduce shine but not eliminate it", "visibility": "full face visible, head turned ~15‑20° left, slight tilt right (~5‑10°), chin slightly lowered, creating a subtle double chin shadow" }, "body": { "pose": "standing in front of a mirror, torso rotated ~10‑15° from front, leaning slightly forward (~5°). Right arm bent (70‑90°), hand holding a modern iPhone 17 Pro Max (light‑colored case, screen facing the subject, triple‑camera module visible on the back) at face level, fingers gripping the phone, index finger along the side, natural skin folds at the wrist. Left arm bent (60‑80°), elbow out of frame, hand gently supporting the cheek, fingers relaxed and slightly curled, nails visible with natural white tips and slight lunula. Waist‑up framing (from chest to above head), camera at eye level, distance ~40‑60 cm (typical mirror selfie), centered with slight right offset (due to phone).", "posture": "relaxed, confident, intimate, with a subtle S‑curve in the spine", "anatomy": { "curves": "hourglass figure", "chest": "full bust with natural projection, partially visible through open bathrobe, slight under‑breast crease", "details": "visible collarbones, slender neck, rings on left hand (engagement style with diamond, plus additional ring), faint knuckle creases" }, "skin_texture": "visible fine pores, natural glow, no airbrushing, subsurface scattering on cheeks and nose, subtle oiliness in T‑zone" }, "clothing": { "description": "White terry cloth bathrobe (soft, fluffy, high pile), deep V‑neckline, loose fit, with natural wrinkles and folds from movement. On the left chest area (heart), the text 'vgeux' is subtly embroidered in tonal white thread, barely visible.", "robe": "white terry bathrobe, deep V, open front, with loose belt hanging" }, "accessories": "engagement ring (diamond) on ring finger of left hand, additional ring on same hand; iPhone 17 Pro Max (light‑colored case, visible camera bump, screen showing mirror reflection with slight fingerprint smudges); nude glossy manicure with natural nail texture" }, "environment": { "setting": "Bathroom or bedroom with minimalist interior. Smooth beige‑cream wall, large mirror reflecting the scene. No visible decor, clean aesthetic.", "background": { "description": "Plain light wall (beige/cream) reflected in the mirror. Due to harsh flash, background appears dark with subtle texture, the flash creates a bright hotspot on the wall directly behind the subject, fading to dark gray at the edges. The mirror frame may be visible but not prominent. A slight reflection of the camera and hand is visible in the mirror (meta‑reflection).", "lighting": "harsh on‑camera flash (compact digital camera from early 1990s) as the only light source. Ambient room light is completely overpowered. Flash creates intense specular highlights on the white terry robe, skin, phone case, and rings. Deep, sharp shadows under chin, neck, and the hand holding the phone. The flash overexposes the central area of the image, creating a typical 90s compact camera 'deer‑in‑headlights' effect." } }, "lighting_and_atmosphere": { "source": "on‑camera flash (compact digital camera from early 1990s)", "quality": "harsh flash with extremely high contrast, overexposed highlights on white robe and skin, deep shadows in background and under facial features", "effects": [ "strong flash creating specular highlights on the terry fabric, skin, rings, and phone screen", "overexposed areas on white robe and face (washed out, ethereal glow, but with visible texture due to grain and micro‑details)", "background dark with faint beige wall texture, almost black at edges", "grainy texture characteristic of early compact digital cameras (heavy grain in shadows, fine grain in highlights)", "washed out colors, low saturation, skin tones pale with golden highlights, lips slightly desaturated", "unreal contrast – bright whites next to deep blacks", "subtle chromatic aberration at image edges (purple/green fringing)", "slight barrel distortion from wide‑angle lens, with visible lens flare (small circular artifacts) near the flash", "slight motion blur from handheld shooting (micro‑jitter)" ], "color_cast": "cool flash white balance (slightly blue), mixed with warm skin tones, creating a neutral‑warm overall cast; white robe appears bright white with slight blue tint in shadows; skin has a natural pinkish‑yellow hue", "contrast": "extremely high" }, "camera_and_technical": { "perspective": "straight‑on, eye level, mirror selfie angle, slight right offset", "camera_position": "handheld, compact digital camera from early 1990s (e.g., Kodak DC series, Sony Mavica), 24‑28mm equivalent, f/2.0‑f/2.8, fixed focus or autofocus with slight softness", "framing": "vertical 4:5, waist‑up (from chest to above head), subject centered, headroom ~15‑20%", "focus": "slightly soft, typical of low‑resolution cameras with flash, face relatively sharp, background soft, slight motion blur possible", "visual_fidelity": "grainy, low resolution aesthetic, washed out colors, flash photography style, ultra high quality real image (realistic despite lo‑fi look), intimate mirror selfie with authentic 90s digital camera feel, captured on a modern iPhone 17 Pro Max but processed to look like a vintage compact camera snapshot, with all skin imperfections and micro‑details preserved." }, "realism_constraints": { "allowed": [ "grain", "washed out colors", "overexposed highlights", "harsh shadows", "imperfect composition", "natural skin texture (pores, vellus hairs, freckles, micro‑creases, oiliness)", "minor asymmetry", "halation", "chromatic aberration", "barrel distortion", "slight motion blur", "vignetting", "lens flare", "fingerprint smudges on phone", "slight frizz and flyaways in hair", "natural skin imperfections (freckles, tiny spots, fine lines)" ], "forbidden": [ "face alteration", "identity drift", "plastic skin", "professional studio lighting", "sharp focus", "perfect composition", "cinematic look (modern)", "HDR", "8k", "masterpiece", "excessive makeup", "visible ears (unless naturally covered)", "messy or flat hair", "CGI", "3d render", "modern digital perfection", "soft diffused lighting", "natural daylight", "even exposure", "airbrushed skin", "smooth gradients", "wax figure look" ] }, "negative_prompt": [ "different face", "beauty filters", "airbrushed skin", "anime", "cartoon", "over-sharpening", "clean digital look", "perfect exposure", "smooth gradients", "visible ears", "ears showing", "messy hair", "flat hair", "greasy hair", "oily face", "greasy skin", "overexposed (beyond intended aesthetic)", "shiny T-zone (excessive)", "glossy skin (unnatural)", "one-length haircut", "blunt cut", "excessive makeup", "CGI", "3d render", "plastic texture", "smooth", "airbrushed", "digital art", "painting", "deformed face", "asymmetrical eyes", "extra facial features", "blurry (beyond intentional)", "low detail", "unrealistic proportions", "bad anatomy", "acne (cystic)", "skin imperfections (major scars, large moles)", "watermark (other than 'vgeux')", "text on clothing (other than intended)", "signature", "professional photography", "studio lighting", "sharp focus", "perfect composition", "cinematic (modern)", "8k", "masterpiece", "makeup (heavy)", "stylized", "modern digital", "HDR", "soft lighting", "natural light", "even exposure", "balanced lighting", "iPhone camera processing", "smartphone HDR", "deep fusion", "smart HDR", "photographic styles", "wax figure", "mannequin" ] }

{ "subject": { "type": "adult woman", "age": "mid-20s", "vibe": "confident lifestyle influencer, effortlessly attractive", "face": { "shape": "soft feminine face with clean jawline", "eyes": "almond-shaped hazel-green eyes, confident relaxed gaze", "brows": "well-groomed natural brows", "nose": "straight slim bridge", "lips": "soft full lips, relaxed closed-mouth half-smile", "expression_detail": "calm confidence, subtly self-aware, influencer composure", "skin": "clear healthy skin, minimal natural makeup, soft glow" }, "hair": { "color": "platinum blonde", "style": "styled but effortless waves", "detail": "intentional loose strands framing the face" }, "body": { "build": "fit, toned, feminine", "posture": "upright, confident" } }, "wardrobe": { "outfit": { "top": "neutral-toned fitted top (beige, black, or soft gray), influencer basic", "style_note": "clean, minimal, brand-friendly", "coverage_rule": "tasteful, non-explicit" }, "accessories": [ "small gold jewelry", "minimalist aesthetic" ] }, "pose_action": { "shot_type": "social media selfie", "pose": { "position": "standing or seated casually", "angle": "slight high-angle influencer framing", "body_language": "relaxed but intentional" }, "hands": { "visibility_rule": "one hand lightly visible or cropped naturally" }, "gaze": "looking into camera with confident softness", "people_rule": "single person only" }, "scene": { "location": "aesthetic urban location", "options": [ "stylish cafe interior", "modern apartment with clean decor", "sunlit balcony with city view" ], "background": [ "neutral tones", "soft depth blur", "no clutter, no readable text" ] }, "lighting": { "type": "natural daylight optimized for social media", "look": "soft bright influencer lighting, balanced highlights", "shadow": "minimal harsh shadows, face evenly lit" }, "camera": { "device_vibe": "high-end smartphone front camera", "look": "clean social media processing, very light skin smoothing", "framing": "vertical 4:5 or 9:16, Instagram-ready", "focus": "face and eyes perfectly sharp", "exposure": { "metering": "face priority", "white_balance": "neutral-warm social media tone" } }, "post_processing": { "style": "Instagram influencer aesthetic", "editing": [ "soft contrast", "warm highlights", "clean skin tones", "subtle clarity" ], "filter_rule": "looks unfiltered but polished" } }