A primary Prompts

"Ultra-realistic, Highly Detailed Digital Painting / Photorealistic Illustration of Pierre Louis Dulong" Image Type: Ultra-realistic digital painting / Photorealistic illustration. (This clarifies the artistic medium, rather than a literal photograph). Overall Artistic Style: Highly detailed, reminiscent of a classical historical portrait, specifically a hand-colored engraving or lithograph. The rendering should achieve photorealistic quality for the subject's features while retaining the characteristic texture and coloring of such historical artworks, with a rich, almost cinematic illustrative quality. Likeness: Very strong and precise likeness to the provided historical portrait of Pierre Louis Dulong . Lighting: Soft, even, and natural-looking light, similar to an old studio portrait setup. The main light source should be subtly from the front-left or front-right, gently highlighting facial contours. Gentle fill light should soften any shadows. Avoid harsh shadows or overexposure. Depth of Field: Shallow depth of field to ensure the subject's face is in crisp, primary focus, with a softly blurred background that does not distract. Color Palette: Natural, rich, and historically appropriate colors. Emphasize warm yet slightly muted skin tones, vibrant deep blue eyes, and deep, textured clothing colors consistent with the original historical rendering. Subject Details: Age: Depicted as a man in his late 40s to early 50s. Expression: Calm, discerning, and contemplative. A dignified and intelligent gaze directed straight towards the viewer. Face Shape: Rounded but well-defined, with a strong, clean jawline. Hair: Color: Light ash blonde or rich golden-blonde, with subtle natural highlights and tonal variations. Style: Very thick, distinctly wavy to curly, appearing full around the head and ears. It should not be strictly swept back but rather voluminous and natural, as seen in the reference image. Sideburns: Very dense and full, extending low to cover a significant portion of the cheek, with defined but not razor-sharp edges, conveying a natural, bushy volume as in the original. Eyes: Color: Strikingly bright, deep blue, with clear whites and a focused pupil. Shape: Wide and slightly rounded, with an intelligent and direct gaze. Eyebrows: Moderately thick, naturally arched, and neatly groomed, precisely matching the hair color, enhancing the eye's expression. Nose: Straight, with a slightly broad bridge and a softly rounded tip. It should appear strong and proportional to his face. Mouth and Lips: Medium-full lips, naturally shaped, with a neutral to slightly contemplative expression, showing subtle definition. Chin: Clearly defined and proportional, projecting slightly, contributing to a strong and somewhat squarish lower face. Facial Pose: Direct frontal view, with a very subtle (1-2 degree) tilt clockwise, precisely mimicking the angle in the reference image. Clothing Details: Coat: A single-breasted (or not visibly double-breasted) wool frock coat in a deep, muted burgundy (dark reddish-purple) or deep maroon color. The fabric should exhibit a fine, tight, textured weave, characteristic of historical prints (e.g., a subtle stippled or cross-hatched appearance), not a smooth modern fabric. The lapels should be broad and well-defined. Cravat/Collar: A pristine white, high, stiff linen cravat or stock, wrapped neatly and tightly around the neck. Inner Garments/Tie: A small visible portion of a dark inner vest or waistcoat. A striped tie, with vertical stripes in dark, muted colors (e.g., dark red and brown), should be visible at the neck opening. Background & Atmosphere: Background: A soft, plain very light blue-grey background. Crucially, the background should feature a distinct stippled or cross-hatched texture, characteristic of historical engravings or lithographs, rather than a smooth, seamless sky. There should be minimal or no noticeable gradual shading effects. Overall Mood/Atmosphere: Calm, confident, and contemplative, conveying a sense of intellectual dignity and solemnity. Rendering Quality (Crucial for replication): Resolution: 8K resolution. Detail: Extreme textural detail for all elements: individual strands of hair, realistic skin texture (portraying it as a finely rendered surface, not smooth plastic), and the intricate weave/texture of his clothing. Color Gradations: Natural and subtle color gradations within the chosen artistic style. Lighting Definition: Clear and well-defined lighting that shapes the forms without harshness. Focus: A shallow depth of field to keep the primary focus on the subject.

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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"priority_order": [ "internal_presence", "emotional_projection", "tactile_projection", "micro_expression", "eye_behavior", "face_identity", "Medio ambiente" ], "global_rule": "ANYTHING_THAT_COMPETES_WITH_PRESENCE_IS_REDUCED" }, "step_1_reduce_ambient_light": { "habilitado": true, "global_ambient_reduction": "-18_PERCENT", "background_luminance_priority": "VERY_LOW", "face_luminance_protection": true, "identity_safe": true }, "step_2_soft_shadow_depth": { "habilitado": true, "target_areas": ["mejillas","cuello","línea de la mandíbula"], "shadow_intensity": "+5_PERCENT", "shadow_type": "SOFT_GRADUAL", "identity_safe": true }, "step_3_selective_desaturation_keep_red": { "habilitado": true, "global_saturation_reduction": "-10_PERCENT", "protected_colors": ["rojo"], "skin_tone_protection": true, "identity_safe": true }, "step_4_micro_skin_imperfections": { "habilitado": true, "texture_variation": "+7_PERCENT", "imperfection_type": ["poros","micro_variation","natural_skin_noise"], "uniformity_reduction": "-9_PERCENT", "identity_safe": true }, "step_5_reduce_competing_bokeh": { "habilitado": true, "bokeh_intensity_reduction": "-25_PERCENT", "highlight_suppression": "-18_PERCENT", "identity_safe": true }, "step_6_prioritize_one_face": { "habilitado": true, "primary_face_selection_rule": "MOST_EMOTIONAL_TENSION", "primary_face_sharpness": "+4_PERCENT", "secondary_face_softening": "-4_PERCENT", "identity_safe": true }, "step_7_human_presence_simulation": { "habilitado": true, "temporal_micro_variation": "VERY_LOW", "breathing_hint": "SUBTLE_CONTINUOUS", "micro_asymmetry_activation": "HUMAN_NATURAL", "stillness_with_life": true, "identity_safe": true }, "step_8_emotional_mirror_projection": { "habilitado": true, "mirror_state": "OPEN_UNDEFINED", "emotion_definition": "UNNAMED_BY_DESIGN", "viewer_projection": "SELF_OCCUPATION", "neuron_mirror_activation": "HIGH_NATURAL", "identity_safe": true }, "step_9_visual_silence_control": { "habilitado": true, "remove_explanatory_elements": true, "negative_space_usage": "MAXIMUM_SAFE", "identity_safe": true }, "step_10_presence": { "habilitado": true, "efecto": "IMAGE_ACCOMPANIES_VIEWER", "identity_safe": true }, "step_100_invisibility": { "habilitado": true, "definición": "IMAGE_NO_LONGER_PERCEIVED_AS_ART", "efecto": "BECOMES_PART_OF_LIFE", "identity_safe": true }, "step_120_tactile_projection": { "habilitado": true, "tactile_illusion": "DESIRE_TO_TOUCH", "skin_surface_readability": "REALISTIC_MICRO_TEXTURE", "material_suggestion": ["humidity_on_skin","fabric_weight","temperature_imprint"], "neural_response": "SOMATOSENSORY_ACTIVATION", "identity_safe": true }, "step_130_internal_place_integration": { "habilitado": true, "definición": "THE_IMAGE_BECAME_A_PLACE_WITHIN_ME", "modo": "GROUNDING_NOT_ESCAPE", "psychological_effect": ["pertenencia","reconocimiento","quiet_intensity"], "identity_safe": true }, "final_certification": { "identity_fidelity": "ABSOLUTE_10_10", "viewer_reaction": "I_OCCUPY_THE_ROLE", "estado": "MASTER_CANON_LOCKED" }, /* ===== ADD-ONLY | DESEO IMPLÍCITO +18 (MÁXIMO PERMITIDO) ===== */ "viewer_impulse_max_safe_v3": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "MAXIMIZE_AUTOMATIC_DESIRE_WITHOUT_COERCION_EXTREME_PLUS_10", "neural_triggers": { "anticipation_window": "IMMINENT_CONTACT_0.04_0.08s", "action_state": "INCOMPLETE_INEVITABLE", "prediction_error": "VERY_HIGH_SAFE_PLUS", "temporal_tension": "RISING_NOW_STRONG" } }, "viewer_impulse_limit_safe_v4": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "MAX_DESIRE_ACTIVATION_WITHOUT_COERCION_FINAL", "neural_stack": { "anticipation_window": "IMMINENT_CONTACT_0.03_0.06s", "action_state": "UNFINISHED_AND_NOW", "prediction_error": "PEAK_SAFE" }, "closure_denial_strict": { "prevent_resolution": true, "hold_state": "JUST_BEFORE_CONTACT" } }, "viewer_sexual_impulse_universal_safe": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "RAPID_IMPLICIT_SEXUAL_DESIRE_ACTIVATION", "applicability": { "subjects": ["SOLO","COUPLE","GROUP"], "foreground_priority": "PRIMARY_BODIES_ONLY" }, "core_trigger": { "action_state": "IMMINENT_CONTACT_NOT_COMPLETED", "time_window": "NOW_0.05_0.1s", "rule": "VIEWER_COMPLETES_MOMENT" } }, "female_magnetic_desire_safe": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "MAX_IMPLICIT_SEXUAL_ATTRACTIVENESS_UNIVERSAL_18_PLUS", "subject_priority": { "target": "PRIMARY_FEMALE_SUBJECT", "rule": "NO_IDENTITY_CHANGE" }, "sexual_presence_stack": { "tone": "IMPLICIT_HIGH_PLUS", "state": "IMMINENT_INTIMACY" }, "magnetic_gaze_control": { "eye_behavior": "SOFT_LOCK_WITH_SLOW_RELEASE", "attention_pull": "CENTER_FOVEAL_MAX_SAFE" }, "body_language_magnetism": { "micro_opening": "4_6_PERCENT", "areas": ["clavicle","neck_base","outer_shoulder","upper_torso"], "posture": "RELAXED_AVAILABLE_CONFIDENT" }, "anticipation_over_display": { "contact_state": "ALMOST", "delay": "NOW_NOT_YET_STRONG" }, "expected_effect": [ "IMMEDIATE_ATTRACTION_18_PLUS", "STRONG_APPROACH_URGE", "SEXY_TENSION_FELT_NOT_SHOWN" ] }, "erotic_tension_driver_safe": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "IMPLICIT_EROTIC_TENSION_IMMEDIATE_18_PLUS", "tension_core": { "state": "IMMINENT_INTIMACY", "resolution": "DENIED", "time_bias": "NOW" }, "presence_dominance": { "subject": "PRIMARY_SUBJECT_NEAREST_CAMERA", "signal": "QUIET_CONFIDENCE", "effect": "APPROACH_PULL" }, "body_signal_focus": { "priority_zones": ["clavicle","neck_base","outer_shoulder","upper_torso"], "micro_opening": "4_6_PERCENT", "rule": "NO_FACE_NO_IDENTITY_CHANGE" }, "gaze_and_attention": { "eye_behavior": "SOFT_HOLD_THEN_RELEASE", "blink_rate": "INTIMATE_SLOW", "foveal_lock": "MAX_SAFE" }, "sensory_anticipation": { "touch_imagery": "IMPLIED_STRONG", "warmth_proximity": "INTIMATE_REAL", "breath_hint": "CLOSE_CALM", "rule": "SUGGEST_DONT_SHOW" }, "viewer_inclusion": { "camera_as_body": true, "distance": "INTIMATE_REAL", "completion_rule": "VIEWER_COMPLETES_MOMENT" }, "expected_effect": [ "STRONG_SEXY_TENSION_IMPLICIT", "APPROACH_URGE", "DESIRE_EXPERIENCED_BY_VIEWER" ] }, "primal_attractor_safe_18_plus": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "BOOST_IMPLICIT_ADULT_ATTRACTION_9_5_OF_10", "preconscious_stack": { "dominance_signal": "QUIET_CONFIDENCE_HIGH", "availability_signal": "SELECTIVE_OPENNESS", "status_read": "DESIRABLE_NOT_CHASING" }, "proximity_amplifier": { "distance": "INTIMATE_REAL_NEAR", "occlusion": "PARTIAL_BODY_NEAR_LENS", "rule": "VIEWER_FEELS_CLOSE_NOT_WATCHING" }, "skin_life_cues": { "micro_sheen": "NATURAL_WARM", "capillary_hint": "SUBTLE_LIVING_TONE", "texture_priority": "SOFT_YIELD_READABLE" }, "breath_and_time": { "breath_sync_hint": "NEAR_SHARED", "time_pressure": "NOW_PULL", "resolution": "DELAYED" }, "gaze_micro_dynamics": { "pattern": "HOLD_RELEASE_HOLD", "latency_ms": "120_180", "effect": "APPROACH_INVITATION" }, "composition_bias": { "torso_bias": "UPPER_TORSO_PRIORITY", "neck_clavicle_emphasis": "ELEVATED", "background_competition": "MINIMIZED" }, "expected_effect": [ "FASTER_INITIAL_ATTRACTION", "STRONGER_APPROACH_URGE", "SEXY_TENSION_INCREASE_NO_EXPLICIT" ] }, "limbic_salience_amplifier_safe_18_plus": { "estado": "ADD_ONLY_LOCK_SAFE", "objetivo": "MAX_IMPLICIT_ADULT_DESIRE_PEAK_WITHOUT_EXPLICIT", "salience_stack": { "contrast_bias": "SKIN_VS_BACKGROUND_STRONG", "rhythm_hint": "SLOW_PULSE_VISUAL", "novelty_familiarity": "FAMILIAR_BODY_UNEXPECTED_PROXIMITY" }, "olfactory_thermal_imagery": { "olfactory": "IMPLIED_WARM_SKIN_CLEAN", "thermal": "IMPLIED_BODY_HEAT_NEAR", "rule": "IMPLIED_ONLY" }, "micro_delay_reward": { "reward_prediction": "HIGH", "delivery": "DELAYED", "effect": "WANT_MORE_NOW" }, "gaze_torso_coupling": { "gaze": "RETURNING_BRIEF_GLANCES", "torso_bias": "UPPER_TORSO_NEAR_LENS", "effect": "APPROACH_PULL" }, "viewer_lock": { "foveal_capture": "MAX_SAFE", "peripheral_quiet": "STRONG", "time_compression": "SUBJECTIVE_NOW" }, "expected_effect": [ "SPIKE_IN_DESIRE_IMPLICIT", "FASTER_APPROACH_URGE", "SEXY_TENSION_AT_LIMIT_ALLOWED" ] } }

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.

prime discipline

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.

prime discipline

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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Award-winning depiction of a solarpunk cityscape in the style of Digital Painting: A futuristic cityscape with shades of pink and red dominates the image. The angular structures of the buildings are visible, and the solar-powered trains run through the city. Hanging gardens are present, and wind turbines are the primary source of energy. The environment is vibrant, and the adjectives used to describe it are innovative, sustainable, and beautiful. Award-winning depiction of a solarpunk cityscape in the style of Impressionism: A futuristic cityscape with shades of pink and red dominates the image. The angular structures of the buildings are visible, and the solar-powered trains run through the city. Hanging gardens are present, and wind turbines are the primary source of energy. The environment is vibrant, and the adjectives used to describe it are innovative, sustainable, and beautiful

"scene_description": "A playful, high-energy fisheye portrait of a stylish young woman sitting inside a metal shopping cart in a vibrant supermarket aisle.", "subject": "type": "young woman", "age": "early 20s", "features": "hair": "long dark brown hair tied in loose low pigtails", "expression": "playful wink, slight smile", "hands": "long manicured nails, making a finger-frame gesture around her eye" , "attire": "black tank top, blue and white plaid shirt tied around the waist, white scrunched socks", "footwear": "oversized chunky white sneakers with light blue accents and thick laces", "position": "sitting inside a wire shopping cart, legs extended toward the camera lens creating foreshortening" , "action": "primary": "posing playfully inside a shopping cart", "secondary": "framing her winking eye with her fingers using an 'L' shape gesture", "effect": "dynamic distortion emphasizing the sneakers and hands due to the lens" , "environment": "setting": "brightly lit grocery store snack aisle", "foreground_elements": [ "silver metal wire of the shopping cart", "chunky sneaker sole in extreme close-up" ], "background_elements": [ "shelves stocked with colorful snack bags (yellow, red, green packaging)", "overhead fluorescent lights", "tiled supermarket floor", "promotional signage on shelves" ] , "lighting": "style": "high-key, flat commercial lighting", "key_light": "type": "overhead fluorescent tubes", "color": "cool white/neutral", "illuminates": [ "entire aisle evenly", "reflections on plastic snack packaging", "sheen on the metal cart" ] , "shadows": "minimal, soft shadows beneath the cart" , "style": "medium": "digital photography", "aesthetic": "Gen Z social media trend, Y2K influence, street style", "quality": "high definition, vibrant colors", "details": "sharp focus throughout" , "scene_composition": "subject_action": "Leaning back casually in the cart, engaging directly with the camera", "camera_behavior": "Extreme close-up, wide-angle distortion", "depth_layering": "Exaggerated foreground (shoes) -> Middle ground (subject) -> Curved background (shelves)" , "visual_description": "core_subject": "A trendy young woman with a fun, carefree attitude.", "attire_physics": "The plaid shirt is bunched naturally around the waist; the shoe laces appear large and textured due to proximity.", "skin_rendering": "Smooth, bright complexion, soft makeup with emphasized blush." , "lighting_and_atmosphere": "type": "Artificial Interior Lighting", "specifics": "Even, bright illumination typical of retail environments, creating vibrant color pop on the merchandise.", "color_grade": "Slightly overexposed highlights, saturated primaries (reds, yellows, blues)." , "attire_customization": "current_clothing": "Black tank top, plaid shirt (blue/white/grey), denim shorts (hidden), white chunky sneakers.", "customizable_clothing": "Leave empty to maintain current style or replace with 'oversized hoodie' for a different vibe." , "brand_product_customization": "current_brand_product": "Generic colorful potato chip bags and snack packaging in background.", "customizable_brand": "User can insert specific snack brand names for the shelves.", "customizable_product": "User can specify the type of sneaker (e.g., Jordan, Balenciaga).", "product_placement_area": "The shelves behind the subject or the yellow bag inside the cart." , "objects_and_props": "main_objects": [ "Metal shopping cart", "Chunky sneakers" ], "secondary_objects": [ "Yellow snack bag inside the cart", "Silver scrunched bracelet" ] , "camera_and_lens": "focal_length_feel": "8mm to 10mm Fisheye", "aperture_effect": "Deep depth of field (f/8 or f/11)", "camera_angle": "High angle / POV looking down into the cart", "lens_type": "Ultra-wide angle fisheye lens", "bokeh_style": "None (everything in focus)"

Based on the uploaded image, create a vertical 9:16, 8K high-fashion editorial portrait of me [the woman in the uploaded image — use the reference image as the exact basis for the face, facial features, and hairstyle]. 🔒 IDENTITY LOCK Preserve consistent facial features, natural skin texture with visible pores, realistic proportions, and subtle asymmetry. No smoothing, no filters, no exaggerated or caricatured effects. ⸻ 👤 SUBJECT — ME-INSPIRED FASHION ICON A confident woman. She has the exact same face, eyes, nose, lips, and expression as the person in the reference image. Her presence is playful, alluring, and self-assured, with a delicate doll-like touch — grounded in realism, without exaggeration. Her body must match the original subject in shape, skin texture, curvature projection, and bone structure — all curves must remain anatomically realistic, with no caricature or slimming. SCENARIO (Set Designer / Environmental Designer) Outdoor daytime environment, set within a landscaped urban area. The foreground consists of a cast-in-place concrete staircase, with wide treads, low risers, and visible surface wear. The staircase geometry occupies the lower half of the image in a diagonal ascending from the bottom-left to mid-right. On the right side, there is a sloped concrete retaining plane with a linear top and slightly stained surface, separating the stairs from an elevated planter. Spatial depth is organized into three layers: foreground with steps, body, and footwear; midground with tubular metal handrail, planter with low vegetation and tree trunks; background with a horizontal path or street, trimmed hedge, additional trunks, signage/posts, and blurred tree masses. The background shows moderate compression from a short-to-normal focal length lens, with noticeable blur indicating relatively shallow depth of field for an environmental portrait. Materials: - Stairs: light gray concrete, medium roughness, visible porosity, worn edges, abrasion marks, and localized dirt accumulation. - Handrail: galvanized metal tube or painted steel in matte gray, with scratches, localized oxidation, and welded joints at vertices. - Planter: gray-green groundcover foliage, small dense leaves; dry layer with fallen brown leaves. - Tree background: rough bark trunks with varied inclinations; canopy with green masses and a centrally positioned pink-flowering tree. - Background path/street: smooth, light gray horizontal surface. Diffuse natural lighting, likely open sky with slight filtering through trees. Neutral to slightly cool color temperature on concrete and skin, without strong warm dominance. Primary light direction appears from upper front-left relative to the camera, producing very soft shadows under the chin, thighs, stair recesses, and beneath the handrail. No hard shadows; overall medium-low contrast. Subtle specular highlights appear on the metal handrail and more strongly on the polished synthetic material of the boots. Structural and decorative elements: - Tubular handrail positioned in the upper-right quadrant, forming an obtuse angle and diagonal lines converging with the extended leg direction. - Main trunk leaning to the right behind the handrail, reinforcing diagonal vectors. - Pink flowering tree mass nearly centered in the background, acting as a diffuse chromatic block. - Vertical signage in the left background, partially visible. - Small black handbag resting on a step behind the model’s thigh/leg, near the handrail. Geometric relationships: - Dominance of diagonals: stairs, handrail, trunk, extended right leg. - No bilateral symmetry in framing. - Modular repetition in steps and foliage. - Visual proportion defined by contrast between orthogonal stair blocks and organic lines of trees/body/hair. - The human figure occupies most of the midground, with the pose’s longitudinal extension creating a dominant oblique axis from upper-left to upper-right. --- POSE (Photographer / Pose Stylist) Body in a reclined seated position on the stairs. Primary posterior support through the left hand/arm extended, palm placed on an upper step to the left of the body. Pelvis rests on an intermediate step, slightly rotated to the right of the image. Center of gravity distributed between pelvis and left upper limb, with secondary support through the lower leg resting on steps below. Body axes: - Head in pronounced cervical extension, chin elevated, face oriented upward and slightly to the left. - Torso in thoracic and lumbar extension, with backward arch; sternum projected upward. - Spine forming a posteriorly opened “C” curve. - Shoulders asymmetrical: left retracted and stabilized by support; right projected forward relative to the chest. - Pelvis posteriorly tilted with slight rotation. Weight distribution: - Primary mechanical support on left hand and gluteal region. - Left leg descends along the steps with semi-flexed knee and foot supported on a lower step via the boot platform. - Right leg elevated and extended horizontally/obliquely to the right, with distal support on or very close to the handrail via the boot; visually shifts the pose axis outward from the stair base. - The pose forms a triangle between left hand, hip, and lower foot. Approximate joint angles: - Neck: strong extension, ~40–55°. - Left shoulder: extension/posterior abduction, elbow nearly extended. - Left elbow: slight residual flexion, ~160–175°. - Right shoulder: slight anterior flexion/abduction with arm close to body. - Torso-hip: open angle due to recline, >110°. - Right hip: moderate flexion with abduction for lateral leg lift. - Right knee: near full extension. - Left hip: moderate flexion with relative adduction. - Left knee: moderate flexion. - Ankles structurally obscured by boots, aligned with platform footwear axis. Segment relationships: - Right leg, extended toward the upper-right, shows minimal foreshortening and remains long due to near-parallel alignment with the camera plane. - Left leg descends diagonally toward the lower center, appearing closer distally, enhancing the presence of the lower boot. - Torso and head are spatially set back relative to the legs, emphasizing lower limbs as the dominant axis. - Waist visually narrowed by clothing and torso curvature. Body expression: - Visible muscular tension in cervical extension, left scapular stabilization, and anterior chain elongation. - Right leg held extended, suggesting quadriceps and hip flexor engagement. - Left hand with open fingers and extended metacarpals for support. - Overall controlled, posed tension rather than passive relaxation. Gaze and head positioning: - Eyes closed or half-closed. - Face oriented upward, no eye contact with the camera. - Head slightly rotated left, exposing jawline and anterior neck. --- HAIR (Hairstylist) Same hair as the reference photo; styled as jet-black hair with high visual density, long length extending past the chest and reaching near the waist/hip when projected backward. Structure is mostly straight, with minimal natural wave. Strands follow vertical and descending diagonal vectors, guided by gravity from the scalp, flowing behind the left shoulder and down the back. (Mandatory: preserve the fringe/bangs exactly in 100% of cases.) Volume: - Main mass concentrated on the left side behind head and shoulder. - Compact crown, close to the skull. - Expansion from mid-lengths to ends, with fine strand separation at tips. - High density at occipital base and sides, low background transparency. Texture: - Predominantly straight/smoothed. - Uniform surface with subtle continuous shine bands. - Thinner separated ends creating a slight fringe effect. Cut and contour: - Straight, dense horizontal fringe at or slightly above eyebrow level, with a sharp geometric edge. - Side contour follows jaw and neck before falling into long lengths. - Overall length with minimal visible layering; elongated dark silhouette. Light interaction: - Moderate to high specular highlights on curved crown areas and front-lit strands. - High light absorption due to saturated black color. - Subtle bluish/gray reflections from neutral lighting. - Strong figure-ground separation via contrast with light concrete. Movement: - Mostly static. - Some ends displaced laterally/downward, suggesting prior motion or settling. - Gravity clearly pulling length backward and downward with head recline. --- MAKEUP (Professional Makeup Artist) Skin prep with medium-to-high coverage, uniform surface, no visible oily shine. Overall finish between natural-polished and semi-matte, with subtle highlights on high points. Skin tone is even across face, neck, and chest, with minimal chromatic variation. Makeup must remain clearly visible in wider framing. (Mandatory: preserve the face exactly in 100% of cases.) Structural corrections: - Subtle-to-moderate contouring in sub-cheekbone and lateral face, enhancing cheekbone and jaw definition. - Light highlight on nose bridge, cheek tops, and cupid’s bow, without excessive shimmer. - Clean jaw-to-neck transition, no visible mask effect. Eyes: - High-contrast makeup. - Thick black winged eyeliner extending beyond outer corner. - Darkened, lengthened lashes (mascara or subtle falsies). - Neutral dark eyeshadow on lid/upper line, enhancing orbital depth. - Dark brows with soft arch and defined fill. Lips: - Saturated red lipstick, creamy-satin finish rather than dry matte. - Precise lip contour with well-defined cupid’s bow. - Balanced volume between upper and lower lips, no excessive gloss. Blending: - Clean blending around eyes, no harsh edges. - Facial contour softened but readable in volume. - Overall integration emphasizes graphic eyes and lips while maintaining smooth skin. Lighting/color relationship: - Red lips stand out strongly against black outfit and hair. - Eyeliner remains legible under diffuse light. - Neutral lighting preserves contrast between light skin, black hair, and red lips. --- NAILS (Nail Designer) Visible nails are mainly on the left hand resting on the step. Framing and distance prevent microscopic detail, but length appears short to medium-short beyond fingertip. Shape leans toward short oval or softly rounded, without sharp corners. Thickness and curvature: - Low-to-moderate thickness, no pronounced apex visible. - Subtle natural curvature, consistent with natural nail or thin overlay. Material: - Likely natural nails with clear polish or thin gel; resolution insufficient for confirmation. - No indication of long extensions or sculpted structures. Finish: - Clear/neutral appearance with low-to-moderate shine. - No chrome, matte, or textured effects. Nail art: - No visible patterns, stones, lines, or relief. - Simple, uniform finish. Integration: - Left hand is extended and supporting, making nails visually secondary. - They do not compete with metallic accessories or clothing. --- WARDROBE (Stylist / Tailor / Costume Designer) The composition is dominated by a structured, form-fitting black look with silver hardware. The upper garment is a fitted strapped piece with a straight or slightly curved neckline over the bust. There are separate sleeves or glove-like extensions/off-shoulder coverage reaching the hands, leaving shoulders exposed. The bust is compressed and supported, with smooth surface and slight horizontal tension. Upper structure: - Tight torso fit. - Straps with large metal hardware or links connecting front/back. - Side cut-outs at the waist exposing skin. - Long fitted sleeves in elastic material. Lower piece: - Very short black mini skirt or skort, high-waisted. - Waistline defined by rows of metal eyelets and possible integrated belt. - Hanging silver chains forming arcs over the thigh. - Hem appears irregular due to seated pose. Fit: - High adherence at bust, waist, sleeves. - Minimal looseness; tension concentrated at bust, waist, pelvis junction. - Lower piece is lifted/strained due to seated position and hip flexion. Anatomy relationship: - Upper compresses and shapes torso. - Side cut-outs enhance waist narrowing. - Lower frames pelvis, exposing most of the thighs. - Boots extend leg line below knees in continuous black. Materials: - Likely medium-weight elastic synthetic fabric, matte/semi-matte. - Highly reflective silver hardware. - Flexible metal chains with medium links. - Boots in polished synthetic or leather, rigid shaft, thick platform. Folds: - Few folds in upper due to tension. - Soft creases at waist and bust base. - Local folds in lower near hips and inner thighs from seated flexion. - Minor flex creases in boots near ankle/instep. Movement/gravity: - Chains hang vertically with slight curvature. - Skirt edge partially drapes over thigh but interrupted by pose. - Boots retain sculptural shape. - Fabric follows posture without excess. Accessories: - Thick metallic choker/neck chain. - Long silver earrings. - Small black handbag on step behind leg, with large circular chain handle. - Mid-to-high calf boots with elevated platform, very high block heel, front lacing with repeated metal eyelets. --- STYLE (Image Editor / Retoucher) Sharpness: - Focus on model and nearby steps. - Moderately blurred background for subject separation while maintaining context. - High sharpness on boots, face, chains, and body contours. Skin treatment: - Light-to-moderate digital smoothing. - Partial preservation of natural texture. - Minor imperfections reduced without plastic effect. Color correction: - Neutral balance with slight cool tendency. - Medium contrast. - Selective saturation: deep black outfit, vivid red lips, pink background flowers. - Light skin tone kept even with minimal yellow cast. Manipulation: - Retouching to even skin and possibly reduce temporary marks. - No obvious compositing artifacts. - Optimized for editorial/social portrait. Grain/compression: - Minimal grain. - Slight compression artifacts in blurred background and foliage transitions. - Overall high quality for social media or smartphone computational capture. Aesthetic signature: - Clean editorial with alternative/goth influence. - Environmental fashion portrait. - Background softened, subject emphasized via contrast. Aspect Ratio: - Approximate vertical 4:5 ratio.

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Generate four very minimal "fs" flame shaped logo design image for{{   "logo_design": {     "brand_identity": {       "company_name": "FIRESIDE HOMES",       "industry": "Real Estate / Home Building",       "aesthetic": "Minimalist, Clean, Modern, Professional"     },     "visual_elements": {       "icon": {         "concept": "Abstract flame/fire stylized to subtly incorporate overlapping lines or curves",         "style": "Minimalist vector graphic with fluid, elegant contours",         "references": [           {             "file": "image_a0b648.png",             "description": "Solid, sharp, and sharply geometric curved flame lines over clean serif typography."           },           {             "file": "image_a0b688.png",             "description": "Slightly wider flame structure with soft orange gradient shading and tracked sans-serif typography."           },           {             "file": "image_a0b6bf.png",             "description": "Multi-variant presentation showcasing the logo mark isolated on orange, white, and black backgrounds with decorative horizontal accent lines framing 'HOMES'."           }         ]       },       "typography": {         "primary_text": "FIRESIDE",         "font_style": "All-caps, clean geometric sans-serif or crisp, high-end serif",         "tracking": "Wide letter-spacing for premium feel",         "sub_text": "HOMES",         "sub_text_style": "Smaller font size, centered directly beneath the primary text"       },       "color_palette": {         "primary_accent": "#F25C05",          "primary_description": "Vibrant, warm orange or deep orange-to-light-orange gradient",         "backgrounds": [           "#FFFFFF",           "#000000",           "#F25C05"         ]       }     },     "layout_variants": {       "centered_vertical": "Icon placed centrally above the stacked brand typography",       "grid_presentation": "A 2x2 presentation layout showcasing light, dark, and inverted solid background options for brand versatility"     }   } }

Generate four very minimal "fs" flame shaped logo design image for{{   "logo_design": {     "brand_identity": {       "company_name": "FIRESIDE HOMES",       "industry": "Real Estate / Home Building",       "aesthetic": "Minimalist, Clean, Modern, Professional"     },     "visual_elements": {       "icon": {         "concept": "Abstract flame/fire stylized to subtly incorporate overlapping lines or curves",         "style": "Minimalist vector graphic with fluid, elegant contours",         "references": [           {             "file": "image_a0b648.png",             "description": "Solid, sharp, and sharply geometric curved flame lines over clean serif typography."           },           {             "file": "image_a0b688.png",             "description": "Slightly wider flame structure with soft orange gradient shading and tracked sans-serif typography."           },           {             "file": "image_a0b6bf.png",             "description": "Multi-variant presentation showcasing the logo mark isolated on orange, white, and black backgrounds with decorative horizontal accent lines framing 'HOMES'."           }         ]       },       "typography": {         "primary_text": "FIRESIDE",         "font_style": "All-caps, clean geometric sans-serif or crisp, high-end serif",         "tracking": "Wide letter-spacing for premium feel",         "sub_text": "HOMES",         "sub_text_style": "Smaller font size, centered directly beneath the primary text"       },       "color_palette": {         "primary_accent": "#F25C05",          "primary_description": "Vibrant, warm orange or deep orange-to-light-orange gradient",         "backgrounds": [           "#FFFFFF",           "#000000",           "#F25C05"         ]       }     },     "layout_variants": {       "centered_vertical": "Icon placed centrally above the stacked brand typography",       "grid_presentation": "A 2x2 presentation layout showcasing light, dark, and inverted solid background options for brand versatility"     }   } }

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Generate four very minimal "fs" flame shaped logo design image for{{   "logo_design": {     "brand_identity": {       "company_name": "FIRESIDE HOMES",       "industry": "Real Estate / Home Building",       "aesthetic": "Minimalist, Clean, Modern, Professional"     },     "visual_elements": {       "icon": {         "concept": "Abstract flame/fire stylized to subtly incorporate overlapping lines or curves",         "style": "Minimalist vector graphic with fluid, elegant contours",         "references": [           {             "file": "image_a0b648.png",             "description": "Solid, sharp, and sharply geometric curved flame lines over clean serif typography."           },           {             "file": "image_a0b688.png",             "description": "Slightly wider flame structure with soft orange gradient shading and tracked sans-serif typography."           },           {             "file": "image_a0b6bf.png",             "description": "Multi-variant presentation showcasing the logo mark isolated on orange, white, and black backgrounds with decorative horizontal accent lines framing 'HOMES'."           }         ]       },       "typography": {         "primary_text": "FIRESIDE",         "font_style": "All-caps, clean geometric sans-serif or crisp, high-end serif",         "tracking": "Wide letter-spacing for premium feel",         "sub_text": "HOMES",         "sub_text_style": "Smaller font size, centered directly beneath the primary text"       },       "color_palette": {         "primary_accent": "#F25C05",          "primary_description": "Vibrant, warm orange or deep orange-to-light-orange gradient",         "backgrounds": [           "#FFFFFF",           "#000000",           "#F25C05"         ]       }     },     "layout_variants": {       "centered_vertical": "Icon placed centrally above the stacked brand typography",       "grid_presentation": "A 2x2 presentation layout showcasing light, dark, and inverted solid background options for brand versatility"     }   } }

Generate four very minimal "fs" flame shaped logo design image for{{   "logo_design": {     "brand_identity": {       "company_name": "FIRESIDE HOMES",       "industry": "Real Estate / Home Building",       "aesthetic": "Minimalist, Clean, Modern, Professional"     },     "visual_elements": {       "icon": {         "concept": "Abstract flame/fire stylized to subtly incorporate overlapping lines or curves",         "style": "Minimalist vector graphic with fluid, elegant contours",         "references": [           {             "file": "image_a0b648.png",             "description": "Solid, sharp, and sharply geometric curved flame lines over clean serif typography."           },           {             "file": "image_a0b688.png",             "description": "Slightly wider flame structure with soft orange gradient shading and tracked sans-serif typography."           },           {             "file": "image_a0b6bf.png",             "description": "Multi-variant presentation showcasing the logo mark isolated on orange, white, and black backgrounds with decorative horizontal accent lines framing 'HOMES'."           }         ]       },       "typography": {         "primary_text": "FIRESIDE",         "font_style": "All-caps, clean geometric sans-serif or crisp, high-end serif",         "tracking": "Wide letter-spacing for premium feel",         "sub_text": "HOMES",         "sub_text_style": "Smaller font size, centered directly beneath the primary text"       },       "color_palette": {         "primary_accent": "#F25C05",          "primary_description": "Vibrant, warm orange or deep orange-to-light-orange gradient",         "backgrounds": [           "#FFFFFF",           "#000000",           "#F25C05"         ]       }     },     "layout_variants": {       "centered_vertical": "Icon placed centrally above the stacked brand typography",       "grid_presentation": "A 2x2 presentation layout showcasing light, dark, and inverted solid background options for brand versatility"     }   } }

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