90 Prompts

Hyper-réaliste portrait photographique d'un jeune homme blanc musclé d'environ 22-25 ans, physique athlétique et légèrement poilu, allongé de manière décontractée et sensuelle sur un lit défait dans une chambre d'étudiant années 90, ambiance nostalgique et désordonnée. Il porte uniquement un boxer blanc classique Fruit of the Loom style années 90 avec bord rose pâle et inscription "FUCK" visible sur l'élastique noir, un débardeur/sleeveless navy bleu foncé université Michigan Wolverines avec gros logo jaune "MICHIGAN" et petit "MC" dessous, des chaussettes de sport grises Adidas mi-mollet. Pose signature : torse nu musclé exposé, poils thoraciques et abdominaux bien visibles (happy trail prononcé), bras droit levé et plié derrière la tête formant un cœur avec les doigts au-dessus de sa casquette, bras gauche reposant le long du corps. Regard direct caméra, expression légèrement provocante, lèvres entrouvertes, sourcils froncés charmeurs, air confiant et un peu insolent.Casquette noire plate style snapback portée à l'envers sur cheveux courts bruns. Tatouages très visibles : serpent rouge stylisé en motif cordes entrelacées sur l'avant-bras droit, texte gothique "V.YXVI.XIX" ou similaire sur l'avant-bras gauche, autres petits tatouages sur poitrine et flanc droit ("Ziggy", "MOST WANTED", etc.).Décor très chargé et vintage : mur entier recouvert de posters et coupures de journaux/presse superposés sans ordre – posters NBA vintage (Kobe Bryant Lakers n°8, Michael Jordan Bulls n°23, scènes de matchs), Playboy Magazine vintage, affiche psychédélique années 60-70 avec silhouette nue et couleurs flashy, vieille pub Datsun voiture, photo de Malcolm X, portraits noir & blanc d'hommes noirs iconiques, coupures de journaux avec titres illisibles, autocollants, photos de pin-up, etc. Ambiance années 90-2000 early internet / chambre ado rebelle.Éclairage naturel doux venant d'une fenêtre hors champ à gauche, lumière chaude de fin d'après-midi, ombres douces sur le corps et les draps. Draps froissés bleu-gris rayés fins blancs, matelas visible, oreiller écrasé derrière lui. Texture de peau réaliste : pores, quelques imperfections, duvet, transpiration légère sur le torse.Style photo : prise avec appareil argentique moyen format ou DSLR haut de gamme, grain fin, couleurs saturées mais naturelles, légère vignette, netteté moyenne, profondeur de champ réduite (arrière-plan un peu flou), mood sexy, brut, authentique, légèrement trash et nostalgique.

Create a vaporwave-themed cell phone with 90's elements: Vibrant neon colors, digital grid landscapes, retro-futuristic cityscapes, and iconic 90's mobile phones. Emphasize pink and turquoise hues, with geometric patterns. Include elements like a classic chunky, vintage mobile phone prominently displayed. Incorporate aesthetic features like VHS glitch effects, chrome typography, and floating geometric shapes. Set the scene at twilight to capture the essence of vaporwave with a nostalgic, yet futuristic feel. the name "NOKIA" etched into the phone, filled with typical vaporwave motifs --s 750 --v 6.0 --style raw

A hyper-realistic, ultra-detailed full-body depiction of a stunning British woman, presented in five distinct views within the same 21:9 frame: a front view, a pure 90-degree side profile, a back view, a close-up of her face in front view, and a close-up of her face in side profile. Each pose is evenly spaced, ensuring her entire figure is fully visible from head to feet without overlap, while the close-up portraits are positioned on the right side of the frame—front view at the top, side profile below. The camera maintains a neutral eye-level position, capturing her full height and facial details with no distortion or cropping. She has a symmetrical, captivating face with deep brown almond-shaped eyes, naturally arched eyebrows, and full, well-defined lips. Her dark brown wavy hair is tied in a messy bun, with a few loose strands framing her face. Her soft, radiant complexion is enhanced by natural skin tones. Her physique is athletic and well-proportioned, featuring a full, naturally balanced bust, a defined waist, elegant shoulders, toned arms, and strong, thick thighs. Standing at 175 cm, she is wearing a black deep V-neck sports bra, high-waisted black yoga pants, and white sneakers. She has no makeup. The front view shows her standing naturally, facing directly toward the camera, arms at her sides, feet flat on the ground. The side profile is a pure 90-degree angle, with her entire body turned to the side, head aligned straight, and arms naturally resting at her sides, ensuring no frontal visibility. The back view captures her from behind, highlighting the back, shoulders, and leg proportions. The close-up front portrait focuses on her face with even lighting, while the side-profile close-up captures the sharp definition of her jawline and nose. The clean white background enhances clarity, while soft, natural lighting casts subtle highlights and shadows for extreme photorealism. HDR 4K resolution captures ultra-realistic textures and perfectly balanced skin tones, achieving a highly cinematic effect. The wide 21:9 framing ensures all five depictions fit seamlessly with accurate proportions, maintaining complete visibility with no cropping or distortion.

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.

one woman at a busy night club, sitting on a chair backview, backview, looking at viewer, long brunette hair , close up full body. High dynamic range, vivid, rich details, clear shadows and highlights, realistic, intense, enhanced contrast, highly detailed(lofi, anime, woman, award-winning drawing, award-winning 90's-anime, award-winning cinematography, high resolution, cinematic) 90's-anime:: CRT-screen-filter:: flat:: lofi:: girl:: high-resolution:: cold-colors:: cinematic:: 4k

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.

Imagem central: Mulher branca na faixa dos 40-50 anos, com cabelo volumoso e corte característico dos anos 80 ou 90 (como o corte "Rachel" da série Friends). Ela está usando roupas da época, como uma jaqueta jeans ou uma blusa com ombreiras. A mulher tem uma expressão de curiosidade e surpresa, com a boca ligeiramente aberta e as sobrancelhas levantadas. Uma mão ou silhueta de outra pessoa está cochichando no ouvido direito da mulher, como se estivesse revelando o segredo sobre o que é a Geração X. Elementos de fundo e decoração: Colagem de itens icônicos dos anos 80 e 90 espalhados pelo fundo, como um Walkman, disquetes coloridos, um telefone com fio, uma fita cassete, um controle remoto de TV antigo, entre outros. Padrões geométricos em cores vibrantes, como triângulos, quadrados e linhas zigzag, remetendo à estética da época. Recortes de revistas e jornais com manchetes e anúncios relacionados às questões enfrentadas pelas mulheres da Geração X, como "Mulheres no mercado de trabalho: a luta por igualdade", "A dupla jornada: o desafio de conciliar carreira e família", "Feminismo em pauta: conquistas e desafios", entre outros. Cores: Paleta de cores vibrantes e contrastantes, como magenta, ciano, amarelo e preto, para transmitir a energia e o espírito da época. Tipografia: Título do livro em uma fonte bold e chamativa, com um efeito de texto 3D ou sombreado, característico dos anos 80 e 90. Subtítulo ou nome da autora em uma fonte mais simples e moderna, para contrastar com o título.

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

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

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

90

{ "input_pl": "Zrób miniaturkę na YOUTUBE - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki YT : \n\n1. Typ obrazu: Fotorealistyczny.\n2. Sceneria: Nowoczesny warsztat samochodowy z logo „VULCANOS” subtelnie widocznym w tle. Czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. Główne postacie: Atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. Tekst i styl: „Matador Nordicca Czy WARTO kupić? (VULCANOS Lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. Nastrój: Profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90.", "input_en": "zrób miniaturkę na youtube - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki yt : \n\n1. typ obrazu: fotorealistyczny.\n2. sceneria: nowoczesny warsztat samochodowy z logo „vulcanos” subtelnie widocznym w tle. czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. główne postacie: atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. tekst i styl: „matador nordicca czy warto kupić? (vulcanos lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. nastrój: profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90.", "full_prompt": "zrób miniaturkę na youtube - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki yt : \n\n1. typ obrazu: fotorealistyczny.\n2. sceneria: nowoczesny warsztat samochodowy z logo „vulcanos” subtelnie widocznym w tle. czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. główne postacie: atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. tekst i styl: „matador nordicca czy warto kupić? (vulcanos lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. nastrój: profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90., cinematic lighting, wide angle shot, epic scale, film grain, IMAX format, ultra wide shot, grand scale, 8K resolution, photorealistic, hyperdetailed, ultra-sharp, professional photography, macro photography, extreme close-up, detailed texture, high noon, harsh sunlight, overhead lighting, strong shadows, clear sky, bright day, vibrant colors, dynamic, energetic, vibrant, action-packed, shot on Hasselblad, medium format, exceptional detail, 35-50mm standard lens, natural perspective, f/2.8 aperture, ISO 1600, long-exposure shutter speed, 8K resolution", "styles": [ "cinematic lighting, wide angle shot, epic scale, film grain", "IMAX format, ultra wide shot, grand scale, 8K resolution", "photorealistic, hyperdetailed, ultra-sharp, professional photography", "macro photography, extreme close-up, detailed texture", "high noon, harsh sunlight, overhead lighting, strong shadows", "clear sky, bright day, vibrant colors", "dynamic, energetic, vibrant, action-packed", "shot on Hasselblad, medium format, exceptional detail", "35-50mm standard lens, natural perspective", "f/2.8 aperture", "ISO 1600", "long-exposure shutter speed", "8K resolution" ], "technical_params": { "time_of_day": "high-noon", "camera": "hasselblad", "lens": "standard", "aperture": "f/2.8", "iso": "1600", "shutter": "long-exposure" } }

A cute little hybrid figure with a Western girl's face, wearing glasses and a gnome-like body floating under water. This is a blind box-style toy with a three-dimensional shape, high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7

"Photo-realistic 3D illustration of a solemn Memorial Day ceremony at sunset in Arlington National Cemetery, with realistic lighting, soft shadows, detailed headstones, and a soldier kneeling by a grave." high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7

A cute little hybrid figure with a Japanese girl's face, wearing glasses and a mokey-like body floating under water. This is a blind box-style toy with a three-dimensional shape, high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7

A cute little hybrid figure with a Japanese girl's face, wearing glasses and a gnome-like body floating under water. This is a blind box-style toy with a three-dimensional shape, high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7

A cute little hybrid figure with an Eastern man's face, wearing glasses and a gnome-like body floating under water. This is a blind box-style toy with a three-dimensional shape, high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7

ROLL-UP BANNER DESIGN FORMAT: Roll-up / Pull-up banner DIMENSIONS: 85cm wide × 200cm tall DIRECTION: "CONFIDENT INFRASTRUCTURE" same visual system as website ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ DESIGN PHILOSOPHY ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ This is a physical event material. It must be readable from 2-3 meters. It must work at business fairs, networking events and conferences in Southern Denmark and Northern Germany. It should feel like a confident, premium regional platform — not a generic EU project poster. NOT: EU-flag aesthetic NOT: stock photo of handshake NOT: wall of text NOT: decorative icons everywhere YES: strong typography YES: clear visual hierarchy YES: one bold visual element YES: one clear call to action ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ DESIGN SYSTEM — IDENTICAL TO WEBSITE ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ COLORS: Deep Navy: #0D1B2A Mid Blue: #415A77 Steel Blue: #778DA9 Cloud Grey: #E0E1DD Orange: #E86300 Warm White: #FAFAF8 Warm Cream: #F5F0E9 TYPOGRAPHY — Raleway: Logo text: 24px / 700 White Headline: 56-64px / 800 / -2px Deep Navy or White Subtext: 20px / 400 / lh 30px Body points: 18px / 400 / lh 28px CTA text: 16px / 700 uppercase QR label: 14px / 600 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ BACKGROUND STRUCTURE ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ TWO-ZONE BACKGROUND: TOP ZONE — top 45% of banner height: Background: Deep Navy #0D1B2A Contains: logo + headline + subtext BOTTOM ZONE — bottom 55% of banner: Background: Warm White #FAFAF8 Contains: network visual + benefit points + QR + footer TRANSITION between zones: A subtle diagonal or straight horizontal cut at the boundary. NO gradient. Clean edge. The Orange accent line 4px horizontal marks the transition point. ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ ZONE 1 — TOP SECTION (0–90cm from top) Background: Deep Navy #0D1B2A ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ LOGO AREA — top, padding 28px: Left: "Business DE-DK" wordmark Raleway Bold 26px White Below wordmark: thin Orange 3px line width equal to wordmark Right of logo: Small label uppercase 10px Steel Blue: "SOUTHERN DENMARK NORTHERN GERMANY" Horizontal 1px #415A77 rule below entire logo area. HEADLINE AREA — below logo, padding 32px: Small eyebrow label: "DANISH–GERMAN BUSINESS NETWORK" 11px / 700 / +2px uppercase Steel Blue #778DA9 Space: 12px MAIN HEADLINE: Raleway 58px / 800 / -2px / lh 62px White: "Connect across the Danish–German border" Space: 20px SUBTEXT: Raleway 19px / 400 / lh 30px Steel Blue #778DA9: "Find companies, advisors, events and practical cases in one cross-border business network." ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ TRANSITION LINE ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 4px solid Orange #E86300 Full banner width: 85cm This line is the only orange element in the top half. It signals the transition and anchors the eye. ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ ZONE 2 — BOTTOM SECTION (90–200cm) Background: Warm White #FAFAF8 ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ NETWORK VISUAL — below transition line: Abstract network graph illustration. Width: full 85cm, height: ~40cm Background: transparent (sits on Warm White) Thin connection lines: 1px #E0E1DD Nodes: circles in two sizes Large nodes: 12px — Orange #E86300 and Mid Blue #415A77 Small nodes: 8px — Steel Blue #778DA9 and Cloud Grey #E0E1DD NO text labels on nodes. NO names of people or organisations. Pure abstract network topology. The graph feels organic — not geometric, not symmetric. Nodes distributed naturally across the full width. 3-4 orange nodes create visual anchors across the composition. Density: medium — not too sparse, not cluttered. Approximately 12-16 nodes total, 20-25 connection lines. The network fades slightly at the bottom edge — opacity drops to 30% at bottom of this visual zone. BENEFIT POINTS SECTION: Sits over or below the network visual. Padding: 0 40px Three rows. Each row: Left: Orange circle 10px flex-shrink: 0 margin-right: 16px Right: Text 18px / 500 Deep Navy line-height 26px Items: "Explore the network" "Meet advisors and partners" "Join events and cases" Thin 1px #E0E1DD rules between rows. Padding: 14px 0 each row. ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ QR CODE ZONE CRITICAL: positioned at 90-110cm from the bottom of the banner. This equals eye/hand level for an adult standing at an event. ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ Background: #FFFFFF Border: 1px solid #E0E1DD Border-radius: 4px Padding: 20px 24px Width: 200px, centered LAYOUT inside QR card: Left: QR code placeholder Size: 80×80px minimum "QR CODE PLACEHOLDER" Black and white, no color Right: Text stack: "Scan to join the network" 16px / 700 Deep Navy Space: 8px "business-region.eu" 13px / 400 Orange text link style CTA BUTTON — below QR card: Full banner width minus 80px padding Background: Orange #E86300 Text: "Scan to join the network" Raleway 16px / 700 uppercase White Height: 52px Border-radius: 4px ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ FOOTER ZONE — bottom 15cm ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ Background: #F5F0E9 Warm Cream Top: 1px #E0E1DD Padding: 16px 40px Horizontal row: Left: Small Interreg logo placeholder Rectangle 80×24px #E0E1DD "Interreg" 11px Steel Blue Center: "Interreg-supported project" 11px / 600 Steel Blue uppercase Right: "DA · DE · EN" 11px / 600 Steel Blue ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ LAYOUT SUMMARY — FROM TOP TO BOTTOM ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ 0–10cm: Logo area (Deep Navy bg) 10–90cm: Headline + subtext (Deep Navy bg) 90cm: 4px Orange transition line 90–130cm: Network graph visual (Warm White) 130–160cm: Benefit points × 3 (Warm White) 160–175cm: QR card + CTA button (Warm White) 185–200cm: Footer strip (Warm Cream) ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ CRITICAL RULES ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ QR CODE placement: NEVER below 175cm from top. ALWAYS at 160-175cm from top. A person of average height (170cm) can scan without bending. Typography minimums for print: Headline: minimum 56px at screen = minimum 20mm in print Body text: minimum 18px at screen = minimum 7mm in print Orange used only for: — Transition line — Network node accents (3-4 nodes) — Orange bullet circles — CTA button — URL text in QR card NO gradient backgrounds NO stock photography NO EU flag imagery NO decorative icons NO text smaller than 11px on screen (= 4mm in print — absolute minimum) MARGINS: Left and right: 40px (screen) = 15mm print Top and bottom zones: 28px padding ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ DELIVERABLE ━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━━ One frame: 850px × 2000px (represents 85cm × 200cm at 10px per cm) Export ready for: — Digital preview (PNG 150dpi) — Print production (PDF 300dpi) The result must feel like it belongs to the same design system as the Business DE-DK website — same colors, same typography, same confidence, same precision. Premium. Regional. Clear. Not an EU poster. Not a startup flyer. A confident cross-border business platform.

{ "prompt_type": "descriptive_replication", "reference_adherence": "STRICT_VISUAL_FIDELITY", "aspect_ratio": "9:16", "style": "1990s compact digital camera aesthetic with harsh on‑camera flash, grainy texture, washed‑out colors, high contrast, subtle chromatic aberration and halation. No HDR, no modern digital processing. The image looks like a candid flash snapshot taken with an early digital point‑and‑shoot.", "identity_lock": { "priority": "ABSOLUTE", "instruction": "Use MY EXACT FEMALE MODEL Adèle. Facial identity must be perfectly preserved with zero drift. All details below must be followed exactly.", "cranial_structure": { "shape": "elongated oval skull with wide bizygomatic width", "forward_growth": "maxilla and mandible projected forward, strong skeletal framework", "facial_thirds": "upper : middle : lower = 1:1:0.9, slightly elongated lower third", "cheekbones": "high‑set, razor‑sharp, beginning directly under eyes, sweeping laterally, forming deep hollow cheeks with natural submalar shadows", "mandible": "sharply defined, gonial angle approx. 118°, clean V‑shaped jawline", "chin": "slightly pointed but firm, aligned with nasal septum" }, "eyes": { "shape": "almond‑shaped, deeply set", "canthal_tilt": "positive 5° (outer corners higher)", "medial_canthi": "acutely angled, extending downward", "scleral_show": "zero (lower lids tightly hug iris)", "eyelids": "hooded with minimal exposure", "iris": "light green with golden‑brown central heterochromia, distinct limbal ring, visible radial fibers", "eyebrows": "thick, straight, set low on supraorbital ridge, soft arch peaking slightly lateral to lateral limbus, individual hairs visible" }, "nose": { "dorsum": "straight, smooth", "bridge": "refined, narrow", "tip": "precisely sculpted, slightly rounded, delicate cartilage definition", "nostrils": "narrow, symmetrical, slight columellar show" }, "lips": { "fullness": "full, lower lip to upper lip ratio approx. 1.3:1", "cupids_bow": "pronounced with distinct peaks", "vermilion_borders": "distinct", "oral_commissures": "sharp, turning slightly upward", "philtrum": "short, well‑defined, approx. 11 mm" }, "skin": { "tone": "warm‑neutral with subtle olive undertone, faint golden undertones in cheeks", "texture": "hyperrealistic, photorealistic, ultra‑detailed", "pores": "barely visible micropores 0.1–0.2 mm in T‑zone", "micro_roughness": "present", "orange_peel": "ultra‑fine micro‑depressions visible under side lighting", "subsurface_scattering": "moderate on nose, cheeks, earlobes, lifelike translucency", "vellus_hairs": "delicate on jawline and cheekbones", "micro_veins": "faintly discernible under translucent skin", "specular_highlights": "healthy on forehead, nose, cheekbones; matte cheeks" }, "hair": { "color": "chestnut brown with natural California blonde balayage (bronde), multi‑tonal, soft caramel and honey streaks", "style": "long wavy, cascading over shoulders, with side‑swept curtain bang grazing outer eye corner", "texture": "glossy, healthy, individual strands visible, anisotropic reflections, no frizz" }, "body": { "height": "approx. 172 cm", "build": "lean athletic, low body fat (18–20%) with pronounced hourglass figure", "neck": "slender, elongated", "clavicles": "prominent, horizontal", "shoulders": "faint muscle definition with delicate venous network", "curves": "subtle feminine curves", "chest": "full bust with natural projection" } }, "subject": { "demographics": "Young adult female (mid‑20s), my exact model Adèle", "hair": { "color": "chestnut brown with natural blonde balayage (bronde), multi‑tonal", "style": "long wavy, cascading over shoulders, with side‑swept curtain bang grazing outer eye corner", "texture": "glossy, healthy, individual strands visible, anisotropic reflections, no frizz" }, "face": { "expression": "soft confident smirk, slightly flirtatious, eyes directly at camera with relaxed gaze, eyelids slightly lowered, chin slightly raised", "gaze": "directly at camera, intense but relaxed", "makeup": "natural, no visible lipstick or heavy foundation", "visibility": "full face visible, head tilted ~15° right, turned ~15° toward camera" }, "body": { "pose": "sitting on a dark couch in a modern restaurant, torso rotated ~20‑30° toward camera, leaning slightly to the right (S‑curve). Left arm bent at elbow (~90°), elbow resting on couch back or armrest, hand relaxed, fingers extended, palm facing down/inward. Right arm raised, bent (~70‑90°), holding wooden chopsticks near face in a pinch grip. Waist‑up framing (from just below bust to above head), camera at chest level (slightly below eye level), distance ~0.8‑1.2 m, centered with slight right offset (rule of thirds).", "posture": "relaxed, confident, elegant", "anatomy": { "curves": "hourglass figure, defined waist", "chest": "full bust with natural projection, accentuated by black bandeau top", "details": "visible collarbones, slender neck, gold bracelets, thin gold necklace" }, "skin_texture": "visible fine pores, micro‑roughness, natural sheen, no airbrushing, subsurface scattering" }, "clothing": { "description": "Black bandeau top (elastic, exposing midriff) and oversized black blazer draped loosely over shoulders. Black trousers with a gold buckle belt. Gold bracelets (multiple, glossy), thin gold necklace. Beige‑brown grain leather handbag on the table. Wooden chopsticks in right hand.", "top": "black bandeau, midriff exposed", "blazer": "black oversized, draped on shoulders", "bottom": "black trousers", "accessories": "gold bracelets, gold necklace, gold belt buckle, beige leather handbag, wooden chopsticks" } }, "environment": { "setting": "Modern restaurant/café with large windows, wooden table, soft couch, indoor palm plant. Bright daylight outside.", "background": { "description": "Large windows with bright daylight, but harsh flash overpowers ambient, making windows appear dark with faint reflections. Blurred people sitting at other tables. Indoor palm leaf partially framing the right side. Wooden table visible at bottom edge, with beige leather handbag.", "lighting": "harsh on‑camera flash (compact digital camera from early 1990s) as main source. Flash creates overexposed highlights on skin, gold jewelry, and chopsticks. Deep shadows under chin, neck, and couch. Ambient daylight is completely overpowered, leaving background dark." } }, "lighting_and_atmosphere": { "source": "on‑camera flash (compact digital camera from early 1990s)", "quality": "harsh flash with high contrast, overexposed highlights on skin and shiny surfaces, deep shadows in background", "effects": [ "strong flash creating specular highlights on cheekbones, nose, collarbones, gold bracelets, necklace, belt buckle, and wooden chopsticks", "overexposed areas on face and body (washed out, ethereal glow)", "background dark with faint window reflections and blurred silhouettes of people and plants", "grainy texture characteristic of early compact digital cameras", "washed out colors, low saturation, with warm undertones from ambient (slightly greenish cast)", "unreal contrast", "subtle chromatic aberration at image edges", "slight barrel distortion from wide‑angle lens" ], "color_cast": "cool flash white balance mixed with warm ambient, creating a unique warm‑cool contrast; blacks appear deep, skin tones pale with golden highlights", "contrast": "very high" }, "camera_and_technical": { "perspective": "slightly low angle (camera at chest level), straight‑on with slight right offset", "camera_position": "handheld, compact digital camera from early 1990s, 28‑35mm equivalent, f/2.8‑f/4", "framing": "vertical 9:16, waist‑up (from just below bust to above head), subject centered with right offset, headroom ~10‑15%", "focus": "slightly soft, typical of low‑resolution cameras with flash, everything in focus (deep focus)", "visual_fidelity": "grainy, low resolution aesthetic, washed out colors, flash photography style, ultra high quality real image (realistic despite lo‑fi look), candid lifestyle fashion snapshot" }, "realism_constraints": { "allowed": [ "grain", "washed out colors", "overexposed highlights", "harsh shadows", "imperfect composition", "natural skin texture", "minor asymmetry", "halation", "chromatic aberration", "barrel distortion" ], "forbidden": [ "face alteration", "identity drift", "plastic skin", "professional studio lighting", "sharp focus", "perfect composition", "cinematic look (modern)", "HDR", "8k", "masterpiece", "excessive makeup", "visible ears (unless naturally covered)", "messy or flat hair", "CGI", "3d render", "modern digital perfection" ] }, "negative_prompt": [ "different face", "beauty filters", "airbrushed skin", "anime", "cartoon", "over-sharpening", "clean digital look", "perfect exposure", "smooth gradients", "visible ears", "ears showing", "messy hair", "flat hair", "greasy hair", "oily face", "greasy skin", "overexposed (beyond intended aesthetic)", "shiny T-zone", "glossy skin", "one-length haircut", "blunt cut", "excessive makeup", "CGI", "3d render", "plastic texture", "smooth", "airbrushed", "digital art", "painting", "deformed face", "asymmetrical eyes", "extra facial features", "blurry", "low detail", "unrealistic proportions", "bad anatomy", "acne", "skin imperfections", "blemishes", "redness", "pimples", "scars", "moles", "watermark (other than 'vgeux')", "text on clothing (other than intended)", "signature", "professional photography", "studio lighting", "sharp focus", "perfect composition", "cinematic (modern)", "8k", "masterpiece", "makeup", "stylized", "modern digital", "HDR" ] }

Ultra-realistic photo of me practicing classical ballet in a bright dance studio. I am wearing white outfit and leggings and ballet slippers, standing at a wooden barre in front of a large mirror. The mirror reflects an empty, spacious room. My body is long 1.80m and athletic 70k C cup, body 90, 60, 90 The floor is made of solid oak parquet in a herringbone pattern. At the back of the room, there are thin blue tatami mats placed on the floor. A small music player is visible in the background, plugged into a wall socket with a cable. On the side of the room, there are two chairs with a small table between them. On the table: a water bottle and a folded pink and white beach towel placed on top of a Nike sports bag. Natural lighting, soft shadows, high detail, photorealistic textures, 50mm lens, depth of field, realistic reflections in the mirror, cinematic composition.

INFRONT OF HIM VIEW,90 DEGREES.kitchen looking towards a sink under a window, with a door on the left of the sink with a 25 cm distance from the kitchen,the kitchen is an L shaped starting from the right corner ,on the far right a fridge nest to it a stove,next the dishwasher then the sink,a smokey grey kitchen with modern touches,taupe walls,a taup ceeling with spot lights inside the celing with 90 cm distance,wooden parquete floor,

looking 90 degrees,human eye infront of him view,kitchen with front perspective looking towards a sink under a window, with a door on the left of the sink with a 25 cm distance from the kitchen,the kitchen is an L shaped starting from the right corner ,on the far right a fridge nest to it a stove,next the dishwasher then the sink,a smokey grey kitchen with modern touches,taupe walls,a taup ceeling with spot lights inside the celing with 90 cm distance,wooden parquete floor,A ultra 4k render created by archviz,elegant,picture like,corona 2023,vray,corona 9,

Create a vaporwave-themed cell phone with 90's elements: Vibrant neon colors, digital grid landscapes, retro-futuristic cityscapes, and iconic 90's mobile phones. Emphasize pink and turquoise hues, with geometric patterns. Include elements like a classic chunky, vintage mobile phone prominently displayed. Incorporate aesthetic features like VHS glitch effects, chrome typography, and floating geometric shapes. Set the scene at twilight to capture the essence of vaporwave with a nostalgic, yet futuristic feel. the name "Google Extension" etched into the phone, filled with typical vaporwave motifs --s 750 --v 6.0 --style raw

A cute little hybrid figure with a Japanese A girl's face, wearing glasses, and a monkey-like body floating on the water. This is a blind box-style toy with a three-dimensional shape, high-definition resolution, and vibrant colors. The overall design is whimsical, charming, and suitable for collectors or decorative purposes. --ar 5:6 --exp 90 --raw --sref https://s.mj.run/9xSByhe7Ve0 --profile 1cmqgxe --sw 60 --oref https://s.mj.run/9xSByhe7Ve0 --ow 90 --stylize 50 --v 7