Summary of the domestic refining, ethylene, and related projects – please provide additional details to complete it
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:Handshake: To facilitate the work of those involved in petrochemical planning, I have listed some information I have at hand; I ask colleagues to add any information they are aware of in this post. Note: All of my data comes from publicly available reports on the Internet. The statistics cover domestic refineries with a capacity of 10 million tons and above, as well as 800,000 tons of ethylene capacity, along with their associated downstream facilities and related investments. Add **details on the petrochemical revitalization plan.** Related content: 40 major projects included in the petrochemical revitalization plan. According to the detailed plans for the petrochemical industry, the overall goal is for the growth rate of this industry to be in line with the overall development pace of the national economy, with an average annual increase in added value of around 15%; by 2011, the added value is expected to reach 1.75 trillion yuan. At the same time, 20 major projects under construction and 20 major new projects have been included in the plan. All of these are based on the adjustment and revitalization plan. The three-year goals are set in a step-by-step manner. It can be seen from the projects given priority in the plan that products such as refining, ethylene, xylene (PX), purified terephthalic acid (PTA), fertilizers, and olefins receive direct support. The 20 key construction projects that need to be given close attention include: Fujian Refining’s 700,000-ton PX plant, Huizhou’s 1 million-ton PX plant, Shanghai Petrochemical’s 600,000-ton PX plant, Urumqi in Xinjiang’s 1 million-ton PX plant, Foshan Shishi in Fujian’s 600,000-ton PTA plant, Jiangyin Hanbang in Jiangsu’s 600,000-ton PTA plant, and Fuling in Chongqing’s 600,000-ton PTA plant. The petrochemical ethylene production capacity includes: 12 million tons of oil refining in Huizhou, Guangdong; 10 million tons of oil refining expansion and upgrade plus 1 million tons of ethylene in Xin*Dushanzi; 12 million tons of oil refining expansion and upgrade plus 800,000 tons of ethylene in Fujian Refining & Chemical; 12.5 million tons of oil refining expansion and upgrade plus 1 million tons of ethylene in Tianjin; 10 million tons of oil refining in Guangxi; 1 million tons of ethylene in Zhenhai; 800,000 tons of ethylene in Fushun; 1.2 million tons of ethylene expansion and upgrade in Daqing; and 500,000 tons of olefins produced from heavy oil in Shenyang. (Add details on the specific supporting projects for each party?) ) The fertilizer projects include: 1.2 million tons of phosphoric ammonium fertilizer produced by Yunnan Yuntianhua, 1 million tons of potash-magnesium fertilizer produced by Qinghai CITIC Guoan, and 800,000 tons of urea produced in Korla, Xinjiang. It also includes Shenhua Baotou’s 600,000-ton coal-to-olefins project. In addition to the overall goal, the revitalization plan sets three-year phased goals: maintaining stable operations in 2009, with the growth rate of industrial added value exceeding 10% ； The upgrade of oil product quality was largely completed in 2010, the goals set out in the 11th Five-Year Plan were mostly achieved, and the growth rate of industrial added value reached 15% ； By 2011, the adjustment of the industrial structure and layout was largely completed, the allocation of resources in industrial clusters was continuously improved, institutional and policy-related issues were properly resolved, and the growth rate of industrial added value reached 20%. Company Name, Project Name, Total Investment, Sub-projects, Plant Capacity, Investment Amount, Status (Completed/Under Construction/Planned). CNPC Group, Sichuan Ethylene – Refining, Refining: 1000, 21 billion. Ethylene and Related Projects (I): Aromatic Extraction – 35; Butadiene Extraction – 150,000 tons per year; Styrene Butadiene Rubber – 150,000 tons per year; Bisphenol A – 130,000 tons per year; Ethylene – 800,000 tons per year. Polyethylene: HDPE – 30, LDPE – 30; Phenol Propyl Ether – 180,000/110,000 tons per year; Ethylene Glycol – 360,000 tons per year; Butanone Octanol – 210,000/80,000 tons per year; Acrylic Acid – 190,000/220,000 tons per year. The main products produced are polyethylene, ethylene glycol, acrylic acid and its derivatives, butanone, octanol, phenol, propyl ether, bisphenol A, and styrene butadiene rubber. Dushanzi Petrochemical – Refining, Ethylene and Related Projects (II): Refining: 1000; Ethylene: 100 (120?): Polyethylene: 60; Polypropylene: 50? Fushun Petrochemical: Refining, Ethylene and Related Projects (I) – Refining: 1000; Ethylene: 80; 12.525 billion. Polyethylene: 60, of which HDPE: 45 and LDPE: 35. Polypropylene: 30. Ethylene glycol. Daqing Petrochemical? Others? Sinopec Group: Company Name, Project Name, Total Investment, Sub-projects, Plant Capacity, Investment Amount, Status (Completed/Under Construction/Planned). Tianjin Petrochemical: Refining, Ethylene and Related Projects (I) – Refining: 12.5 million tons per year; Ethylene: 1.2 million tons per year; Polyethylene: 600,000 tons per year; Polypropylene: 600,000 tons per year; Ethylene Glycol: 360,000 tons per year; Pure Benzene: 200,000 tons per year; Ethylene Tar: 170,000 tons per year; Styrene: 550,000 tons per year; Polystyrene: 200,000 tons per year; ABS: 300,000 tons per year. Fujian Refining & Chemical: Refining, Ethylene and Related Projects (II) – Refining: 12 million tons per year; Ethylene: 800,000 tons per year; Polyethylene: 800,000 tons per year; Polypropylene: 400,000 tons per year; Xylenes and Other Aromatic Compounds: 700,000 tons per year. Wuhan Petrochemical: Refining, Ethylene and Related Projects (II) – Refining: ?; Ethylene: 800,000 tons per year; Investment amount: 14.67 billion yuan; Yangba? Shanghai Petrochemical? Zhenhai Petrochemical? Yanbian Petrochemical? CNOOC Group: Project Name, Total Investment, Sub-projects, Plant Capacity, Investment Amount. Refining, Ethylene and Related Projects (I): Refining – 1200; Ethylene – 80; Polyethylene – 24; HDPE – 20; LDPE – 25; Ethylene Oxide/Styrene – 25/56; Ethylene Glycol – 32. Refining, Ethylene and Related Projects (II): Refining – 1200; Ethylene – 100; Polyethylene – 70; Polypropylene – 60; Butyl Octyl Alcohol – 25; Others?
The Sinopec and Guangdong refinery project in Jieyang was signed during that period.
With so many new oil refining and ethylene production projects being launched, it seems that competition in this industry will become increasingly fierce in the future
The 10-million-ton refinery, a joint venture between CNPC and Russia, is located in the Tianjin Lingang New Area.
Dalian is also planning to launch an ethylene project; the site has been prepared and is awaiting **approval**.
Chongqing’s MDI integration project in collaboration with BASF: a chemical industry project in the upper reaches of the Yangtze River
Relevant statistical data on Jinxī Petrochemical Branch’s 10 million tons per year processing project for Russian crude oil: (1) Location of construction: Within the Comprehensive Industrial Park in Beigang Industrial Zone, Huludao Economic Development Zone, Liaoning Province. (2) Total project investment: 18.57214 billion yuan. (3) Investment structure: The entire project is funded and constructed by PetroChina Corporation. (4) Construction period and commissioning date: The project’s construction period is 3 years, with commissioning expected in 2011. List of main items in refinery engineering: Plant name, Capacity, Main engineering contents. I. Main plants: Atmospheric and vacuum distillation unit, 1000×104 t/a; 1. Crude oil heat exchange ； 2. Electrodesalination ； 3. Initial distillation ； 4. Atmospheric distillation 5. Vacuum distillation ； 6. Light hydrocarbon recovery ； 7. One removal, three injections, etc. Residue hydrodesulfurization unit: 300×104 t/a; 1. Hydrogenation reaction ； 2. Hydrogen compression ； 3. Cyclohydrogen desulfurization 4. Fractionation, etc. Wax oil hydrocracking unit: 170×104 t/a. 1. Hydrogenation reaction (including compressor) ； 2. Fractionation ； 3. Desulfurization 4. LPG recovery, etc. Heavy oil catalytic cracking (including dry gas and liquefied gas desulfurization, liquefied gas hydrodesulfurization): 260×104 t/a. The catalytic cracking section includes reaction-regeneration units, distillation units, absorption and stabilization systems, main fan flue gas energy recovery units, air compression units, and waste heat boilers. 2. Product refining includes desulfurization of dry gas and liquefied gas, as well as desulfurization and denaturation of liquefied gas. Continuous reforming – Aromatic extraction: Continuous reforming capacity: 220×104 t/a; Continuous reforming unit (reforming reaction section and catalyst regeneration section). Aromatic extraction capacity: 100×104 t/a. 1. Aromatic extraction ； 2. Benzene-toluene distillation ； 3. Xylene separation. Catalytic gasoline hydrogenation 80×104 t/a 1. Selective hydrogenation ； 2. Hydrodesulfurization. Diesel hydrorefining 330×104 t/a 1. Hydrogenation reaction (including compressor) ； 2. Cyclohydrogen desulfurization ； 3. Fractionation section, etc. Diesel hydroprocessing 100×104 t/a 1. Hydrogenation reaction (including compressor) ； 2. Fractionation section, etc. Naphtha hydrogenation 240×104 t/a 1. Hydrogenation reaction ； 2. Gas-liquid separation. Light hydrocarbon recovery: 300×104 t/a 1. Raw gas treatment section ； 2. Butane removal section ； 3. Deethanization section ； 4. LPG treatment section ； 5. Naphtha separation section: Gas distillation unit, 40×104 t/a. 1. Four precision liquefied gas distillation columns, namely a propylene removal column, an ethane removal column, and two propylene columns ； 2 pumps ； 3. Heat exchange system. Polypropylene 15×104 t/a 1. Preparation of promoters and catalysts ； 2. Polymerization ； 3. Polymer degassing ； 4. Vapor-phase copolymerization ； 5. Polymer vaporization ； 6. Process facilities ； 7. Monomer purification ； 8. Addition of additives, extrusion granulation, and packaging ； 9. Storage. MTBE plant 7×104t/a 1. Etherification reactor ； 2. Catalytic distillation ； 3. Methanol recovery. Hydrogen production unit: 7×104 m3/h; 1. Raw material compression ； 2. Raw material refinement ； 3. Water vapor conversion ； 4. Conversion gas transformation ； 5. PSA purification ； 6. Steam generation and waste heat recovery. Hydrogen purification 11×104 m3/h 1. Raw material pretreatment ； 2. PSA purification ； 3. Desorbed gas compression. Construction scale of various units in the refining project
Serial Number | Unit Name | Nominal Production Capacity (104 t/a) | Actual Processing Capacity (104 t/a) | Source
1 | Atmospheric and Vacuum Distillation | 1000 | Russian crude oil: 1000, transported to the crude oil tank farm via pipelines outside the boundary area |
2 | Residue Hydrodesulfurization | 300 | Paraffin oil: 104.41, from atmospheric and vacuum distillation; Vacuum residue: 146.20; Recycled oil: 45.00, from heavy oil catalytic cracking |
3 | Paraffin Oil Hydrocracking | 170 | Paraffin oil: 170.19, from atmospheric and vacuum distillation |
4 | Heavy Oil Catalytic Cracking | 260 | Hydrodesulfurized residue: 248.99, from residue hydrodesulfurization; Hydrocracking tail oil: 0.85, from paraffin oil hydrocracking |
5 | Gas Fractionation | 40 | FCC liquefied gas: 38.00, from heavy oil catalytic cracking |
6 | Polypropylene | 15 | Propylene: 12.63, from gas fractionation |
7 | MTBE | 7 | Mixed C4: 21.51, from gas fractionation; Methanol: 2.24, purchased externally |
8 | Catalytic Gasoline Hydrogenation | 80 | Catalytic gasoline: 72.65, from heavy oil catalytic cracking; Reforming hydrogen: 0.49, from continuous reforming |
9 | Naphtha Hydrogenation | 240 | Top stream from residue hydrodesulfurization stripper: 1.09, from residue hydrodesulfurization; Top stream from residue hydrodesulfurization fractionator: 2.60; Straight-run naphtha: 226.62, from atmospheric and vacuum distillation; Top stream from diesel hydrogenation fractionator: 5.79, from diesel hydrogenation |
10 | Light Hydrocarbon Recovery | 300 | Reforming liquefied gas: 7.10, from continuous reforming; Top stream from hydrocracking fractionator: 36.47, from paraffin oil hydrocracking; Top gas from diesel hydrogenation stripper: 5.41, from diesel hydrogenation; Top gas from hydrocracking stripper: 1.45, from paraffin oil hydrocracking; Top stream from hydrocracking stripper: 12.34; Top gas from residue hydrodesulfurization stripper: 5.91, from residue hydrodesulfurization; Products after naphtha hydrogenation reaction: 237.16, from naphtha hydrogenation |
11 | Continuous Reforming – Aromatics Extraction | 220 | Heavy naphtha: 221.93, from light hydrocarbon recovery |
12 | Diesel Hydrogenation Refining | 330 | Straight-run diesel: 325.58, from atmospheric and vacuum distillation |
13 | Diesel Hydrogenation Modification | 100 | Catalytic diesel: 57.22, from heavy oil catalytic cracking; Diesel from residue hydrodesulfurization: 34.20, from residue hydrodesulfurization |
14 | Sulfur Recovery | 10 | Acidic gas: 10.46, from acidic gases generated by various units |
15 | Hydrogen Production | 7×10^4 Nm³/h | Liquefied gas: 10.79, transported to the unit via pipelines; Dry gas from the unit: 5.52 |
16 | PSA | 11×10^4 Nm³/h | Light ends gas from diesel hydrogenation modification: 0.46, from diesel hydrogenation modification; Light ends gas from diesel hydrogenation refining: 1.63, from diesel hydrogenation refining; Light ends gas from paraffin oil hydrocracking: 1.62, from paraffin oil hydrocracking; Light ends gas from residue hydrodesulfurization: 1.63, from residue hydrodesulfurization; Hydrogen-containing gas from continuous reforming: 16.82, from continuous reforming |
Table: Overall product plan for the refining project
Serial Number | Name | Specification | Output (104 t/a) | Production Unit or Source
1 | Benzene | — | 17.75 | Aromatics extraction |
2 | Xylenes | — | 42.61 | Aromatics extraction |
3 | Polypropylene | — | 12.44 | Polypropylene production |
4 | Liquefied Gas | — | 40.03 | Various units |
5 | Gasoline, 97# (component for ethanol-blended gasoline) | — | 60.48 | Heavy oil catalytic cracking: 71.90; Continuous reforming – Aromatics extraction: 135.82 | ； Naphtha: 40.13 ； MTBE: 6.09 97# (National IV) 81.25 93# (National IV) 66.14 93# (component for ethanol-blended gasoline) 46.07 Total: 253.94 6 Aviation kerosene (150–230°C): 38.62 Atmospheric and vacuum distillation: 25.00 ； Wax oil hydrocracking: 13.62. 7 Diesel, Euro IV: 511.10; Diesel hydroprocessing: 320.76 ； Diesel hydroprocessing: 84.82 ； Wax oil hydrocracked diesel: 105.52; 8 – Propane; 3.66 – Gas fractionation; 9 – Sulfur; 9.82 – Sulfur recovery. Subtotal 929.98
Serial Number | Unit Name | Nominal Production Capacity (104 t/a) | Actual Processing Capacity (104 t/a) | Source
1 | Atmospheric and Vacuum Distillation | 1000 | Russian crude oil: 1000, transported to the crude oil tank farm via pipelines outside the boundary area |
2 | Residue Hydrodesulfurization | 300 | Paraffin oil: 104.41, from atmospheric and vacuum distillation; Vacuum residue: 146.20; Recycled oil: 45.00, from heavy oil catalytic cracking |
3 | Paraffin Oil Hydrocracking | 170 | Paraffin oil: 170.19, from atmospheric and vacuum distillation |
4 | Heavy Oil Catalytic Cracking | 260 | Hydrodesulfurized residue: 248.99, from residue hydrodesulfurization; Hydrocracking tail oil: 0.85, from paraffin oil hydrocracking |
5 | Gas Fractionation | 40 | FCC liquefied gas: 38.00, from heavy oil catalytic cracking |
6 | Polypropylene | 15 | Propylene: 12.63, from gas fractionation |
7 | MTBE | 7 | Mixed C4: 21.51, from gas fractionation; Methanol: 2.24, purchased externally |
8 | Catalytic Gasoline Hydrogenation | 80 | Catalytic gasoline: 72.65, from heavy oil catalytic cracking; Reforming hydrogen: 0.49, from continuous reforming |
9 | Naphtha Hydrogenation | 240 | Top stream from residue hydrodesulfurization stripper: 1.09, from residue hydrodesulfurization; Top stream from residue hydrodesulfurization fractionator: 2.60; Straight-run naphtha: 226.62, from atmospheric and vacuum distillation; Top stream from diesel hydrogenation fractionator: 5.79, from diesel hydrogenation |
10 | Light Hydrocarbon Recovery | 300 | Reforming liquefied gas: 7.10, from continuous reforming; Top stream from hydrocracking fractionator: 36.47, from paraffin oil hydrocracking; Top gas from diesel hydrogenation stripper: 5.41, from diesel hydrogenation; Top gas from hydrocracking stripper: 1.45, from paraffin oil hydrocracking; Top stream from hydrocracking stripper: 12.34; Top gas from residue hydrodesulfurization stripper: 5.91, from residue hydrodesulfurization; Products after naphtha hydrogenation reaction: 237.16, from naphtha hydrogenation |
11 | Continuous Reforming – Aromatics Extraction | 220 | Heavy naphtha: 221.93, from light hydrocarbon recovery |
12 | Diesel Hydrogenation Refining | 330 | Straight-run diesel: 325.58, from atmospheric and vacuum distillation |
13 | Diesel Hydrogenation Modification | 100 | Catalytic diesel: 57.22, from heavy oil catalytic cracking; Diesel from residue hydrodesulfurization: 34.20, from residue hydrodesulfurization |
14 | Sulfur Recovery | 10 | Acidic gas: 10.46, from acidic gases generated by various units |
15 | Hydrogen Production | 7×10^4 Nm³/h | Liquefied gas: 10.79, transported to the unit via pipelines; Dry gas from the unit: 5.52 |
16 | PSA | 11×10^4 Nm³/h | Light ends gas from diesel hydrogenation modification: 0.46, from diesel hydrogenation modification; Light ends gas from diesel hydrogenation refining: 1.63, from diesel hydrogenation refining; Light ends gas from paraffin oil hydrocracking: 1.62, from paraffin oil hydrocracking; Light ends gas from residue hydrodesulfurization: 1.63, from residue hydrodesulfurization; Hydrogen-containing gas from continuous reforming: 16.82, from continuous reforming |
Table: Overall product plan for the refining project
Serial Number | Name | Specification | Output (104 t/a) | Production Unit or Source
1 | Benzene | — | 17.75 | Aromatics extraction |
2 | Xylenes | — | 42.61 | Aromatics extraction |
3 | Polypropylene | — | 12.44 | Polypropylene production |
4 | Liquefied Gas | — | 40.03 | Various units |
5 | Gasoline, 97# (component for ethanol-blended gasoline) | — | 60.48 | Heavy oil catalytic cracking: 71.90; Continuous reforming – Aromatics extraction: 135.82 | ； Naphtha: 40.13 ； MTBE: 6.09 97# (National IV) 81.25 93# (National IV) 66.14 93# (component for ethanol-blended gasoline) 46.07 Total: 253.94 6 Aviation kerosene (150–230°C): 38.62 Atmospheric and vacuum distillation: 25.00 ； Wax oil hydrocracking: 13.62. 7 Diesel, Euro IV: 511.10; Diesel hydroprocessing: 320.76 ； Diesel hydroprocessing: 84.82 ； Wax oil hydrocracked diesel: 105.52; 8 – Propane; 3.66 – Gas fractionation; 9 – Sulfur; 9.82 – Sulfur recovery. Subtotal 929.98
1 Overview of the construction project The Sinopec 10 million tons per year refining project in China is planned to be built within the Sichuan Petrochemical Complex in Longfeng Town, Pengzhou City, Sichuan Province. The total investment for this project amounts to 16.92605 billion RMB ； China National Petroleum Corporation holds 75%, while Sichuan Chengdu Petrochemical Co., Ltd. holds 25%. Of this amount, 15.84665 billion yuan is allocated to construction investments, while approximately 3.17724 billion yuan is needed for environmental protection efforts; thus, the proportion invested in environmental protection is around 20.05%. The project construction period is 3 years, with production expected to begin in 2010. 1.1 Project Composition, Production Scale, and Product Plan The refining project consists of the main plant, utility systems, auxiliary facilities, storage and transportation systems, and environmental protection measures. The main project includes 12 sets of units, namely: 8 oil refining units: a vacuum distillation unit with a capacity of 1000×104 t/a, a residue hydrodesulfurization unit with a capacity of 300×104 t/a, a wax oil hydrocracking unit with a capacity of 220×104 t/a, a diesel hydrorefining unit with a capacity of 350×104 t/a, a heavy oil catalytic cracking unit with a capacity of 250×104 t/a, a gas fractionation unit with a capacity of 60×104 t/a, an MTBE production unit with a capacity of 17×104 t/a, a continuous reforming unit with a capacity of 200×104 t/a, and a PX production unit with a capacity of 60×104 t/a. 2 sets of chemical plants: a 6.5×104 t/a butene-1 plant and a 30×104 t/a polypropylene plant. 2 hydrogen production units: a 7×104 m3/h hydrogen production unit and a 6×104 m3/h PSA unit. Utility facilities include water, electricity, steam, etc ； Supporting services include telecommunications, fire protection, office systems, maintenance, etc ； Environmental protection projects consist of two parts. The environmental protection facilities for the refining project include a 6.0×104 t/a sulfur recovery unit (including acidic water stripping and solvent regeneration), 4 on-site pretreatment stations for oily wastewater, a plant-wide wastewater treatment plant with a capacity of 700 m3/h, and flares ； The other part consists of integrated refining and chemical processing facilities, including a 120 m3/h high-concentration saline wastewater treatment unit, a 1400 m3/h plant-wide wastewater reuse treatment station, a 1300 m3/h low-concentration saline wastewater reuse treatment station, 2×500 m3/h rainwater reuse treatment stations, a 65,000 m3 plant-wide emergency wastewater storage tank, a 65,000 m3 plant-wide fire wastewater storage tank, a 100,000 m3 plant-wide post-rainwater collection tank, an environmental protection monitoring station, and landscaping areas. The total crude oil processing capacity of the entire plant is 1000×104 tons per year; the detailed product portfolio is shown in Table 21.1-1. Table 1.1-1 Overall Product Plan for the Refining Project Sequence Number Name Specification Production Volume (104 t/a) Production Unit or Source I. Products 1 Benzene 37.07 Aromatic complex and ethylene unit. 2 Diphenylxylene 60.22 Aromatic compounds combined. 3 Polypropylene 27.31 Polypropylene. 4-butene-1 6.52 Butene-1. 6 Diesel, Euro IV, 358.53 – Diesel hydroprocessing. 7 Gasoline, Euro III, 97# 41.55 Paraffin hydrocracking: Light naphtha 14.64 ； Heavy oil catalytic cracking: gasoline 105.97 ； Continuous reforming pretreatment: 0.36 for gasoline ； PX Combined: Heavy Aromatics 10.82 ； Continuous reforming: High-octane gasoline 52.0 ； MTBE: 17.18. Euro III 93# 82.59 Euro IV 97# 38.72 Euro IV 93# 38.11 Total 200.97 8 Aviation kerosene (190–210°C) 51.66 Atmospheric and vacuum distillation: 34.04 ； Wax oil hydrocracking: 17.62. 9 Sulfur 5.22 Sulfur recovery. Subtotal: 747.50, accounting for 69.2% of the total product volume. II. Feedstocks for ethylene cracking: 1. Propane, 5.64 – Gas fractionation. 2 Saturated liquefied gas 20.24 Atmospheric and vacuum distillation, wax oil hydrogenation, continuous reforming. 3 C4 24.3 Gas fractionation, butene-1. 4 Hydrogenated naphtha 21.29 Paraffin hydrocracking, residue hydrogenation, and diesel hydrogenation. 4 Straight-run naphtha 65.4 Atmospheric and vacuum distillation. 6 Reformate residue oil 31.41 Continuous reforming–PX combined process. 7 Hydrocracking tail oil 81.67 Paraffin hydrocracking. Subtotal: 249.95, accounting for 23.2% of the total product volume. III. Fuels 1. Catalyst slurry 7.26 – Heavy oil catalytic cracking. 2 Catalytic coke 19.37 Heavy oil catalytic cracking. 3 Hydrogen production exhaust gas 11.56 Hydrogen production. 4 Fuel dry gas: 37.87; various units: subtotal of 76.06, accounting for 7.6% of the total output. Total: 1073.51 1.2 Raw materials, fuels, and sources The main raw materials used in this project are crude oil, methanol, and natural gas. The crude oil processing capacity of this project is 10 million tons per year, of which 6 million tons per year are Kazakhstani crude oil represented by Kumkol oil, 2 million tons per year are crude oil from southern Xinjiang, and 2 million tons per year are crude oil from northern Xinjiang. The methanol used in this project is purchased from the market, with a consumption volume of 65,100 tons per year. The annual consumption of natural gas for this project is 311,200 tons, of which 167,600 tons are used as raw material for hydrogen production, and 143,600 tons are used as fuel. Natural gas is purchased from the market and supplied by the Southwest Oilfield Branch of PetroChina. The fuel used in this project is domestically produced desulfurized dry gas, with any shortfall supplemented by commercial natural gas provided by the Southwest Oilfield Branch of China National Petroleum Corporation. The total fuel consumption is estimated to be around 532,800 tons per year, of which 389,300 tons per year will come from domestically produced desulfurized dry gas, while 143,600 tons per year will be supplied as natural gas from external sources.
Normally it’s just bits and pieces of information; here, they’re compiled together, which saves us time. Thank you, friends :) :)
Could the design institute in charge of these projects provide some additional information?
The overall design firm for Chongqing’s MDI integration project is Chengdu Chengda Company, which was formerly known as the Eighth Chemical Research Institute. The design firm for Dalian Petrochemical’s expansion project to process sulfur-containing crude oil from Russia seems to be Sinopec Luoyang Petrochemical Engineering Company. Everyone can also share information regarding project management, such as the project management company (PMC) and the supervision agency, etc. This post was last edited by Ponny on 2009-4-21 at 11:16
I didn’t see any introduction to the Guangxi Petrochemical refining project, so let’s add that information. CNPC’s Guangxi Petrochemical refinery with a capacity of 10 million tons per year is located in the Qinzhou Port Economic Development Zone along the Beibu Gulf in southern China. Its main purpose is to process a portion of the crude oil produced by CNPC overseas. The main units include key production facilities such as 10 million tons per year of atmospheric and vacuum distillation, 3.5 million tons per year of heavy oil catalytic cracking, 2.2 million tons per year of wax oil hydrocracking, 2.2 million tons per year of continuous reforming, 2.4 million tons per year of diesel hydrotreating, 600,000 tons per year of gas fractionation, 1.2 million tons per year of gasoline hydrotreating, 200,000 tons per year of polypropylene production, and 10,000 tons per year of sulfur recovery; in addition, there are supporting facilities such as utility systems, tank farms, docks and dock storage areas, and dedicated railway lines. The process technologies are mostly introduced from abroad. The basic design is mainly carried out by foreign companies, while the detailed design is entrusted to domestic engineering firms; the main design institute is the PetroChina East China Design Institute.