The Shenyang Air Blower (Group) Company, Ltd. has developed the large pyrolysis gas compressor (type H598) with independent intellectual property rights. The compressor train rated at 640 kt/a of ethylene is compo...The Shenyang Air Blower (Group) Company, Ltd. has developed the large pyrolysis gas compressor (type H598) with independent intellectual property rights. The compressor train rated at 640 kt/a of ethylene is composed of a triple cylinder joint movement structure and is specially designed for the steam cracking unit at Maoming Petrochemical Co. Currently this compressor has been shipped to Maoming. The test run of the compressor has shown that the high-, medium- and low-pressure cylinders worked normally in terms of their mechanical movement and performance. The vibration values at all vibration testing points were below 20μ,展开更多
SINOPEC Zhenhai Refining and Chemical Branch Company intends to invest 20 billion RMB (2.4 billion US dollars) to construct in 2010 in Ningbo, Zhejiang province a largest in China petrochemical integrated unit, includ...SINOPEC Zhenhai Refining and Chemical Branch Company intends to invest 20 billion RMB (2.4 billion US dollars) to construct in 2010 in Ningbo, Zhejiang province a largest in China petrochemical integrated unit, including a 1.0 Mt/a ethylene unit. The proposal on construction of this project is awaiting the approval by the Central Govemment. It will take three years to execute the project construction.展开更多
The technology for forced heat transfer in steam cracking furnace tubes invented by the CAS Institute of Metals has been successfully applied within the SINOPEC system and was granted the SINOPEC's first grade Award ...The technology for forced heat transfer in steam cracking furnace tubes invented by the CAS Institute of Metals has been successfully applied within the SINOPEC system and was granted the SINOPEC's first grade Award on Science and Technology Advancement in 2006.展开更多
SINOPEC plans during the “11th Five-Year Plan” period to construct a 800 kt/a steam cracking unit at Zhenhai Refining and Chemical Company. SINOPE has approved the proposal on construction of this unit, which is sch...SINOPEC plans during the “11th Five-Year Plan” period to construct a 800 kt/a steam cracking unit at Zhenhai Refining and Chemical Company. SINOPE has approved the proposal on construction of this unit, which is scheduled for startup by 2008 or 2009. Zhenhai Refining and Chemical Company is located in Zhejiang province and is a giant domestic展开更多
The core of the 1.0 Mt/a ethylene revamp project the 640 kt/a steam cracking unit at SINOPEC Maoming Branch Company after its mechanical completion in July 2006 has been in the phase of production preparations in a bi...The core of the 1.0 Mt/a ethylene revamp project the 640 kt/a steam cracking unit at SINOPEC Maoming Branch Company after its mechanical completion in July 2006 has been in the phase of production preparations in a bid to boost the design ethylene capacity from 360 kt/a to 1.0 Mt/a to become the first in China 1.0-Mt/a-class ethylene base.展开更多
Eight steam cracker convection sections with a treating capacity of 150 kt/a each successfully developed and fabricated by the Maoming Petrochemical Machinery Manufacturing Company, Ltd. have been tested and inspected...Eight steam cracker convection sections with a treating capacity of 150 kt/a each successfully developed and fabricated by the Maoming Petrochemical Machinery Manufacturing Company, Ltd. have been tested and inspected prior to delivery to the 1.2 Mt/a ethylene project site at Dushanzi Petrochemical Company in Xinjiang Uygur Autonomous Region.展开更多
In the course of steam cracking the furnace tubes are apt to coking inside the tube wall, which not only can affect the heat transfer efficiency of the furnace, but also needs regu-lar shutdown for decoking that can r...In the course of steam cracking the furnace tubes are apt to coking inside the tube wall, which not only can affect the heat transfer efficiency of the furnace, but also needs regu-lar shutdown for decoking that can reduce the operating展开更多
The Board of Directors of China Petroleum Company of Taiwan province has ratified the plan for onsite revamp of the third steam cracking unit, intending to construct a naphtha cracking unit to produce 1.0 Mt/a of ethy...The Board of Directors of China Petroleum Company of Taiwan province has ratified the plan for onsite revamp of the third steam cracking unit, intending to construct a naphtha cracking unit to produce 1.0 Mt/a of ethylene and 600 kt/a of propylene. Construction is expected to be commenced in January 2005, and mechanical completion and commissioning of facilities are slated for the end of 2009, and official startup is scheduled in 2011.展开更多
The project “Online Optimized Operation of Steam Cracker Based on Data Searching Technique” implemented jointly by SINOPEC Tianjing Petrochemical Company, SEI and Beijing Chemical University has recently passed in B...The project “Online Optimized Operation of Steam Cracker Based on Data Searching Technique” implemented jointly by SINOPEC Tianjing Petrochemical Company, SEI and Beijing Chemical University has recently passed in Beijing the appraisal on scientific and technical achievements organized by China Petroleum and Chemical Industry Society.展开更多
The technical project relating to the pilot-scale manufactured oil-soluble product--the yellow oil inhibitor used in steam cracker,which is performed by the Beijing SBL Science&Technology Co.,Ltd.,has passed the e...The technical project relating to the pilot-scale manufactured oil-soluble product--the yellow oil inhibitor used in steam cracker,which is performed by the Beijing SBL Science&Technology Co.,Ltd.,has passed the experts’acceptance tests sponsored by Beijing Municipal Science and Technology Commission.This achievement is regarded as an innovative attempt in the world.This product展开更多
PetroChina Fushun Petrochemical Company has rejected a plan to expand the existing 148 kt/a steam cracking unit to 190 kt/a, while intending to construct a 800 kt/a steam cracking unit. The feasibility study is underw...PetroChina Fushun Petrochemical Company has rejected a plan to expand the existing 148 kt/a steam cracking unit to 190 kt/a, while intending to construct a 800 kt/a steam cracking unit. The feasibility study is underway and will be submitted after its completion to relevant government departments. The steam crackers will run on naphtha, and their展开更多
The 600kt/a steam cracker and 300kt/a ethylene glycol(MEG)unit owned by Yangzi-BASF Company,a joint venture be-tween SINOPEC Yangzi Petrochemical Branch Company andBASK have been successfully put on stream.The steamcr...The 600kt/a steam cracker and 300kt/a ethylene glycol(MEG)unit owned by Yangzi-BASF Company,a joint venture be-tween SINOPEC Yangzi Petrochemical Branch Company andBASK have been successfully put on stream.The steamcracker has been operating smoothly since its startup。展开更多
The Research Institute of Yangzi Petrochemical Company (YPC) has completed the study on the project "Use of LPG as Steam Cracking Feedstock" and raised a rationalization proposal. The forecast has shown that the e...The Research Institute of Yangzi Petrochemical Company (YPC) has completed the study on the project "Use of LPG as Steam Cracking Feedstock" and raised a rationalization proposal. The forecast has shown that the economic benefits for production of ethylene brought about by the hydrocracker LPG are enormous. Compared to the naphtha feedstock currently used by YPC, the economic benefit for manufacturing one ton of ethylene from LPG can be higher by 800 RMB. If the annual consumption of LPG amounts to 220 thousand tons,展开更多
Silver modified HZSM-5 (AgHZ) zeolite catalysts were prepared by ion exchange method and their catalytic properties in the l-butene cracking reaction were measured. The catalysts were characterized by infrared spec-...Silver modified HZSM-5 (AgHZ) zeolite catalysts were prepared by ion exchange method and their catalytic properties in the l-butene cracking reaction were measured. The catalysts were characterized by infrared spec- troscopy with pyridine adsorption (Py-IR), N2 adsorption and X-ray diffraction (XRD). The effects of Ag loading and steaming treatment on catalytic performances were studied. It is found that the activity ofHT_SM-5 (HZ) catalyst significantly decreases with the steaming time, whereas AgHZ catalysts show stable activity in the steaming time of 24-48 h and their activities increase with the Ag loading. When the steaming time is 24-48 h, the yield of propylene over HZ catalyst significantly decreases, whereas it is stable over AgHZ catalysts. The AgHZ catalysts with Ag loadings of 0.28%-0.43% (by mass) show similar propylene yields (-30%), which are higher than that over the AgHZ catalyst with a Ag loading of 0.55% (by mass). These results indicate that the steam-treated AgHZ catalysts with optimum Ag loadings have higher yield of propylene and are more stable than the steam- treated HZ catalyst. The regeneration stability measurement in butene cracking also shows that the AgHZ catalyst steam-treated under a suitable condition has better stability than the HZ catalyst.展开更多
文摘The Shenyang Air Blower (Group) Company, Ltd. has developed the large pyrolysis gas compressor (type H598) with independent intellectual property rights. The compressor train rated at 640 kt/a of ethylene is composed of a triple cylinder joint movement structure and is specially designed for the steam cracking unit at Maoming Petrochemical Co. Currently this compressor has been shipped to Maoming. The test run of the compressor has shown that the high-, medium- and low-pressure cylinders worked normally in terms of their mechanical movement and performance. The vibration values at all vibration testing points were below 20μ,
文摘SINOPEC Zhenhai Refining and Chemical Branch Company intends to invest 20 billion RMB (2.4 billion US dollars) to construct in 2010 in Ningbo, Zhejiang province a largest in China petrochemical integrated unit, including a 1.0 Mt/a ethylene unit. The proposal on construction of this project is awaiting the approval by the Central Govemment. It will take three years to execute the project construction.
文摘The technology for forced heat transfer in steam cracking furnace tubes invented by the CAS Institute of Metals has been successfully applied within the SINOPEC system and was granted the SINOPEC's first grade Award on Science and Technology Advancement in 2006.
文摘SINOPEC plans during the “11th Five-Year Plan” period to construct a 800 kt/a steam cracking unit at Zhenhai Refining and Chemical Company. SINOPE has approved the proposal on construction of this unit, which is scheduled for startup by 2008 or 2009. Zhenhai Refining and Chemical Company is located in Zhejiang province and is a giant domestic
文摘The core of the 1.0 Mt/a ethylene revamp project the 640 kt/a steam cracking unit at SINOPEC Maoming Branch Company after its mechanical completion in July 2006 has been in the phase of production preparations in a bid to boost the design ethylene capacity from 360 kt/a to 1.0 Mt/a to become the first in China 1.0-Mt/a-class ethylene base.
文摘Eight steam cracker convection sections with a treating capacity of 150 kt/a each successfully developed and fabricated by the Maoming Petrochemical Machinery Manufacturing Company, Ltd. have been tested and inspected prior to delivery to the 1.2 Mt/a ethylene project site at Dushanzi Petrochemical Company in Xinjiang Uygur Autonomous Region.
文摘In the course of steam cracking the furnace tubes are apt to coking inside the tube wall, which not only can affect the heat transfer efficiency of the furnace, but also needs regu-lar shutdown for decoking that can reduce the operating
文摘The Board of Directors of China Petroleum Company of Taiwan province has ratified the plan for onsite revamp of the third steam cracking unit, intending to construct a naphtha cracking unit to produce 1.0 Mt/a of ethylene and 600 kt/a of propylene. Construction is expected to be commenced in January 2005, and mechanical completion and commissioning of facilities are slated for the end of 2009, and official startup is scheduled in 2011.
文摘The project “Online Optimized Operation of Steam Cracker Based on Data Searching Technique” implemented jointly by SINOPEC Tianjing Petrochemical Company, SEI and Beijing Chemical University has recently passed in Beijing the appraisal on scientific and technical achievements organized by China Petroleum and Chemical Industry Society.
文摘The technical project relating to the pilot-scale manufactured oil-soluble product--the yellow oil inhibitor used in steam cracker,which is performed by the Beijing SBL Science&Technology Co.,Ltd.,has passed the experts’acceptance tests sponsored by Beijing Municipal Science and Technology Commission.This achievement is regarded as an innovative attempt in the world.This product
文摘PetroChina Fushun Petrochemical Company has rejected a plan to expand the existing 148 kt/a steam cracking unit to 190 kt/a, while intending to construct a 800 kt/a steam cracking unit. The feasibility study is underway and will be submitted after its completion to relevant government departments. The steam crackers will run on naphtha, and their
文摘The 600kt/a steam cracker and 300kt/a ethylene glycol(MEG)unit owned by Yangzi-BASF Company,a joint venture be-tween SINOPEC Yangzi Petrochemical Branch Company andBASK have been successfully put on stream.The steamcracker has been operating smoothly since its startup。
文摘The Research Institute of Yangzi Petrochemical Company (YPC) has completed the study on the project "Use of LPG as Steam Cracking Feedstock" and raised a rationalization proposal. The forecast has shown that the economic benefits for production of ethylene brought about by the hydrocracker LPG are enormous. Compared to the naphtha feedstock currently used by YPC, the economic benefit for manufacturing one ton of ethylene from LPG can be higher by 800 RMB. If the annual consumption of LPG amounts to 220 thousand tons,
基金Supported by the National Science Foundation of China(U1162129)the Science and Technology Department of Zhejiang Province(2009R50020)
文摘Silver modified HZSM-5 (AgHZ) zeolite catalysts were prepared by ion exchange method and their catalytic properties in the l-butene cracking reaction were measured. The catalysts were characterized by infrared spec- troscopy with pyridine adsorption (Py-IR), N2 adsorption and X-ray diffraction (XRD). The effects of Ag loading and steaming treatment on catalytic performances were studied. It is found that the activity ofHT_SM-5 (HZ) catalyst significantly decreases with the steaming time, whereas AgHZ catalysts show stable activity in the steaming time of 24-48 h and their activities increase with the Ag loading. When the steaming time is 24-48 h, the yield of propylene over HZ catalyst significantly decreases, whereas it is stable over AgHZ catalysts. The AgHZ catalysts with Ag loadings of 0.28%-0.43% (by mass) show similar propylene yields (-30%), which are higher than that over the AgHZ catalyst with a Ag loading of 0.55% (by mass). These results indicate that the steam-treated AgHZ catalysts with optimum Ag loadings have higher yield of propylene and are more stable than the steam- treated HZ catalyst. The regeneration stability measurement in butene cracking also shows that the AgHZ catalyst steam-treated under a suitable condition has better stability than the HZ catalyst.