On November 29,2013 the Shaanxi Coal Chemicals Technology Engineering Center,Ltd.(SCCTEC),the CNOOC Huizhou Refining and Chemical Company and the SINOPEC Luoyang Engineering Company,Ltd.signed an agreement on cooperat...On November 29,2013 the Shaanxi Coal Chemicals Technology Engineering Center,Ltd.(SCCTEC),the CNOOC Huizhou Refining and Chemical Company and the SINOPEC Luoyang Engineering Company,Ltd.signed an agreement on cooperation in development of展开更多
Low-carbon light olefins are the basic feedstocks for the petrochemical industry. Catalytic cracking of crude bio-oil and its model compounds （including methanol, ethanol, acetic acid, acetone, and phenol） to light ...Low-carbon light olefins are the basic feedstocks for the petrochemical industry. Catalytic cracking of crude bio-oil and its model compounds （including methanol, ethanol, acetic acid, acetone, and phenol） to light olefins were performed by using the La/HZSM-5 catalyst. The highest olefins yield from crude bio-oil reached 0.19 kg/（kg crude bio-oil）. The reaction conditions including temperature, weight hourly space velocity, and addition of La into the HZSM-5 zeolite can be used to control both olefins yield and selectivity. Moderate adjusting the acidity with a suitable ratio between the strong acid and weak acid sites through adding La to the zeolite effectively enhanced the olefins selectivity and improved the catalyst stability. The production of light olefins from crude bio-oil is closely associated with the chemical composition and hydrogen to carbon effective ratios of feedstock. The comparison between the catalytic cracking and pyrolysis of bio-oil was studied. The mechanism of the bio-oil conversion to light olefins was also discussed.展开更多
From the viewpoint of process specifics and thermodynamics, this article has put forward a route for maximiza- tion of low-carbon olefins via co-processing of methanol and heavy oil. Catalytic cracking experiments on ...From the viewpoint of process specifics and thermodynamics, this article has put forward a route for maximiza- tion of low-carbon olefins via co-processing of methanol and heavy oil. Catalytic cracking experiments on co-processing of methanol and heavy oil at different ratios in a fixed fluidized bed reactor had been conducted. Test results have revealed that when 12.5% of methanol was blended to the heavy oil a good products distribution and relatively higher yield of low-carbon olefins could be obtained. The overall yield of low-carbon olefins could reach 50.16%, with the yield of ethylene, propylene and butylene equating to 5.47 %, 28.93% and 15.76 %, respectively.展开更多
On November 30, 2018 “The technology for manufacture of xylene from toluene and methanol with coproduction of low-carbon olefins” jointly developed by the Yanchang Petroleum Group (YPG) and the CAS Dalian Institute ...On November 30, 2018 “The technology for manufacture of xylene from toluene and methanol with coproduction of low-carbon olefins” jointly developed by the Yanchang Petroleum Group (YPG) and the CAS Dalian Institute of Chemical Physics (DICP) had passed the appraisal of research achievements. In order to open up a new In order to open up a new technical route for alkylation of toluene to p-xylene, the technical personnel of YPG and DICP have been jointly engaging in the activities for tackling key problems to set up a 10 kt/a commercial unit for producing xylene through reaction of methanol with toluene along with coproduction of low-carbon olefins.展开更多
The complex reaction system of the coal gasification coupling C1 reaction was analyzed based on the principles of thermodynamics. The results show that an increase in the temperature is beneficial to the generation of...The complex reaction system of the coal gasification coupling C1 reaction was analyzed based on the principles of thermodynamics. The results show that an increase in the temperature is beneficial to the generation of hydrocarbons with high carbon-atom contents, in which the alkane yield is higher than the alkene yield. The complex reaction system consisting of C, H20, CO, CO2, H2, C2H4, C3H6 and C4Hs was studied, and the obtained results indicated that when the maximum mole fraction content of C2-C4 olefins was regarded as the optimized objective function, the optimum temperature was approximately 648 K, the pressure was 0.1 MPa, the feed ratio was approximately 0.6, and the maximum mole fraction content of C2-C4 olefins was approximately 28.24%. The thermodynamic simulation and calculation of the complex reaction system can provide a basis for the determination and optimization of actual process conditions and are therefore of great theoretical and practical significance.展开更多
In order to meet the urgent need for reducing olefin content in cracked naphtha, the influence of feedstock characteristics on the olefin content was discussed. The different types and performance of catalysts develop...In order to meet the urgent need for reducing olefin content in cracked naphtha, the influence of feedstock characteristics on the olefin content was discussed. The different types and performance of catalysts developed by RIPP were introduced. Moreover, some effective operation approaches in commercial units were presented to serve as a reference to the refiners for catalyst selection.展开更多
Palladium-catalyzed Mizoroki-Heck reaction is a powerful and efficient method for construction of Csp2–Csp2 bonds.Herein,four palladium complexes(I—IV)with N,O-bidentate ligands(L1—L4)based on N-oxide units from cy...Palladium-catalyzed Mizoroki-Heck reaction is a powerful and efficient method for construction of Csp2–Csp2 bonds.Herein,four palladium complexes(I—IV)with N,O-bidentate ligands(L1—L4)based on N-oxide units from cyclic secondary amines were easily synthesized and successfully applied in Mizoroki-Heck reaction of aryl bromides with electron-deficient olefins.X-ray diffraction analyses indicated the palladium(II)atom of II took the distorted square planar geometry and was four-coordinated by nitrogen and oxygen atoms from two ligands(L2).Two free chloride ions were presented as counter anions in complex II.But the palladium(II)center of IV was coordinated by nitrogen and oxygen atoms from one ligand(L4)as well as two chlorine atoms,which exhibited the nearly square-planar geometry.The study on catalytic properties of palladium complexes revealed that complex II exhibited high activity superior to the other complexes.The coupling reactions of a series of aryl bromides and olefin derivatives proceeded in the presence of 2—5 mol%palladium complex II,giving the desired products in good to excellent yields.The advantages of this method such as good compatibility of functional groups,high yields,and short reaction times made it more attractive for constructing Csp2–Csp2 bonds in the synthesis of functional molecules and materials.展开更多
甲醇制烯烃技术(DMTO,Dimethylether/Methanol to Olefin)是中科院大连化学物理研究所与中石化洛阳工程有限公司和新兴能源科技公司合作开发的具有自主知识产权的低碳烯烃生产新技术。2010年8月采用DMTO技术的世界上首套甲醇制烯烃工业...甲醇制烯烃技术(DMTO,Dimethylether/Methanol to Olefin)是中科院大连化学物理研究所与中石化洛阳工程有限公司和新兴能源科技公司合作开发的具有自主知识产权的低碳烯烃生产新技术。2010年8月采用DMTO技术的世界上首套甲醇制烯烃工业装置在神华包头投料开车成功;2013年2月宁波禾元的DMTO工业装置也投入运行。这两套装置的甲醇进料量均为1.80 Mt/a,烯烃产量为600 kt/a。本文对DMTO工艺机理、工程设计特点和投料运行进行了介绍。DMTO工业装置运行结果表明,DMTO专用催化剂具有非常好的活性、选择性及抗磨损性能;采用大型浅层密相流化床反应器可以发挥催化剂性能,保障反应床层恒温及提高运行可靠性。为了减少开工阶段喷燃烧油可能对催化剂带来的不利影响,两套工业装置的投料开车均采用首创的利用反应热来进行再生器和反应器升温的方法。DMTO工业装置稳定运行时甲醇转化率接近100%,双烯选择性达到80%。72 h标定结果显示,生产1 t烯烃所需要的甲醇原料约为2.97 t。展开更多
文摘On November 29,2013 the Shaanxi Coal Chemicals Technology Engineering Center,Ltd.(SCCTEC),the CNOOC Huizhou Refining and Chemical Company and the SINOPEC Luoyang Engineering Company,Ltd.signed an agreement on cooperation in development of
基金This work is supported by the National Key Basic Program of China （No.2013CB228105） and the National Natural Science Foundation of China （No.51161140331）.
文摘Low-carbon light olefins are the basic feedstocks for the petrochemical industry. Catalytic cracking of crude bio-oil and its model compounds （including methanol, ethanol, acetic acid, acetone, and phenol） to light olefins were performed by using the La/HZSM-5 catalyst. The highest olefins yield from crude bio-oil reached 0.19 kg/（kg crude bio-oil）. The reaction conditions including temperature, weight hourly space velocity, and addition of La into the HZSM-5 zeolite can be used to control both olefins yield and selectivity. Moderate adjusting the acidity with a suitable ratio between the strong acid and weak acid sites through adding La to the zeolite effectively enhanced the olefins selectivity and improved the catalyst stability. The production of light olefins from crude bio-oil is closely associated with the chemical composition and hydrogen to carbon effective ratios of feedstock. The comparison between the catalytic cracking and pyrolysis of bio-oil was studied. The mechanism of the bio-oil conversion to light olefins was also discussed.
文摘From the viewpoint of process specifics and thermodynamics, this article has put forward a route for maximiza- tion of low-carbon olefins via co-processing of methanol and heavy oil. Catalytic cracking experiments on co-processing of methanol and heavy oil at different ratios in a fixed fluidized bed reactor had been conducted. Test results have revealed that when 12.5% of methanol was blended to the heavy oil a good products distribution and relatively higher yield of low-carbon olefins could be obtained. The overall yield of low-carbon olefins could reach 50.16%, with the yield of ethylene, propylene and butylene equating to 5.47 %, 28.93% and 15.76 %, respectively.
文摘On November 30, 2018 “The technology for manufacture of xylene from toluene and methanol with coproduction of low-carbon olefins” jointly developed by the Yanchang Petroleum Group (YPG) and the CAS Dalian Institute of Chemical Physics (DICP) had passed the appraisal of research achievements. In order to open up a new In order to open up a new technical route for alkylation of toluene to p-xylene, the technical personnel of YPG and DICP have been jointly engaging in the activities for tackling key problems to set up a 10 kt/a commercial unit for producing xylene through reaction of methanol with toluene along with coproduction of low-carbon olefins.
基金supported by the National Natural Science Foundation of China(NSFC Grant No. 51706168)
文摘The complex reaction system of the coal gasification coupling C1 reaction was analyzed based on the principles of thermodynamics. The results show that an increase in the temperature is beneficial to the generation of hydrocarbons with high carbon-atom contents, in which the alkane yield is higher than the alkene yield. The complex reaction system consisting of C, H20, CO, CO2, H2, C2H4, C3H6 and C4Hs was studied, and the obtained results indicated that when the maximum mole fraction content of C2-C4 olefins was regarded as the optimized objective function, the optimum temperature was approximately 648 K, the pressure was 0.1 MPa, the feed ratio was approximately 0.6, and the maximum mole fraction content of C2-C4 olefins was approximately 28.24%. The thermodynamic simulation and calculation of the complex reaction system can provide a basis for the determination and optimization of actual process conditions and are therefore of great theoretical and practical significance.
文摘In order to meet the urgent need for reducing olefin content in cracked naphtha, the influence of feedstock characteristics on the olefin content was discussed. The different types and performance of catalysts developed by RIPP were introduced. Moreover, some effective operation approaches in commercial units were presented to serve as a reference to the refiners for catalyst selection.
基金the Natural Science Foundation of Shanxi Province(No.201901D111276)Innovative Program of Graduate Education in Shanxi Province(No.2023KY464)for financial support ofthis work.
文摘Palladium-catalyzed Mizoroki-Heck reaction is a powerful and efficient method for construction of Csp2–Csp2 bonds.Herein,four palladium complexes(I—IV)with N,O-bidentate ligands(L1—L4)based on N-oxide units from cyclic secondary amines were easily synthesized and successfully applied in Mizoroki-Heck reaction of aryl bromides with electron-deficient olefins.X-ray diffraction analyses indicated the palladium(II)atom of II took the distorted square planar geometry and was four-coordinated by nitrogen and oxygen atoms from two ligands(L2).Two free chloride ions were presented as counter anions in complex II.But the palladium(II)center of IV was coordinated by nitrogen and oxygen atoms from one ligand(L4)as well as two chlorine atoms,which exhibited the nearly square-planar geometry.The study on catalytic properties of palladium complexes revealed that complex II exhibited high activity superior to the other complexes.The coupling reactions of a series of aryl bromides and olefin derivatives proceeded in the presence of 2—5 mol%palladium complex II,giving the desired products in good to excellent yields.The advantages of this method such as good compatibility of functional groups,high yields,and short reaction times made it more attractive for constructing Csp2–Csp2 bonds in the synthesis of functional molecules and materials.
