Industrial Catalysis 2012 Vol.20

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Research progress in Keggintype heteropolyacids catalysts for esterification
LI Jinlei, HU Bing
   DOI: 10.3969/j.issn.10081143.2012.01.001
Abstract937)      PDF(pc) (374KB)(2090)       Save
The structure and properties of heteropoly acids were summarized.The research on and application of heteropolyacids and heteropolyacid supported catalysts in the esterification at home and abroad were reviewed.The development prospects of heteropolyacids were also outlined.The problems of the solubility of active components,and the relationship of catalytic activity and supporting mechanism are the research emphases in the future.Heteropolyacid supported catalysts in the esterification have good application prospect.
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Transesterification of dimethyl carbonate and phenyl acetate to diphenyl carbonate
WANG Lihui1,2;MA Fei1;LI Jianguo1;YANG Xiangui1;WANG Gongying1
   DOI: 10.3969/j.issn.10081143.2012.01.002
Abstract869)      PDF(pc) (373KB)(1634)       Save
The different synthesis methods and application of diphenyl carbonate(DPC) were introduced.The research status of reaction thermodynamics and the catalysts for the interesterification system of dimethyl carbonate and phenyl acetate to diphenyl carbonate was reviewed on the basis of comparison of synthesis methods.The application prospect of the interesterification system was outlined.
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Development status of ethylbenzene dehydrogenation catalysts
YIN Huiming;LIN Hong;WANG Jilong;WANG Tao;YAO Wenjun;HU Xiaoli;BAI Jiejun;XIN Guoping
   DOI: 10.3969/j.issn.10081143.2012.01.003
Abstract1008)      PDF(pc) (392KB)(3755)       Save
Advance on ethylbenzene dehydrogenation catalysts was reviewed and the companies that developed and produced ethylbenzene dehydrogenation catalysts were introduced. Based on the development status of ethylbenzene dehydrogenation to styrene,the Smart technology and oxidative dehydrogenation technology were summarized,including the catalysts applied in the new processes.
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Study on nano copper-based catalyst for catalytic hydrogenolysis of glycerol to 1,3-propanediol
JIAO Guozhu;ZHANG Weiwei;LvZhiguo
   DOI: 10.3969/j.issn.1008-1143.2012.01.004
Abstract961)      PDF(pc) (477KB)(1349)       Save
Nano CuO-TiO2/SiO2 copper-based catalyst was prepared by co-precipitation method and was used in the catalytic hydrogenolysis of glycerol to 1,3-propanediol in a fixed bed microreactor.The structure and morphology of the catalyst were characterized by XRD and SEM.The catalytic performance of the catalyst for hydrogenolysis of glycerol was investigated.The results showed that glycerol conversion of 35.66% and the selectivity to 1,3- propanediol of 78.18% were attained under the optimum condition as follows:reaction temperature 190 ℃,hydrogen pressure 4.5 MPa,n(hydrogen)∶n(glycerol)=50∶1 and liquid hourly space velocity 0.30 h-1.
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Effect of pretreatment temperature on the performance of SAPO-11 catalyst for the skeletal isomerization of n-butene
LI Xiuming1,2;LIAO Kejian1;TONG Mingyou2;ZHU Jinjian1,2
   DOI: 10.3969/j.issn.1008-1143.2012.01.005
Abstract972)      PDF(pc) (356KB)(986)       Save
SAPO-11 molecular sieve was synthesized by hydrothermal method.H-SAPO-11 molecular sieve was prepared by oxalic acid washing,dryness and calcination.The influence of pretreatment temperature on the physicochemical properties of the catalyst was investigated.The catalyst was characterized by XRD,XRF,IR and NH3-TPD.The results indicated that H-SAPO-11 molecular sieve pretreated at 500 ℃ had higher crystallinity and more Brnsted acid sites,and exhibited better catalytic activity,selectivity and stability for the skeletal isomerization reaction of n-butene.
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Influence of γ-Al2O3 support modification on the performance of the catalysts for cyclohexanone dimer dehydrogenation to o-phenylphenol
LI Jie;QU Yixin;WANG Shui;WANG Jidong
   DOI: 10.3969/j.issn.1008-1143.2012.01.006
Abstract835)      PDF(pc) (436KB)(1203)       Save
The influence of modification of γ-Al2O3 with metal oxides La2O3,Ce2O3,MgO and CaO on the properties of 0.5%Pt-5%K2O/γ-Al2O3 catalyst for the dehydrogenation of cyclohexanone dimer(dimer) to o-phenylphenol was investigated.The results showed that the catalyst prepared by using γ-Al2O3 modified with CaO could significantly increase the yield of o-phenylphenol.The highest yield of o-phenylphenol of 95.6% over the catalyst was attained under the optimal modification condition as follows: CaO dosage 20% of support mass,calcination temperature 600 ℃,calcination time 5 h.The catalysts were characterized by XRD,XPS,H2-TPR and NH3-TPD techniques and the effects of CaO modification on the catalyst performance were discussed.
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Synthesis of NaY molecular sieve with high ratio of Si/Al
GU Jianfeng1;Cui Louwei1;Wang Xinxing1;YUAN Zhongyong2
   DOI: 10.3969/j.issn.1008-1143.2012.01.007
Abstract917)      PDF(pc) (384KB)(1291)       Save
Using commercial raw materials,NaY molecular sieves with high SiO2/Al2O3 ratio and high crystallinity were directly synthesized by hydrothermal crystallization method.NaY molecular sieves with SiO2/Al2O3 molar ratio of 5.85-6.05 and relative crystallinity of over 85% were attained.The influence of aging time and temperature of the seed-gel,the alkalinity of the initial gel and pre-crystallization temperature and time on SiO2/Al2O3 ratio and relative crystallinity of NaY molecular sieves was investigated.The optimal synthesis condition of high-silica NaY molecular sieves was proposed.
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Research on olefin selective hydrogenation catalyst for reforming heavy aromatic oil
HE Long1,2;GAO Junbin2;YAO Zhilong2
   DOI: 10.3969/j.issn.1008-1143.2012.01.008
Abstract1004)      PDF(pc) (377KB)(1087)       Save
The performance of palladium supported catalysts for selective hydrogenation and deolefin of reforming heavy aromatic oil was studied.The catalyst supports,loadings of noble metal and the additive were investigated using the reforming residual heavy aromatic oil as the raw material.The results showed that the catalyst with the loadings of 2%Ni and 0.2%Pd on γ-Al2O3 and calcined at 700 ℃ exhibited ideal catalytic properties.The experimental results of the catalyst stability indicated that the product bromine index of less than 200 mg-Br·(100 g)-1 and the loss of naphthalene ring of less than 2% in the raw material were attained over the catalyst within 500 h.
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Study on catalytic cracking reaction of alkanes with different structures
LU Wenwen;CHENG Dangguo;CHEN Fengqiu;ZHAN Xiaoli
   DOI: 10.3969/j.issn.1008-1143.2012.01.009
Abstract1076)      PDF(pc) (350KB)(1222)       Save
Catalytic cracking of n-heptane,2-methylpentane and cyclohexane were studied on a fixed-bed reactor over catalysts 1# and 2#,which were supplied by Sinopec Shanghai Research Institute of Petrochemical Technology.The effects of different temperature on the catalytic cracking reaction and mechanisms were investigated.The results showed that the activity of the catalyst 2# was superior to that of catalyst 1#.And the structure of alkane influenced the products distribution obviously.The cracking mechanism ratio increased with the enhancement of reaction temperature.The cracking mechanism ratio of catalyst 1# was higher than that of catalyst 2#.Cyclohexane had the highest value of cracking mechanism ratio among the three raw materials,and the single-molecule cracking route for cyclohexane easily occurred;2-methylpentane had the lowest value of cracking mechanism ratio and the double-molecule cracking reaction for relatively more 2-methylpentane occured.
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Molecular simulation research on the catalytic mechanism of selective hydrogenation of acetylene
CHE Chunxia1;SHEN Lijun2;TAN Duping1;LIANG Yulong1;XUE Chunyu3;MI Jianguo3;LIANG Kun1;GAO Yuan1;HAN Wei1;LI He1;ZHANG Feng1;CHANG Xiaoxin1;XIE Wei1
   DOI: 10.3969/j.issn.1008-1143.2012.01.010
Abstract1168)      PDF(pc) (804KB)(1388)       Save

The catalytic mechanism of selective hydrogenation of acetylene was researched by quantum mechanics theory and Monte Carlo methods and using Pd-Ag alloy as the active component,Al2O3 as the carrier and the as-prepared catalyst as the study object.The relationship of catalyst activity and selectivity with dispersion of Pd-Ag catalyst was obtained.The results showed that the capacity of acetylene desorption from the surface of the catalyst was enhanced,and the formation possibility of ethane from ethylene was reduced with the increase of Ag loading,thereby the selectivity of acetylene hydrogenation was enhanced.The activation energy of H2 dissociation process on the catalyst surface and hydrogenation process of acetylene and ethylene was attained by calculation.The optimal condition of acetylene selective hydrogenation was as follows: temperature (70-80) ℃,and hydrogen partial pressure (0.03-0.04) MPa.

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Influence of acid/basic character of La2O3/γ-Al2O3 samples on MPV reaction of cinnamaldehyde
Lv Jia, CHEN Xihui
   DOI: 10.3969/j.issn.1008-1143.2012.01.011
Abstract983)      PDF(pc) (360KB)(1216)       Save
The effects of acid/base sites character of La2O3/γ-Al2O3 catalysts on Meerwein-Ponndorf-Verley(MPV) reduction of cinnamaldehyde to cinnamyl acohol were investigated by blockading the acid/base sites on the catalysts. The experimental results showed that the acid and base sites of the catalysts had influence on the reaction and the influence of acid sites on the reaction was larger than that of base sites.
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Synthesis of acetophenone cyclic ethylic ketal catalyzed by nanosolid superacid SO2-4/Fe2O3
LI Jiagui;ZHU Wanren;WEI Qingmin
   DOI: 10.3969/j.issn.1008-1143.2012.01.012
Abstract951)      PDF(pc) (366KB)(1104)       Save
Acetophenone cyclic ethylic ketal was synthesized by using acetophenone and ethylene glycol as the raw materials and nanosolid superacid SO2-4/Fe2O3 as the catalyst.The conditions of the catalyst preparation and condensation reaction were optimized.The results showed that the yield of acetophenone cylic ethylic ketal of 94.2% was attaind under the optimum reaction condition as follows:acetophenone amount 170 mmol,acetophenone/ethylene glycol molar ratio 1∶1.7,catalyst dosage 100 mg(4.4% of the total mass of the reactants),reaction temperature (98-112) ℃,and reaction time 1.5 h.
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Synthesis of methyl oleate catalyzed by ionic liquid [Hnhm]H2PO4
WANG Jilin1;WANG Lulu1;LI Mingxin1;YANG Xiao2
   DOI: 10.3969/j.issn.1008-1143.2012.01.013
Abstract884)      PDF(pc) (348KB)(1255)       Save
Ionic liquid [Hnhm]H2PO4 was synthesized and characterized by IR.The solubility and water absorption of the ionic liquid were studied.The catalytic activity of as-synthesized ionic liquid [Hnhm]H2PO4 was investigated by using esterification of oleic acid with methanol to methyl oleate as the probe reaction.The results showed that the esterification rate of oleic acid of over 63% was attained under the condition as follows: ionic liquid [Hnhm]H2PO4 dosage 8% of oleic acid mass,n(methanol)∶n(oleic acid)=3.5∶1,reaction temperature 90 ℃,and reaction time 9 h.The ionic liquid could be easily separated from raw materials and esterification products.
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Study on the copolymerization of carbon dioxide and propylene oxide over composite catalysts
YANG Hui;LI Yanming;HUANG Kai;HUANG Ribo
   DOI: 10.3969/j.issn.1008-1143.2012.01.0014
Abstract916)      PDF(pc) (392KB)(1166)       Save
The double metal cyanide/zinc glutarate(DMC/ZnGA) composite catalyst was prepared.The influence of catalyst component on the copolymerization of carbon dioxide(CO2) with propylene oxide(PO) was investigated.The copolymerization products were characterized by gel permeation chromatography(GPC),1H nuclear magnetic resonance(1H NMR),Fourier-transform infrared spectroscopy(FI-RT) and thermogravimetric analysis(TGA).The results indicated that DMC/ZnGA composite catalyst exhibited obviously synergetic effect and high catalytic efficiency for copolymerization of CO2 and propylene.The number average molecular weight of the copolymer was 18 000-31 000.The highest catalytic efficiency of 168 g-polymer·(g-catalyst)-1 was attained by optimizing the mass ratio of DMC and ZnGA in the catalyst.The selectivity to the copolymer was more than 97%.
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Photocatalytic degradation of alizarin red on Ag/TiO2 catalyst
FU Wen1,2;WANG Li1;HUANG Junzuo1
   DOI: 10.3969/j.issn.1008-1143.2012.01.015
Abstract881)      PDF(pc) (363KB)(1089)       Save
Using tetrabutyl titanate as the precursor and glacial acetic acid as the hydrolysis inhibitor,Ag/TiO2 catalyst was prepared by means of sol-gel method.The photo-degradation activity of the as-prepared catalyst for alizarin red was investigated.The results showed that Ag/TiO2 catalyst exhibited better catalytic properties.
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Development in pollution control technology of indoor formaldehyde
SUN Quan;LI Fei;ZHANG Yong;HOU Xin;LAN Liqiang;LU Dan
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.001
Progress in preparation of aluminum fluoride materials with high surface area
YU Hongbo; LIN Jianjun;XIE Guanqun;WANG Yuejuan;LUO Mengfei
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.003
Rare earth doped TiO2 catalysts for CO2 photocatalytic reduction
XU Yanfeng;WANG Jianbo;ZHANG Xiaolong; SUN Yuan
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.007
Preparation of TS-1 zeolites with inorganic materials and their catalytic properties for ammoxidation of cyclohexanone
WU Ting;ZHANG Ning;HUA Jianli;WEN Yiqiang;LI Baojun;WANG Xiangyu
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.008
Researches on hydrodesulfurization process of catalytic cracking gasoline
YU Jiwei;WANG Tong;JIANG Haibo;ZHAO Yue;HE Xin
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.009
Effect of phosphorus on properties of MoNi/γ-Al2O3 hydrotreating catalysts
PENG Weixing;WANG Jifeng;YANG Zhanlin;TANG Zhaoji;JIANG Hong
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.010
Study on LHQ-11 catalyst in a Unipol pilot plant
ZHANG Peng;WEI Shaoyi;GAO Yuxin;QIAO Tongsen;WANG Hai;ZHANG Pingsheng;LI Pengpeng
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.012
Simultaneous catalytic reduction of NO and SO2 with CO over Fe/γ-Al2O3catalysts
WANG Xuehai;FANG Xiangchen;LIU Zhongsheng
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.10.014
Progress in modification research on kaolin used for catalytic cracking catalysts
ZHENG Yunfeng;LI Di;CHEN Shukun;SUN Shuhong;LIU Conghua;GAO Xionghou
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.11.001
Influence of reduction temperature on reactive performance of Co/ZnO catalyst for Fischer-Tropsch synthesis
CHEN Tao;YANG Shoubin;DI Wanming;WANG Xiaoqin;NING Wensheng
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.11.002
Effect of La2O3-modification methods on alumina thermostability
ZHOU Renmei;YU Qin;WANG Shuyuan;JIN Lingyun;HU Gengshen;LUO Mengfei
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.11.006
Influence of nitrogen doping on photocatalytic properties of SrTiO3
Lv Lu;WU Guangwen;WU Hao;ZHOU Yaohua;ZHAO Liang
Industrial Catalysis    DOI: 10.3969/j.issn.1008-1143.2012.11.007