Industrial Catalysis 2005 Vol.13

Please wait a minute...
For Selected: Toggle Thumbnails
Activated carbon fiber and its application in catalysis
HU Xiao-min;LIU Hua-zhang
  
Abstract911)      PDF(pc) (367KB)(1784)       Save
A new catalytic material-activated carbon fiber(ACF) and its application in catalysis were reviewed. Comparison was made between ACF and granule activated carbon(GAC) with respect to surface structure and properties. Application of ACF in removal of SO2, HCl and NOx as well as catalyst supports.
Related Articles | Metrics | Comments0
Latest researches in co-immobilization technology for enzyme catalysts
ZHANG Zhi-hua;JIANG Chang-ming
  
Abstract929)      PDF(pc) (328KB)(1725)       Save
Several co-immobilization methods for enzyme catalysts were reviewed and compared. Co-immobilization overcome the limitations on traditional immobili
zation methods and has good prospects of application.
Related Articles | Metrics | Comments0
Influence of reaction condition on thiophene hydrodesulfurization over Ni-Mo/TiO2-Al2O3 catalyst
LIU Bai-jun1;ZHENG Yu-yin1;MENG Qing-min1;JIANG Ying-tian2;SHENG Shi-shan3;YANG Wei-shen3
  
Abstract955)      PDF(pc) (99KB)(1308)       Save
TiO2-Al2O3 composite support was prepared by sol-gel technique and Ni-Mo/TiO2-Al2O3 catalysts were prepared by impregnation on the modified supports. The influences of reaction condition on hydrodesulfurization (HDS) activity of the catalysts were tested in a fixed-bed microreactor. The results showed that thiophene conversion of 100% was attained under reaction temperature 260-270 ℃, hydrogen pressure 3.0 MPa, LHSV 3.0-5.0 h-1 and hydrogen/oil ratio 480-500.
Related Articles | Metrics | Comments0
Effect of nickel content on sulfur tolerance of nickel-based catalysts for aromatic hydrogenation
HUANG Hua1;YIN Du-lin2;WEN Jian-jun3;ZHANG Mao-kun1;XU Bin1
  
Abstract1059)      PDF(pc) (340KB)(1199)       Save
Ni/Al2O3 catalysts with different nickel content were prepared by impregnation method. Tolerance of the nickel-based catalysts to sulfur poisoning was investigated via hydrogenation of toluene containing thiophene in a fixed-bed continuous-flow microreactor at 1.0 MPa, 200 ℃ and LHSV 2.0 h-1. Physicochemical properties and structure of the catalysts were examined by XRD, TPR,DSC and BET. The results showed that the catalysts with high nickel content exhibited very high aromatic hydrogenation activity and tolerance to sulfur, while catalysts with low nickel content (less than 60%) was likely to form NiAl2O4 of no aromatic hydrogenation activity.
Related Articles | Metrics | Comments0
Development and application of TH-1 dehydrogenation catalyst
LI Su-yan;XUE Yun-na;WANG Zhi;ZUO Man-hong;LIU En-li;WANG Xiao-dong
  
Abstract937)      PDF(pc) (241KB)(1256)       Save
The development and commercial application of TH-1 dehydrogenation catalyst are described. Commercial application results showed that the catalyst can effectively remove hydrogen in carbon dioxide for urea synthesis and eliminate potential explosion risk of the tail gas from urea synthesis reactor. The catalyst has been in operation for 14 months at 120 ℃,with hydrogen content in treated gas below 10×10-6. The catalyst features high activity, low operation cost and long service life.
Related Articles | Metrics | Comments0
Application of photocatalysis in organic synthesis
TANG Sheng-shan;ZHANG Ning;ZHU Jing
  
Abstract978)      PDF(pc) (347KB)(3114)       Save
Application of photocatalysis in organic synthesis, mainly polymerization, olefins oxidation and carbonylation was reviewed, and trends in the field outlined.
Related Articles | Metrics | Comments0
Study on different feeding methods for C4 catalytic cracking kinetic experimental apparatus
LIU Jun-tao1,2;XU Chun-ming2;Xie Zai-ku1;Zhong Si-qing1
  
Abstract933)      PDF(pc) (291KB)(1201)       Save
Influence of different feeding method, such as liquid feeding and indirect gas-phase feeding, on mass balance of the kinetic experimental apparatus for C4 hydrocarbon catalytic cracking were discussed. The results showed that indirect gas-phase feeding can meet the requirement of kinetic study, which established stable and reliable kinetic experimental apparatus.
Related Articles | Metrics | Comments0
Isomerization of diisopropylbenzene over zeolite catalysts
ZHAO Pei-xia;ZHANG Chun-yong;LIU Jing
  
Abstract949)      PDF(pc) (314KB)(1311)       Save
Isomerization of diisopropylbenzene was investigated over zeolite catalysts,i.e.HY,MCM-22,HZSM-5,MCM-41 and Hβ.The results showed that Hβ zeolite is a high-active catalyst for the reaction. The reaction conditions over Hβ were investigated. 1,4-DIPB conversion increased but the selectivity to 1,3-DIPB decreased with reaction temperature. 1,4-DIPB conversion of 45% and selectivity to 1,3-DIPB were attained at optimum condition of 170 ℃, 3.5 MPa, and 2 h-1. The catalyst also showed good stability.
Related Articles | Metrics | Comments0
Catalytic synthesis of tert-butylamine and its application in fine chemicals
HUANG Zhao-hui1,2;YIN Du-lin1
  
Abstract979)      PDF(pc) (262KB)(1990)       Save
The advances in the technologies and catalytic synthesis methods for tert-butylamine were reviewed. It was proposed that the catalytic amination of metyl t-butyl ether by solid acid was a promising "green" process. The application of tert-butylamine in fine chemicals,such as medicine, pesticide and rubber additives, were reviewed, too.
Related Articles | Metrics | Comments0
Preparation and photocatalytic properties of zinc oxide thin film
WANG Ying-lian1;SUN Wang-dian1;REN Si-yu1;LU Xi-long2
  
Abstract977)      PDF(pc) (407KB)(1041)       Save
Highly photoactive ZnO thin films on glass substrates and quartz substrates were prepared by sol-gel method. Structures, surface morphology were studied using XRD, AFM and UV-VIS absorption spectroscopy. The influences of temperature, initial concentration of phenol and air flux on phenol degradation rates were investigated. The optimum condition was as follows: degradation temperature 25-45 ℃, air flux 40 mL·min-1. The lower the initial concentration of phenol, the higher the degradation rate. Adhesion of the ZnO thin films was studied an
d the catalysts formed were recyclable with high phenol degradation rate.
Related Articles | Metrics | Comments0
Synthesis and characterization of mesoporous molecular sieve MCM-41 in organic weak base
TAI Xiu-mei;WANG Hong-xia;SHI Xiu-qi;WANG Ping
  
Abstract952)      PDF(pc) (267KB)(1226)       Save
Using tetraethyl orthosilicate (TEOS) as silica source and cetyltrimethyl ammonium bromide(CTAB) as templating agent,mesoporous molecular sieve MCM-41 was synthesized at room temperature in organic weak base system(pH≈10) The product has short-range order compared with that synthesized hydrothermally in strong base. Influence of reaction condition (crystallization time, surfactant mass fraction and crystallization temperature) on as-synthesized sample quality were investigated in detail. The synthesized products were characterized by XRD. The experimental results showed that the longer crystallization time,the better order of the samples; structural and crystalline integrity of the samples improved
with increasing surfactant mass fraction until 6%, after which the integrity declined; regularity of the samples declined with increasing crystallization temp
erature, while lattice constant a0 increased with temperature.
Related Articles | Metrics | Comments0
Improvement on Pd-Pb/CaCO3 catalyst for selective hydrogenation of acetylenic linkage in hydrocarbons
LI Chang-you;YANG Le-fu;HUANG Bo;HU Yu-xiang;CAI Jun-xiu
  
Abstract842)      PDF(pc) (366KB)(1168)       Save
Influences of additives (PVA, oxalic acid, EDTA, ZnCl2) on microstructure of precipitated calcium carbonate (CaCO3) were investigated using SEM and XRD. The results indicated that crystal form and shape of CaCO3 vary with both type and quantity of the additives. XRD results showed that the deposit crystallized in
calcite in the presence of oxalic acid,which exhibited distinct template effect in Pd-Pb/CaCO3 system. The test results of different reduction methods showed that hydrazine hydrate was a good reducing agent. TEM images showed that palladium particles on the catalyst surface agglomerated after appropriate aging treatment and thus improved partial hydrogenation selectivity of the catalyst.
Related Articles | Metrics | Comments0
Expansion bed process for ex-situ pre-sulfiding of a hydrotreating catalyst
DONG Qun1;QI Xing-guo1;WANG Jian1;YU Chun-mei2;MA Shou-bo3
  
Abstract931)      PDF(pc) (348KB)(1301)       Save

Ex-situ pre-sulfiding of a hydrotreating catalyst in expansion bed was studied. The influence of presulfiding conditions on sulfiding degree (α) was investigated. The results showed thatαincreased with sulfiding temperature till 370 ℃, where maximum hydrogenation activity was attained. Pyridine-TPD results indicated that acidity increased with sulfiding temperature, which then affected hydrogenation activity of the catalyst. Comparison was made between ex-situ expansion bed and in-situ fixed-bed method. The catalyst presulfided by ex-situ expansion bed exhibited higher α and hydrogenation activity. The suitable condition for ex-situ expansion bed pre-sulfiding was as follows: sulfiding time ≤ 10
t0; sulfiding temperature = 370 ℃; bed expansion rate = 12%. Better activity was attained when pre-sulfiding and reduction were carried out simultaneously.

Related Articles | Metrics | Comments0
Latest researches in processes and catalysts for
conversion of heavy aromatics to light one
WANG Donghui;KONG Dejin;Guo Yanglong;Qi Xiaolan;Wang Junsong
  
Abstract941)      PDF(pc) (289KB)(1401)       Save
The catalysts and processes for conversion of heavy aromatics to light one were reviewed, especially those for catalytic hydrodealkylation and transalkylation. Most catalysts for the conversion to light aromatics were acidic. Development of solid acid catalysts with small particle size, larger pore diameters and good inhibition of coke formation, especially those for hydrodealkylation and transalkylation, is the trends in this field.
Related Articles | Metrics | Comments0
Advances in technologies for catalytic cracking of olefins to propylene
LIU Dongmei;LIU Bo;WANG Haiyan;MA Jun;WEI Min
  
Abstract828)      PDF(pc) (296KB)(1238)       Save
Technologies and catalysts for catalytic cracking of olefins to propylene were reviewed. It is pointed out that the trends in feedstock and processes for propylene are manifold feeds and renovation in the techniques. Catalytic cracking of olefins features simplicity in operation and low cost, and should be developed in preference.
Related Articles | Metrics | Comments0
Influence of methanol on conversion of thiophene over HZSM-5 zeolites
LUO Liwen, LI Hu, YU Huizheng, XIA Daohong
  
Abstract877)      PDF(pc) (286KB)(1179)       Save
Influence of methanol on catalytic desulfurization of thiophene over HZSM-5 (silica-to-alumina molar ratio = 25) was studied in fixed bed micro-reactor. The experimental results showed that thiophene conversion of over 51% was obtained at the temperature of over 350 ℃. The appropriate volumetric ratio between methanol and benzene was 1∶2. Satisfactory results (thiophene conversion of 51.3% and hydrogen sulfide yield of 18.1%) were attained over HZSM-5 zeolite modified by 1.0% La (mass fraction), with enhancement in thiophene conversion and hydrogen sulfide yield by 36.0% and 11.9%, respectively, compared with purely HZSM-5 zeolite. Weight hourly space velocity(WHSV) of 14 h-1 was preferable.
Related Articles | Metrics | Comments0
Desulfurization of straight-run diesel oil by gas-liquid phase catalytic oxidation
CUI Yingxian;TANG Xiaodong;AN Rong;XIAO Huangfei
  
Abstract951)      PDF(pc) (288KB)(1238)       Save
Oxidative desulfurization of diesel oil has drawn much attention due to the shortcomings of hydrodesulfurization, i.e., high investment, severe operation condition and pollution to environment. Considering the problems with hydrogen peroxide oxidative desulfurization, such as high cost of the oxidant, low diesel yield and sulfur containing wastewater emission, A straight-run diesel oil desulfurization method using liquid-phase homogeneous oxidation catalyst TS-1 and oxidant O2 in high pressure reactor was developed, with high desulfurization efficiency and low oxygen consumption. The test results showed that total sulfur in diesel oil was cut down from 2 217.2 μg·g-1 to 265 μg·g-1 under optimal condition as follows: 150 ℃, 0.8 MPa, 60 min, m(catalyst)/m(diesel)=1 500 μg·g-1. Diesel oil treated is up to European Ⅱ diesel standard (≤ 300 μg·g-1), with diesel oil yield of 95.2%.
Related Articles | Metrics | Comments0
Production of bunker fuel oil by deep visbreaking of Tahe residue oil
LI Heming;YANG Tao;WANG Jun;JIA Yongzhong;JIA Li;YANG Guang
  
Abstract858)      PDF(pc) (231KB)(1215)       Save
A process for hydrogen visbreaking of Tahe residue oil in suspension bed was described. Favorable operation condition for the process was obtained upon basis of investigation on the influence of reaction temperature, reaction time and dosage of additives.
Related Articles | Metrics | Comments0
Application of JT-1G/JT-4 hydrogenation catalysts
in countercurrent isothermal-adiabatic hydrogenation process

LIU Jun, YANG Guodong, LIU Weigong, QI Guoliang, ZHANG Shijie, HUANG Zhi

  
Abstract893)      PDF(pc) (207KB)(1079)       Save
The commercial application of JT-1G/JT-4 hydrogenation, for the first time in countercurrent isothermal-adiabatic hydrogenation process for hydrogenation of CO-rich coking gas, was described. The catalysts exhibited high olefin-saturation(hydrogenation) and hydrodesulfurization(HDS) activity, with sulfur mass fraction in the outlet gas as low as 0.2×10-6 after hydrogenation of organic sulfur to inorganic sulfur followed by absorption by zinc oxide, which meets the requirement of hydrogen plant on olefin saturation.
Related Articles | Metrics | Comments0
Application of N-Ⅲ propylene polymerization catalyst
YU Haijiang, CHANG Bo
  
Abstract894)      PDF(pc) (206KB)(1211)       Save
The application of N-Ⅲ highefficiency propylene polymerization catalyst in a batchwise polypropylene plant was described. Compared with Cs-Ⅰ catalyst, the catalyst features higher activity, high tolerance to impurities, highly directional and less influence by hydrogen adjustment. A drawback with the catalyst is slightly overlarger particle size of the polypropylene product.
Related Articles | Metrics | Comments0
Advances in application of iron-based catalysts in direct coal liquefaction
LI Yuzhen; ZHANG Xuejun1;CAO Duanlin1;PANG Wenji
  
Abstract842)      PDF(pc) (246KB)(1358)       Save
The catalytic mechanisms of iron-based catalyst for direct coal liquefaction and the influential factors of the activity were reviewed. Drawbacks of current catalysts and trends in development of the catalysts were discussed, too.
Related Articles | Metrics | Comments0
Effects of surface modified activated carbon on
Ru/AC ammonia synthesis catalyst

ZHENG Chao;WANG Rong;RONG Cheng;WEI Kemei

  
Abstract921)      PDF(pc) (287KB)(1432)       Save
The effects of surface modification of activated carbon (AC) by washing with HNO3 on behaviors of Ru/AC ammonia synthesis catalysts were investigated. The activated carbon supports and the catalysts were characterized by chemical titration of surface groups, N2 physical adsorption and CO chemical adsorption. Activity of Ru/AC ammonia synthesis catalysts were tested. The results showed that treatment of activated carbon support by washing with appropriate quantity of HNO3 resulted in increase in the amount of mesopores and remarkable increase in the surface carboxyl with higher hydrophilic property. These led to higher dispersion of ruthenium and enhanced activity of the catalysts prepared by impregnation of RuCl3 aqueous solution. Treatment of activated carbon by excessive quantity of HNO3 led to increase in some unstable surface groups, which were unfavorable to the catalytic activity and dispersion of ruthenium. Optimum results were obtained by treatment with 5 mol·L-1 HNO3.
Related Articles | Metrics | Comments0
Coupling of formaldehyde and methyl formate catalyzed by aminosulfonic acid
WANG Kebing;YAO Jie;WANG Yue;WANG Gongying
  
Abstract987)      PDF(pc) (274KB)(1243)       Save
Coupling of formaldehyde and methyl formate using aminosulfonic acid as a catalyst was studied in an autoclave reactor, including influence of reaction temperature, reaction time, reactants ratio and catalyst dosage on the yield of methyl glycolate(MG) and methyl methoxy acetate(MMAc). The optimal reaction condition was obtained as follows: 150-160 ℃, reaction time 4 h, n(formaldehyde)∶n(methyl formate)=0.5, with overall yield of 21.34 mmol·(g-cat)-1.
Related Articles | Metrics | Comments0
Green sythesis of cyclohexanone ethylene ketal over LaSiW12O40 catalyst
XU Zhaohui;CHEN Dekai;HUANG Yixiang;LIU Deyong;WANG Sheng
  
Abstract930)      PDF(pc) (261KB)(1345)       Save

A new environmentally-benign Keggin catalyst, LaSiW12O40, was prepared and characterized by FTIR. Catalytic properties of the catalyst were investigated using synthesis of cyclohexanone ethylene ketal from cyclohexanone and ethylene as the probe reaction,including influence of cyclohexanone/ethylene molar ratio,catalyst dosage,reaction time and repeated use of the catalyst. The catalyst exhibited high activity for synthesis of cyclohexanone ethylene ketal,with cyclohexanone conversion of 99.0% under favorable condition. Meanwhile, it featured simplicity in preparation and good properties in repeated use .

Related Articles | Metrics | Comments0
Screening of the heteropoly acid catalysts for hydrolysis of methyl acetate
CHEN Haibo;WU Wei;YE Gang;YU Fang;YU Huili
  
Abstract941)      PDF(pc) (249KB)(1269)       Save
Salts of heteropoly acids were synthesized and their catalytic properties for hydrolysis of methyl acetate and structure investigated. The experimental results showed that activity of the salts of heteropoly acids is in association with their structure and composition. Ammonium salt of the heteropoly acid (NH4H2PW12O40), with the strongest acidity (pKa=-11.99, close to that ofH3PW12O40) and the highest total acidity, exhibited higher activity than other materials such as resin, heteropoly acids and other salts of heteropoly acids. It also showed good structural stability.
Related Articles | Metrics | Comments0
Development of a liquid-phase furfural hydrogenation catalyst
and its commercial application
Zhao Xiubo;Jiang Xin;Zhou Hongjun
  
Abstract907)      PDF(pc) (261KB)(1105)       Save
Influences of preparation condition on properties of QKJ-01 Cu-Cr liquid-phase furfural hydrogenation catalyst were investigated by SEM, BET and XRD. The appropriate preparation condition was obtained as follows: pH 4-6.7, precipitation temperature 30-40 ℃, calcined at 450 ℃ for 2 h. Commercial application showed that the catalyst features low catalyst loadings and excellent catalytic properties, with furfural conversion of over 99.96% and selectivity to furfuralcohol of over 98.4%.
Related Articles | Metrics | Comments0
Characterization of W-Mo-Ni-Cr/Al2O3 catalyst and
its hydrodenitrogenation(HDN) behaviors

LI Baoshan, WANG Zhaohong

  
Abstract882)      PDF(pc) (283KB)(1225)       Save
A W-Mo-Ni-Cr/Al2O3 catalyst was prepared by stepwise impregnation and characterized by XRD, TG/DTA, N2 adsorption (BET) , TPD, TPR and IR. hydrodenitrogenation(HDN) activity of the catalyst was investigated using pyridine as the model compound. Optimum behaviors were achieved under 180 ℃ and reaction time of 1 h, with one-step pyridine conversion of 88.5%.
Related Articles | Metrics | Comments0
Controlled synthesis of larger crystal ZSM-5 zeolites
using different templates
LIU Chunying;LIU Yunqi;ZHAO Huanyu;HU Chengjiang;LIU Ping;LIU Chenguang
  
Abstract850)      PDF(pc) (541KB)(1424)       Save
ZSM-5 zeolites with similar Si/Al ratio were synthesized using different templates (tetrapropylammonium bromide (TPABr),n-tetrabutylamine (TBA), ethyldiamine (EDA) )and no template (NT) under hydrothermal conditions. The samples were characterized by XRD and SEM to investigate effects of the templates and difference in crystal size of the ZSM-5 samples. A method for controlled synthesis of ZSM-5 with moderate crystal size was consequently proposed. ZSM-5 zeolites with evenly larger crystal size ( about 10 μm) were synthesized using composite templates.
Related Articles | Metrics | Comments0
Effects of successive washing on structure and
properties of pseudoboehmite in preparation of γ-Al2O3
YAN Yuefeng;ZHI Jianping;ZHANG Gaoyong
  
Abstract922)      PDF(pc) (344KB)(1300)       Save
Influences of successive washing instead of batch-wise washing on crystalline phase, particle size,crystallinity and pore structure in preparation of γ-Al2O3 were investigated using XRD, SEM,TEM and thermal analyzer(DTA). The results showed that neither the crystalline composition nor the shape and size of primary particles of pseudoboehmite were affected by successive washing. But much difference in size of the secondary particles and their aggregates was observed between successive washing and batch-wise washing. Differential thermal analysis(DTA) and calculation of n in Al2O3· nH2O were used to investigate the order of pseudoboehmite. It was found that successive washing favored transition of the crystal structure from disorder to order.
Related Articles | Metrics | Comments0
Application of spin flash drier in manufacture of alumina catalyst support
HUANG Kezhi
  
Abstract819)      PDF(pc) (196KB)(1295)       Save
Drying process, structure and application of spin flash drier in manufacture of alumina catalyst support were described. Compared with reinforced boiling drier, spin flash drier features higher output and lower energy consumption.
Related Articles | Metrics | Comments0
Catalysis-assisted non-thermal plasma technology for decomposition of volatile organic compounds (VOCs)
GUO Yu-fang, YE Dai-qi, CHEN Ke-fu
  
Abstract889)      PDF(pc) (301KB)(1460)       Save
Catalysis-assisted non-thermal plasma is an ideal technology for poll
ution control. Catalyst could enhance pollutants removal efficiency and selectivity to carbon d
ioxide in the plasma reaction, inhibit by-products formation and lower energy c
onsumption. In this paper the synergetic effects and (principle of catalysis-ass
isted non-thermal plasma technology in decomposition of volatile organic compoun
ds (VOCs) were discussed. Advances in decomposition of volatile organic compounds
(VOCs) using catalysis-assisted non-thermal plasma technology were reviewed,
including the factors influencing decomposition efficiency, products distribution
and reaction kinetics. The prospects for application of this technology in the f
ield of environmental protection and trends of development were discussed, too.
Related Articles | Metrics | Comments0
Latest researches in the sorbents for hot coal gas desulfurization
GE Xiao-hua, GUO Bo, CHANG Li-ping
  
Abstract864)      PDF(pc) (315KB)(1548)       Save
Hot coal gas desulfurization, which can enhance efficiency of IGCC ele
ctric generation, lower electricity cost and simplify the process, has been paid
much attention. The key to researches in this aspect are mechanism of the inter
action between regeneratible metal oxides and hydrogen sulfide and other sulfide
s, and behaviors of the oxides. Latest researches in the sorbents for high tempe
rature coal gas desulfurization were reviewed in this paper, especially calcium
-, zinc-, iron-, copper-and manganese-based sorbents. The trends in this fiel
d would be a transfer from single metal oxide to multifunctional mixed metal oxides
with high-temperature resistance and good regeneratibility.
Related Articles | Metrics | Comments0
Influence of organic nitrogen compounds on deep hydrodesulfurization(HDS)
ZHANG Sheng;LI Xiang;WANG An-jie
  
Abstract840)      PDF(pc) (307KB)(1258)       Save
The influence of nitrogen compounds on the activity, selectivity and deactivation of hydrodesulfurization(HDS) catalysts was investigated. The studiesshowed that nitrogen compounds strongly inhibited HDS activity via competitive adsorption with sulfur compounds on surface of the catalysts. Nitrogen compounds inhibited both the two parallel reactions for HDS process:hydrogenation (HYD) and hydrogenolysis (HYG), with inhibition on then former. Nitrogen compounds also impaired HDS activity and selectivity of the catalysts by poisoning the active
sites. Strong adsorption of nitrogen compounds was also a important factor causing coke formation and deactivation of the catalysts.
Related Articles | Metrics | Comments0
Behaviors and commercial application of DZCⅡ-1 second-stage pyrolysis gasoline hydrotreating catalyst
ZHAO Ye;WANG Gang
  
Abstract949)      PDF(pc) (244KB)(1222)       Save
A new DZCⅡ-1 catalyst was developed on the basis of DZ-1 catalyst for application in second-stage hydrotreating of pyrolysis gasoline. Overload test for 19 months proved that the catalyst has good adaptability to feedstock, with no change in bed pressure drop, inlet temperature and bed temperature rise.
Related Articles | Metrics | Comments0
Aromatization of FCC gasoline fraction over hydrothermally treated Zn/HZSM-5 catalyst
CUI Guo-jing;WEI Min;ZHAO Liang;BAI Ying-zhi;ZHU Jing;MIAO Xing-dong;WANG Hai-yan;MA Jun
  
Abstract925)      PDF(pc) (290KB)(1103)       Save
Zn/HZSM-5 catalysts for aromatization of FCC gasoline fraction were prepared by hydrothermal treatment at different temperature (from 300 ℃ to 500 ℃). Influence of hydrothermal treatment temperature on aromatization behavior of the catalyst was investigated. Influence of hydrothermal treatment temperature on surface acidity of the catalyst was studied using FT-IR. The results showed that stability of the aromatization activity was enhanced by hydrothermal treatment. For Zn (2%)/HZSM-5 catalyst treated at 400 ℃, aromatics mass fraction in the product of 74.25% was attainable after reacting for 36 h. The quantity of Brnsted acid sites changed little in 300~400 ℃, but decreased significantly at 500 ℃. The quantity of Lewis acid sites increased with treatment temperature, but declined after 400 ℃. Optimum amomatization results were attained over the catalyst treated at 400 ℃, with olefins conversion, alkenes conversion and mass fraction of aromatics in the product of 83.6%, 95.44% and 92.23%, respectively, which means that best coordination between of Brnsted and Lewis acid sites was attained at this treatment temperature.
Related Articles | Metrics | Comments0
Selection and application of dechlorination sorbent in treatment of catalyst regeneration stream from catalytic reforming unit
ZHAO Zhen-hui;YE Xiao-dong;FENG Jin-song
  
Abstract918)      PDF(pc) (279KB)(1265)       Save
Dechlorination sorbent was adopted instead of existing alkaline scrubbing unit in treatment of catalyst regeneration stream at Sinopec Luoyang Company during a retrofit to existing catalytic reforming unit. Stable and satisfactory operation of the catalyst regeneration system were attained after the retrofit. The key to the successful retrofit was adoption of a high-performance high temperature dechlorination sorbent.
Related Articles | Metrics | Comments0
Latest researches in the catalysts for synthesis of carbamate by ammonolysis of dimethyl carbonate
KANG Wukui;WANG Gongying;LI Shixin;XUE Yuan
  
Abstract927)      PDF(pc) (320KB)(1554)       Save
Different routes for synthesis of carbamate were reviewed, including oxidative carbonylation of amino, reductive carbonylation of nitryl, anilinenitrobenzene method and ammonolysis of dimethyl carbonate. Ammonolysis of dimethyl carbonate (DMC) to carbamate, a more promisin route for synthesis of carbamate, was reviewed in detail, especially the catalysts.
Related Articles | Metrics | Comments0
Advances in the technologies for catalytic partial oxidation of methane
WANG Wei;SHEN Xin;SUN Dao-xing;CHENG Yu-chun
  
Abstract826)      PDF(pc) (314KB)(1497)       Save
Advances in the technologies for catalytic partial oxidation of methane to make synthesis gas were reviewed, including fixed-bed process, fluidized-bed process and ceramic membrane process. Two latest patents on reactors were discussed in detail. The trends in the technologies for catalytic partial oxidation of methane were outlined.
Related Articles | Metrics | Comments0
Advances in the technologies for synthesis of cyclohexanone by oxidation
JIANG Xue-yuan;SONG Hua
  
Abstract974)      PDF(pc) (325KB)(2527)       Save
Latest researches in synthesis of cyclohexanone from different feedstock by oxidation were reviewed. Cyclohexane catalytic oxidation, a predominant cyclohexanone production route, was described in detail. It was pointed out that development of green route for cyclohexane oxidation with high efficiency and hi
gh selectivity is the tendency in this aspect.
Related Articles | Metrics | Comments0
Synthesis of exo-tetrahydrodicyclopentadiene by catalytic isomerization
DU Yong-mei;LI Chun-ying;SHI Qiang;LUJian
  
Abstract969)      PDF(pc) (236KB)(1166)       Save
Preparation of exo-tetrahydrodicyclopentadiene by isomerization of endo-tetrahydrodicyclopentadiene over AlCl3 catalyst was studied. The effects of solvents, catalyst loadings, solvent amount and reaction time were investigated. The optimum operation conditions were obtained as follows:n(CH2Cl2)∶n(endo-tetrahydrodicyclopentadiene)=0.8; catalyst loading=20%; reaction time=3 h. Conversion of 9712% and selectivity of 9928% were attained under the optimum conditions.
Related Articles | Metrics | Comments0