Industrial Catalysis 2002 Vol.10

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Effects of sepiolite and samarium on properties of nickel catalyst
DENG Geng-feng;XU Zhi-feng; LUO Lia-tao;LI Feng-yi
  
Abstract831)      PDF(pc) (81KB)(1118)       Save
The effects of sepiolite and samarium on the activity of nick
el catalyst for hydrogenation of benzene and carbon dioxide were investigated.
The surface behavior of Ni/Sep and Ni-Sm/Sep were characterized by XPS, CO chemical adsorption and CS poisoning. The results showed that both sepiolite and samarium can increase catalytic activity, sulfure tolerance and active surface area of the catalyst and electronic cloud density of the nickel atoms, meanwhile decrease activation energy of CO methanation.
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Effect of pore structure of residue hydrodesulfurization\=catalyst on its activity
WANG Gang;WANG Yong-lin;SUN Su-hua
  
Abstract857)      PDF(pc) (241KB)(1370)       Save
The effect of pore structure of residue hydrodesulfurization
catalyst on its activity was studied on a 3L hydrotreating pilot plant. Result
s showed that hydrodesulfurization, hydrodenitrogenation, hydrodecarbon and hydrodemetalation activity of the catalyst varied with its pore structure in different ways.
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Development and industrial application of a hydrcracking catalystspreparation technology via co-gelling method
WAN Xue-bing;DING Lian-jie
  
Abstract835)      PDF(pc) (87KB)(1103)       Save
This paper reviewed the features of hydrocracking catalysts preparation technologies via co-gelling method, as well as industrial production
and application of the catalysts. It was shown that full-scale production of
the catalysts is readily feasible. The catalysts exhibit high tolerance to nitro
gen poisoning, higher selectivity to desirable products and good hydrocracking a
ctivity stability.
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Commercial application of NT-03 and NT-13 gaseous\=ammonia desulfurization agents
YUAN Ming;GAO Jun-wen;YANG Guo-qi;QIU Gui-lin;DU Cai-xia;ZHANG Yong;, WANG Ya-li
  
Abstract1155)      PDF(pc) (77KB)(1298)       Save
Experimental and side stream test showed that combined use of
NT-03 and NT-13 gaseous ammonia desulfurization agent can remove hydrogen sulfide in ammonia by-product from waste water stripping process to less than 1 ppm. The two desulfurization agents, developed by the Northwest Research Institute of Chemical Industry (NRICI, Lintong, Xi'an, China), have successfully used in refinery waste water stripping plants.
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Timely correction of the kinetics of gasoline hydrogenation reaction and simulation on the reactor
ZHANG Shou-chen; WANG Li-qiu;LIU Chang-hou; HAN Ying
  
Abstract827)      PDF(pc) (81KB)(1243)       Save
Main reactions of gasoline hydrogenation process were analyze
d. Mathematic model of he hydrogenation reactor was established upon basis of summarization and simplification made to reaction kinetics of the complicated syst
em. Operating parameters for the hydrogenation reactor were simulated and calculated using timely correction method. Influence of some operating parameters on hydrogenation efficiency and operation of the system were discussed.
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Influence of properties of support on sulfiding performance of sulfurtolerant shift catalyst
CHEN Yipin;LI Xin;ZHANG Xintang;ZONG Qiuyun
  
Abstract819)      PDF(pc) (81KB)(1351)       Save
Sulfiding performane of four sulfurtolerant shift catalysts with different supports were investigated using temperatureprogrammed sulfiding (TPS) technique. Results showed that the properties of supports is an important factor influencing on sulfiding performane of the catalyst. Incorporation of special promoter can considerably enhance sulfidability of the catalyst and lower its sulfiding temperature.
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A look into the causes for rapid deactivation of V2O5-K2SO4/SiO2 catalyst for SO2 oxidation
BI Hong;XU Bo-lian;LIU Yan-mei;ZHAO Zong-yan
  
Abstract889)      PDF(pc) (115KB)(1259)       Save
X-ray diffraction (XRD), temperature programmed reduction (TP
R), surface area measurement(BET)and scanning electron microscope (SEM ) were used to analyze the crystalline structure、catalytic activity and surface area of V2O5-K2SO4/SiO2 catalyst A and B for SO2 oxidation. Main causes f
or deactivation of catalyst B in industrial use were discussed, too.
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An investigation on mechanism for aromatization of n-hexane on Zn/HZSM-5 catalyst
YIN Shuang-feng;ChEN Yi;LIN Jie;YU-Zhong-wei
  
Abstract925)      PDF(pc) (91KB)(1616)       Save
The aromatization of n-hexane over Al2O3, Zn/Al2O3 an
d HZSM-5 was compared. Influence of zinc content and hydrothermal treatment on aromatization properties of Zn/HZSM-5 was investigated. It was found that B acid is indispensable active centre for n-hexane aromatization while Al-L acid
shows very weak activation to n-hexane. Incorporation of zinc onto surface of H
ZSM-5 greatly enhances the its aromatization activity. When zinc content excee
ds 1.8%, it has little effect on aromatization properties of Zn/HZSM-5. There
exists synergistic interaction between B acid sites and Zn-L acid sites on Zn/H
ZSM-5 catalyst, which is necessary to enhancement of aromatization performance of HZSM-5. Mechanism for n-hexane aromatization on Zn/HZSM-5 catalyst is prop
osed on the basis of the experimental results.
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Research on a new ethylene oxychlorination catalyst
WANG Hong-xia;HUANG Feng-xing;ZHU Hong-fa QI Lan-zhi; LIU Xiao-hong; WEI Yu-ying
  
Abstract871)      PDF(pc) (84KB)(1745)       Save
A new CuCl3-based ethylene oxychlorination catalyst contai
ning appropriate amounts of as promoter was prepared by co-precipitation. Incor
poration of KCl significantly improved property of the catalyst, which exhibite
d superior performance than currently used imported catalysts, with better activ
ity , higher selectivity to 1,2-dichloroethane and inhibition of side reactions.
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Advances in researches in the catalysts for aniline hydrogenation to cyclohexylamine
YAN Jing;WANG Ri-jie
  
Abstract897)      PDF(pc) (83KB)(1764)       Save
The mechanism of hydrogenation of aniline to cyclohexylamine
is introduced. Emphasis is put on the catalysts for liquid phase and gas phase h
ydrogenation. The research of non-noble catalyst for gas phase hydrogenation is
recommended.
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Influence of pore-expanding agents on properties of carriers forautomotive catalysts
ZHANG Xing-yan;WANG Li-qiong;ZENG Qing-xuan;AN Qin;WANG Da-xiang;HU Yu-cai
  
Abstract955)      PDF(pc) (202KB)(1679)       Save
BET and SEM techniques were used to study the influence of pore-expan
ding agents(urotropine and urea) on properties of the carriers for automotive ca
talysts. It was shown that addition of an appropriate amount of pore-expanding
agents (about 30%) can effectively increase surface area of the carriers and imp
rove its properties.
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The effect of preparation temperature on surface area of VPO catalyst
LAO Li-hua;CHEN Shen-li
  
Abstract810)      PDF(pc) (100KB)(1222)       Save
VPO catalysts were prepared at different temperature. BET, XRD and SEM techniques were used to investigate the effect of preparation tempera
ture on surface area and phase composition of the catalysts. The results showed
that there is an optimum temperature for surface area and phase composition. Surface area and amount of active phase can be ienhanced at the optimum preparation temperature.
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Pore structure of modified alumina and its pseudoboehmite precursor
ZHAO Yan
  
Abstract908)      PDF(pc) (115KB)(2240)       Save
The structural characteristics of γ-Al2O3 and its pseudo
boehmite precursor were discussed. These original particles retained their respe
ctive structures and had profound effect on pore size distribution of γAl2O3converted from pseudoboehmites upon calcination at above 300℃, Method for distinguishing among amorphous pseudoboehmite and boehmite were discussed. Factors affecting pore structure of resultant γ-and θ-Al2O3 were invesigated, such as preparation method, calcination and hydrothermal treatment condition, pore enlarger and improvement on extruding or forming process.
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Designing concept for the FCC catalyst series for increasing diesel
Production and application of the catalysts
YU Sheng-yang;DENG Yang;ZHONG Xiang-sheng;TAO Xiang-meng;ZHANG Zheng-yi
  
Abstract840)      PDF(pc) (81KB)(1324)       Save
Basic designing concept for a series for FCC catalysts for increasing diesel production and application of the catalysts were described. Commercial application showed that the catalyst series brought about considerable increase in diesel production with excellent performance.
Key words:fluid catalytic cracking CFCC7; catalyst; diesel oil; overall liquid yield
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Commercial application of LV-23 FCC catalyst in RFCC units
LIU Dong-hui
  
Abstract873)      PDF(pc) (280KB)(1084)       Save
Commercial application of LV-23 FCC catalyst in residue fluid catalytic cracking units (RFCCU) were described. The results from commercial operation showed that LV-23 catalyst exhibited strong heavy-metal-tolerant performance, high selectivity to gasoline and coke, enhanced light oil yield and good adaptability to different production schemes.
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The Commercial Application of FH-98 Hydrotreating Catalyst
CHU Xing-bang; LI Xi-jun;HAO He-chao;MENG Fan
  
Abstract859)      PDF(pc) (84KB)(1219)       Save
This article described the loading, drying, sulfiding, activity stabilizing and trial running of FH-98 catalyst in the hydrotreating unit of the Refinery of Daqing Petrochemical Company. Results from commercial application showed that FH-98 catalyst , with satisfactory activity and stability, was an excellent hydrotreating catalyst.
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Application of B119 HTS catalyst in methanol plant
SUN Chuan-bao
  
Abstract924)      PDF(pc) (74KB)(1205)       Save
Application results of B119 high-temperature shift (HTS) catalyst in The Second Chemical Fertilizer Plant of Qilu Petrochemical Corp. were described. It was shown that crush strength and activity of the catalyst  meet the requirements of industrial use.
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B119 HTS catalyst-properties and its application
XIE Su-nian;WEI Shi-xin;GAO Feng;ZHANG Tian-sheng;LIU Lian-you
  
Abstract988)      PDF(pc) (266KB)(1092)       Save
Properties and application of B119 HTS catalyst were reviewed. Commercial run results of the catalyst in a low-pressure methanol plant is comparable to that of imported reference catalyst.
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Commercial application of Z103PH pre-reforming catalyst
in large-scale ammonia plant
GAO Yu-xia; CAI Bin;LIU Yu
  
Abstract805)      PDF(pc) (131KB)(1140)       Save
The first commercial run of Z103PH pre-reforming catalyst on an ammonia plant of Jinxi Natural Gas Co., Ltd was described.
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The Causes for temperature jump during preheating of carbon monoxide HTS catalyst in air and countermeasures
WU Si-cao
  
Abstract875)      PDF(pc) (74KB)(1201)       Save
The causes for temperature jump during preheating of carbon monoxide HTS catalyst in air were discussed . Some suggestions were made from the point of catalyst manufacture and its industrial use to prevent this phenomenon.
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Process and catalysts for manufacture of benzyl alcohol
WU Xin-gan;Li Ling-lan
  
Abstract976)      PDF(pc) (149KB)(3462)       Save
This paper reviewed various technologies for manufacture of benzyl alcohol and trends of their developments. It was pointed out that, toluene oxidation, which produces 10%~15%(wt) benzyl alcohol as by-product while manufacturing benzoic acid, is a route of great commercial potential. Advantages and disadvantages of various routes were discussed from viewpoint of “green chemistry”.
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Researches in peroxidation of alkyl aromatics and the catalyst
WANG Ri-jie; XUE Chang-hai;ZHANG Ji-yan
  
Abstract917)      PDF(pc) (120KB)(1610)       Save
Peroxidation of alkyl aromatics is the key step to synthesis of phenols. Compared with traditional phenol synthesis routes, the reaction is featured by low pollution and 100% utilization of reactant atoms, which makes it an ideal green synthesis route. This article reviews researches in various catalysts for alkyl aromatics peroxidation.
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Advances in the researches in preparation of ethylene glycol via ethylene oxide catalytic hydration
LI Ying-cheng, HE Wen-jun,CHEN Yong-fu
  
Abstract950)      PDF(pc) (110KB)(3314)       Save
Latest advances in preparation of ethylene glycol via ethylene oxide catalytic hydration were reviewed, including reaction mechanism, catalysts system, problems with currently-used catalysts and trends in this field.
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Studies on CuO-ZnO-Al2O3/HZSM-5 catalyst
for dimethyl ether synthesis from CO2/H2
LIU Zhi-jian1;LIAO Jian-jun1;TAN Jing-pin1;LI Da-dong2
  
Abstract859)      PDF(pc) (81KB)(1462)       Save
A CuO-ZnO-Al2O3/HZSM-5 catalyst for synthesis of dimethyl ether from CO2/H2 was prepared using ethanol as solvent and oxalic acid as precipitator. At 245℃, 2.2MPa, 2400h-1 and H2/CO2 of 2.79, CO2 conversion of 22.61%, selectivity to dimethyl ether of 45.90%, selectivity to methanol of 14.81% and yield of oxo-compounds (CH3OH+CH3OCH3) of 13.73% were obtained. Preliminary investigation into reaction condition and activity stability of the catalyst were made.
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Study on nickel-tolerant matrix for FCC catalysts
PANG Xin-mei;SUN Shu-hong;Ding Wei
  
Abstract827)      PDF(pc) (139KB)(1301)       Save
The effects of two kinds of alumina with different surface area and pore size distribution on performances of FCC catalysts were studied. The results showed that alumina with low surface area and large pore size can enhance conversion for cracking of heavy oil, coke selectivity and nickel tolerance of FCC catalysts.
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Acidity of alumina, modified alumina and aluminum silicate
ZHAO Yan
  
Abstract864)      PDF(pc) (89KB)(2855)       Save
Acidic characteristics of alumina, modified alumina and aluminum silicate, including acidity, acid strength, acid type and microscopic structure of acidic site were reviewed in this paper. Effects of incorporation of P, B, F, Ti, Zr and Si into alumina on its properties and acidity of modified Y zeolite were discussed, too.
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Influence of acidic additives on cracking performance of RFCC catalyst and feed oil
SUN Xue-wen1;LIU Yan-hui2; FAN Gui-chen2;GAO Yu-qing3
  
Abstract892)      PDF(pc) (99KB)(1337)       Save
In order to counteract against the decline in activity, selectivity of RFCC catalyst and yield of light oil caused by existence of basic nitrogen compounds, Acidic additive is added to residue feedstock. simulating the condition of commercial,Comparison tests were made on a small catalytic cracking unit to investigate the effects of acidic additives on cracking performance of RFCC catalyst and residue feedstock as well as properties of the gasoline and diesel products. Results from the tests showed that incorporation of appropriate amount of the acidic additive into residue feedstock can enhance micro-reactor activity of the catalysts by 3~4 units,the yield of light oil by 3%~4%(wt),and improve product distribution. The acidic additive will not come into final products. The optimum amount of the acid additive was 0.25%~0.35%(wt),depending on feedstock and catalyst.
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Advances in hydrocarbon steam reforming catalysts and tec
hniques for hydrogen production
WANG Wei,CHENG Yuchun, DAI Jianbo, HAO Shuren
  
Abstract911)      PDF(pc) (356KB)(1988)       Save
Advances in material, processes, equipment and catalysts invol
ved in hydrocarbon steam reforming for hydrogen production were discussed in the article. The development trends were outlined and some suggestions made.
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Studies on lube oil isodewaxing catalyst
YANG Jun1,2;LU Guan-zhong1
  
Abstract929)      PDF(pc) (339KB)(1219)       Save
The application of Pd/SAPO-11 catalyst in isodewaxing of lube oil distillate and isomerization of n-dodecane was studied. The effects of Si content in SAPO-11 molecular sieve and preparation method on properties and hydroisomerization activity and selectivity were studied, too. It was shown that isodewaxing reaction of lube oil distillate and hydroisomerization reaction of n-dodecane were controlled by diffusion, so both Pd/SAPO-11 catalysts prepared by SAPO-11 with abundant secondary pores and those prepared by SAPO-11 with clean surface exhibited high isomerization activity and selectivity.
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Development of S-RHT guard catalyst and demetalation catalyst for residue hydrogenation
ZHAO Yusheng;WANG Zhiwu;LIU Xilai
  
Abstract961)      PDF(pc) (162KB)(1135)       Save
In response to the requirement arising from processing imported Middle East crude oil, SINOPEC Fushun Research Institute of Petroleum & Petrochemicals(FRIPP, Fushun, Liaoning 113003, China ) developed new S-RHT guard catalyst and demetalation catalyst with better performance than her first generation guard catalyst and demetalation catalyst as well as the imported catalysts. Physicochemical properties of the new catalysts were greatly improved, and the impurity removal activity and the stability enhanced.
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On-situ regeneration of hydrogenation catalysts
LI Yang,SHAN Jiangfeng,HUAN Weifang
  
Abstract862)      PDF(pc) (229KB)(1560)       Save
SINOPEC Fushun Research Institute of Petroleum & Petrochemicals,Liaoning Fushun 113001, China
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Commercial Application of LV-23BC residue cracking catalyst in a FCC unit
FAN Weilin
  
Abstract776)      PDF(pc) (170KB)(1156)       Save
Operation, process condition and run results of LV-23BC catalyst in a
FCC unit at Qingyang Chemical Co., Ltd. were described. The application results
showed that LV-23BC catalyst exhibited high tolerance to metal contamination, re
sidue cracking activity, selectivity to coke and LPG, low specific consumption a
nd good stability.
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Advances in oxidative cross-coupling oftoluene and methane to styrene
ZHANG Quanxin;LIU Xiyao
  
Abstract811)      PDF(pc) (194KB)(1276)       Save
Research Institute of Yanshan Petrochemical Corporation, Beijing 102550, China
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TPR study on copper-based methanol synthesis catalysts

GUO Xianji;YE Changming;ZHAO Lei;WANG Xiangyu;LI Limin

  
Abstract1020)      PDF(pc) (317KB)(1189)       Save
A series of copper-based catalysts with different Cu/Zn ratio(mole) were prepared by one-step parallel flow co-precipitation. The activity test showed that the optimum Cu/Zn ratio was around 1.25. TPR results of the catalysts showed that when aluminum content is fixed, the catalyst sample with the optimum Cu/Zn ratio has the lowest reduction temperature. The TPR results of the catalyst samples prepared at different pH values showed that the structure of copper-based catalyst is greatly affected by pH values in the precipitation process. The causes behind this were discussed in detail. Effect of aluminum content on reduction behaviour of copper-based catalyst was also investigated. TPR results at different rate of heating were compared.
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Effect of calcination condition on the water-tolerant stability of ethylbenzene dehydrogenation catalyst
MIAO Changxi
  
Abstract843)      PDF(pc) (317KB)(1045)       Save

Effect of calcination condition on the water-tolerant stability of ethylbenzene dehydrogenation catalyst was studied. It was found that increase in calcination temperature and calcination time is favorable to enhancement of the water-tolerant stability of the catalyst, inhibiting the decline in mechanical strength and increase in attrition when the catalyst is subjected to water atmosphere. Possible cause for this is that variation in calcination condition promotes formation of KFe11O17, which is stable to water owing to its structure. The experimental results were well explained by BET, pore structure, XRD and Mōssbauer measurement.

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Application of domestic triethylaluminum in batch production of polypropylene
WANG Yuzhang, SU Xia
  
Abstract901)      PDF(pc) (232KB)(1647)       Save

This paper described the application of domestic triethylalumi
num in a 100kt/a batch polypropylene (PP) plant of the Plastic Factory of Jin
ling Petrochemical Co., Ltd.

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Study on Catalyst for the Synthesis of 2,6-Dimethylaniline by Gas Phase Amination
SUN Ronghua1;ZHANG Xiucheng1;CHEN Liyu1;WANG Wanqin2
  
Abstract919)      PDF(pc) (127KB)(1243)       Save
The spinel-supported catalyst was studied for the amination of 2,6-Dimethylphenol.The effects of different carriers and the composition of spinel on the catalytic activity were experimentally investigated.The effect of reaction temperature on the amination reaction was investigated too.
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Rational operation of palladium catalyst inhydrogen peroxide manufacture
FU Qi
  
Abstract903)      PDF(pc) (233KB)(2289)       Save
Status of hydrogen peroxide manufacture over palladium cataly
st via anthraquinone process is reviewed in this paper.
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Study on catalytic hydrogenation of carbon dioxide to dimethyl ether
YANG Yan, XIA Daikuan, TANG Wenlong
  
Abstract945)      PDF(pc) (355KB)(1399)       Save
A bifunctional catalyst for one-step synthesis of methanol and dimethyl ether via carbon dioxide hydrogenation was prepared from CNJ202 methanol synthesis catalyst and HZSM-5. Experimental results showed that the appropriate HZSM-5/CNJ202 ratio is 0.5(wt/wt); optimum calcination temperatureis 550℃; recommended reduction condition for the catalyst is at atmospheric pressure, 250℃, in N2 stream containing 2%H2 for 6h. Particle size of the bifunctional catalyst and GHSV has no evident effect on its selectivity to dimethyl ether ,but higher temperature favours selectivity to dimethyl ether. It was shown that further improvement on the bifunctional catalyst may greatly enhance CO2 conversion to meet the requirement of commercial production.
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Effect of transition metal on the hydrogenation performance and surface property of Ru/sepiolite catalyst
LI Songjun, LUO Laitao
  
Abstract864)      PDF(pc) (294KB)(1176)       Save
A series of Ru/sepiolite catalysts containing promoters such as Mo, Co, Mn, Cu, Zr were prepared by impregnation. The influence of promoter on the hydrogenation activity, surface properties of Ru/sepiolite catalyst and adsorption-activation properties of reactant molecules were investigated using TPD, CS2 poisoning and the probe reaction(CO2 and benzene hydrogenation). The results showed that addition of promoter remarkably affects the catalytic activity of Ru/sepiolite catalyst, and the degree of the effect increases with the size of reactant molecule. Effect of promoter on the adsorption-activation properties of reactants is an important factor for its effect on catalytic activity of Ru/sepiolite catalyst. Promoter also adjusts the surface properties of Ru/sepiolite without changing category of the active centers.
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