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Katalizatory niklowe i rutenowo-niklowe na nośnikach zawierających zeolit ZSM-5 i tlenek glinu. Wybrane właściwości fizykochemiczne i katalityczne

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EN
Nickel catalysts and ruthenium-nickel catalysts supported on AI2O3+ZSM-5: Physicochemical and catalytic properties
Języki publikacji
PL
Abstrakty
PL
Przedstawiono wyniki prac dotyczących charakterystyki właściwości fizykochemicznych zeoli-tów, układów dwuskładnikowych ZSM-5+Al203 oraz katalizatorów niklowych i rutenowo-niklo-wych zawierających jako nośnik układ dwuskładnikowy w powiązaniu ze składem chemicznym, sposobem otrzymywania i ich właściwościami katalitycznymi. Określono wpływ sposobu łączenia zeolitu z wodorotlenkiem glinu na teksturę i właściwości kwasowe układów ZSM-5+Al203 oraz wpływ metody preparatyki katalizatorów niklowych na oddziaływania metal-nośnik i ich aktywność w krakingu oraz selektywnym krakingu węglowodorów parafinowych o łańcuchu normalnym (oraz ich monometylowych izomerów). Ustalono zależność między składem chemicznym, sposobem otrzymywania katalizatorów niklowych i rutenowo-niklowych a ich aktywnością uwodorniającą w konwersji węglowodorów aromatycznych. Określono korelację pomiędzy stosunkiem liczby centrów metalicznych do liczby centrów kwasowych w katalizatorach niklowych a ich selektywnością w reakcji uwodornienia toluenu. Udokumentowano wpływ warunków obróbki termicznej i sposobu wprowadzania niklu na oddziaływania metal-nośnik oraz wpływ ilości rutenu, rodzaju prekursora rutenu i sposobu preparatyki katalizatorów niklowych na oddziaływania metal-metal (Ru-Ni) i metal-nośnik oraz właściwości uwodorniające katalizatorów w konwersji 1 -metylonaftalenu. Opracowano formułę katalizatora umożliwiającego otrzymanie zadowalających ilości produktów w dwóch przeciwstawnych reakcjach (uwodornienie-reakcja egzotermiczna, kraking-reakcja endo-termiczna); w optymalnej temperaturze reakcji podczas przemiany frakcji oleju napędowego otrzymano produkty o korzystnych właściwościach niskotemperaturowych przy jednoczesnym ponad 50-procentowym stopniu odaromatyzowania surowca. Opisano zależność pomiędzy składem chemicznym i właściwościami fizykochemicznymi katalizatorów a stopniem ich zakoksowania oraz charakterem depozytów węglowych, ze szczególnym uwzględnieniem podatności koksu na utlenienie.
EN
ZSM-5 zeolites, two-component ZSM-5+Al203 systems, nickel catalysts and nickel-ruthenium catalysts supported on the ZSM-5+Al203 were analyzed for physicochemical and catalytic properties, which were related to the preparation method used, as well as to the chemical composition. Consideration was given to the problem of how the method of combining the zeolite with aluminium hydroxide affects the texture and acid properties of ZSM-5+Al203 systems, and how the method of nickel catalyst preparation influences metal-support interactions and catalyst activity in cracking and selective cracking (dewaxing) straight-chain paraffin hydrocarbons and their monomethyl isomers. For nickel and nickel-ruthenium catalysts, a correlation was found to occur between chemical composition, preparation method and hydrogenating activity in aromatics conversion. For nickel catalysts, a correlation was established between the metal to acid ratio and selectivity in toluene hydrogénation. It has been demonstrated that the method of nickel incorporation and the conditions of thermal treatment influence the nickel-support interactions, and that the quantity of ruthenium, the type of ruthenium precursor and the method of nickel catalyst preparation impact on the metal-metal (Ru-Ni) and metal-support interactions, as well as on the hydrogenating properties of the catalysts in the conversion of 1-methyl-naphthalene. A catalyst formula was derived for obtaining the desired quantity of products which form during conversion of the diesel oil fraction in two 'opposite' reactions (exothermic hydrogénation reaction and en-dothermic cracking reaction). The products attained at optimal temperature displayed sufficiently good cold-flow properties, and the dearomatization of the feed exceeded 50%. The chemical composition and physicochemical properties of the catalysts were related to the degree of coking and to the character of the carbonaceous deposits, particular consideration being given to the oxidability of the coke.
Rocznik
Strony
190--190
Opis fizyczny
s., bibliogr. 298 poz.
Twórcy
autor
  • Wydział Chemiczny Politechniki Wrocławskiej, Wybrzeże Wyspiańskiego 27, 50-370 Wrocław.
Bibliografia
  • [1] ABBOT J., WOJCIECHOWSKI B.W., Catalytic Cracking and Skeletal homerization of n-Hexene on ZSM-5 Zeolite, Can. J. Chem. Eng., 1985, Vol. 63, 451-461
  • [2] ABOUL-GHEIT A.K., ABOUL-GHEIT N.A.K., Iridium/H-ZSM-5 zeolite catalyst promoted via hydrochlorination or hydrofluorination for the hydroconversion of cyclohexene, Appl. Catal. A: Gen., 2006, Vol.303, 141-151
  • [3] ABOUL-GHEIT A.K., ABOUL-FOTOUH S.M., ABDEL-HAMID S.M., ABOUL-GHEIT N.A.K., Hydroconversion of cyclohexene using H-ZSM-5 zeolite catalysts promoted via hydrochlorination and/or platinum incorporation, J. Mol. Catal. A, Chem., 2006, Vol. 245, 167-177
  • [4] ABOUL-GHEIT A.K., AWADALLAH A.E., ABOUL-GHEIT N.A.K., SOLYMAN E.S.A., ABDEL-AATY M.A., Effect of hydrochlorination and hydrofluorination of Pt/H-ZSM-5 and Pt-Ir/H-ZSM-5 catalysts for n-hexane hydroconversion, Appl. Catal. A: Gen., 2008, Vol. 334, 304-310
  • [5] AGUAYO A.T., GAYUBO A.G., ORTEGA J.M., OLAZAR M., BILBAO J., Catalyst deactivation by coking in the MTG process in fixed and fluidized bed reactors, Catal. Today, 1997, Vol. 37, 239-248
  • [6] AKHMEDOV V.M., AL-KHOWAITER S.H., AKHMEDOV E., SADIKHOV A., Low temperature hydrocracking of hydrocarbons on Ni-supported catalysts, Appl. Catal. A, 1999, Vol. 181, 51-61
  • [7] AKHMEDOV V.M., AL-KHOWAITER S.H., Hydroconversion of hydrocarbons over Ru-containing supported catalysts prepared by metal vapor method, Appl. Catal. A, 2000, Vol. 197, 201-212
  • [8] AKHMEDOV V.M., AL-KHOWAITER S.H., AL-REFAI J.K., Hydroconversion of C5-C8 alkanes over Zr-containing supported catalysts prepared by metal vapor method, Appl. Catal. A: Gen., 2003, Vol.252, 353-361
  • [9] ALHUMAIZI K.I., AKHMEDOV V.M., AL-ZAHRANI S.M., AL-KHOWAITER S.H., Low temperature hydrocracking of n-heptane over Ni-supported catalysts: study of global kinetics, Appl. Catal. A: Gen., 2001, Vol. 219, 131-140
  • [10] AL-DALAMA K., STANISLAUS A., Comparison between deactivation pattern of catalysts in fixed-bed and ebullating-bed residue hydroprocessing units, Chem. Eng. J., 2006, Vol. 120, 33-42
  • [11] ALI A., ALI L.I., ABOUL-FOTOUH S.M., ABOUL-GHEIT A.K., Hydrogénation of aromatics on modified platinum-alumina catalysts, Appl. Catal. A: Chem., 1998, Vol. 170, 285-296.
  • [12] ALVAREZ-RODRIGUEZ J., GUERRERO-RUIZ A., RODRIGUEZ-RAMOZ I., ARCOYA-MARTIN A., Modifications of the citral hydrogenation selectivities over Ru/KL-zeolite catalysts induced by the metal precursors, Catal. Today, 2005, Vol. 107-108, 302-309
  • [13] ARCOYA A., SEOANE X.L., GÓMEZ-SAINERO L.M., Activity of Pd/Al203 and Ru/Al203 catalysts in the hydrogenation of o-xylene: Effect of thiophene, Appl. Surf. Sci., 2003, Vol. 211, 341-351
  • [14] ASSAF E.M., JESUS L.C., ASSAF J.M., The active phase distribution in Ni/Al203 catalysts and mathematical modelling of the impregnation process, Chem. Eng. J., 2003, Vol. 94, 93-98.
  • [15] BARBIER J., CARRO G., ZHAG Y., BOURNORICILLE LP., FRANK P., Coke formation on platinum-alumina catalyst of wide varying dispersion, Appl. Catal., 1985, Vol. 13, 245-255.
  • [16] BARBIER J., Deactivation of reforming catalysts by coking - a review, Appl. Catal., 1986, Vol. 23, 225-243.
  • [17] BARBIER J., CHURIN E., MARECOT P., MENEZO J.C., Deactivation by coking of platinum/aluminacatalysts: Effects of operating temperature and pressure, Appl. Catal. 1988, Vol. 36, 277-285.
  • [18] BARRIO V.L., ARIAS P.L., CAMBRA J.F., GÜEMEZ M.B., PAWELEC B., FIERRO J.L.G.,Aromatics hydrogénation on silica-alumina supported palladium-nickel catalysts, Appl. Catal. A:Gen., 2003, Vol. 242, 17-30.
  • [19] BARRIO V.L., ARIAS P.L., CAMBRA J.F., GÜEMEZ M.B., CAMPOS-MARTIN J.M.,PAWELEC B., FIERRO J.G.L., Evaluation of silica-alumina-supported nickel catalysts in dibenzothiophene hydrodesulphurisation, Appl. Catal. A: Gen., 2003, Vol. 248, 211-225.
  • [20] BARRIO V.L., ARIAS P.L., CAMBRA J.F., GÜEMEZ M.B., PAWELEC B., FIERRO J.L.G.,Modification of the Pd/Si02-Al203 catalyst's thioresistance by the addition of a second metal (Pt,Ru, and Ni), Catal. Commun., 2004, Vol. 5, 173-178.
  • [21] BARTHOLDY J., ZEUTHEN P., MASSOTH F.E., Temperature-programmed oxidation studies of aged hydroprocessing catalysts, Appl. Catal. A, 1995, Vol. 129, 33-42.
  • [22] BARTHOLOMEW CH., AGRA W AL P.K., KATZER J.R., Sulfur poisoning of metals, Advances inCatalysis, 1982, Vol. 31, 135-242.
  • [23] BARTHOLOMEW CH., Mechanisms of catalyst deactivation, Appl. Catal. A:Gen., 2001, Vol. 212,17-60.[
  • [24] BAYRAKTAR O., KUGLER E.L., Temperature-programmed oxidation of equilibrium fluid catalytic cracking catalysts effects of pretreatment on coke formation, J. Therm. Anal. Cal., 2004, Vol. 75, 989-998.;
  • [25] BEHRSING T., JAEGER H., SANDERS J.V., Coke Deposits on H-ZSM-5 Zeolite, Appl. Catal., 1989, Vol. 54, 289-302
  • [26] BERNAS A., KUMAR N., LAUKKANEN P., VÂYRYNEN J., SALMI T., MURZIN D.YU., Influence of ruthenium precursor on catalytic activity of Ru/Al203 catalyst in selective isomerization of linoleic acid, Appl. Catal. A: Gen., 2004, Vol. 267, 121-133
  • [27] BETANCOURT P., RIVES A., HUBAUT R., SCOTT CE., GOLDWASSER J., A study of the ruthenium-alumina system, Appl. Catal., 1998, Vol. 170, 307-314
  • [28] BHAT Y.S., DAS J., HALGERI A.B., Effect of extrusion and silylation ofZSM-5 on para selectivity of diethylbenzenes, Appl. Catal. A: Gen., 1995, Vol. 122, 161-168
  • [29] BHATIA S., BELTRAMINI J., DO D.D., Temperature programmed analysis and its applications in catalytic systems, Catal. Today, 1990, Vol. 7, 309-438
  • [30] BIBBY D.M., HOWE R.F., MC LELLAN G.D., Coke formation in high-silica zeolites, Appl. Catal., 1992, Vol.93, 1-34
  • [31] BLOMSMA E., MARTENS J.A., JACOBS P. A., Mechanisms of heptane isomerization on bifunctional Pd/H-Beta zeolites, J. Catal., 1996, Vol. 159, 323-331.
  • [32] BORGNA A., GARETTO T.F., APESTEGUÍA C.R., Simultaneous deactivation by coke and sulfur of bimetallic Pt-Re(Ge, Sn)/Al203 catalysts for n-hexane reforming, Appl. Catal. A:Gen., 2000, Vol.197, 11-21
  • [33] CAIRON O., THOMAS K, CHAMBELLAN A., CHEVREAU T., Acid-catalysed benzene hydro-conversion using various zeolites: Brônsted acidity, hydrogenation and side-reactions, Appl. Catal. A:Gen., 2003, Vol. 238, 167-183
  • [34] CANIZARES P., DE LUCAS A., DORADO F., DURAN A., ASCENCIO I., Characterization of Ni and Pd supported on H-mordenite catalysts: Influence of the metal loading method, Appl. Catal. A: Gen., 1998, Vol. 169, 137-150.
  • [35] CARUSO F., JABŁOŃSKI E.L., GRAU J.M., PARERA J.M., Crystallinity of coke on platinum-rhenium/alumina reforming catalyst during the commercial cycle, Appl. Catal., 1989, Vol. 51, 195-202
  • [36] CARVALHO L.S., PIECK C.L., RANGEL M.C., FIGOLI N.S., VERA C.R., PARERA J.M., Tri-metallic naphtha reforming catalysts II. Properties of the acid function and influence of the order of addition of the metallic precursors on Pt-Re-Sn/y-Al2OrCl, Appl. Catal. A:Gen., 2004, Vol. 269, 105-116
  • [37] CATTENOT M., GEANTET C, GLASSON C, BREYSSE M„ Promoting effect of ruthenium on NiMo/Al203 hydrotreating catalysts, Appl. Catal. A:Gen., 2001, Vol. 213, 217-224
  • [38] CERQUEIRA H.S., AYRAULT P., DATKA J., GUISNET M., Influence of coke on the acid properties of a USHY zeolite, Micropor. Mesopor. Mater., 2000, Vol. 38, 197-205
  • [39] CERQUEIRA H.S., MAGNOUX P., MARTIN D., GUISNET M., Coke formation and coke profiles during the transformation of various reactants at 450 °C over USHY zeolite, Appl. Catal. A: Gen., 2001, Vol. 208, 359-367
  • [40] CERRO-ALARCON M., MAROTO-VALIENTE A., RODRIGUEZ-RAMOS I., GUERRERO-RUIZ A., Further insights into the Ru nanoparticles-carbon interactions and their role in the catalytic properties, Carbon, 2005, Vol. 43, 2711-2722
  • [41] CHAO K.J., WU H.C., LEU L.J., Hydroisomerization of light normal paraffins over series of platinum-loaded mordenite and beta catalysts, Appl. Catal. A: Gen., 1996, Vol. 143, 223-243
  • [42] CHATTERJEE C, GREENE H.L., PARK Y.J., Deactivation of metal exchanged zeolite catalysts during exposure to chlorinated hydrocarbons under oxidizing conditions, Catal. Today, 1992, Vol. 11, 569-596
  • [43] CHEAH K.V., ALEXANDER P., GLADDEN L.F., Investigation of coking phenomena in zeoliteHYusing deuterium NMR, Appl. Catal. A: Gen., 1997, Vol. 148, 387-403.
  • [44] CHEN N.Y., GORRING R.L., IRELAND H.R., STEIN T.R., New process cut pour point of distillates, Oil and Gas J., 1977, Vol. 75, Nr 23, 165-170.
  • [45] CHOU P., VANNICE M.A., Benzene hydrogenation over supported and unsupported palladium: I. Kinetic behavior, J. Catal., 1987, Vol. 107, 129-139.
  • [46] CHOUDHARY V.R., DEVADAS P., KINAGE A.K., GUISNET M., Influence of binder on theacidity and performance of H-Gallosilicate (MFI) zeolite in propane aromatization, Appl. Catal. A:Gen., 1997, Vol. 162, 223-233.
  • [47] CHUPIN J., GNEP N.S., LACOMBE S., GUISNET M„ Influence of the metal and of the support onthe activity and stability of bifunctional catalysts for toluene hydrogenation, Appl. Catal. A: Gen.,2001, Vol. 206, 43-56
  • [48] COMELLI R.A., CANAVESE S.A., QUERINI C.A., FIGOLI N.S., Coke deposition on platinum promoted WOx-Zr02 during n-hexane isomerization, Appl. Catal. A: Gen., 1999, Vol. 182, 275-283
  • [49] COOPER B.H., DONNIS B.B.L., Aromatic saturation of distillates: an overview, Appl. Catal. A:Gen., 1996, Vol. 137, 203-223.
  • [50] CORDOBA G., FIERRO J.L.G., LOPEZ-GAONA A., MARTIN N., VINIEGRA M„ Probing Ru-Pd/Si02 catalysts by gas phase o-xylene hydrogenation, J. Mol. Catal. A: Chem., 1995, Vol. 96,155-161
  • [51] CRISAFULLI C, MAGGIORE R., SCIRE S., GALVAGNO S., Ru-Cu/Si02 catalysts: characterization by FTIR spectroscopy, J. Chem. Soc. Faraday Trans., 1994, Vol. 90, 2809-2813.
  • [52] CRISAFULLI C, SCIRE S., MAGGIORE R., MINICO S., GALVAGNO S., C02 reforming ofmethane over Ni-Ru and Ni-Pd bimetallic catalysts, Catal. Lett., 1999, Vol. 59, 21-26.
  • [53] CRISAFULLI C, SCIRE S„ MINICO S., SOLARINO L., Ni-Ru bimetallic catalysts for the C02 reforming of methane, Appl. Catal. A: Gen., 2002, Vol. 225, 1-9.164
  • [54] CZERWIŃSKA B„ MOSTOWICZ R., MEJSNER J., PIENIĄŻEK J., SZTYLLER J., WOSZEK B.,MAŁECKI Z., Poland Patent 156 978 (1990), to IChP Warsaw.
  • [55] DAI P.S.E., TAYLOR R.J. Jr., PETTY R.H., Zeolite catalyst for dewaxing hydrocarbon feed stocks,U.S. 5,391,286 Feb., 21, 1995; Appl. Nov. 3,1993.
  • [56] DEAN J.W., DADYBURJOR D.B., Activity and coke deposition on a composite acid catalyst andits components, Ind. Eng. Chem. Res., 1989, Vol. 28, 271-276.
  • [57] DEGNAN, T.F. Jr., Applications of zeolites in petroleum refining, Topics in Catalysis, 2000, Vol. 13,349-356
  • [58] DEGNAN T.F., The implications of the fundamentals of shape selectivity for the development of catalysts for the petroleum and petrochemical industries, J. Catal., 2003, Vol. 216, 32-46
  • [59] DESSAU R.M., MIDDLESEX N.J., Shape selective hydrogenation of aromatics over modified non-acidic platinum/ZSM-5 catalysts, US Patent 5350504, 1994, to Mobil Oil Corporation
  • [60] DING C, WANG X., GUO X., ZHANG S., Characterization and catalytic alkylation of hydrothermally dealuminated nanoscale ZSM-5 zeolite catalyst, Catal. Commun., 2007, Vol. 9, 487-493
  • [61] DOESBURG E.B.M., van HOOFF J.H.C., Preparation of catalyst support and zeolites, Stud. Surf. Sci. Catal., 1993, Vol. 79, 309-333
  • [62] van DOORN J., VERHEUL R.C.S., SINGOREDJO L., MOULIJN J.A., Characterization of carbon deposits on alumina supported cobalt and nickel by temperature programmed gasification with 02, C02 andH2, Fuel, 1986, Vol. 651, 385-1385
  • [63] van DOORN J., BARBOLINA H.A.A., MOULIJN J.A., Temperature-programmed gasification of the coke on spent hydrotreating catalysts with oxygen and hydrogen, Ind. Eng. Chem. Res., 1992, Vol. 31, 101-107
  • [64] DORADO F., ROMERO R., CAÑIZARES P., Influence of clay binders on the performance of Pd/HZSM-5 catalysts for the hydroisomerization of n-butane, Ind. Eng. Chem. Res., 2001, Vol. 40, 3428-3434
  • [65] DORADO F., ROMERO R., CAÑIZARES P., Hydroisomerization of n-butane over Pd/HZSM-5 andPd/HR with and without binder, Appl. Catal. A: Gen., 2002, Vol. 236, 235-243
  • [66] DUCHET J.C., GUILLAUME D., MONNIER A., DUJARDIN C, GILSON J.P., van GESTEL J., SZABO G., NASCIMENTO P., Isomerization of n-hexane over sulfated zirconia: Influence of hydrogen and platinum, J. Catal., 2001, Vol. 198, 328-337
  • [67] DUPREZ D., MÉNDEZ M., The effect of partial reduction on the thioresistance of Ni/Al20¡ catalysts, Stud. Surf. Sci. Catal., 1987, Vol. 34, 523-534
  • [68] DUPREZ D., HADJ-AISSA M., BARBIER J., Effect of steam on coking of Pt catalysts, Appl. Catal., 1989, Vol. 49, 67-74
  • [69] ELICHE-QUESADA D., MÉRIDA-ROBLES J.M., RODRÍGUEZ-CASTELLÓN E., JIMÉNEZ-LÓPEZ A., Ru, Os and Ru-Os supported on mesoporous silica doped with zirconium as mild thio-tolerant catalysts in the hydrogénation and hydrogenolysis/ hydrocracking of tetralin, Appl. Catal. A: Gen., 2005, Vol. 279, 209-221
  • [70] ELICHE-QUESADA D., MÉRIDA-ROBLES J.M., RODRÍGUEZ-CASTELLÓN E., JIMÉNEZ-LÓPEZ A., Influence of the incorporation of palladium on Ru/MCM hydrotreating catalysts, Appl. Catal. B: Environ., 2006, Vol. 65, 118-126
  • [71] FERNANDES L.D., MONTEIRO J.L.F., SOUSA-AGUIAR E.F., MARTINEZ A., CORMA A., Ethylbenzene hydroisomerization over bifunctional zeolite based catalysts: The influence of framework and extraframework composition and zeolite structure, J. Catal., 1998, Vol. 177, 363-377
  • [72] FOGASH K.B., HONG Z., KOBE J.M., DUMESIC J.A., Deactivation of sulfated-zirconia and H-mordenite catalysts during n-butane and isobutane isomerization, Appl. Catal. A:Gen., 1998, Vol. 172, 107-116
  • [73] FORZATTI P., LETTI L„ Catalyst deactivation, Catal. Today, 1999, Vol. 52, 165-181.
  • [74] FOUGERIT J.M., GNEP N.S., GUISNET M., AMIGUES P., DUPLAN J.H., HUGUES F.E., Effectof binder on the properties of a mordenite catalysts for the selective conversion of the methanol intolight olefins, Stud. Surf. Sci. Catal., 1994, Vol. 84, 1723-1730.
  • [75] FROMENT G. F., Kinetics of the hydroisomerization and hydrocracking of paraffins on a platinum containing bifunctional Y-zeolite, Catal. Today, 1987, Vol. 1, 455-473.
  • [76] FUNG S.C., QUERINI C.A., A highly sensitive detection method for temperature programmed oxidation of coke deposits: Methanation of C02 in the presence of O2 J. Catal., 1992, Vol. 138,240-254
  • [77] FURIMSKY E., MASSOTH F.E., Regeneration of hydroprocessing catalysts. Introduction, Catal.Today, 1993, Vol. 17, 537-659.
  • [78] FURIMSKY E., Selection of catalysts and reactors for hydroprocessing, Appl. Catal. A:Gen., 1998,Vol. 171, 177-206
  • [79] FURIMSKY E., MASSOTH F.E., Deactivation of hydroprocessing catalyst, Catal. Today, 1999, Vol. 52, 381-495
  • [80] GALPERIN L.B., BRADLEY S.A., MEZZA T.M., Hydroisomerization ofn-decane in the presence of sulfur: Effect of metal-acid balance and metal location, Appl. Catal. A: Gen., 2001, Vol. 219, 79-88.
  • [81] GAVRILIDIS A., VARMA A., Optimal distribution of catalyst in pellets, Catal. Rev. Sci. Eng.,1993, Vol. 35, 399-456
  • [82] GERVASINI A., Characterization of the textural properties of metal loaded ZSM-5 zeolites, Appl.Catal. A: Gen., 1999, Vol. 180, 71-82.
  • [83] GEUS J.W., van VEEN J.A.R., Catalysis. An integrated approach to homogeneous, heterogeneousand industrial catalysis, Stud. Surf. Sci. Catal., 1993, Vol. 79, 335-362.
  • [84] GIL A., DIAZ A., GANDIA L.M., MONTES M., Influence of the preparation method and the natureof the support on the stability of nickel catalysts, Appl. Catal. A: Gen., 1994, Vol. 109, 167-179.
  • [85] GOPAL S., SMIRNIOTIS P.G., Deactivation behavior of bifunctional Pt/H-zeolite catalysts duringcyclopentane hydroconversion, J. Catal., 2002, Vol. 205, 231-243.
  • [86] GÓRALSKI J., GRAMS J., LUDOMIRSKA I., PARYJCZAK T., RZEŹNICKA I., Carbonaceous deposits and their investigations by various techniques, Wiadomości Chemiczne, 2000, Vol. 54,591-614
  • [87] GRAU J.M., PARERA J.M., Deactivation of Pt-Re/Al203 catalysts with different metallic charge, Appl. Catal., 1991, Vol. 70, 9-18
  • [88] GRZECHOWIAK R.J., MASALSKA A., ROMOTOWSKI T., KOMOREK J., The role of ion exchange method of Na ZSM-5 zeolite and influence of hydrogenation components on properties and activity of dewaxing catalysts, Collect. Czech. Chem. Commun., 1992, Vol. 57, 969-977'
  • [89] GRZECHOWIAK R.J., MASALSKA A., Zeolite catalysts Ni,H-ZSM-5/Al203 in ecologically friendly process, Scientific Papers of the Institute of Chemistry and Technology of Petroleum and Coal of the Wroclaw University of Technology, 1994, No. 52, 147-152
  • [90] GRZECHOWIAK R.J., MASALSKA A., Influence of heteropoly acid and USY zeolite on activity of ZSM-5 containing catalysts, Scientific Papers of the Institute of Chemistry and Technology of Petroleum and Coal of the Wrocław University of Technology, 2002, No. 57, 343-348
  • [91] GRZECHOWIAK R.J., MASALSKA A., GRZECHOWIAK J., Katalizatory dla procesu katalitycznego odparafinowania, Materiały I Kongresu Technologii Chemicznej, p. 462, 19-22 września,1994, Wydawnictwo Politechniki Szczecińskiej, Szczecin, 1995, 462-465
  • [92] GRZECHOWIAK R. I, MASALSKA A., GRZECHOWIAK J., Z badań nad opracowaniem katalizatora dla procesu katalitycznego odparafinowania olejów napędowych, Przem. Chem., 1996, Vol. 75, Nr 8, 295-298
  • [93] GRZECHOWIAK R.J., MASALSKA A., KĘPIŃSKI L., RYNKOWSKI I, Deactivation studies on Ni,H-ZSM-5 containing catalysts: Effect of nickel incorporation, Stud. Surf. Sci. Catal., 1997, Vol. 111,681-686.166
  • [94] GUISNET M., ALVAREZ F., GIANETTA G., PEROT G., Hydroisomerization and hydrocracking of n-heptane on PtH zeolites. Effect of the porosity and of the distribution of metallic and acid sites, Catal. Today, 1987, Vol. 1,415-433
  • [95] GUISNET M., MAGNOUX P., Coking and deactivation of zeolites: Influence of the pore structure, Appl. Catal., 1989, Vol. 54, 1-27
  • [96] GUISNET M, MAGNOUX P., Fundamental description of deactivation and regeneration of acid zeolites, Stud. Surf. Sci. Catal., 1994, Vol. 88, 53-68
  • [97] GUISNET M., MAGNOUX P., Deactivation by coking of zeolite catalyst. Prevention of deactivation. Optimal condition for regeneration, Catal. Today, 1997, Vol. 36, 477—483
  • [98] GUISNET M., MAGNOUX P., Organic chemistry of coke formation, Appl. Catal. A: Gen., 2001, Vol.212, 83-96
  • [99] GUISNET M., COSTA L., RIBEIRO F.R., Prevention of zeolite deactivation by coking, J. Mol. Catal. A: Chem., 2009, Vol. 305, 69-83
  • [100] HADJILOIZOV G.C., BUTT J.B., DRANOFF J.S., Piperidine hydrogenolysis on a commercial hydrocracking catalyst: II. The effects of initial piperidine concentration, temperature, catalyst presulfidation, and hydrogen partial pressure on catalyst activity, deactivation, and coke formation, J. Catal., 1992, Vol. 135, 27-44
  • [101] HAGEN A., SCHNEIDER E., KLEINERT A., ROESSNER F., Modification of acid supports by solid-state redox reaction: Part I. Preparation and characterization, J. Catal., 2004, Vol. 222, 227-237
  • [102] HAGEN A., SCHNEIDER E., BENTER M., KROGH A., KLEINERT A., ROESSNER F., Modification of acid supports by solid-state redox reaction: Part II. Acid and catalytic properties, J. Catal., 2004, Vol. 226, 171-182
  • [103] HARGROVE J.D., ELKES G.J., RICHARDSON A.H., New dewaxing process in operations, Oil and Gas J., 1979, Vol. 77, 103-105
  • [104] HARTMANN M., BISHOF C, LU AN Z., KEVAN L., Preparation and characterization of ruthenium clusters on mesoporous supports, Micropor. Mesopor. Mater., 2001, Vol. 44-45, 385-394
  • [105] HARVEY T.G., PRATT K.C., The effect of ruthenium loading on Ru-zeolite/NiMo HDN catalysts, Appl. Catal. A: Gen., 1996, Vol. 146, 317-321
  • [106] HELTON T.E., DEGNAN T.F. JR, MAZZONE D.N., Mc GUINNESS M.P., HILBERT T.L., DOUGHERTY R.C., Catalytic hydroprocessing a good alternative to solvent processing, Oil and Gas I, 1998, Vol. 96, Nr 29, 58-63
  • [107] HERACLEOUS E., LEE A.F., WILSON K, LEMONIDOU A.A., Investigation of Ni-based alumina-supported catalysts for the oxidative dehydrogenation of ethane to ethylene: structural characterization and reactivity studies, J. Catal., 2005, Vol. 231, 159-171
  • [108] HOANG D.L., BERNDT H., MIESSNER H., SCHREIER E., VÔLTER J., LIESKE H., Nickiel modifiedH-ZSM-5 catalysts, Appl. Catal. A:Gen., 1994, Vol. 114, 295-311
  • [109] HOFFER B.W., LANGEVELD A.D., JANSSENS J.-P., BONNE R.L.C., LOK CM., MOULIJN J.A., Stability of highly dispersed Ni/Al203 catalysts: Effects of pretreatment, J. Catal., 2000, Vol. 192, 432-440
  • [110] HOLMES S.M., GARFORTH A., MAUNDERS B„ DWYER J., A solvent extraction method to study the location and concentration of coke formed on zeolite catalysts, Appl. Catal. A: Gen., 1997, Vol. 151, 355-372
  • [111] HOMAN FREE H.W., SCHOCKAERT T., SONNEMANS I.W.M., The Akzo-Fina cold flow improvement process, Fuel Process. Technol., 1993, Vol. 35, 111 117
  • [112] HOPKINS P.D., MILLER J.T., MEYERS B.L., RAY G.J., ROGINSKI R.T., KUEHNE M.A., KUNG H.H., Acidity and cracking activity changes during coke deactivation of ultrastable Y zeolite, Appl. Catal. A: Gen., 1996, Vol. 136, 29-48.167
  • [113] HOUZVICKA J., HANSILDAAR S., NIENHUIS J.G., PONEC V., The role of deposits in butene isomerisation, Appl. Catal. A: Gen., 1999, Vol. 176, 83-89
  • [114] HUANG T.C., KANG B.C., Kinetic study of naphtalene hydrogénation over Pt/Al203 catalyst, Ind. Eng. Chem. Res., 1995, Vol. 34, 1140-1148
  • [115] HUYBRECHTS W., THYBAUT J.W., DE WAELE B.R., VANBUTSELE G., HOUTHOOFD K.J., BERTINCHAMPS F., DENAYER J.F.M., GAIGNEAUX E.M., MARIN G.B., BARON G.V., JACOBS P.A., MARTENS J.A., Bifunctional catalytic isomerization of decane over MTT-type aluminosilicate zeolite crystals -with siliceous rim, J. Catal., 2006, Vol. 239, 451- 459
  • [116] INUI T., SUZUKI T., INOUE M„ MURAKAMI Y., TAKEGAMI Y., Relation between acidic properties of ZSM-5 and catalyst performance of methanol conversion to gasoline, Structure and reactivity of modified zeolites, Stud. Surf. Sei. Catal., 1984, Vol. 18, 201-208
  • [117] IRELAND H.R., REDINI C, RAFF A.S., FAVA L., Distillate dewaxing in operation, Hydrocar. Proc., 1979, Vol. 58, Nr 5, 119-122
  • [118] ISAZA M.N., PACHON Z., KAFAROV V., RESASCO D.E., Deactivation of Ni-Mo/Al203 catalysts aged in a commercial reactor during the hydrotreating of deasphalted vacuum residuum, Appl. Catal. A: Gen., 2000, Vol. 199, 263-273
  • [119] ISHIHARA A., QIAN E.W., FINAHARI I.N., SUTRISNA I.P., KABE T., Addition effect of ruthenium on nickel steam reforming catalysts, Fuel, 2005, Vol. 84, 1462-1468
  • [120] JACOBS P.A., MARTENS J.A., Introduction to acid catalysis with zeolites in hydrocarbon reactions, Stud. Surf. Sei. Catal., 1991, Vol. 58, 445-496
  • [121] JACOBSEN C.J.H., MADSEN C, JANSSENS T.V.W., JAKOBSEN HJ., SKIBSTED J., Zeolites by confined space synthesis - characterization of the acid sites in nanosized ZSM-5 by ammonia desorption and 27AlfSi-MAS NMR spectroscopy, Micropor. Mesopor. Mater., 2000, Vol. 39, 393-401
  • [122] JACONO M.L., SCHHIAVELLO M., CIMINO A., Structural, magnetic, and optical properties of nickel oxide supported on n- and y-aluminas, J. Phys. Chem., 1971, Vol. 75, 1044-1050
  • [123] JACQUIN M., JONES D.J., ROZIÈRE J., ALBERTAZZI S., VACCARI A., LENARDA M., STORARO L., GANZERLA R., Novel supported Rh, Pt, Ir and Ru mesoporous aluminosilicates as catalysts for the hydrogénation of naphthalene, Appl. Catal. A: Gen., 2003, Vol. 251, 131-141
  • [124] JENTYS A., LUGSTEIN A., VINEK H., Characterization of metallic species on Ni- and Co-containing ZSM-5 catalysts - reduction behavior and catalytic properties, Zeolites, 1997, Vol. 18, 391-397
  • [125] JIMENEZ C, ROMERO F.J., ROLDÂN R., MARINAS J.M., GÖMEZ J.P., Hydroisomerization of a hydrocarbon feed containing n-hexane, n-heptane and cyclohexane on zeolite-supported platinum catalysts, Appl. Catal. A: Gen., 2003, Vol. 249, 175-185
  • [126] JOLLY S., SAUSSEY J., BETTAHAR M.M., LA VALLEY J.C., BENAZZI E., Reaction mechanisms and kinetics in n-hexane cracking over zeolites, Appl. Catal. A: Gen., 1997, Vol. 156, 71 -96
  • [127] JÔZWIAK W.K., NOWOSIELSKA M., RYNKOWSKI J., Reforming of methane with carbon dioxide over supported bimetallic catalysts containing Ni and noble metal: I. Characterization and activity ofSi02 supportedNi-Rh catalysts, Appl. Catal. A: Gen., 2005, Vol. 280, 233-244
  • [128] KARGE H.G., BOLDINGH E.P., Spectroscopic investigations on deactivation of zeolite catalysts during reactions of olefins, Catal. Today, 1988, Vol. 3, 379-386
  • [129] KASTORE M.W., NIPHADKAR P.S., BOKADE V.V., JOSHI P.N., On the catalytic performance in isopropylation of benzene over H/ß zeolite catalysts: Influence of binder, Catal. Commun., 2007, Vol. 8, 1003-1008
  • [130] KE J.A., WANG I., Elucidation of the role of potassium fluoride in the chemical and physicalnature of ZSM-5 zeolite, Mater. Chem. Phys., 2001, Vol. 68, 157-165.
  • [131] KEANE M.A., The hydrogénation of o-,m-, and p-xylene over Ni/Si02, J. Catal. 1997, Vol. 166,347-355.168
  • [132] KEANE M.A., PATTERSON P.M., The role of hydrogen partial pressure in the gas-phase hydrogénation of aromatics over supported nickel, Ind. Eng. Chem. Res., 1999, Vol. 38, 1295-1305
  • [133] KESKITALO T.J., LIP1ÀINEN K.J.T., KRAUSE A.O.I., Modelling of carbon and hydrogen oxidation kinetics of a coked ferrierite catalyst, Chem. Eng. J., 2006, Vol. 120, 63-71
  • [134] KHARAT A.N., PENDLETON P., BAD AL Y AN A., ABEDINI M., AMINI M.M., Decomposition of nickel formate on sol-gel alumina and characterization of product by X-ray photoelectron and TOF-SJMS Spectroscopies, J. Catal., 2002, Vol. 205, 7-15
  • [135] KINGER G., LUGSTEIN A., SWAGERA R., EBEL M., JENTYS A., VINEK H., Comparison of impregnation, liquid- and solid-state ion exchange procedures for the incorporation of nickel in HMFf HMOR and HBEA: Activity and selectivity in n-nonane hydroconversion, Micropor. Meso-por. Mater., 2000, Vol. 39, 307-317
  • [136] KIRUMAKKI S.R., SHPEIZER B.G., SAGAR G.V., CHARY K.V.R., CLEARFIELD A., Hydrogenation of naphthalene over NiO/Si02-Al20; catalysts: Structure-activity correlation, J. Catal., 2006, Vol. 242,319-331
  • [137] KLUG H.P., ALEXANDER L.E., X-ray Diffraction Procedures, Wiley, New York (1974), 661
  • [138] KOTANIGAWA T., YAMAMOTO M., YOSHIDA T., Selective nuclear hydrogenation of naphthalene, anthracene and coal-derived oil over Ru supported on mixed oxide, Appl. Catal. A: Gen., 1997, Vol. 164,323-332
  • [139] KOUGIONAS V., CATTENOT M., ZOTIN J.L. PORTEFAIX J.L., BREYSSE M„ Enhancement of the catalytic properties of NiMo and CoMo alumina-supported sulfide catalysts by addition of ruthenium sulfide dispersed in Y zeolite, Appl. Catal. A: Gen., 1995, Vol. 124, 153-164
  • [140] KOUSSATHANA M., VAMVOUKA D., ECONOMOU H., VERYKIOS X., Slurry-phase hydrogenation of aromatic compounds over supported noble metal catalysts, Appl. Catal., 1991, Vol. 77, 283-301
  • [141] KOUSSATHANA M., VAMVOUKA D., TSAPATSIS M., VERYKIOS X., Hydrogénation of aromatic compounds over noble metals dispersed on doped titania carriers, Appl. Catal. A: Gen., 1992, Vol.80, 99-113
  • [142] KRIZ F., SHIMADA H., YOSHIMURA Y., MATSUBAYASHI N., NISHIJIMA A., Nickel-containing catalysts for hydroprocessing of aromatic oils, Fuel, 1995, Vol., 74, 1852-1857
  • [143] KUKLINSKII A.YA., PUSHKINA R.A., A study of the structure of saturated hydrocarbons of oils, petroleum products and organic rock matter from infrared absorption spectra, Neftekhimiya, 1980, Vol. 20, No. 3, 346-353
  • [144] LEDERHOS C.R., L'ARGIENTIERE P.C., COLOMA-PASCUAL F., FIGOLI N.S., A study about the effect of the temperature of hydrogen treatment on the properties of Ru/Al2Oj and Ru/C and their catalytic behavior during 1-heptyne semi-hydrogenation, Catal. Lett., 2006, Vol. 110, 23-28
  • [145] LEE M.H., CHENG CF., HEINE V., KLINOWSKI J., Distribution of tetrahedral and octahedral AI sites in gamma alumina, Chem. Phys. Lett., 1997, Vol. 265, 673-676
  • [146] LEKHAL A., GLASSER B.J., KHINAST J.G., Influence of pH and ionic strength on the metal profile of impregnation catalysts, Chem. Eng. Sci., 2004, Vol. 59, 1063-1077
  • [147] LI CH., CHEN Y.W., Temperature-programmed-reduction studies of nickel oxide/alumina catalysts, Thermochimica Acta, 1995, Vol. 256, 457-465
  • [148] LI B., GONZALEZ R.D., The effect of coke deposition on the deactivation of sulfated zirconia catalysts, Appl. Catal. A: Gen., 1998, Vol. 174, 109-119
  • [149] LI C, MINH C.L., BROWN T.C., Kinetics of CO and C02 evolution during the temperature-programmed oxidation of coke deposited on cracking catalysts, J. Catal., 1998, Vol. 178, 275-283
  • [150] LI C.L., NOVARO O., MUNOZ E., BOLDU J.L., BOKHIMI X„ WANG J.A., LOPEZ T, GOMEZ R., Coke deactivation of Pd/H-mordenite catalysts used for C5/C6 hydroisomerization, Appl. Catal. A, 2000, Vol. 199, 211-220.169
  • [151] LI G., HU L., HILL J.M., Comparison of reducibility and stability of alumina-supported Ni catalysts prepared by impregnation and co-precipitation, Appl. Catal. A: Gen., 2006, Vol. 301, 16-24
  • [152] LI F., YI X., FANG W., Effect of organic nickel precursor on the reduction performance and hydrogenation activity of Ni/Al203 catalysts, Catal. Lett., 2009, Vol. 130, 335-340
  • [153] LIAW S.J., LIN R., RAJE A., DAVIS B.H., Hydrotreatment of coal-derived naphtha. Properties of zeolite-supported Ru sulfide catalysts, Appl. Catal. A: Gen., 1997, Vol. 151, 423-435
  • [154] LIN S.D., VANNICE M.A., Hydrogenation of Aromatic Hydrocarbons over Supported Pt Catalysts, J. Catal., 1993, Vol. 143, 554-562
  • [155] LIN X., FAN Y., SHI G., LIU H., XIAOJUN B„ Coking and deactivation behavior of HZSM-5 zeolite-based FCC gasoline hydro-upgrading catalyst, Energy and Fuels, 2007, Vol. 21, 2517-2524
  • [156] LONG-XIANG T., FENG-MEI Z., LU-BIN Z., XPS study of nickel deposited on USY zeolites, React. Kinet. Catal. Lett., 1996, Vol. 57, 99-104
  • [157] LOPEZ T., BOSCH P., ASOMOZA M., GOMEZ R., Ru/Si02-impregnated and sol-gel-prepared catalysts: synthesis, characterization, and catalytic properties, J. Catal., 1992, Vol. 133, 247-259
  • [158] De LUCAS A., CANIZARES P., DURAN A., CARRERO A., Coke formation, location, nature and regeneration on dealuminatedHZSM-5 type zeolites, Appl. Catal. A:Gen., 1997, Vol. 156, 299-317
  • [159] De LUCAS A., VAL VERDE J.L., SANCHEZ P., DORADO F., RAMOS M.J., Influence of the binder on the n-octane hydroisomerization over palladium-containing zeolite catalysts, Ind. Eng. Chem. Res., 2004, Vol. 43, 8217-8225
  • [160] De LUCAS A., VAL VERDE J.L., DORADO F., ROMERO A., ASENCIO I., Influence of the ion exchanged metal (Cu, Co, Ni and Mn) on the selective catalytic reduction of NOx over mordenite andZSM-S, J. Mol. Catal. A: Chem., 2005, Vol. 225, 47-58
  • [161] De LUCAS A., RAMOS M.J., DORADO F., SANCHEZ P., VAL VERDE J.L., Influence of the Si/Al ratio in the hydroisomerization of n-octane over platinum and palladium beta zeolite-based catalysts with or without binder, Appl. Catal. A: Gen., 2005, Vol. 289, 205-213
  • [162] De LUCAS A., VAL VERDE J.L., SANCHEZ P., DORADO F., RAMOS M.J., Hydroisomerization of n-octane over platinum catalysts with or without binder, Appl. Catal. A:Gen., 2005, Vol. 282, 15-24
  • [163] LUGSTEIN A., JENTYS A., VINEK H., Hydroisomerization and cracking of n-octane and C8 isomers on Ni-conlaining zeolites, Appl. Catal. A:Gen., 1999, Vol. 176, 119-128
  • [164] MACLEOD N., FRYER J.R., STIRLING D., WEBB G., Deactivation of bi- and multimetallic reforming catalysts: influence of alloy formation on catalyst activity, Catal. Today, 1998, Vol. 46, 37-54
  • [165] MAGNOUX P., CARTRAUD P., MIGNARD S., GUISNET M., Coking, aging, and regeneration of zeolites: III. Comparison of the deactivation modes of H-mordenite, HZSM-5, and HY during n-heptane cracking, J. Catal., 1987, Vol. 106, 242-250
  • [166] MAGNOUX P., CANAFF C, MACHADO F., GUISNET M., Coking, aging, and regeneration of zeolites XIII: Composition of the carbonaceous compounds responsible for the deactivation of a USHY zeolite during toluene disproportionation, J. Catal., 1992, Vol. 134, 286-298
  • [167] MARAFI M., STANISLAUS A., Influence of catalyst acidity and feedstock quality on hydrotreating catalyst deactivation by coke deposition, Petroleum Science and Technology, 2001, Vol. 19, 697-710
  • [168] MARÉCOT P., AKHACHANE A., MICHEAUD C, BARBIER J., Deactivation by coking of supported palladium catalysts. Effect of time and temperature, Appl. Catal. A: Gen., 1998, Vol. 169, 189-196
  • [169] MAROTO-VALIENTE A., CERRO-ALARCÔN M., GUERRERO-RUIZ A., RODRIGUEZ-RAMOS I., Effect of the metal precursor on the surface site distribution of Al203-supported Ru catalysts: catalytic effects on the n-butane/H2 test, Appl. Catal. A: Gen., 2005, Vol. 283, 23-32.
  • [170] MARTENS J.A., JACOBS P.A., WEITKAMP J., Attempts to rationalize the distribution of hydrocracked products. II. Relative rates of primary hydrocracking modes of long chain paraffins in open zeolites, Appl. Catal., 1986, Vol. 20, 283-303.
  • [171] MARTENS J.A., JACOBS P.A., WEITKAMP J., Attempts to rationalize the distribution of hydrocracked products. I. Qualitative description of the primaty hydrocracking modes of long chain paraffins in open zeolites, Appl. Catal., 1986, Vol. 20, 239-281.
  • [172] MARTENS J.A., TIELEN M., JACOBS P.A., Attempts to rationalize the distribution of hydrocracked products. III. Mechanistic aspects of isomerization and hydrocracking of branched alkanes on ideal bifunctional large-pore zeolite catalysts, Catal. Today, 1987, Vol. 1, 435-453.
  • [173] MARTIN N., VINIEGRA M., LIMA E., ESPINOSA G„ Coke characterization on Pt/Al2O3-β-zeolite reforming catalysts, Ind. Eng. Chem. Res., 2004, Vol. 43, 1206-1210.
  • [174] MARTINS A., SILVA J.M., BLANCHARD J., MASSIANI P., BREYSSE M., RIBEIRO F.R., RIBEIRO M.F., Transformation of n-hexane on PtAl/MCM-41 and PtAl/SBA-15, React. Kinet. Catal. Lett., 2004, Vol. 82, 139-147.
  • [175] MASALSKA A., GRZECHOWIAK R.J., Effect of acidic properties of ZSM-5 containing catalysts on craking of n-hexane, Proc. 7th Int. Sym. Heterogeneous Catalysts, Burgas, Bulgarian 1991, part 1,319-324.
  • [176] MASALSKA A., GRZECHOWIAK R.J., Coke deposits on Ni,H-ZSM-5 containing catalysts, Proc. 36th Int. Conf. Petrol., Bratislava, Slovakia, 1993, 263-270.
  • [177] MASALSKA A., GRZECHOWIAK R.J., Deactivation studies on Ni,H-ZSM-5 containing catalysts. 1. Effect of chemical composition, Stud. Surf. Sci. Catal., 1994, Vol. 88, 561-566.
  • [178] MASALSKA A., GRZECHOWIAK R.J., Charakteryzowanie techniką TPO depozytów węglowych osadzonych na katalizatorach, Przem. Chem., 1996, Vol. 75, nr 10, 382-384.
  • [179] MASALSKA A., Some aspects of the preparation and catalytic activity of Ni,H-ZSM-5 containing catalysts, Praca przedstawiona na EuropaCat-VI, Innsbruck, Austria, 2003.
  • [180] MASALSKA A., Preparation and properties of Ni,H-ZSM-5 containing catalysts, Scientific Papers of the Institute of Chemistry and Technology of Petroleum and Coal of the Wroclaw University of Technology, 1999, No. 56, 193-198.
  • [181] MASALSKA A., The effect of catalysts composition on the hydrocracking activity, Scientific Papers of the Institute of Chemistry and Technology of Petroleum and Coal of the Wroclaw University of Technology, 1999, No. 56, 199-204.
  • [182] MASALSKA A., Activity and stability of alumina zeolite nickel catalysts, Catal. Today, 2001, Vol. 65, 271-277.
  • [183] MASALSKA A., Ni-loaded catalyst containing ZSM-5 zeolite for toluene hydrogenation, Appl. Catal. A: Gen., 2005, Vol. 294, 260-272.
  • [184] MASALSKA A., DATKA J., Transformation of n-hexane over ZSM-5 containing catalysts, Polish J. Environ. Stud., 2005, Vol. 14, 251-254.
  • [185] MASALSKA A., The effect of ruthenium loading on the catalytic properties of alumina-zeolite-nickel catalysts, Polish J. Environ. Stud., 2005, Vol. 14, 247-250.
  • [186] MASALSKA A., Effect of Ru precursors on the activity of Ni-Ru catalysts containing zeolite ZSM-5, Praca przedstawiona na 14th ICC, Seoul, Korea, 2008. Materiały przygotowane do druku w Catal. Today.
  • [187] MASALSKA A., Activity of NiRu catalysts containing ZSM-5 zeolite in 1-MN hydrogenation and in gas oil hydrodewaxing, Mat. Konf. XV. Forum Zeolitowe, Kocierz 2008, 227-232.
  • [188] MASALSKA A., Hydrogenation of aromatic compounds during gas oil hydrodewaxing: I. Effect ofruthenium content and method of nickel catalyst preparation, Catal. Today, 2008, Vol. 137,439-445.
  • [189] MASALSKA A., Properties and activity of Al203+ZSM-5 supported Ni and NiRu catalysts in1-methylnaphthalene hydrogenation: Effect of Ni incorporation method and calcining procedure,Catal. Lett., 2009, Vol. 127, 158-166.
  • [190] MASALSKA A., Wpływ rutenu na zakoksowanie katalizatorów NiO/ZSM-5+Al2Os podczas hydrokonwersji frakcji oleju napędowego, Praca przedstawiona na VI Kongresie Technologii Chemicznej, Warszawa 2009, Materiały przygotowane do druku w czasopiśmie Przemysł Chemiczny
  • [191] MASALSKA A., Carbonaceous deposits on ZSM-5 containing catalysts. Effect of metal and acid function, Polish J. Environ. Stud., 2009, Vol. 18, 129 134
  • [192] MASALSKA A., Effect of metal content on the activity and selectivity of ZSM-5 containing catalyst in n-hexane hydroconversion, Polish J. Environ. Stud., 2009, Vol. 18, 135-140
  • [193] MATSUSHITA K, HAUSER A., MARAFI A., KOIDE R„ STANISLAUS A., Initial coke deposition on hydrotreating catalysts. Part 1. Changes in coke properties as a function of time on stream, Fuel, 2004, Vol. 83, 1031-1038
  • [194] MAZZIERI V., COLOMA-PASCUAL F., ARCOYA A., L'ARGENTIÉRE P.C., FIGOLI N.S., XPS, FTIR and TPR characterization ofRu/Al203 catalysts, Appl. Surf. Sci., 2003, Vol. 210, 222-230
  • [195] MAZZIERI V.A., PIECK C.L., VERA C.R., YORI J.C., GRAU J.M., Analysis of coke deposition and study of the variables of regeneration and rejuvenation of naphtha reforming trimetallic catalysts, Catal. Today, 2008, Vol. 133-135, 870-878
  • [196] MICHIELS P., DE HERDT O.C.E., Molecular Sieve Catalysts, European Patent Office, Pergamon Press, 1987
  • [197] MILONE C, NERI G., DONATO A„ MUSOLINO M.G., MERCADANTE L., Selective hydrogénation of benzene to cyclohexene on Ru/y-Al203, J. Catal., 1996, Vol. 159, 253-258
  • [198] MINCHEV C, ZUBKOV S.A., VALTCHEV V., MINKOV V., MICHEVA N., KANAZIREV V., Nature of the active sites and catalytic activity of SAPO-5 synthesized in the presence of nickel cations, Appl. Catal. A: Gen., 1994, Vol. 119, 195-204
  • [199] MOLJORD K., MAGNOUX P., GUISNET M., Coking, aging and regeneration of zeolites. XV. Influence of the composition of HY zeolites on the mode of formation of coke from propene at 450 °C, Appl. Catal. A: Gen., 1995, Vol. 122, 21-32
  • [200] MOLJORD K., MAGNOUX P., GUISNET M., Coking, aging and regeneration of zeolites. XVI. Influence of the composition of HY zeolites on the removal of coke through oxidative treatment, Appl. Catal., 1995, Vol. 121, 245-259
  • [201] MONTEIRO-GEZORK A.C., EFFENDI A., WINTERBOTTOM J.M., Hydrogénation of naphthalene on NiMo- and Ni/Al203 catalysts: Pre-treatment and deactivation, Catal. Today, 2007, Vol. 128, 63-73
  • [202] MONTEIRO-GEZORK A.C., NATIVIDAD R., WINTERBOTTOM J.M., Hydrogenation of naphthalene on NiMo- Ni- and Ru/Al203 catalysts: Langmuir-Hinshelwood kinetic modelling, Catal. Today, 2008, Vol. 130, 471-485
  • [203] MORI N., NISHIYAMA S., TSURUYA S., MASAI M., Deactivation of zeolites in n-hexane conversion, Appl. Catal., 1991, Vol. 74, 37-52
  • [204] NAGAI M., KOIZUMI K, OMI S., NH3-TPD and XPS studies of Ru/Al203 catalyst and HDS activity, Catal. Today, 1997, Vol. 35, 393-405
  • [205] NAWDALI M., BIANCHI D., The impact of the Ru precursor on the adsorption of CO on Ru/Al203: amount and reactivity of the adsorbed species, Appl. Catal. A: Gen., 2002, Vol. 231, 45-54
  • [206] NIU F., HOFMANN H., Activity and deactivation behavior of various zeolite catalysts, Appl.Catal. A., 1995, Vol. 128, 107-118.
  • [207] NOMURA M., AKAGI K, MURATA S., MATSUI H., Hydrocracking of polycyclic aromaticscompounds using zeolite catalysts: Explanation of product distribution based on a computer aidedmolecular design study on the interaction of zeolite and substrates, Catal. Today, 1996, Vol. 29,235-240.172
  • [208] NOWOSIELSKA M., JOZWIAK W.K., RYNKOWSKI J., Physicochemical characterization of Al203 supported Ni-Rh systems and their catalytic performance in CHJC02 reforming, Catal. Lett., 2009, Vol. 128, 83-93
  • [209] O'REAR D.J., LOK B.K., Kinetics of dewaxing neutral oils over ZSM-5, Ind. Eng. Chem. Res., 1991, Vol. 30, 1100-1105
  • [210] OKAMOTO Y., ARIMA Y., NAKAI K., UMENO S., KATADA N„ YOSHIDA H., TANAKA T„ YAMADA M., AKAI Y., SEGAWA K., NISHIJIMA A., MATSUMOTO H., NIWA M., UCHIJIMA T., A study on the preparation of supported metal oxide catalysts using JRC-reference catalysts. I. Preparation of a molybdena-alumina catalyst. Part 1. Surface area of alumina, Appl. Catal. A: Gen., 1998, Vol. 170, 315-328
  • [211] OKAMOTO Y., ARIMA Y., HAGIO M., NAKAI K., UMENO S., AKAI Y., UCHIKAWA K., INAMURA K., USHIKUBO T., KATADA N., HASEGAWA S., YOSHIDA H., TANAKA T., ISODA T., MOCHIDA I., SEGAWA K., NISHIJIMA A., YAMADA M., MATSUMOTO H., NIWA M., UCHIJIMA T., A study on the preparation of supported metal oxide catalysts using JRC-reference catalysts. I. Preparation of a molybdena-alumina catalyst. Part 2. Volume of an impregnation solution, Appl. Catal. A: Gen., 1998, Vol. 170, 329-342
  • [212] OKAMOTO Y., UMENO S., ARIMA Y., NAKAI K., TAKAHASHI T., UCHIKAWA K„ INAMURA K., AKAI Y., CHIYODA O., KATADA N., SHISHIDO T„ HATTORI H., HASEGAWA S., YOSHIDA H., SEGAWA K., KOIZUMI N„ YAMADA M., NISHIJIMA A., KABE T., ISHIHARA A., ISODA T., MOCHIDA I., MATSUMOTO H., NIWA M., UCHIJIMA T., A study on the preparation of supported metal oxide catalysts using JRC-reference catalysts. I. Preparation of a molybdena-alumina catalyst. Part 3. Drying process, Appl. Catal. A: Gen., 1998, Vol. 170, 343-357
  • [213] OKAMOTO Y., UMENO S., SHIRAKI Y., ARIMA Y., NAKAI K., CHIYODA O, YOSHIDA H., UCHIKAWA K., INAMURA K., AKAI Y., HASEGAWA S., SHISHIDO T., HATTORI H., KATADA N., SEGAWA K, KOIZUMI N„ YAMADA M., MOCHIDA I., ISHIHARA A., KABE T., NISHIJIMA A., MATSUMOTO H., NIWA M., UCHIJIMA T., A study on the preparation of supported metal oxide catalysts using JRC-reference catalysts. I. Preparation of a molybdena-alumina catalyst. Part 4. Preparation parameters and impact index, Appl. Catal. A: Gen., 1998, Vol. 170, 359-379
  • [214] PARERA J.M., FIGOLI N.S., TRAFFANO E.M., Catalytic action of platinum on coke burning,J. Catal. 1983, Vol. 79, 481-484.
  • [215] PARERA J.M., QUERINI C.A., FIGOLI N.S., Deactivation of the Pt-Re/Al203 catalytic functionsduring a commercial cycle, Appl. Catal., 1988, Vol. 44, 1-8.
  • [216] PARK K, IHM S., Comparison of Pt/zeolite catalysts for n-hexadecane hydroizomerization, Appl.Catal. A: Gen., 2000, Vol. 203, 201-209.
  • [217] PAWEEWAN B., BARRIE P.J., GLADDEN L.F., Coking during ethene conversion on ultrastable zeolite Y, Appl. Catal. A: Gen., 1998, Vol. 167, 353-362.
  • [218] PAWEEWAN B., BARRIE P.J., GLADDEN L.F., Coking and deactivation during n-hexane cracking in ultrastable zeolite Y, Appl. Catal. A: Gen., 1999, Vol. 185, 259-268.
  • [219] PAWELEC B., MARISCAL R., NAVARRO R.M., van BOKHORST S., ROJAS S., FIERROJ.L.G., Hydrogenation of aromatics over supported Pt-Pd catalysts, Appl. Catal. A: Gen., 2002,Vol. 225, 223-237
  • [220] PAWELEC B., MARISCAL R., NAVARRO R.M., CAMPOS-MARTIN J.M., FERRO J.L.G., Simultaneous l-pentene hydroisomerisation and thiophene hydrodesulphurisation over sulphided Ni/FAUandNi/ZSM-5 catalysts, Appl. Catal. A: Gen., 2004, Vol. 262, 155-166
  • [221] PAWELEC B., CASTANO P., ARANDES J.M., BILBAO J., THOMAS S., PENA M.A., FIERRO J.L.G., Factors influencing the thioresistance of nickel catalysts in aromatics hydrogenation, Appl. Catal. A: Gen., 2007, Vol. 317, 20-33173
  • [222] PEREGO C, VILLA P., Catalyst preparation methods, Catal. Today, 1997, Vol. 34, 281-305
  • [223] PETTI T.F., TOMCZAK D., PEREIRA C.J., CHENG W.C., Investigation of nickel species on commercial FCC equilibrium catalysts-implications on catalyst performance and laboratory evaluation, Appl. Catal. A: Gen., 1998, Vol. 169, 95-109
  • [224] PIECK C.L., JABLONSKI E.L., PARERA J.M., Recovering of the catalytic functions of naphtha reforming catalysts by partial coke burning, Appl. Catal., 1991, Vol. 70, 19-28
  • [225] PIECK C.L., MARECOT P., PARERA J.M., BARBIER J., Influence of chlorine content on Pt-Re interaction and coke deposition, Appl. Catal. A: Gen., 1995, Vol. 126, 153-163
  • [226] PIECK C.L, VERA C.R., QUERINI C.A., PARERA J.M., Differences in coke burning-offfrom Pt-Sn/Al203 catalyst with oxygen or ozone, Appl. Catal. A: Gen., 2005, Vol. 278, 173-180
  • [227] PINNA F., Supported metal catalysts preparation, Catal. Today, 1998, Vol. 41, 129-137
  • [228] PRASERTHDAM P., ISARANGURA N.A., AYUTTHAYA S., Roles of NO and 02 on coke deposition and removal over Cu-ZSM-5, Catal. Today, 2004, Vol. 97, 137-143
  • [229] PREDA R., PARVULESCU V.I., PETRIDE A., BANCIU A., POPESCU A., BANCIU M.D., Hydrogenolysis of l,1a,6,10b-tetrahydro-l,6-methano-dibenzo[a,e]cyclopropa[c] cycloheptene over Ru-zeolites, J. Mol. Catal. A: Chem., 2002, Vol. 178, 79-87
  • [230] PSARO R., RECCHIA S., Supported metals derived from organometallics, Catal. Today, 1998, Vol. 139-147
  • [231] QUERINI C.A., FIGOLI N.S., PARERA J.M., Hydrocarbons reforming on Pt-Re-S/Al203-C lcoked in a commercial reactor, Appl. Catal., 1989, Vol. 52, 249-262.
  • [232] QUERINI C.A., FUNG S.C., Temperature-programmed oxidation technique: kinetics of coke-02 reaction on supported metal catalysts, Appl. Catal. A, 1994, Vol. 117, 53-74.
  • [233] QUERINI C.A., FUNG S.C., Coke characterization by temperature programmed techniques, Catal.Today, 1997, Vol. 37, 277-283.
  • [234] RADWAN A.M., KYOTANI T., TOMITA A., Characterization of coke deposited from cracking of benzene over USY zeolite catalyst, Appl. Catal. A: Gen., 2000, Vol. 192, 43-50.
  • [235] RAHAMAN M.V., VANNICE M.A., The hydrogenation of toluene and o-, m-, and p-xylene over palladium, J. Catal., 1991, Vol. 127, 267-275.
  • [236] Di RENZO F., Zeolites as tailor-made catalysts: Control of the crystal size, Catal. Today, 1998,Vol. 41, 37-40
  • [237] DE LOS REYES J.A., VRINAT M., GEANTET C, BREYSSE M., Ruthenium sulphide catalyst ssupported on alumina: physicochemical characterization and catalytic properties in hydrotreating reactions, Catal. Today, 1991, Vol. 10, 645-664.
  • [238] REYES P., KONIG M.E., PECCHI G., CONCHA I., LOPEZ-GRANADOS M., FIERRO J.L.G.,o-Xylene hydrogenation on supported ruthenium catalysts, Catal. Lett., 1997, Vol. 46, 71-75.
  • [239] REYMOND J.P., KOLENDA F., Estimation of the point of zero charge of simple and mixed oxidesby mass titration, Powder Technology, 1999, Vol. 103, 30-36.
  • [240] REYNIERS M.-F., BEIRNAERT H., MARIN G.B., Influence of coke formation on the conversion of hydrocarbons: I. Alkanes on a USY-zeoIite, Appl. Catal. A: Gen., 2000, Vol. 202, 49-63.
  • [241] REYNOLDS J.G., Nickel in Petroleum Refining, Petroleum Science and Technology, 2001, Vol.19, 979-1009
  • [242] RHODES A.K., Refinery operating variables key to enhanced lube oil quality, Oil and Gas J.,1993, Vol. 91, No 1,45-51.
  • [243] RHODES A.K., New lubes plants use state-of-the-art hydrodewaxing technology, Oil and Gas J.,1997, Vol. 95, No 35, 63-67.
  • [244] RIBEIRO F.R., ALVAREZ F.A., HENRIQUES C, LEMOS F., LOPEZ J.N., RIBEIRO M.F.,Structure-activity relationship in zeolites, J. Mol. Catal. A: Chem., 1995, Vol. 96, 245-270.
  • [245] RICHARDSON J.T., TWIGG M.V., Reduction of impregnated NiO/a-AI203 association of AI3+ ions with NiO, Appl. Catal. A: Gen., 1998, Vol. 167, 57-64
  • [246] RINGELHAN C, BURGFELS G., NEUMAYR J.G., SEUFFERT W., KLOSE J., KURTH V., Conversion of naphthenes to a high value steamcracker feedstock using H-ZSM-5 based catalysts in the second step of theARINO 1-process, Catal. Today, 2004, Vol. 97, 277-282
  • [247] RODRÍGUEZ J.C., ROMEO E„ FIERRO J.L.G., SANTAMARÍA J., Deactivation by coking and poisoning of spinel-type Ni catalysts, Catal. Today, 1997, Vol. 37, 255-265
  • [248] ROMBI E., MONACI R., SOLINAS V., Kinetics of catalyst deactivation. An example: methyl-naphthalene transformation, Catal. Today, 1999, Vol. 52, 321-330
  • [249] ROMERO M., LUKAS D.A., CALLES J.A., RODRIGUEZ A., Bifunctional catalyst Ni/HZSM-5: effects of the nickel incorporation method, Appl. Catal. A: Gen., 1996, Vol. 146, 425-441
  • [250] ROSSETTI I., FORNI L., Effect of Ru loading and of Ru precursor in Ru/C catalysts for ammonia synthesis, Appl. Catal. A: Gen., 2005, Vol. 282, 315-320
  • [251] ROUND C.I., WILLIAMS CD., LATHAM K, DUKE C.V.A., Thermogravimetric evidence of nickel or copper isomorphously substituted into a zeolite, J. Therm. Anal. Calorim., 2001, Vol. 63, 329-338
  • [252] RYNKOWSKI J.M., PARYJCZAK T., LENNIK M., On the nature of oxidic nickel phases in NiO/y-Al203 catalysts, Appl. Catal. A: Gen., 1993, Vol. 106, 73-82
  • [253] RYNKOWSKI J.M., PARYJCZAK T., LENNIK M., FARBOTKO M., GÓRALSKI J., Temperature-programmed reduction of alumina-supported Ni-Pt systems, J. Chem. Soc. Faraday Trans., 1995, Vol. 91,3481-3484
  • [254] RYNKOWSKI J.M., PARYJCZAK T., LENNIK M., Characterization of alumina supported nickel-ruthenium systems, Appl. Catal. A: Gen., 1995, Vol. 126, 257-271
  • [255] SALAGRE P., FIERRO J.L.G., MEDINA F., SUBIRAS J.E., Characterization of nickel species on several y-alumina supported nickel samples, J. Mol. Catal. A: Chem., 1996, Vol. 106, 125-134
  • [256] SANCHEZ P., DORADO F., RAMOS M.J., ROMERO R., JIMENEZ V., VALVERDE J.L., Hydroisomerization of C6-C8 n-alkanes, cyclohexane and benzene over palladium and platinum beta catalysts agglomerated with bentonite, Appl. Catal. A: Gen., 2006, Vol. 314, 248-255
  • [257] SAWA P.G., GOUNDANI K, VAKROS J., BOURIKAS K, FOUNTZOULA CH., VATTIS D„ LYCOURGHIOTIS A., KORDULIS CH., Benzene hydrogenation over Ni/Al203 catalysts prepared by conventional and sol-gel technique, Appl. Catal. B: Environ., 2008, Vol. 79, 199-207
  • [258] SCHERZER J., GRUIA A.J., Hydrocracking Science and Technology, Marcel Dekker, INC., New York, 1996, Chapter 6, 223
  • [259] SCHREIER M., REGALBUTO J.R., A fundamental study of Pt tetraammine impregnation of silica: 1. The electrostatic nature of platinum adsorption, J. Catal., 2004, Vol. 225, 190-202
  • [260] SCOTT CE., ROMERO T., LEPORE E., ARRUEBARRENA M., BETANCOURT P., BOLIVAR C, PEREZ-ZURITA M.J., MARCANO P., GOLDWASSER J., Interaction between ruthenium and molybdenum in RuMo/Al203 catalysts, Appl. Catal. A: Gen., 1995, Vol. 125, 71-79
  • [261] SEPÚLVEDA J., FÍGOLI N.S., Ni/Si02 catalysts, effect of Ni reduction on activity and thitolerance during ethylbenzene hydrogenation, React. Kinet. Catal. Lett., 1995, Vol. 55, 383-389
  • [262] SEXTON B.A., HUGNES A.E., BIBBY D.M., An XPS study of coke distribution on ZSM-5, J. Catal., 1988, Vol. 109, 126-131
  • [263] SHAMSI A., BALTRUS J.P., SPIVEY J.J., Characterization of coke deposited on Pt/alumina catalyst during reforming of liquid hydrocarbons, Appl. Catal. A, 2005, Vol. 293, 145-152
  • [264] SHEN S.C KAWI, S. MCM-41 with improved hydrothermal stability: Formation and prevention of Al content dependent structural defects, Langmuir, 2002, Vol. 18, 4720-4728
  • [265] SHIHABI D., GARWOOD W.E., CHU P., MIALE J.N., LAGO R.M., CHU CT.-W., CHANG CD., Aluminum insertion into high-silica zeolite framework. II. Binder activation of high-silica ZSM-5, J. Catal, 1985, Vol. 93, 471-474.175
  • [266] SIVASANKER S., RAMASWAMY A.V., RATNASAMY P., Design of catalyst and process for the dewaxing of petroleum oils, Appl. Catal. A: Gen., 1996, Vol. 138, 369-379
  • [267] SKRĘT I., Charakterystyka nowych komponentów oleju napędowego z procesu hydrokrakingu destylatów próżniowych, Bulletin of Institute of Petroleum Processing (ISSN 1233-3867), 2000, XII/4, 296-302
  • [268] SMITH K.W., STARR W.C., CHEN N.Y., New process dewaxes lube base stocks, Oil and Gas J., 1980, Vol. 79, 75-84
  • [269] SMITH F.A., BORTZ R.W., Applications vary for dewaxing process over 10-year spon, Oil and Gas J., 1990, Vol. 88,51-55
  • [270] SNAPE CE., MC GHEE B.J., MARTIN S.C., ANDRESEN J.M., Structural characterisation of catalytic coke by solid-state ,3C-NMR spectroscopy, Catal. Today, 1997, Vol. 37, 285-293
  • [271] SONG C, SCHMITZ A.D., Zeolite-supported Pd and Pt catalysts for low-temperature hydrogenation of naphthalene in the absence and presence of benzothiophene, Energy and Fuels, 1997, Vol. 11,656-661
  • [272] SONG C, MA H, New design approaches to ultra-clean diesel fuels by deep desulfurization and deep dearomatization, Appl. Catal. B: Environ, 2003, Vol. 41, 207-238
  • [273] SOUALAH A., LEMBERTON J.L., PINARD L., CHATER M., MAGNOUX P., MOLJORD K, Hydroisomerization of long-chain n-alkanes on bifunctional Pt/zeolite catalysts: Effect of the zeolite structure on the product selectivity and on the reaction mechanism, Appl. Catal. A: Gen., 2008, Vol. 336, 23-28
  • [274] SRIHIRANPULLOP S., PRASERTHDAM P., A new approach of coke characterization on metal and support for Pt/Al203 by combination of Al203 and Pt/Si02, Catal. Today, 2004, Vol. 93-95, 723-727
  • [275] STANISLAUS A., COOPER B.H., Aromatic Hydrogenation Catalysis: A Review, Catal. Rev. Sci. Eng., 1994, Vol.36, 75-123
  • [276] STEPANOV V.G., PAUKSHTIS E.A., CHESNOKOV V.V., IONE K.G., Mechanism of coking and regeneration of catalysts containing ZSM-5 zeolite, Proc. 12th ICC Granada, Spain, July 9-14, 2000, Vol. 130,2969-2974
  • [277] TAYLOR R.J., MC CORNACK A.J., Study of solvent and catalytic lube oil dewaxing by analysis of feedstocks andproducts, Ind. Eng. Chem. Res., 1992, Vol. 31, 1731-1738
  • [278] THYBAUT J.W., NARASIMHAN C.S.L., DENAYER J.F., BARON G.V., JACOBS P.A., MARTENS J.A., MARIN G.B., Acid-metal balance of a hydrocracking catalyst: Ideal versus nonideal behavior, Ind. Eng. Chem. Res., 2005, Vol. 44, 5159-5169
  • [279] TIAN P., BLANCHARD J., FAJERWERG K, BREYSSE M., VRINAT M., LIU Z., Preparation of Ru metal nanoparticles in mesoporous materials: influence of sulfur on the hydrogenating activity, Micropor. Mesopor. Mater., 2003, Vol. 60, 197-206
  • [280] TREACY M.M.J., HIGGINS J.B., Collection of simulated XRD powder patterns for zeolites, 5th revised éd., IZA Ed., Elsevier, Amsterdam, 2007, 278-279
  • [281] TSIAO C, DYBOWSKI C, GAFFNEY A.M., SOFRANKO J.A., Coke formation on ZSM-5 zeolites: Evidence from NMR spectrometry of sorbed xenon gas, J. Catal., 1991, Vol. 128, 520-525
  • [282] TWIGG M.V., RICHARDSON J.T., Effects of alumina incorporation in coprecipitated NiO-Al203 catalysts, Appl. Catal. A: Gen., 2000, Vol. 190, 61-72
  • [283] UNGAR S., HUNTER K, LICHTSCHEIDL J., Independent pilot testing adds to the benefits of the refiner, Proc. ERTC 8th Ann. Meeting, 17-19 Nov. 2003, London
  • [284] WANG J., HUANG L., LI Q., Influence of different diluents in Pt/Al203 catalyst on the hydrogenation of benzene, toluene and o-xylene, Appl. Catal. A: Gen., 1998, Vol. 175, 191-199
  • [285] WANG J., LI Q., YAO J., The effect of metal-acid balance in Pt-loading dealuminated Y zeolite catalysts on the hydrogenation of benzene, Appl. Catal. A: Gen., 1999, Vol. 184, 181-188.
  • [286] WANG J., CHEN H., LI Q., Influence of the Brônsted and Lewis acid sites in platinum/solid acid catalysts on the hydrogenation of benzene and toluene, React. Kinet. Catal. Lett., 2000, Vol. 69, 277-284
  • [287] WANG B., MANOS G., Role of strong zeolitic acid sites on hydrocarbon reactions, Ind. Eng.Chem. Res., 2008, Vol. 47, 2948-2955.
  • [288] WEITKAMP J., Zeolites and catalysis, Solid State Ionics, 2000, Vol. 131, 175-188.
  • [289] WEITKAMP J., HUNGER M., Acid and base catalysis on zeolites, Stud. Surf. Sci. Catal., 2007,Vol. 168, 787-835
  • [290] WILLIAMS B.A., JI W., MILLER J.T., SNURR R.Q., KUNG H.H., Evidence of different reaction mechanisms during the cracking of n-hexane on H-USY, Appl. Catal. A: Gen., 2000, Vol. 203, 179-190
  • [291] World-Wide Fuel Charter, 4-th Ed., September 2006
  • [292] WU X., ALKHAWALDEH A., ANTHONY R.G., Investigation on acidity of zeolites bound with silica and alumina, Stud. Surf. Sci. Catal., 2002, Vol. 143, 217-225.
  • [293] XIANG L., GONG Y.L., LI J.C., WANG Z.W., Influence of hydrothermal modification on the properties ofNi/Al20} catalyst, Appl. Surf. Sci., 2004, Vol. 239, 94-100.
  • [294] YASHIMA T., WANG Z.B., KAMO A., YONEDA T., KOMATSU T., Isomerization of n-hexane over platinium loaded zeolite catalysts, Catal. Today, 1996, Vol. 29, 279-283.
  • [295] YASUDA H., SATO T., YOSHIMURA Y., Infuence of the acidity of USY zeolite on the sulfur tolerance ofPd-Pt catalysts for aromatic hydrogenation, Catal. Today, 1999, Vol. 50, 63-71.
  • [296] ZEUTHEN P., BARTHOLDY J.J., MASSOTH F.E., Temperature-programmed oxidation studies of aged V-containing hydroprocessing catalysts, Appl. Catal. 1995, Vol. 129, 43-55.
  • [297] ZHANG W.P., SUN M.Y., PRINS R., Multinuclear MAS NMR identification of fluorine species onthe surface of fluorinated y-alumina, J. Phys. Chem. B, 2002, Vol. 106, 11805-11809.
  • [298] ZHANG Y., ZHOU Y., QIU A., WANG Y., XU Y., WU P., Effect of alumina binder on catalytic performance of PtSnNa/ZSM-5 catalyst for propane dehydrogenation, Ind. Eng. Chem. Res., 2006,Vol. 45, 2213-2219.
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