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61. 发明专利

ZA200708237B Surface features in microprocess technology 未知
公开(公告)号：ZA200708237B
公开(公告)日：2008-05-28
申请号：ZA200708237
申请日：2007-09-19
申请人： VELOCYS INC
发明人： TONKOVICH ANNA LEE
IPC分类号： B01F20090101 , B01J20090101

62. 发明专利

ZA200706066B Fluidized bed CVD arrangement 未知
公开(公告)号：ZA200706066B
公开(公告)日：2008-05-28
申请号：ZA200706066
申请日：2007-07-23
申请人： BWX TECHNOLOGIES INC
发明人： HALFINGER JEFFREY A , RICHARDSON WILLIAM C , KEELEY JOSEPH T , NAGLEY SCOTT G , TOMLIN BRUCE L
IPC分类号： B01J20090101 , B05B20090101

63. 发明专利

ZA200610754B A process for the preparation of an olefin oxide or a chemical derivable from an olefin oxide, and a reactor suitable for such a process 未知
公开(公告)号：ZA200610754B
公开(公告)日：2008-05-28
申请号：ZA200610754
申请日：2006-12-20
申请人： SHELL INT RESEARCH
发明人： WILLEM BOLK JEROEN , RENUE BOS ALOUISIUS NICOLAAS , ERROL EVANS WAYNE , ROBERT LOCKEMEYER JOHN , MICHAEL MCALLISTER PAUL , MARIE RAMAKERS BERNARDUS FRANCISCUS JOSEF , MARIA REKERS DOMINICUS , PAUL SLAPAK MATHIAS JOZEF
IPC分类号： B01J20090101 , C07B20090101 , C07D20090101
摘要： An olefin 1,2-carbonate is reacted, in one or more process microchannels of a microchannel reactor, with water or an alcohol to form the corresponding 1,2-diol, optionally in the presence of an catalyst. The olefin 1,2-carbonate is optionally obtained by: ```firstly reacting a feed comprising an olefin and oxygen in the presence of an epoxidation catalyst contained in one or more process microchannels in a first section of the microchannel reactor; and ```secondly converting the resulting olefin oxide with carbon dioxide, optionally in the presence of an catalyst. The reaction mixture may optionally be quenched by reducing the temperature (preferably to no more than 200{C) using a heat exchange fluid downstream of the epoxidation catalyst. A microchannel reactor suitable for such a process comprises: ```one or more process microchannels (210), each comprising: ```an upstream end (220); ```a downstream end (230); ```a first section (240) which is adapted: ```to contain an epoxidation catalyst, ```to receive a feed comprising an olefin and oxygen, ```and to allow conversion of at least a portion of the feed into an olefin oxide; ```a second section (340) ```positioned downstream of the first section and adapted ```to receive the olefin oxide and carbon dioxide, and ```to allow conversion of the olefin oxide; and ```a third section ```positioned downstream of the second section and adapted ```to receive the olefin 1,2-carbonate, and water or an alcohol, and ```to allow conversion of the olefin 1,2-carbonate to the 1,2-diol. The reactor may also comprise one or more heat exchange channels (250, 350) to exchange heat with the first, second and third sections, and one or more heat exchange channels (e.g. 450) to exchange heat with intermediate sections (e.g. 440, for reaction quenching) between the first and second sections, and between the second and third sections.

64. 发明专利

ZA200610750B A method of installing an epoxidation catalyst in a reactor a process for the preparation of an olefin oxide or s chemical derivable from an olefin oxide, and a reactor suitable for such a process 未知
公开(公告)号：ZA200610750B
公开(公告)日：2008-05-28
申请号：ZA200610750
申请日：2006-12-20
申请人： SHELL INT RESEARCH
发明人： WILLEM BOLK JEROEN , ERROL EVANS WAYNE , MICHAEL MCALLISTER PAUL , MARAIA REKERS DOMINICUS , RENEE BOS ALOUISIUS NICOLAAS , ROBERT LOCKEMEYER JOHN , MARIE RAMAKERS BERNARDUS FRANCISCUS JOSEF , PAUL SLAPAK MATHIAS JOZEF
IPC分类号： B01J20090101 , C07B20090101 , C07D20090101
摘要： An olefin 1,2-carbonate is reacted, in one or more process microchannels of a microchannel reactor, with water or an alcohol to form the corresponding 1,2-diol, optionally in the presence of an catalyst. The olefin 1,2-carbonate is optionally obtained by: ```firstly reacting a feed comprising an olefin and oxygen in the presence of an epoxidation catalyst contained in one or more process microchannels in a first section of the microchannel reactor; and ```secondly converting the resulting olefin oxide with carbon dioxide, optionally in the presence of an catalyst. The reaction mixture may optionally be quenched by reducing the temperature (preferably to no more than 200{C) using a heat exchange fluid downstream of the epoxidation catalyst. A microchannel reactor suitable for such a process comprises: ```one or more process microchannels (210), each comprising: ```an upstream end (220); ```a downstream end (230); ```a first section (240) which is adapted: ```to contain an epoxidation catalyst, ```to receive a feed comprising an olefin and oxygen, ```and to allow conversion of at least a portion of the feed into an olefin oxide; ```a second section (340) ```positioned downstream of the first section and adapted ```to receive the olefin oxide and carbon dioxide, and ```to allow conversion of the olefin oxide; and ```a third section ```positioned downstream of the second section and adapted ```to receive the olefin 1,2-carbonate, and water or an alcohol, and ```to allow conversion of the olefin 1,2-carbonate to the 1,2-diol. The reactor may also comprise one or more heat exchange channels (250, 350) to exchange heat with the first, second and third sections, and one or more heat exchange channels (e.g. 450) to exchange heat with intermediate sections (e.g. 440, for reaction quenching) between the first and second sections, and between the second and third sections.

65. 发明专利

ZA200608863B Catalyst comprising a zeolite with structure type NES and a zeolite with structure type EUO, and use in isomerizing C8 aromatic compounds 未知
公开(公告)号：ZA200608863B
公开(公告)日：2008-05-28
申请号：ZA200608863
申请日：2006-10-25
申请人： INST FRANCAIS DU PETROLE
发明人： EMMANUELLE GUILLON , ERIC SANCHEZ , SYLVIE LACOMBE
IPC分类号： B01J20090101 , C01B20090101 , C07C20090101

66. 发明专利

ZA200704129B Tubular polymerization reactors and polymers made therein 未知
公开(公告)号：ZA200704129B
公开(公告)日：2008-04-30
申请号：ZA200704129
申请日：2007-05-22
申请人： EXXONMOBIL CHEM PATENTS INC
发明人： DONCK JAN C , LAMMENS HENRI A
IPC分类号： B01J20090101 , B01J19/24 , C08F20090101 , C08F2/00 , C08F10/00 , C08F10/02 , C08F110/02
摘要： Tubular reactor apparatus and processes are provided for improved polymerization including using chain transfer agents and multiple monomer feeds spaced lengthwise along the tubular reactor providing high conversions of monomer into polymer. The invention also relates to polymers made from such a tubular reactor apparatus and processes including those polymers having a low haze value, a density over 0.92 g/cm3 and/or having terminal carbonyl groups. The apparatus and methods uncouple or reduce the dependency between the monomer concentration and transfer agent concentration. The uncoupling in other embodiments may also be varied leading to multiple desirable effects.

67. 发明专利

ZA200603201B Method for the production of annular-shaped super catalysts 未知
公开(公告)号：ZA200603201B
公开(公告)日：2008-02-27
申请号：ZA200603201
申请日：2006-04-21
申请人： BASF AG
发明人： JOCHEN PETZOLDT , JOACHIM MULLER-ENGEL KLAUS , SIGNE UNVERRICHT
IPC分类号： B01J20090101 , B01J23/00 , B01J23/887 , B01J23/888 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/00 , B01J37/08 , C07C45/35 , C07C45/37 , C07C51/25
摘要： A process for the production of ring-shaped solid mixed oxide catalysts with a length of 2-11 mm, an outer diameter of 2-11 mm and a wall thickness of 0.75-1.75 mm, comprises production of a fine-particulate mixture from sources of the elementary constituents of the active mass, followed by forming to shape and thermal treatment at elevated temperature to form catalysts having a lateral compressive strength of 12-23 N. A process for the production of ring-shaped solid catalysts (I) having optionally curved faces, whose active mass is of formula (1) or (2), and having a geometry, without reference to any optional curvature of the faces, with a length of 2-11 mm, an outer diameter of 2-11 mm and a wall thickness of 0.75-1.75 mm, comprises production of a fine-particulate mixture from sources of the elementary constituents of the active mass, optionally following addition of forming and/or reinforcing agents, followed by forming of ring-shaped solid catalyst precursor molded articles having optionally curved faces and thermal treatment at elevated temperature to form the catalysts (I) having a lateral compressive strength of 12-23 N. Mo12BiaFebX1cX2dX3eX4fOn (1) (Y1a'Y2b'Ox')p(Y3c'Y4d'Y5e'Y6f'Y7g'Y2h'Oy')q (2) X1 = Ni and/or Co; X2 = Th, an alkali metal or alkaline earth metal; X3 = Zn, P, Ar, B, Sb, Sn, Ce, Pb and/or W; X4 = Si, Al, Ti and/or Zr; a = 0.2-5; b = 0.01-5; c = 0-10; d = 0-2; e = 0-8; f = 0-10; n = a number dependent upon the valency and frequency of non-oxygen elements; Y1 = Bi or Bi and Te, Sb, Sn and/or Cu; Y2 = Mo or Mo and W; Y3 = alkali metal; Th and/or Sm; Y4 = alkaline earth metal, Ni, Co, Cu, Mn, Zn, Sn, Cd and/or Hg; Y5 = Fe or Fe and V, Cr and/or Ce'; Y6 = P, Ar, B and/or Sb; Y7 = rare earth metal, Ti, Zr, Nb, Ta, Rh, Ru, Re, Ag, Au, Al, Ga, In, Si, Ge, Pb, Th and/or U; a' = 0.01-8; b' = 0.1-30; c' = 0-4; d' = 0-20; e' = greater than 0-20; f' = 0-6; g' = 0-15; h' = 8-16; x', y' = numbers dependent upon the valency and frequency of non-oxygen elements; and p/q = 0.1-10. Independent claims are also included for: (1) a solid catalyst (I) having a specific surface area of 5-23 m2/g, total pore volume of 0.1-1 cm3/g and no greater than 5 vol.% of pores of less than 0.03 microns in diameter, no greater than 25 vol.% of pores having a diameter of 0.03-0.1 microns, at least 70 vol.% of pores having a diameter of 0.1-1 microns and no greater than 10 vol.% of pores having a diameter of 1-13 microns; (2) a process for the production of acrolein and/or methacrolein by heterogeneous partial gas phase oxidation of propene, iso-butene and/or tert.-butanol in the presence of the heterogeneous solid catalyst (I).

68. 发明专利

ZA200606305B Process for turning fly ash into useful building blocks and the like 未知
公开(公告)号：ZA200606305B
公开(公告)日：2007-12-27
申请号：ZA200606305
申请日：2006-07-31
申请人： LOGGERS HENDRIK , VERSTEEG GIJSBERT
发明人： HENDRIK LOGGERS , GIJSBERT VERSTEEG
IPC分类号： B01J20090101 , C04B20090101

69. 发明专利

ZA200604817B Mixed metal oxide sorbents 未知
公开(公告)号：ZA200604817B
公开(公告)日：2007-12-27
申请号：ZA200604817
申请日：2004-11-22
申请人： INTERACT INC
发明人： VIERHEILIG ALBERT A
IPC分类号： B01D53/02 , B01D53/50 , B01D53/56 , B01D53/60 , B01D53/86 , B01D53/94 , B01J20090101 , B01J8/18 , C01B17/00 , C01B21/20 , C01B32/40 , C01F7/00 , C01F7/16 , C10G25/00
摘要： The present invention is directed to methods for reducing SOx, NOx, and CO emissions from a fluid stream comprising contacting said fluid stream with a compound comprising magnesium and aluminum and having an X-ray diffraction pattern displaying at least a reflection at a two theta peak position at about 43 degrees and about 62 degrees, wherein the ratio of magnesium to aluminum in the compound is from about 1:1 to about 10:1. In one embodiment, the ratio of magnesium to aluminum in the compound is from about 1:1 to about 6:1. In one embodiment, the ratio of magnesium to aluminum in the compound is from about 1.5:1 to about 10:1. In another embodiment, the invention is directed to methods wherein the ratio of magnesium to aluminum in the compound is from about 1.5:1 to about 6:1.

70. 发明专利

ZA200605545B Method of producing low-dust granules from polymer additives 未知
公开(公告)号：ZA200605545B
公开(公告)日：2007-11-28
申请号：ZA200605545
申请日：2006-07-05
申请人： CIBA SC HOLDING AG
发明人： BENJAMIN BREITENSTEIN , GEORG GFRORER THOMAS , ROLF WALDNER , PIERRE LUTZ
IPC分类号： B01J20090101 , B01J2/00 , B01J2/20 , B01J2/22 , B01J2/24 , C08J3/22 , C08K20090101 , C08K3/00 , C08K5/00 , C08K5/13 , C08K7/16 , C08K13/02
摘要： The invention relates to a technically advantageous method of producing low-dust granules of polymer additives or polymer additive mixtures. The granule-forming polymer additives are mixed together, the mixture is converted into a workable mass and pressed through an orifice. The pre-shaped strand-like extruded mass is cooled and, while still in a workable state, formed into granules by rolling, impressing, cooling and comminuting.

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