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1. 发明申请

WO2013105112A8 CATALYST COMPOSITE FOR DEHYDROGENATION OF HYDROCARBONS AND METHOD OF PREPARATION THEREOF 审中-公开
标题翻译：用于脱氢烃的催化复合物及其制备方法
公开(公告)号：WO2013105112A8
公开(公告)日：2014-01-03
申请号：PCT/IN2012000757
申请日：2012-11-20
申请人： RELIANCE IND LTD
发明人： LANDE SHARAD VASUDERAO , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R , UNNIKRISHNAN SREEDHARAN , SHARMA NAGESH , VAIDYA SHASHANK , DONGARA RAJESHWER , KRISHNAMURTHY RAMASWAMY KONDA
IPC分类号： B01J37/02 , B01J21/04 , B01J23/58 , B01J23/62 , B01J35/00 , B01J35/02 , B01J35/08 , B01J35/10 , B01J37/18 , C07C5/333
CPC分类号： B01J31/26 , B01J21/04 , B01J23/42 , B01J23/468 , B01J23/626 , B01J35/0013 , B01J35/002 , B01J35/006 , B01J35/008 , B01J35/023 , B01J35/08 , B01J35/1014 , B01J35/1019 , B01J37/0205 , B01J37/0207 , B01J37/16 , C07C5/325 , C07C5/3337 , C07C2521/04 , C07C2523/04 , C07C2523/14 , C07C2523/42 , C07C2523/46 , C07C2523/62 , C07C11/02
摘要： The present invention provides a dehydrogenation catalyst composite that is capable of providing a dehydrogenated hydrocarbon product characterized by a bromine number of at least 19. for hydrocarbons. The dehydrogenation catalyst of the present invention comprises a nano-sized complex containing a Group VIII component; a group IVA component and a sulfur containing capping agent; an alkali component; a halogen component; and a support with an inner core of alpha alumina and an outer layer comprising a mixture of gamma alumina and delta alumina.
摘要翻译：本发明提供一种脱氢催化剂复合材料，其能够提供特征在于烃的至少为19的溴值的脱氢烃产物。本发明的脱氢催化剂包含含有VIII族成分的纳米级复合物; IVA组分和含硫封端剂; 碱组分; 卤素组分; 以及具有α氧化铝内核和包含γ氧化铝和δ氧化铝的混合物的外层的载体。

2. 发明申请

WO2014033737A8 A DEHYDROGENATION CATALYST FOR HYDROCARBONS AND METHOD OF PREPARATION THEREOF 审中-公开
标题翻译：一种烃类脱氢催化剂及其制备方法
公开(公告)号：WO2014033737A8
公开(公告)日：2014-06-12
申请号：PCT/IN2013000435
申请日：2013-07-15
申请人： RELIANCE IND LTD
发明人： LANDE SHARAD VASUDEORAO , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R , UNNIKRISHNAN SREEDHARAN , SHARMA NAGESH , VAIDYA SHASHANK , JASRA RAKSH VIR
IPC分类号： B01J37/02 , B01J21/04 , B01J23/02 , B01J23/58 , B01J23/62 , B01J35/00 , B01J35/02 , B01J35/08 , B01J35/10 , B01J37/18 , C07C5/333 , C10G35/00
CPC分类号： B01J37/18 , B01J21/04 , B01J23/02 , B01J23/58 , B01J23/626 , B01J27/13 , B01J27/135 , B01J35/0066 , B01J35/008 , B01J35/023 , B01J35/026 , B01J35/08 , B01J35/1014 , B01J35/1019 , B01J37/0018 , B01J37/0203 , B01J37/0205 , B01J37/0223 , B01J37/0242 , B01J37/08 , C07C5/3337 , C07C2521/04 , C07C2521/10 , C07C2523/04 , C07C2523/14 , C07C2523/42 , C07C2523/62 , C07C2527/10 , C10G11/00 , C10G11/02 , C10G2400/20 , C10G2400/22 , C07C11/02
摘要： The present disclosure relates to a dehydrogenation catalyst composite comprising at least one alumina support, comprising a core of alpha alumina and at least one layer of gamma alumina, delta alumina or theta alumina, impregnated with at least one layer of at least one alkaline earth metal element and at least one layer comprising at least one catalytic metal element, at least one group VIA element and optionally, at least one halogen element. The present disclosure also relates to a process for preparation of the dehydrogenation catalyst composite.
摘要翻译：本发明涉及一种脱氢催化剂复合材料，其包含至少一种氧化铝载体，所述氧化铝载体包含α氧化铝芯和至少一层γ氧化铝，δ氧化铝或θ氧化铝，所述层由至少一层碱土金属元素和至少一个包含至少一种催化金属元素，至少一种VIA族元素和任选至少一种卤族元素的层。本公开还涉及制备脱氢催化剂复合材料的方法。

3. 发明申请

WO2010067379A3 A FLUID CATALYTIC CRACKING (FCC) PROCESS FOR MANUFACTURING PROPYLENE AND ETHYLENE IN INCREASED YIELD 审中-公开
标题翻译：流化催化裂化（FCC）在增加乙烯和乙烯中制备丙烯和乙烯的方法
公开(公告)号：WO2010067379A3
公开(公告)日：2011-03-24
申请号：PCT/IN2009000708
申请日：2009-12-08
申请人： RELIANCE IND LTD , MANDAL SUKUMAR , DAS ASIT KUMAR , YADAV ASHWANI , YADAV MANOJ , BHATNAGAR AKHILESH , DONGARA RAJESHWAR , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R
发明人： MANDAL SUKUMAR , DAS ASIT KUMAR , YADAV ASHWANI , YADAV MANOJ , BHATNAGAR AKHILESH , DONGARA RAJESHWAR , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R
IPC分类号： C10G11/05
CPC分类号： C10G11/18 , C10G11/05 , C10G2400/20
摘要： A fluid catalytic cracking (FCC) process for manufacturing propylene and ethylene in increased yield. The process comprises cracking an olefinic naphtha stream and main hydrocarbon stock in combination with an olefinic C4 hydrocarbon stream in different zones of one or more risers of an FCC unit. Each FCC riser comprises an acceleration zone at the lower portion thereof, a lift stream feed nozzle at the bottom of the acceleration zone, a main hydrocarbon stock feed nozzle above the acceleration zone and an olefinic naphtha feed nozzle at a location along the acceleration zone between the lift stream feed nozzle and main hydrocarbon stock feed nozzle. The cracking is carried out on a mixed FCC catalyst comprising atleast 2 percent by weight pentasil zeolite and at least 10 percent by weight Y- zeolite. The catalyst is injected at the bottom of each FCC riser, the olefinic naptha is injected through the olefinic feed nozzle, the main hydrocarbon stock is injected through the main hydrocarbon stock feed nozzle and the lift stream is injected through the lift stream feed nozzle at the bottom of the acceleration zone. The lift stream comprises the olefinic C4 hydrocarbon stream with or without steam and/or a fuel gas. The olefinic C4 hydrcarbon steam is cracked in the acceleration zone at 600 to 8000°C and pressure of 0.8 to 5 kg/cm up 2 (gauge) and weight hourly space velocity (WHSV) of 0.2 to 100 hr up 1 and vapour residence time of 0.2 to 5 seconds.
摘要翻译：用于以增加的产率制造丙烯和乙烯的流化催化裂化（FCC）方法。该方法包括在FCC单元的一个或多个立管的不同区域中与烯属烃石脑油流和主要烃类物料一起裂化。每个FCC提升管包括其下部的加速区，加速区底部的升力流进料喷嘴，加速区上方的主烃储料供给喷嘴和沿加速区的位置处的烯烃石脑油进料喷嘴，升降机进料喷嘴和主油料进料喷嘴。裂化在含至少2重量百分比的pentasil沸石和至少10重量％Y-沸石的混合FCC催化剂上进行。在每个FCC提升管的底部注入催化剂，通过烯烃进料喷嘴注入烯烃萘，主要烃类原料通过主要烃类原料进料喷嘴注入，提升流通过提升料流进料喷嘴注入底部的加速区。提升流包括具有或不具有蒸汽和/或燃料气体的烯烃C4烃流。烯烃C4碳氢化合物蒸汽在加速区600〜8000℃，压力0.8〜5kg / cm 2（表压），重时空速（WHSV）为0.2〜100小时-1，蒸汽停留时间为0.2〜5秒。

4. 发明申请

WO2015128823A3 A PROCESS FOR PREPARING A CATALYST 审中-公开
标题翻译：制备催化剂的方法
公开(公告)号：WO2015128823A3
公开(公告)日：2016-01-07
申请号：PCT/IB2015051423
申请日：2015-02-26
申请人： RELIANCE IND LTD
发明人： SHARMA NAGESH , KUMAR AJAY , METTU ANILKUMAR , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R , GOPALAKRISHNAN KALPANA , JASRA RAKSH VIR
IPC分类号： B01J29/06 , B01J21/04 , B01J37/00
CPC分类号： B01J29/068 , B01J29/072 , B01J29/076 , B01J29/084 , B01J29/18 , B01J29/40 , B01J29/42 , B01J29/44 , B01J29/48 , B01J29/7007 , B01J29/7034 , B01J29/7038 , B01J35/023 , B01J37/0236 , B01J37/0242 , B01J37/0246 , B01J37/06 , B01J37/08 , B01J2229/186 , B01J2229/64 , C10G35/09 , C10G35/095
摘要： The present disclosure relates to a process for preparing a catalyst. The process comprises coating zeolite gel over the alumina support to obtain a chloride free zeolite gel coated alumina support, crystallizing the chloride free zeolite gel coated alumina support, washing, drying and calcining the crystallized zeolite coated alumina support to obtain a calcined crystallized chloride free zeolite coated alumina support, treating the calcined crystallized chloride free zeolite coated alumina support with ammonium nitrate to obtain sodium free support, washing, drying, and calcining the support to obtain a calcined chloride free zeolite coated alumina support, immersing the calcined chloride free zeolite coated alumina support in an active metal and a promoter metal solution mixture followed by stirring to obtain a metal coated chloride free zeolite coated alumina support, and drying and calcining the metal coated chloride free zeolite coated alumina support to obtain the catalyst.
摘要翻译：本发明涉及制备催化剂的方法。该方法包括在氧化铝载体上涂布沸石凝胶以获得无氯化物的沸石凝胶涂覆的氧化铝载体，结晶无氯化物的沸石凝胶涂覆的氧化铝载体，洗涤，干燥和煅烧结晶的沸石涂覆的氧化铝载体以获得煅烧的无结晶氯化物的沸石涂覆氧化铝载体，用硝酸铵处理煅烧的无结晶氯化物的沸石涂层的氧化铝载体以获得无钠载体，洗涤，干燥和煅烧载体以获得无煅烧氯化物的沸石涂覆的氧化铝载体，将煅烧过的无氯化物的沸石涂覆的氧化铝支持活性金属和助催化剂金属溶液混合物，随后搅拌，得到金属涂覆的无氯化物沸石涂层氧化铝载体，并干燥和煅烧金属涂覆的无氯化物的沸石涂层氧化铝载体以获得催化剂。

5. 发明申请

WO2010067379A8 A FLUID CATALYTIC CRACKING (FCC) PROCESS FOR MANUFACTURING PROPYLENE AND ETHYLENE IN INCREASED YIELD 审中-公开
标题翻译：流化催化裂化（FCC）在增加乙烯和乙烯中制备丙烯和乙烯的方法
公开(公告)号：WO2010067379A8
公开(公告)日：2010-09-10
申请号：PCT/IN2009000708
申请日：2009-12-08
申请人： RELIANCE IND LTD , MANDAL SUKUMAR , DAS ASIT KUMAR , YADAV ASHWANI , YADAV MANOJ , BHATNAGAR AKHILESH , DONGARA RAJESHWAR , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R
发明人： MANDAL SUKUMAR , DAS ASIT KUMAR , YADAV ASHWANI , YADAV MANOJ , BHATNAGAR AKHILESH , DONGARA RAJESHWAR , KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA R
CPC分类号： C10G11/18 , C10G11/05 , C10G2400/20
摘要： A fluid catalytic cracking (FCC) process for manufacturing propylene and ethylene in increased yield. The process comprises cracking an olefinic naphtha stream and main hydrocarbon stock in combination with an olefinic C4 hydrocarbon stream in different zones of one or more risers of an FCC unit. Each FCC riser comprises an acceleration zone at the lower portion thereof, a lift stream feed nozzle at the bottom of the acceleration zone, a main hydrocarbon stock feed nozzle above the acceleration zone and an olefinic naphtha feed nozzle at a location along the acceleration zone between the lift stream feed nozzle and main hydrocarbon stock feed nozzle. The cracking is carried out on a mixed FCC catalyst comprising atleast 2 percent by weight pentasil zeolite and at least 10 percent by weight Y- zeolite. The catalyst is injected at the bottom of each FCC riser, the olefinic naptha is injected through the olefinic feed nozzle, the main hydrocarbon stock is injected through the main hydrocarbon stock feed nozzle and the lift stream is injected through the lift stream feed nozzle at the bottom of the acceleration zone. The lift stream comprises the olefinic C4 hydrocarbon stream with or without steam and/or a fuel gas. The olefinic C4 hydrcarbon steam is cracked in the acceleration zone at 600 to 8000°C and pressure of 0.8 to 5 kg/cm up 2 (gauge) and weight hourly space velocity (WHSV) of 0.2 to 100 hr up 1 and vapour residence time of 0.2 to 5 seconds.
摘要翻译：用于以增加的产率制造丙烯和乙烯的流化催化裂化（FCC）方法。该方法包括在FCC单元的一个或多个立管的不同区域中与烯属烃石脑油流和主要烃类物料一起裂化。每个FCC提升管包括其下部的加速区，加速区底部的升力流进料喷嘴，加速区上方的主烃储料供给喷嘴和沿加速区的位置处的烯烃石脑油进料喷嘴，升降机进料喷嘴和主油料进料喷嘴。裂化在含至少2重量百分比的pentasil沸石和至少10重量％Y-沸石的混合FCC催化剂上进行。在每个FCC提升管的底部注入催化剂，通过烯烃进料喷嘴注入烯烃萘，主要烃类原料通过主要烃类原料进料喷嘴注入，提升流通过提升料流进料喷嘴注入底部的加速区。提升流包括具有或不具有蒸汽和/或燃料气体的烯烃C4烃流。烯烃C4碳氢化合物蒸汽在加速区600〜8000℃，压力0.8〜5kg / cm 2（表压），重时空速（WHSV）0.2〜100小时-1，蒸气停留时间为0.2〜5秒。

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