公开(公告)号：EP2954033A4

公开(公告)日：2017-02-15

申请号：EP13874434

申请日：2013-12-18

Applicant: RELIANCE IND LTD

Inventor： DAGGUPATI SATEESH ,  MANDAL SUKUMAR ,  DAS ASIT KUMAR ,  SAPRE AJIT VISHWANATH

IPC: C10L3/08 ,  B01J23/04 ,  B01J27/232 ,  B01J27/25 ,  B01J29/08 ,  B01J29/40 ,  B01J37/02 ,  C10J3/46 ,  C10K3/02

CPC classification number: C10J3/466 ,  B01J23/04 ,  B01J27/232 ,  B01J27/25 ,  B01J29/084 ,  B01J29/40 ,  B01J37/0201 ,  C10J3/463 ,  C10J2300/0943 ,  C10J2300/0976 ,  C10J2300/0986 ,  C10J2300/1246 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10J2300/1853 ,  Y02P20/52 ,  Y02P20/584

Abstract: An improved process for the catalytic gasification of a carbonaceous feedstock in a dual fluidized bed reactor for producing synthesis gas is disclosed. The disclosure uses γ-alumina as a catalyst support i and heat carrier in the gasification zone (102). The gasification zone (102) is operated at 700-750° C. to prevent substantial conversion of γ-alumina to α-alumina, which would manifest in the enablement of high catalyst loading and high recyclability. The catalyst is an alkali metal, preferably K2CO3, so that conversion proportional to total K2CO3 to solid carbon ratio is achieved with as high K2CO3 loading as 50 wt % on the solid support. The combustion zone (140) is operated at 800°-840° C., to prevent any conversion of the γ-alumina to α-alumina, so that catalyst recyclability of up to 98% is achieved between two successive cycles.

公开(公告)号：EP3116853A4

公开(公告)日：2017-11-15

申请号：EP15761919

申请日：2015-03-13

Applicant: RELIANCE IND LTD

Inventor： SHOWN BISWAJIT ,  MURTHY NAGARATHINAM SHENBAGA ,  DAS ASIT KUMAR ,  GHOSH SWAPAN ,  DAS BIDHAYAK ,  DONGARA RAJESHWER ,  RAY ANIRBAN ,  PANSERIYA CHIRAG DALPATBHAI ,  SIVATHANU RAMALAKSHMI UDAYAN ,  KATHIRIA ATUL

IPC: C07C319/30 ,  C07C321/14

CPC classification number: C07C319/30 ,  C07C321/04 ,  C07C321/14

Abstract: In the present disclosure there is provided a process for obtaining di-sulfide oil having sodium level below 0.1 ppm wherein a stream comprising di-sulfide oil having sodium level 1 ppm, collected as a waste stream from LPG desulfurization unit, is passed through an alumina bed packed in a column at a pre-determined liquid hourly space velocity (LHSV) and at pre-determined temperature to obtain a treated stream comprising di-sulfide oil having sodium level below 0.1 ppm.

公开(公告)号：EP2449059A4

公开(公告)日：2017-03-08

申请号：EP10793730

申请日：2010-06-09

Applicant: RELIANCE IND LTD

Inventor： YADAV MANOJ ,  MANDAL SUKUMAR ,  DAS ASIT KUMAR ,  GUPTA YOGESH ,  MAKHANIA MINAZ ,  TULSI GOBIND ,  ARORA SHAILENDRA ,  JAGUSTE SHUBHANGI

IPC: C10G53/08 ,  C10G31/06

CPC classification number: C10G53/08 ,  C10G5/04 ,  C10G5/06 ,  C10G7/02 ,  C10G11/18 ,  C10G31/06 ,  C10G55/06 ,  C10G70/06 ,  C10G2300/301 ,  C10G2400/20 ,  C10G2400/26 ,  C10G2400/28

Abstract: A process is disclosed for enhanced recovery of propylene and LPG from the fuel gas produced in Fluid catalytic cracking unit by contacting a heavier hydrocarbon feed with FCC catalyst. In the conventional process, the product mixture from FCC main column overhead comprising naphtha, LPG and fuel gas, are first condensed and gravity separated to produce unstabilized naphtha, which is subsequently used in the absorber to absorb propylene and LPG from fuel gas. However, the recovery of propylene beyond 97 wt % is difficult in this process since unstabilized naphtha already contains propylene of 5 mol % or above. In the present invention, C4 and lighter components from unstabilized naphtha are first stripped off in a separate column to obtain a liquid fraction almost free from propylene (

公开(公告)号：EP3116832A4

公开(公告)日：2017-10-18

申请号：EP15760686

申请日：2015-01-28

Applicant: RELIANCE IND LTD

Inventor： REDDY AKUIRI SATYANARAYANA ,  SENGUPTA SURAJIT ,  DONGARA RAJESHWER ,  DAS ASIT KUMAR ,  AMTE VINAY ,  YADAV ASHWANI ,  BAJPAI PRAMOD KUMAR ,  BHUNIA HARIPADA

IPC: C02F7/00 ,  B01D53/62 ,  B01J20/04

CPC classification number: B01J20/041 ,  B01D53/62 ,  B01D53/8671 ,  B01D53/8681 ,  B01D2251/306 ,  B01D2251/606 ,  B01D2253/104 ,  B01D2255/2092 ,  B01D2257/504 ,  B01D2258/0283 ,  B01J20/08 ,  B01J20/28057 ,  B01J20/28061 ,  B01J20/28064 ,  B01J20/28069 ,  B01J20/28071 ,  B01J20/28073 ,  B01J20/28083 ,  B01J20/2809 ,  B01J20/3078 ,  B01J20/3204 ,  B01J20/3236 ,  B01J20/3433 ,  B01J20/3483 ,  B01J23/04 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/08 ,  Y02W10/33

Abstract: The present invention relates to a stabilized inorganic oxide support for capturing carbon dioxide from gases having high regeneration capacities over many cycles. The method for preparing the stabilized inorganic oxide support includes stabilizing an alumina-containing precursor by either calcining or steaming, impregnating an alkali or alkaline earth compound into the stabilized alumina-and drying the alkali or alkaline earth compound-impregnated stabilized alumina. The stabilized inorganic oxide support can be regenerated at lower temperatures between 100 and 150° C. The carbon dioxide adsorption capacity of the regenerated support is between 70 and 90% of the theoretical carbon dioxide adsorption capacity.

公开(公告)号：EP2364343A4

公开(公告)日：2013-11-20

申请号：EP09831572

申请日：2009-12-08

Applicant: RELIANCE IND LTD

Inventor： MANDAL SUKUMAR ,  DAS ASIT KUMAR ,  YADAV ASHWANI ,  YADAV MANOJ ,  BHATNAGAR AKHILESH ,  DONGARA RAJESHWAR ,  KATRAVULAPALLI VEERA VENKATA SATYA BHASKARA SITA

IPC: C10G11/05 ,  C10G11/18

CPC classification number: C10G11/18 ,  C10G11/05 ,  C10G2400/20

Abstract: 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 at least 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 hydrocarbon 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.

Abstract translation: 丙烯和乙烯的制造在FCC单元。 每个FCC提升管包括加速区，升降流进料喷嘴，主烃原料喷嘴的，并且在烯烃石脑油进料喷嘴。 混合FCC催化剂重量Y型沸石，其包含至少2重量％的五元环沸石和至少10％的在每个FCC提升管的底部注入。 烯烃石脑油通过烯烃进料喷嘴喷射，主烃股票通过主烃原料和喷嘴升降流注入通过升降流进料喷嘴喷射。 升程流包含烯烃的C 4烃料流和任选的蒸汽和/或燃料气体。 烯属C 4烃蒸汽在加速区在600裂化以800℃，0.8〜5千克/厘米2（表压）的压力，WHSV 0.2至100小时上升1和蒸气的停留时间为0.2至5秒。

公开(公告)号：EP3041889A4

公开(公告)日：2017-04-26

申请号：EP14841192

申请日：2014-08-19

Applicant: RELIANCE IND LTD

Inventor： SHOWN BISWAJIT ,  GHOSH SWAPAN ,  DAS ASIT KUMAR ,  SALGARKAR SUYOG SUBHASH ,  BAISHYA MUKUNDA MADHAV ,  LADANI MITUL AMRUTBHAI ,  PANSERIYA CHIRAG DALPATBHAI

IPC: B01J41/20 ,  B01D15/08 ,  B01J49/57 ,  B01J49/60 ,  C08J5/20

CPC classification number: C09K8/524 ,  B01J41/20 ,  B01J49/57 ,  B01J49/60

Abstract: The present disclosure relates to a method for regeneration of spent ion exchange resins to obtain regenerated ion-exchange resins. The regenerated ion exchange resins can efficiently reduce the total acid number (TAN) of highly acidic crude oils. The present disclosure particularly relates to a method of treatment of spent ion exchange resins using at least one non-acidic crude oil condensate and at least one polar organic solvent.

Abstract translation: 本公开涉及再生废离子交换树脂以获得再生离子交换树脂的方法。 再生离子交换树脂可以有效地降低高酸性原油的总酸值（TAN）。 本公开尤其涉及使用至少一种非酸性原油冷凝物和至少一种极性有机溶剂来处理废离子交换树脂的方法。

公开(公告)号：EP2729553A4

公开(公告)日：2015-04-29

申请号：EP11869173

申请日：2011-09-29

Applicant: RELIANCE IND LTD

Inventor： DINDA SRIKANTA ,  CHINTHALA PRAVEEN KUMAR ,  GOHEL AMIT ,  YADAV ASHWANI ,  MANDAL SUKUMAR ,  RAVICHANDRAN GOPAL ,  DAS ASIT KUMAR

IPC: C10G11/05 ,  B01J29/08 ,  B01J29/40 ,  B01J29/70 ,  B01J29/80 ,  B01J35/02 ,  B01J35/10 ,  B01J37/00 ,  B01J37/02 ,  C10G11/02

CPC classification number: C10G11/05 ,  B01J29/088 ,  B01J29/40 ,  B01J29/7046 ,  B01J29/7057 ,  B01J29/80 ,  B01J35/023 ,  B01J35/1019 ,  B01J35/1038 ,  B01J37/0045 ,  B01J2229/183 ,  B01J2229/186 ,  B01J2229/36 ,  B01J2229/42 ,  C10G11/18 ,  C10G2400/02 ,  C10G2400/20 ,  C10G2400/26 ,  C10G2400/28