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公开(公告)号：US20220097279A1
公开(公告)日：2022-03-31
申请号：US17425458
申请日：2020-01-24
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Anthoni VAN ZIJL , Nicolas GOYHENEIX , Lara GALAN-SANCHEZ , Christoph ROOSEN , Johan PASTWA , Safa FARAJZADEH BIBALAN
IPC: B29C48/275 , C08J11/06 , B29B17/02 , C10G51/02
Abstract: The present invention relates to a process for the production of propylene-based polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising propylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an propylene-based polymer; wherein in step (d): • the coil outlet temperature is ≥800 and ≤850° C., preferably ≥805 and ≤835° C.; and • the weight ratio of steam to feed C is >0.3 and
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12.发明授权公开(公告)号：US11072747B2
公开(公告)日：2021-07-27
申请号：US16888916
申请日：2020-06-01
Applicant: Lummus Technology Inc.
Inventor： Liang Chen , Peter Loezos , Rama Rao Marri , Bryan Tomsula , Jon A. Hood , Hardik Singh , Michael Dorsey , Justin Breckenridge
Abstract: Apparatus and processes herein provide for converting hydrocarbon feeds to light olefins and other hydrocarbons. The processes and apparatus include, in some embodiments, feeding a hydrocarbon, a first catalyst and a second catalyst to a reactor, wherein the first catalyst has a smaller average particle size and is less dense than the second catalyst. A first portion of the second catalyst may be recovered as a bottoms product from the reactor, and a cracked hydrocarbon effluent, a second portion of the second catalyst, and the first catalyst may be recovered as an overhead product from the reactor. The second portion of the second catalyst may be separated from the overhead product, providing a first stream comprising the first catalyst and the hydrocarbon effluent and a second stream comprising the separated second catalyst, allowing return of the separated second catalyst in the second stream to the reactor.
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公开(公告)号：US10995281B2
公开(公告)日：2021-05-04
申请号：US16836273
申请日：2020-03-31
Applicant: Saudi Arabian Oil Company
Inventor： Ki-Hyouk Choi , Abdullah T. Alabdulhadi , Mohammad A. Al-Abdullah
IPC: C10G31/08 , C10G65/02 , C10G49/18 , C10G65/10 , C10G65/12 , B01J3/00 , C10G75/00 , B01J3/02 , C10G11/10 , C10G51/02 , C10G75/04
Abstract: Supercritical upgrading reactors and reactor systems are provided for upgrading a petroleum-based composition using one or more purging fluid inlets to prevent plugging of the catalyst layer in the reactor. Processes for upgrading petroleum-based compositions by utilizing a reactor having at least one purging fluid inlet are also provided.
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公开(公告)号：US10899684B2
公开(公告)日：2021-01-26
申请号：US16242465
申请日：2019-01-08
Applicant: Swift Fuels, LLC
Inventor： Chris D'Acosta , Jeffery Miller , Robert Hoch
Abstract: Methods for making higher-octane fuel components from a feed stream of C8+ paraffins, including catalytically cracking the C8+ paraffins using a Zeolite catalyst to produce a reaction product of mid-chain paraffins and olefins and short-chain paraffins and olefins. The reaction product comprises liquid phase paraffins having an increased Octane Value over the feed stream paraffins. The reaction product further comprises a gas phase of short-chain paraffins which are separated from the liquid phase. In embodiments, the short chain olefins are hydrogenated to form mid-chain paraffins and a gas phase containing short-chain paraffins.
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公开(公告)号：US10808188B2
公开(公告)日：2020-10-20
申请号：US16141619
申请日：2018-09-25
Applicant: CHINA PETROLEUM & CHEMICAL CORPORATION , RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC
Inventor： Jianhong Gong , Zekun Li , Jinlian Tang , Anguo Mao , Jiushun Zhang , Yuying Zhang , Jun Long
Abstract: A catalytic cracking process includes the following steps: i) subjecting a heavy feedstock oil to flail catalytic cracking; ii) separating the catalytic cracking reaction product obtained from step i) to obtain a catalytic cracking gasoline and a catalytic cracking light cycle oil; iii) splitting the catalytic cracking gasoline to obtain a light gasoline fraction, a medium gasoline fraction and a heavy gasoline fraction; iv) subjecting the catalytic cracking light cycle oil to hydrogenation to obtain a hydrogenated light cycle oil); v) mixing a portion of the light gasoline fraction with at least a portion of the hydrogenated light cycle oil to obtain a mixed fraction; vi) subjecting the mixed fraction to catalytic cracking; and vii) subjecting a portion of the medium gasoline fraction to flail catalytic cracking. The process is capable of producing more catalytic cracking gasoline, reducing the olefin content of the catalytic cracking gasoline, and increasing its octane number.
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Patent Agency Ranking
公开(公告)号：US10808177B2
公开(公告)日：2020-10-20
申请号：US15935828
申请日：2018-03-26
Applicant: Indian Oil Corporation Limited
Inventor： Satyen Kumar Das , Ponoly Ramachandran Pradeep , Terapalli Hari Venkata Devi Prasad , Arjun Kumar Kottakuna , Madhusudan Sau , Debasis Bhattacharyya , Sanjiv Kumar Mazumdar , Sankara Sri Venkata Ramakumar
IPC: C10G9/00 , C10B57/02 , C10G7/00 , C10G51/02 , C10B17/00 , B01J19/18 , C10B49/02 , C10B55/00 , C10B57/04
Abstract: The present invention relates to delayed coking of heavy petroleum residue producing petroleum coke and lighter hydrocarbon products. The invented process utilize a pre-cracking reactor and a reactor furnace for mild thermal cracking of the feedstock and an intermediate separator, before being subjected to higher severity thermal cracking treatment in a coker furnace and a coking drums, resulting in reduction in overall coke yield.
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17.发明授权公开(公告)号：US10696907B2
公开(公告)日：2020-06-30
申请号：US16511425
申请日：2019-07-15
Applicant: Lummus Technology Inc.
Inventor： Liang Chen , Peter Loezos , Rama Rao Marri , Bryan Tomsula , Jon A. Hood , Hardik Singh , Michael Dorsey , Justin Breckenridge
Abstract: Apparatus and processes herein provide for converting hydrocarbon feeds to light olefins and other hydrocarbons. The processes and apparatus include, in some embodiments, feeding a hydrocarbon, a first catalyst and a second catalyst to a reactor, wherein the first catalyst has a smaller average particle size and is less dense than the second catalyst. A first portion of the second catalyst may be recovered as a bottoms product from the reactor, and a cracked hydrocarbon effluent, a second portion of the second catalyst, and the first catalyst may be recovered as an overhead product from the reactor. The second portion of the second catalyst may be separated from the overhead product, providing a first stream comprising the first catalyst and the hydrocarbon effluent and a second stream comprising the separated second catalyst, allowing return of the separated second catalyst in the second stream to the reactor.
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公开(公告)号：US20190185765A1
公开(公告)日：2019-06-20
申请号：US16176679
申请日：2018-10-31
Applicant: Indian Oil Corporation Limited
Inventor： Satyen Kumar DAS , Terapalli Hari Venkata Devi PRASAD , Ponoly Ramachandran PRADEEP , Arjun Kumar KOTTAKUNA , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
CPC classification number: C10G51/023 , C10G7/06 , C10G9/005 , C10G9/14 , C10G11/18 , C10G45/00 , C10G47/00 , C10G55/04 , C10G69/06 , C10G2300/1044 , C10G2300/107 , C10G2300/1077 , C10G2300/708 , C10G2400/06
Abstract: The present invention relates to Delayed Coking of heavy petroleum residue producing petroleum coke and lighter hydrocarbon products. The invented process utilizes a pre-cracking reactor for mild thermal cracking of the feedstock and intermediate multistage separation system before being subjected to higher severity thermal cracking in delayed coking process, resulting in reduction in overall coke yield.
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公开(公告)号：US20180265792A1
公开(公告)日：2018-09-20
申请号：US15920099
申请日：2018-03-13
Applicant: Saudi Arabian Oil Company
Inventor： Ki-Hyouk CHOI , Abdullah T. ALABDULHADI , Gonzalo Feijoo MARTINEZ , Ali M. ALSOMALI , Mohammad A. ALABDULLAH , Essam A. AL-SAYED
Abstract: A method for producing a supercritical water (SCW)-treated product is provided. The method comprising the steps of introducing a crude oil stream and a water stream to a supercritical water process, wherein the crude oil stream can undergo conversion reactions to produce the supercritical water (SCW)-treated product, wherein the SCW-treated product includes an increased paraffin concentration as compared to crude oil stream. The method further includes the step of introducing the SCW-treated product to a steam cracking process, wherein the SCW-treated product can undergo conversion reactions to produce furnace effluent.
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公开(公告)号：US10066172B2
公开(公告)日：2018-09-04
申请号：US15374289
申请日：2016-12-09
Applicant: Saudi Arabian Oil Company
Inventor： Ki-Hyouk Choi , Mohammad A. AlAbdullah , Ashok K. Punetha , Emad N. Al-Shafei
CPC classification number: C10G51/023 , C10G9/36 , C10G47/32 , C10G49/007 , C10G65/10 , C10G75/00 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2400/00 , C10G2400/10
Abstract: Embodiments of a process for producing paraffins from a petroleum-based composition comprising long chain aromatics comprise mixing a supercritical water stream with a pressurized, heated petroleum-based composition to create a combined feed stream, introducing the combined feed stream to a first reactor through an inlet port of the first reactor, where the first reactor operates at supercritical pressure and temperature, cracking at least a portion of the long chain aromatics in the first reactor to form a first reactor product, and then introducing the first reactor product to a second reactor through an upper inlet port of the second reactor operating at supercritical pressure and temperature, where the second reactor is a downflow reactor comprising an upper inlet port, a lower outlet port, and a middle outlet port are provided. The middle outlet product passing out of the middle outlet port comprises paraffins and short chain aromatics.
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