JP2013139562A5 - - Google Patents

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Publication number
JP2013139562A5
JP2013139562A5 JP2012275192A JP2012275192A JP2013139562A5 JP 2013139562 A5 JP2013139562 A5 JP 2013139562A5 JP 2012275192 A JP2012275192 A JP 2012275192A JP 2012275192 A JP2012275192 A JP 2012275192A JP 2013139562 A5 JP2013139562 A5 JP 2013139562A5
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JP
Japan
Prior art keywords
amine
capture
fcc
integrated
dmea
Prior art date
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JP2012275192A
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English (en)
Japanese (ja)
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JP6159524B2 (ja
JP2013139562A (ja
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Publication date
Priority claimed from FR1103999A external-priority patent/FR2984177B1/fr
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Publication of JP2013139562A publication Critical patent/JP2013139562A/ja
Publication of JP2013139562A5 publication Critical patent/JP2013139562A5/ja
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Publication of JP6159524B2 publication Critical patent/JP6159524B2/ja
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JP2012275192A 2011-12-20 2012-12-18 改善されたco2バランスを有する、アミン処理装置と関連する接触分解のための方法 Active JP6159524B2 (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1103999A FR2984177B1 (fr) 2011-12-20 2011-12-20 Procede de craquage catalytique associe a une unite de traitement aux amines avec bilan co2 ameliore
FR11/03999 2011-12-20

Publications (3)

Publication Number Publication Date
JP2013139562A JP2013139562A (ja) 2013-07-18
JP2013139562A5 true JP2013139562A5 (enExample) 2016-01-14
JP6159524B2 JP6159524B2 (ja) 2017-07-05

Family

ID=47257720

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012275192A Active JP6159524B2 (ja) 2011-12-20 2012-12-18 改善されたco2バランスを有する、アミン処理装置と関連する接触分解のための方法

Country Status (8)

Country Link
US (1) US9352272B2 (enExample)
EP (1) EP2606951B1 (enExample)
JP (1) JP6159524B2 (enExample)
KR (1) KR102047551B1 (enExample)
CN (1) CN103170215B (enExample)
ES (1) ES2612508T3 (enExample)
FR (1) FR2984177B1 (enExample)
RU (1) RU2610868C2 (enExample)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9816759B2 (en) * 2015-08-24 2017-11-14 Saudi Arabian Oil Company Power generation using independent triple organic rankine cycles from waste heat in integrated crude oil refining and aromatics facilities
FR3045401B1 (fr) * 2015-12-17 2018-02-02 IFP Energies Nouvelles Solution absorbante a base de derives hydroxyles de la 1,6-hexanediamine et procede d'elimination de composes acides d'un effluent gazeux
CN109663496B (zh) * 2017-10-17 2021-09-07 中国石油化工股份有限公司 一种脱除烟气中硫氧化物和/或氮氧化物的方法
CN114100324A (zh) * 2021-12-10 2022-03-01 南京中昙气体有限公司 一种二氧化碳捕集工艺和设备

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4143521A (en) * 1977-02-08 1979-03-13 Stone & Webster Engineering Corporation Process for the production of ethylene
SU1391503A3 (ru) * 1981-05-20 1988-04-23 Энгельхард Минералз Энд Кемикалз Корпорейшн (Фирма) Способ декарбонизации и деметаллизации сырой нефти или ее остаточной фракции
CH669829A5 (enExample) * 1986-03-20 1989-04-14 Sulzer Ag
US4904372A (en) 1988-11-18 1990-02-27 Stone & Webster Engineering Corporation Process and apparatus for recovering heat energy from catalyst regenerator flue gases
JPH04350303A (ja) * 1991-05-27 1992-12-04 Jgc Corp 炭酸ガス回収型火力発電システム
CN2864101Y (zh) * 2005-09-22 2007-01-31 雷泽永 抽汽-背压式汽轮机用于拖动气体压缩机节汽装置
FR2939693B1 (fr) * 2008-12-16 2011-12-23 Inst Francais Du Petrole Nouveau procede de recuperation du co2 issu des fumees de regeneration d'une unite de craquage catalytique
US8007729B2 (en) * 2009-03-20 2011-08-30 Uop Llc Apparatus for feed preheating with flue gas cooler
US20100243528A1 (en) * 2009-03-30 2010-09-30 Bell Leonard E Method and system relating to a wet gas compressor
EA201270250A1 (ru) * 2009-08-11 2012-07-30 Флуор Текнолоджиз Корпорейшн Конфигурации и способы производства пара низкого давления
GB0922140D0 (en) * 2009-12-18 2010-02-03 Wellstream Int Ltd Regeneration of absorption solution
FR2959748B1 (fr) * 2010-05-06 2012-05-18 Inst Francais Du Petrole Procede de craquage catalytique avec recycle d'une coupe olefinique prelevee en amont de la section de separation des gaz afin de maximiser la production de propylene.

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