JP2011256386A - 還元流出物を第1の反応器の上流に再循環させ再循環ガスを一連の反応器の最後の反応器に再循環させる新規接触改質方法 - Google Patents
還元流出物を第1の反応器の上流に再循環させ再循環ガスを一連の反応器の最後の反応器に再循環させる新規接触改質方法 Download PDFInfo
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- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
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- C07C4/06—Catalytic processes
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/16—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "moving bed" method
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/10—Catalytic reforming with moving catalysts
- C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °C
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4081—Recycling aspects
Abstract
【解決手段】触媒還元帯域からの流出物の少なくとも一部を、供給原料を予備加熱することができる供給原料/流出物熱交換器の入口に再循環させ、他の部分を、場合により第1の反応器の頭部に再循環させることによって、かつ再循環圧縮機からのガスを一連の反応器のうちの最後から2番目の反応器の頭部に再循環する。
【選択図】図1
Description
・ 反応システムへの水の再導入を減少させるか、更には省くことができる;
・ ナフテンの脱水素化反応、および供給原料中に含まれるパラフィンの脱水素環化反応、すなわち、最初の2つの反応器内の水素分圧の減少により、これら2つの反応器内で起こる反応を促進する(この減少は、当該反応にとって熱力学的に有利である);
・ 正確にはコークスが優先的に形成される傾向を有する反応器である、最後のまたは最後から2番目の反応器に関するH2/HC(HC:炭化水素)比を増加させることにより、種々の反応器間の水素の分布を有利に改変する。
・ 反応器(R1)、(R2)、(R3)、(R4)が横並びに配置され、触媒が、1つの反応器(Rp)の底部から次の反応器(Rp+1)の頭部へと運ばれ、次いで最後の反応器に到達し、リフトラインを介して再生塔に供給される;
・ 反応器(R1)、(R2)、(R3)、(R4)が垂直に積み重ねられて配置され、触媒が、1つの反応器(Rp)からその下に位置する次の反応器(Rp+1)へと重力下に流れる。最後の反応器の底部におけるリフトラインにより、触媒を再生塔の頭部に導入することができる。
温度: 450〜520℃
水素含量: 90〜99.9容積%
塩素含量: 20〜50容積ppm
含水量: 50〜100容積ppm
第1の反応器の入口圧力: 4.9有効バール
(実施例)
2つの実施例を提供する、一方は従来技術に合致し、他方は本発明に合致する。本発明の実施例は、いかなる場合も本発明の操作条件を限定するものではない。それは、単に、従来技術の実施例と比較した、本発明に起因する利点の度合いを提供する役割を果たすものである。
供給原料の流量: 75トン/時
蒸留範囲: 60〜250℃
PNA(パラフィン、ナフテン、芳香族化合物)(容積%): 53/41/6
モーター法オクタン価: 102
操作条件
毎時空間速度: 2h−1
再循環比: 再循環圧縮機(RCY)に由来する、H2(7)のモル流量/新鮮なHC供給原料(1)のモル流量:
1.5に等しく、R1に送られる(従来技術による)
1.5に等しく、R3に送られる(本発明による)
反応器(R1)、(R2)、(R3)、(R4)の入口温度: 515℃
a)従来技術によると、低圧の分離ドラム(BS)からの再循環ガスは、第1の反応器(R1)に先行する供給原料/流出物熱交換器の上流に送られる。反応器(R1)に送られるH2/HC比は、1.5(モル/モル)である。
4:気体流出物
R1:第1の反応器
E1:供給原料/流出物熱交換器
BS:分離ドラム
RCY:再循環圧縮機
7:流出物
Claims (3)
- 直列の4つの反応器(R1、R2、R3、およびR4)を有する反応帯域と、水素による触媒還元工程を含む前記触媒の再生帯域とを含む移動床接触改質装置内での、60〜250℃の範囲の蒸留範囲を有するガソリンの接触改質方法であって、前記触媒還元工程からの気体流出物(4)は、一部が一連の反応器のうちの第1の反応器(R1)に先行する供給原料/流出物熱交換器 (E1)の入口に再循環させられ、かつ別の一部が第1の反応器(R1)の頭部に直接再循環させられ、並びに、分離ドラム(BS)と一連の反応器(R1、R2、R3、およびR4)の間に位置する再循環圧縮機(RCY)に由来する流出物(7)は、その全体又は一部が、最後から2番目の反応器(R3)の頭部に再循環させられる、方法。
- 気体の還元流出物(4)は、その全体が第1の反応器(R1)の頭部に送られ、再循環圧縮機(RCY)からの流出物(7)は、その全体が最後から2番目の反応器(R3)に再循環させられる、請求項1に記載のガソリンの接触改質方法。
- 気体の還元流出物(4)は、その全体が供給原料/流出物熱交換器(E1)の入口に送られ、再循環圧縮機(RCY)からの流出物(7)は、その全体が最後から2番目の反応器(R3)に再循環させられる、請求項1に記載のガソリンの接触改質方法。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1002425A FR2961215B1 (fr) | 2010-06-09 | 2010-06-09 | Nouveau procede de reformage catalytique avec recyclage de l'effluent de reduction en amont du premier reacteur et recyclage du gaz de recyclage sur le ou les derniers reacteurs de la serie. |
FR1002425 | 2010-06-09 |
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JP2011256386A true JP2011256386A (ja) | 2011-12-22 |
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JP2011126816A Ceased JP2011256386A (ja) | 2010-06-09 | 2011-06-07 | 還元流出物を第1の反応器の上流に再循環させ再循環ガスを一連の反応器の最後の反応器に再循環させる新規接触改質方法 |
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US (1) | US20120000822A1 (ja) |
EP (1) | EP2395067B1 (ja) |
JP (1) | JP2011256386A (ja) |
KR (1) | KR101845555B1 (ja) |
CN (1) | CN102277190B (ja) |
BR (1) | BRPI1102927B1 (ja) |
FR (1) | FR2961215B1 (ja) |
RU (1) | RU2563643C2 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103191677A (zh) * | 2013-04-26 | 2013-07-10 | 华东理工大学 | 一种模拟移动床反应器及其操作方法与应用 |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
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US9024098B2 (en) * | 2011-12-15 | 2015-05-05 | Uop Llc | Initial hydrotreating of naphthenes with subsequent high temperature reforming |
US9138738B1 (en) | 2014-04-14 | 2015-09-22 | Uop Llc | Processes for the continuous regeneration of a catalyst |
CN107406362B (zh) | 2015-02-13 | 2020-12-22 | 诺沃梅尔公司 | 灵活的化学生产平台 |
KR102524765B1 (ko) * | 2017-02-16 | 2023-04-25 | 엑손모빌 테크놀로지 앤드 엔지니어링 컴퍼니 | 경질 파라핀 전환을 위한 고정층 방사류 반응기 |
FR3063440B1 (fr) * | 2017-03-01 | 2019-06-07 | IFP Energies Nouvelles | Reacteur compartimente a faible capacite. |
US10233396B1 (en) * | 2018-06-01 | 2019-03-19 | Chevron Phillips Chemical Company Lp | Method of producing aromatic hydrocarbons |
FR3090007B1 (fr) | 2018-12-18 | 2020-12-25 | Ifp Energies Now | Procede de conversion d’hydrocarbures avec recyclage des effluents de reduction |
RU2752382C1 (ru) * | 2020-06-19 | 2021-07-26 | Общество с ограниченной ответственностью "Газпром переработка" | Способ каталитического риформинга бензиновых фракций |
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JP2003515657A (ja) * | 1999-11-30 | 2003-05-07 | アンスティテュ フランセ デュ ペトロール | 触媒の還元を含む、芳香族化合物の製造方法および装置 |
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BE790431A (fr) * | 1971-11-16 | 1973-04-24 | Inst Francais Du Petrole | Procede et appareillage pour procedes de conversions d'hydrocarbures |
FR2213335B1 (ja) * | 1973-01-10 | 1976-04-23 | Inst Francais Du Petrole | |
US4441988A (en) * | 1979-05-30 | 1984-04-10 | Irvine Robert L | Catalytic reformer process |
US5203988A (en) * | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
US5196110A (en) * | 1991-12-09 | 1993-03-23 | Exxon Research And Engineering Company | Hydrogen recycle between stages of two stage fixed-bed/moving-bed unit |
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US5683573A (en) * | 1994-12-22 | 1997-11-04 | Uop | Continuous catalytic reforming process with dual zones |
FR2801604B1 (fr) * | 1999-11-30 | 2002-04-26 | Inst Francais Du Petrole | Procede pour la production d'aromatiques en lit mobile incluant une reduction du catalyseur |
US20040129605A1 (en) * | 2002-10-29 | 2004-07-08 | Goldstein Stuart S. | Method for revamping fixed-bed catalytic reformers |
FR2852323B1 (fr) * | 2003-03-11 | 2006-07-14 | Inst Francais Du Petrole | Nouveau procede de reformage regeneratif |
CN101163536B (zh) * | 2005-01-21 | 2011-12-07 | 埃克森美孚研究工程公司 | 采用精炼工艺单元如加氢处理、加氢裂化的快速循环压力摆动吸附的改进的集成 |
USH2244H1 (en) * | 2005-03-22 | 2010-08-03 | Exxonmobil Research And Engineering Company | Method for operating catalytic reformers |
-
2010
- 2010-06-09 FR FR1002425A patent/FR2961215B1/fr not_active Expired - Fee Related
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2011
- 2011-04-12 EP EP11290183.0A patent/EP2395067B1/fr active Active
- 2011-06-01 KR KR1020110052792A patent/KR101845555B1/ko active IP Right Grant
- 2011-06-06 BR BRPI1102927A patent/BRPI1102927B1/pt not_active IP Right Cessation
- 2011-06-07 JP JP2011126816A patent/JP2011256386A/ja not_active Ceased
- 2011-06-08 RU RU2011123173/04A patent/RU2563643C2/ru active
- 2011-06-08 US US13/155,560 patent/US20120000822A1/en not_active Abandoned
- 2011-06-09 CN CN201110153669.0A patent/CN102277190B/zh active Active
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JPS52119604A (en) * | 1976-01-19 | 1977-10-07 | Uop Inc | Method of converting hydrocarbon by gravity flow catalyst particle |
JP2003515657A (ja) * | 1999-11-30 | 2003-05-07 | アンスティテュ フランセ デュ ペトロール | 触媒の還元を含む、芳香族化合物の製造方法および装置 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103191677A (zh) * | 2013-04-26 | 2013-07-10 | 华东理工大学 | 一种模拟移动床反应器及其操作方法与应用 |
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Publication number | Publication date |
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BRPI1102927B1 (pt) | 2019-08-27 |
FR2961215B1 (fr) | 2013-11-08 |
KR20110134831A (ko) | 2011-12-15 |
US20120000822A1 (en) | 2012-01-05 |
RU2011123173A (ru) | 2012-12-20 |
FR2961215A1 (fr) | 2011-12-16 |
CN102277190A (zh) | 2011-12-14 |
EP2395067A1 (fr) | 2011-12-14 |
KR101845555B1 (ko) | 2018-04-04 |
RU2563643C2 (ru) | 2015-09-20 |
BRPI1102927A2 (pt) | 2013-03-19 |
EP2395067B1 (fr) | 2018-09-05 |
CN102277190B (zh) | 2015-09-09 |
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