JP2012092009A - 最適化された水蒸気の生成を伴う、オイルカットを水蒸気改質することによる水素製造方法 - Google Patents
最適化された水蒸気の生成を伴う、オイルカットを水蒸気改質することによる水素製造方法 Download PDFInfo
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Abstract
【解決手段】本方法によって生成させられる水蒸気は、方法の全体において用いられ、水蒸気の第1の部分(17)は、供給原料(1)との混合物として交換器−反応器(25)に導入され、第2の部分(21)は、高温煙道ガスを圧縮するための圧縮機(32)を駆動する蒸気タービン(33)に供給する。
【選択図】図2
Description
・ 処理からの水蒸気の流れ(17)は、炭化水素供給原料(1)との混合物として水蒸気改質反応器(25)に送られ、その流れは、水蒸気(17)対炭化水素供給原料(1)の比が1.5〜3の範囲、好ましくは1.5〜2の範囲の値に調整されるように制御され;
・ 生じた残りの水蒸気(21)を、圧縮機(32)と関連する蒸気タービン(33)に供給するために用い、前記圧縮機(32)に供給する空気流(20)は、煙道ガス回路(35)上において交換機(7−1)および(6−1)の下流に置かれた弁(36)によって、圧縮機(32)の作動圧力が3〜5絶対バールに調整されて、前記圧縮機の特性曲線上に留まるように制御される。
本発明は、高純度の水素、すなわち少なくとも99.5%(重量による)の純度の水素の製造方法であって、燃焼室によって生じた、圧力下の高温煙道ガスを伝熱流体として用いる交換器−反応器において炭化水素留分を水蒸気改質することによる、方法として定義され得る。従来技術の方法の全てと比較して、本発明の方法は、本方法の要件(すなわち、一方で、炭化水素供給原料の水蒸気改質に必要な水蒸気、他方で、伝熱流体を加圧するための圧縮機を駆動することができる水蒸気タービンのためのエネルギーの供給)に厳密に相当する量の水蒸気を発生させる。
・ 本処理からの水蒸気の流れは、ライン(17)を経て、ライン(1)からの炭化水素供給原料との混合物として水蒸気改質反応器(25)に送られ、その流れは、ライン(17)からの水蒸気対ライン(1)からの炭化水素供給原料の比が1.5〜3の範囲、好ましくは1.5〜2の範囲の値に調整されるように制御され;
・ 生じた残りの水蒸気は、ライン(21)を経て、圧縮機(32)と関連する蒸気タービン(33)に供給するように用いられ、前記圧縮機(32)に供給する、ライン(20)からの空気流は、煙道ガス回路を示すライン(35)上において交換器(7−1)および(6−1)の下流に置かれた弁(36)によって、圧縮機(32)の作動圧力が3〜5絶対バールに調整されて、前記圧縮機の特性曲線上に留まるように制御される。
本発明の方法の適切な理解のために、図1のフローチャートを説明する必要がある。このフローチャートは、最も近い従来技術を構成するHygensys法を示す;本発明は、サイトが水蒸気を必要とせず(水蒸気改質方法自体によって要求された水蒸気を除く)、電気も必要としない状況への適応として見られ得る。
供給原料、好ましくは、天然ガスは、ライン(17)を介して到達する水蒸気との混合物として、ライン(1)を介して交換器−反応器(25)に送られる。
100000Nm3/時の水素を99.9重量%の純度で製造することを検討する。
5 蒸気ドラム
6−1、7−1、11、12、13 交換器
14 分離ドラム
24 バヨネット管
25 交換器−反応器
27 燃焼室
32、43 圧縮機
33 蒸気タービン
36 弁
40 シーブ分離装置
Claims (3)
- オイルカットを水蒸気改質することによる水素の製造方法であって、空気流(20)および燃料ガス(19)から出発して高温煙道ガス(34)を生じさせる燃焼室(27)を採用し、前記高温煙道ガス(34)は、圧縮機(32)によって圧縮され、かつそれらの熱を、交換器−反応器(25)に供給し、該交換器−反応器(25)内で水蒸気(17)と混合された炭化水素供給原料(1)を水蒸気改質する反応が行われ、合成ガスと称される反応流出物(2)は一連の交換器内で冷却され、煙道ガス(35)は別の一連の交換器(6−1)、(7−1)内で冷却され、その結果水蒸気が発生し、該水蒸気は、流れ(8)、(8’)、および(9’)を介して蒸気ドラム(5)内に導入され、本方法によって生じた水蒸気(18)は、全体として、それ自体本方法において、以下の手順によって用いられる方法:
・ 方法からの水蒸気(17)の流れは、炭化水素供給原料(1)との混合物として水蒸気改質反応器(25)に送られ、その流れは、水蒸気(17)対炭化水素供給原料(1)の比が1.5〜3の範囲、好ましくは1.5〜2の範囲の値に調整されるように制御され;
・ 生じた残りの水蒸気(21)を、圧縮機(32)と関連する蒸気タービン(33)に供給するために用い、前記圧縮機(32)に供給する空気流(20)は、煙道ガス回路(35)上において交換機(7−1)および(6−1)の下流に置かれた弁(36)によって、圧縮機(32)の作動圧力が3〜5絶対バールに調整されて、前記圧縮機の特性曲線上に留まるように制御される。 - 流出ガス(2)(「合成ガス」として知られる)は、一連の交換器(11)、(12)、(13)内での冷却後(37)に、分離器(14)内で水を分離した後、シーブ分離装置(40)に導入され、一方で、該シーブ分離装置(40)は、方法の水素(41)を99.9重量%超の純度で製造し、他方で、パージガス(42)を生じさせ、該パージガス(42)は、圧縮機(43)によって圧縮されて、燃焼ガス(22)が構成され、該燃焼ガス(22)を、燃焼室(27)に、場合によっては、補給燃料ガス(19)との混合物として供給することを特徴とする、請求項1に記載の方法。
- 水蒸気改質反応器のための供給原料は、1〜10個の範囲、好ましくは1〜5個の範囲の炭素原子を含有するオイルカットである、請求項1または2に記載の水蒸気改質による水素製造方法。
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FR1004242A FR2966814B1 (fr) | 2010-10-28 | 2010-10-28 | Procede de production d'hydrogene par vaporeformage d'une coupe petroliere avec production de vapeur optimisee. |
FR1004242 | 2010-10-28 |
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JP2012092009A true JP2012092009A (ja) | 2012-05-17 |
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FR3053033A1 (fr) * | 2016-06-28 | 2017-12-29 | Ifp Energies Now | Procede de vaporeformage de gaz naturel presentant deux chambres de combustion generant les fumees chaudes apportant les calories necessaires au procede et connectees en serie ou en parallele. |
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JP4451741B2 (ja) * | 2004-08-03 | 2010-04-14 | 株式会社日立製作所 | 重質油改質装置、改質方法及びコンバインド発電システム |
FR2890955B1 (fr) | 2005-09-21 | 2008-02-01 | Inst Francais Du Petrole | Procede de production de gaz de synthese par vaporeformage dans un reacteur-echangeur |
FR2914395B1 (fr) | 2007-03-30 | 2009-11-20 | Inst Francais Du Petrole | Nouveau reacteur echangeur compact utilisant un bruleur poreux |
WO2008137815A1 (en) * | 2007-05-04 | 2008-11-13 | Clark Steve L | Reduced-emission gasification and oxidation of hydrocarbon materials for liquid fuel production |
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2010
- 2010-10-28 FR FR1004242A patent/FR2966814B1/fr not_active Expired - Fee Related
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2011
- 2011-09-19 SI SI201130044T patent/SI2447210T1/sl unknown
- 2011-09-19 RS RS20130308A patent/RS52868B/en unknown
- 2011-09-19 PT PT112904198T patent/PT2447210E/pt unknown
- 2011-09-19 ES ES11290419T patent/ES2422903T3/es active Active
- 2011-09-19 PL PL11290419T patent/PL2447210T3/pl unknown
- 2011-09-19 EP EP11290419.8A patent/EP2447210B1/fr not_active Not-in-force
- 2011-10-24 CA CA2756613A patent/CA2756613C/fr not_active Expired - Fee Related
- 2011-10-27 US US13/282,699 patent/US8529866B2/en not_active Expired - Fee Related
- 2011-10-27 RU RU2011143514/05A patent/RU2599762C2/ru not_active IP Right Cessation
- 2011-10-28 CN CN201110340869.7A patent/CN102530865B/zh not_active Expired - Fee Related
- 2011-10-28 JP JP2011237047A patent/JP5887103B2/ja not_active Expired - Fee Related
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2013
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JP2003040603A (ja) * | 2001-07-26 | 2003-02-13 | Fuji Electric Co Ltd | 水素発生装置 |
US20030110693A1 (en) * | 2001-12-17 | 2003-06-19 | Drnevich Raymond Francis | Production enhancement for a reactor |
US20090229239A1 (en) * | 2008-03-14 | 2009-09-17 | Keller Arnold P | Integrated Pressurized Steam Hydrocarbon Reformer and Combined Cycle Process |
US20090232729A1 (en) * | 2008-03-17 | 2009-09-17 | Air Products And Chemicals, Inc. | Steam-Hydrocarbon Reforming Method with Limited Steam Export |
Also Published As
Publication number | Publication date |
---|---|
SI2447210T1 (sl) | 2013-09-30 |
US8529866B2 (en) | 2013-09-10 |
PL2447210T3 (pl) | 2013-10-31 |
EP2447210B1 (fr) | 2013-04-24 |
ES2422903T3 (es) | 2013-09-16 |
RU2011143514A (ru) | 2013-05-10 |
RS52868B (en) | 2013-12-31 |
CN102530865A (zh) | 2012-07-04 |
HRP20130672T1 (en) | 2013-08-31 |
CA2756613A1 (fr) | 2012-04-28 |
CN102530865B (zh) | 2015-11-25 |
RU2599762C2 (ru) | 2016-10-10 |
PT2447210E (pt) | 2013-07-22 |
FR2966814B1 (fr) | 2016-01-01 |
JP5887103B2 (ja) | 2016-03-16 |
US20120107227A1 (en) | 2012-05-03 |
EP2447210A1 (fr) | 2012-05-02 |
CA2756613C (fr) | 2017-06-20 |
FR2966814A1 (fr) | 2012-05-04 |
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