JP2014529670A - Gtl環境における炭化水素燃料組成物のためのフィッシャー・トロプシュ法の改良 - Google Patents
Gtl環境における炭化水素燃料組成物のためのフィッシャー・トロプシュ法の改良 Download PDFInfo
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- JP2014529670A JP2014529670A JP2014528809A JP2014528809A JP2014529670A JP 2014529670 A JP2014529670 A JP 2014529670A JP 2014528809 A JP2014528809 A JP 2014528809A JP 2014528809 A JP2014528809 A JP 2014528809A JP 2014529670 A JP2014529670 A JP 2014529670A
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- hydrogen
- naphtha
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- gas generator
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Abstract
Description
a)合成ガス発生器で水素に富んだ流れを調製することと、
b)触媒的に前記流れを変換して、少なくともナフサを含む炭化水素を生成することと、
c)前記ナフサの少なくとも一部を前記合成ガス発生器へリサイクルして強化された水素に富んだ流れを形成することと;
d)ステップ(b)の転換に対して、ステップ(c)から前記強化された水素に富んだ流れを再循環させて、炭化水素の合成を強化することと、を含む、炭化水素を合成するためのプロセスが提供される。
2CH4+O2+CO2→3H3+3CO+H2O+熱
4CH4+O2+2H2O+熱→10H2+4CO
天然ガス+ナフサ+スチーム+熱→CO+nH2+CO2
少なくともナフサを含む炭化水素のソースを提供し、
合成ガス発生器へナフサをリサイクルさせて、水素に富んだ流れを生成し、および
水素に富んだ流れを触媒的に変換して、炭化水素を合成するステップを含む、炭化水素を合成するプロセスに提供する。
形成されたナフサを前記合成ガス発生器にリサイクルして、触媒的に水素に富んだ流れを変換し、炭化水素を合成することを含む。
a)高品質なディーゼル製品または添加剤である、
b)硫黄を含まない高品質ディーゼルおよびジェット燃料である、
c)石油副生成物またはナフサ等の低価値供給原料を含まない、
d)低排出でクリーンな燃焼のディーゼルおよびジェット燃料である、
e)高性能化を伴う上昇セタン価である、
f)フィッシャー・トロプシュリアクタを用いる従来のプロセスと比較して、ディーゼル/ジェット燃料をかなりの量を産出する。
(i)FTユニット40および製品アップグレーダー50への供給のめに強化された合成ガスから過剰水素を除去するために、水素分離ユニットを加える;
(ii)燃料としての使用に適さない水素も富んだ流れの一部を、単独でまたは全ての組み合わせで精製燃料64として、前処理ユニット20の方法でATR24にリサイクル102することができる;
(iii)炭素を逆移動およびリサイクルしてシンディーゼルの製造を強化する目的で、任意の二酸化炭素除去の段階21をFT合成ガス供給流れの上に設けて、FTユニット40への不活性蒸気導入を低減し、二酸化炭素の少なくとも一部12を前処理ユニット20の方法でATR24に再導入してもよい。
Claims (23)
- 炭化水素を合成するためのプロセスであって、以下のステップを備える:
(a)合成ガス発生器で水素リッチな流れを整流するステップ;
(b)前記流れを触媒により変換し、少なくともナフサを含む炭化水素を生成するステップ;
(c)前記ナフサの少なくとも一部を前記合成ガス発生器へリサイクルして、強化された水素リッチな流れを形成するステップ;および
(d)ステップ(b)の転換のため、ステップ(c)から前記強化された水素リッチな流れを再循環させて、炭化水素の合成を強化するステップ。 - 転換は、フィッシャー−トロプシュリアクタを用いて実現される請求項1に記載のプロセス。
- 水素の補助ソースが前記合成ガス発生器に加えられる請求項1または2に記載のプロセス。
- 重質炭化水素、軽質炭化水素および精製燃料ガスに加えて、ナフサを発生する請求項1〜3のいずれかに記載のプロセス。
- 前記合成ガス発生器は、スチームメタン改質炉(SMR)を備える請求項1〜4のいずれかに記載のプロセス。
- 前記合成ガス発生器は、自己熱改質炉(ATR)を備える請求項1〜5のいずれかに記載のプロセス。
- 前記合成ガス発生器は、自己熱改質炉およびスチームメタン改質炉の組合せを備える請求項1〜6のいずれかに記載のプロセス。
- 前記合成ガス発生器は、スチームメタン改質炉(XTR)と単一ユニットで結合した自己熱改質炉を有する合併されたユニットを備える請求項1〜7のいずれかに記載のプロセス。
- ステップ(d)からの精製燃料の少なくとも一部は、フィッシャー-トロプシュユニット、排ガス、炭化水素アップグレーダーユニットからのオフガスまたはこれらの組合せから成る群より選択される請求項4〜8のいずれかに記載のプロセス。
- 前記補助ソースは、天然ガスを備える請求項3〜9のいずれかに記載のプロセス。
- 前記ナフサから前記重質炭化水素の少なくとも一部を分離するステップをさらに備える請求項2〜10のいずれかに記載のプロセス。
- 水素精製ユニット内で前記水素リッチな流れの部分を処理するステップをさらに備える請求項1〜11のいずれかに記載のプロセス。
- 前記水素精製ユニットは、圧力スイング吸着法または膜ユニットを備える請求項12に記載のプロセス。
- 前記合成ガス発生器からの前記水素リッチな流れは、触媒作用の転換の前に二酸化炭素除去操作で処理される請求項1〜13のいずれかに記載のプロセス。
- 触媒により変換された流れは、炭化水素改質操作で処理される請求項1〜14のいずれかに記載のプロセス。
- 前記合成ガス発生器から回収されるエネルギーは、電力の製造に用いられる請求項1〜15のいずれかに記載のプロセス。
- 前記水素リッチな流れの触媒作用の転換から回収されるエネルギーは、電力の製造に用いられる請求項1〜16のいずれかに記載のプロセス。
- 炭化水素を合成するためのプロセスであって、以下のステップを備え:
少なくともナフサを含む炭化水素のソースを提供するステップと、
前記ナフサを合成ガス発生器へリサイクルさせて、水素リッチな流れを形成するステップと、
前記水素リッチな流れを触媒変換して、炭化水素を合成するステップと
を有するプロセス。 - 一体化されたATRおよびSMRを備える合成ガス発生器を提供するステップをさらに備える請求項18に記載のプロセス。
- 炭化水素合成収率を最適化するため、供給流れを各ATRおよびSMRのそれぞれにバランスさせるステップをさらに備える請求項19に記載のプロセス。
- リサイクルされたガスを使用して、前記SMRに供給した天然ガスを相殺するステップをさらに備える請求項20に記載のプロセス。
- フィッシャートロプシュリアクタを有する炭化水素を合成するためのガス−液体合成回路において、合成ガス発生器および触媒作用の転換および分留ための手段は、形成されたナフサを前記合成ガス発生器にリサイクルして、次の触媒による転換反応で水素リッチな流れを形成するガス−液体合成回路。
- 前記ナフサは、前記合成ガス発生器にリサイクルされ、前記ガス発生器が、スチームメタン改質炉と、自己熱改質炉と、自己熱改質炉およびスチームメタン改質炉が合併されたユニットとから成る群より選択される請求項22に記載のガス−液体合成回路。
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CA2731376C (en) * | 2011-02-11 | 2012-10-09 | Steve Kresnyak | Enhancement of fischer-tropsch process for hydrocarbon fuel formulation |
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BR112014005500A2 (pt) | 2017-04-04 |
CN104024182A (zh) | 2014-09-03 |
MX368516B (es) | 2019-10-07 |
EP2753596A4 (en) | 2015-04-15 |
EP2753596A1 (en) | 2014-07-16 |
RU2577547C2 (ru) | 2016-03-20 |
WO2013033812A1 (en) | 2013-03-14 |
EP3473609A1 (en) | 2019-04-24 |
AU2011376695A1 (en) | 2014-04-10 |
BR112014005500B1 (pt) | 2019-08-20 |
AU2011376695B2 (en) | 2016-05-19 |
EP2753596B1 (en) | 2019-05-01 |
MX2014002825A (es) | 2014-09-25 |
CN109135798A (zh) | 2019-01-04 |
AU2011376695A2 (en) | 2014-05-08 |
JP5902302B2 (ja) | 2016-04-13 |
RU2014112944A (ru) | 2015-10-20 |
CN109135798B (zh) | 2021-04-06 |
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