JP2008544846A - 2つ以上の流体を混合及び反応させると共に当該流体間で熱を移動させる反応器、及び当該反応器を操作する方法 - Google Patents
2つ以上の流体を混合及び反応させると共に当該流体間で熱を移動させる反応器、及び当該反応器を操作する方法 Download PDFInfo
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- C01B2203/1294—Evaporation by heat exchange with hot process stream
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Abstract
Description
・排熱を用いて反応物を予熱する熱エネルギー移動機構
・燃焼体積(加圧されている可能性がある)
・壁を通した熱移動と触媒の有効な作用とに必要な比較的大きな内面/体積比
・外部装置への熱移動を行う比較的大きな上面積及び底面積
「スイスロール」構造と同様に動作することができる別の構造は、マルチチャネルモノリシック構造である。しかしながら、この構造は、この構造内で流路を変えることを可能にする方法及び装置がないため適用可能ではない。
I CH4+H2O=3H2+CO 水蒸気メタン改質(SMR)
II CH4+0.5O2=CO+2H2 部分酸化(POx)
III CO+H2O=CO2+H2 水性ガスシフト反応(WGS)
Claims (16)
- 2つ以上の流体を混合及び反応させると共に該流体間で熱を移動させる反応器であって、
少なくとも1つの入口及び1つの出口を有し、且つマルチチャネルモノリシック構造(f)を囲む、圧力容器(g)と、
前記構造に流体を供給するため及び該構造から流体を排出するための、該構造のうちチャネル開口がある一端にシールされるマニホルドアセンブリ(b)と、
前記流れが前記構造のチャネルから出るときに流体流路の方向を180度変えるための、該構造のうち前記マニホルドアセンブリがシールされるのとは反対の端にシールされる手段(h)と
を備えることを特徴とする、2つ以上の流体を混合及び反応させると共に該流体間で熱を移動させる反応器。 - 前記手段はキャップであることを特徴とする、請求項1に記載の反応器。
- 前記チャネル開口は、前記モノリシック構造の断面積全体にわたって均一に分布することを特徴とする、請求項1に記載の反応器。
- 前記圧力容器は、前記マニホルドアセンブリ(b)に接続されるベロー(a)を囲むことを特徴とする、請求項1に記載の反応器
- 前記圧力容器は、流れ分配プレート(c)及びチョークプレート(d)を囲んで、前記マルチチャネルモノリシック構造(f)内で「チェスパターン」の流れを可能にすることを特徴とする、請求項1に記載の反応器。
- 前記チャネル壁の少なくとも1つは、触媒で被覆されることを特徴とする、請求項1に記載の反応器。
- 前記キャップは、前記モノリシック構造に流体を供給するノズルを備えることを特徴とする、請求項2に記載の反応器。
- 前記ノズルの断面積は、前記チャネルの断面積よりも小さく、
該ノズルの開口の位置は、前記供給される流体が反応ゾーン(A)の前に前記チャネル内の流体と混ざり合うような位置でなければならないことを特徴とする、請求項7に記載の反応器。 - 前記流体は、底部フランジを通して前記圧力容器に供給され、該圧力容器の内壁に沿って、但し前記構造の外側で上向きに流れ、さらに前記ノズルを通って前記チャネルに流れ込むことを特徴とする、請求項7に記載の反応器。
- 前記モノリシック構造はセラミック材料製であることを特徴とする、請求項1に記載の反応器。
- 前記モノリシックアセンブリは金属材料製であることを特徴とする、請求項1に記載の反応器。
- 前記キャップは金属材料製であることを特徴とする、請求項1に記載の反応器。
- 請求項1〜12に記載の反応器を操作する方法であって、
以下のステップ:
流体1が前記マニホルドアセンブリに供給され、前記モノリシック構造の一端にある1つ又は複数のチャネル開口に流れ込み、さらに前記構造の1つ又は複数のチャネルに流れ込み、そこで前記流体流れ中の成分が吸熱反応を起こし、生成物の流れが前記構造の反対端にある前記チャネル開口から流れ出て、該流れが180度方向転換して今度は流体2として前記構造の隣接チャネル開口に流れ込むステップと、
流体2が前記流体1と向流で前記隣接チャネルを通って流れ、そこで前記流体2中の成分が発熱反応を起こすことで高温の生成物の流れが得られるステップと、
前記発熱反応によって発生した熱が前記チャネル壁を通して移動させられて前記流体1を加熱するステップと、
前記構造のうち前記流体1が該構造に入るのと同じ端において前記生成物の流れ(流体2)が前記チャネルから流れ出るステップと
を含むことを特徴とする、反応器を操作する方法。 - 流体3が前記圧力容器に供給され、そこで該流体中の成分が流体2の1つ又は複数の成分との発熱反応を開始し、前記流体1と向流で前記チャネルを通って流れる高温の生成物の流れが得られることを特徴とする、請求項13に記載の方法。
- 前記流体は、触媒で被覆される1つ又は複数のチャネルに供給されることを特徴とする、請求項13に記載の方法。
- 前記流体は、前記モノリシック構造の断面積全体にわたって均一に分布するチャネル開口に供給されることを特徴とする、請求項13に記載の方法。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO20053257A NO328777B1 (no) | 2005-07-01 | 2005-07-01 | Metode og anordning for a blande og reagere to eller flere fluider samt overforing av varme mellom disse. |
PCT/NO2006/000236 WO2007004888A1 (en) | 2005-07-01 | 2006-06-21 | A reactor for mixing and reacting two or more fluids as well as transferring heat between said fluids and a method for operating said reactor |
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JP2008544846A true JP2008544846A (ja) | 2008-12-11 |
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JP2008519197A Pending JP2008544846A (ja) | 2005-07-01 | 2006-06-21 | 2つ以上の流体を混合及び反応させると共に当該流体間で熱を移動させる反応器、及び当該反応器を操作する方法 |
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Country | Link |
---|---|
US (1) | US20080263832A1 (ja) |
EP (1) | EP1901841A4 (ja) |
JP (1) | JP2008544846A (ja) |
NO (1) | NO328777B1 (ja) |
WO (1) | WO2007004888A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101063665B1 (ko) | 2009-10-15 | 2011-09-07 | 김정식 | 공작기계의 절삭유 열교환기 |
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GB201502589D0 (en) * | 2015-02-16 | 2015-04-01 | Airbusgroup Ltd | Pressure vessel |
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EP0967005A2 (de) * | 1998-06-23 | 1999-12-29 | dbb fuel cell engines GmbH | Wasserdampfreformierungsreaktor, insbesondere mit autothermer Prozessführung |
WO2001094005A1 (de) * | 2000-06-08 | 2001-12-13 | Paul Scherrer Institut | Katalytischer plattenreaktor mit interner wärmerekuperation |
WO2004090451A1 (en) * | 2003-04-11 | 2004-10-21 | Norsk Hydro Asa | Method and equipment for distribution of two fluids into and out of the channels in a multi-channel monolithic structure and use thereof |
WO2005052330A1 (en) * | 2003-11-28 | 2005-06-09 | Reccat Aps | Method for treatment of a fluid quantity including chemical reacting means such as combustible materials and a catalytic device |
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DE19653989C2 (de) * | 1996-12-21 | 1998-11-26 | Degussa | Reaktorkopf für einen monolithischen Gleich- oder Genstromreaktor |
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US6786275B2 (en) * | 2002-05-23 | 2004-09-07 | Valeo Engine Cooling | Heat exchanger header assembly |
EP1559679B1 (en) * | 2002-10-17 | 2016-02-24 | T.RAD Co., Ltd. | Autooxidation internal heating type steam reforming system |
-
2005
- 2005-07-01 NO NO20053257A patent/NO328777B1/no not_active IP Right Cessation
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2006
- 2006-06-21 EP EP06757879A patent/EP1901841A4/en not_active Withdrawn
- 2006-06-21 WO PCT/NO2006/000236 patent/WO2007004888A1/en active Application Filing
- 2006-06-21 JP JP2008519197A patent/JP2008544846A/ja active Pending
- 2006-06-21 US US11/887,223 patent/US20080263832A1/en not_active Abandoned
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0967005A2 (de) * | 1998-06-23 | 1999-12-29 | dbb fuel cell engines GmbH | Wasserdampfreformierungsreaktor, insbesondere mit autothermer Prozessführung |
WO2001094005A1 (de) * | 2000-06-08 | 2001-12-13 | Paul Scherrer Institut | Katalytischer plattenreaktor mit interner wärmerekuperation |
WO2004090451A1 (en) * | 2003-04-11 | 2004-10-21 | Norsk Hydro Asa | Method and equipment for distribution of two fluids into and out of the channels in a multi-channel monolithic structure and use thereof |
WO2005052330A1 (en) * | 2003-11-28 | 2005-06-09 | Reccat Aps | Method for treatment of a fluid quantity including chemical reacting means such as combustible materials and a catalytic device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101063665B1 (ko) | 2009-10-15 | 2011-09-07 | 김정식 | 공작기계의 절삭유 열교환기 |
Also Published As
Publication number | Publication date |
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NO328777B1 (no) | 2010-05-10 |
WO2007004888A1 (en) | 2007-01-11 |
EP1901841A1 (en) | 2008-03-26 |
EP1901841A4 (en) | 2012-01-25 |
NO20053257L (no) | 2007-01-02 |
US20080263832A1 (en) | 2008-10-30 |
NO20053257D0 (no) | 2005-07-01 |
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