JPS61106401A - Reforming apparatus - Google Patents
Reforming apparatusInfo
- Publication number
- JPS61106401A JPS61106401A JP59228227A JP22822784A JPS61106401A JP S61106401 A JPS61106401 A JP S61106401A JP 59228227 A JP59228227 A JP 59228227A JP 22822784 A JP22822784 A JP 22822784A JP S61106401 A JPS61106401 A JP S61106401A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- furnace body
- circumferential direction
- reforming
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
- H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/062—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 in tube reactors; the solid particles being arranged in tubes being installed in a furnace
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Development (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Organic Chemistry (AREA)
- Sustainable Energy (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
Description
【発明の詳細な説明】 〔発明の属する技術分野〕 本発明は1例えば埠料電池発電システムに関し。[Detailed description of the invention] [Technical field to which the invention pertains] 1. Field of the Invention The present invention relates to, for example, a charging battery power generation system.
更に詳しくは、熱エネルギー交換後率を向上させ、その
熱エネルギーを有効に利用でき、かつ装置の温度分布を
小さくできる改質装置に個する。More specifically, the present invention relates to a reforming apparatus that can improve the rate of thermal energy exchange, effectively utilize the thermal energy, and reduce the temperature distribution of the apparatus.
各種プラントにおいて、効率の向上、省エネルギー等を
実現させるためには、エネルギー特に熱エネルギーの交
換効率を向上させ、・有効に利用することが重要である
0例えば、水素を発電用原料として使用する燃料電池に
おいては、経済性を向上するために、アノードの排ガス
を、改質装置における加熱用燃料としている。従来の具
1体的な改質装置としては、第3図および第4図に示す
構造が知られている。すなわち、改質装置1oは1通風
ガイドである内筒1.炉体である外筒2および改質用触
媒3の充填しである触媒管4よりなり、熱媒体である燃
焼ガスが内筒内のバーナ5により供給される。燃焼ガス
は内筒内を図の下方lζくだり−、底部管板6の上側で
おり返し、内外筒間を上昇する。上昇中に燃焼の熱エネ
ルギーがガスより触媒管に伝達され、このエネルギーが
改質エネルギーとして利用される。エネルギー交換後、
燃焼ガスは上部ガス排出ロアより排出管8を介して外部
に廃棄される。In order to improve efficiency and save energy in various plants, it is important to improve the exchange efficiency of energy, especially thermal energy, and use it effectively. For example, fuel that uses hydrogen as a raw material for power generation. In batteries, in order to improve economic efficiency, the exhaust gas from the anode is used as heating fuel in the reformer. As a conventional concrete reformer, the structures shown in FIGS. 3 and 4 are known. That is, the reformer 1o has an inner cylinder 1. which is a ventilation guide. It consists of an outer cylinder 2 which is a furnace body and a catalyst tube 4 which is filled with a reforming catalyst 3, and combustion gas which is a heat medium is supplied by a burner 5 in the inner cylinder. The combustion gas flows down the inside of the inner cylinder toward the bottom lζ in the figure, returns to the upper side of the bottom tube plate 6, and rises between the inner and outer cylinders. During the ascent, the thermal energy of combustion is transferred from the gas to the catalyst tubes, and this energy is used as reforming energy. After energy exchange,
The combustion gas is discharged to the outside from the upper gas discharge lower via the discharge pipe 8.
このような装置において、従来より周知の手段を適用す
ることにより、熱エネルギーの変換効率を向上すること
は可能である0例えば、触媒を細い多数の管に分配して
炉内に入れることにより伝熱面積を増加させたり、さら
に触媒管にフィンを付けたり、ひだ竹管にすることによ
り伝熱面積を増加させることが考えられる。また、内外
筒間にガスの流量に直角な方向にじゃま板をもうけ、燃
焼ガスの流れを乱し、ガスから触媒管への熱伝達特性を
向上させることも考えられる。しかしながら以上のよう
な手段によれば、それぞれの触媒管についての熱交換の
効率は上昇するが、全体的に均一な温度で上昇させるこ
とは不可能である。実際に製作上における装置の不均等
性、すなわち内筒と外筒の中心が一致しておらず、内筒
が偏心しでたり傾いたりしている状態、あるいは廃棄ガ
ス出口に近い部分とそれ以外の部分とでは、燃焼ガスの
流量に差がでて、どの触媒管も均等な温度になることは
きわめて難しい、実験によると、温度が定常な状態にな
っても温度の高い管と温度の低い管では円周方向の分布
として100℃以上の差がついてしまう。In such devices, it is possible to improve the conversion efficiency of thermal energy by applying conventionally well-known means. It is possible to increase the heat transfer area by increasing the heat area, adding fins to the catalyst tube, or making it a pleated bamboo tube. It is also conceivable to provide a baffle plate between the inner and outer cylinders in a direction perpendicular to the gas flow rate to disrupt the flow of combustion gas and improve the heat transfer characteristics from the gas to the catalyst tube. However, according to the above-mentioned means, although the efficiency of heat exchange for each catalyst tube increases, it is impossible to raise the temperature uniformly throughout. In fact, unevenness of the device due to manufacturing, that is, the center of the inner cylinder and the outer cylinder do not match, the inner cylinder is eccentric or tilted, or the part near the waste gas outlet and the other part There is a difference in the flow rate of combustion gas between the two parts, and it is extremely difficult to achieve an equal temperature in all catalyst tubes.According to experiments, even when the temperature is in a steady state, there are tubes with high temperature and tubes with low temperature. In a tube, there is a difference of 100°C or more in the distribution in the circumferential direction.
この発明は、上述の欠点を除去して、炉体内部の円周方
向全体に均一な温度分布を実現することのできる改質装
置を提供することを目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a reformer that can eliminate the above-mentioned drawbacks and realize a uniform temperature distribution throughout the circumferential direction inside the furnace body.
この発明は、炉体の内壁に沿って螺旋状のガイド板を設
け、熱媒体を炉体内部で円周方向に旋回させながら上昇
あるいは移動させることにより。In this invention, a spiral guide plate is provided along the inner wall of the furnace body, and the heating medium is raised or moved inside the furnace body while swirling in the circumferential direction.
各触媒管の円周方向の温度のバラツキをなくし、また熱
媒体から触媒管への全体としての熱交換効率を上げよう
とするものである。The purpose is to eliminate variations in temperature in the circumferential direction of each catalyst tube and to increase the overall heat exchange efficiency from the heat medium to the catalyst tubes.
第1図および第2図に本発明の実施例を示す。 Embodiments of the present invention are shown in FIGS. 1 and 2. FIG.
なお、第3図および第4図と同一の構成については同一
符号を付し、その説明を省略している。9は燃焼ガスが
スパイラルアップすなわち円周方向に旋回しながら上昇
していくようにもうけたガイド板である。外筒径250
順、内筒径150朋、触媒管径201EI の小型改質
装置20において、燃焼ガスが排気部に至るまでに3回
回転するようにガイド板9を設ければ、熱伝達係数は約
2倍になる。Note that the same components as in FIGS. 3 and 4 are given the same reference numerals, and their explanations are omitted. Reference numeral 9 denotes a guide plate provided so that the combustion gas spirals up, that is, rises while turning in the circumferential direction. Outer cylinder diameter 250
In a small reformer 20 with an inner cylinder diameter of 150 mm and a catalyst tube diameter of 201 EI, if the guide plate 9 is provided so that the combustion gas rotates three times before reaching the exhaust section, the heat transfer coefficient will be approximately doubled. become.
またガイド板を設ける前には円周方向の温度差が100
℃以上あったものが、ガイド板を設けることにより1円
周方向の温度差が約20℃になった。Also, before installing the guide plate, the temperature difference in the circumferential direction was 100
℃ or more, but by providing a guide plate, the temperature difference in one circumferential direction became about 20℃.
また、触媒により多段反応を行なわせるような場合、た
とえばメタノールのスチームリホーミングでは、2段反
応のうち第1段のメタノール分解は吸熱反応でエネルギ
ーを消費し、第2段のCOとH2Oの反応は発熱反応で
エネルギニを放出する。In addition, when a multi-stage reaction is carried out using a catalyst, for example, in steam reforming of methanol, the first stage of methanol decomposition is an endothermic reaction that consumes energy, and the second stage of the reaction between CO and H2O consumes energy. releases energy in an exothermic reaction.
このような時には、触媒管4の下部で多くの熱エネルギ
ーを伝?させたいこ七になる。この場合、熱伝達量を多
くしたい部分だけに、スパイラルアップするようなガイ
ド板を設ければ、より効果的な熱エネルギーの利用が可
能である。In such a case, a lot of heat energy is transferred at the bottom of the catalyst tube 4. I want to be seven. In this case, more effective use of thermal energy can be achieved by providing a guide plate that spirals up only in the portion where the amount of heat transfer is desired to be increased.
以上の説明から明らかなように、炉体の内壁に沿って螺
旋状のガイド板を設けたことにより、複数の触媒管が均
一に加熱され触Iy、、管の円周方向の温度分布が小さ
くなる。この結果、触媒の反応速度が均一となり、各反
応管への反応物の供給量が一均一になるという効果が得
られる。また、触媒の一部への極端な過負荷がなべなり
、全体として触媒の寿命を延ばすことができる。As is clear from the above explanation, by providing a spiral guide plate along the inner wall of the furnace body, the multiple catalyst tubes are heated uniformly, and the temperature distribution in the circumferential direction of the tubes is small. Become. As a result, the reaction rate of the catalyst becomes uniform, and the amount of reactants supplied to each reaction tube becomes uniform. In addition, extreme overload on a portion of the catalyst can be avoided, and the life of the catalyst as a whole can be extended.
第1図、第2図はそれぞれ本発明の実施例を示す改質装
置の平面断面図および外筒のみを縦割りに切り欠いて示
す側断面図、第3図、第4図はそれぞれ従来の改質装置
を示す平面断面図および側断面図である。
1;内筒、2;外筒、3:改質用触媒、4;触媒管、5
;バーナ、6;底部管板、7;ガス排出口、8;排出管
、9;ガイド板、11;メツシュプレート、20;改質
装置。
ヤIII!
才J図Figures 1 and 2 are a plan sectional view and a side sectional view showing only the outer cylinder cut away vertically, respectively, showing an embodiment of the present invention, and Figures 3 and 4 are respectively a conventional reformer. FIG. 1 is a plan sectional view and a side sectional view showing a reforming device. 1; Inner cylinder, 2; Outer cylinder, 3: Reforming catalyst, 4; Catalyst tube, 5
burner, 6; bottom tube plate, 7; gas outlet, 8; discharge pipe, 9; guide plate, 11; mesh plate, 20; reformer. Ya III! talented J figure
Claims (1)
設け、当該炉体の下方より熱媒体を供給してなる改質装
置において、前記炉体の内壁に沿つて螺旋状のガイド板
を設けたことを特徴とする改質装置。In a reforming device in which a plurality of catalyst tubes filled with a reforming catalyst are provided inside a cylindrical furnace body, and a heat medium is supplied from below the furnace body, a spiral shape is formed along the inner wall of the furnace body. A reforming device characterized by being provided with a guide plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59228227A JPS61106401A (en) | 1984-10-30 | 1984-10-30 | Reforming apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59228227A JPS61106401A (en) | 1984-10-30 | 1984-10-30 | Reforming apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61106401A true JPS61106401A (en) | 1986-05-24 |
Family
ID=16873160
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59228227A Pending JPS61106401A (en) | 1984-10-30 | 1984-10-30 | Reforming apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61106401A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01168332A (en) * | 1987-12-25 | 1989-07-03 | Hitachi Ltd | Apparatus for reforming fuel |
WO2003072234A1 (en) * | 2002-02-28 | 2003-09-04 | Webasto Thermosysteme Gmbh | Systems for reacting fuel and air to a reformate |
WO2004028679A1 (en) * | 2002-09-27 | 2004-04-08 | Erik Dessen | Method for the filling of particulate material in vertical tubes |
WO2005073126A1 (en) | 2004-01-30 | 2005-08-11 | Idemitsu Kosan Co., Ltd. | Reformer |
WO2005077820A1 (en) * | 2004-02-12 | 2005-08-25 | Ishikawajima-Harima Heavy Industries Co., Ltd. | Fuel reformer |
KR100741651B1 (en) | 2005-10-04 | 2007-07-24 | 이시가와지마 하리마 쥬우고오교 가부시끼가이샤 | Fuel reformer |
JP2008030997A (en) * | 2006-07-28 | 2008-02-14 | Osaka Gas Co Ltd | Reformer |
US7673660B2 (en) | 2005-03-25 | 2010-03-09 | Catalyst Services, Inc. | Filling tubes with catalyst and/or other particulate |
US8025472B2 (en) | 2007-06-01 | 2011-09-27 | Catalyst Services, Inc. | Catalyst loading system |
US10279330B2 (en) | 2015-04-29 | 2019-05-07 | Precision Consulting Services, LLC | Loading vertical tubes with particulate material |
CN114405413A (en) * | 2021-12-09 | 2022-04-29 | 西安航天华威化工生物工程有限公司 | Reaction device for producing maleic anhydride by n-butane method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5514802A (en) * | 1978-06-30 | 1980-02-01 | Nippon Kokan Kk <Nkk> | Treating method for molten metal generated at reduction treatment for slag from steel manufacture |
-
1984
- 1984-10-30 JP JP59228227A patent/JPS61106401A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5514802A (en) * | 1978-06-30 | 1980-02-01 | Nippon Kokan Kk <Nkk> | Treating method for molten metal generated at reduction treatment for slag from steel manufacture |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01168332A (en) * | 1987-12-25 | 1989-07-03 | Hitachi Ltd | Apparatus for reforming fuel |
WO2003072234A1 (en) * | 2002-02-28 | 2003-09-04 | Webasto Thermosysteme Gmbh | Systems for reacting fuel and air to a reformate |
US7753086B2 (en) | 2002-09-27 | 2010-07-13 | Catalyst Services, Inc. | Method for the filling of particulate material in vertical tubes |
WO2004028679A1 (en) * | 2002-09-27 | 2004-04-08 | Erik Dessen | Method for the filling of particulate material in vertical tubes |
WO2005073126A1 (en) | 2004-01-30 | 2005-08-11 | Idemitsu Kosan Co., Ltd. | Reformer |
US8038960B2 (en) | 2004-01-30 | 2011-10-18 | Idemitsu Kosan Co., Ltd. | Reformer |
JPWO2005073126A1 (en) * | 2004-01-30 | 2007-09-06 | 出光興産株式会社 | Reformer |
JP4714023B2 (en) * | 2004-01-30 | 2011-06-29 | 出光興産株式会社 | Reformer |
WO2005077820A1 (en) * | 2004-02-12 | 2005-08-25 | Ishikawajima-Harima Heavy Industries Co., Ltd. | Fuel reformer |
US7673660B2 (en) | 2005-03-25 | 2010-03-09 | Catalyst Services, Inc. | Filling tubes with catalyst and/or other particulate |
KR100741651B1 (en) | 2005-10-04 | 2007-07-24 | 이시가와지마 하리마 쥬우고오교 가부시끼가이샤 | Fuel reformer |
JP2008030997A (en) * | 2006-07-28 | 2008-02-14 | Osaka Gas Co Ltd | Reformer |
US8025472B2 (en) | 2007-06-01 | 2011-09-27 | Catalyst Services, Inc. | Catalyst loading system |
US10279330B2 (en) | 2015-04-29 | 2019-05-07 | Precision Consulting Services, LLC | Loading vertical tubes with particulate material |
CN114405413A (en) * | 2021-12-09 | 2022-04-29 | 西安航天华威化工生物工程有限公司 | Reaction device for producing maleic anhydride by n-butane method |
CN114405413B (en) * | 2021-12-09 | 2023-04-28 | 西安航天华威化工生物工程有限公司 | Reaction device for producing maleic anhydride by n-butane method |
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