JPH0576774A - Fuel reformer - Google Patents
Fuel reformerInfo
- Publication number
- JPH0576774A JPH0576774A JP3240050A JP24005091A JPH0576774A JP H0576774 A JPH0576774 A JP H0576774A JP 3240050 A JP3240050 A JP 3240050A JP 24005091 A JP24005091 A JP 24005091A JP H0576774 A JPH0576774 A JP H0576774A
- Authority
- JP
- Japan
- Prior art keywords
- reforming
- catalyst
- filled
- fuel reformer
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 35
- 238000002407 reforming Methods 0.000 claims abstract description 49
- 239000003054 catalyst Substances 0.000 claims abstract description 42
- 239000007789 gas Substances 0.000 claims abstract description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000001257 hydrogen Substances 0.000 claims abstract description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 4
- 239000002184 metal Substances 0.000 claims abstract description 3
- 229910052751 metal Inorganic materials 0.000 claims abstract description 3
- 239000002737 fuel gas Substances 0.000 claims abstract 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 6
- 238000000227 grinding Methods 0.000 abstract description 3
- 238000005299 abrasion Methods 0.000 abstract 1
- 230000003247 decreasing effect Effects 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000003252 repetitive effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000000629 steam reforming Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
-
- 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
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、車両搭載型の燃料電池
発電装置用として好適な燃料改質器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel reformer suitable for a vehicle-mounted fuel cell power generator.
【0002】[0002]
【従来の技術】最近になり、燃料電池の低公害性,高発
電効率の利点を生かして車両に燃料電池発電装置を搭載
した電気自動車の開発が進められており、この開発プロ
ジェクトに並行して車両搭載用の燃料電池発電装置の実
用化が進められている。図3はかかる燃料電池発電装置
のプロセスフロー図であり、メタノールを原燃料として
燃料改質器で水素リッチなガスに改質(水蒸気改質)
し、これを燃料電池に供給して発電する。なお、燃料電
池の動作原理は周知であり、ここではその説明を省略す
る。2. Description of the Related Art Recently, an electric vehicle having a fuel cell power generator installed in a vehicle has been under development by taking advantage of the low pollution and high power generation efficiency of the fuel cell, and in parallel with this development project. Practical application of fuel cell power generators for vehicles is under way. FIG. 3 is a process flow diagram of such a fuel cell power generation device, in which methanol is used as a raw fuel for reforming into a hydrogen-rich gas in a fuel reformer (steam reforming).
Then, this is supplied to the fuel cell to generate electricity. The operating principle of the fuel cell is well known, and the description thereof is omitted here.
【0003】次に、前記した燃料改質器の従来構造を図
4に示す。図において、1は改質器の炉本体、1aは炉
本体1の燃焼ガス排気口、2は炉本体1の頂部中央に設
置したバーナ、3はバーナ2を囲んで炉内に収設した改
質管、4は改質管3の管内に充填した粒状の改質触媒で
ある。なお、図示には改質管3が略示的に描かれている
が、実際の改質管には二重円筒管が採用されている。か
かる構成で、原燃料であるメタノール水溶液を気化して
改質管3の入口3aより導入すると、管内に充填されて
いる改質触媒4との接触反応(吸熱反応)により水蒸気
改質されて水素リッチな改質ガスに変換される。そして
改質ガスは改質管3の出口3bを通じて後段の燃料電池
に供給される。Next, a conventional structure of the above-mentioned fuel reformer is shown in FIG. In the figure, 1 is a reformer main body, 1a is a combustion gas exhaust port of the main body 1, 2 is a burner installed at the center of the top of the main body 1, and 3 is a reformer housed in the furnace surrounding the burner 2. The quality tubes 4 are granular reforming catalysts filled in the reforming tube 3. Although the reforming pipe 3 is schematically illustrated in the drawing, a double cylindrical pipe is adopted as an actual reforming pipe. With this configuration, when the aqueous methanol solution that is the raw fuel is vaporized and introduced from the inlet 3a of the reforming pipe 3, the hydrogen is reformed by steam by a contact reaction (endothermic reaction) with the reforming catalyst 4 filled in the pipe. Converted to rich reformed gas. Then, the reformed gas is supplied to the fuel cell in the subsequent stage through the outlet 3b of the reforming tube 3.
【0004】[0004]
【発明が解決しようとする課題】ところで、前記した従
来構造の燃料改質器をそのまま車両搭載型燃料電池発電
装置に組み込んで使用すると、車両の発進,走行,停止
に伴って燃料改質器には振動,揺れなどの繰り返し荷
重,衝撃荷重が加わるようになる。一方、燃料改質器の
改質管に充填した改質触媒には、粒径数mm程度の担体
(例えばアルミナ)の表面に微粒子の銅系触媒をバイン
ダで結着して担持させたものを用いている。このため
に、改質管内で拘束なしに充填した改質触媒に対し外部
から繰り返し荷重,衝撃荷重が加わると、その加振力に
よる粒状触媒の管内での揺動で触媒同士が擦られて触媒
微粒子が担体から剥離したり、触媒粒子が圧壊して粉化
が促進される。しかも、改質管内に触媒の粉体が生じる
と、粉体が触媒粒子間の空隙を埋めて管内を通流するガ
スの圧損増加を招くほか、粉体が改質管内を流れるガス
と一緒に改質器より流出して次第に触媒量が目減りし、
この結果として改質器の能力が次第に低下するようにな
る。さらに、改質器からの触媒粉体の流出量が増える
と、改質器と燃料電池とのガス導管に設けたフィルタの
目詰まりが早まって短期間周期でフィルタの交換が必要
となるなどの保守上の問題にも波及する。By the way, if the above-described conventional fuel reformer is used by incorporating it into a vehicle-mounted fuel cell power generator as it is, the fuel reformer is used as the vehicle starts, runs, or stops. Is subject to repeated loads such as vibration and shaking, and impact loads. On the other hand, for the reforming catalyst filled in the reforming tube of the fuel reformer, a carrier (for example, alumina) having a particle size of about several millimeters is supported by binding a particulate copper-based catalyst with a binder. I am using. Therefore, when a repetitive load or impact load is applied to the reforming catalyst filled in the reforming pipe without restraint from the outside, the catalyst is rubbed with each other due to the rocking of the granular catalyst in the pipe due to the vibrating force, and the catalyst is rubbed. The fine particles are separated from the carrier and the catalyst particles are crushed to promote pulverization. Moreover, when powder of the catalyst is generated in the reforming pipe, the powder fills the voids between the catalyst particles and causes an increase in pressure loss of the gas flowing through the pipe. The amount of catalyst gradually decreases as it flows out of the reformer,
As a result, the capacity of the reformer gradually decreases. Furthermore, when the outflow amount of the catalyst powder from the reformer increases, the filters provided in the gas conduits between the reformer and the fuel cell become prematurely clogged and the filters need to be replaced in a short period. It also affects maintenance problems.
【0005】本発明は上記の点にかんがみなされたもの
であり、その目的は改質管内に簡単な部材を追加装備す
ることで、外部から加わる振動などによって管内に充填
した改質触媒の粉化が軽減できるできるようにした、特
に車両搭載型燃料電池発電装置に好適な燃料改質器を提
供することにある。The present invention has been made in view of the above points, and an object thereof is to additionally equip a simple member in the reforming pipe so as to pulverize the reforming catalyst filled in the pipe by vibration applied from the outside. It is an object of the present invention to provide a fuel reformer, which is particularly suitable for a vehicle-mounted fuel cell power generation device, in which fuel consumption can be reduced.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明の燃料改質器においては、改質管内に充填す
る粒状の改質触媒をほぼ定量ずつ小分けにしてガス透過
性の可撓容器に充填し、該触媒入り容器を積層して改質
管内に装填して構成するものとする。そして、前記構成
における可撓容器にはステンレスなどの金属線で編んだ
網状ネットを採用することができ、かつ、前記網状ネッ
トには残余空隙を残すことなく粒状の改質触媒をタイト
に充填するのがよい。In order to solve the above-mentioned problems, in the fuel reformer of the present invention, the granular reforming catalyst to be filled in the reforming pipe is divided into substantially fixed amounts and gas permeability is improved. A flexible container is filled with the catalyst, and the catalyst-containing container is laminated and loaded in the reforming tube. A reticulated net braided with a metal wire such as stainless steel can be adopted for the flexible container in the above structure, and the reticulated net is tightly filled with a granular reforming catalyst without leaving a residual void. Is good.
【0007】[0007]
【作用】上記の構成によれば、改質管内に充填された粒
状触媒は、定量ずつ小分けにして網状ネットの容器内に
ぎっしり詰るようにタイトに充填されており、かつ該容
器は相互間でガタつきなしに積層して管内に装填されて
いる。したがって、外部から振動などが加わっても粒状
触媒は個々に流動して擦れ合ったり、衝突し合うことが
殆どなく、これにより触媒の粉化が軽減される。According to the above construction, the granular catalyst packed in the reforming tube is tightly packed into the container of the mesh net tightly so as to be packed into the container of the mesh net in a small amount. It is stacked in the tube without rattling. Therefore, even if vibration or the like is applied from the outside, the granular catalysts hardly flow individually and rub against each other or collide with each other, which reduces powdering of the catalyst.
【0008】[0008]
【実施例】図1は本発明の実施例を示すものであり、図
3に対応する同一部材には同じ符号が付してある。すな
わち、図1の構成においては、改質管3の内部に充填さ
れる改質触媒4が、あらかじめ略定量ずつ小分けにして
符号5で示す網状ネットとして作られた可撓容器に充填
され、かつこの触媒入りの網状ネット5を上下に積み上
げて改質管3の内部に装填されている。ここで、網状ネ
ット5は例えばステンレス鋼線で、その網目のメッシュ
を粒状触媒の粒径よりも小さく編んだ袋状のものであ
り、かつこの網状ネット5には改質触媒4がぎっしりと
詰るようにタイトに充填されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an embodiment of the present invention, in which the same members corresponding to those in FIG. That is, in the configuration of FIG. 1, the reforming catalyst 4 filled in the reforming pipe 3 is preliminarily subdivided into a flexible container made into a mesh net shown by reference numeral 5 and divided into substantially fixed amounts, and The mesh nets 5 containing the catalyst are vertically stacked and loaded inside the reforming pipe 3. Here, the reticulated net 5 is, for example, a stainless steel wire, is a bag-shaped mesh of the mesh of which is smaller than the particle size of the granular catalyst, and the reforming catalyst 4 is closely packed in the reticulated net 5. So tightly packed.
【0009】かかる構成により、車両の発進,走行,停
止に伴って振動などの繰り返し荷重,衝撃荷重が車両に
搭載した燃料改質器に加わっても、改質管内に充填され
た改質触媒4は網状ネット5の中に拘束され、かつ網状
ネットはネット同士の間でガタつきなしに管内に装填さ
れていので、改質触媒4が個々の粒子間で流動して擦れ
合ったり,衝突し合ったりすることが殆どなく、これに
より粒状触媒の振動による粉化を僅少に抑えることがで
きる。With such a structure, even if a repeated load such as vibration or a shock load is applied to the fuel reformer mounted on the vehicle when the vehicle starts, runs, or stops, the reforming catalyst 4 filled in the reforming pipe 4 Are restrained in the mesh net 5, and the mesh net is loaded in the tube without rattling between the nets, so that the reforming catalyst 4 flows between the individual particles and rubs or collides with each other. As a result, pulverization due to vibration of the granular catalyst can be suppressed to a small extent.
【0010】[0010]
【発明の効果】本発明の燃料改質器は、以上述べたよう
に構成されているので、特に車両搭載型燃料電池発電装
置に適用した場合でも、車両の発進,走行,停止に伴っ
て燃料改質器に加わる振動などで改質触媒が粉化するの
を軽減して改質触媒の長寿命化,並びに改質器能力の安
定維持が図れる。Since the fuel reformer of the present invention is configured as described above, even when it is applied to a vehicle-mounted fuel cell power generator, the fuel reformer can be used as the vehicle starts, runs, or stops. It is possible to reduce the pulverization of the reforming catalyst due to the vibration applied to the reformer, to prolong the life of the reforming catalyst and to maintain the reformer capacity stably.
【図1】本発明実施例の構成断面図FIG. 1 is a sectional view of the configuration of an embodiment of the present invention.
【図2】図1における網状ネット1個分の構造図FIG. 2 is a structural diagram of one mesh net in FIG.
【図3】燃料電池発電装置のシステムフロー図FIG. 3 is a system flow diagram of a fuel cell power generator.
【図4】従来における燃料改質器の構成断面図FIG. 4 is a sectional view showing the structure of a conventional fuel reformer.
1 炉本体 2 バーナ 3 改質管 4 改質触媒 5 網状ネット 1 furnace body 2 burner 3 reforming pipe 4 reforming catalyst 5 reticulated net
Claims (3)
改質管を収設し、該改質管に原燃料ガスを導入して水素
リッチな改質ガスを得る燃料改質器において、改質管内
に充填する粒状の改質触媒をほぼ定量ずつ小分けにして
ガス透過性の可撓容器に充填し、該触媒入り容器を積層
して改質管内に装填したことを特徴とする燃料改質器。1. A fuel reformer in which a reforming pipe filled with a reforming catalyst is housed in a furnace equipped with a burner, and a raw fuel gas is introduced into the reforming pipe to obtain a hydrogen-rich reformed gas. In the above, the granular reforming catalyst to be filled in the reforming pipe is subdivided into substantially fixed amounts and is filled in a gas-permeable flexible container, and the catalyst-containing container is stacked and loaded in the reforming pipe. Fuel reformer.
容器がステンレスなどの金属線で編んだ網状ネットであ
ることを特徴とする燃料改質器。2. The fuel reformer according to claim 1, wherein the flexible container is a mesh net woven with metal wires such as stainless steel.
触媒が可撓容器内にタイトに充填されていることを特徴
とする燃料改質器。3. The fuel reformer according to claim 1, wherein the reforming catalyst is tightly filled in the flexible container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3240050A JPH0576774A (en) | 1991-09-20 | 1991-09-20 | Fuel reformer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3240050A JPH0576774A (en) | 1991-09-20 | 1991-09-20 | Fuel reformer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0576774A true JPH0576774A (en) | 1993-03-30 |
Family
ID=17053735
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3240050A Pending JPH0576774A (en) | 1991-09-20 | 1991-09-20 | Fuel reformer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0576774A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100813244B1 (en) * | 2006-07-11 | 2008-03-13 | 삼성에스디아이 주식회사 | Reformer burner |
-
1991
- 1991-09-20 JP JP3240050A patent/JPH0576774A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100813244B1 (en) * | 2006-07-11 | 2008-03-13 | 삼성에스디아이 주식회사 | Reformer burner |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Gao et al. | Production of ammonia via a chemical looping process based on metal imides as nitrogen carriers | |
US6093501A (en) | Fuel cell using an aqueous hydrogen-generating process | |
US6875536B2 (en) | Catalytic hydrogen storage composite material and fuel cell employing same | |
KR100801861B1 (en) | A process for the autothermal catalytic steam reforming of hydrocarbons | |
US20160214858A1 (en) | Multi-zone dehydrogenation reactor and ballasting system for storage and delivery of hydrogen | |
WO2000048261A1 (en) | Carbon monoxide converting apparatus for fuel cell and generating system of fuel cell | |
JP2005230809A (en) | Composition and method for hydrogen storage and recovery | |
EP0637291A1 (en) | Improved hydrogen generating system. | |
EP2520674B1 (en) | Apparatus for manufacturing molten iron | |
WO2007032839A1 (en) | Hydrogen production and use in an internal combustion engine system | |
US7985704B2 (en) | Method of regenerating absorbent | |
WO2009087955A1 (en) | Cylindrical steam reformer | |
JPH0576774A (en) | Fuel reformer | |
Kato et al. | Study on a regenerative fuel reformer for a zero-emission vehicle system | |
JPH0576773A (en) | Fuel reformer for on-vehicle fuel cell generating equipment | |
EP1468722A2 (en) | System and method for reducing emissions from engines | |
KR100824527B1 (en) | Plate type preferential oxidation reactor | |
JPH0748101A (en) | Production of hydrogen-containing gas for fuel cell | |
JP4301362B2 (en) | Lower hydrocarbon direct cracking catalyst, lower hydrocarbon direct cracking reactor, and lower hydrocarbon direct cracking reactor | |
JPH07192746A (en) | Fuel cell power generating system | |
JP2002220202A (en) | Method of manufacturing hydrogen | |
Amin | Modelling and experimental study of methane catalytic cracking as a hydrogen production technology | |
JP2013079174A (en) | Hydrogen generator and fuel cell system | |
JPH0576775A (en) | Fuel reformer | |
JP4056773B2 (en) | Hydrogen generator and fuel cell power generation system |