JPH0645441B2 - Reformer - Google Patents

Reformer

Info

Publication number
JPH0645441B2
JPH0645441B2 JP59130009A JP13000984A JPH0645441B2 JP H0645441 B2 JPH0645441 B2 JP H0645441B2 JP 59130009 A JP59130009 A JP 59130009A JP 13000984 A JP13000984 A JP 13000984A JP H0645441 B2 JPH0645441 B2 JP H0645441B2
Authority
JP
Japan
Prior art keywords
combustion
catalyst
reforming
reformer
pipe
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.)
Expired - Fee Related
Application number
JP59130009A
Other languages
Japanese (ja)
Other versions
JPS6111134A (en
Inventor
長生 岡村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP59130009A priority Critical patent/JPH0645441B2/en
Publication of JPS6111134A publication Critical patent/JPS6111134A/en
Publication of JPH0645441B2 publication Critical patent/JPH0645441B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination 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
    • H01M8/0625Combination 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
    • H01M8/0631Reactor construction specially adapted for combination reactor/fuel cell
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は改質管の外側に高温燃焼ガスを流して改質管を
加熱することにより、原料ガスを水蒸気改質して改質ガ
スを得る改質装置の改良に関する。
Description: TECHNICAL FIELD OF THE INVENTION The present invention provides a reformed gas by steam reforming a raw material gas by flowing a high temperature combustion gas to the outside of the reforming tube to heat the reforming tube. The present invention relates to improvement of a reformer.

[発明の技術的背景] 第2図は、従来から用いられている二重管式の改質装置
の構成例を断面図にて示したものである。図において、
1は改質器容器、2は一端部(上端部)が密閉されると
共に内側管路と外側管路との間に改質触媒層3が設けら
れた断面環状の改質管であり、かかる改質管1が上記改
質器容器1の内部に複数本並べて配設されている。ま
た、上記改質器容器1の上部に取付けられた燃焼空気入
口管4および燃焼ガス入口管5から、燃焼器としての燃
焼バーナノズル6に燃焼用空気および燃焼ガスを夫々導
入して燃焼室7で燃焼させ、これにより得られる高温燃
焼ガスが上記改質管2の外側の目皿8上に設けられた伝
熱充填層9を通過することによって改質管2が加熱さ
れ、その後この高温燃焼ガスは排ガス出口管10から改
質器容器1外部に排出される。一方、上記改質管1の内
側に設けられた改質触媒層3には原料ガス入口管11を
通して水蒸気と共に原料ガスを導入し、これが改質触媒
層3で加熱されることによって改質ガスに生成し、これ
が改質管頂部12にて反転してリターンパス13を下降
する間に改質触媒層3に熱を与えて温度が低下し、その
後改質ガス出口管14から改質器容器1外部に排出され
る。また、上記複数本の改質管2はその他端部(下端
部)が管板15に取付けられ、かつこの管板15は断熱
材16を介して上記改質器容器1に設けた支持台17に
取付けられている。さらに、上記改質器容器1と上記高
温燃焼ガスの通路である伝熱充填層9との間には、熱の
逃げを少なくするために断熱層18を設けて保温するよ
うにしている。ここで、断熱層18の断熱材としてはレ
ンガ、セラミックウール、グラスウール等の種々の材料
を使用することが考えられるが、特にこの改質装置の起
動、停止が繁雑に行なわれるような場合には、レンガは
亀裂が入り易いことから使用することができず、主にセ
ラミックウール材が使用されている。なお、19は上記
伝熱充填層9の周囲に設けられた充填層円筒である。
[Technical Background of the Invention] FIG. 2 is a cross-sectional view showing an example of the configuration of a conventional double-tube reformer. In the figure,
Reference numeral 1 is a reformer vessel, 2 is a reforming tube having an annular cross section in which one end (upper end) is sealed and a reforming catalyst layer 3 is provided between an inner pipe line and an outer pipe line. A plurality of reforming tubes 1 are arranged side by side inside the reformer container 1. Combustion air and combustion gas are introduced into a combustion burner nozzle 6 as a combustor from a combustion air inlet pipe 4 and a combustion gas inlet pipe 5 attached to the upper part of the reformer vessel 1, respectively. The reforming tube 2 is heated by burning and the high temperature combustion gas obtained thereby passing through the heat transfer packing layer 9 provided on the outer plate 8 of the reforming tube 2, and thereafter the high temperature combustion gas is heated. Is discharged from the exhaust gas outlet pipe 10 to the outside of the reformer container 1. On the other hand, the raw material gas is introduced into the reforming catalyst layer 3 provided inside the reforming pipe 1 through the raw material gas inlet pipe 11 together with the steam, and the raw material gas is heated in the reforming catalyst layer 3 to form the reformed gas. The generated gas is inverted at the top 12 of the reforming tube and heats the reforming catalyst layer 3 while descending the return path 13 to lower the temperature, and then the reforming gas outlet pipe 14 is used to reform the reformer vessel 1. It is discharged to the outside. Further, the other ends (lower ends) of the plurality of reforming tubes 2 are attached to a tube sheet 15, and the tube sheet 15 is provided with a support stand 17 provided on the reformer container 1 via a heat insulating material 16. Installed on. Further, a heat insulating layer 18 is provided between the reformer vessel 1 and the heat transfer filling layer 9 which is a passage for the high temperature combustion gas to keep the heat therein. Here, as the heat insulating material of the heat insulating layer 18, it is conceivable to use various materials such as brick, ceramic wool, glass wool, etc., but especially when the starting and stopping of the reforming device is complicatedly performed. However, bricks cannot be used because they tend to crack, and ceramic wool materials are mainly used. Reference numeral 19 is a packed bed cylinder provided around the heat transfer packed bed 9.

[背景技術の問題点] ところでかかる構成の改質装置においては、燃焼空気入
口管4および燃焼ガス入口管5から燃焼バーナノズル6
に燃焼用空気および燃焼ガスを夫々導入し、これを燃焼
室7で燃焼させて高温燃焼ガスを得る場合に、燃焼ガス
が完全に燃焼しないで燃焼ガスの未燃分が出たり、ある
いは不完全燃焼によって生ずるNOX分などの多い燃焼
排ガスが生じることから、この燃焼排ガスを大気中に放
出したような場合には公害問題発生の原因となる。ま
た、燃焼ガスの完全な燃焼が行なわれないことから、改
質装置全体の改質効率が低下してしまうという問題があ
る。
[Problems of Background Art] In the reformer having such a configuration, the combustion air inlet pipe 4 and the combustion gas inlet pipe 5 through the combustion burner nozzle 6 are used.
When the combustion air and the combustion gas are introduced into the combustion chamber 7 and are burned in the combustion chamber 7 to obtain the high temperature combustion gas, the combustion gas does not completely burn and an unburned portion of the combustion gas appears or is incomplete. Since combustion exhaust gas containing a large amount of NOX, which is generated by combustion, is generated, when the combustion exhaust gas is released into the atmosphere, it causes a pollution problem. Further, since the combustion gas is not completely combusted, there is a problem that the reforming efficiency of the entire reformer is lowered.

[発明の目的] 本発明は上記のような問題を解決するために成されたも
ので、その目的は燃焼ガスを完全に燃焼させて未燃分や
NOXのない燃焼排ガスを得て公害問題の発生を未然に
防止すると共に極めて効率の良い改質を行なうことが可
能な改質装置を提供することにある。
[Object of the Invention] The present invention has been made to solve the above problems, and its purpose is to completely burn combustion gas to obtain combustion exhaust gas without unburned components and NOX, and to solve pollution problems. An object of the present invention is to provide a reforming device capable of preventing the occurrence of the generation and performing the reforming with extremely high efficiency.

[発明の概要] 上記の目的を達成するために本発明では、一端部が密閉
されると共に内側管路と外側管路との間に改質触媒層が
設けられた断面環状の複数本の改質管を改質器容器の内
部に配設し、燃焼ガスおよび燃焼用空気を燃焼器により
混合し改質器容器内部に形成された燃焼室で燃焼させて
得られる高温燃焼ガスを改質管の一端部よりその外側に
設けられた伝熱充填層を通して他端部より外部へ流出さ
せると共に、原料ガスを改質管の他端部より流入させ改
質触媒層を通して改質ガスとしさらにその一端部より内
側管路を通して他端部より流出させるように構成された
改質装置において、少なくとも伝熱充填層近傍部分が多
孔質部材から形成されると共に内部に燃焼触媒を収納し
てなる燃焼触媒収納部を改質器容器内部に設け、かつ燃
焼触媒収納部の燃焼触媒内に燃焼器を埋設し、さらに夫
々一端が改質器容器外部に通ずると共に他端が燃焼触媒
収納部に通じ、当該燃焼触媒収納部に対して燃焼触媒を
供給および排出する燃焼触媒供給管および排出管を設け
るようにしている。
[Summary of the Invention] In order to achieve the above-mentioned object, in the present invention, a plurality of modified pipes having an annular cross section in which one end is sealed and a reforming catalyst layer is provided between an inner pipe and an outer pipe. A high-quality combustion gas obtained by arranging a quality pipe inside a reformer container, mixing combustion gas and combustion air by a combustor, and combusting in a combustion chamber formed inside the reformer container While flowing out from the other end through the heat transfer packed layer provided outside the one end, the raw material gas is introduced from the other end of the reforming tube to form the reformed gas through the reforming catalyst layer, and one end thereof In a reformer configured so as to flow from the other end through the inner pipe from the other end, at least a portion near the heat transfer filling layer is formed of a porous member and a combustion catalyst is stored inside Part inside the reformer container and burning A combustor is embedded in the combustion catalyst of the catalyst storage unit, and one end of each is connected to the outside of the reformer container and the other end is connected to the combustion catalyst storage unit, and the combustion catalyst is supplied to and discharged from the combustion catalyst storage unit. A combustion catalyst supply pipe and an exhaust pipe are provided.

[発明の実施例] 以下、本発明を図面に示す一実施例について説明する。
第1図は、本発明による改質装置の構成例を断面図にて
示したもので、第2図と同一部分には同一符号を付して
その説明を省略し、ここでは異なる点についてのみ説明
する。つまり第1図においては、少なくとも前記伝熱充
填層9近傍部分が多孔質部材である円錐状の目皿20か
ら形成されると共に、内部に燃焼触媒21を収納してな
る燃焼触媒収納部としてのケース22を前記改質器容器
1内部の上方に設け、かつ上記ケース22の燃焼触媒2
1内に前記燃焼バーナノズル6を埋設している。また、
上記ケース22の上部には一端が上記改質器容器1外部
に通ずる燃焼触媒供給管23を接続すると共に、その下
部には同じく一端が上記改質器容器1外部に通ずる燃焼
触媒排出管24を接続して、上記ケース22内に燃焼触
媒を夫々供給および排出可能なように構成している。さ
らに、上記燃焼触媒供給管23上には触媒供給弁および
入口弁25および26を夫々設け、かつ上記燃焼触媒排
出管24上には触媒排出弁27を設けている。なお、上
記において目皿20は高温に耐え得るアルミナなどの耐
熱材から構成し、また燃焼触媒21はアルミナやセラミ
ックにプラチナなどを付着した触媒粒子から構成してい
る。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention shown in the drawings will be described below.
FIG. 1 is a sectional view showing a structural example of a reforming apparatus according to the present invention. The same parts as those in FIG. 2 are designated by the same reference numerals and the description thereof will be omitted. Here, only different points will be described. explain. That is, in FIG. 1, at least the portion in the vicinity of the heat transfer filling layer 9 is formed from the conical plate 20 that is a porous member, and the combustion catalyst 21 is housed therein as a combustion catalyst housing portion. A case 22 is provided above the inside of the reformer container 1, and the combustion catalyst 2 of the case 22 is provided.
The combustion burner nozzle 6 is embedded in the nozzle 1. Also,
A combustion catalyst supply pipe 23 whose one end communicates with the outside of the reformer container 1 is connected to the upper portion of the case 22, and a combustion catalyst discharge pipe 24 whose one end communicates with the outside of the reformer container 1 is connected to the lower portion thereof. The combustion catalyst is connected and connected to the case 22 so that the combustion catalyst can be supplied and discharged, respectively. Further, a catalyst supply valve and inlet valves 25 and 26 are provided on the combustion catalyst supply pipe 23, respectively, and a catalyst discharge valve 27 is provided on the combustion catalyst discharge pipe 24. In the above description, the plate 20 is made of a heat-resistant material such as alumina capable of withstanding high temperatures, and the combustion catalyst 21 is made of catalyst particles obtained by adhering platinum or the like to alumina or ceramic.

かかる構成の改質装置においては、伝熱充填層9近傍部
分が目皿20から形成されると共に、内部に燃焼触媒2
1を収納してなるケース22の燃焼触媒21内に燃焼バ
ーナノズル6を埋設していることにより、燃焼ガスおよ
び燃焼用空気は燃焼触媒21内で燃焼し、これにより得
られる高温燃焼ガスが目皿20から外部の燃焼室7に流
出することになる。これにより、燃焼ガスが完全に燃焼
できることから、従来のように燃焼ガスの未燃分が出た
り、あるいは不完全燃焼によって生ずるNOX分などの
多い燃焼排ガスが生じたりすることがなくなり、この燃
焼排ガスを大気中に放出したような場合においても公害
問題の発生を未然に防止することができる。また、燃焼
ガスの完全な燃焼が行なわれることから、極めて効率の
良い改質を行なうことが可能となる。さらに、上記ケー
ス22の上部には燃焼触媒供給管23を接続すると共
に、その下部には同じく燃焼触媒排出管24を接続し
て、上記ケース22内に燃焼触媒を夫々供給および排出
可能なようにしていることから、長期間の使用によって
燃焼触媒21が触媒としての効果が低下したような場合
には、燃焼触媒排出管24上に設けられた触媒排出弁2
7を開放してケース22内の燃焼触媒21を外部へ排出
し、かつ燃焼触媒供給管23上に設けられた触媒供給弁
25および入口弁26を開放して外部から上記で排出し
た量と同量あるいはこれと等価な新しい燃焼触媒を供給
することができる。これにより、装置内には新しい燃焼
触媒を逐次入れ換えて改質に使用することができるた
め、燃焼触媒の交換を容易にかつ運転中に行なうことが
でき、もって装置寿命を長期化することが可能となる。
さらにまた、改質装置を最初に燃焼を開始するときトー
チで燃焼触媒21を加熱することにより、容易に点火で
きるという利点も得られるものである。
In the reformer having such a configuration, the portion near the heat transfer packed layer 9 is formed from the mesh 20, and the combustion catalyst 2 is provided inside.
By embedding the combustion burner nozzle 6 in the combustion catalyst 21 of the case 22 that accommodates 1, the combustion gas and the combustion air are combusted in the combustion catalyst 21, and the high temperature combustion gas obtained by this burns out. It will flow from 20 to the external combustion chamber 7. As a result, since the combustion gas can be completely combusted, the unburned content of the combustion gas as in the prior art or the generation of combustion exhaust gas with a large amount of NOX generated due to incomplete combustion does not occur. It is possible to prevent the occurrence of pollution problems even when the air is released into the atmosphere. Further, since the combustion gas is completely combusted, it is possible to perform reforming with extremely high efficiency. Further, a combustion catalyst supply pipe 23 is connected to the upper portion of the case 22 and a combustion catalyst discharge pipe 24 is also connected to the lower portion thereof so that the combustion catalyst can be supplied to and discharged from the case 22, respectively. Therefore, when the combustion catalyst 21 is less effective as a catalyst due to long-term use, the catalyst discharge valve 2 provided on the combustion catalyst discharge pipe 24 is provided.
7 is opened to discharge the combustion catalyst 21 in the case 22 to the outside, and the catalyst supply valve 25 and the inlet valve 26 provided on the combustion catalyst supply pipe 23 are opened to the same amount as the amount discharged from the outside. It is possible to supply fresh combustion catalyst in quantity or equivalent. As a result, a new combustion catalyst can be sequentially replaced in the device and used for reforming, so that the combustion catalyst can be replaced easily and during operation, and the device life can be extended. Becomes
Furthermore, by heating the combustion catalyst 21 with the torch when the combustion is first started in the reformer, there is an advantage that ignition can be easily performed.

尚、上記実施例では燃焼触媒収納部の一部に目皿を用い
たが、これに限らず燃焼触媒収納部の少なくとも一部つ
まり伝熱充填層近傍部分を多孔質部材により形成するよ
うにすればよいものである。
Incidentally, in the above-mentioned embodiment, the perforated plate was used as a part of the combustion catalyst housing portion, but the present invention is not limited to this. It ’s good.

[発明の効果] 以上説明したように本発明によれば、少なくとも伝熱充
填層近傍部分が多孔質部材から形成されると共に内部に
燃焼触媒を収納してなる燃焼触媒収納部を改質器容器内
部に設け、かつ燃焼触媒収納部の燃焼触媒内に燃焼器を
埋設し、さらに夫々一端が改質器容器外部に通ずると共
に他端が燃焼触媒収納部に通じ、当該燃焼触媒収納部に
対して燃焼触媒を供給および排出する燃焼触媒供給管お
よび排出管を設けるようにしたので、燃焼ガスを完全に
燃焼させて未燃分やNOxのない燃焼排ガスを得て公害
問題の発生を未然に防止すると共に極めて効率の良い改
質を行ない、しかも燃焼触媒の交換を容易にかつ運転中
に行なうことが可能な信頼性の高い改質装置が提供でき
る。
[Effects of the Invention] As described above, according to the present invention, at least the portion in the vicinity of the heat transfer filling layer is formed of the porous member, and the combustion catalyst storage portion in which the combustion catalyst is stored is provided in the reformer container. A combustor is provided inside and the combustion catalyst is embedded in the combustion catalyst of the combustion catalyst storage portion. Further, one end of the combustion catalyst storage portion is connected to the outside of the reformer container and the other end of the combustion catalyst storage portion is connected to the combustion catalyst storage portion. Since the combustion catalyst supply pipe and the exhaust pipe for supplying and discharging the combustion catalyst are provided, the combustion gas is completely burned to obtain the combustion exhaust gas having no unburned components and NOx, thereby preventing the occurrence of pollution problems. At the same time, it is possible to provide a highly reliable reforming device that can perform reforming with extremely high efficiency and that can easily replace the combustion catalyst during operation.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施例を示す断面構成図、第2図は
従来の改質装置の構成を示す断面図である。 1……改質器容器、2……改質管、3……改質触媒層、
4……燃焼空気入口管、5……燃焼ガス入口管、6……
燃焼バーナノズル、7……燃焼室、8……目皿、9……
伝熱充填層、10……排ガス出口管、11……原料ガス
入口管、13……リターンパス、14……改質ガス出口
管、15……管板、16……断熱材、18……断熱層
(低温断熱層)、19……充填層円筒、20……目皿、
21……燃焼触媒、22……ケース、23……燃焼触媒
供給管、24……燃焼触媒排出管、25……触媒供給
弁、26……入口弁、27……触媒排出弁。
FIG. 1 is a cross sectional view showing an embodiment of the present invention, and FIG. 2 is a cross sectional view showing the structure of a conventional reformer. 1 ... reformer container, 2 ... reforming tube, 3 ... reforming catalyst layer,
4 ... Combustion air inlet pipe, 5 ... Combustion gas inlet pipe, 6 ...
Combustion burner nozzle, 7 ... Combustion chamber, 8 ... Eye plate, 9 ...
Heat transfer packed bed, 10 ... Exhaust gas outlet pipe, 11 ... Raw material gas inlet pipe, 13 ... Return path, 14 ... Reformed gas outlet pipe, 15 ... Tube plate, 16 ... Heat insulating material, 18 ... Heat insulation layer (low temperature heat insulation layer), 19 ... Packed bed cylinder, 20 ...
21 ... Combustion catalyst, 22 ... Case, 23 ... Combustion catalyst supply pipe, 24 ... Combustion catalyst discharge pipe, 25 ... Catalyst supply valve, 26 ... Inlet valve, 27 ... Catalyst discharge valve.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】一端部が密閉されると共に内側管路と外側
管路との間に改質触媒層が設けられた断面環状の複数本
の改質管を改質器容器の内部に配設し、燃焼ガスおよび
燃焼用空気を燃焼器により混合し前記改質器容器内部に
形成された燃焼室で燃焼させて得られる高温燃焼ガスを
前記改質管の一端部よりその外側に設けられた伝熱充填
層を通して他端部より外部へ流出させると共に、原料ガ
スを前記改質管の他端部より流入させ改質触媒層を通し
て改質ガスとしさらにその一端部より内側管路を通して
他端部より流出させるように構成された改質装置におい
て、 少なくとも前記伝熱充填層近傍部分が多孔質部材から形
成されると共に内部に燃焼触媒を収納してなる燃焼触媒
収納部を前記改質器容器内部に設け、 かつ前記燃焼触媒収納部の燃焼触媒内に前記燃焼器を埋
設し、 さらに、夫々一端が前記改質器容器外部に通ずると共に
他端が前記燃焼触媒収納部に通じ、当該燃焼触媒収納部
に対して燃焼触媒を供給および排出する燃焼触媒供給管
および排出管を設けるようにしたことを特徴とする改質
装置。
1. A plurality of reforming pipes each having an annular cross section, one end of which is hermetically sealed and a reforming catalyst layer is provided between an inner pipe and an outer pipe. The high-temperature combustion gas obtained by mixing the combustion gas and the combustion air with the combustor and combusting the mixture in the combustion chamber formed inside the reformer container is provided outside one end of the reformer pipe. The raw material gas is made to flow out from the other end through the heat transfer packed layer, and the raw material gas is made to flow in from the other end of the reforming pipe to form the reformed gas through the reforming catalyst layer and the other end is passed through the inner pipe line from the one end. In the reformer configured to allow more outflow, at least a portion near the heat transfer filling layer is formed of a porous member, and a combustion catalyst storage portion in which a combustion catalyst is stored is provided inside the reformer container. Is installed in the The combustor is embedded in the catalyst, and one end of the combustor communicates with the outside of the reformer container and the other end communicates with the combustion catalyst storage part, and the combustion catalyst is supplied to and discharged from the combustion catalyst storage part. A reforming device characterized in that a combustion catalyst supply pipe and an exhaust pipe are provided.
JP59130009A 1984-06-26 1984-06-26 Reformer Expired - Fee Related JPH0645441B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59130009A JPH0645441B2 (en) 1984-06-26 1984-06-26 Reformer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59130009A JPH0645441B2 (en) 1984-06-26 1984-06-26 Reformer

Publications (2)

Publication Number Publication Date
JPS6111134A JPS6111134A (en) 1986-01-18
JPH0645441B2 true JPH0645441B2 (en) 1994-06-15

Family

ID=15023888

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59130009A Expired - Fee Related JPH0645441B2 (en) 1984-06-26 1984-06-26 Reformer

Country Status (1)

Country Link
JP (1) JPH0645441B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58124534A (en) * 1982-01-22 1983-07-25 Mitsui Toatsu Chem Inc Endothermic reaction apparatus
JPS5978905A (en) * 1982-10-23 1984-05-08 Jgc Corp Steam reforming reactor

Also Published As

Publication number Publication date
JPS6111134A (en) 1986-01-18

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