JPH01317102A - Reforming apparatus - Google Patents

Reforming apparatus

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Publication number
JPH01317102A
JPH01317102A JP14771288A JP14771288A JPH01317102A JP H01317102 A JPH01317102 A JP H01317102A JP 14771288 A JP14771288 A JP 14771288A JP 14771288 A JP14771288 A JP 14771288A JP H01317102 A JPH01317102 A JP H01317102A
Authority
JP
Japan
Prior art keywords
combustion
reaction tube
tube
burner
reaction
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
Application number
JP14771288A
Other languages
Japanese (ja)
Inventor
Sadatoshi Takayanagi
高柳 貞敏
Hiroko Tsuji
辻 博子
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP14771288A priority Critical patent/JPH01317102A/en
Publication of JPH01317102A publication Critical patent/JPH01317102A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To suppress the heat loss from the surface of furnace and to uniformly heat the reaction tube by forming a combustion space between a reaction tube and a burner, dividing the space with flame guides to separate the reaction tubes from each other and pairing the reaction tube with the combustion space containing the burner. CONSTITUTION:The objective reforming apparatus for reforming a hydrocarbon fuel to a hydrogen-rich gas by steam-reforming is provided with ring-shaped reaction tubes 23... (composed of an inner tube 24, an intermediate tube 25 and an outer tube 26) acting also as a flow channel of combustion gas, combustion burners 27... (27a is burner nozzle) forming pairs with each of the above reaction tubes 23..., combustion spaces 32 formed between the reaction tubes 23 and the combustion burners 27 and flame guides 36... to devide the combustion space 32 corresponding to the reaction tube 23.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は複数個の反応管の均一加熱と装置の小形化を
はかった改質装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a reforming apparatus that uniformly heats a plurality of reaction tubes and is made smaller.

〔従来の技術〕[Conventional technology]

第3図は例えば特開昭60−103001号公報に示さ
れた従来の改質装置を示す断面図であり、第3図(4)
、@において、(1)は改質炉容器、(2)は充填材層
加熱部、(3)は二重触媒管の外管、(4)は耐火材、
(5)は排ガスダクト、(6)は二重触媒管の内管、(
7)はバーナ、(8)は空気箱、(9)は消炎整流格子
、QQは充填材(第4図中の(ト))を保持する網目状
板、(II)は燃焼空間にこでは竪形で排ガスが上方に
流れ、上部で反転して下方に流れるものを示したが、こ
の逆の形式のものでも、また横形のものでもよい)であ
る。
FIG. 3 is a sectional view showing a conventional reforming device disclosed in, for example, Japanese Patent Application Laid-Open No. 60-103001, and FIG. 3 (4)
, @, (1) is the reforming furnace vessel, (2) is the filler layer heating section, (3) is the outer tube of the double catalyst tube, (4) is the refractory material,
(5) is the exhaust gas duct, (6) is the inner pipe of the double catalyst tube, (
7) is the burner, (8) is the air box, (9) is the flame-extinguishing rectifying grid, QQ is the mesh plate that holds the filler ((g) in Figure 4), and (II) is the combustion space. Although the exhaust gas is shown as having a vertical shape and flowing upward, and then turning around at the top and flowing downward, it may also be in the opposite shape or horizontal.

第4図において(3)は触媒管、(へ)は充填材(融点
が1000℃以上の鉱物質のものが使用され、粒径は例
えば5〜110Inのものが使用される)を示す。
In FIG. 4, (3) indicates a catalyst tube, and (f) indicates a filler (a mineral material having a melting point of 1000 DEG C. or higher is used, and a particle size of, for example, 5 to 110 In is used).

次に動作について説明する。Next, the operation will be explained.

第3図に示す燃焼用空気箱(8)に供給された空気は、
バーナ(7)より噴射される燃料によって燃焼空間Oυ
にて燃焼する。一部子均一となり長くのびた火炎は、消
炎整流格子(9)により消火される。燃焼ガスは整流さ
れた後180°方向を変え、充填材層加熱部(2)へ向
う。
The air supplied to the combustion air box (8) shown in Figure 3 is
Combustion space Oυ due to fuel injected from burner (7)
Burn at. The flame, which has become partially uniform and extends for a long time, is extinguished by the flame-extinguishing rectifying grid (9). After being rectified, the combustion gas changes its direction by 180 degrees and heads toward the filler layer heating section (2).

充填材層加熱部では充填材(ト)の為、燃焼ガスのガス
流速が上昇し、良好かつ均一な熱伝達が確保される。
In the filler layer heating section, due to the filler (g), the gas flow rate of the combustion gas increases, ensuring good and uniform heat transfer.

燃焼ガスは網目状板(10を通過後、排出ダクト(5)
より排出される。燃焼空間(ロ)は耐火材(4)にて囲
まれており、消炎整流格子(9)及び二重触媒管頂部を
覆う充填材(至)の為に二重触媒管が直接火炎にさらさ
れることがなく、受ける熱負荷も均一にすることができ
る。従って、二重触媒管の安全性は高まり急速起動もで
きる。
After passing through the mesh plate (10), the combustion gas flows through the exhaust duct (5).
more excreted. The combustion space (B) is surrounded by a fireproof material (4), and the double catalyst tube is directly exposed to the flame due to the flame-extinguishing rectifier grid (9) and the filler material (to) that covers the top of the double catalyst tube. Therefore, the heat load received can be made uniform. Therefore, the safety of the double catalytic tube is increased and rapid startup is possible.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の改質装置は以上の様に構成されており、各バーナ
(7)の燃焼空間(ロ)が共通なため、燃焼空間(ロ)
内で燃焼ガスの対流がおこり、炉体表面からのヒートロ
スが大きい。
The conventional reformer is configured as described above, and since the combustion space (B) of each burner (7) is common, the combustion space (B)
Convection of combustion gas occurs within the furnace, resulting in large heat loss from the furnace surface.

この発明は上記の様な課題を解決するためになされたも
ので、炉体表面からのヒートロスを抑制するとともに反
応管を均一に加熱する装置を得ることを目的とする。
This invention was made to solve the above-mentioned problems, and aims to provide an apparatus that suppresses heat loss from the surface of a furnace body and uniformly heats a reaction tube.

〔課題を解決するための手段〕[Means to solve the problem]

この発明に係る装置は、反応管とバーナとの間に設けた
燃焼空間を、火炎ガイドによって各反応管毎に区切り反
応管とバーナを含む燃焼空間を1対にしたものである。
In the apparatus according to the present invention, a combustion space provided between a reaction tube and a burner is separated for each reaction tube by a flame guide, and a pair of combustion spaces including the reaction tube and the burner are formed.

〔作用〕[Effect]

この発明における改質装置は、火炎ガイドにより燃焼空
間が限定されることにより、火炎ガイド外側の空間が断
熱効果を待ち、炉体からのヒートロスが小さくなる。
In the reformer according to the present invention, since the combustion space is limited by the flame guide, the space outside the flame guide has an adiabatic effect, and heat loss from the furnace body is reduced.

また、火炎ガイドは燃焼ガスの整流効果があり、複数個
の反応管を均一に加熱することができる。
Further, the flame guide has a rectifying effect on combustion gas, and can uniformly heat a plurality of reaction tubes.

〔発明の実施例〕[Embodiments of the invention]

以下、この発明の一実施例を図について説明する。第1
図において、(ハ)は改質器容器、に)は容器断熱材、
(至)は反応管、(ハ)は内管、に)は中間管、に)は
外管、←カはバーナ、C27a)はバーナノズル、に)
は燃料箱、翰は空気箱、(ト)は充てん材、曽は充てん
材Coを保持する網目状板、(イ)は燃焼空間、器はバ
ーナに)で燃焼し内管(財)の中を通過して排ガスダク
l−、(財)は火炎、(至)はバーナ(イ)に点火する
ためのパイロットバーナ、・X+6)は火炎ガイドであ
る。
An embodiment of the present invention will be described below with reference to the drawings. 1st
In the figure, (c) is the reformer container, (b) is the container insulation material,
(to) is the reaction tube, (c) is the inner tube, ni) is the intermediate tube, ni) is the outer tube, ← is the burner, C27a) is the burner nozzle, ni)
is a fuel box, 翺 is an air box, (g) is a filling material, so is a mesh plate that holds the filling material Co, (b) is a combustion space, and a vessel is a burner). passing through the exhaust gas duct l-, (F) is the flame, (T) is the pilot burner for igniting the burner (A), and *X+6) is the flame guide.

第1図に示す燃料M■に供給された燃碍はバーナノズル
(27a) le通り空気箱(2)から供給される空気
と混合され燃焼空間に)で燃焼する。この時バーナノズ
ル(27a)は細いため火炎(財)は短い。このバーナ
ノズル(27a)は数十個集計して1つのバーナ(財)
を形成する。このバーナに)は内管(財)、中管(2)
、外管に)の3重管より成る反応管に)の下部に反応管
に)と対となるように配置しである。火炎ガイド側で限
定された空間内でバーナに)により燃焼した燃焼ガスは
3重管の中央を通り上部の排ガスダクト(イ)へ流れる
。この時、3重管の中央部の充てん材に)が加熱され、
その充てん材に)が反応管(至)の内管(ハ)へ熱を伝
える。
The fuel supplied to the fuel M shown in FIG. 1 is mixed with air supplied from the air box (2) through the burner nozzle (27a) and combusted in the combustion space. At this time, since the burner nozzle (27a) is thin, the flame is short. Dozens of these burner nozzles (27a) are combined into one burner (goods).
form. For this burner), the inner pipe (goods) and the middle pipe (2)
, in the outer tube), in the reaction tube consisting of triple tubes), and in the lower part of the reaction tube) are arranged so as to form a pair. The combustion gas combusted by the burner in a limited space on the flame guide side passes through the center of the triple pipe and flows to the upper exhaust gas duct (A). At this time, the filling material in the center of the triple pipe is heated,
The filling material) transfers heat to the inner tube (c) of the reaction tube (to).

この様な動作状態において、1対のバーナ(財)と反応
管に)は火炎ガイド図により形成された1個の燃焼空間
に)でつながれているため1つのバーナに)の燃焼ガス
はすべて1つの反応管(至)に供給される。
In this operating state, a pair of burners and a reaction tube are connected to one combustion space formed by the flame guide diagram, so all the combustion gas in one burner is 1 1 reaction tube (to).

従って同じ特性のバーナを用いれば各バーナに)により
得られる燃焼ガス量は各反応管に)の燃焼ガス通路の充
てん材に)の圧力損失差にのみ依存し、この充てん材(
7)の圧力損失が一定になるように調整すれば前記の燃
焼ガス量は同流量となり反応管(2)の均一加熱が可能
となる。
Therefore, if burners with the same characteristics are used, the amount of combustion gas obtained by each burner (in each reaction tube) depends only on the pressure drop difference between the filling material in the combustion gas passage (in each reaction tube);
If the pressure loss in step 7) is adjusted to be constant, the above-mentioned amount of combustion gas will be the same flow rate, making it possible to uniformly heat the reaction tube (2).

また、火炎ガイド−外側の空間が断熱効果を持つためヒ
ートロスが抑制され装置の効率を上げることが可能であ
る。
Furthermore, since the space outside the flame guide has a heat insulating effect, heat loss can be suppressed and the efficiency of the device can be increased.

上記実施例では反応管を上部に、バーナを下部に配置し
た場合を説明したが反応管を下部に、バーナを上部に配
置しても上記実施例と同様の効果を奏する。
In the above embodiment, a case has been described in which the reaction tube is arranged at the upper part and the burner is arranged at the lower part, but even if the reaction tube is arranged at the lower part and the burner is arranged at the upper part, the same effect as in the above embodiment can be obtained.

また、火炎ガイド外側の空間に断熱材を充填すれば更に
断熱効果が高まり、ヒートロスも小さくなる。
Furthermore, if the space outside the flame guide is filled with a heat insulating material, the heat insulation effect will be further enhanced and heat loss will be reduced.

〔発明の効果〕〔Effect of the invention〕

以上の様に、この発明によれば火炎ガイドにより複数個
の反応管に対応して燃焼空間を限定し区切ったので、炉
体表面からの放熱によるヒートロスが減少し、かつ、燃
焼ガスが整流され、各反応管の均一加熱も可能となる。
As described above, according to the present invention, since the combustion space is limited and divided according to the plurality of reaction tubes using the flame guide, heat loss due to heat radiation from the furnace surface is reduced, and the combustion gas is rectified. , uniform heating of each reaction tube is also possible.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の一実施例による改質装置の断面側面
図、第2図は第1図の反応管先端部の拡大図、第3図(
5)、@は従来の改質装置の断面側面図と断面平面図、
第4図は第3図の反応管先端部の拡大図である。 図において、に)は反応管、に)はバーナ、に)は燃焼
空間、(ト)は火炎ガイドである。 尚、図中同一符号は同−又は相当部分を示す。
FIG. 1 is a cross-sectional side view of a reformer according to an embodiment of the present invention, FIG. 2 is an enlarged view of the tip of the reaction tube in FIG.
5), @ is a cross-sectional side view and a cross-sectional plan view of a conventional reformer,
FIG. 4 is an enlarged view of the tip of the reaction tube in FIG. 3. In the figure, a) is a reaction tube, a) is a burner, a) is a combustion space, and a) is a flame guide. Note that the same reference numerals in the figures indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】[Claims] 炭化水素系燃料を水蒸気改良法により水素リッチガスに
改質する改質装置において、燃焼ガス流路を兼ねた環状
の反応管と、この反応管と対をなして配設された燃焼バ
ーナと、上記反応管と上記燃焼バーナとの間に設けられ
た燃焼空間と、この燃焼空間を上記反応管に対応して区
切るように設けられた火炎ガイドとを備えたことを特徴
とする改質装置。
A reformer for reforming hydrocarbon fuel into hydrogen-rich gas by a steam reforming method includes: an annular reaction tube that also serves as a combustion gas flow path; a combustion burner disposed in a pair with the reaction tube; A reformer comprising: a combustion space provided between a reaction tube and the combustion burner; and a flame guide provided to partition the combustion space in correspondence with the reaction tube.
JP14771288A 1988-06-14 1988-06-14 Reforming apparatus Pending JPH01317102A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14771288A JPH01317102A (en) 1988-06-14 1988-06-14 Reforming apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14771288A JPH01317102A (en) 1988-06-14 1988-06-14 Reforming apparatus

Publications (1)

Publication Number Publication Date
JPH01317102A true JPH01317102A (en) 1989-12-21

Family

ID=15436501

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14771288A Pending JPH01317102A (en) 1988-06-14 1988-06-14 Reforming apparatus

Country Status (1)

Country Link
JP (1) JPH01317102A (en)

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