JP2003212505A - Apparatus for producing hydrogen-containing gas and method of controlling quantity of production of hydrogen-containing gas - Google Patents

Apparatus for producing hydrogen-containing gas and method of controlling quantity of production of hydrogen-containing gas

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Publication number
JP2003212505A
JP2003212505A JP2002329655A JP2002329655A JP2003212505A JP 2003212505 A JP2003212505 A JP 2003212505A JP 2002329655 A JP2002329655 A JP 2002329655A JP 2002329655 A JP2002329655 A JP 2002329655A JP 2003212505 A JP2003212505 A JP 2003212505A
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JP
Japan
Prior art keywords
amount
steam
hydrogen
containing gas
raw fuel
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.)
Granted
Application number
JP2002329655A
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Japanese (ja)
Other versions
JP3986419B2 (en
Inventor
Susumu Takami
晋 高見
Satoshi Ibe
聰 伊部
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
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Priority to JP2002329655A priority Critical patent/JP3986419B2/en
Publication of JP2003212505A publication Critical patent/JP2003212505A/en
Application granted granted Critical
Publication of JP3986419B2 publication Critical patent/JP3986419B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To establish a technique to control the production quantity of a hydrogen-containing gas by which the quantity the hydrogen-containing gas is easily increased in a hydrogen-containing gas production apparatus provided with a steam production part for heating water by a steam production part heating means to produce steam and a reforming part for reforming the hydrocarbon-containing gas heated with a reforming part heating means by using steam produced in the steam production part. <P>SOLUTION: A treatment for increasing the quantity of the production of steam is carried out to increase the quantity of the production of steam in the steam production part before the supply quantity of the gaseous raw material to the reforming part is increased in order to increase the quantity of the production of the hydrogen-containing gas. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、水を水蒸気生成部
加熱手段で加熱して水蒸気を生成する水蒸気生成部と、
改質処理部加熱手段により加熱され、炭化水素系の原燃
料ガスを前記水蒸気生成部で生成した水蒸気を用いて改
質処理して水素含有ガスを生成する改質処理部と、前記
水蒸気生成部の水蒸気生成量を調整する水蒸気生成量調
整手段と、前記改質処理部への原燃料ガス供給量を調整
可能な原燃料ガス供給量調整手段と、前記水蒸気生成量
調整手段により前記水蒸気生成部での水蒸気生成量を調
整すると共に、前記原燃料ガス供給量調整手段により前
記改質処理部への原燃料ガス供給量を調整して、前記改
質処理部での水素含有ガス生成量を調整する水素含有ガ
ス生成量調整手段とを備えた水素含有ガス生成装置、及
びその水素含有ガス生成量調整方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam generating section for heating water with a steam generating section heating means to generate steam.
Reformation processing unit: A reforming processing unit that is heated by a heating unit and reforms a hydrocarbon-based raw fuel gas using the steam generated in the steam generation unit to generate a hydrogen-containing gas; and the steam generation unit. Water vapor generation amount adjusting means for adjusting the water vapor generation amount, raw fuel gas supply amount adjusting means capable of adjusting the raw fuel gas supply amount to the reforming processing unit, and the water vapor generating unit by the water vapor generation amount adjusting means. The amount of water vapor produced in the reforming unit and the amount of raw fuel gas supplied to the reforming unit are adjusted by the raw fuel gas supply amount adjusting means to adjust the amount of hydrogen-containing gas produced in the reforming unit. The present invention relates to a hydrogen-containing gas generation apparatus including a hydrogen-containing gas generation amount adjusting means, and a hydrogen-containing gas generation amount adjusting method thereof.

【0002】[0002]

【従来の技術】上記のような水素含有ガス生成装置は、
燃焼器等の改質処理部加熱手段により加熱され、原燃料
ガスに高温で水蒸気を加えて反応させる所謂水蒸気改質
処理を行なって、水素と一酸化炭素等を含む水素含有ガ
スを生成する改質処理部を備える。さらに、水素含有ガ
ス生成装置は、その改質処理部で生成された水素含有ガ
ス中の一酸化炭素を二酸化炭素に変成させることにより
変成処理する変成処理部や、その変成処理された水素含
有ガス中の一酸化炭素を選択酸化処理する一酸化炭素選
択酸化処理部等を備え、一酸化炭素濃度の極めて低い
(例えば10ppm以下)水素リッチな水素含有ガスを
生成するように構成され、このように生成された水素含
有ガスは、例えば、燃料電池における発電反応用の燃料
ガスとして用いられる。また、改質処理部に供給する水
蒸気は水蒸気生成部において生成されたものであり、水
蒸気生成部は、改質処理部に設けられた燃焼器から排出
される燃焼排ガスとの熱交換により水を加熱して水蒸気
を生成する熱交換器等により構成される(例えば、特許
文献1参照。)。
2. Description of the Related Art A hydrogen-containing gas generator as described above is
A reformer that generates hydrogen-containing gas containing hydrogen and carbon monoxide by performing a so-called steam reforming process in which steam is added to the raw fuel gas at a high temperature to cause a reaction by being heated by a reforming unit heating means such as a combustor. A quality processing unit is provided. Furthermore, the hydrogen-containing gas generation device is a shift treatment unit that shifts carbon monoxide in the hydrogen-containing gas generated in the reforming treatment unit to carbon dioxide, and the hydrogen-containing gas that has been subjected to the shift treatment. It is provided with a carbon monoxide selective oxidation treatment unit for selectively oxidizing carbon monoxide therein, and is configured to generate a hydrogen-rich hydrogen-containing gas having an extremely low carbon monoxide concentration (for example, 10 ppm or less). The generated hydrogen-containing gas is used, for example, as a fuel gas for a power generation reaction in a fuel cell. Further, the steam supplied to the reforming processing unit is generated in the steam generating unit, and the steam generating unit generates water by heat exchange with the combustion exhaust gas discharged from the combustor provided in the reforming processing unit. It is configured by a heat exchanger or the like that generates steam by heating (see, for example, Patent Document 1).

【0003】このような水素含有ガス生成装置は、燃料
電池の電力出力を電力負荷に追従させるために、燃料電
池の水素含有ガスの生成量を電力負荷に追従したものに
調整する水素含有ガス生成量調整手段を備える場合があ
る。そして、このような水素含有ガス生成量調整手段
は、改質処理部に水蒸気として供給される水分子のモル
数と原燃料ガスとして供給される炭素のモル数との比、
所謂スチーム/カーボン比を所定の値に維持しながら、
調整弁等で構成された上記原燃料ガス供給量調整手段に
より改質処理部への原燃料ガス供給量を調整すると共
に、水蒸気生成量調整手段により水蒸気生成部での水蒸
気生成量を調整するなどして、改質処理部への水蒸気供
給量とを調整し、結果、改質処理部における水素含有ガ
ス生成量を調整するように構成される。ちなみに、水蒸
気生成量調整手段は、水蒸気生成部への水供給量を調整
可能な水供給量調整手段や、入熱量を調整可能なように
構成された水蒸気生成部加熱手段にて構成され、水供給
量調整手段は具体的には調整弁等で構成される。
In such a hydrogen-containing gas generation device, in order to make the electric power output of the fuel cell follow the electric load, the hydrogen-containing gas generation is adjusted so that the amount of the hydrogen-containing gas produced by the fuel cell follows the electric load. It may be provided with a quantity adjusting means. Further, such a hydrogen-containing gas production amount adjusting means is a ratio of the number of moles of water molecules supplied as steam to the reforming processing section and the number of moles of carbon supplied as raw fuel gas,
While maintaining the so-called steam / carbon ratio at a predetermined value,
The raw fuel gas supply amount adjusting means composed of an adjusting valve or the like adjusts the raw fuel gas supply amount to the reforming processing unit, and the steam generation amount adjusting unit adjusts the steam generation amount in the steam generating unit. Then, the amount of steam supplied to the reforming treatment unit is adjusted, and as a result, the amount of hydrogen-containing gas produced in the reforming treatment unit is adjusted. By the way, the steam generation amount adjusting means is constituted by a water supply amount adjusting means capable of adjusting the water supply amount to the steam generating portion and a steam generating portion heating means configured so that the heat input amount can be adjusted. The supply amount adjusting means is specifically composed of an adjusting valve or the like.

【0004】[0004]

【特許文献1】特開2002−83620号公報[Patent Document 1] Japanese Unexamined Patent Publication No. 2002-83620

【0005】[0005]

【発明が解決しようとする課題】上記のような水素含有
ガス生成装置において、改質処理部で消費される水蒸気
量をできるだけ小さくして効率を向上するために、上記
スチーム/カーボン比をできるだけ小さくすることが求
められるが、スチーム/カーボン比が極端に低下した場
合には、充分な量の水素が生成されなくなったり、燃料
電池の燃料極に使用されている白金を被毒させる一酸化
炭素の生成量が増加してしまうという問題が生じる。
In the hydrogen-containing gas generator as described above, the steam / carbon ratio is made as small as possible in order to reduce the amount of water vapor consumed in the reforming section as much as possible and improve the efficiency. However, if the steam / carbon ratio is extremely reduced, a sufficient amount of hydrogen will not be produced, or carbon monoxide that poisons platinum used in the fuel electrode of the fuel cell There is a problem that the production amount increases.

【0006】特に、水素含有ガス生成量調整手段によ
り、燃料電池の電力負荷の増加等に追従させて、水素含
有ガス生成量を増加させる場合には、水蒸気生成部にお
ける水の蒸発の遅れや、水蒸気生成部の入熱量増加の遅
れや、水蒸気生成部への水供給量増加による水蒸気生成
部加熱手段の温度低下等により、一時的に改質処理部へ
の水蒸気供給量が改質処理部への原燃料ガスの供給量に
対して小さくなってしまうことがあり、例えば燃料電池
へ供給する水素含有ガスを上記電力負荷の増加に追従し
たものとすることができなかったり、燃料電池へ供給す
る水素含有ガス中の一酸化炭素が増加して燃料極の寿命
を縮めてしまうことがある。
In particular, when the hydrogen-containing gas production amount adjusting means is used to increase the hydrogen-containing gas production amount in accordance with an increase in the electric power load of the fuel cell or the like, there is a delay in water vaporization in the water vapor production section, Due to a delay in the increase in heat input to the steam generation unit or a decrease in the temperature of the steam generation unit heating means due to an increase in the amount of water supplied to the steam generation unit, the steam supply amount to the reforming processing unit is temporarily transferred to the reforming processing unit. The amount of raw fuel gas supplied to the fuel cell may be smaller than that of the original fuel gas. For example, the hydrogen-containing gas supplied to the fuel cell cannot be made to follow the increase in the electric power load, or is supplied to the fuel cell. Carbon monoxide in the hydrogen-containing gas may increase to shorten the life of the fuel electrode.

【0007】改質処理部への水蒸気供給量が原燃料ガス
の供給量に対して減少すると、水素含有ガス生成装置に
て生成される水素含有ガス中の一酸化炭素が増加する点
について説明を加える。改質処理部では、原燃料ガスが
例えばメタンガスの場合、下記の〔化1〕にて示される
反応式にて改質反応して、メタンガスが水素と一酸化炭
素を含む水素含有ガスに改質処理されるが、改質処理部
における改質反応は平衡反応であることから、同じ反応
温度、同じ反応圧力であれば、改質反応用の水蒸気の比
率が高いほど、生成される水素含有ガス中の一酸化炭素
の比率が低く、逆に、改質反応用の水蒸気の比率が低い
ほど、生成される水素含有ガス中の一酸化炭素の比率が
高くなる。従って、改質反応用の水蒸気の比率が一時的
に低下した場合には、改質処理部にて生成される水素含
有ガス中の一酸化炭素の比率も一時的に高くなることに
なる。
[0007] When the amount of steam supplied to the reforming processing unit decreases with respect to the amount of raw fuel gas supplied, the point that carbon monoxide in the hydrogen-containing gas produced by the hydrogen-containing gas generator increases will be explained. Add. In the reforming processing section, when the raw fuel gas is, for example, methane gas, a reforming reaction is performed according to the reaction formula shown in [Chemical formula 1] below, and the methane gas is reformed into a hydrogen-containing gas containing hydrogen and carbon monoxide. However, since the reforming reaction in the reforming processing section is an equilibrium reaction, the higher the ratio of steam for reforming reaction is, the more hydrogen-containing gas is produced at the same reaction temperature and the same reaction pressure. The lower the proportion of carbon monoxide in the interior and, conversely, the lower the proportion of steam for the reforming reaction, the higher the proportion of carbon monoxide in the hydrogen-containing gas produced. Therefore, when the ratio of steam for the reforming reaction is temporarily reduced, the ratio of carbon monoxide in the hydrogen-containing gas produced in the reforming processing unit is also temporarily increased.

【0008】[0008]

【化1】CH4+H2O→CO+3H2 [Chemical formula 1] CH 4 + H 2 O → CO + 3H 2

【0009】変成処理部では、下記の〔化2〕にて示さ
れる反応式にて変成反応して、改質処理部にて生成され
た水素含有ガス中の一酸化炭素が二酸化炭素に変成処理
されるが、変成処理部における変成反応は平衡反応であ
ることから、同じ反応温度であれば、水素含有ガス中の
水蒸気の比率が高いほど、二酸化炭素への変成比率が高
くなり、逆に、水素含有ガス中の水蒸気の比率が低いほ
ど、二酸化炭素への変成比率が低くなる。又、同様に、
同じ反応温度であれば、水素含有ガス中の一酸化炭素の
比率が低いほど、二酸化炭素への変成比率が高くなり、
逆に、水素含有ガス中の一酸化炭素の比率が高いほど、
二酸化炭素への変成比率が低くなる。従って、改質反応
用の水蒸気の比率が一時的に低下した場合には、前述の
ように、改質処理部にて生成された水素含有ガス中の一
酸化炭素の比率が一時的に増加すると共に、改質処理部
にて生成された水素含有ガス中の水蒸気の比率が一時的
に低下することから、変成処理部における一酸化炭素の
二酸化炭素への変成比率が一時的に低くなることにな
る。
In the shift conversion treatment section, a shift reaction is carried out according to the reaction formula shown in the following [Chemical formula 2], and carbon monoxide in the hydrogen-containing gas produced in the reforming treatment section is changed to carbon dioxide. However, since the shift reaction in the shift treatment section is an equilibrium reaction, at the same reaction temperature, the higher the ratio of water vapor in the hydrogen-containing gas, the higher the shift ratio to carbon dioxide, and vice versa. The lower the rate of water vapor in the hydrogen-containing gas, the lower the rate of conversion to carbon dioxide. Also, similarly,
At the same reaction temperature, the lower the ratio of carbon monoxide in the hydrogen-containing gas, the higher the conversion ratio to carbon dioxide,
Conversely, the higher the ratio of carbon monoxide in the hydrogen-containing gas,
The rate of conversion to carbon dioxide is low. Therefore, when the ratio of steam for the reforming reaction is temporarily decreased, the ratio of carbon monoxide in the hydrogen-containing gas generated in the reforming processing part is temporarily increased, as described above. At the same time, since the ratio of water vapor in the hydrogen-containing gas generated in the reforming processing unit temporarily decreases, the conversion ratio of carbon monoxide to carbon dioxide in the conversion processing unit temporarily decreases. Become.

【0010】[0010]

【化2】CO+H2O→CO2+H2 [Chemical formula 2] CO + H 2 O → CO 2 + H 2

【0011】選択酸化処理部では、下記の〔化3〕にて
示される反応式にて選択酸化反応して、変成処理部にて
変成処理された水素含有ガス中の一酸化炭素が二酸化炭
素に選択酸化されるが、選択酸化反応に必要な酸素は水
素含有ガス中の一酸化炭素が多いほど多くの量を必要と
する。従って、改質反応用の水蒸気の比率が一時的に低
下した場合には、前述のように、変成処理部にて変成処
理された水素含有ガス中の一酸化炭素の比率が一時的に
増加するため、選択酸化反応に必要な酸素量が不足する
ことにより、選択酸化処理部における一酸化炭素の選択
酸化比率が一時的に低くなることになる。
In the selective oxidation treatment section, the selective oxidation reaction is carried out according to the reaction formula shown in the following [Chemical formula 3], and carbon monoxide in the hydrogen-containing gas subjected to the shift treatment in the shift treatment section becomes carbon dioxide. Although it is selectively oxidized, more oxygen is required for the selective oxidation reaction as the amount of carbon monoxide in the hydrogen-containing gas increases. Therefore, when the ratio of the steam for the reforming reaction is temporarily decreased, the ratio of carbon monoxide in the hydrogen-containing gas subjected to the shift conversion treatment in the shift conversion treatment section is temporarily increased as described above. Therefore, the amount of oxygen required for the selective oxidation reaction is insufficient, so that the selective oxidation ratio of carbon monoxide in the selective oxidation treatment unit is temporarily reduced.

【0012】[0012]

【化3】CO+(1/2)O2→CO2 [Chemical Formula 3] CO + (1/2) O 2 → CO 2

【0013】上述のように、改質反応用の水蒸気の比率
が一時的に低下すると、改質処理部にて生成される水素
含有ガス中の一酸化炭素の比率が一時的に高くなると共
に、変成処理部における変成比率及び選択酸化処理部に
おける選択酸化比率が一時的に低くなることから、水素
含有ガス生成装置にて生成される水素含有ガス中の一酸
化炭素が一時的に増加することになる。
As described above, when the ratio of the steam for the reforming reaction is temporarily reduced, the ratio of carbon monoxide in the hydrogen-containing gas produced in the reforming treatment section is temporarily increased, and Since the conversion ratio in the shift conversion unit and the selective oxidation ratio in the selective oxidation unit are temporarily lowered, carbon monoxide in the hydrogen-containing gas generated by the hydrogen-containing gas generation device is temporarily increased. Become.

【0014】従って、本発明は、上記のような事情に鑑
みて、水素含有ガス生成装置において、良好に水素含有
ガス生成量を増加させることができる水素含有ガス生成
量調整技術を確立することを目的とする。
Therefore, in view of the above circumstances, the present invention aims to establish a hydrogen-containing gas production amount adjusting technique capable of satisfactorily increasing the hydrogen-containing gas production amount in a hydrogen-containing gas production apparatus. To aim.

【0015】[0015]

【課題を解決するための手段】〔構成1〕本発明に係る
水素含有ガス生成量調整方法は、請求項1に記載したご
とく、水素含有ガス生成装置において、前記水蒸気生成
部での水蒸気生成量と前記改質処理部への原燃料ガス供
給量とを調整して、前記改質処理部での水素含有ガス生
成量を調整する水素含有ガス生成量調整方法であって、
前記水素含有ガス生成量を増加させるに、前記改質処理
部への原燃料ガス供給量を増加させる時点より前に、前
記水蒸気生成部の水蒸気生成量を増加させるための水蒸
気生成量増加用処理を行うことを特徴とする。
[Means for Solving the Problems] [Structure 1] According to the method for adjusting the amount of hydrogen-containing gas generation according to the present invention, as described in claim 1, in the hydrogen-containing gas generator, the amount of water vapor generation in the water vapor generation unit. And a raw fuel gas supply amount to the reforming processing unit, a hydrogen-containing gas generation amount adjusting method for adjusting the hydrogen-containing gas generation amount in the reforming processing unit,
In order to increase the hydrogen-containing gas generation amount, a steam generation amount increasing process for increasing the steam generation amount of the steam generation unit before the time of increasing the raw fuel gas supply amount to the reforming processing unit. It is characterized by performing.

【0016】〔作用効果〕本構成の水素含有ガス生成量
調整方法によれば、例えば、燃料電池の電力負荷の増加
等に追従させて、改質処理部の水素含有ガス生成量を増
加させる場合において、水蒸気生成部の水蒸気生成量を
増加させるための水蒸気生成量増加用処理を行った後
に、改質処理部への原燃料ガス供給量を増加させるの
で、改質処理部への原燃料ガス供給量を増加させる時点
において、水蒸気生成部は既に改質処理部への水蒸気供
給量を増加させることができる状態となる。よって、改
質処理部への原燃料ガスの供給量が増加される時点で
は、改質処理部への水蒸気の供給量も増加されることに
なるので、一時的に改質処理部への水蒸気の供給量が改
質処理部への原燃料ガスの供給量に対して不足するのを
防止する、又は、一時的に改質処理部への水蒸気の供給
量が改質処理部への原燃料ガスの供給量に対して不足す
るにしてもその不足量を極力小さくすることが可能とな
り、改質処理部において一時的にスチーム/カーボン比
が極端に低下することを抑制して、水素含有ガス中の水
素量の低下及び一酸化炭素の増加を抑止することができ
る。
[Operation and Effect] According to the hydrogen-containing gas production amount adjusting method of the present configuration, for example, when the hydrogen-containing gas production amount of the reforming processing unit is increased by following the increase of the electric power load of the fuel cell and the like. In the above, since the raw fuel gas supply amount to the reforming processing unit is increased after performing the steam generation amount increasing process for increasing the steam generation amount of the steam generating unit, the raw fuel gas to the reforming processing unit is increased. At the time of increasing the supply amount, the steam generation unit is already in a state where the steam supply amount to the reforming processing unit can be increased. Therefore, at the time when the supply amount of the raw fuel gas to the reforming processing unit is increased, the supply amount of steam to the reforming processing unit is also increased. Of the raw fuel gas to the reforming processing unit is prevented from becoming insufficient with respect to the supply amount of the raw fuel gas to the reforming processing unit, or the supply amount of steam to the reforming processing unit is temporarily changed to the raw fuel to the reforming processing unit. Even if the amount of gas supplied is insufficient, the amount can be made as small as possible, and the steam / carbon ratio can be prevented from temporarily decreasing extremely in the reforming treatment section, and the hydrogen-containing gas can be prevented. A decrease in the amount of hydrogen in the inside and an increase in carbon monoxide can be suppressed.

【0017】〔構成2〕本発明に係る水素含有ガス生成
量調整方法は、請求項2に記載したごとく、上記構成1
の水素含有ガス生成量調整方法の構成に加えて、前記水
蒸気生成量増加用処理を、前記改質処理部への原燃料ガ
ス供給量を増加させるときに、その増加に見合う量の水
蒸気が生成されるように行うことを特徴とする。
[Structure 2] The method for adjusting the amount of hydrogen-containing gas generation according to the present invention, as described in claim 2, has the structure 1 described above.
In addition to the configuration of the method for adjusting the amount of hydrogen-containing gas generation, the process for increasing the amount of steam generation, when increasing the amount of raw fuel gas supplied to the reforming processing unit, generates an amount of steam commensurate with the increase. It is characterized by performing as described above.

【0018】〔作用効果〕本構成の水素含有ガス生成量
調整方法によれば、前記水蒸気生成量増加用処理を、前
記改質処理部への原燃料ガス供給量を増加させるとき
に、その増加に見合う量の水蒸気が生成されるように行
うので、改質処理部への原燃料ガスの供給量が増加され
ると、その増加量に見合う量の水蒸気が改質処理部に供
給されることになり、一時的に改質処理部への水蒸気供
給量が改質処理部への原燃料ガスの供給量に対して不足
することを防止することが可能となる。よって、一時的
な水素含有ガス中の水素量の低下及び一酸化炭素の増加
を一層抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas production amount adjusting method of the present configuration, the steam production amount increasing process is increased when increasing the raw fuel gas supply amount to the reforming processing unit. Therefore, when the amount of supply of the raw fuel gas to the reforming processing unit is increased, the amount of steam corresponding to the increased amount is supplied to the reforming processing unit. Therefore, it becomes possible to prevent the steam supply amount to the reforming processing unit from temporarily becoming insufficient with respect to the supply amount of the raw fuel gas to the reforming processing unit. Therefore, it is possible to further suppress the temporary decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0019】〔構成3〕本発明に係る水素含有ガス生成
量調整方法は、請求項3に記載したごとく、上記構成1
又は2の水素含有ガス生成量調整方法の構成に加えて、
前記水蒸気生成量増加用処理として、前記水蒸気生成部
加熱手段への入熱量を増加させる処理、及び、前記水蒸
気生成部への水供給量を増加させる処理の少なくとも一
方を行うことを特徴とする。
[Structure 3] The method for adjusting the amount of hydrogen-containing gas generation according to the present invention, as described in claim 3, has the structure 1 described above.
Or in addition to the configuration of the hydrogen-containing gas production amount adjustment method of 2,
As the steam generation amount increasing process, at least one of a process of increasing an amount of heat input to the steam generating unit heating unit and a process of increasing a water supply amount to the steam generating unit is performed.

【0020】〔作用効果〕本構成の水素含有ガス生成量
調整方法によれば、水蒸気生成量増加用処理として、水
蒸気生成部加熱手段への入熱量を増加させる処理、及
び、水蒸気生成部への水供給量を増加させる処理の少な
くとも一方を行うので、改質処理部への原燃料ガス供給
量を増加させる時点において、水蒸気生成部は既に改質
処理部への水蒸気供給量を増加させることができる状態
となり、上記の構成1によるのと同様の作用効果が得ら
れて、一時的な水素含有ガス中の水素量の低下及び一酸
化炭素の増加を抑止することができる。ちなみに、水蒸
気生成量増加用処理として、水蒸気生成部加熱手段への
入熱量を増加させる処理、及び、水蒸気生成部への水供
給量を増加させる処理の両方を行うと、つまり、改質処
理部への原燃料ガス供給量を増加させる時点より所定の
時間前に、水蒸気生成部への水供給量を増加させると共
に、その水供給量を増加させる時点より所定の時間前
に、水蒸気生成部加熱手段への入熱量を増加させるよう
にすると、水供給量を増加させる時点において、水蒸気
生成部は既に水供給量を増加させても充分な水蒸気を生
成することができる状態となっており、さらに、原燃料
ガスを増加させる時点において、水蒸気生成部は、その
増加する原燃料ガス供給量に対して充分な量の水蒸気を
供給することができる状態となる。よって、一時的な水
素含有ガス中の水素量の低下及び一酸化炭素の増加を一
層抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas production amount adjusting method of the present configuration, as the process for increasing the production amount of steam, the process of increasing the heat input to the steam producing unit heating means and the process of increasing the amount of heat input to the steam producing unit. Since at least one of the processes for increasing the water supply amount is performed, the steam generation unit may already increase the steam supply amount to the reforming treatment unit at the time of increasing the raw fuel gas supply amount to the reforming treatment unit. In this state, the same operational effects as those of the above-described configuration 1 are obtained, and it is possible to suppress a temporary decrease in the amount of hydrogen in the hydrogen-containing gas and an increase in carbon monoxide. By the way, as the process for increasing the steam generation amount, if both the process of increasing the heat input amount to the steam generating unit heating means and the process of increasing the water supply amount to the steam generating unit are performed, that is, the reforming processing unit Increase the amount of water supplied to the steam generator at a predetermined time before increasing the amount of raw fuel gas supplied to the steam generator, and heat the steam generator at a predetermined time before increasing the amount of water supply. If the amount of heat input to the means is increased, at the time of increasing the water supply amount, the steam generation unit is already in a state of being able to generate sufficient steam even if the water supply amount is increased. At the time of increasing the amount of raw fuel gas, the steam generator is in a state where it can supply a sufficient amount of steam to the increased amount of supply of raw fuel gas. Therefore, it is possible to further suppress the temporary decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0021】〔構成4〕本発明に係る水素含有ガス生成
量調整方法は、請求項4に記載したごとく、水素含有ガ
ス生成装置において、前記水蒸気生成部での水蒸気生成
量と前記改質処理部への原燃料ガス供給量とを調整し
て、前記改質処理部での水素含有ガス生成量を調整する
水素含有ガス生成量調整方法であって、前記水素含有ガ
ス生成量を増加させるに、前記水蒸気生成部の水蒸気生
成量を増加させるための水蒸気生成量増加用処理、及
び、前記改質処理部への原燃料ガス供給量を漸増させる
原燃料ガス供給量漸増処理を行うことを特徴とする。
[Structure 4] A hydrogen-containing gas generation amount adjusting method according to the present invention is, in the hydrogen-containing gas generating device, as described in claim 4, wherein the steam generation amount in the steam generating unit and the reforming treatment unit are the same. A method for adjusting the amount of hydrogen-containing gas produced in the reforming processing unit by adjusting the amount of raw fuel gas supplied to the reforming treatment unit, in order to increase the amount of hydrogen-containing gas produced, A steam generation increasing process for increasing the steam generation amount of the steam generating unit, and a raw fuel gas supply amount increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit. To do.

【0022】〔作用効果〕本構成の水素含有ガス生成量
調整方法によれば、例えば、燃料電池の電力負荷の増加
等に追従させて、改質処理部の水素含有ガス生成量を増
加させる場合において、前記水蒸気生成部の水蒸気生成
量を増加させるための水蒸気生成量増加用処理、及び、
前記改質処理部への原燃料ガス供給量を漸増させる原燃
料ガス供給量漸増処理を行うので、改質処理部への原燃
料ガス供給量の増加に対して、不足することなく、ある
いは、不足量を極力小さくしながら、改質処理部へ水蒸
気を供給することが可能となる。説明を加えると、水蒸
気生成量増加用処理により水蒸気生成部における水蒸気
生成量を増加させるに際しては、水蒸気生成量は漸増す
ることになるので、改質処理部への原燃料ガス供給量を
漸増させることにより、一時的に改質処理部への水蒸気
の供給量が改質処理部への原燃料ガスの供給量に対して
不足するのを防止する、又は、一時的に改質処理部への
水蒸気の供給量が改質処理部への原燃料ガスの供給量に
対して不足するにしてもその不足量を極力小さくするこ
とが可能となる。従って、改質処理部において一時的に
スチーム/カーボン比が極端に低下することを抑制し
て、水素含有ガス中の水素量の低下及び一酸化炭素の増
加を抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas production amount adjusting method of this configuration, for example, when the hydrogen-containing gas production amount of the reforming processing unit is increased by following an increase in the electric power load of the fuel cell, etc. In the above, in the steam generation amount increasing process for increasing the steam generation amount of the steam generation unit, and
Since the raw fuel gas supply amount gradually increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit is performed, an increase in the raw fuel gas supply amount to the reforming processing unit is not insufficient, or, It becomes possible to supply the steam to the reforming treatment unit while minimizing the deficiency. In addition, when the steam generation amount is increased by the steam generation amount increasing process, the steam generation amount is gradually increased. Therefore, the raw fuel gas supply amount to the reforming processing unit is gradually increased. This temporarily prevents the supply amount of steam to the reforming processing unit from becoming insufficient with respect to the supply amount of the raw fuel gas to the reforming processing unit, or temporarily prevents the supply of steam to the reforming processing unit. Even if the supply amount of water vapor is insufficient with respect to the supply amount of the raw fuel gas to the reforming processing unit, the insufficient amount can be minimized. Therefore, it is possible to suppress the steam / carbon ratio from temporarily decreasing extremely in the reforming treatment section, and to suppress the decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0023】〔構成5〕本発明の水素含有ガス生成装置
は、請求項5に記載したごとく、水を水蒸気生成部加熱
手段で加熱して水蒸気を生成する水蒸気生成部と、改質
処理部加熱手段により加熱され、炭化水素系の原燃料ガ
スを前記水蒸気生成部で生成した水蒸気を用いて改質処
理して水素含有ガスを生成する改質処理部と、前記水蒸
気生成部の水蒸気生成量を調整する水蒸気生成量調整手
段と、前記改質処理部への原燃料ガス供給量を調整可能
な原燃料ガス供給量調整手段と、前記水蒸気生成量調整
手段により前記水蒸気生成部での水蒸気生成量を調整す
ると共に、前記原燃料ガス供給量調整手段により前記改
質処理部への原燃料ガス供給量を調整して、前記改質処
理部での水素含有ガス生成量を調整する水素含有ガス生
成量調整手段とを備えた水素含有ガス生成装置であっ
て、前記水素含有ガス生成量調整手段が、前記水素含有
ガス生成量を増加させるに、前記原燃料ガス供給量調整
手段により前記改質処理部への原燃料ガス供給量を増加
させる時点より前に、前記水蒸気生成部の水蒸気生成量
を増加させるべく前記水蒸気生成量調整手段を作動させ
る水蒸気生成量増加用処理を行うように構成されている
ことを特徴とする。
[Structure 5] The hydrogen-containing gas generator according to the present invention, as described in claim 5, comprises: a steam generating part for heating water by the steam generating part heating means to generate steam; and a reforming process heating part. And a reforming treatment unit that reforms a hydrocarbon-based raw fuel gas using the steam produced in the steam producing unit to produce a hydrogen-containing gas, and a steam production amount of the steam producing unit. A steam generation amount adjusting unit for adjusting, a raw fuel gas supply amount adjusting unit capable of adjusting a raw fuel gas supply amount to the reforming processing unit, and a steam generation amount in the steam generating unit by the steam generation amount adjusting unit. And adjusting the raw fuel gas supply amount adjusting means to adjust the raw fuel gas supply amount to the reforming processing unit to adjust the hydrogen-containing gas generation amount in the reforming processing unit. Quantity adjustment means In the hydrogen-containing gas generation device, the hydrogen-containing gas generation amount adjusting means increases the hydrogen-containing gas generation amount by the raw fuel gas supply amount adjusting means to supply the raw fuel gas to the reforming processing unit. Before the time point of increasing the supply amount, it is configured to perform a steam generation amount increasing process for operating the steam generation amount adjusting means to increase the steam generation amount of the steam generation unit. .

【0024】〔作用効果〕本構成の水素含有ガス生成装
置によれば、水素含有ガス生成量調整手段により、例え
ば、燃料電池の電力負荷の増加等に追従させて、改質処
理部の水素含有ガス生成量を増加させる場合において、
水蒸気生成部の水蒸気生成量を増加させるべく水蒸気生
成量調整手段を作動させる水蒸気生成量増加用処理を行
った後に、原燃料ガス供給量調整手段により改質処理部
への原燃料ガス供給量を増加させるので、少なくとも改
質処理部への原燃料ガス供給量を増加させる時点におい
ては、水蒸気生成部は既に改質処理部への水蒸気供給量
を増加させることができる状態となる。よって、改質処
理部への原燃料ガスの供給量が増加される時点では,改
質処理部への水蒸気の供給量も増加されることになるの
で、一時的に改質処理部への水蒸気の供給量が改質処理
部への原燃料ガスの供給量に対して不足するのを防止す
る、又は、一時的に改質処理部への水蒸気の供給量が改
質処理部への原燃料ガスの供給量に対して不足するにし
てもその不足量を極力小さくすることが可能となり、改
質処理部において一時的にスチーム/カーボン比が極端
に低下することを抑制して、水素含有ガス中の水素量の
低下及び一酸化炭素の増加を抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas generation apparatus of the present configuration, the hydrogen-containing gas generation amount adjusting means causes the hydrogen-containing gas in the reforming processing unit to follow the increase in the electric power load of the fuel cell, for example. When increasing gas production,
After performing the process for increasing the amount of steam generation by operating the steam generation amount adjusting means to increase the amount of steam generation of the steam generating part, the raw fuel gas supply amount adjusting means adjusts the raw fuel gas supply amount to the reforming processing part. Since it is increased, at least at the time when the raw fuel gas supply amount to the reforming processing unit is increased, the steam generating unit is already in a state where the steam supply amount to the reforming processing unit can be increased. Therefore, when the supply amount of the raw fuel gas to the reforming processing unit is increased, the supply amount of steam to the reforming processing unit is also increased, so that the steam supply to the reforming processing unit is temporarily performed. Of the raw fuel gas to the reforming processing unit is prevented from becoming insufficient with respect to the supply amount of the raw fuel gas to the reforming processing unit, or the supply amount of steam to the reforming processing unit is temporarily changed to the raw fuel to the reforming processing unit. Even if the amount of gas supplied is insufficient, the amount can be made as small as possible, and the steam / carbon ratio can be prevented from temporarily decreasing extremely in the reforming treatment section, and the hydrogen-containing gas can be prevented. A decrease in the amount of hydrogen in the inside and an increase in carbon monoxide can be suppressed.

【0025】〔構成6〕本発明に係る水素含有ガス生成
装置は、請求項6に記載したごとく、上記構成5の水素
含有ガス生成装置の構成に加えて、前記水素含有ガス生
成量調整手段が、前記水蒸気生成量増加用処理を、前記
原燃料ガス供給量調整手段により前記改質処理部への原
燃料ガス供給量を増加させるときに、その増加に見合う
量の水蒸気が生成されるように、前記水蒸気生成量調整
手段を作動させるべく行うように構成されていることを
特徴とする。
[Structure 6] In the hydrogen-containing gas generator according to the present invention, as described in claim 6, in addition to the structure of the hydrogen-containing gas generator of Structure 5, the hydrogen-containing gas generation amount adjusting means is provided. In the process for increasing the amount of steam generation, when the amount of raw fuel gas supply to the reforming processing unit is increased by the raw fuel gas supply amount adjusting means, an amount of steam commensurate with the increase is generated. It is characterized in that it is configured to operate the water vapor production amount adjusting means.

【0026】〔作用効果〕本構成の水素含有ガス生成装
置によれば、水素含有ガス生成量調整手段により、前記
水蒸気生成量増加用処理を、前記改質処理部への原燃料
ガス供給量を増加させるときに、その増加に見合う量の
水蒸気が生成されるように、水蒸気生成量調整手段を作
動させるべく行うので、改質処理部への原燃料ガスの供
給量が増加されると、その増加量に見合う量の水蒸気が
改質処理部に供給されることになり、一時的に改質処理
部への水蒸気供給量が改質処理部への原燃料ガスの供給
量に対して不足することを防止することが可能となる。
よって、一時的な水素含有ガス中の水素量の低下及び一
酸化炭素の増加を一層抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas generation apparatus of the present configuration, the hydrogen-containing gas generation amount adjusting means performs the steam generation amount increasing process and the raw fuel gas supply amount to the reforming processing unit. When the supply amount of the raw fuel gas to the reforming processing part is increased, the steam generation amount adjusting means is operated so that the amount of steam corresponding to the increase is generated when the supply amount is increased. The amount of steam commensurate with the increase will be supplied to the reforming processing unit, and the amount of steam supply to the reforming processing unit will temporarily be insufficient with respect to the amount of raw fuel gas supplied to the reforming processing unit. It is possible to prevent this.
Therefore, it is possible to further suppress the temporary decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0027】〔構成7〕本発明の水素含有ガス生成装置
は、請求項7に記載したごとく、上記構成5又は6の水
素含有ガス生成装置の構成に加えて、前記水蒸気生成量
調整手段が、前記水蒸気生成部への水供給量を調整可能
な水供給量調整手段と、入熱量を調整可能なように構成
された前記水蒸気生成部加熱手段にて構成され、前記水
素含有ガス生成量調整手段が、前記水蒸気生成量増加用
処理として、前記水蒸気生成部加熱手段への入熱量を増
加させる処理、及び、前記水供給量調整手段により前記
水蒸気生成部への水供給量を増加させる処理の少なくと
も一方を行うように構成されていることを特徴とする。
[Structure 7] In the hydrogen-containing gas generator of the present invention, as described in claim 7, in addition to the structure of the hydrogen-containing gas generator of Structure 5 or 6, the water vapor production amount adjusting means includes: The water supply amount adjusting means capable of adjusting the water supply amount to the steam generating portion and the steam generating portion heating means configured to be able to adjust the heat input amount, and the hydrogen-containing gas generation amount adjusting means. However, as the steam generation amount increasing process, at least a process of increasing the heat input amount to the steam generating unit heating unit, and a process of increasing the water supply amount to the steam generating unit by the water supply amount adjusting unit. It is characterized in that it is configured to perform one.

【0028】〔作用効果〕本発明の水素含有ガス生成装
置によれば、水素含有ガス生成量調整手段により、水蒸
気生成量増加用処理として、水蒸気生成部加熱手段への
入熱量を増加させる処理、及び、水供給量調整手段によ
り水蒸気生成部への水供給量を増加させる処理の少なく
とも一方を行うので、改質処理部への原燃料ガス供給量
を増加させる時点において、水蒸気生成部は既に改質処
理部への水蒸気供給量を増加させることができる状態と
なり、上記の構成5によるのと同様の作用効果が得られ
て、一時的な水素含有ガス中の水素量の低下及び一酸化
炭素の増加を抑止することができる。ちなみに、水蒸気
生成量増加用処理として、水蒸気生成部加熱手段への入
熱量を増加させる処理、及び、水蒸気生成部への水供給
量を増加させる処理の両方を行うと、つまり、原燃料ガ
ス供給量調整手段により改質処理部への原燃料ガス供給
量を増加させる時点より所定の時間前に、水蒸気生成部
への水供給量を増加させると共に、その水供給量を増加
させる時点より所定の時間前に、水蒸気生成部加熱手段
への入熱量を増加させるようにすると、水供給量を増加
させる時点において、水蒸気生成部は既に水供給量を増
加させても充分な水蒸気を生成することができる状態と
なっており、さらに、原燃料ガスを増加させる時点にお
いて、水蒸気生成部は、その増加する原燃料ガス供給量
に対して充分な量の水蒸気を供給することができる状態
となる。よって、一時的な水素含有ガス中の水素量の低
下及び一酸化炭素の増加を一層抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas generator of the present invention, the hydrogen-containing gas production amount adjusting means increases the amount of heat input to the steam producing portion heating means as the steam production increasing treatment. Also, since at least one of the treatments for increasing the water supply amount to the steam generation unit is performed by the water supply amount adjusting means, at the time of increasing the raw fuel gas supply amount to the reforming treatment unit, the steam generation unit has already been modified. As a result, the amount of steam supplied to the quality treatment unit can be increased, and the same operational effect as that of the above-mentioned configuration 5 can be obtained, and the amount of hydrogen in the hydrogen-containing gas can be temporarily reduced and carbon monoxide can be reduced. The increase can be suppressed. By the way, as the process for increasing the amount of steam generation, if both the process of increasing the heat input to the steam generating unit heating means and the process of increasing the water supply amount to the steam generating unit are performed, that is, the raw fuel gas supply The amount of water supplied to the steam generation unit is increased at a predetermined time before the amount of raw fuel gas supplied to the reforming processing unit is increased by the amount adjusting means, and the amount of water supplied to the steam generation unit is increased from the time when the amount of water supply is increased to a predetermined amount. If the amount of heat input to the steam generator heating means is increased before the time, the steam generator can generate sufficient steam even when the water supply amount is already increased, at the time of increasing the water supply amount. In addition, when the raw fuel gas is increased, the steam generation unit can supply a sufficient amount of steam to the increased raw fuel gas supply amount. It made. Therefore, it is possible to further suppress the temporary decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0029】〔構成8〕本発明に係る水素含有ガス生成
装置は、請求項8に記載したごとく、上記構成7の水素
含有ガス生成装置の構成に加えて、前記改質処理部加熱
手段が、燃焼熱により前記改質処理部を加熱する燃焼器
で構成され、前記水蒸気生成部加熱手段が、前記燃焼器
から排出される燃焼排ガスとの熱交換により水を加熱す
る熱交換器と電気ヒータとで構成され、前記水素含有ガ
ス生成量調整手段が、前記電気ヒータの出力を増加させ
て前記水蒸気生成部加熱手段への入熱量を増加させるよ
うに構成されていることを特徴とする。
[Structure 8] In the hydrogen-containing gas generator according to the present invention, as described in claim 8, in addition to the structure of the hydrogen-containing gas generator in Structure 7, It is composed of a combustor that heats the reforming processing unit by combustion heat, and the steam generation unit heating means heats water by heat exchange with combustion exhaust gas discharged from the combustor, and an electric heater. The hydrogen-containing gas production amount adjusting means is configured to increase the output of the electric heater to increase the heat input amount to the steam generating part heating means.

【0030】〔作用効果〕水蒸気生成部加熱手段におい
て、改質処理部加熱手段としての燃焼器から排出される
燃焼排ガスと水とを熱交換器に供給して、水を燃焼排ガ
スとの熱交換により加熱する場合に、水蒸気生成部加熱
手段への入熱量を調整可能な入熱量調整手段を、燃焼器
から排出される燃焼排ガスの熱量を調整可能なものとし
て構成すると、改質処理部の水素含有ガス生成量を増加
させるべく原燃料ガス供給量を増加させる時点に対して
所定の時間前に行われる前記水蒸気生成部加熱手段への
入熱量の増加に伴って、改質処理部加熱手段としての燃
焼器の燃焼量を増加させる必要があり、改質処理部の温
度が異常に上昇することがある。
[Operation and Effect] In the steam generating part heating means, the combustion exhaust gas and water discharged from the combustor as the reforming treatment part heating means are supplied to the heat exchanger to exchange heat with the combustion exhaust gas. If the heat input amount adjusting means capable of adjusting the heat input amount to the steam generating part heating means is configured as the heat amount of the combustion exhaust gas discharged from the combustor to be adjusted by the Along with the increase in the heat input to the steam generator heating means performed a predetermined time before the time when the raw fuel gas supply quantity is increased to increase the contained gas generation quantity, the reforming processing section heating means is provided. It is necessary to increase the amount of combustion in the combustor, and the temperature of the reforming processing part may rise abnormally.

【0031】そこで、本構成の水素含有ガス生成装置に
よれば、水蒸気生成部加熱手段を、改質処理部加熱手段
としての燃焼器から排出され改質処理部の温度を所定の
温度に設定した後の燃焼排ガスとの熱交換により水を加
熱する熱交換器と電気ヒータにより構成すると共に、前
記入熱量調整手段を上記電気ヒータの出力を調整するこ
とで、水蒸気生成部加熱手段への入熱量を調整可能に構
成することができ、水素含有ガス生成量増加のために、
水蒸気生成部への水供給量を増加させる時点に対して所
定の時間前に、改質処理部加熱手段への入熱量を増加さ
せることなく、水蒸気生成部加熱手段への入熱量を増加
させることができ、改質処理部の異常昇温を防止するこ
とができる。
Therefore, according to the hydrogen-containing gas generating apparatus of this configuration, the steam generating section heating means is set to a predetermined temperature as the temperature of the reforming processing section discharged from the combustor as the reforming processing section heating means. A heat exchanger that heats water by heat exchange with the subsequent combustion exhaust gas and an electric heater, and the heat input amount adjusting means adjusts the output of the electric heater to input heat amount to the steam generator heating means. Can be configured to be adjustable, in order to increase the production amount of hydrogen-containing gas,
Increasing the heat input to the steam generating part heating means without increasing the heat input to the reforming processing part heating means at a predetermined time before the time of increasing the water supply amount to the steam generating part. Therefore, it is possible to prevent abnormal temperature rise in the reforming processing section.

【0032】〔構成9〕本発明の水素含有ガス生成装置
は、請求項9に記載したごとく、水を水蒸気生成部加熱
手段で加熱して水蒸気を生成する水蒸気生成部と、改質
処理部加熱手段により加熱され、炭化水素系の原燃料ガ
スを前記水蒸気生成部で生成した水蒸気を用いて改質処
理して水素含有ガスを生成する改質処理部と、前記水蒸
気生成部の水蒸気生成量を調整する水蒸気生成量調整手
段と、前記改質処理部への原燃料ガス供給量を調整可能
な原燃料ガス供給量調整手段と、前記水蒸気生成量調整
手段により前記水蒸気生成部での水蒸気生成量を調整す
ると共に、前記原燃料ガス供給量調整手段により前記改
質処理部への原燃料ガス供給量を調整して、前記改質処
理部での水素含有ガス生成量を調整する水素含有ガス生
成量調整手段とを備えた水素含有ガス生成装置であっ
て、前記水素含有ガス生成量調整手段が、前記水素含有
ガス生成量を増加させるに、前記水蒸気生成部の水蒸気
生成量を増加させるべく前記水蒸気生成量調整手段を作
動させる水蒸気生成量増加用処理、及び、前記原燃料ガ
ス供給量調整手段により前記改質処理部への原燃料ガス
供給量を漸増させる原燃料ガス供給量漸増処理を行うよ
うに構成されていることを特徴とする。
[Structure 9] A hydrogen-containing gas generator according to the present invention has a steam generating section for heating water by a steam generating section heating means to generate steam, and a heating for a reforming section. And a reforming treatment unit that reforms a hydrocarbon-based raw fuel gas using the steam produced in the steam producing unit to produce a hydrogen-containing gas, and a steam production amount of the steam producing unit. A steam generation amount adjusting unit for adjusting, a raw fuel gas supply amount adjusting unit capable of adjusting a raw fuel gas supply amount to the reforming processing unit, and a steam generation amount in the steam generating unit by the steam generation amount adjusting unit. And adjusting the raw fuel gas supply amount adjusting means to adjust the raw fuel gas supply amount to the reforming processing unit to adjust the hydrogen-containing gas generation amount in the reforming processing unit. Quantity adjustment means In the above hydrogen-containing gas generation device, the hydrogen-containing gas generation amount adjusting means increases the water-vapor generation amount of the water-vapor generating unit to increase the hydrogen-containing gas generation amount. It is configured to perform a steam generation amount increasing process to be operated and a raw fuel gas supply amount gradually increasing process to gradually increase the raw fuel gas supply amount to the reforming processing section by the raw fuel gas supply amount adjusting means. It is characterized by

【0033】〔作用効果〕本構成の水素含有ガス生成装
置によれば、水素含有ガス生成量調整手段により、例え
ば、燃料電池の電力負荷の増加等に追従させて、改質処
理部の水素含有ガス生成量を増加させる場合において、
水素含有ガス生成量調整手段により、水蒸気生成部の水
蒸気生成量を増加させるべく水蒸気生成量調整手段を作
動させる水蒸気生成量増加用処理、及び、原燃料ガス供
給量調整手段により改質処理部への原燃料ガス供給量を
漸増させる原燃料ガス供給量漸増処理を行うので、改質
処理部への原燃料ガス供給量の増加に対して、不足する
ことなく、あるいは、不足量を極力小さくしながら、改
質処理部へ水蒸気を供給することが可能となる。説明を
加えると、水蒸気生成量調整手段による水蒸気生成量増
加用処理により水蒸気生成部における水蒸気生成量を増
加させるに際しては、水蒸気生成量は漸増することにな
るので、原燃料ガス供給量調整手段により改質処理部へ
の原燃料ガス供給量を漸増させることにより、一時的に
改質処理部への原燃料ガスの供給量に対して改質処理部
への水蒸気の供給量が不足するのを防止する、又は、一
時的に改質処理部への原燃料ガスの供給量に対して改質
処理部への水蒸気の供給量が不足するにしても、その不
足量を極力少なくすることが可能となる。従って、改質
処理部において一時的にスチーム/カーボン比が極端に
低下することを抑制して、水素含有ガス中の水素量の低
下及び一酸化炭素の増加を抑止することができる。
[Operation and Effect] According to the hydrogen-containing gas generating apparatus of the present configuration, the hydrogen-containing gas generation amount adjusting means causes the hydrogen-containing gas in the reforming processing unit to follow the increase in the power load of the fuel cell, for example. When increasing gas production,
The hydrogen-containing gas production amount adjusting means operates the vapor production amount adjusting means to increase the vapor production amount of the water vapor producing portion, and the raw fuel gas supply amount adjusting means brings the reforming treatment portion to the reforming treatment portion. Since the raw fuel gas supply amount increasing process for gradually increasing the raw fuel gas supply amount is performed, the increase in the raw fuel gas supply amount to the reforming processing unit does not become insufficient, or the shortage amount is minimized. However, it becomes possible to supply the steam to the reforming processing section. In addition, when increasing the amount of steam generation in the steam generation unit by the steam generation amount increasing process by the steam generation amount adjusting means, the steam generation amount is gradually increased. By gradually increasing the amount of raw fuel gas supplied to the reforming processing unit, it is possible to temporarily prevent the amount of steam supplied to the reforming processing unit from becoming insufficient with respect to the amount of raw fuel gas supplied to the reforming processing unit. It is possible to prevent or even if the supply amount of steam to the reforming processing unit becomes temporarily short of the supply amount of the raw fuel gas to the reforming processing unit, the shortage amount can be minimized as much as possible. Becomes Therefore, it is possible to suppress the steam / carbon ratio from temporarily decreasing extremely in the reforming treatment section, and to suppress the decrease in the amount of hydrogen in the hydrogen-containing gas and the increase in carbon monoxide.

【0034】[0034]

【発明の実施の形態】本発明に係る水素含有ガス生成装
置(以下、本生成装置と呼ぶ。)の実施の形態につい
て、図面に基づいて説明する。図1に示すように、本生
成装置Pは、調整弁11(原燃料ガス供給量調整手段の
一例)による供給量調整を伴って供給される天然ガス等
の炭化水素系の原燃料ガスを脱硫処理する脱硫処理部1
と、供給される原料水を加熱して水蒸気を生成する水蒸
気生成部Sと、燃焼式の改質処理部加熱手段としての燃
焼器4にて加熱されて、脱硫処理部1から供給される脱
硫原燃料ガスを水蒸気生成部Sで生成された水蒸気を用
いて水素ガスと一酸化炭素ガスを含むガスに改質処理す
る改質処理部3と、改質処理部3から供給される改質処
理ガス中の一酸化炭素ガスを水蒸気を用いて二酸化炭素
ガスに変成させることにより変成処理する変成処理部5
と、その変成処理部5から供給される変成処理ガス中の
一酸化炭素ガスを選択酸化することにより選択酸化処理
する選択酸化処理部6と、本生成装置Pの運転を制御す
る制御部20を備えて構成して、一酸化炭素ガス濃度の
低い(例えば10ppm以下)水素リッチな水素含有ガ
スを生成するように構成してある。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of a hydrogen-containing gas generator according to the present invention (hereinafter referred to as the present generator) will be described with reference to the drawings. As shown in FIG. 1, the present production apparatus P desulfurizes a hydrocarbon-based raw fuel gas such as natural gas which is supplied with a supply amount adjustment by an adjusting valve 11 (an example of a raw fuel gas supply amount adjusting means). Desulfurization treatment section 1 to be treated
A steam generator S for heating the supplied raw material water to generate steam, and a desulfurizer supplied from the desulfurization processor 1 after being heated by the combustor 4 as a combustion-type reforming processor heating means. A reforming process section 3 for reforming the raw fuel gas into a gas containing hydrogen gas and carbon monoxide gas using the steam produced in the steam producing section S, and a reforming process supplied from the reforming process section 3. Metamorphism processing unit 5 for performing metamorphism processing by converting carbon monoxide gas in the gas into carbon dioxide gas using steam.
A selective oxidation treatment unit 6 for selectively oxidizing the carbon monoxide gas in the transformation treatment gas supplied from the transformation treatment unit 5; and a control unit 20 for controlling the operation of the generator P. It is configured so as to generate a hydrogen-containing gas rich in hydrogen with a low carbon monoxide gas concentration (for example, 10 ppm or less).

【0035】脱硫処理部1においては、例えば150〜
300°Cの範囲の脱硫処理温度で、脱硫触媒にて原燃
料ガス中の硫黄化合物が水素化され、その水素化物が酸
化亜鉛に吸着されて脱硫される。ちなみに、脱硫処理部
1における脱硫反応は発熱反応である。脱硫処理部1に
は、ニッケル−モリブデン系、クロム−モリブデン系な
どの水素化脱硫触媒の粒状成型体の多数が充填されてい
る。また、上記の脱硫処理温度は、制御部20により、
脱硫処理温度センサT1により脱硫処理温度を検出しな
がら、脱硫処理部1を加熱する脱硫処理部用ヒータ32
の出力を調整することで、維持されている。
In the desulfurization treatment section 1, for example, 150 to
At a desulfurization treatment temperature in the range of 300 ° C., the sulfur compound in the raw fuel gas is hydrogenated by the desulfurization catalyst, and the hydride is adsorbed by zinc oxide and desulfurized. By the way, the desulfurization reaction in the desulfurization treatment section 1 is an exothermic reaction. The desulfurization treatment section 1 is filled with a large number of granular molded bodies of a hydrodesulfurization catalyst such as a nickel-molybdenum system and a chromium-molybdenum system. The desulfurization treatment temperature is controlled by the controller 20.
The desulfurization treatment unit heater 32 that heats the desulfurization treatment unit 1 while detecting the desulfurization treatment temperature with the desulfurization treatment temperature sensor T1.
It is maintained by adjusting the output of.

【0036】改質処理部3においては、メタンガスを主
成分とする天然ガスが原燃料ガスである場合は、ルテニ
ウム、ニッケル、白金等の改質触媒の触媒作用により、
例えば600〜700°Cの範囲の改質処理温度の下
で、メタンガスと水蒸気とが下記の反応式[化4]にて
改質反応して、水素ガスと一酸化炭素ガスを含むガスに
改質処理される。ちなみに、改質処理部3における改質
反応は吸熱反応である。また、上記改質用触媒は、セラ
ミック製の多孔質粒状体に保持され、改質処理部3に
は、その多孔質粒状体の多数が充填されている。
In the reforming processing unit 3, when the natural gas containing methane gas as the main component is the raw fuel gas, the catalytic action of the reforming catalyst such as ruthenium, nickel, platinum, etc.
For example, under a reforming treatment temperature in the range of 600 to 700 ° C., methane gas and steam undergo a reforming reaction according to the following reaction formula [Chemical formula 4] to convert into a gas containing hydrogen gas and carbon monoxide gas. The quality is processed. By the way, the reforming reaction in the reforming processing section 3 is an endothermic reaction. Further, the reforming catalyst is held in a porous granular body made of ceramic, and the reforming treatment section 3 is filled with a large number of the porous granular bodies.

【0037】[0037]

【化4】CH4+H2O→CO+3H2 Embedded image CH 4 + H 2 O → CO + 3H 2

【0038】また、改質処理部3に設けられた燃焼器4
は、燃料電池Gから排出されたオフガスと原燃料ガスと
同じ天然ガスとの燃料が調整弁13による供給量調整を
伴って供給されると共に、その燃料を燃焼させるための
燃焼用空気が調整弁14による供給量調整を伴って供給
される。そして、上記の改質処理温度は、制御部20に
より、改質処理温度センサT3により改質処理温度を検
出しながら、調整弁13及び調整弁14の開度を調整し
て燃焼器4の燃焼量を調整することで、維持される。
Further, the combustor 4 provided in the reforming processing section 3
Is supplied with the fuel of off-gas discharged from the fuel cell G and the same natural gas as the raw fuel gas with the adjustment of the supply amount by the adjustment valve 13, and the combustion air for burning the fuel is adjusted by the adjustment valve. It is supplied with the supply amount adjustment by 14. The above-mentioned reforming treatment temperature is controlled by the control unit 20 while the reforming treatment temperature sensor T3 detects the reforming treatment temperature and the opening degree of the regulating valve 13 and the regulating valve 14 is adjusted to burn the combustor 4. It is maintained by adjusting the amount.

【0039】変成処理部5においては、改質処理ガス中
の一酸化炭素ガスと水蒸気とが、酸化鉄又は銅亜鉛の変
成触媒の触媒作用により、例えば150〜300°Cの
範囲の変成処理温度の下で、下記の反応式[化5]にて
変成反応して、一酸化炭素ガスが二酸化炭素ガスに変成
処理される。ちなみに、変成処理部5における変成反応
は発熱反応である。変成処理部5には、粒状成型体の多
数が充填されている。また、上記の変成処理温度は、制
御部20により、変成処理温度センサT5により変成処
理温度を検出しながら、変成処理部5を加熱する変成処
理部用ヒータ33の出力を調整することで、維持されて
いる。
In the shift treatment section 5, the carbon monoxide gas and the steam in the reforming treatment gas are subjected to the shift action temperature in the range of 150 to 300 ° C. by the catalytic action of the shift catalyst of iron oxide or copper zinc. Under the conditions, the carbon monoxide gas is converted into carbon dioxide gas by the conversion reaction according to the following reaction formula [Chemical formula 5]. By the way, the shift reaction in the shift processing unit 5 is an exothermic reaction. The transformation processing section 5 is filled with a large number of granular molded bodies. Further, the above-mentioned shift treatment temperature is maintained by adjusting the output of the shift treatment heater 33 that heats the shift treatment unit 5 while the control unit 20 detects the shift treatment temperature by the shift treatment temperature sensor T5. Has been done.

【0040】[0040]

【化5】CO+H2O→CO2+H2 [Chemical formula 5] CO + H 2 O → CO 2 + H 2

【0041】選択酸化処理部6においては、白金、ルテ
ニウム、ロジウム等の貴金属系の選択酸化触媒の触媒作
用によって、例えば80〜120°Cの範囲の選択酸化
処理温度の下で、変成処理ガス中に残っている一酸化炭
素ガスが選択酸化される。ちなみに、選択酸化処理部6
における酸化反応は発熱反応である。また、上記選択酸
化用触媒は、セラミック製の多孔質粒状体に保持され、
選択酸化処理部6には、その多孔質粒状体の多数が充填
されている。
In the selective oxidation treatment section 6, the catalytic treatment of the noble metal selective oxidation catalyst such as platinum, ruthenium, rhodium, etc., in the shift treatment gas under the selective oxidation treatment temperature in the range of 80 to 120 ° C. The remaining carbon monoxide gas is selectively oxidized. By the way, the selective oxidation treatment unit 6
The oxidation reaction in is an exothermic reaction. Also, the selective oxidation catalyst is retained in a porous granular body made of ceramic,
The selective oxidation treatment section 6 is filled with a large number of the porous particles.

【0042】そして、本生成装置Pにて生成された水素
含有ガスは燃料ガスとして、燃料電池Gに供給される。
燃料電池Gは、詳細な説明は省略するが、高分子膜を電
解質とする固体高分子型であり、本生成装置Pから供給
される燃料ガス中の水素と、ブロア(図示せず)から供
給される反応用空気中の酸素との電気化学反応により発
電するように構成してある。
Then, the hydrogen-containing gas produced by the production apparatus P is supplied to the fuel cell G as a fuel gas.
Although the detailed description is omitted, the fuel cell G is a solid polymer type having a polymer membrane as an electrolyte, and is supplied from hydrogen in the fuel gas supplied from the generator P and a blower (not shown). Power is generated by an electrochemical reaction with oxygen in the reaction air.

【0043】また、水蒸気生成部Sの水蒸気生成量を調
整する水蒸気生成量調整手段Vが設けられ、水蒸気生成
部Sには、燃焼器4から供給された改質処理温度以上の
高温の燃焼排ガスと、調整弁10(水供給量調整手段の
一例)による供給量調整を伴って供給された水との熱交
換を行ない、水蒸気を生成する熱交換器8が設けられて
いる。また、水蒸気生成部Sには、熱交換器8に供給さ
れる水を予熱可能な電気ヒータ7が設けられている。そ
して、上記熱交換器8と電気ヒータ7とを、水蒸気生成
部Sにおいて水を加熱する水蒸気生成部加熱手段9と呼
ぶ。そして、上記電気ヒータ7への電力供給を断続した
り、熱交換器8に供給される燃焼排ガスの熱量を調整す
ることにより、水蒸気生成部加熱手段9への入熱量が調
整可能なように構成されている。また、上記水蒸気生成
量調整手段Vは、水蒸気生成部Sへの水供給量を調整可
能な水供給量調整手段としての調整弁10と、上述のよ
うに入熱量を調整可能に構成された水蒸気生成部加熱手
段9にて構成されている。
Further, a steam production amount adjusting means V for adjusting the steam production amount of the steam production unit S is provided, and the steam production unit S is provided with combustion exhaust gas having a temperature higher than the reforming treatment temperature supplied from the combustor 4. And a heat exchanger 8 for generating water vapor by exchanging heat with the supplied water while adjusting the supply amount by the adjusting valve 10 (an example of water supply amount adjusting means). In addition, the steam generator S is provided with an electric heater 7 capable of preheating the water supplied to the heat exchanger 8. The heat exchanger 8 and the electric heater 7 are referred to as a steam generating unit heating means 9 for heating water in the steam generating unit S. The heat input to the steam generator heating means 9 can be adjusted by intermittently supplying power to the electric heater 7 or adjusting the heat quantity of the combustion exhaust gas supplied to the heat exchanger 8. Has been done. Further, the steam generation amount adjusting means V is a control valve 10 as a water supply amount adjusting means capable of adjusting the water supply amount to the steam generating portion S, and the steam configured to be able to adjust the heat input amount as described above. It is composed of the generator heating means 9.

【0044】上記のように構成された本生成装置Pは、
燃料電池Gの電力負荷に追従させて、水素含有ガス生成
量を調整可能な水素含有ガス生成量調整手段21を備え
て構成されている。即ち、制御部20の水素含有ガス生
成量調整手段21は、燃料電池G側等から入力された電
力負荷情報に基づいて、調整弁11を働かせて脱硫処理
部1への原燃料ガス供給量を調整し、本生成装置Pの水
蒸気含有ガス生成量を燃料電池G側の電力負荷に追従す
るものに調整する。さらに、水素含有ガス生成量調整手
段21は、このように脱硫処理部1への原燃料ガス供給
量を調整するときに、その原燃料ガス供給量に基づい
て、調整弁10を働かせて水蒸気生成部Sに供給する水
供給量を、その原燃料ガス供給量と水蒸気生成部Sの水
蒸気生成量の比が所定のスチーム/カーボン比となるよ
うに調整する。
The present generator P configured as described above is
The fuel cell G is configured to include a hydrogen-containing gas production amount adjusting means 21 capable of adjusting the hydrogen-containing gas production amount so as to follow the electric power load of the fuel cell G. That is, the hydrogen-containing gas production amount adjusting means 21 of the control unit 20 operates the adjustment valve 11 to adjust the raw fuel gas supply amount to the desulfurization processing unit 1 based on the power load information input from the fuel cell G side or the like. The amount of steam-containing gas produced by the production apparatus P is adjusted so as to follow the power load on the fuel cell G side. Further, when adjusting the amount of raw fuel gas supplied to the desulfurization processing unit 1 in this way, the hydrogen-containing gas production amount adjusting means 21 activates the adjustment valve 10 to generate steam based on the amount of raw fuel gas supplied. The amount of water supplied to the part S is adjusted so that the ratio of the amount of raw fuel gas supplied to the amount of steam generated in the steam generating part S becomes a predetermined steam / carbon ratio.

【0045】詳しくは、燃料電池G側の電力負荷が増加
した場合には、水素含有ガス生成量調整手段21は、脱
硫処理部1への原燃料ガス供給量を増加させると共に、
水蒸気生成部Sへ供給する水供給量を増加させて水蒸気
生成部Sの水蒸気生成量を増加させ、本生成装置Pの水
素含有ガス生成量を増加させて、燃料電池Gの出力を増
加させる。逆に、燃料電池G側の電力負荷が減少した場
合には、水素含有ガス生成量調整手段21は、脱硫処理
部1への原燃料ガス供給量を減少させると共に、水蒸気
生成部Sへ供給する水供給量を減少させて水蒸気生成部
Sの水蒸気生成量を減少させ、本生成装置Pの水素含有
ガス生成量を減少させて、燃料電池Gの出力を減少させ
る。
More specifically, when the electric power load on the fuel cell G side increases, the hydrogen-containing gas production amount adjusting means 21 increases the raw fuel gas supply amount to the desulfurization treatment section 1, and
The amount of water supplied to the steam generation unit S is increased to increase the amount of steam generation of the steam generation unit S, the amount of hydrogen-containing gas generation of the present generation device P is increased, and the output of the fuel cell G is increased. On the contrary, when the electric power load on the fuel cell G side decreases, the hydrogen-containing gas production amount adjusting means 21 reduces the raw fuel gas supply amount to the desulfurization treatment unit 1 and supplies the raw fuel gas to the steam generation unit S. The amount of water supply is reduced to reduce the amount of water vapor produced by the water vapor producing unit S, the amount of hydrogen-containing gas produced by the production apparatus P is reduced, and the output of the fuel cell G is reduced.

【0046】また、水素含有ガス生成量調整手段21に
より原燃料ガス供給量を変化させた場合には、改質処理
部3に処理負荷が変化するので、改質処理温度センサT
3の検出結果に基づいて制御部20により調整される調
整弁13,14の開度は変化し、燃焼器4の燃料量も変
化する。即ち、原燃料ガス供給量を増加させると、燃焼
器4の燃焼量も増加し、逆に、原燃料ガス供給量が減少
すると、燃焼器4の燃焼量も減少する。さらに、燃焼器
4の燃焼量が変化した場合には、燃焼器4から排出され
る燃焼排ガスの熱量も変化するので、その燃焼排ガスが
供給される水蒸気生成部加熱手段9への入熱量も変化す
る。
Further, when the raw fuel gas supply amount is changed by the hydrogen-containing gas production amount adjusting means 21, the processing load on the reforming processing unit 3 changes, so the reforming processing temperature sensor T
The opening degree of the adjusting valves 13 and 14 adjusted by the control unit 20 based on the detection result of No. 3 changes, and the fuel amount of the combustor 4 also changes. That is, when the raw fuel gas supply amount is increased, the combustion amount of the combustor 4 also increases, and conversely, when the raw fuel gas supply amount decreases, the combustion amount of the combustor 4 also decreases. Furthermore, when the combustion amount of the combustor 4 changes, the heat amount of the combustion exhaust gas discharged from the combustor 4 also changes, so the heat input amount to the steam generating unit heating means 9 to which the combustion exhaust gas is supplied also changes. To do.

【0047】これまで説明してきた本生成装置Pの水素
含有ガス生成量調整手段21における水素含有ガス生成
量調整方法は、水素含有ガス生成量を増加させるときの
制御手順に特徴を有し、その詳細な実施例について以下
に説明する。尚、図2,図3,図4,図5は、水素含有
ガス生成量を増加させるときの、原燃料ガス供給量の増
加状態(a)、水蒸気生成部Sへの水供給量の増加状態
(b)、水蒸気生成部加熱手段9への入熱量の増加状態
(c)、水蒸気生成部Sの水蒸気生成量の増加状態
(d)とを示す図であり、図中において右方向に向って
時間が経過している。
The hydrogen-containing gas production amount adjusting method in the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P, which has been described so far, is characterized by the control procedure for increasing the hydrogen-containing gas production amount. Detailed examples will be described below. 2, FIG. 3, FIG. 4, and FIG. 5 show an increasing state (a) of the raw fuel gas supply amount and an increasing state of the water supply amount to the steam generation part S when increasing the hydrogen-containing gas generation amount. (B) is a diagram showing an increasing state (c) of the heat input to the steam generating part heating means 9 and an increasing state (d) of the steam generating amount of the steam generating part S, and is directed to the right in the figure. Time has passed.

【0048】〔実施例1〕この実施例1においては、水
素含有ガス生成量調整手段21が、本生成装置Pが水素
含有ガス生成量を増加させるために前記水素含有ガス生
成量を増加させるに、調整弁11により改質処理部3へ
の原燃料ガス供給量を増加させる時点より前に、水蒸気
生成部Pの水蒸気生成量を増加させるべく水蒸気生成量
調整手段Vを作動させる水蒸気生成量増加用処理を行う
ように構成され、更に、水素含有ガス生成量調整手段2
1が、水蒸気生成量増加用処理を、調整弁11により改
質処理部3への原燃料ガス供給量を増加させるときに、
その増加に見合う量の水蒸気が生成されるように、水蒸
気生成量調整手段Vを作動させるべく行うように構成さ
れている。
[Embodiment 1] In Embodiment 1, the hydrogen-containing gas production amount adjusting means 21 increases the hydrogen-containing gas production amount in order for the production apparatus P to increase the hydrogen-containing gas production amount. , Increasing the amount of steam generation by operating the steam generation amount adjusting means V to increase the amount of steam generation of the steam generation unit P before the time when the amount of raw fuel gas supplied to the reforming processing unit 3 is increased by the adjustment valve 11. And a hydrogen-containing gas production amount adjusting means 2
When the control valve 11 increases the amount of raw fuel gas supplied to the reforming processing unit 3 by the steam generation amount increasing process,
It is configured to operate the steam generation amount adjusting means V so that the amount of steam corresponding to the increase is generated.

【0049】上述のように水素含有ガス生成量調整手段
21が構成される場合の一例として、図2に示すよう
に、水素含有ガス生成量調整手段21が、調整弁11に
より原燃料ガス供給量を増加させるに、その原燃料ガス
供給量増加時点よりも所定の時間前に調整弁10により
水蒸気生成部Sへの水供給量を増加させるように構成さ
れる場合について説明する。このような場合には、水蒸
気生成部Sへの水供給量を増加させる時点の水蒸気生成
部加熱手段9への入熱量、即ち、燃焼器4から熱交換器
8に供給される燃焼排ガス中の熱量が、供給される水を
加熱して水蒸気とするのに充分な量である場合には、図
2(d)に示すように、原燃料ガス供給量を増加させる
時点では、既に水蒸気生成部Sの水蒸気生成量が増加さ
れ、増加した原燃料ガスに対して充分な水蒸気を改質処
理部3に供給することができる。また、この場合、水蒸
気生成部加熱手段9の入熱量は、燃焼器4の燃料量が増
加して熱交換器8に供給される燃焼排ガス中の熱量を増
加させることで増加するので、原燃料ガス供給量の増加
した時点で増加することになる。
As an example of the case where the hydrogen-containing gas production amount adjusting means 21 is configured as described above, as shown in FIG. 2, the hydrogen-containing gas production amount adjusting means 21 uses the adjustment valve 11 to supply the raw fuel gas. A case will be described in which the control valve 10 increases the water supply amount to the water vapor generation unit S a predetermined time before the point at which the raw fuel gas supply amount increases. In such a case, the amount of heat input to the steam generator heating means 9 at the time of increasing the amount of water supplied to the steam generator S, that is, the amount of heat in the combustion exhaust gas supplied from the combustor 4 to the heat exchanger 8. When the amount of heat is sufficient to heat the supplied water to steam, as shown in FIG. 2 (d), at the time when the raw fuel gas supply amount is increased, the steam generator is already in use. The steam generation amount of S is increased, and sufficient steam can be supplied to the reforming processing unit 3 with respect to the increased raw fuel gas. Further, in this case, the heat input amount of the steam generating unit heating means 9 increases as the fuel amount of the combustor 4 increases and the heat amount in the combustion exhaust gas supplied to the heat exchanger 8 increases. It will increase when the gas supply increases.

【0050】よって、本生成装置Pの水素含有ガス生成
量調整手段21は、水素含有ガス生成量を増加させる
に、水蒸気生成部Sへの水供給量を増加させてから、所
定の時間経過後に、原燃料ガス供給量を増加させること
で、改質処理部3への水蒸気供給量不足による一酸化炭
素生成量増加を抑制することができる。一方、図2
(b)に破線で示すように、従来のように水供給量の増
加を、原燃料ガス供給量を増加させる時点で行なった場
合では、図2(d)に破線で示すように、原燃料ガス供
給量を増加させる時点から、水蒸気生成量が徐々に増加
するので、改質処理部3において、一時的に原燃料ガス
供給量増加時点では水蒸気量が不足して、一時的に一酸
化炭素生成量が増加する。そして、このような本生成装
置Pの水素含有ガス生成量調整手段21においては、例
えば、図7に示すように、従来のように原燃料ガス供給
量増加と水供給量増加とを同時に増加させた場合(図7
の比較例)と比較して、原燃料ガス供給量増加時点に対
して30秒前に水供給量を増加させた場合(図7の実施
例1a)には、一酸化炭素生成量が増加する時間が半減
し、さらに、原燃料ガス供給量増加時点に対して1分前
に水供給量を増加させた場合(図7の実施例1b)に
は、殆ど一酸化炭素は生成されないことが実験により確
認された。尚、図7は、定格負荷が4.2L/min
(Normal)(天然ガス系都市ガス13A)の水素
含有ガス生成装置において、負荷を50%から100%
まで瞬時に増加させた場合に生成された水素含有ガス中
の一酸化炭素濃度を計測した結果である。
Therefore, the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P increases the hydrogen-containing gas production amount, after increasing the water supply amount to the steam production unit S, and after a predetermined time elapses. By increasing the raw fuel gas supply amount, it is possible to suppress an increase in the carbon monoxide production amount due to the insufficient steam supply amount to the reforming processing unit 3. On the other hand, FIG.
As shown by the broken line in (b), when the water supply amount is increased as in the conventional case at the time when the raw fuel gas supply amount is increased, as shown by the broken line in FIG. Since the steam generation amount gradually increases from the time when the gas supply amount is increased, the steam amount is temporarily insufficient in the reforming processing unit 3 at the time when the raw fuel gas supply amount is increased, and the carbon monoxide is temporarily increased. The production amount increases. Then, in the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P as described above, for example, as shown in FIG. 7, the raw fuel gas supply amount and the water supply amount are simultaneously increased as in the conventional case. (Fig. 7
Comparative Example), the carbon monoxide production amount increases when the water supply amount is increased 30 seconds before the raw fuel gas supply amount is increased (Example 1a in FIG. 7). Experiments have shown that when the time is halved and the water supply amount is increased 1 minute before the raw fuel gas supply amount is increased (Example 1b in FIG. 7), almost no carbon monoxide is produced. Confirmed by. In addition, in FIG. 7, the rated load is 4.2 L / min.
(Normal) (natural gas city gas 13A) hydrogen-containing gas generator, load from 50% to 100%
It is the result of measuring the carbon monoxide concentration in the hydrogen-containing gas generated when the gas was instantaneously increased to.

【0051】〔実施例2〕この実施例2においても、水
素含有ガス生成量調整手段21が、前記水素含有ガス生
成量を増加させるに、調整弁11により改質処理部3へ
の原燃料ガス供給量を増加させる時点より前に、水蒸気
生成部Pの水蒸気生成量を増加させるべく水蒸気生成量
調整手段Vを作動させる水蒸気生成量増加用処理を行う
ように構成され、更に、水素含有ガス生成量調整手段2
1が、水蒸気生成量増加用処理を、調整弁11により改
質処理部3への原燃料ガス供給量を増加させるときに、
その増加に見合う量の水蒸気が生成されるように、水蒸
気生成量調整手段Vを作動させるべく行うように構成さ
れている。
[Embodiment 2] In this Embodiment 2 as well, the hydrogen-containing gas production amount adjusting means 21 increases the hydrogen-containing gas production amount by using the adjusting valve 11 to feed the raw fuel gas to the reforming treatment section 3. Before the time point of increasing the supply amount, it is configured to perform a steam generation amount increasing process for operating the steam generation amount adjusting means V to increase the steam generation amount of the steam generation unit P. Quantity adjusting means 2
When the control valve 11 increases the amount of raw fuel gas supplied to the reforming processing unit 3 by the steam generation amount increasing process,
It is configured to operate the steam generation amount adjusting means V so that the amount of steam corresponding to the increase is generated.

【0052】上述のように水素含有ガス生成量調整手段
21が構成される場合の一例として、図3に示すよう
に、本生成装置Pの水素含有ガス生成量調整手段21
が、調整弁11により原燃料ガス供給量を増加させる
に、その原燃料ガス供給量増加時点よりも所定の時間前
に調整弁10により水蒸気生成部Sへの水供給量を増加
させると共に、その水供給を増加させる時点よりも所定
の時間前に、水蒸気生成部加熱手段9への入熱量を増加
させるように構成される場合について説明する。このよ
うな場合には、水蒸気生成部Sへの水供給量を増加させ
る時点の水蒸気生成部加熱手段9への入熱量、即ち、熱
交換器8に供給される燃焼排ガス中の熱量が、供給され
る水を加熱して水蒸気とするのに充分な量でない場合
に、図6(a)に示すように、水供給量を増加させる時
点よりも所定の時間前から、燃焼器4の燃料量が増加し
て熱交換器8に供給される燃焼排ガス中の熱量が図6
(b)に示すように増加する時点まで、電気ヒータ7を
ON状態として、水蒸気生成部加熱手段9への入熱量
が、原燃料ガス供給量増加時点の所定の時間前に増加さ
れる。つまり、水素含有ガス生成量調整手段Vが、前記
水蒸気生成量増加用処理として、水蒸気生成部加熱手段
9への入熱量を増加させる処理、及び、調整弁10によ
り水蒸気生成部Pへの水供給量を増加させる処理を行う
ように構成されていることになる。
As an example of the case where the hydrogen-containing gas production amount adjusting means 21 is configured as described above, as shown in FIG. 3, the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P is shown.
However, in order to increase the raw fuel gas supply amount by the adjustment valve 11, the adjustment valve 10 increases the water supply amount to the water vapor generation unit S by a predetermined time before the raw fuel gas supply amount is increased. A case will be described in which the heat input to the steam generator heating means 9 is increased a predetermined time before the time of increasing the water supply. In such a case, the heat input amount to the steam generating unit heating means 9 at the time of increasing the water supply amount to the steam generating unit S, that is, the heat amount in the combustion exhaust gas supplied to the heat exchanger 8 is supplied. When the amount of water to be generated is not sufficient to heat it into steam, as shown in FIG. 6 (a), the amount of fuel in the combustor 4 is increased from a predetermined time before the time of increasing the amount of water supply. Is increased and the heat quantity in the combustion exhaust gas supplied to the heat exchanger 8 is shown in FIG.
As shown in (b), the electric heater 7 is turned on until the time of increase, and the amount of heat input to the steam generator heating means 9 is increased a predetermined time before the time when the raw fuel gas supply amount is increased. That is, the hydrogen-containing gas production amount adjusting means V increases the amount of heat input to the steam producing portion heating means 9 as the vapor production amount increasing processing, and supplies water to the steam producing portion P by the adjusting valve 10. It will be configured to perform the process of increasing the amount.

【0053】そして、この場合において、図3(d)に
示すように、水供給量を増加させる時点では、水蒸気生
成部Sは、既に水供給量を増加させても充分な水蒸気を
生成することができ、迅速に水蒸気生成部Sの水蒸気生
成量が増加され、さらに、原燃料ガスを増加させる時点
では、既に水蒸気生成部Sの水蒸気生成量が増加されて
おり、増加した原燃料ガスに対して充分な水蒸気を改質
処理部3に供給することができる。
In this case, as shown in FIG. 3 (d), at the time when the water supply amount is increased, the steam generator S must generate sufficient water vapor even if the water supply amount is already increased. The steam generation amount of the steam generation unit S is rapidly increased, and at the time of increasing the raw fuel gas, the steam generation amount of the steam generation unit S has already been increased. And sufficient steam can be supplied to the reforming processing unit 3.

【0054】よって、本生成装置Pの水素含有ガス生成
量調整手段21は、水素含有ガス生成量を増加させる
に、水蒸気生成部加熱手段9への入熱量と、水蒸気生成
部Sへの水供給量と、原燃料ガス供給量とを所定の時間
間隔を介して順に増加させることで、改質処理部3への
水蒸気供給量不足による一酸化炭素生成量増加を抑制す
ることができる。
Therefore, the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P increases the hydrogen-containing gas production amount in order to increase the amount of heat input to the steam producing portion heating means 9 and supply water to the steam producing portion S. By sequentially increasing the amount and the raw fuel gas supply amount through a predetermined time interval, it is possible to suppress the increase in the carbon monoxide production amount due to the insufficient steam supply amount to the reforming processing unit 3.

【0055】また、原燃料ガス供給量を増加させる所定
の時間前に、水蒸気生成部加熱手段9への入熱量と水蒸
気生成部Sへの水供給量とを同時に増加させても良く、
この場合においても、原燃料ガス供給量を増加させる時
点において、既に水蒸気生成部Sの水蒸気生成量が増加
されており、増加した原燃料ガスに対して充分な水蒸気
を改質処理部3に供給することができる。そして、この
ような本生成装置Pの水素含有ガス生成量調整手段21
においては、例えば、図7に示すように、従来のように
原燃料ガス供給量増加と水供給量増加とを同時に増加さ
せた場合(図7の比較例)と比較して、原燃料ガス供給
量増加時点に対して10秒前に水供給量及び入熱量を増
加させた場合(図7の実施例2a)には、ごく微量の一
酸化炭素しか生成せず、さらに、原燃料ガス供給量増加
時点に対して30秒前に水供給量及び入熱量を増加させ
た場合(図7の実施例2b)には、殆ど一酸化炭素は生
成されないことが実験により確認された。
Further, the heat input to the steam generating section heating means 9 and the water supply to the steam generating section S may be simultaneously increased at a predetermined time before increasing the raw fuel gas supply rate.
Even in this case, when the raw fuel gas supply amount is increased, the steam generation amount of the steam generation unit S has already been increased, and sufficient steam is supplied to the reforming processing unit 3 with respect to the increased raw fuel gas. can do. Then, the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P as described above.
For example, as shown in FIG. 7, compared with the case where the increase in the raw fuel gas supply amount and the increase in the water supply amount are simultaneously increased as in the conventional case (comparative example of FIG. 7), the raw fuel gas supply is increased. When the water supply amount and the heat input amount are increased 10 seconds before the amount increase time (Example 2a in FIG. 7), only a very small amount of carbon monoxide is produced, and further, the raw fuel gas supply amount is increased. It was confirmed by experiments that when the water supply amount and the heat input amount were increased 30 seconds before the increasing time (Example 2b in FIG. 7), almost no carbon monoxide was produced.

【0056】〔実施例3〕この第3実施例においては、
水素含有ガス生成量調整手段21が、前記水素含有ガス
生成量を増加させるに、調整弁11により改質処理部3
への原燃料ガス供給量を増加させる時点より前に、水蒸
気生成部Pの水蒸気生成量を増加させるべく水蒸気生成
量調整手段Vを作動させる水蒸気生成量増加用処理を行
うように構成されている。
[Third Embodiment] In the third embodiment,
In order to increase the hydrogen-containing gas production amount, the hydrogen-containing gas production amount adjusting means 21 uses the adjustment valve 11 to modify the reforming processing unit 3.
Before the time point of increasing the raw fuel gas supply amount to the steam generator, the steam generation amount increasing process for activating the steam generation amount adjusting means V to increase the steam generation amount of the steam generation unit P is performed. .

【0057】上述のように水素含有ガス生成量調整手段
21が構成される場合の一例として、図4に示すよう
に、本生成装置Pの水素含有ガス生成量調整手段21
が、調整弁11により原燃料ガス供給量を増加させる
に、調整弁10により水蒸気生成部Sへの水供給量を原
燃料ガス供給量増加時点と同時に増加させ、水蒸気生成
部加熱手段9への入熱量を、上記実施例2と同様に、そ
の原燃料ガス供給量増加時点よりも所定の時間前に増加
させるように構成される場合について説明する。
As an example of the case where the hydrogen-containing gas production amount adjusting means 21 is configured as described above, as shown in FIG. 4, the hydrogen-containing gas production amount adjusting means 21 of the present production apparatus P is shown.
However, in order to increase the raw fuel gas supply amount by the adjustment valve 11, the adjustment valve 10 increases the water supply amount to the steam generation unit S at the same time when the raw fuel gas supply amount is increased, and the steam generation unit heating means 9 is supplied. A case will be described in which the heat input amount is configured to be increased a predetermined time before the raw fuel gas supply amount is increased, as in the second embodiment.

【0058】このような場合には、実施例2と同様に、
図6に示すように、その原燃料ガス供給量増加時点より
も所定の時間前の時点から、燃焼器4の燃料量が増加し
て熱交換器8に供給される燃焼排ガス中の熱量が増加す
る時点まで、電気ヒータ7をON状態として、水蒸気生
成部加熱手段9への入熱量が、原燃料ガス供給量増加時
点の所定の時間前に増加される。
In such a case, as in the second embodiment,
As shown in FIG. 6, from a time point before a predetermined time before the raw fuel gas supply amount increases, the fuel amount in the combustor 4 increases and the heat amount in the combustion exhaust gas supplied to the heat exchanger 8 increases. Until then, the electric heater 7 is turned on and the heat input to the steam generator heating means 9 is increased a predetermined time before the raw fuel gas supply amount is increased.

【0059】そして、この場合においても、図4(d)
に示すように、原燃料ガス供給量及び水供給量を増加さ
せる時点では、水蒸気生成部加熱手段9は既に水供給量
を増加させても充分な水蒸気を生成することができる状
態となっており、水蒸気生成部Sの水蒸気生成量が従来
よりも短時間で増加される。従って、原燃料ガス供給量
の増加に対して、水蒸気生成部Sにおける水蒸気生成の
増加が多少遅れるにしても、水蒸気生成部Sの水蒸気生
成量を従来よりも短時間で増加させることが可能となっ
て、原燃料ガス供給量の増加に対する水蒸気生成の増加
の遅れを極力小さくすることが可能となり、改質処理部
3への水蒸気供給量不足による一酸化炭素生成量増加を
抑制することができる。
Also in this case, as shown in FIG.
As shown in, when the raw fuel gas supply amount and the water supply amount are increased, the steam generator heating means 9 is already in a state of being able to generate sufficient steam even if the water supply amount is increased. The amount of steam generated in the steam generator S is increased in a shorter time than before. Therefore, even if the increase in the steam generation in the steam generating unit S is slightly delayed with respect to the increase in the raw fuel gas supply amount, it is possible to increase the steam generating amount in the steam generating unit S in a shorter time than in the conventional case. Therefore, it becomes possible to minimize the delay in the increase in steam generation with respect to the increase in the raw fuel gas supply amount, and it is possible to suppress the increase in the carbon monoxide production amount due to the insufficient steam supply amount to the reforming processing unit 3. .

【0060】〔実施例4〕この実施例4においては、水
素含有ガス生成量調整手段21が、前記水素含有ガス生
成量を増加させるに、水蒸気生成部Pの水蒸気生成量を
増加させるべく水蒸気生成量調整手段Vを作動させる水
蒸気生成量増加用処理、及び、調整弁11により改質処
理部3への原燃料ガス供給量を漸増させる原燃料ガス供
給量漸増処理を行うように構成されている。
[Embodiment 4] In this Embodiment 4, the hydrogen-containing gas production amount adjusting means 21 generates steam to increase the production amount of the hydrogen-containing gas in order to increase the production amount of the steam in the steam production unit P. It is configured to perform a steam generation amount increasing process for operating the amount adjusting means V and a raw fuel gas supply amount gradually increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit 3 by the adjusting valve 11. .

【0061】上述のように水素含有ガス生成量調整手段
21が構成される場合の一例として、図5に示すよう
に、水素含有ガス生成量調整手段21が、調整弁11に
より原燃料ガス供給量を所定の時間を要して所定の目標
原燃料ガス供給量になるように漸増させ、その漸増開始
と同時に、調整弁10により水蒸気生成部Sへの水供給
量を増加させると共に、水蒸気生成部加熱手段9への入
熱量を増加させるように構成される場合について説明す
る。
As an example of the case where the hydrogen-containing gas production amount adjusting means 21 is configured as described above, as shown in FIG. 5, the hydrogen-containing gas production amount adjusting means 21 uses the adjustment valve 11 to supply the raw fuel gas. Is gradually increased so as to reach a predetermined target raw fuel gas supply amount over a predetermined period of time, and at the same time when the gradual increase is started, the water supply amount to the steam generating unit S is increased by the adjusting valve 10 and the steam generating unit is increased. A case in which the heat input to the heating means 9 is increased will be described.

【0062】即ち、水蒸気生成部Sへの水供給量を増加
させる時点の水蒸気生成部加熱手段9への入熱量、即
ち、熱交換器8に供給される燃焼排ガス中の熱量が、供
給される水を加熱して水蒸気とするのに充分な量でない
場合には、原燃料ガス供給量の漸増開始時点から、原燃
料ガス供給量の増加により、熱交換器8に供給される燃
焼排ガス中の熱量が供給される水を加熱して水蒸気とす
るのに充分な量に増加する時点まで、電気ヒータ7をO
N状態として、水蒸気生成部加熱手段9への入熱量が増
加されることになる。
That is, the amount of heat input to the steam generator heating means 9 at the time of increasing the amount of water supplied to the steam generator S, that is, the amount of heat in the combustion exhaust gas supplied to the heat exchanger 8 is supplied. When the amount of water is not sufficient to heat it to steam, the amount of raw fuel gas supplied increases from the start of the gradual increase of the amount of raw fuel gas supplied, and the amount of combustion exhaust gas supplied to the heat exchanger 8 increases. The electric heater 7 is turned on until the amount of heat increases to an amount sufficient to heat the supplied water to steam.
In the N state, the amount of heat input to the steam generator heating means 9 is increased.

【0063】そして、図5(b),(d)に示すよう
に、水蒸気生成部Sへの水供給量を増加させても、水蒸
気生成部Sの水蒸気生成量は直ぐに所定の量に増加する
のではなく漸増するのであるが、図5(a)に示すよう
に、原燃料ガス供給量を漸増させるので、水蒸気生成部
Sへの水供給量を原燃料ガス供給量の漸増開始時点と同
時に増加させても、原燃料ガスに対する水蒸気の比率が
低下しないため、改質処理部3への水蒸気供給量不足に
よる一酸化炭素生成量増加を抑制することができる。一
方、図5(b)に破線で示すように、従来のように水供
給量の増加を、原燃料ガス供給量が目標原燃料ガス供給
量に達した時点で行なった場合では、図5(d)に破線
で示すように、原燃料ガス供給量が目標原燃料ガス供給
量に達した時点から、水蒸気生成量が徐々に増加するの
で、改質処理部3において、一時的に原燃料ガス供給量
増加時点では水蒸気量が不足して、一時的に一酸化炭素
生成量が増加する。
Then, as shown in FIGS. 5 (b) and 5 (d), even if the amount of water supplied to the steam generator S is increased, the amount of steam generated in the steam generator S immediately increases to a predetermined amount. However, as shown in FIG. 5A, since the raw fuel gas supply amount is gradually increased, the water supply amount to the steam generator S is increased at the same time when the raw fuel gas supply amount is gradually increased. Even if the amount is increased, the ratio of water vapor to the raw fuel gas does not decrease, so it is possible to suppress an increase in the amount of carbon monoxide produced due to the insufficient amount of water vapor supplied to the reforming processing unit 3. On the other hand, as shown by the broken line in FIG. 5B, when the water supply amount is increased as in the conventional case when the raw fuel gas supply amount reaches the target raw fuel gas supply amount, As indicated by the broken line in d), since the steam generation amount gradually increases from the time when the raw fuel gas supply amount reaches the target raw fuel gas supply amount, in the reforming processing unit 3, the raw fuel gas is temporarily changed. When the supply amount is increased, the amount of water vapor is insufficient and the amount of carbon monoxide produced is temporarily increased.

【0064】本生成装置Pには、脱硫処理部1からの脱
硫原燃料ガスと改質処理部3からの高温の改質処理ガス
とを熱交換させて、改質処理部3に供給される脱硫原燃
料ガスを予熱する脱硫原燃料ガス用熱交換器Epと、改
質処理部3からの高温の改質処理ガスと脱硫処理部1に
供給される原燃料ガスを熱交換させて原燃料ガスを予熱
する原燃料ガス用熱交換器Eaとを設けてある。又、変
成処理部5から排出された変成処理ガスと、水蒸気生成
部Sへ供給する原料水とを熱交換させて、原料水を予熱
する原料水予熱用熱交換器17を設けてある。
In the present production apparatus P, the desulfurization raw fuel gas from the desulfurization treatment section 1 and the high temperature reforming treatment gas from the reforming treatment section 3 are heat-exchanged and supplied to the reforming treatment section 3. The desulfurization raw fuel gas heat exchanger Ep for preheating the desulfurization raw fuel gas, and the high temperature reforming treatment gas from the reforming treatment unit 3 and the raw fuel gas supplied to the desulfurization treatment unit 1 are heat-exchanged to obtain the raw fuel. A raw fuel gas heat exchanger Ea for preheating the gas is provided. A heat exchanger 17 for preheating raw material water is provided to preheat the raw material water by exchanging heat with the raw material water supplied to the steam generating section S and the metamorphic processing gas discharged from the metamorphic processing section 5.

【0065】起動時に、脱硫処理部1を脱硫処理可能な
ように加熱する脱硫処理部用ヒータ32、変成処理部を
変成処理可能なように加熱する2個の変成処理部用ヒー
タ33を設けてあり、それらヒータ32,33は電気ヒ
ータから成る。
At the time of start-up, a desulfurization treatment section heater 32 for heating the desulfurization treatment section 1 so that it can be desulfurized, and two transformation treatment section heaters 33 for heating the transformation processing section so that they can be subjected to transformation processing are provided. The heaters 32 and 33 are electric heaters.

【0066】更に、脱硫処理部1の温度を検出する脱硫
処理温度センサT1、及び、選択酸化処理部6の温度を
検出する選択酸化処理温度センサT5を設けてある。
Further, a desulfurization treatment temperature sensor T1 for detecting the temperature of the desulfurization treatment section 1 and a selective oxidation treatment temperature sensor T5 for detecting the temperature of the selective oxidation treatment section 6 are provided.

【0067】〔別実施形態〕次に別実施形態を説明す
る。 (イ) 水素含有ガス生成量調整手段21を、前記水素
含有ガス生成量を増加させるに、調整弁11により改質
処理部3への原燃料ガス供給量を増加させる時点より前
に、水蒸気生成部Pの水蒸気生成量を増加させるべく水
蒸気生成量調整手段Vを作動させる水蒸気生成量増加用
処理を行うように構成する場合において、水素含有ガス
生成量調整手段Vを、前記水蒸気生成量増加用処理とし
て、水蒸気生成部加熱手段9への入熱量を増加させる処
理、及び、調整弁10により水蒸気生成部Pへの水供給
量を増加させる処理を行うように構成するに当たって
は、それら入熱量を増加させる処理及び水供給量を増加
させる処理を行うタイミングは種々に変更可能である。
例えば、上記の実施例2において例示した如く、入熱量
を増加させる処理を水供給量を増加させる処理よりも先
に行ったり、入熱量を増加させる処理と水供給量を増加
させる処理とを同時に行う他に、水供給量を増加させる
処理を入熱量を増加させる処理よりも先に行っても良
い。
Another Embodiment Next, another embodiment will be described. (A) In order to increase the hydrogen-containing gas production amount, the hydrogen-containing gas production amount adjusting means 21 generates steam before the time when the raw fuel gas supply amount to the reforming processing unit 3 is increased by the adjustment valve 11. In a case where the steam generation amount increasing means for activating the steam generation amount adjusting means V is operated to increase the steam generation amount of the part P, the hydrogen containing gas generation amount adjusting means V is used for increasing the steam generation amount. In the process of increasing the heat input amount to the steam generating unit heating means 9 and the process of increasing the water supply amount to the steam generating unit P by the adjusting valve 10, the heat input amounts are changed. The timing of performing the increasing treatment and the increasing water supply amount can be variously changed.
For example, as illustrated in Example 2 above, the process of increasing the heat input amount is performed before the process of increasing the water supply amount, or the process of increasing the heat input amount and the process of increasing the water supply amount are performed at the same time. In addition to the process, the process of increasing the water supply amount may be performed before the process of increasing the heat input amount.

【0068】(ロ) 水素含有ガス生成量調整手段21
を、前記水素含有ガス生成量を増加させるに、水蒸気生
成部Pの水蒸気生成量を増加させるべく水蒸気生成量調
整手段Vを作動させる水蒸気生成量増加用処理、及び、
調整弁11により改質処理部3への原燃料ガス供給量を
漸増させる原燃料ガス供給量漸増処理を行うように構成
する場合、上記の実施例4においては、水蒸気生成量増
加用処理を原燃料ガス供給量の漸増開始時点と同時に行
う場合について例示したが、水蒸気生成量増加用処理を
原燃料ガス供給量の漸増開始時点よりも前に行っても良
い。
(B) Hydrogen-containing gas production amount adjusting means 21
To increase the amount of hydrogen-containing gas produced, to increase the amount of produced steam in the water vapor production unit P, to operate the amount of vapor production adjusting means V to increase the amount of produced water vapor;
In the case where the adjustment valve 11 is configured to perform the raw fuel gas supply amount gradually increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit 3, in the above-described fourth embodiment, the steam generation amount increasing process is not performed. The case where it is performed at the same time when the fuel gas supply amount is gradually increased has been described, but the steam generation amount increasing process may be performed before the raw fuel gas supply amount is gradually increased.

【0069】又、水蒸気生成量増加用処理を原燃料ガス
供給量の漸増開始時点と同時に行う場合、及び、水蒸気
生成量増加用処理を原燃料ガス供給量の漸増開始時点よ
りも前に行う場合のいずれにおいても、前記水蒸気生成
量増加用処理として、水蒸気生成部加熱手段9への入熱
量を増加させる処理、及び、調整弁10により水蒸気生
成部Pへの水供給量を増加させる処理の両方を行うよう
に構成しても良いし、いずれか一方を行うように構成し
ても良い。
When the process for increasing the amount of steam generation is performed at the same time as the start of gradually increasing the supply amount of raw fuel gas, and when the process for increasing the amount of steam generation is performed before the start time of gradually increasing the supply amount of raw fuel gas. In any of the above, both the process of increasing the heat input amount to the steam generating part heating means 9 and the process of increasing the water supply amount to the steam generating part P by the adjusting valve 10 as the process for increasing the steam generating amount. May be performed, or either one of them may be performed.

【0070】(ハ) 水素含有ガス生成量調整手段21
を、前記水素含有ガス生成量を増加させるに、水蒸気生
成部Pの水蒸気生成量を増加させるべく水蒸気生成量調
整手段Vを作動させる水蒸気生成量増加用処理、及び、
調整弁11により改質処理部3への原燃料ガス供給量を
漸増させる原燃料ガス供給量漸増処理を行うように構成
する場合に、前記水蒸気生成量増加用処理として、水蒸
気生成部加熱手段9への入熱量を増加させる処理、及
び、調整弁10により水蒸気生成部Pへの水供給量を増
加させる処理の両方を行うように構成するに当たって
は、それら入熱量を増加させる処理及び水供給量を増加
させる処理を行うタイミングは種々に変更可能である。
例えば、水供給量を増加させる処理を原燃料ガス供給量
の漸増開始時点と同時に行い、入熱量を増加させる処理
を水供給量を増加させる処理よりも前に行うように構成
しても良い。
(C) Hydrogen-containing gas production amount adjusting means 21
To increase the amount of hydrogen-containing gas produced, to increase the amount of produced steam in the water vapor production unit P, to operate the amount of vapor production adjusting means V to increase the amount of produced water vapor;
When the raw fuel gas supply amount gradually increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit 3 by the adjusting valve 11 is performed, the steam generating unit heating means 9 is used as the steam generation amount increasing process. In the configuration for performing both the process of increasing the heat input amount to the steam generation unit and the process of increasing the water supply amount to the steam generation unit P by the adjustment valve 10, the process of increasing the heat input amount and the water supply amount. The timing for performing the process of increasing the can be variously changed.
For example, the process of increasing the water supply amount may be performed at the same time when the raw fuel gas supply amount is gradually increased, and the process of increasing the heat input amount may be performed before the process of increasing the water supply amount.

【0071】(ニ) 前記水蒸気生成量増加用処理とし
て、水蒸気生成部加熱手段9への入熱量を増加させるこ
とにより行う場合、水蒸気生成部加熱手段9への入熱量
を調整するための具体構成としては、上記の実施形態に
おいて例示した如き電気ヒータ7をオンオフさせる構成
に限定されるものではない。例えば、電気ヒータ7への
電力供給量を調整するように構成したり、熱交換器8へ
の燃焼排ガスの供給量を調整するように構成することが
可能である。
(D) When the steam generation amount increasing process is carried out by increasing the heat input amount to the steam generating part heating means 9, a specific configuration for adjusting the heat input amount to the steam generating part heating means 9 However, the configuration is not limited to the configuration in which the electric heater 7 is turned on and off as illustrated in the above embodiment. For example, it may be configured to adjust the amount of power supplied to the electric heater 7 or to adjust the amount of combustion exhaust gas supplied to the heat exchanger 8.

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

【図1】水素含有ガス生成装置の概略構成図FIG. 1 is a schematic configuration diagram of a hydrogen-containing gas generation device.

【図2】水素含有ガス生成量を増加させるときの各種状
態を示す図
FIG. 2 is a diagram showing various states when increasing the amount of hydrogen-containing gas produced.

【図3】水素含有ガス生成量を増加させるときの各種状
態を示す図
FIG. 3 is a diagram showing various states when increasing the amount of hydrogen-containing gas produced.

【図4】水素含有ガス生成量を増加させるときの各種状
態を示す図
FIG. 4 is a diagram showing various states when increasing the amount of hydrogen-containing gas produced.

【図5】水素含有ガス生成量を増加させるときの各種状
態を示す図
FIG. 5 is a diagram showing various states when increasing the amount of hydrogen-containing gas produced.

【図6】水蒸気生成部加熱手段の入熱量増加の状態を示
す図
FIG. 6 is a diagram showing a state in which the heat input amount of the steam generator heating means is increased.

【図7】水素含有ガス生成量増加に伴って生成される一
酸化炭素濃度を示すグラフ図
FIG. 7 is a graph showing the concentration of carbon monoxide produced as the amount of hydrogen-containing gas produced increases.

【符号の説明】[Explanation of symbols]

1 脱硫処理部 3 改質処理部 4 燃焼器(改質処理部加熱手段) 5 変成処理部 6 選択酸化処理部 7 電気ヒータ 8 熱交換器 9 水蒸気生成部加熱手段 10 調整弁(水供給量調整手段) 11 調整弁(原燃料ガス供給量調整手段) 20 制御部 21 水素含有ガス生成量調整手段 P 水素含有ガス生成装置 S 水蒸気生成部 G 燃料電池 V 水蒸気生成量調整手段 1 Desulfurization unit 3 Modification processing section 4 Combustor (heating means for reforming process part) 5 Metamorphic processing section 6 Selective oxidation treatment section 7 Electric heater 8 heat exchanger 9 Steam generator heating means 10 Adjustment valve (water supply amount adjustment means) 11 Regulator valve (raw fuel gas supply amount adjustment means) 20 Control unit 21 Hydrogen-containing gas production amount adjusting means P Hydrogen-containing gas generator S Steam generator G fuel cell V Water vapor production amount adjusting means

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 水を水蒸気生成部加熱手段で加熱して水
蒸気を生成する水蒸気生成部と、改質処理部加熱手段に
より加熱され、炭化水素系の原燃料ガスを前記水蒸気生
成部で生成した水蒸気を用いて改質処理して水素含有ガ
スを生成する改質処理部とを備えた水素含有ガス生成装
置において、前記水蒸気生成部での水蒸気生成量と前記
改質処理部への原燃料ガス供給量とを調整して、前記改
質処理部での水素含有ガス生成量を調整する水素含有ガ
ス生成量調整方法であって、 前記水素含有ガス生成量を増加させるに、前記改質処理
部への原燃料ガス供給量を増加させる時点より前に、前
記水蒸気生成部の水蒸気生成量を増加させるための水蒸
気生成量増加用処理を行う水素含有ガス生成量調整方
法。
1. A steam producing part for producing water vapor by heating water with a steam producing part heating means and a reforming treatment part heating means to produce a hydrocarbon-based raw fuel gas in the steam producing part. In a hydrogen-containing gas generation apparatus including a reforming processing unit that reforms using steam to generate a hydrogen-containing gas, a steam generation amount in the steam generating unit and a raw fuel gas to the reforming processing unit A hydrogen-containing gas production amount adjusting method of adjusting a supply amount and adjusting a hydrogen-containing gas production amount in the reforming treatment unit, wherein the reforming treatment unit is used to increase the hydrogen-containing gas production amount. A method for adjusting a hydrogen-containing gas production amount, which comprises performing a steam production amount increasing process for increasing a steam production amount of the steam production unit before a time point of increasing a raw fuel gas supply amount to the steam generation unit.
【請求項2】 前記水蒸気生成量増加用処理を、前記改
質処理部への原燃料ガス供給量を増加させるときに、そ
の増加に見合う量の水蒸気が生成されるように行う請求
項1記載の水素含有ガス生成量調整方法。
2. The process for increasing the amount of steam generation is performed so that when the amount of raw fuel gas supplied to the reforming processing unit is increased, an amount of steam corresponding to the increase is generated. Method for adjusting the amount of hydrogen-containing gas produced.
【請求項3】 前記水蒸気生成量増加用処理として、前
記水蒸気生成部加熱手段への入熱量を増加させる処理、
及び、前記水蒸気生成部への水供給量を増加させる処理
の少なくとも一方を行う請求項1又は2に記載の水素含
有ガス生成量調整方法。
3. A process for increasing the heat input to the steam generator heating means as the process for increasing the steam generation amount,
The method for adjusting the hydrogen-containing gas production amount according to claim 1 or 2, wherein at least one of the treatments for increasing the water supply amount to the water vapor production unit is performed.
【請求項4】 水を水蒸気生成部加熱手段で加熱して水
蒸気を生成する水蒸気生成部と、改質処理部加熱手段に
より加熱され、炭化水素系の原燃料ガスを前記水蒸気生
成部で生成した水蒸気を用いて改質処理して水素含有ガ
スを生成する改質処理部とを備えた水素含有ガス生成装
置において、前記水蒸気生成部での水蒸気生成量と前記
改質処理部への原燃料ガス供給量とを調整して、前記改
質処理部での水素含有ガス生成量を調整する水素含有ガ
ス生成量調整方法であって、 前記水素含有ガス生成量を増加させるに、前記水蒸気生
成部の水蒸気生成量を増加させるための水蒸気生成量増
加用処理、及び、前記改質処理部への原燃料ガス供給量
を漸増させる原燃料ガス供給量漸増処理を行う水素含有
ガス生成量調整方法。
4. A steam producing part for producing water vapor by heating water with a steam producing part heating means and a reforming treatment part heating means to produce a hydrocarbon-based raw fuel gas in the steam producing part. In a hydrogen-containing gas generation apparatus including a reforming processing unit that reforms using steam to generate a hydrogen-containing gas, a steam generation amount in the steam generating unit and a raw fuel gas to the reforming processing unit A method for adjusting a hydrogen-containing gas generation amount by adjusting a supply amount and adjusting a hydrogen-containing gas generation amount in the reforming processing unit, wherein the hydrogen-containing gas generation amount is increased by increasing the hydrogen-containing gas generation amount. A method for adjusting a hydrogen-containing gas generation amount, comprising: a process for increasing a steam generation amount for increasing a steam generation amount; and a raw fuel gas supply amount gradually increasing process for gradually increasing a raw fuel gas supply amount to the reforming processing section.
【請求項5】 水を水蒸気生成部加熱手段で加熱して水
蒸気を生成する水蒸気生成部と、改質処理部加熱手段に
より加熱され、炭化水素系の原燃料ガスを前記水蒸気生
成部で生成した水蒸気を用いて改質処理して水素含有ガ
スを生成する改質処理部と、前記水蒸気生成部の水蒸気
生成量を調整する水蒸気生成量調整手段と、前記改質処
理部への原燃料ガス供給量を調整可能な原燃料ガス供給
量調整手段と、前記水蒸気生成量調整手段により前記水
蒸気生成部での水蒸気生成量を調整すると共に、前記原
燃料ガス供給量調整手段により前記改質処理部への原燃
料ガス供給量を調整して、前記改質処理部での水素含有
ガス生成量を調整する水素含有ガス生成量調整手段とを
備えた水素含有ガス生成装置であって、 前記水素含有ガス生成量調整手段が、前記水素含有ガス
生成量を増加させるに、前記原燃料ガス供給量調整手段
により前記改質処理部への原燃料ガス供給量を増加させ
る時点より前に、前記水蒸気生成部の水蒸気生成量を増
加させるべく前記水蒸気生成量調整手段を作動させる水
蒸気生成量増加用処理を行うように構成されている水素
含有ガス生成装置。
5. A steam producing section for producing water vapor by heating water with a steam producing section heating means and a reforming treatment section heating means to produce a hydrocarbon-based raw fuel gas in the steam producing section. A reforming processing unit that reforms using steam to generate a hydrogen-containing gas, a steam generation amount adjusting unit that adjusts the steam generation amount of the steam generating unit, and a raw fuel gas supply to the reforming unit. The raw fuel gas supply amount adjusting means capable of adjusting the amount, and the steam producing amount adjusting means to adjust the steam producing amount in the steam producing part, and the raw fuel gas supplying amount adjusting means to the reforming processing part. A hydrogen-containing gas generation apparatus comprising: a hydrogen-containing gas generation amount adjusting unit that adjusts a raw fuel gas supply amount to adjust the hydrogen-containing gas generation amount in the reforming processing unit. Production amount adjustment means In order to increase the hydrogen-containing gas production amount, the steam production amount of the steam production unit is changed before the time point of increasing the raw fuel gas supply amount to the reforming processing unit by the raw fuel gas supply amount adjusting means. A hydrogen-containing gas generator configured to perform a process for increasing the amount of steam generation, which operates the steam generation amount adjusting means to increase the amount.
【請求項6】 前記水素含有ガス生成量調整手段が、前
記水蒸気生成量増加用処理を、前記原燃料ガス供給量調
整手段により前記改質処理部への原燃料ガス供給量を増
加させるときに、その増加に見合う量の水蒸気が生成さ
れるように、前記水蒸気生成量調整手段を作動させるべ
く行うように構成されている請求項5に記載の水素含有
ガス生成装置。
6. The hydrogen-containing gas production amount adjusting means, when increasing the raw fuel gas supply amount to the reforming processing section by the raw fuel gas supply amount adjusting means, performs the water vapor production amount increasing process. The hydrogen-containing gas generator according to claim 5, wherein the hydrogen-containing gas generator is configured so as to operate the steam generation amount adjusting means so that an amount of steam corresponding to the increase is generated.
【請求項7】 前記水蒸気生成量調整手段が、前記水蒸
気生成部への水供給量を調整可能な水供給量調整手段
と、入熱量を調整可能なように構成された前記水蒸気生
成部加熱手段にて構成され、 前記水素含有ガス生成量調整手段が、前記水蒸気生成量
増加用処理として、前記水蒸気生成部加熱手段への入熱
量を増加させる処理、及び、前記水供給量調整手段によ
り前記水蒸気生成部への水供給量を増加させる処理の少
なくとも一方を行うように構成されている請求項5又は
6に記載の水素含有ガス生成装置。
7. The water vapor production amount adjusting means, which is capable of adjusting the water supply amount to the water vapor producing portion, and the water vapor producing portion heating means, which is configured to be able to adjust the heat input amount. The hydrogen-containing gas production amount adjusting means, as the water vapor production amount increasing processing, a treatment for increasing the heat input amount to the water vapor producing section heating means, and the water vapor by the water supply amount adjusting means. The hydrogen-containing gas generation device according to claim 5 or 6, which is configured to perform at least one of treatments for increasing the amount of water supplied to the generation unit.
【請求項8】 前記改質処理部加熱手段が、燃焼熱によ
り前記改質処理部を加熱する燃焼器で構成され、 前記水蒸気生成部加熱手段が、前記燃焼器から排出され
る燃焼排ガスとの熱交換により水を加熱する熱交換器と
電気ヒータとで構成され、 前記水素含有ガス生成量調整手段が、前記電気ヒータの
出力を増加させて前記水蒸気生成部加熱手段への入熱量
を増加させるように構成されている請求項7に記載の水
素含有ガス生成装置。
8. The reforming treatment section heating means is composed of a combustor for heating the reforming treatment section with combustion heat, and the steam generation section heating means is used for combustion exhaust gas discharged from the combustor. It is composed of a heat exchanger that heats water by heat exchange and an electric heater, and the hydrogen-containing gas production amount adjusting means increases the output of the electric heater to increase the heat input amount to the steam producing part heating means. The hydrogen-containing gas generator according to claim 7, which is configured as described above.
【請求項9】 水を水蒸気生成部加熱手段で加熱して水
蒸気を生成する水蒸気生成部と、改質処理部加熱手段に
より加熱され、炭化水素系の原燃料ガスを前記水蒸気生
成部で生成した水蒸気を用いて改質処理して水素含有ガ
スを生成する改質処理部と、前記水蒸気生成部の水蒸気
生成量を調整する水蒸気生成量調整手段と、前記改質処
理部への原燃料ガス供給量を調整可能な原燃料ガス供給
量調整手段と、前記水蒸気生成量調整手段により前記水
蒸気生成部での水蒸気生成量を調整すると共に、前記原
燃料ガス供給量調整手段により前記改質処理部への原燃
料ガス供給量を調整して、前記改質処理部での水素含有
ガス生成量を調整する水素含有ガス生成量調整手段とを
備えた水素含有ガス生成装置であって、 前記水素含有ガス生成量調整手段が、前記水素含有ガス
生成量を増加させるに、前記水蒸気生成部の水蒸気生成
量を増加させるべく前記水蒸気生成量調整手段を作動さ
せる水蒸気生成量増加用処理、及び、前記原燃料ガス供
給量調整手段により前記改質処理部への原燃料ガス供給
量を漸増させる原燃料ガス供給量漸増処理を行うように
構成されている水素含有ガス生成装置。
9. A steam producing part for producing water vapor by heating water with a steam producing part heating means and a reforming treatment part heating means to produce a hydrocarbon-based raw fuel gas in the steam producing part. A reforming processing unit that reforms using steam to generate a hydrogen-containing gas, a steam generation amount adjusting unit that adjusts the steam generation amount of the steam generating unit, and a raw fuel gas supply to the reforming unit. The raw fuel gas supply amount adjusting means capable of adjusting the amount, and the steam producing amount adjusting means to adjust the steam producing amount in the steam producing part, and the raw fuel gas supplying amount adjusting means to the reforming processing part. A hydrogen-containing gas generation apparatus comprising: a hydrogen-containing gas generation amount adjusting unit that adjusts a raw fuel gas supply amount to adjust the hydrogen-containing gas generation amount in the reforming processing unit. Production amount adjustment means A process for increasing the amount of generated steam that increases the amount of generated hydrogen-containing gas, the steam generation amount adjusting unit operates to increase the amount of steam generation of the steam generation unit; and the raw fuel gas supply amount adjusting unit. The hydrogen-containing gas generation device configured to perform the raw fuel gas supply amount gradually increasing process for gradually increasing the raw fuel gas supply amount to the reforming processing unit.
JP2002329655A 2001-11-13 2002-11-13 Hydrogen-containing gas generator and method for adjusting the amount of hydrogen-containing gas Expired - Fee Related JP3986419B2 (en)

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JP2001347136 2001-11-13
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006347788A (en) * 2005-06-14 2006-12-28 T Rad Co Ltd Method for controlling load of reforming system
JP2007525398A (en) * 2004-02-17 2007-09-06 モーディーン・マニュファクチャリング・カンパニー Integrated fuel processor for distributed hydrogen production
JP2009242205A (en) * 2008-03-31 2009-10-22 Osaka Gas Co Ltd Start-up method of hydrogen-containing gas producing apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007525398A (en) * 2004-02-17 2007-09-06 モーディーン・マニュファクチャリング・カンパニー Integrated fuel processor for distributed hydrogen production
JP2006347788A (en) * 2005-06-14 2006-12-28 T Rad Co Ltd Method for controlling load of reforming system
JP2009242205A (en) * 2008-03-31 2009-10-22 Osaka Gas Co Ltd Start-up method of hydrogen-containing gas producing apparatus

Also Published As

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