JP2014047083A - Hydrogen-containing gas generator, and method of adjusting generation rate of hydrogen-containing gas - Google Patents

Hydrogen-containing gas generator, and method of adjusting generation rate of hydrogen-containing gas Download PDF

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JP2014047083A
JP2014047083A JP2012189109A JP2012189109A JP2014047083A JP 2014047083 A JP2014047083 A JP 2014047083A JP 2012189109 A JP2012189109 A JP 2012189109A JP 2012189109 A JP2012189109 A JP 2012189109A JP 2014047083 A JP2014047083 A JP 2014047083A
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reformer
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Akio Inaya
章雄 稲家
Norihisa Kamiya
規寿 神家
Yukio Yasuda
征雄 安田
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Osaka Gas Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a hydrogen-containing gas generator capable of precisely controlling a ratio of raw fuel and steam to be supplied to a reformer.SOLUTION: In a hydrogen-containing gas generator, when a feed rate of raw fuel to a reformer 2 and a feed rate of water to a steam generator 6 are both increased for the purpose of increasing a generation rate of a hydrogen-containing gas, the feed rate of water to the steam generator 6 is increased before the feed rate of raw fuel to the reformer 2 is increased. A pressure detector 12 is installed to detect a pressure value which is used to estimate a steam rate supplied to the reformer 2 from the steam generator 6. When the generation rate of the hydrogen-containing gas is intended to be increased in the reformer 2, reformer control means 13a determines a timing to increase the feed rate of raw fuel to the reformer 2 based on a detection result of the pressure detector 12 after increasing the feed rate of water to the steam generator 6.

Description

本発明は、炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素含有ガスを生成する改質器と、供給される水を蒸発させて、改質器に水蒸気を供給する水蒸気発生器と、改質器への原燃料の供給量と水蒸気発生器への水の供給量とを制御する改質制御手段とを備える水素含有ガス生成装置、及び、その水素含有ガス生成装置において行われる水素含有ガス生成量調節方法に関する。   The present invention relates to a reformer that generates a hydrogen-containing gas by reforming a raw fuel containing hydrocarbons in the presence of steam, and a steam that evaporates supplied water and supplies steam to the reformer. In a hydrogen-containing gas generation device including a generator, and a reforming control unit that controls a supply amount of raw fuel to the reformer and a supply amount of water to the steam generator, and the hydrogen-containing gas generation device The present invention relates to a method for adjusting the amount of hydrogen-containing gas produced.

燃料電池の燃料ガスとして用いられる水素を生成するための装置として、炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素を主に含む水素含有ガスを生成する改質器と、供給される水を蒸発させて、改質器に水蒸気を供給する水蒸気発生器と、改質器への原燃料の供給量と水蒸気発生器への水の供給量とを制御する改質制御手段とを備える水素含有ガス生成装置がある。   As a device for generating hydrogen used as a fuel gas of a fuel cell, a reformer that generates a hydrogen-containing gas mainly containing hydrogen by reforming raw fuel containing hydrocarbon in the presence of water vapor; A steam generator that evaporates the supplied water and supplies steam to the reformer, and a reforming control means that controls the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator There is a hydrogen-containing gas generator.

水素含有ガス生成装置において原燃料の水蒸気改質を行なう場合、改質器が有する改質触媒におけるカーボン析出の防止や、改質器の下流側に設けられる一酸化炭素変成器の出口ガス中のCO濃度を一定値以下に収めるため、改質器に供給される原燃料中のカーボンに対する水蒸気の当量比(以下、「S/C」と記載することもある)を一定以上の大きさに制御する必要がある。但し、必要以上に水蒸気を供給した場合、水蒸気を発生させるのに要する熱量の元となる燃料を余分に消費し、エネルギー効率が低下するため、S/Cは一定範囲内での制御が必要となる。   When steam reforming of raw fuel is performed in a hydrogen-containing gas generator, prevention of carbon deposition in the reforming catalyst of the reformer, or in the outlet gas of a carbon monoxide converter provided downstream of the reformer In order to keep the CO concentration below a certain value, the equivalent ratio of water vapor to carbon in the raw fuel supplied to the reformer (hereinafter sometimes referred to as “S / C”) is controlled to a certain level or more. There is a need to. However, if water vapor is supplied more than necessary, the fuel that is the source of heat required to generate water vapor is consumed excessively and energy efficiency is reduced, so S / C needs to be controlled within a certain range. Become.

燃料電池の起動時や電力負荷上昇時、水素含有ガス生成装置から燃料電池へ供給する水素を増加させるためには、改質器へ供給する原燃料を増加させる必要がある。このとき、改質器へ供給する原燃料量を増加させるだけでなく、上述したS/Cを維持するために水蒸気発生器へ供給する水の量を増加させて水蒸気発生量を増加させ、その結果として改質器へ供給する水蒸気量も増加させる必要がある。但し、改質器に対して目標水蒸気量を供給するために水蒸気発生器に対して目標水量の水を供給しても、その目標水量の水の全てが蒸発するまでに時間を要する場合、実際には目標水蒸気量よりも少ない量の水蒸気しか改質器に供給できていないこともある。そのため、従来は、改質器へ供給する水蒸気量が所要量に到達するまで時間を要することを考慮して、負荷上昇時においてはあらかじめ定めた時限をもって負荷上昇前に改質水の先行増量を行なっている。   In order to increase the amount of hydrogen supplied from the hydrogen-containing gas generator to the fuel cell when the fuel cell is started or when the power load is increased, it is necessary to increase the raw fuel supplied to the reformer. At this time, not only the amount of raw fuel supplied to the reformer is increased, but also the amount of water supplied to the steam generator is increased in order to maintain the above-mentioned S / C, and the amount of steam generated is increased. As a result, it is also necessary to increase the amount of steam supplied to the reformer. However, even if supplying the target water amount to the steam generator to supply the target steam amount to the reformer, if it takes time to evaporate all of the target water amount, In some cases, only a smaller amount of water vapor than the target water vapor amount can be supplied to the reformer. Therefore, in the past, taking into account the time required for the amount of steam supplied to the reformer to reach the required amount, when the load increases, a prior increase in the amount of reforming water is performed before the load increase with a predetermined time limit. Is doing.

例えば、特許文献1に記載の水素含有ガス生成装置は、改質器での水素含有ガスの生成量を増加させるために改質器への原燃料の供給量と水蒸気発生器への水の供給量とを共に増加変化させるとき、改質器への原燃料の供給量を増加変化させる時点よりも前に水蒸気発生器への水の供給量を増加変化させるように構成されている。   For example, in the hydrogen-containing gas generation device described in Patent Document 1, in order to increase the amount of hydrogen-containing gas generated in the reformer, the amount of raw fuel supplied to the reformer and the water supply to the steam generator When both the amount and the amount of fuel are increased, the amount of water supplied to the steam generator is increased and changed before the time when the amount of supply of raw fuel to the reformer is increased.

特開2003−212505号公報JP 2003-212505 A

しかしながら、供給された水を蒸発させるのに十分な熱を水蒸気発生器で供給できていないと、水が所要量蒸発するまでの時間は一定でない。つまり、改質器への原燃料の供給量を増加変化させる時点よりも一定時限前に水蒸気発生器への水の供給量を増加変化させたとしても、原燃料の供給量を増加変化させる時点で水が所要量蒸発しているとは限らず、S/Cについては誤差が生じることがある。
つまり、改質器に対して目標水蒸気量を供給するために水蒸気発生器に対して目標水量を供給しても、その目標水量の全てが蒸発するとは限らず、実際には目標水蒸気量よりも少ない量の水蒸気しか改質器に供給できていないこともある。その場合、S/Cが適切な範囲とならないため、上述したように改質器においてコーキングの発生や、水蒸気不足によって、改質処理により得られる水素ガス中のCOの濃度が上昇するなどの問題が発生し得る。
However, if the steam generator cannot supply sufficient heat to evaporate the supplied water, the time until the required amount of water evaporates is not constant. In other words, even if the amount of water supplied to the steam generator is increased and changed a certain time before the time when the amount of raw fuel supplied to the reformer is increased and changed, the time when the amount of raw fuel supplied is increased and changed. However, the required amount of water is not necessarily evaporated, and an error may occur in S / C.
That is, even if the target water amount is supplied to the steam generator in order to supply the target steam amount to the reformer, not all of the target water amount evaporates. In some cases, only a small amount of water vapor can be supplied to the reformer. In this case, since the S / C is not in an appropriate range, problems such as the occurrence of coking in the reformer and the concentration of CO in the hydrogen gas obtained by the reforming process due to insufficient steam as described above. Can occur.

本発明は、上記の課題に鑑みてなされたものであり、その目的は、改質器での水蒸気不足の発生を回避可能な水素含有ガス生成装置、及び、その水素含有ガス生成装置において行われる水素含有ガス生成量調節方法を提供する点にある。   The present invention has been made in view of the above-described problems, and the object thereof is performed in a hydrogen-containing gas generation device capable of avoiding the occurrence of steam shortage in a reformer and the hydrogen-containing gas generation device. The object is to provide a method for adjusting the amount of hydrogen-containing gas produced.

上記目的を達成するための本発明に係る水素含有ガス生成装置の特徴構成は、炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素含有ガスを生成する改質器と、
供給される水を蒸発させて、前記改質器に水蒸気を供給する水蒸気発生器と、
前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを制御する改質制御手段とを備え、
前記改質制御手段は、前記改質器での水素含有ガスの生成量を増加させるために前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に増加変化させるとき、前記改質器への原燃料の供給量を増加変化させる時点よりも前に前記水蒸気発生器への水の供給量を増加変化させるように構成されている水素含有ガス生成装置であって、
前記水蒸気発生器から前記改質器に供給される水蒸気の量を推定可能な圧力値を、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内で検出する圧力検出器を備え、
前記改質制御手段は、前記改質器での水素含有ガスの生成量を増加させるとき、前記水蒸気発生器への水の供給量を増加変化させた後の前記圧力検出器の検出結果に基づいて、前記改質器への原燃料の供給量を増加変化させるタイミングを決定するように構成されている点にある。
In order to achieve the above object, the hydrogen-containing gas generator according to the present invention includes a reformer that generates a hydrogen-containing gas by reforming a raw fuel containing hydrocarbons in the presence of steam;
A steam generator for evaporating the supplied water and supplying steam to the reformer;
Reforming control means for controlling the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator;
The reforming control unit increases both the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator in order to increase the amount of hydrogen-containing gas generated in the reformer. A hydrogen-containing gas generator configured to increase and change the amount of water supplied to the steam generator before the time of increasing the amount of raw fuel supplied to the reformer when changing There,
A pressure value capable of estimating the amount of steam supplied from the steam generator to the reformer is set in a flow path through which water supplied to the steam generator or steam generated by the steam generator flows. Equipped with a pressure detector to detect,
The reforming control unit is configured to increase the amount of hydrogen-containing gas generated in the reformer based on the detection result of the pressure detector after increasing the amount of water supplied to the steam generator. Thus, the timing for increasing and changing the supply amount of the raw fuel to the reformer is determined.

上記特徴構成によれば、圧力検出器が、水蒸気発生器から改質器に供給される水蒸気の量を推定可能な圧力値を、水蒸気発生器に供給される水又は水蒸気発生器で発生された水蒸気が流通する流路内で検出する。つまり、改質制御手段は、圧力検出器が検出する圧力値に基づいて、水蒸気発生器から改質器に供給される水蒸気の量を高い精度で知ることができる。その結果、改質制御手段は、改質器に供給される原燃料の量と水蒸気の量とが適切な当量比(S/C)となるように制御できる。
従って、改質器での水蒸気不足の発生を回避可能な水素含有ガス生成装置を提供できる。
According to the above characteristic configuration, the pressure detector generates a pressure value capable of estimating the amount of steam supplied from the steam generator to the reformer, with water supplied to the steam generator or the steam generator. Detection is performed in a flow path through which water vapor flows. That is, the reforming control means can know the amount of steam supplied from the steam generator to the reformer with high accuracy based on the pressure value detected by the pressure detector. As a result, the reforming control means can control the amount of raw fuel supplied to the reformer and the amount of water vapor to have an appropriate equivalent ratio (S / C).
Therefore, it is possible to provide a hydrogen-containing gas generation device that can avoid the occurrence of water vapor shortage in the reformer.

本発明に係る水素含有ガス生成装置の別の特徴構成は、前記水蒸気発生器と前記改質器との間の流路途中に設けられて、水蒸気の流量を制限する流量制限手段を備え、
前記圧力検出器は、前記流量制限手段よりも上流側の、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内の圧力を検出する点にある。
Another characteristic configuration of the hydrogen-containing gas generation device according to the present invention is provided in the middle of the flow path between the steam generator and the reformer, and includes a flow rate limiting unit that limits the flow rate of the steam,
The pressure detector is to detect a pressure in a flow path through which water supplied to the water vapor generator or water vapor generated by the water vapor generator flows, upstream of the flow rate restricting means.

上記特徴構成によれば、水蒸気発生器から改質器へ流れる水蒸気の流量を流量制限手段によって制限することで、流量制限手段よりも上流側の空間での圧力が、流量制限手段よりも上流側の水蒸気発生器で発生した水蒸気による圧力をより良く代表することとなる。その結果、改質制御手段は、圧力検出器が検出する圧力値に基づいて、水蒸気発生器から改質器に供給される水蒸気の量を更に高い精度で知ることができる。   According to the above characteristic configuration, the flow rate of the steam flowing from the steam generator to the reformer is limited by the flow rate limiting unit, so that the pressure in the space upstream of the flow rate limiting unit is higher than the flow rate limiting unit. The pressure due to the water vapor generated by the water vapor generator is better represented. As a result, the reforming control means can know the amount of steam supplied from the steam generator to the reformer with higher accuracy based on the pressure value detected by the pressure detector.

本発明に係る水素含有ガス生成装置の更に別の特徴構成は、前記改質制御手段は、前記改質器での水素含有ガスの生成量を目標生成量へと増加させるために、前記改質器への原燃料の供給量を目標原燃料量へと増加変化させ、前記水蒸気発生器への水の供給量を目標水量へと増加変化させるとき、
前記水蒸気発生器への水の供給量を増加させた後の前記圧力検出器の検出値が、前記目標水量に対応した目標圧力値になると、前記改質器への原燃料の供給量を前記目標原燃料量へと増加変化させるタイミングであると決定するように構成されている点にある。
Still another characteristic configuration of the hydrogen-containing gas generation device according to the present invention is that the reforming control unit is configured to increase the amount of hydrogen-containing gas generated in the reformer to a target generation amount. When increasing the supply amount of raw fuel to the steam generator to the target raw fuel amount and increasing the supply amount of water to the steam generator to the target water amount,
When the detection value of the pressure detector after increasing the supply amount of water to the steam generator becomes a target pressure value corresponding to the target water amount, the supply amount of raw fuel to the reformer is The point is that it is determined that it is the timing for increasing the target raw fuel amount.

上記特徴構成によれば、水蒸気発生器に対して目標水量の水を供給したとき、その水の蒸発量が不十分であれば圧力検出器で検出される圧力値は目標圧力値に満たないが、その水の蒸発量が十分であれば圧力検出器で検出される圧力値は目標圧力値になる。つまり、圧力検出器の検出値に基づいて、水蒸気発生器に供給した目標水量に対応した水蒸気量の水蒸気が改質器へ供給されることを知ることができる。その結果、改質制御手段は、改質器に供給される原燃料の量と水蒸気の量とが適切な当量比(S/C)となるように制御できる。   According to the above characteristic configuration, when the target water amount of water is supplied to the steam generator, the pressure value detected by the pressure detector is less than the target pressure value if the water evaporation amount is insufficient. If the evaporation amount of the water is sufficient, the pressure value detected by the pressure detector becomes the target pressure value. That is, based on the detection value of the pressure detector, it can be known that water vapor having a water vapor amount corresponding to the target water amount supplied to the water vapor generator is supplied to the reformer. As a result, the reforming control means can control the amount of raw fuel supplied to the reformer and the amount of water vapor to have an appropriate equivalent ratio (S / C).

本発明に係る水素含有ガス生成装置の更に別の特徴構成は、前記圧力検出器が圧力値を検出する部位での温度を検出する温度検出器を備え、
前記改質制御手段は、前記温度検出器の検出結果に基づいて、前記圧力検出器の検出結果を補正換算する点にある。
Still another characteristic configuration of the hydrogen-containing gas generation device according to the present invention includes a temperature detector that detects a temperature at a portion where the pressure detector detects a pressure value,
The reforming control unit is configured to correct and convert the detection result of the pressure detector based on the detection result of the temperature detector.

上記特徴構成によれば、温度検出器での検出結果に基づいて圧力検出器の検出結果を補正換算することで、水蒸気発生器から改質器に供給される水蒸気の量を高い精度で知ることができる。   According to the above characteristic configuration, the amount of steam supplied from the steam generator to the reformer is known with high accuracy by correcting and converting the detection result of the pressure detector based on the detection result of the temperature detector. Can do.

上記目的を達成するための本発明に係る水素含有ガス生成量調節方法の特徴構成は、炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素含有ガスを生成する改質器と、供給される水を蒸発させて、前記改質器に水蒸気を供給する水蒸気発生器とを備える水素含有ガス生成装置において、前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に制御することで前記改質器での水素含有ガスの生成量を調節する水素含有ガス生成量調節方法であって、
前記改質器での水素含有ガスの生成量を増加させるために前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に増加変化させるとき、前記改質器への原燃料の供給量を増加変化させる時点よりも前に前記水蒸気発生器への水の供給量を増加変化させ、前記水蒸気発生器への水の供給量を増加変化させた後の、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内での圧力値に基づいて、前記改質器への原燃料の供給量を増加変化させるタイミングを決定する点にある。
In order to achieve the above object, the characteristic configuration of the method for adjusting the amount of hydrogen-containing gas production according to the present invention includes a reformer that produces a hydrogen-containing gas by reforming raw fuel containing hydrocarbons in the presence of steam. A hydrogen-containing gas generating device comprising a water vapor generator for evaporating supplied water and supplying water vapor to the reformer, and a supply amount of raw fuel to the reformer and the water vapor generator A method for adjusting the amount of hydrogen-containing gas produced by adjusting the amount of hydrogen-containing gas produced in the reformer by controlling both the amount of water supplied,
When the supply amount of raw fuel to the reformer and the supply amount of water to the steam generator are both increased and changed in order to increase the amount of hydrogen-containing gas generated in the reformer, the reforming After increasing the supply amount of water to the steam generator before the time of increasing the supply amount of raw fuel to the steam generator, and after increasing the supply amount of water to the steam generator, The timing for increasing and changing the supply amount of raw fuel to the reformer based on the pressure value in the flow path through which the water supplied to the steam generator or the steam generated by the steam generator flows. The point is to decide.

上記特徴構成によれば、改質器での水素含有ガスの生成量を増加させるために改質器への原燃料の供給量と水蒸気発生器への水の供給量とを共に増加変化させるとき、改質器への原燃料の供給量を増加変化させる時点よりも前に水蒸気発生器への水の供給量を増加変化させる。そして、水蒸気発生器への水の供給量を増加変化させた後の、水蒸気発生器に供給される水又は水蒸気発生器で発生された水蒸気が流通する流路内での圧力値に基づいて、改質器への原燃料の供給量を増加変化させるタイミングを決定する。つまり、水蒸気発生器から改質器に供給される水蒸気の量を推定可能な圧力値を、水蒸気発生器に供給される水又は水蒸気発生器で発生された水蒸気が流通する流路内で検出することで、水蒸気発生器から改質器に供給される水蒸気の量を高い精度で知ることができる。その結果、改質器に供給される原燃料の量と水蒸気の量とが適切な当量比(S/C)となるように制御できる。   According to the above characteristic configuration, when both the supply amount of raw fuel to the reformer and the supply amount of water to the steam generator are increased to increase the amount of hydrogen-containing gas generated in the reformer. The supply amount of water to the steam generator is increased and changed before the time when the supply amount of raw fuel to the reformer is increased and changed. And based on the pressure value in the flow path through which the water supplied to the steam generator or the steam generated by the steam generator flows after changing the supply amount of water to the steam generator, The timing for increasing the supply amount of raw fuel to the reformer is determined. In other words, a pressure value capable of estimating the amount of steam supplied from the steam generator to the reformer is detected in a flow path through which water supplied to the steam generator or steam generated by the steam generator flows. Thus, the amount of steam supplied from the steam generator to the reformer can be known with high accuracy. As a result, the amount of raw fuel supplied to the reformer and the amount of water vapor can be controlled so as to have an appropriate equivalent ratio (S / C).

燃料電池システムの構成を示す図である。It is a figure which shows the structure of a fuel cell system. 各機器の動作状態の推移を説明するタイミング図である。It is a timing diagram explaining transition of the operating state of each device. 目標水量と目標圧力値との関係を示すグラフである。It is a graph which shows the relationship between a target water amount and a target pressure value.

以下に図面を参照して本発明に係る水素含有ガス生成装置について説明する。
図1は、水素含有ガス生成装置を含む燃料電池システムの構成を示す図である。図示するように、燃料電池システムは、水素含有ガス生成装置を用いて生成した、水素を主成分とする燃料ガスを燃料電池FCに供給して、燃料電池FCにおいて発電反応を行わせるように構成されている。水素含有ガス生成装置は、改質器2と、水蒸気発生器6と、改質制御手段13aとして機能する制御装置13とを備える。加えて、図1に示す本実施形態の水素含有ガス生成装置は、脱硫器1と、一酸化炭素変成器3と、一酸化炭素除去器4と、燃焼器5を備える。
A hydrogen-containing gas generator according to the present invention will be described below with reference to the drawings.
FIG. 1 is a diagram illustrating a configuration of a fuel cell system including a hydrogen-containing gas generation device. As shown in the figure, the fuel cell system is configured to supply a fuel gas mainly composed of hydrogen, which is generated using a hydrogen-containing gas generation device, to the fuel cell FC so that a power generation reaction is performed in the fuel cell FC. Has been. The hydrogen-containing gas generating device includes a reformer 2, a steam generator 6, and a control device 13 that functions as the reforming control means 13a. In addition, the hydrogen-containing gas generator of this embodiment shown in FIG. 1 includes a desulfurizer 1, a carbon monoxide converter 3, a carbon monoxide remover 4, and a combustor 5.

脱硫器1は、供給される原燃料(例えば都市ガス)などに付臭剤として含まれる硫黄化合物を脱硫処理する。   The desulfurizer 1 desulfurizes a sulfur compound contained as an odorant in the supplied raw fuel (for example, city gas).

水蒸気発生器6は、供給される水を蒸発させて、改質器2に水蒸気を供給する。具体的には、水蒸気発生器6に隣接して設けられる熱交換器8には、燃焼器5から排出された燃焼排ガスが供給され、その燃焼排ガスが有する熱が水蒸気発生器6に伝達されて水の蒸発に利用される。水蒸気発生器6で生成された水蒸気は、脱硫処理後の原燃料に添加される。また、本実施形態の水素含有ガス生成装置は、水蒸気発生器6を加熱可能な電気ヒーターHも備えている。つまり、水蒸気発生器6は、熱交換器8及び電気ヒーターHの少なくとも何れか一方から得られる熱を利用して、供給される水を蒸発させるように構成されている。   The steam generator 6 evaporates the supplied water and supplies the reformer 2 with water vapor. Specifically, the combustion exhaust gas discharged from the combustor 5 is supplied to the heat exchanger 8 provided adjacent to the steam generator 6, and the heat of the combustion exhaust gas is transmitted to the steam generator 6. Used for water evaporation. The steam generated by the steam generator 6 is added to the raw fuel after the desulfurization treatment. In addition, the hydrogen-containing gas generation apparatus of the present embodiment also includes an electric heater H that can heat the steam generator 6. That is, the steam generator 6 is configured to evaporate the supplied water by using heat obtained from at least one of the heat exchanger 8 and the electric heater H.

燃焼器5は、可燃性ガスと酸素ガスとの混合ガスを燃焼して燃焼熱を発生させる。可燃性ガスとしては、燃料電池FCから排出された排燃料ガス(発電反応に用いられなかった水素を含むガス)を用いることができる。   The combustor 5 burns a mixed gas of combustible gas and oxygen gas to generate combustion heat. As the combustible gas, exhaust fuel gas discharged from the fuel cell FC (a gas containing hydrogen that has not been used in the power generation reaction) can be used.

改質器2は、原燃料を水蒸気の存在下で改質処理して、水素を主成分とする水素含有ガスを生成する。具体的には、改質器2は、隣接して設けられる燃焼器5で発生された燃焼熱を利用して原燃料を水蒸気改質して、水素を主成分とし、副生成物としての一酸化炭素と二酸化炭素とを含む改質ガスを生成する。   The reformer 2 reforms the raw fuel in the presence of steam to generate a hydrogen-containing gas containing hydrogen as a main component. Specifically, the reformer 2 steam-reforms the raw fuel by using the combustion heat generated in the adjacent combustor 5 to form hydrogen as a main component and a by-product. A reformed gas containing carbon oxide and carbon dioxide is generated.

一酸化炭素変成器3は、改質器2にて生成されたガスに含まれる一酸化炭素を低減するように処理する。具体的には、一酸化炭素変成器3において、改質器2で生成された改質ガス中に含まれている一酸化炭素と水蒸気とが反応して、一酸化炭素が二酸化炭素に変成処理される。   The carbon monoxide converter 3 performs processing so as to reduce carbon monoxide contained in the gas generated in the reformer 2. Specifically, in the carbon monoxide converter 3, carbon monoxide contained in the reformed gas generated in the reformer 2 reacts with water vapor, and the carbon monoxide is converted into carbon dioxide. Is done.

一酸化炭素除去器4は、一酸化炭素変成器3から排出される変成処理後の改質ガス中に残留している一酸化炭素を除去する。例えば、一酸化炭素除去器4において、変成処理後の改質ガス中に残っている一酸化炭素が、新たに添加された空気中の酸素によって酸化除去される。その結果、一酸化炭素濃度の非常に低い、水素リッチな燃料ガスが生成される。
一酸化炭素除去器4によって処理された後の改質ガスは、燃料電池FCに供給されて発電反応に用いられる。
The carbon monoxide remover 4 removes carbon monoxide remaining in the reformed gas after the shift treatment discharged from the carbon monoxide shifter 3. For example, in the carbon monoxide remover 4, carbon monoxide remaining in the reformed gas after the shift treatment is oxidized and removed by oxygen in the newly added air. As a result, a hydrogen-rich fuel gas with a very low carbon monoxide concentration is produced.
The reformed gas after being treated by the carbon monoxide remover 4 is supplied to the fuel cell FC and used for a power generation reaction.

図1に例示する燃料電池システムにおいて、燃料電池FCで発電された電力は、パワーコンディショナ9に供給されるように構成されている。
制御装置13は、燃料電池システムに設けられている各種機器の動作を制御する。具体的には、制御装置13の一機能である改質制御手段13aは、改質器2への原燃料の供給量と水蒸気発生器6への水の供給量とを制御する。改質器2への原燃料の供給量、即ち、脱硫器1への原燃料の供給量は、脱硫器1の上流側に設けられる流量調節手段としての原燃料流量調節弁10によって調節可能である。また、改質器2には、水蒸気供給路を介して水蒸気が供給される。この水蒸気は水蒸気発生器6で発生されたものである。水蒸気発生器6には水供給路を介して水が供給される。水蒸気発生器6への水の供給量は、水蒸気発生器6の上流側に設けられる給水量調節手段としてのポンプ11によって調節可能である。これら原燃料流量調節弁10及びポンプ11の動作は改質制御手段13aが制御する。
制御装置13は、パワーコンディショナ9の動作、例えば、燃料電池FCの出力電流を制御する。
In the fuel cell system illustrated in FIG. 1, the power generated by the fuel cell FC is configured to be supplied to the power conditioner 9.
The control device 13 controls operations of various devices provided in the fuel cell system. Specifically, the reforming control means 13 a, which is a function of the control device 13, controls the amount of raw fuel supplied to the reformer 2 and the amount of water supplied to the steam generator 6. The supply amount of the raw fuel to the reformer 2, that is, the supply amount of the raw fuel to the desulfurizer 1 can be adjusted by a raw fuel flow rate adjustment valve 10 as a flow rate adjusting means provided on the upstream side of the desulfurizer 1. is there. Further, steam is supplied to the reformer 2 via a steam supply path. This water vapor is generated by the water vapor generator 6. Water is supplied to the steam generator 6 through a water supply path. The amount of water supplied to the steam generator 6 can be adjusted by a pump 11 serving as a water supply amount adjusting means provided on the upstream side of the steam generator 6. The operations of the raw fuel flow rate adjusting valve 10 and the pump 11 are controlled by the reforming control means 13a.
The control device 13 controls the operation of the power conditioner 9, for example, the output current of the fuel cell FC.

水素含有ガス生成装置は、水蒸気発生器6と改質器2との間の流路途中に設けられて、水蒸気の流量を制限する流量制限手段7を備える。例えば、流量制限手段7としてオリフィスを用いることができる。他にも、開度を調節可能な弁によって水蒸気の流量を制限するような流量制限手段7を用いてもよい。   The hydrogen-containing gas generation device includes a flow rate limiting unit 7 provided in the middle of the flow path between the water vapor generator 6 and the reformer 2 to limit the flow rate of water vapor. For example, an orifice can be used as the flow restriction means 7. In addition, a flow rate limiting means 7 that limits the flow rate of water vapor with a valve whose opening degree can be adjusted may be used.

加えて、水素含有ガス生成装置は、水蒸気発生器6から改質器2に供給される水蒸気の量を推定可能な圧力値を、水蒸気発生器6に供給される水又は水蒸気発生器6で発生された水蒸気が流通する流路内で検出する圧力検出器12を備える。本実施形態では、圧力検出器12は、水蒸気発生器6よりも上流側、即ち、ポンプ11と水蒸気発生器6との間に設けられている。圧力検出器12をこの位置に設けることで、水蒸気発生器6での圧力が圧力検出器12の検出結果に反映されることとなる。   In addition, the hydrogen-containing gas generation device generates a pressure value that can estimate the amount of steam supplied from the steam generator 6 to the reformer 2 in the water supplied to the steam generator 6 or the steam generator 6. A pressure detector 12 is provided for detection in a flow path through which the water vapor flows. In the present embodiment, the pressure detector 12 is provided upstream of the water vapor generator 6, that is, between the pump 11 and the water vapor generator 6. By providing the pressure detector 12 at this position, the pressure in the water vapor generator 6 is reflected in the detection result of the pressure detector 12.

更に、本実施形態において、圧力検出器12は、流量制限手段7よりも上流側の、水蒸気発生器6に供給される水又は水蒸気発生器6で発生された水蒸気が流通する流路内の圧力を検出する位置に設けられている。この圧力検出器12が設けられている位置は、水蒸気発生器6から改質器2へ流れる水蒸気の流量が流量制限手段7によって制限されることにより、検出される圧力値が、流量制限手段7よりも上流側の水蒸気発生器6で発生した水蒸気による圧力をより良く代表することとなる位置である。その結果、改質制御手段13aは、圧力検出器12が検出する圧力値に基づいて、水蒸気発生器6から改質器2に供給される水蒸気の量を更に高い精度で知ることができる。   Furthermore, in the present embodiment, the pressure detector 12 is a pressure in a flow path upstream of the flow rate restricting means 7 and through which water supplied to the steam generator 6 or steam generated by the steam generator 6 flows. Is provided at a position to detect. The position where the pressure detector 12 is provided is that the flow rate of water vapor flowing from the steam generator 6 to the reformer 2 is restricted by the flow restriction means 7, so that the detected pressure value is the flow restriction means 7. This is a position that better represents the pressure due to the steam generated by the steam generator 6 on the upstream side. As a result, the reforming control means 13a can know the amount of steam supplied from the steam generator 6 to the reformer 2 with higher accuracy based on the pressure value detected by the pressure detector 12.

また、圧力検出器12による検出結果の精度を更に高めるために、温度検出器14の検出結果を用いることもできる。具体的には、本実施形態の水素含有ガス生成装置は、圧力検出器12が圧力値を検出する部位での温度を検出する温度検出器14を備え、改質制御手段13aは、温度検出器14の検出結果に基づいて、圧力検出器12の検出結果を補正換算する。尚、どのような補正演算式を用いて、圧力検出器12の検出結果を温度で補正するのかは適宜設定可能である。   Further, in order to further improve the accuracy of the detection result by the pressure detector 12, the detection result of the temperature detector 14 can be used. Specifically, the hydrogen-containing gas generation apparatus of the present embodiment includes a temperature detector 14 that detects the temperature at a portion where the pressure detector 12 detects the pressure value, and the reforming control means 13a includes the temperature detector. Based on the detection result of 14, the detection result of the pressure detector 12 is corrected and converted. It should be noted that it is possible to appropriately set which correction calculation formula is used to correct the detection result of the pressure detector 12 with the temperature.

本実施形態では、改質制御手段13aは、改質器2での水素含有ガスの生成量を増加させるために改質器2への原燃料の供給量と水蒸気発生器6への水の供給量とを共に増加変化させるとき、改質器2への原燃料の供給量を増加変化させる時点よりも前に水蒸気発生器6への水の供給量を増加変化させる。特に、改質制御手段13aは、改質器2での水素含有ガスの生成量を増加させるとき、水蒸気発生器6への水の供給量を増加変化させた後の圧力検出器12の検出結果に基づいて、改質器2への原燃料の供給量を増加変化させるタイミングを決定する。   In the present embodiment, the reforming control means 13 a supplies the raw fuel to the reformer 2 and the water to the steam generator 6 in order to increase the amount of hydrogen-containing gas produced in the reformer 2. When both are increased, the amount of water supplied to the steam generator 6 is increased before the time when the amount of raw fuel supplied to the reformer 2 is increased. In particular, when the reforming control means 13a increases the production amount of the hydrogen-containing gas in the reformer 2, the detection result of the pressure detector 12 after changing the supply amount of water to the steam generator 6 is increased. Based on the above, the timing for increasing the supply amount of the raw fuel to the reformer 2 is determined.

図2は、改質器2での水素含有ガスの生成量を増加させるときの各機器の動作状態の推移を説明するタイミング図である。具体的には、燃料電池FCの出力上昇指令が発生した後での、ポンプ11によって調節される「水蒸気発生器6への水の供給量」、「圧力検出器12の検出値」、原燃料流量調節弁10によって調節される「脱硫器1への原燃料の供給量」、パワーコンディショナ9によって調節される「燃料電池FCの出力電流」の推移を示す。
以下、図1及び図2を参照して、水素含有ガス生成装置において行われる水素含有ガス生成量調節方法について説明する。
FIG. 2 is a timing diagram for explaining the transition of the operating state of each device when the amount of hydrogen-containing gas produced in the reformer 2 is increased. Specifically, after the output increase command of the fuel cell FC is generated, “the amount of water supplied to the steam generator 6”, “the detection value of the pressure detector 12” adjusted by the pump 11, raw fuel Changes in “the amount of raw fuel supplied to the desulfurizer 1” adjusted by the flow rate control valve 10 and “the output current of the fuel cell FC” adjusted by the power conditioner 9 are shown.
Hereinafter, with reference to FIG.1 and FIG.2, the hydrogen-containing gas production amount adjustment method performed in a hydrogen-containing gas production | generation apparatus is demonstrated.

図2に示す時刻t0において燃料電池FCの出力上昇指令が発生したとき、制御装置13の改質制御手段13aは、時刻t0以後に、改質器2での水素含有ガスの生成量を目標生成量へと増加させるために、改質器2への原燃料の供給量を目標原燃料量へと増加変化させ、水蒸気発生器6への水の供給量を目標水量へと増加変化させるような制御を行う。但し、時刻t0において改質制御手段13aは、改質器2への原燃料の供給量を目標原燃料量へと増加変化させることなく、先ず、水蒸気発生器6への水の供給量を目標水量へと増加変化させ始め、時刻t2において水蒸気発生器6への水の供給量を目標水量まで増加変化させる調節を完了する。   When a command to increase the output of the fuel cell FC is generated at time t0 shown in FIG. 2, the reforming control means 13a of the control device 13 sets the generation amount of the hydrogen-containing gas in the reformer 2 as the target generation after time t0. In order to increase the amount, the amount of raw fuel supplied to the reformer 2 is increased to the target raw fuel amount, and the amount of water supplied to the steam generator 6 is increased to the target water amount. Take control. However, at time t0, the reforming control means 13a first sets the target amount of water supplied to the steam generator 6 without increasing the supply amount of the raw fuel to the reformer 2 to the target raw fuel amount. Starting to increase the amount of water, the adjustment for increasing the amount of water supplied to the steam generator 6 to the target water amount at time t2 is completed.

また、時刻t0において水蒸気発生器6への水の供給量が増加し始めると、一定の時間遅れをもって水蒸気発生器6での水蒸気の生成量も増加し始めるため、時刻t1において圧力検出器12で検出される圧力値も上昇し始める。そして、時刻t3において、圧力検出器12で検出される圧力値は、上記目標水量に対応した目標圧力値となる。図3は、目標水量と目標圧力値との関係を示すグラフ、即ち、水蒸気発生器6に対して目標水量の水を供給して、その目標水量の水が全て蒸発されたとき、圧力検出器12で検出される圧力値がどれだけになるのかを示すグラフである。つまり、目標水量に増加変化させた後、圧力検出器12で検出される圧力値が図3に示された目標圧力値になると、その目標水量の水が全て蒸発されて、改質器2へ目標水蒸気量の水蒸気が供給されていると見なすことができる。本実施形態では、図3に示したような目標水量と目標圧力値との関係が、制御装置13に内蔵される記憶部又は制御装置13が読み出し可能な記憶装置に予め記憶されており、制御装置13の改質制御手段13aが目標水量と目標圧力値との関係を適宜読み出すものとする。   Further, when the supply amount of water to the steam generator 6 starts to increase at time t0, the amount of steam generated in the steam generator 6 also starts to increase with a certain time delay, so that the pressure detector 12 at time t1. The detected pressure value also begins to rise. At time t3, the pressure value detected by the pressure detector 12 becomes a target pressure value corresponding to the target water amount. FIG. 3 is a graph showing the relationship between the target water amount and the target pressure value, that is, when the target water amount of water is supplied to the steam generator 6 and all of the target water amount is evaporated, the pressure detector 12 is a graph showing how much pressure value is detected at 12; That is, when the pressure value detected by the pressure detector 12 reaches the target pressure value shown in FIG. 3 after increasing the target water amount, all the water of the target water amount is evaporated to the reformer 2. It can be considered that the target water vapor amount is supplied. In the present embodiment, the relationship between the target water amount and the target pressure value as shown in FIG. 3 is stored in advance in a storage unit built in the control device 13 or a storage device that can be read by the control device 13. It is assumed that the reforming control means 13a of the apparatus 13 reads the relationship between the target water amount and the target pressure value as appropriate.

時刻t3において制御装置13の改質制御手段13aは、水蒸気発生器6への水の供給量を目標水量へと増加させた後の圧力検出器12の検出値が、その目標水量に対応した目標圧力値になると、脱硫器1への原燃料の供給量を目標原燃料量へと増加変化させる。その結果、改質器2に供給される原燃料中のカーボンに対する水蒸気の当量比(S/C)を適切な範囲に保った状態で、原燃料の水蒸気改質が行なわれるようになる。これにより、改質器2でのコーキングの発生や、水蒸気不足によって、改質処理により得られる水素ガス中のCOの濃度が上昇するなどの問題の発生を抑制できる。   At time t3, the reforming control means 13a of the control device 13 determines that the detected value of the pressure detector 12 after increasing the amount of water supplied to the steam generator 6 to the target water amount corresponds to the target water amount. When the pressure value is reached, the supply amount of the raw fuel to the desulfurizer 1 is increased and changed to the target raw fuel amount. As a result, steam reforming of the raw fuel is performed in a state where the equivalent ratio (S / C) of water vapor to carbon in the raw fuel supplied to the reformer 2 is maintained in an appropriate range. Thereby, generation | occurrence | production of problems, such as generation | occurrence | production of coking in the reformer 2, and the density | concentration of CO in hydrogen gas obtained by a reforming process by water vapor | steam shortage, can be suppressed.

また、時刻t3において制御装置13は、脱硫器1への原燃料の供給量の増加変化と合わせて、燃料電池FCの出力電流をパワーコンディショナ9の動作を制御して目標電流値へと増加変化させる。   At time t3, the control device 13 controls the operation of the power conditioner 9 to increase the output current of the fuel cell FC to the target current value in accordance with the increase in the supply amount of the raw fuel to the desulfurizer 1. Change.

以上のように、本実施形態では、圧力検出器12が、水蒸気発生器6から改質器2に供給される水蒸気の量を推定可能な圧力値を、水蒸気発生器6に供給される水又は水蒸気発生器6で発生された水蒸気が流通する流路内で検出する。つまり、制御装置13の改質制御手段13aは、圧力検出器12が検出する圧力値に基づいて、水蒸気発生器6から改質器2に供給される水蒸気の量を高い精度で知ることができる。その結果、改質制御手段13aは、改質器2に供給される原燃料の量と水蒸気の量とが適切な当量比(S/C)となるように制御できる。   As described above, in the present embodiment, the pressure detector 12 uses the water pressure supplied to the steam generator 6 or the pressure value that can estimate the amount of steam supplied from the steam generator 6 to the reformer 2. Detection is performed in a flow path through which water vapor generated by the water vapor generator 6 flows. That is, the reforming control means 13a of the control device 13 can know the amount of steam supplied from the steam generator 6 to the reformer 2 with high accuracy based on the pressure value detected by the pressure detector 12. . As a result, the reforming control means 13a can control the amount of raw fuel supplied to the reformer 2 and the amount of water vapor so as to have an appropriate equivalent ratio (S / C).

<別実施形態>
上記実施形態では、本発明に係る水素含有ガス生成装置が設けられる燃料電池システムの構成について具体例を挙げて説明したが、その燃料電池システムの構成は適宜変更可能である。例えば、上記実施形態では、水蒸気発生器6を加熱するために熱交換器8及び電気ヒーターHを設けた構成を説明したが、電気ヒーターHを設けない構成であってもよい。また、上記実施形態では、燃料電池FCから排出された排燃料ガスを燃焼器5に供給して燃焼させる構成を説明したが、燃焼器5に上記原燃料として用いる都市ガスなどの他の可燃性ガスを供給して燃焼させるような構成変更を行ってもよい。
他にも、圧力検出器12や温度検出器14の設置位置を変更するような構成変更、流量制限手段7や温度検出器14を設けないような構成変更などを行ってもよい。
<Another embodiment>
In the above-described embodiment, the configuration of the fuel cell system provided with the hydrogen-containing gas generation device according to the present invention has been described with a specific example, but the configuration of the fuel cell system can be changed as appropriate. For example, in the above embodiment, the configuration in which the heat exchanger 8 and the electric heater H are provided in order to heat the steam generator 6 has been described, but the configuration in which the electric heater H is not provided may be used. Moreover, in the said embodiment, although the structure which supplies the exhaust fuel gas discharged | emitted from the fuel cell FC to the combustor 5, and combusts was demonstrated, other combustibility, such as city gas used for the said combustor 5, as said raw fuel The configuration may be changed such that gas is supplied and burned.
In addition, a configuration change in which the installation position of the pressure detector 12 and the temperature detector 14 is changed, or a configuration change in which the flow rate limiting unit 7 and the temperature detector 14 are not provided may be performed.

本発明は、改質器での水蒸気不足の発生を回避可能な水素含有ガス生成装置及び水素含有ガス生成量調節方法に利用できる。   INDUSTRIAL APPLICABILITY The present invention can be used for a hydrogen-containing gas generation device and a hydrogen-containing gas generation amount adjustment method that can avoid the occurrence of steam shortage in a reformer.

2 改質器
6 水蒸気発生器
7 流量制限手段
10 原燃料流量調節弁(流量調節手段)
11 ポンプ(給水量調節手段)
12 圧力検出器
13a 改質制御手段
14 温度検出器
2 Reformer 6 Steam generator 7 Flow rate limiting means 10 Raw fuel flow rate control valve (flow rate control unit)
11 Pump (Water supply amount adjustment means)
12 pressure detector 13a reforming control means 14 temperature detector

Claims (5)

炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素含有ガスを生成する改質器と、
供給される水を蒸発させて、前記改質器に水蒸気を供給する水蒸気発生器と、
前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを制御する改質制御手段とを備え、
前記改質制御手段は、前記改質器での水素含有ガスの生成量を増加させるために前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に増加変化させるとき、前記改質器への原燃料の供給量を増加変化させる時点よりも前に前記水蒸気発生器への水の供給量を増加変化させるように構成されている水素含有ガス生成装置であって、
前記水蒸気発生器から前記改質器に供給される水蒸気の量を推定可能な圧力値を、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内で検出する圧力検出器を備え、
前記改質制御手段は、前記改質器での水素含有ガスの生成量を増加させるとき、前記水蒸気発生器への水の供給量を増加変化させた後の前記圧力検出器の検出結果に基づいて、前記改質器への原燃料の供給量を増加変化させるタイミングを決定するように構成されている水素含有ガス生成装置。
A reformer that produces a hydrogen-containing gas by reforming raw fuel containing hydrocarbons in the presence of steam;
A steam generator for evaporating the supplied water and supplying steam to the reformer;
Reforming control means for controlling the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator;
The reforming control unit increases both the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator in order to increase the amount of hydrogen-containing gas generated in the reformer. A hydrogen-containing gas generator configured to increase and change the amount of water supplied to the steam generator before the time of increasing the amount of raw fuel supplied to the reformer when changing There,
A pressure value capable of estimating the amount of steam supplied from the steam generator to the reformer is set in a flow path through which water supplied to the steam generator or steam generated by the steam generator flows. Equipped with a pressure detector to detect,
The reforming control unit is configured to increase the amount of hydrogen-containing gas generated in the reformer based on the detection result of the pressure detector after increasing the amount of water supplied to the steam generator. A hydrogen-containing gas generator configured to determine a timing for increasing and changing the amount of raw fuel supplied to the reformer.
前記水蒸気発生器と前記改質器との間の流路途中に設けられて、水蒸気の流量を制限する流量制限手段を備え、
前記圧力検出器は、前記流量制限手段よりも上流側の、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内の圧力を検出する請求項1に記載の水素含有ガス生成装置。
Provided in the middle of the flow path between the steam generator and the reformer, comprising a flow rate limiting means for limiting the flow rate of the steam,
The pressure detector detects a pressure in a flow path through which water supplied to the water vapor generator or water vapor generated by the water vapor generator flows, upstream of the flow rate restricting means. The hydrogen-containing gas generating device described.
前記改質制御手段は、前記改質器での水素含有ガスの生成量を目標生成量へと増加させるために、前記改質器への原燃料の供給量を目標原燃料量へと増加変化させ、前記水蒸気発生器への水の供給量を目標水量へと増加変化させるとき、
前記水蒸気発生器への水の供給量を増加させた後の前記圧力検出器の検出値が、前記目標水量に対応した目標圧力値になると、前記改質器への原燃料の供給量を前記目標原燃料量へと増加変化させるタイミングであると決定するように構成されている請求項1又は2に記載の水素含有ガス生成装置。
The reforming control means increases the supply amount of the raw fuel to the reformer to the target raw fuel amount in order to increase the production amount of the hydrogen-containing gas in the reformer to the target production amount. When the supply amount of water to the steam generator is increased and changed to the target water amount,
When the detection value of the pressure detector after increasing the supply amount of water to the steam generator becomes a target pressure value corresponding to the target water amount, the supply amount of raw fuel to the reformer is The hydrogen-containing gas generation device according to claim 1, wherein the hydrogen-containing gas generation device is configured to determine that it is a timing of increasing and changing to a target raw fuel amount.
前記圧力検出器が圧力値を検出する部位での温度を検出する温度検出器を備え、
前記改質制御手段は、前記温度検出器の検出結果に基づいて、前記圧力検出器の検出結果を補正換算する請求項1〜3の何れか一項に記載の水素含有ガス生成装置。
The pressure detector comprises a temperature detector that detects the temperature at the site where the pressure value is detected,
The hydrogen-containing gas generating device according to any one of claims 1 to 3, wherein the reforming control unit corrects and converts the detection result of the pressure detector based on the detection result of the temperature detector.
炭化水素を含む原燃料を水蒸気の存在下で改質処理して水素含有ガスを生成する改質器と、供給される水を蒸発させて、前記改質器に水蒸気を供給する水蒸気発生器とを備える水素含有ガス生成装置において、前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に制御することで前記改質器での水素含有ガスの生成量を調節する水素含有ガス生成量調節方法であって、
前記改質器での水素含有ガスの生成量を増加させるために前記改質器への原燃料の供給量と前記水蒸気発生器への水の供給量とを共に増加変化させるとき、前記改質器への原燃料の供給量を増加変化させる時点よりも前に前記水蒸気発生器への水の供給量を増加変化させ、前記水蒸気発生器への水の供給量を増加変化させた後の、前記水蒸気発生器に供給される水又は前記水蒸気発生器で発生された水蒸気が流通する流路内での圧力値に基づいて、前記改質器への原燃料の供給量を増加変化させるタイミングを決定する水素含有ガス生成量調節方法。
A reformer that reforms raw fuel containing hydrocarbons in the presence of steam to generate a hydrogen-containing gas; and a steam generator that evaporates supplied water and supplies steam to the reformer. The amount of hydrogen-containing gas produced in the reformer by controlling both the amount of raw fuel supplied to the reformer and the amount of water supplied to the steam generator A method for adjusting the amount of hydrogen-containing gas produced by adjusting
When the supply amount of raw fuel to the reformer and the supply amount of water to the steam generator are both increased and changed in order to increase the amount of hydrogen-containing gas generated in the reformer, the reforming After increasing the supply amount of water to the steam generator before the time of increasing the supply amount of raw fuel to the steam generator, and after increasing the supply amount of water to the steam generator, The timing for increasing and changing the supply amount of raw fuel to the reformer based on the pressure value in the flow path through which the water supplied to the steam generator or the steam generated by the steam generator flows. A method for adjusting the production amount of hydrogen-containing gas to be determined.
JP2012189109A 2012-08-29 2012-08-29 Hydrogen-containing gas generator, and method of adjusting generation rate of hydrogen-containing gas Pending JP2014047083A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016067589A1 (en) * 2014-10-29 2016-05-06 パナソニックIpマネジメント株式会社 Hydrogen generation device, method for operating same, and fuel cell system
JP2021193060A (en) * 2020-06-08 2021-12-23 株式会社神戸製鋼所 Reforming unit and hydrogen production device
CN115805045A (en) * 2022-10-14 2023-03-17 清华大学 Aluminum water hydrogen production device and control method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016067589A1 (en) * 2014-10-29 2016-05-06 パナソニックIpマネジメント株式会社 Hydrogen generation device, method for operating same, and fuel cell system
JP2021193060A (en) * 2020-06-08 2021-12-23 株式会社神戸製鋼所 Reforming unit and hydrogen production device
JP7370934B2 (en) 2020-06-08 2023-10-30 株式会社神戸製鋼所 Reforming unit and hydrogen production equipment
CN115805045A (en) * 2022-10-14 2023-03-17 清华大学 Aluminum water hydrogen production device and control method thereof
CN115805045B (en) * 2022-10-14 2024-04-09 清华大学 Control method of aluminum water hydrogen production device

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