JP2012041851A - Heating value adjusting device - Google Patents

Heating value adjusting device Download PDF

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JP2012041851A
JP2012041851A JP2010183136A JP2010183136A JP2012041851A JP 2012041851 A JP2012041851 A JP 2012041851A JP 2010183136 A JP2010183136 A JP 2010183136A JP 2010183136 A JP2010183136 A JP 2010183136A JP 2012041851 A JP2012041851 A JP 2012041851A
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JP5608011B2 (en
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Koji Matsuda
考司 松田
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Osaka Gas Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

PROBLEM TO BE SOLVED: To provide a heating value adjusting device that has a simple structure and appropriately adjusts the heating value of mixed gas while suppressing the facility cost.SOLUTION: This heating value adjusting device includes a flow rate adjusting means 13 for adjusting the flow rate of fuel gas G2 for heat increase flowing through a fuel gas supply system 11 for heat increase, a first mass flow rate measuring means 14 for measuring a first mass flow rate, which is the first mass flow rate of mixed gas G3 having a target heating value demanded for the mixed gas G3 after heat increase in a mixed gas supply system 12, and a first controlling means 15 for generating a first control command for adjusting the heating value of the mixed gas G3 to the target heating value based on the first mass flow rate measured by the first mass flow rate measuring means 14. The flow rate adjusting means 13 receives the first control command generated in the first controlling means 15, and adjusts the flow rate of the fuel gas G2 for heat increase flowing through the fuel gas supply system 11 for heat increase.

Description

本発明は、主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスの増熱用に混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、所定の目標熱量に調整した混合ガスを燃料ガス消費部へ導く熱量調整装置に関する。   The present invention provides a main fuel gas supply system for flowing main fuel gas in a predetermined pressure state, and an increase in which a heat increasing fuel gas mixed for increasing the heat of the main fuel gas is flowed in a predetermined pressure state. A fuel gas supply system for heat and a gas mixture supply system through which a mixed gas obtained by mixing the main fuel gas with the fuel gas for increasing heat flows, and the mixed gas adjusted to a predetermined target heat amount is consumed as fuel gas It is related with the calorie | heat amount adjustment apparatus guide | induced to a part.

従来、主燃料ガスに増熱用燃料ガスを混合した混合ガスを所望の目標熱量に調整して、下流側の燃料ガス消費部等に供給する熱量調整装置では、主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、主燃料ガスに増熱用燃料ガスが混合された混合ガスを通流する混合ガス供給系統と、当該混合ガス供給系統を通流する混合ガスの熱量を測定する熱量計と、増熱用燃料ガス供給系統にて増熱用燃料ガスの流量を調整する流量調整手段と、熱量計の計測結果に基づいて流量調整手段を制御する制御手段とを備えている。
当該熱量調整装置では、熱量計により直接混合ガスの熱量を測定して、当該熱量が所望の目標熱量となるように制御手段が流量調整手段を制御して、主燃料ガスに混合される増熱用燃料ガスの流量を調整している(特許文献1を参照。)。
Conventionally, in a calorific value adjusting device that adjusts a mixed gas obtained by mixing a fuel gas for increasing heat to a main fuel gas to a desired target calorific value and supplies it to a fuel gas consuming unit on the downstream side, the main fuel gas is in a predetermined pressure state. A main fuel gas supply system through which the heat increase fuel gas flows in a predetermined pressure state, and a mixed gas in which the main fuel gas is mixed with the heat increase fuel gas. A mixed gas supply system that flows, a calorimeter that measures the amount of heat of the mixed gas flowing through the mixed gas supply system, and a flow rate adjustment that adjusts the flow rate of the fuel gas for increasing heat in the fuel gas supplying system for increasing heat And a control means for controlling the flow rate adjusting means based on the measurement result of the calorimeter.
In the calorific value adjusting device, the heat quantity of the mixed gas is directly measured by a calorimeter, and the control means controls the flow rate adjusting means so that the calorific value becomes a desired target calorific value, and the heat increase mixed with the main fuel gas. The fuel gas flow rate is adjusted (see Patent Document 1).

実公平6−22429号Reality 6-22429

しかしながら、通常、熱量計として知られるガスクロ(高精度成分分析器)は、構造が複雑で、比較的高価であった。このため、当該熱量計を用いた熱量調整装置では、構造が複雑となり、設備コストがかかるという問題があった。   However, a gas chromatograph (high-accuracy component analyzer) commonly known as a calorimeter has a complicated structure and is relatively expensive. For this reason, in the calorie | heat amount adjustment apparatus using the said calorimeter, there existed a problem that a structure became complicated and installation cost started.

本発明は、上述の課題に鑑みてなされたものであり、その目的は、構造が簡単で、製造コストを抑制できながらも、適切に混合ガスの熱量を調整可能な熱量調整装置を提供する点にある。   The present invention has been made in view of the above-described problems, and an object of the present invention is to provide a calorific value adjusting device capable of appropriately adjusting the calorific value of a mixed gas while having a simple structure and suppressing the manufacturing cost. It is in.

上記目的を達成するための本発明の熱量調整装置は、主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、その第1特徴構成は、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記第1質量流量計測手段により計測される前記第1質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第1制御指令を生成する第1制御手段を備え、
前記流量調整手段が、前記第1制御手段に生成される前記第1制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する点にある。
In order to achieve the above object, a calorific value adjusting device according to the present invention comprises a main fuel gas supply system that allows main fuel gas to flow in a predetermined pressure state, and a heat-increasing fuel gas mixed with the main fuel gas. A fuel gas supply system for increasing heat that flows in a pressure state, and a gas supply system that supplies a mixed gas in which the fuel gas for increasing heat is mixed with the main fuel gas. A calorific value adjusting device that adjusts the mixed gas guided to the downstream side to a target calorific value, the first characteristic configuration is:
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
Based on the first mass flow rate measured by the first mass flow rate measurement means, comprising first control means for generating a first control command for adjusting the heat quantity of the mixed gas to the target heat quantity,
The flow rate adjusting means receives the first control command generated by the first control means and adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system. .

本発明は、質量流量計測手段(具体的には、計器に設定される所定の質量のガスの流量を計測する質量流量計)が測定する質量流量が、燃料ガスの熱量に対応する点に着目し、この質量流量計測手段により計測される質量流量の増減に従って、主燃料ガスに混合する増熱用燃料ガスの量を調整することができることを見出して、完成したものである。
本願にあって、質量流量計測手段(具体的には質量流量計)とは、上述の「計器で計測すべき所定の質量(所定体積当りの質量)」の設定が可能な計測機器であり、その出力である質量流量は、例えば「リットル/min」のように、体積流量の形態で出力される。従って、「設定される所定の質量」×「出力(リットル/min)」により、測定部位を流れる流体の質量を知ることができる。
即ち、第1質量流量計測手段、第1制御手段及び流量調整手段を備えた構成にあっては、第1質量流量計測手段は、その設置位置において、要求される混合ガスの目標熱量を有する所定質量のガスの流量(第1質量流量)を測定する。そして、当該設置位置を流れる混合ガスの熱量が、前記の目標熱量に対して不足している場合は、流量は低流量側の値として計測される。
このように低流量側の流量が計測される場合、混合ガスの熱量が不足している(所定質量の混合ガスが流れていない)こととなるため、第1制御手段にあっては、主燃料ガスに混合する増熱用燃料ガスを現状より増加させる第1制御指令を生成し、この第1制御指令に従って、流量調整手段が働く。結果、一般的な質量流量計を混合ガス供給系統に設置するだけで、混合ガスの増熱における熱量調整を、簡易かつ低コストで実現できる。
The present invention pays attention to the fact that the mass flow rate measured by the mass flow rate measuring means (specifically, the mass flow meter for measuring the flow rate of the gas having a predetermined mass set in the meter) corresponds to the heat amount of the fuel gas. However, the present inventors have found that the amount of the heat increasing fuel gas mixed with the main fuel gas can be adjusted according to the increase or decrease of the mass flow rate measured by the mass flow rate measuring means.
In the present application, the mass flow rate measuring means (specifically, the mass flow meter) is a measuring device capable of setting the above-mentioned “predetermined mass to be measured by a meter (mass per predetermined volume)”. The output mass flow rate is output in the form of a volume flow rate, for example, “liter / min”. Accordingly, it is possible to know the mass of the fluid flowing through the measurement site by “predetermined mass to be set” × “output (liter / min)”.
That is, in the configuration including the first mass flow measurement means, the first control means, and the flow rate adjustment means, the first mass flow measurement means has a predetermined target heat amount of the mixed gas at the installation position. The mass gas flow rate (first mass flow rate) is measured. And when the calorie | heat amount of the mixed gas which flows through the said installation position is insufficient with respect to the said target calorie | heat amount, a flow volume is measured as a value on the low flow rate side.
When the flow rate on the low flow rate side is measured in this way, the amount of heat of the mixed gas is insufficient (the mixed gas of a predetermined mass is not flowing). Therefore, in the first control means, the main fuel A first control command for increasing the heat-increasing fuel gas mixed with the gas from the current state is generated, and the flow rate adjusting means operates according to the first control command. As a result, by simply installing a general mass flow meter in the mixed gas supply system, it is possible to easily and inexpensively adjust the amount of heat in increasing the temperature of the mixed gas.

ここで、第1制御手段における第1制御指令の生成に関しては、第1質量流量計測手段の計測値に従って、前記流量調整手段による増熱用燃料ガスの流量調整を行った場合の制御特性を予め調べておいて、例えば、比例制御、一次遅れ制御、積分制御等を行えるように構成しておけばよい。
以上より、本願独特の第1質量流量測定手段及び第1制御手段を用いることで、比較的構造が簡単で、製造コストを抑制できながらも、適切に熱量調整が可能な熱量調整装置を実現できる。
Here, regarding the generation of the first control command in the first control means, the control characteristics when the flow rate adjustment of the fuel gas for heat increase by the flow rate adjustment means is performed in advance according to the measurement value of the first mass flow rate measurement means. For example, it may be configured to perform proportional control, first-order lag control, integral control, and the like.
As described above, by using the first mass flow rate measuring means and the first control means unique to the present application, it is possible to realize a heat quantity adjusting device capable of appropriately adjusting the heat quantity while having a relatively simple structure and suppressing the manufacturing cost. .

〔第2特徴構成〕
本発明の熱量調整装置の更なる特徴構成は、
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
主燃料ガス供給系統を通流する主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備えるとともに、
前記第2質量流量計測手段により計測される前記第2質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第2制御指令を生成する第2制御手段を備え、
前記流量調整手段が、前記第2制御手段に生成される前記第2制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する点にある。
[Second feature configuration]
A further characteristic configuration of the heat quantity adjusting device of the present invention is as follows.
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having a main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system is provided in the main fuel gas supply system. And prepare for
Based on the second mass flow rate measured by the second mass flow rate measurement means, comprising second control means for generating a second control command for adjusting the heat quantity of the mixed gas to the target heat quantity,
The flow rate adjusting means adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system in response to the second control command generated by the second control means. .

この発明も、質量流量計測手段(具体的には、計器に設定される所定の質量のガスの流量を計測する質量流量計)が測定する質量流量が、燃料ガスの熱量に対応する点に着目し、この質量流量計測手段により計測される質量流量の増減に従って、主燃料ガスに混合する増熱用燃料ガスの流量を調整することができることを見出して完成した。
即ち、第2質量流量計測手段、第2制御手段及び流量調整手段を備えた構成にあっては、第2質量流量計測手段は、その設置位置において、要求される主燃料ガスの主燃料ガス熱量を有する所定質量のガスの流量(第2質量流量)を測定する。そして、当該設置位置を流れる主燃料ガスの熱量が、前記の要求される主燃料ガス熱量に対して不足している場合は、第2質量流量は低流量側の値として計測される。
このように低流量側の流量が計測された場合、所定比の増熱用燃料ガスを主燃料ガスに混合したとしても混合ガスの熱量が不足することとなるため、第2制御手段にあっては、主燃料ガスに混合する増熱用燃料ガスを現状より増加させる第2制御指令を生成し、この第2制御指令に従って、流量調整手段が働く。結果、一般的な質量流量計を主燃料ガス供給系統に設置するだけで、混合ガスの増熱における熱量調整を、簡易かつ低コストで実現できる。
This invention also pays attention to the fact that the mass flow rate measured by the mass flow rate measuring means (specifically, the mass flow meter for measuring the flow rate of the gas having a predetermined mass set in the meter) corresponds to the heat amount of the fuel gas. The present inventors have found that the flow rate of the heat-increasing fuel gas mixed with the main fuel gas can be adjusted according to the increase / decrease in the mass flow rate measured by the mass flow rate measuring means.
That is, in the configuration including the second mass flow rate measuring means, the second control means, and the flow rate adjusting means, the second mass flow rate measuring means has the required main fuel gas calorie of the main fuel gas at the installation position. A flow rate (second mass flow rate) of a gas having a predetermined mass is measured. When the amount of heat of the main fuel gas flowing through the installation position is insufficient with respect to the required amount of heat of the main fuel gas, the second mass flow rate is measured as a value on the low flow rate side.
When the flow rate on the low flow rate side is measured in this way, the heat amount of the mixed gas is insufficient even if the fuel gas for increasing the heat in a predetermined ratio is mixed with the main fuel gas. Generates a second control command for increasing the heat-increasing fuel gas mixed with the main fuel gas from the current state, and the flow rate adjusting means operates according to the second control command. As a result, by simply installing a general mass flow meter in the main fuel gas supply system, it is possible to easily and inexpensively adjust the amount of heat in increasing the temperature of the mixed gas.

〔第3特徴構成〕
本発明の熱量調整装置の更なる特徴構成は、
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
主燃料ガス供給系統を通流する主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備え、
前記第1質量流量計測手段及び前記第2質量流量計測手段により計測される前記第1質量流量、及び前記第2質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第3制御指令を生成する第3制御手段を備え、
前記流量調整手段が、前記第3制御手段に生成される前記第3制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する点にある。
[Third feature configuration]
A further characteristic configuration of the heat quantity adjusting device of the present invention is as follows.
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
A second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having a main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system is provided in the main fuel gas supply system. In preparation for
Third control for adjusting the heat amount of the mixed gas to the target heat amount based on the first mass flow rate and the second mass flow rate measured by the first mass flow rate measuring unit and the second mass flow rate measuring unit. A third control means for generating a command;
The flow rate adjusting means receives the third control command generated by the third control means and adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system. .

この発明も、質量流量計測手段(具体的には、計器に設定される所定の質量のガスの流量を計測する質量流量計)が測定する質量流量が、燃料ガスの熱量に対応する点に着目し、この質量流量計測手段により計測される質量流量の増減に従って、主燃料ガスに混合する増熱用燃料ガスの流量を調整することができることを見出して完成した。
即ち、第1質量流量計測手段、第2質量流量計測手段、第3制御手段及び流量調整手段を備えた構成にあっては、第1質量流量計測手段は、その設置位置において、要求される混合ガスの目標熱量の所定質量を有するガスの流量(第1質量流量としての値)を測定する。一方、第2質量流量計測手段は、その測定位置において、要求される主燃料ガス熱量を有する所定質量のガスの流量(第2質量流量としての値)を測定する。ここで、増熱用燃料ガスが、主燃料ガスに対して適切な比で混合された場合、第1質量流量計測手段で計測される流量は、混合に伴うガス質量の増加(増熱)に寄与するだけであるため、結果的に、第1質量流量計測手段により計測される第1質量流量としての値と、第2質量流量計測手段により計測される第2質量流量としての値とは一致する。
This invention also pays attention to the fact that the mass flow rate measured by the mass flow rate measuring means (specifically, the mass flow meter for measuring the flow rate of the gas having a predetermined mass set in the meter) corresponds to the heat amount of the fuel gas. The present inventors have found that the flow rate of the heat-increasing fuel gas mixed with the main fuel gas can be adjusted according to the increase / decrease in the mass flow rate measured by the mass flow rate measuring means.
That is, in the configuration provided with the first mass flow measurement means, the second mass flow measurement means, the third control means, and the flow rate adjustment means, the first mass flow measurement means has the required mixing at the installation position. The flow rate of gas having a predetermined mass of the target heat quantity of gas (value as the first mass flow rate) is measured. On the other hand, the second mass flow rate measuring means measures a flow rate (a value as the second mass flow rate) of a predetermined mass gas having the required amount of heat of the main fuel gas at the measurement position. Here, when the fuel gas for heat increase is mixed at an appropriate ratio with respect to the main fuel gas, the flow rate measured by the first mass flow rate measuring means is the increase (heat increase) of the gas mass accompanying the mixing. As a result, the value as the first mass flow rate measured by the first mass flow rate measuring unit coincides with the value as the second mass flow rate measured by the second mass flow rate measuring unit. To do.

従って、第3制御手段にあっては、第1質量流量としての値と第2質量流量としての値とが一致するように、第3制御指令を生成し、この第3制御指令に従って、流量調整手段が働く。結果、一般的な質量流量計を主燃料ガス供給系統に設置するだけで、混合ガスの増熱における熱量調整を、簡易かつ低コストで実現できる。   Therefore, in the third control means, a third control command is generated so that the value as the first mass flow rate and the value as the second mass flow rate coincide with each other, and the flow rate adjustment is performed according to the third control command. Means work. As a result, by simply installing a general mass flow meter in the main fuel gas supply system, it is possible to easily and inexpensively adjust the amount of heat in increasing the temperature of the mixed gas.

ここで、第3制御手段における第3制御指令の生成に関しては、第1質量流量計測手段及び第2質量流量計測手段の計測値に従って、流量調整手段による増熱用燃料ガスの流量調整を行った場合の制御特性を調べておいて、例えば、比例制御、一次遅れ制御、積分制御等を行えるように構成しておけばよい。   Here, regarding the generation of the third control command in the third control unit, the flow rate of the fuel gas for heat increase was adjusted by the flow rate adjusting unit according to the measurement values of the first mass flow rate measuring unit and the second mass flow rate measuring unit. The control characteristics of the case may be examined, and for example, it may be configured so that proportional control, first-order lag control, integration control, and the like can be performed.

これまで説明してきた発明にあっては、混合ガスの熱量を所望の熱量である目標熱量に調整する(増熱する)ことを目的とした構成に関し説明した。
以下の説明では、上記の目標熱量への調整(増熱)に加えて、燃料ガス消費部へ供給される総熱量の制御(増熱されて所定の目標熱量の混合ガスを所定の流量供給する制御)に関して説明する。
In the invention described so far, the configuration for the purpose of adjusting (increasing the heat) the heat amount of the mixed gas to the target heat amount which is a desired heat amount has been described.
In the following description, in addition to the above adjustment (increase in heat) to the target heat amount, control of the total heat amount supplied to the fuel gas consumption unit (supplied heat and supply of a mixed gas having a predetermined target heat amount at a predetermined flow rate) Control) will be described.

〔第4特徴構成〕
本発明の熱量調整装置の更なる特徴構成は、
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記混合ガス供給系統を通流する前記混合ガスの容積流量を測定する容積流量測定手段を備え、
前記第1質量流量計測手段により計測される前記第1質量流量及び前記容積流量測定手段により測定される容積流量に基づいて、前記混合ガスの熱量を前記目標熱量に、前記混合ガスの容積流量を目標流量に調整する第4制御指令を生成する第4制御手段を備え、
前記流量調整手段が、前記第4制御手段に生成される前記第4制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する点にある。
[Fourth feature configuration]
A further characteristic configuration of the heat quantity adjusting device of the present invention is as follows.
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
A volumetric flow rate measuring means for measuring a volumetric flow rate of the mixed gas flowing through the mixed gas supply system;
Based on the first mass flow rate measured by the first mass flow rate measuring means and the volumetric flow rate measured by the volumetric flow rate measuring means, the heat amount of the mixed gas is set as the target heat amount, and the volume flow rate of the mixed gas is set as the target heat amount. A fourth control means for generating a fourth control command for adjusting to the target flow rate;
The flow rate adjusting means receives the fourth control command generated by the fourth control means, and adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system. .

この構成にあっても、混合ガスの増熱に関しては、第1質量計測手段の計測値を、上記第1特徴構成にて説明した制御構成と同様のものを使用する。即ち、第4制御手段は、先に説明した第1制御手段としての機能部位を備えることで、混合ガスの熱量を目標熱量に調整(増熱調整)する。
また、第4制御手段には、容積流量測定手段により測定される容積流量に基づいて、混合ガスの容積流量を目標流量とする機能部位を備えておく。
ここで、両制御のどちらを優先するかの優劣は、混合ガスの熱量が所定の目標熱量範囲内に収まっていることを条件として、混合ガスの容積流量を所定の目標の流量範囲に収まるように制御するものとできる。
結果、所定の目標熱量の混合ガスを所定の目標流量供給でき、混合ガスの総熱量までをも調整することができることとなる。
Even in this configuration, for the heat increase of the mixed gas, the measurement value of the first mass measuring means is the same as the control configuration described in the first characteristic configuration. That is, a 4th control means adjusts the calorie | heat amount of mixed gas to a target calorie | heat amount (heat increase adjustment) by providing the functional part as a 1st control means demonstrated previously.
Further, the fourth control means is provided with a functional part having the volumetric flow rate of the mixed gas as a target flow rate based on the volumetric flow rate measured by the volumetric flow rate measuring means.
Here, the superiority or inferiority of which control is prioritized is such that the volumetric flow rate of the mixed gas falls within the predetermined target flow rate range, provided that the heat amount of the mixed gas is within the predetermined target heat amount range. Can be controlled.
As a result, a mixed gas having a predetermined target heat amount can be supplied at a predetermined target flow rate, and even the total heat amount of the mixed gas can be adjusted.

〔第5特徴構成〕
本発明の熱量調整装置の更なる特徴構成は、
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記主燃料ガス供給系統を流れる主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備え、
さらに、前記主燃料ガス供給系統を流れる主燃料ガスの比重を測定する比重測定手段を備え、
前記第1質量流量計測手段及び第2質量流量計測手段により計測される前記第1質量流量、及び第2質量流量及び比重測定手段により測定される比重に基づいて、前記混合ガスの熱量を前記目標熱量に、流量を目標流量に調整する第5制御指令を生成する第5制御手段を備え、
前記流量調整手段が、前記第5制御手段に生成される前記第5制御指令受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する点にある。
[Fifth feature configuration]
A further characteristic configuration of the heat quantity adjusting device of the present invention is as follows.
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
The main fuel gas supply system is provided with a second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having the main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system. Prepared,
Furthermore, it comprises specific gravity measuring means for measuring the specific gravity of the main fuel gas flowing through the main fuel gas supply system,
Based on the first mass flow rate measured by the first mass flow rate measurement unit and the second mass flow rate measurement unit and the specific gravity measured by the second mass flow rate and specific gravity measurement unit, the heat quantity of the mixed gas is determined as the target. A fifth control means for generating a fifth control command for adjusting the flow rate to the target flow rate in the amount of heat;
The flow rate adjusting means receives the fifth control command generated by the fifth control means and adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system.

この構成は、先に説明した第3特徴構成をさらに発展させた技術である。
先に説明した第3特徴構成では、第3制御手段は、第1質量流量計測手段により計測される第1質量流量と第2質量流量計測手段により計測される第2質量流量とが一致するように、第3制御指令を生成し、この第3制御指令に従って、流量調整手段が働く。結果、一般的な質量流量計を主燃料ガス供給系統に設置するだけで、混合ガスの増熱における熱量調整を、簡易かつ低コストで実現できる。
そこで、この第5制御手段に、第3制御手段に相当する機能部位を備えておくことで、混合ガスの熱量は目標熱量に調整される。この機能部位のみでは、混合ガスの総熱量までは制御できない。
This configuration is a technology obtained by further developing the third feature configuration described above.
In the third characteristic configuration described above, the third control unit causes the first mass flow rate measured by the first mass flow rate measurement unit and the second mass flow rate measured by the second mass flow rate measurement unit to coincide with each other. In addition, a third control command is generated, and the flow rate adjusting means works according to the third control command. As a result, by simply installing a general mass flow meter in the main fuel gas supply system, it is possible to easily and inexpensively adjust the amount of heat in increasing the temperature of the mixed gas.
Therefore, by providing the fifth control means with a functional portion corresponding to the third control means, the amount of heat of the mixed gas is adjusted to the target amount of heat. Only this functional part cannot control the total amount of heat of the mixed gas.

そこで、主燃料ガス供給系統に比重測定手段を備えて、主燃料ガスの真の比重(主燃料ガスの真の熱量)を計測するものとする。
ここで、第2質量流量計測手段は、主燃料ガスに求められる熱量のガス(発熱量のガス)の質量流量を計測する手段であるため、主燃料ガスの真の比重が判明すると、第2質量流量計測手段において計測される質量流量から、現在流れている主燃料ガスの真の流量が判明する。
そして、先の第3特徴構成に従って、増熱用燃料ガスの混合量を調整した場合、結果的に、現在流れている主燃料ガスの真の流量だけ目標熱量の混合ガスを得ることができることとなり、熱量と流量との制御が可能となる。
Therefore, the main fuel gas supply system is provided with specific gravity measuring means to measure the true specific gravity of the main fuel gas (the true amount of heat of the main fuel gas).
Here, since the second mass flow rate measuring means is a means for measuring the mass flow rate of the calorific gas (calorific value gas) required for the main fuel gas, if the true specific gravity of the main fuel gas is found, From the mass flow rate measured by the mass flow rate measuring means, the true flow rate of the main fuel gas that is currently flowing is determined.
When the mixing amount of the fuel gas for increasing heat is adjusted according to the third characteristic configuration, the mixed gas having the target heat amount can be obtained as much as the true flow rate of the main fuel gas that is currently flowing. It is possible to control the heat quantity and the flow rate.

ここで、第5制御手段における、比重測定手段により比重を得た場合の、第2質量流量計測手段により計測される流量の補正に関しては、予め、比重測定手段の出力及び主燃料ガスとして供給される所定熱量のガスの質量流量を計測する場合の第2質量流量計測手段の出力の関係を調べておいて、上述の補正を行えるように構成しておけばよい。
以上より、本願独特の第1質量流量測定手段、第2質量流量測定手段、比重測定手段及び第5制御手段を用いることで、比較的構造が簡単で、製造コストを抑制できながらも、適切に熱量調整が可能な熱量調整装置を実現できる。
Here, regarding the correction of the flow rate measured by the second mass flow rate measuring unit when the specific gravity is obtained by the specific gravity measuring unit in the fifth control unit, the output of the specific gravity measuring unit and the main fuel gas are supplied in advance. What is necessary is just to comprise so that the above-mentioned correction | amendment can be performed by investigating the relationship of the output of the 2nd mass flow measurement means when measuring the mass flow rate of the gas of the predetermined calorie | heat amount.
From the above, by using the first mass flow measuring means, the second mass flow measuring means, the specific gravity measuring means and the fifth control means unique to the present application, the structure is relatively simple and the manufacturing cost can be suppressed appropriately. A calorific value adjustment device capable of adjusting the calorific value can be realized.

本発明の第1実施形態に係る熱量調整装置の概略構成図である。It is a schematic block diagram of the calorie | heat amount adjustment apparatus which concerns on 1st Embodiment of this invention. 本発明の第2実施形態に係る熱量調整装置の概略構成図である。It is a schematic block diagram of the calorie | heat amount adjustment apparatus which concerns on 2nd Embodiment of this invention. 本発明の第3実施形態に係る熱量調整装置の概略構成図である。It is a schematic block diagram of the calorie | heat amount adjustment apparatus which concerns on 3rd Embodiment of this invention. 本発明の第4実施形態に係る熱量調整装置の概略構成図である。It is a schematic block diagram of the calorie | heat amount adjustment apparatus which concerns on 4th Embodiment of this invention. 本発明の第5実施形態に係る熱量調整装置の概略構成図である。It is a schematic block diagram of the calorie | heat amount adjustment apparatus which concerns on 5th Embodiment of this invention.

本発明の熱量調整装置は、質量流量計測手段(具体的には、計器に設定される所定の質量のガスの流量を計測する質量流量計14、26)が測定する質量流量が、燃料ガスの熱量に対応する点に着目し、この質量流量計14、26により計測される質量流量の増減に従って、主燃料ガスG1に混合する増熱用燃料ガスG2の量を調整することができることを見出して、完成させたものである。
尚、以下に示す、第1、第2、第3実施形態に係る熱量調整装置は、混合ガスG3の熱量を所望の熱量である目標熱量TQ1に調整(増熱する)ことを目的とするものであり、第4、第5実施形態に係る熱量調整装置は、上記の目標熱量TQ1への調整(増熱)に加えて、燃料ガス消費部へ供給される総熱量の制御(増熱されて所定の目標熱量TQ1の混合ガスG3を所定の流量供給する制御)を目的とするものである。
The calorific value adjustment device of the present invention has a mass flow rate measuring means (specifically, mass flow meters 14 and 26 for measuring a flow rate of a gas having a predetermined mass set in a meter) that has a mass flow rate of fuel gas. Focusing on the point corresponding to the amount of heat, it has been found that the amount of the heat-increasing fuel gas G2 mixed with the main fuel gas G1 can be adjusted according to the increase or decrease in the mass flow rate measured by the mass flow meters 14, 26. , Completed.
In addition, the calorie | heat amount adjustment apparatus which concerns on 1st, 2nd, 3rd embodiment shown below aims at adjusting the heat amount of mixed gas G3 to target heat amount TQ1 which is desired heat amount (heat increase). In addition to the adjustment (heat increase) to the target heat amount TQ1 described above, the heat amount adjustment device according to the fourth and fifth embodiments controls the total heat amount supplied to the fuel gas consumption unit (heat is increased). The purpose is to control the supply of a mixed gas G3 having a predetermined target heat quantity TQ1 at a predetermined flow rate.

〔第1実施形態〕
第1実施形態に係る熱量調整装置は、低カロリーの主燃料ガスG1(例えば、都市ガス13A等)に、高カロリーの増熱用燃料ガスG2(例えば、LPG等)を混合して増熱する形態で、主燃料ガスG1に増熱用燃料ガスG2を混合した混合ガスG3を、所望の目標熱量TQ1に調整する。
そして、図1に示す様に、主燃料ガスG1を所定の圧力状態で通流する主燃料ガス供給系統10と、主燃料ガスG1に混合される増熱用燃料ガスG2を所定の圧力状態で通流する増熱用燃料ガス供給系統11と、主燃料ガスG1に増熱用燃料ガスG2が混合された混合ガスG3が通流する混合ガス供給系統12とを備え、混合ガス供給系統12の下流側へ導かれる混合ガスG3を目標熱量TQ1に調整するように構成されている。この熱量調整装置は、増熱用燃料ガス供給系統11を通流する増熱用燃料ガスの流量を調整する流量調整弁13(流量調整手段の一例)を設け、増熱後の混合ガスG3に要求される目標熱量TQ1を有する混合ガスG3の質量流量である第1質量流量を計測する第1質量流量計14(第1質量流量計測手段の一例)を混合ガス供給系統12に備えるとともに、第1質量流量計14により計測される第1質量流量に基づいて、混合ガスG3の熱量を目標熱量TQ1に調整する第1制御指令を生成する制御装置15(第1制御手段の一例)を備えている。流量調整弁13は、制御装置15に生成される第1制御指令を受けて、増熱用燃料ガス供給系統11を通流する増熱用燃料ガスG2の流量を調整する。
[First Embodiment]
The calorific value adjusting device according to the first embodiment increases heat by mixing a low-calorie main fuel gas G1 (for example, city gas 13A) with a high-calorie heat increase fuel gas G2 (for example, LPG). In this embodiment, the mixed gas G3 obtained by mixing the main fuel gas G1 with the heat-increasing fuel gas G2 is adjusted to a desired target heat quantity TQ1.
Then, as shown in FIG. 1, the main fuel gas supply system 10 for flowing the main fuel gas G1 in a predetermined pressure state and the heat increasing fuel gas G2 mixed with the main fuel gas G1 in a predetermined pressure state. A heat-increasing fuel gas supply system 11 that flows through, and a gas mixture system 12 through which a mixed gas G3 in which the heat-increasing fuel gas G2 is mixed with the main fuel gas G1 flow. The mixed gas G3 guided to the downstream side is configured to be adjusted to the target heat amount TQ1. This calorific value adjusting device is provided with a flow rate adjusting valve 13 (an example of a flow rate adjusting means) for adjusting the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system 11, and the mixed gas G3 after the heat increase is provided. The mixed gas supply system 12 includes a first mass flow meter 14 (an example of a first mass flow measuring means) that measures a first mass flow rate that is a mass flow rate of the mixed gas G3 having the required target heat quantity TQ1. A control device 15 (an example of a first control unit) that generates a first control command for adjusting the amount of heat of the mixed gas G3 to the target heat amount TQ1 based on the first mass flow rate measured by the 1 mass flow meter 14 is provided. Yes. The flow rate adjusting valve 13 receives the first control command generated by the control device 15 and adjusts the flow rate of the heat increasing fuel gas G2 flowing through the heat increasing fuel gas supply system 11.

主燃料ガス供給系統10は、主燃料ガスG1を通流させる主燃料ガス流路16と、当該主燃料ガス流路16にて主燃料ガスG1の圧力を測定する圧力測定器17と、当該圧力測定器17の上流側で圧力測定器17の測定結果に基づいて主燃料ガスG1の圧力を一定の圧力に調整する圧力調整弁18と、当該圧力調整弁18の下流側にて主燃料ガスG1が上流側に逆流することを防止する逆止弁19とを備えている。
増熱用燃料ガス供給系統11についても、増熱用燃料ガスG2を通流させる増熱用燃料ガス流路20と、当該増熱用燃料ガス流路20にて増熱用燃料ガスG2の圧力を測定する圧力測定器21と、当該圧力測定器21の上流側で圧力測定器21の測定結果に基づいて増熱用燃料ガスG2の圧力を一定の圧力に調整する圧力調整弁22と、当該圧力調整弁22の下流側にて増熱用燃料ガスG2が上流側に逆流することを防止する逆止弁23とを備えている。
そして、混合ガス供給系統12は、第1質量流量計14の上流側にて主燃料ガスG1と増熱用燃料ガスG2とを適切に混合する混合装置24を備えるとともに、その下流側にて混合ガスG3の圧力を測定する圧力測定器25とを備えている。
The main fuel gas supply system 10 includes a main fuel gas channel 16 through which the main fuel gas G1 flows, a pressure measuring device 17 that measures the pressure of the main fuel gas G1 in the main fuel gas channel 16, and the pressure A pressure regulating valve 18 for adjusting the pressure of the main fuel gas G1 to a constant pressure based on the measurement result of the pressure measuring device 17 on the upstream side of the measuring device 17, and the main fuel gas G1 on the downstream side of the pressure regulating valve 18 Is provided with a check valve 19 for preventing the air from flowing back to the upstream side.
Also for the heat-increasing fuel gas supply system 11, the heat-increasing fuel gas channel 20 through which the heat-increasing fuel gas G2 flows, and the pressure of the heat-increasing fuel gas G2 in the heat-increasing fuel gas channel 20 A pressure measuring valve 21 that measures the pressure of the heat-increasing fuel gas G2 to a constant pressure based on the measurement result of the pressure measuring device 21 upstream of the pressure measuring device 21, A check valve 23 is provided on the downstream side of the pressure regulating valve 22 to prevent the heat-increasing fuel gas G2 from flowing back to the upstream side.
The mixed gas supply system 12 includes a mixing device 24 for appropriately mixing the main fuel gas G1 and the heat-increasing fuel gas G2 on the upstream side of the first mass flow meter 14, and mixing on the downstream side thereof. And a pressure measuring device 25 for measuring the pressure of the gas G3.

上記混合ガス供給系統12に設けられた第1質量流量計14は、要求される混合ガスG3の目標熱量TQ1の流量を計測する場合、第1質量流量として混合ガスG3の目標熱量TQ1に対応する目標質量流量TL1と等しい値を出力し、目標熱量TQ1より低い熱量LQを有する混合ガスG3の流量を計測する場合、第1質量流量として混合ガスG3の目標熱量TQ1に対応する目標質量流量TL1よりも低流量側の値L1を出力するように構成されている。   The first mass flow meter 14 provided in the mixed gas supply system 12 corresponds to the target heat amount TQ1 of the mixed gas G3 as the first mass flow rate when the required flow rate of the target heat amount TQ1 of the mixed gas G3 is measured. When measuring the flow rate of the mixed gas G3 that outputs a value equal to the target mass flow rate TL1 and has a heat quantity LQ lower than the target heat amount TQ1, the target mass flow rate TL1 corresponding to the target heat amount TQ1 of the mixed gas G3 is used as the first mass flow rate. Is also configured to output the value L1 on the low flow rate side.

当該第1質量流量計14により計測された第1質量流量に基づいて、制御装置15は、混合ガスG3の熱量を目標熱量TQ1に調整する第1制御指令を生成して、流量調整弁13に送るわけであるが、当該第1制御指令は、具体的には、増熱用燃料ガス供給系統11にて増熱用燃料ガスG2の流量を調整する流量調整弁13の弁開度に係る制御信号である。流量調整弁13は、当該第1制御指令に基づいて、第1質量流量が目標質量流量TL1よりも低流量側であるほど弁開度を大きくする形態で、その弁開度を調整する。
尚、制御装置15は、混合ガスG3の目標質量流量TL1毎に、第1質量流量と流量調整弁13の弁開度との関係を予め記憶した記憶部(図示せず)を有している。即ち、制御装置15は、第1質量流量計14の計測値に従って、流量調整弁13による増熱用燃料ガスG2の流量調整を行った場合の制御特性を予め記憶しておき、当該記憶した制御特性に基づいて、比例制御、一次遅れ制御、積分制御等を行う第1制御指令を出力するように構成されている。
Based on the first mass flow rate measured by the first mass flow meter 14, the control device 15 generates a first control command for adjusting the heat amount of the mixed gas G 3 to the target heat amount TQ 1, and sends it to the flow rate adjustment valve 13. Specifically, the first control command is a control related to the valve opening degree of the flow rate adjusting valve 13 that adjusts the flow rate of the heat increasing fuel gas G2 in the heat increasing fuel gas supply system 11. Signal. Based on the first control command, the flow rate adjustment valve 13 adjusts the valve opening degree in such a manner that the valve opening degree is increased as the first mass flow rate is lower than the target mass flow rate TL1.
The control device 15 has a storage unit (not shown) that stores in advance the relationship between the first mass flow rate and the valve opening degree of the flow rate adjustment valve 13 for each target mass flow rate TL1 of the mixed gas G3. . That is, the control device 15 stores in advance the control characteristics when the flow rate adjustment of the heat-increasing fuel gas G2 by the flow rate adjustment valve 13 is performed according to the measurement value of the first mass flow meter 14, and the stored control is performed. Based on the characteristics, a first control command for performing proportional control, first-order lag control, integral control, and the like is output.

以下に、当該制御装置15による第1質量流量に基づく流量調整弁13の具体的な制御の一例を示す。尚、以下では、主燃料ガスG1として低い熱量LQのものが供給されているものとし、下流側に供給される混合ガスG3の熱量は、目標熱量TQ1とする。
第1質量流量計14は、混合ガス供給系統12に低い熱量LQの混合ガスG3が通流すると、第1質量流量として低い熱量LQに対応した低流量側の値L1を出力する。制御装置15は、当該第1質量流量としての低流量側の値L1を、予め記憶している目標熱量TQ1に対応する混合ガスG3の目標質量流量TL1と比較する。第1質量流量としての低流量側の値L1が混合ガスG3の目標質量流量TL1よりも低い場合、流量調整弁13の開度を開弁側の所定の開度に調整する。これにより、下流側に供給される混合ガスG3の熱量は、目標熱量TQ1に増熱調整されることとなる。
即ち、このように、第1質量流量計14の出力としての第1質量流量を用いて熱量調整するように構成することで、一般的な質量流量計を混合ガス供給系統12に設置するだけで、混合ガスG3の増熱調整を実行できる。
Below, an example of the specific control of the flow control valve 13 based on the 1st mass flow by the said control apparatus 15 is shown. In the following, it is assumed that the main fuel gas G1 is supplied with a low heat quantity LQ, and the heat quantity of the mixed gas G3 supplied downstream is set as a target heat quantity TQ1.
When the mixed gas G3 having a low heat quantity LQ flows through the mixed gas supply system 12, the first mass flow meter 14 outputs a low flow rate value L1 corresponding to the low heat quantity LQ as the first mass flow rate. The control device 15 compares the value L1 on the low flow rate side as the first mass flow rate with the target mass flow rate TL1 of the mixed gas G3 corresponding to the target heat amount TQ1 stored in advance. When the value L1 on the low flow rate side as the first mass flow rate is lower than the target mass flow rate TL1 of the mixed gas G3, the opening degree of the flow rate adjustment valve 13 is adjusted to a predetermined opening degree on the valve opening side. Thereby, the heat quantity of the mixed gas G3 supplied downstream is adjusted to increase in heat to the target heat quantity TQ1.
That is, by configuring the mass flow meter to use the first mass flow rate as the output of the first mass flow meter 14 in this way, the general mass flow meter is simply installed in the mixed gas supply system 12. The heat increase adjustment of the mixed gas G3 can be executed.

〔第2実施形態〕
当該第2実施形態の熱量調整装置は、図2に示す様に、第1実施形態の第1質量流量計14に替えて、第2質量流量計26が主燃料ガス供給系統10に設けられている点、及び当該第2質量流量計26の計測結果に基づく制御装置15(第2制御手段の一例)の制御に特徴がある。そこで、以下では、上記第1実施形態と同一の構成については、同一の符号を付することとし、説明を割愛することがある。
[Second Embodiment]
As shown in FIG. 2, the heat quantity adjusting device of the second embodiment has a second mass flow meter 26 provided in the main fuel gas supply system 10 instead of the first mass flow meter 14 of the first embodiment. And the control of the control device 15 (an example of second control means) based on the measurement result of the second mass flow meter 26. Therefore, in the following, the same components as those in the first embodiment will be denoted by the same reference numerals, and description thereof may be omitted.

第2実施形態に係る熱量調整装置は、主燃料ガス供給系統10を通流する主燃料ガスG1に要求される主燃料ガス熱量TQ2を有する主燃料ガスG2の質量流量である第2質量流量を計測する第2質量流量計26を主燃料ガス供給系統10に備えるとともに、第2質量流量計26により計測される第2質量流量に基づいて、混合ガスG3の熱量を目標熱量TQ1に調整する第2制御指令を生成する制御装置15(第2制御手段の一例)を備え、増熱用燃料ガス供給系統11に設けられ増熱用燃料ガスG2の流量を調整する流量調整弁13が、制御装置15に生成される第2制御指令を受けて、増熱用燃料ガス供給系統11を通流する増熱用燃料ガスG2の流量を調整するように構成されている。   The calorie | heat amount adjustment apparatus which concerns on 2nd Embodiment adjusts the 2nd mass flow rate which is the mass flow rate of the main fuel gas G2 which has the main fuel gas calorie | heat amount TQ2 requested | required of the main fuel gas G1 which flows through the main fuel gas supply system 10. A second mass flow meter 26 to be measured is provided in the main fuel gas supply system 10, and the heat amount of the mixed gas G3 is adjusted to the target heat amount TQ1 based on the second mass flow rate measured by the second mass flow meter 26. 2 is provided with a control device 15 (an example of a second control means) that generates a control command, and a flow rate adjusting valve 13 that is provided in the heat increase fuel gas supply system 11 and adjusts the flow rate of the heat increase fuel gas G2 is provided in the control device. In response to the second control command generated at 15, the flow rate of the heat-increasing fuel gas G2 flowing through the heat-increasing fuel gas supply system 11 is adjusted.

上記主燃料ガス供給系統10に設けられた第2質量流量計26は、要求される主燃料ガスG1の目標熱量TQ2の流量を計測する場合、第2質量流量として主燃料ガスG1の目標熱量TQ2に対応する目標質量流量TL2と等しい値を出力し、目標熱量TQ2より低い熱量を有する主燃料ガスG1の流量を計測する場合、第2質量流量として主燃料ガスG1の目標熱量TQ2に対応する目標質量流量TL2よりも低流量側の値L1を出力するように構成されている。
制御装置15は、主燃料ガスG1の目標質量流量TL2毎に、第2質量流量と流量調整弁13の弁開度との関係を予め記憶した記憶部(図示せず)を有している。制御装置15は、記憶部に記憶された関係に基づき、第2制御指令を出力するように構成されている。
以下に、制御装置15による第2質量流量に基づく流量調整弁13の制御の一例を示す。
The second mass flow meter 26 provided in the main fuel gas supply system 10 measures the target heat quantity TQ2 of the main fuel gas G1 as the second mass flow rate when measuring the required flow quantity of the target heat quantity TQ2 of the main fuel gas G1. When the flow rate of the main fuel gas G1 having a heat quantity lower than the target heat quantity TQ2 is measured, a value corresponding to the target heat quantity TQ2 of the main fuel gas G1 is output as the second mass flow rate. A value L1 on the lower flow rate side than the mass flow rate TL2 is output.
The control device 15 has a storage unit (not shown) that stores in advance the relationship between the second mass flow rate and the valve opening degree of the flow rate adjustment valve 13 for each target mass flow rate TL2 of the main fuel gas G1. The control device 15 is configured to output a second control command based on the relationship stored in the storage unit.
Hereinafter, an example of the control of the flow rate adjustment valve 13 based on the second mass flow rate by the control device 15 will be shown.

主燃料ガス供給系統10に主燃料ガスG1が供給されると、第2質量流量計26は、主燃料ガスG1の有する所定の熱量に対応する第2質量流量を出力する。制御装置15は、当該第2質量流量と主燃料ガスG1の目標質量流量TL2とを比較し一致している場合、要求される主燃料ガス熱量TQ2の主燃料ガスG1が、問題なく供給されていると判断し、当該主燃料ガスG1の熱量(要求される主燃料ガス熱量TQ2)に対して、予め決められた一定の比率で所定の熱量の増熱用燃料ガスG2を供給する第2制御指令を生成する。流量調整弁13は、当該第2制御指令に基づいて、その開度を予め記憶された目標開度に設定する。これにより、要求される主燃料ガス熱量TQ2の主燃料ガスG1に一定比率で増熱用燃料ガスG2を混合して、混合ガスG3の熱量を、要求される目標熱量TQ1に増熱調整することができる。
一方、主燃料ガス供給系統10を通流する主燃料ガスG1の熱量が、要求される主燃料ガス熱量TQ2に対して不足している場合、第2質量流量計26は、第2質量流量として低流量側の値L3を出力する。この場合、制御装置15が、当該第2質量流量として低流量側の値L3と主燃料ガスG1の目標質量流量TL2とを比較すると、低流量側の値L3が目標質量流量TL2より小さくなるので、制御装置15は、主燃料ガスG1の熱量が、要求される主燃料ガス熱量TQ2より小さいと判断する。これにより、制御装置15は、増熱用燃料ガスG2の供給熱量を、要求される主燃料ガス熱量TQ2に対して予め決められた一定の比率の熱量よりも多い熱量を供給する第2制御指令を生成する。流量調整弁13は、当該第2制御指令に基づいて、その開度を大きめの開度に設定する。これにより、混合ガスG3の熱量を、目標熱量TQ1に近づけるように調整することができる。
When the main fuel gas G1 is supplied to the main fuel gas supply system 10, the second mass flow meter 26 outputs a second mass flow rate corresponding to a predetermined amount of heat of the main fuel gas G1. When the control unit 15 compares the second mass flow rate with the target mass flow rate TL2 of the main fuel gas G1, the control device 15 supplies the main fuel gas G1 having the required main fuel gas heat quantity TQ2 without any problem. A second control for supplying the fuel gas G2 for increasing heat with a predetermined amount of heat to the amount of heat of the main fuel gas G1 (required amount of heat of main fuel gas TQ2). Generate directives. Based on the second control command, the flow rate adjusting valve 13 sets the opening degree to a previously stored target opening degree. Thereby, the fuel gas G2 for increasing heat is mixed with the main fuel gas G1 having the required main fuel gas calorific value TQ2 at a constant ratio, and the calorific value of the mixed gas G3 is adjusted to increase to the required target calorie TQ1. Can do.
On the other hand, when the amount of heat of the main fuel gas G1 flowing through the main fuel gas supply system 10 is insufficient with respect to the required amount of main fuel gas heat TQ2, the second mass flow meter 26 sets the second mass flow rate as the second mass flow rate. The value L3 on the low flow rate side is output. In this case, when the control device 15 compares the low flow rate value L3 and the target mass flow rate TL2 of the main fuel gas G1 as the second mass flow rate, the low flow rate value L3 is smaller than the target mass flow rate TL2. The control device 15 determines that the heat quantity of the main fuel gas G1 is smaller than the required main fuel gas heat quantity TQ2. As a result, the control device 15 supplies the heat quantity of the heat increase fuel gas G2 to a quantity of heat that is greater than a predetermined ratio of quantity of heat with respect to the required main fuel gas quantity of heat TQ2. Is generated. The flow rate adjustment valve 13 sets the opening degree to a larger opening degree based on the second control command. Thereby, the calorie | heat amount of mixed gas G3 can be adjusted so that it may approach target calorie | heat amount TQ1.

〔第3実施形態〕
この発明も、質量流量計測手段(具体的には、計器に設定される所定の質量のガスの流量を計測する第1、第2質量流量計14、26)が測定する第1質量流量及び第2質量流量が、測定対象の燃料ガスの熱量に対応する点に着目し、第1、第2質量流量計14、26により計測される質量流量の増減に従って、主燃料ガスG1に混合する増熱用燃料ガスG2の流量を調整することができることを見出して完成した。
[Third Embodiment]
In the present invention, the first mass flow rate and the first mass flow rate measuring means (specifically, the first and second mass flow meters 14 and 26 for measuring the flow rate of the gas having a predetermined mass set in the meter) are also measured. Focusing on the point that the 2 mass flow rate corresponds to the heat quantity of the fuel gas to be measured, the heat increase mixed with the main fuel gas G1 according to the increase or decrease of the mass flow rate measured by the first and second mass flow meters 14 and 26 And found that the flow rate of the fuel gas G2 can be adjusted.

当該第3実施形態に係る熱量調整装置では、混合ガス供給系統12に第1質量流量計14を設けると共に、主燃料ガス供給系統10に第2質量流量計26を設けている点、及び第1質量流量計14及び第2質量流量計26の出力に基づく制御装置15(第3制御手段の一例)による制御を特徴とする。これ以外の点については、上記第1、第2実施形態と変るところがないため、上記第1、第2実施形態と同一の構成については、同一の符号を付すこととし、説明を割愛することがある。   In the calorific value adjustment device according to the third embodiment, the first mass flow meter 14 is provided in the mixed gas supply system 12, and the second mass flow meter 26 is provided in the main fuel gas supply system 10. It is characterized by control by the control device 15 (an example of third control means) based on the outputs of the mass flow meter 14 and the second mass flow meter 26. Since there is no difference from the first and second embodiments with respect to other points, the same components as those in the first and second embodiments are denoted by the same reference numerals, and description thereof may be omitted. is there.

当該第3実施形態の熱量調整装置は、図3に示す様に、増熱後の混合ガスG3に要求される目標熱量TQ1を有する混合ガスG3の質量流量である第1質量流量を計測する第1質量流量計14を混合ガス供給系統12に備えるとともに、主燃料ガス供給系統10を通流する主燃料ガスG1に要求される主燃料ガス熱量TQ2を有する主燃料ガスG1の質量流量である第2質量流量を計測する第2質量流量計26を主燃料ガス供給系統10に備え、第1質量流量計14及び第2質量流量計26により計測される第1質量流量としての値L1、及び第2質量流量としての値L3に基づいて、混合ガスG3の熱量を目標熱量TQ1に調整する第3制御指令を生成する制御装置15(第3制御手段の一例)を備え、増熱用燃料ガス供給系統11に設けられている流量調整弁13が、制御装置15に生成される第3制御指令を受けて、増熱用燃料ガス供給系統11を通流する増熱用燃料ガスG2の流量を調整するように構成されている。   As shown in FIG. 3, the heat quantity adjusting device of the third embodiment measures the first mass flow rate that is the mass flow rate of the mixed gas G3 having the target heat amount TQ1 required for the mixed gas G3 after the heat increase. The mass flow rate of the main fuel gas G1 having the main fuel gas heat quantity TQ2 required for the main fuel gas G1 flowing through the main fuel gas supply system 10 is provided in the mixed gas supply system 12 with the 1 mass flow meter 14 A second mass flow meter 26 for measuring two mass flow rates is provided in the main fuel gas supply system 10, and a value L1 as the first mass flow rate measured by the first mass flow meter 14 and the second mass flow meter 26, and the first A control device 15 (an example of third control means) that generates a third control command for adjusting the amount of heat of the mixed gas G3 to the target amount of heat TQ1 based on the value L3 as the two mass flow rates, and supplying the fuel gas for increasing heat Provided in system 11 The flow rate adjusting valve 13 is configured to adjust the flow rate of the heat-increasing fuel gas G2 flowing through the heat-increasing fuel gas supply system 11 in response to the third control command generated by the control device 15. Has been.

尚、当該第3〜第5実施形態において、第1質量流量としての値L1及び第2質量流量としての値L3は、第1質量流量計14及び第2質量流量計26の指示値を示すものであり、具体的には、例えば(リトッル/min)の物理量である。
そして、当該第1質量流量計14及び第2質量流量計26は、測定対象のガスの目標の質量を設定可能に構成されており、第1質量流量計14には、混合ガスG3の目標の質量(熱量)が設定されると共に、第2質量流量計26には、主燃料ガスG1の目標の質量(熱量)が設定される。上記第1質量流量としての値L1や上記第2質量流量としての値L3は、当該設定される目標の質量(熱量)に基づいて、計測されるものである。
例えば、熱量調整がされる前の状態の主燃料ガスG1を、そのまま、第1質量流量計14で測定した場合と、第2質量流量計26で測定した場合とでは、第1質量流量計14の方が第2質量流量計26より設定される目標の質量(熱量)が大きいので、第1質量流量としての値L1は、第2質量流量としての値L3より小さくなる。そこで、当該第3実施形態では、第1質量流量としての値L1が、第2質量流量としての値L3に一致するように、増熱用燃料ガスG2の供給量を制御する。これにより、混合ガスG3は、その質量(熱量)が目標の質量(熱量)に調整された状態で、下流側に導かれることとなる。以下、増熱用燃料ガスG2の供給量の制御について、具体的に説明する。
In the third to fifth embodiments, the value L1 as the first mass flow rate and the value L3 as the second mass flow rate indicate the indicated values of the first mass flow meter 14 and the second mass flow meter 26. Specifically, for example, the physical quantity is (liter / min).
The first mass flow meter 14 and the second mass flow meter 26 are configured to be able to set the target mass of the gas to be measured, and the first mass flow meter 14 includes the target mass of the mixed gas G3. A mass (amount of heat) is set, and a target mass (amount of heat) of the main fuel gas G1 is set in the second mass flow meter 26. The value L1 as the first mass flow rate and the value L3 as the second mass flow rate are measured based on the set target mass (heat amount).
For example, the first mass flow meter 14 is measured when the main fuel gas G1 in a state before the calorific value is adjusted as it is with the first mass flow meter 14 and when measured with the second mass flow meter 26. Since the target mass (heat amount) set by the second mass flow meter 26 is larger, the value L1 as the first mass flow rate is smaller than the value L3 as the second mass flow rate. Therefore, in the third embodiment, the supply amount of the heat increasing fuel gas G2 is controlled so that the value L1 as the first mass flow rate matches the value L3 as the second mass flow rate. As a result, the mixed gas G3 is guided downstream in a state in which the mass (heat amount) is adjusted to the target mass (heat amount). Hereinafter, the control of the supply amount of the heat increasing fuel gas G2 will be specifically described.

制御装置15は、混合ガスG3の目標質量流量TL1毎に、第1質量流量と第2質量流量と流量調整弁13の弁開度との関係を予め記憶した記憶部(図示せず)を有している。即ち、制御装置15は、第1質量流量計14、第2質量流量計26の計測値(指示値)に従って、流量調整弁13による増熱用燃料ガスG2の流量調整を行った場合の制御特性を予め記憶しておき、当該記憶した制御特性に基づいて、比例制御、一次遅れ制御、積分制御等を行う第3制御指令を出力するように構成されている。
以下、本発明の熱量調整装置にて、混合ガスG3の増熱を行う場合において、制御装置15による流量調整弁13の弁開度の調整について説明する。
The control device 15 has a storage unit (not shown) that stores in advance the relationship between the first mass flow rate, the second mass flow rate, and the valve opening degree of the flow rate adjustment valve 13 for each target mass flow rate TL1 of the mixed gas G3. is doing. That is, the control device 15 performs control characteristics when the flow rate adjustment valve 13 adjusts the flow rate of the fuel gas G2 for heat increase according to the measurement values (instruction values) of the first mass flow meter 14 and the second mass flow meter 26. Are stored in advance, and based on the stored control characteristics, a third control command for performing proportional control, first-order lag control, integral control, and the like is output.
Hereinafter, adjustment of the valve opening degree of the flow rate adjusting valve 13 by the control device 15 when the heat of the mixed gas G3 is increased in the heat quantity adjusting device of the present invention will be described.

第1質量流量計14は、混合ガス供給系統12において、要求される混合ガスG3の目標熱量TQ1の所定質量のガスの流量を測定する。一方、第2質量流量計26は、主燃料ガス供給系統10にて、要求される主燃料ガス熱量TQ2の所定質量のガスの流量を測定する。ここで、増熱用燃料ガスG2が、主燃料ガスG1に対して適切な比で混合された場合、第1質量流量計14で計測される流量は、混合に伴うガス質量の増加(増熱)に寄与するだけであるため、結果的に、第1質量流量計14により計測される第1質量流量としての値L1と、第2質量流量計26により計測される第2質量流量としての値L3とは一致する。
従って、制御装置15は、第1質量流量計14により計測される第1質量流量としての値L1と第2質量流量計26により計測される第2質量流量としての値L3とが一致するように、第3制御指令を生成する。流量調整弁13は、当該第3制御指令に従って、その開度を調整する。これにより、一般的な質量流量計を主燃料ガス供給系統10に設置するだけで、混合ガスG3の熱量の増熱調整を、簡易且つ低コストに実現できることとなる。
In the mixed gas supply system 12, the first mass flow meter 14 measures the flow rate of a gas having a predetermined mass corresponding to the required target heat quantity TQ1 of the mixed gas G3. On the other hand, the second mass flow meter 26 measures the flow rate of the gas having a predetermined mass of the required main fuel gas calorific value TQ2 in the main fuel gas supply system 10. Here, when the fuel gas G2 for heat increase is mixed at an appropriate ratio with respect to the main fuel gas G1, the flow rate measured by the first mass flow meter 14 is an increase in gas mass due to mixing (heat increase). As a result, the value L1 as the first mass flow rate measured by the first mass flow meter 14 and the value as the second mass flow rate measured by the second mass flow meter 26 are obtained. It matches L3.
Therefore, the control device 15 causes the value L1 as the first mass flow rate measured by the first mass flow meter 14 and the value L3 as the second mass flow rate measured by the second mass flow meter 26 to coincide with each other. The third control command is generated. The flow rate adjusting valve 13 adjusts the opening degree according to the third control command. Thereby, only by installing a general mass flow meter in the main fuel gas supply system 10, the heat increase adjustment of the heat quantity of the mixed gas G3 can be realized simply and at low cost.

〔第4実施形態〕
第4実施形態に係る熱量調整装置は、上記第1実施形態に係る熱量調整装置を、さらに発展させたものである。当該第4実施形態に係る熱量調整装置は、これまで説明した第1〜第3実施形態と同様に混合ガスG3の増熱調整できるように構成されていると共に、下流側に供給する混合ガスG3の総熱量の制御(増熱されて所定の目標熱量TQ1の混合ガスG3を所定の流量供給する制御)ができるように構成されているものである。そして、混合ガス供給系統12を通流する混合ガスG3の容積流量VLを測定する流量計27(容積流量測定手段の一例)を備える点、及び当該流量計27の計測結果をも加味した制御装置15(第4制御手段の一例)による制御に特徴がある。尚、これら以外の構成については、上記第1実施形態に示した構成と同一であるため、同一の符号を付することとし、その説明を割愛することがある。
[Fourth Embodiment]
The heat quantity adjusting device according to the fourth embodiment is a further development of the heat quantity adjusting device according to the first embodiment. The calorific value adjusting device according to the fourth embodiment is configured so that the heat increase of the mixed gas G3 can be adjusted similarly to the first to third embodiments described so far, and the mixed gas G3 supplied to the downstream side. The total heat quantity can be controlled (control for supplying a predetermined flow rate of the mixed gas G3 having a predetermined target heat quantity TQ1 increased in temperature). And the control apparatus which also considered the point provided with the flowmeter 27 (an example of a volumetric flow measurement means) which measures the volumetric flow VL of the mixed gas G3 which flows through the mixed gas supply system 12, and the measurement result of the said flowmeter 27 15 (an example of fourth control means) is characterized by control. In addition, since it is the same as that of the structure shown in the said 1st Embodiment about the structure other than these, it shall attach | subject the same code | symbol and may omit the description.

第4実施形態に係る熱量調整装置は、第1実施形態に係る熱量調整装置の構成に加えて、混合ガス供給系統12を通流する混合ガスG3の容積流量VLを測定する流量計27(容積流量測定手段の一例)を備え、第1質量流量計14により計測される第1質量流量としての値L1及び流量計27により測定される容積流量VLに基づいて、混合ガスG3の熱量を目標熱量TQ1に、混合ガスG3の容積流量VLを目標流量TVに調整する第4制御指令を生成する制御装置15(第4制御手段の一例)を備え、増熱用燃料ガス供給系統11に設けられ増熱用燃料ガスG2の流量を調整する流量調整弁13が、制御装置15の第4制御指令を受けて、増熱用燃料ガスG2の流量を調整するものである。
制御装置15は、混合ガスG3の目標質量流量TL1毎に、第1質量流量と流量調整弁13の弁開度との関係、及び容積流量VLと流量調整弁13の弁開度との関係を記憶した記憶部(図示せず)を有している。即ち、制御装置15は、第1質量流量計14、流量計27の計測値に従って、流量調整弁13による増熱用燃料ガスG2の流量調整を行った場合の制御特性を予め記憶しておき、当該記憶した制御特性に基づいて、比例制御、一次遅れ制御、積分制御等を行うように構成されている。
このように、当該第4実施形態の熱量調整装置では、混合ガスG3の増熱に関しては、第1質量流量計14の計測値(指示値)を、上記第1実施形態にて説明した制御構成と同様のものを使用する。即ち、制御装置15(第4制御手段の一例)は、上記第1実施形態にて説明した第1制御手段としての機能部位を備え、第1制御手段の第1制御指令を含む第4制御指令を出力して、当該第4制御指令に基づいて流量調整弁13が弁開度を調整することで、混合ガスG3の熱量を目標熱量TQ1に調整(増熱調整)する。
また、制御装置15が第4制御手段として機能する場合、制御装置15は、流量計27により測定される容積流量VLに基づいて、混合ガスG3の容積流量VLを目標流量TVとする第4制御指令を生成し、流量調整弁13が当該第4制御指令に従って、その弁開度を調整する形態で、混合ガスG3の流量を目標流量TVに調整することができる。
即ち、第4制御手段として機能する制御装置15は、第1質量流量計14の計測値(指示値)と、流量計27の計測値とに基づいて、上記第4制御指令を生成するように構成されている。
ここで、混合ガスG3の熱量を目標熱量TQ1の調整(増熱調整)と、混合ガスG3の流量を目標流量TVに調整(流量調整)とのどちらを優先するかの優劣は、混合ガスG3の熱量が所定の目標の熱量範囲(例えば、目標熱量TQ1を中心とした所定の範囲)内に収まっていることを条件として、混合ガスG3の容積流量VLを所定の目標の流量範囲(例えば、目標流量TVを中心とした所定の範囲)に収まるように制御するものとできる。
結果、第4実施形態における流量調整装置では、一般的な質量流量計に流量計を備えるといった比較的簡易な構成を採用することで、混合ガスG3を適切に増熱するとともに、適切な流量に調整することができ、所謂、混合ガスG3の総熱量の調整を実現できる。
In addition to the configuration of the heat quantity adjusting device according to the first embodiment, the heat quantity adjusting device according to the fourth embodiment includes a flow meter 27 (volume) that measures the volume flow rate VL of the mixed gas G3 flowing through the mixed gas supply system 12. An example of a flow rate measuring means), and based on the value L1 as the first mass flow rate measured by the first mass flow meter 14 and the volume flow rate VL measured by the flow meter 27, the heat amount of the mixed gas G3 is determined as the target heat amount. TQ1 includes a control device 15 (an example of fourth control means) that generates a fourth control command for adjusting the volumetric flow rate VL of the mixed gas G3 to the target flow rate TV, and is provided in the heat-increasing fuel gas supply system 11. A flow rate adjustment valve 13 that adjusts the flow rate of the thermal fuel gas G2 receives the fourth control command from the control device 15 and adjusts the flow rate of the thermal increase fuel gas G2.
For each target mass flow rate TL1 of the mixed gas G3, the control device 15 determines the relationship between the first mass flow rate and the valve opening degree of the flow rate adjustment valve 13, and the relationship between the volume flow rate VL and the valve opening degree of the flow rate adjustment valve 13. A storage unit (not shown) is stored. That is, the control device 15 stores in advance control characteristics when the flow rate adjustment of the fuel gas G2 for heat increase by the flow rate adjustment valve 13 is performed according to the measurement values of the first mass flow meter 14 and the flow meter 27, Based on the stored control characteristics, proportional control, first-order lag control, integral control, and the like are performed.
Thus, in the calorie | heat amount adjustment apparatus of the said 4th Embodiment, regarding the heat increase of the mixed gas G3, the measured value (indication value) of the 1st mass flow meter 14 is the control structure demonstrated in the said 1st Embodiment. Use the same as above. That is, the control device 15 (an example of the fourth control unit) includes the functional part as the first control unit described in the first embodiment, and includes the fourth control command including the first control command of the first control unit. And the flow rate adjustment valve 13 adjusts the valve opening based on the fourth control command, thereby adjusting the heat amount of the mixed gas G3 to the target heat amount TQ1 (heat increase adjustment).
When the control device 15 functions as the fourth control means, the control device 15 uses the volume flow VL of the mixed gas G3 as the target flow TV based on the volume flow VL measured by the flow meter 27. The flow rate of the mixed gas G3 can be adjusted to the target flow rate TV in such a manner that the flow rate adjustment valve 13 adjusts the valve opening according to the fourth control command.
That is, the control device 15 functioning as the fourth control means generates the fourth control command based on the measured value (indicated value) of the first mass flow meter 14 and the measured value of the flow meter 27. It is configured.
Here, the superiority or inferiority of adjusting the heat amount of the mixed gas G3 to the target heat amount TQ1 (heat increase adjustment) or adjusting the flow rate of the mixed gas G3 to the target flow rate TV (flow rate adjustment) is the mixed gas G3. Is within a predetermined target heat amount range (for example, a predetermined range centered on the target heat amount TQ1), the volumetric flow rate VL of the mixed gas G3 is set to a predetermined target flow range (for example, It can be controlled to fall within a predetermined range centered on the target flow rate TV.
As a result, in the flow rate adjusting device in the fourth embodiment, by adopting a relatively simple configuration in which a general mass flow meter is equipped with a flow meter, the mixed gas G3 is appropriately heated, and the flow rate is adjusted appropriately. It is possible to adjust so-called adjustment of the total heat quantity of the mixed gas G3.

〔第5実施形態〕
第5実施形態に係る熱量調整装置は、第3実施形態に係る熱量調整装置をさらに発展させた技術であり、混合ガスG3の熱量を増熱調整するとともに、その総熱量の調整をも可能とするものである。具体的には、主燃料ガス供給系統10を通流する主燃料ガスG1の比重を測定する比重計28(比重計測手段の一例)を備える点、及び当該比重計28の計測結果をも加味した制御装置15(第5制御手段の一例)の制御に、特徴がある。これ以外の構成については、上記第3実施形態に係る構成と同一であるため、同一の符号を付すこととし、その説明を割愛することがある。
[Fifth Embodiment]
The calorific value adjustment device according to the fifth embodiment is a technology that is a further development of the calorific value adjustment device according to the third embodiment, and can adjust the total calorific value of the mixed gas G3 while increasing the calorific value thereof. To do. Specifically, a point including a hydrometer 28 (an example of a specific gravity measuring unit) that measures the specific gravity of the main fuel gas G1 flowing through the main fuel gas supply system 10 and the measurement result of the hydrometer 28 are also taken into account. There is a feature in the control of the control device 15 (an example of fifth control means). Since the configuration other than this is the same as the configuration according to the third embodiment, the same reference numerals are used, and the description thereof may be omitted.

第5実施形態に係る熱量調整装置は、主燃料ガス供給系統10を流れる主燃料ガスG1の比重SGを測定する比重計28(比重測定手段の一例)を備え、第1質量流量計14及び第2質量流量計26により計測される第1質量流量としての値L1、及び第2質量流量としての値L3及び比重計28により測定される比重SGに基づいて、混合ガスG3の熱量を目標熱量TQ1に、流量を目標流量TVに調整する第5制御指令を生成する制御装置15(第5制御手段の一例)を備え、増熱用燃料ガス供給系統11にて増熱用燃料ガスG2の流量を調整する流量調整弁13が、制御装置15に生成される第5制御指令を受けて、増熱用燃料ガス供給系統11を通流する増熱用燃料ガスG2の流量を調整するように構成されている。   The calorific value adjustment device according to the fifth embodiment includes a hydrometer 28 (an example of specific gravity measuring means) that measures the specific gravity SG of the main fuel gas G1 flowing through the main fuel gas supply system 10, and includes the first mass flow meter 14 and the first mass flow meter 14. Based on the value L1 as the first mass flow rate measured by the two mass flow meter 26, the value L3 as the second mass flow rate, and the specific gravity SG measured by the hydrometer 28, the heat amount of the mixed gas G3 is set to the target heat amount TQ1. Are provided with a control device 15 (an example of fifth control means) for generating a fifth control command for adjusting the flow rate to the target flow rate TV, and the flow rate of the heat-increasing fuel gas G2 in the heat-increasing fuel gas supply system 11 is adjusted. The flow rate adjusting valve 13 to be adjusted is configured to adjust the flow rate of the heat-increasing fuel gas G2 flowing through the heat-increasing fuel gas supply system 11 in response to the fifth control command generated by the control device 15. ing.

先に説明した第3実施形態に係る熱量調整装置では、制御装置15は、第1質量流量計14により計測される第1質量流量としての値L1と第2質量流量計26により計測される第2質量流量としての値L3とが一致するように第3制御指令を生成する。そして、流量調整弁13が、当該第3制御指令に従って、その弁開度を調整できる。
即ち、第5実施形態に係る熱量調整装置において、制御装置15が上記第3制御手段に相当する機能部位を備えておくことで、混合ガスG3の熱量は目標熱量TQ1に調整される。しかしながら、当該第3制御手段に係る機能部位のみでは、混合ガスG3の総熱量までは制御することはできない。
In the calorific value adjusting device according to the third embodiment described above, the control device 15 has a value L1 as the first mass flow rate measured by the first mass flow meter 14 and a second mass flow meter 26 measured by the second mass flow meter 26. The third control command is generated so that the value L3 as the 2 mass flow rate matches. And the flow volume adjustment valve 13 can adjust the valve opening degree according to the said 3rd control command.
That is, in the heat quantity adjusting device according to the fifth embodiment, the heat amount of the mixed gas G3 is adjusted to the target heat amount TQ1 when the control device 15 includes a functional portion corresponding to the third control means. However, it is impossible to control the total amount of heat of the mixed gas G3 only by the functional part related to the third control means.

そこで、第5実施形態に係る流量調整装置では、上述の如く、主燃料ガス供給系統10に比重計28を備えて、主燃料ガスG1の真の比重SG(主燃料ガスG1の真の熱量)を計測するように構成している。
ここで、第2質量流量計26は、主燃料ガスG1に求められる熱量のガス(発熱量のガス)の質量流量を計測する手段であるため、主燃料ガスG1の真の比重SGが判明すると、第2質量流量計26において計測される質量流量から、現在流れている主燃料ガスG1の真の流量(容積流量)が判明する。
ここで、先の第3実施形態に係る熱量調整装置に示した制御に従い、制御装置15が、増熱用燃料ガスG2の流量を調整すると、結果的に、現在流れている主燃料ガスG1の真の流量だけ目標熱量TQ1の混合ガスG3を得ることとなり、熱量と流量の双方の制御が可能となる。
Therefore, in the flow control device according to the fifth embodiment, as described above, the main fuel gas supply system 10 includes the hydrometer 28, and the true specific gravity SG of the main fuel gas G1 (the true amount of heat of the main fuel gas G1). Is configured to measure.
Here, since the second mass flow meter 26 is a means for measuring the mass flow rate of the calorie gas (calorific value gas) required for the main fuel gas G1, the true specific gravity SG of the main fuel gas G1 is found. From the mass flow rate measured by the second mass flow meter 26, the true flow rate (volumetric flow rate) of the currently flowing main fuel gas G1 is determined.
Here, when the control device 15 adjusts the flow rate of the fuel gas G2 for heat increase in accordance with the control shown in the heat quantity adjusting device according to the third embodiment, as a result, the main fuel gas G1 that is currently flowing is changed. The mixed gas G3 having the target heat quantity TQ1 is obtained by the true flow rate, and both the heat quantity and the flow rate can be controlled.

ここで、第5制御手段として機能する制御装置15が、比重計28により計測された比重SGにより、第2質量流量計26により計測される流量を補正する第5制御指令を出力する場合、制御装置15は、予め測定した比重計28の出力と、主燃料ガスG1に供給される熱量のガスの質量流量を計測するときの第2質量流量計26の出力との関係に基づいて第5制御指令を出力するように構成されている。
結果、質量流量計と比重計とを備えた比較的簡易な構成であっても、製造コストを抑制できながらも、適切に熱量調整が可能な熱量調整装置を実現できる。
Here, when the control device 15 functioning as the fifth control unit outputs a fifth control command for correcting the flow rate measured by the second mass flow meter 26 based on the specific gravity SG measured by the hydrometer 28, the control is performed. The device 15 performs the fifth control based on the relationship between the output of the hydrometer 28 measured in advance and the output of the second mass flow meter 26 when measuring the mass flow rate of the heat gas supplied to the main fuel gas G1. It is configured to output a command.
As a result, even with a relatively simple configuration including a mass flow meter and a specific gravity meter, it is possible to realize a heat quantity adjusting device capable of appropriately adjusting the heat quantity while suppressing the manufacturing cost.

〔別実施形態〕
(1)上記実施形態では、流量調整手段として流量調整弁13を備えた構成としたが、例えば、増熱用燃料ガスG2の熱量と直接的に対応する質量流量を調整可能な質量流量調整装置(マスフローコントローラ)を備えても良い。
[Another embodiment]
(1) In the above embodiment, the flow rate adjusting valve 13 is provided as the flow rate adjusting means. However, for example, a mass flow rate adjusting device capable of adjusting the mass flow rate directly corresponding to the heat amount of the fuel gas G2 for heat increase. (Mass flow controller) may be provided.

本発明の熱量調整装置は、構造が簡単で、設備コストを抑えながらも、適切に混合ガスの熱量を調整可能な熱量調整装置として、有効に利用可能である。   The heat quantity adjusting device of the present invention has a simple structure and can be effectively used as a heat quantity adjusting device capable of appropriately adjusting the heat quantity of the mixed gas while suppressing the equipment cost.

G1 :主燃料ガス
G2 :増熱用燃料ガス
G3 :混合ガス
TQ1 :混合ガスの目標熱量
TQ2 :主燃料ガスの目標熱量
L1 :低流量側の値(第1質量流量)
L3 :低流量側の値(第2質量流量)
VL :容積流量
SG :比重
10 :主燃料ガス供給系統
11 :増熱用燃料ガス供給系統
12 :混合ガス供給系統
13 :流量調整弁(流量調整手段の一例)
14 :第1質量流量計(第1質量流量計測手段の一例)
15 :制御装置(第1〜第5制御手段の一例)
26 :第2質量流量計(第2質量流量計測手段の一例)
27 :流量計(容積流量測定手段の一例)
28 :比重計(比重計測手段の一例)
G1: Main fuel gas G2: Fuel gas G3 for increasing heat: Mixed gas TQ1: Target heat amount TQ2 of mixed gas: Target heat amount L1 of main fuel gas: Value on the low flow rate side (first mass flow rate)
L3: Value on the low flow rate side (second mass flow rate)
VL: Volumetric flow rate SG: Specific gravity 10: Main fuel gas supply system 11: Fuel gas supply system for heat increase 12: Mixed gas supply system 13: Flow rate adjustment valve (an example of flow rate adjustment means)
14: 1st mass flow meter (an example of 1st mass flow measurement means)
15: Control device (an example of first to fifth control means)
26: second mass flow meter (an example of second mass flow measurement means)
27: Flow meter (an example of volumetric flow rate measuring means)
28: Specific gravity meter (an example of specific gravity measurement means)

Claims (5)

主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記第1質量流量計測手段により計測される前記第1質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第1制御指令を生成する第1制御手段を備え、
前記流量調整手段が、前記第1制御手段に生成される前記第1制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する熱量調整装置。
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
Based on the first mass flow rate measured by the first mass flow rate measurement means, comprising first control means for generating a first control command for adjusting the heat quantity of the mixed gas to the target heat quantity,
A calorific value adjusting device for adjusting the flow rate of the heat-increasing fuel gas flowing through the heat-increasing fuel gas supply system in response to the first control command generated by the first control unit. .
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
主燃料ガス供給系統を通流する主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備えるとともに、
前記第2質量流量計測手段により計測される前記第2質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第2制御指令を生成する第2制御手段を備え、
前記流量調整手段が、前記第2制御手段に生成される前記第2制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する熱量調整装置。
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having a main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system is provided in the main fuel gas supply system. And prepare for
Based on the second mass flow rate measured by the second mass flow rate measurement means, comprising second control means for generating a second control command for adjusting the heat quantity of the mixed gas to the target heat quantity,
A calorific value adjusting device for adjusting the flow rate of the heat-increasing fuel gas flowing through the heat-increasing fuel gas supply system in response to the second control command generated by the second control unit. .
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
主燃料ガス供給系統を通流する主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備え、
前記第1質量流量計測手段及び前記第2質量流量計測手段により計測される前記第1質量流量、及び前記第2質量流量に基づいて、前記混合ガスの熱量を前記目標熱量に調整する第3制御指令を生成する第3制御手段を備え、
前記流量調整手段が、前記第3制御手段に生成される前記第3制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する熱量調整装置。
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
A second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having a main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system is provided in the main fuel gas supply system. In preparation for
Third control for adjusting the heat amount of the mixed gas to the target heat amount based on the first mass flow rate and the second mass flow rate measured by the first mass flow rate measuring unit and the second mass flow rate measuring unit. A third control means for generating a command;
A calorific value adjusting device for adjusting the flow rate of the heat-increasing fuel gas flowing through the heat-increasing fuel gas supply system in response to the third control command generated by the third control unit. .
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記混合ガス供給系統を通流する前記混合ガスの容積流量を測定する容積流量測定手段を備え、
前記第1質量流量計測手段により計測される前記第1質量流量及び前記容積流量測定手段により測定される容積流量に基づいて、前記混合ガスの熱量を前記目標熱量に、前記混合ガスの容積流量を目標流量に調整する第4制御指令を生成する第4制御手段を備え、
前記流量調整手段が、前記第4制御手段に生成される前記第4制御指令を受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する熱量調整装置。
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
A volumetric flow rate measuring means for measuring a volumetric flow rate of the mixed gas flowing through the mixed gas supply system;
Based on the first mass flow rate measured by the first mass flow rate measuring means and the volumetric flow rate measured by the volumetric flow rate measuring means, the heat amount of the mixed gas is set as the target heat amount, and the volume flow rate of the mixed gas is set as the target heat amount. A fourth control means for generating a fourth control command for adjusting to the target flow rate;
A calorific value adjusting device for adjusting the flow rate of the heat-increasing fuel gas flowing through the heat-increasing fuel gas supply system in response to the fourth control command generated by the fourth control unit. .
主燃料ガスを所定の圧力状態で通流する主燃料ガス供給系統と、前記主燃料ガスに混合される増熱用燃料ガスを所定の圧力状態で通流する増熱用燃料ガス供給系統と、前記主燃料ガスに前記増熱用燃料ガスが混合された混合ガスが通流する混合ガス供給系統とを備え、前記混合ガス供給系統の下流側へ導かれる前記混合ガスを目標熱量に調整する熱量調整装置であって、
前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する流量調整手段を設け、
増熱後の混合ガスに要求される目標熱量を有する混合ガスの質量流量である第1質量流量を計測する第1質量流量計測手段を前記混合ガス供給系統に備えるとともに、
前記主燃料ガス供給系統を流れる主燃料ガスに要求される主燃料ガス熱量を有する主燃料ガスの質量流量である第2質量流量を計測する第2質量流量計測手段を前記主燃料ガス供給系統に備え、
さらに、前記主燃料ガス供給系統を流れる主燃料ガスの比重を測定する比重測定手段を備え、
前記第1質量流量計測手段及び第2質量流量計測手段により計測される前記第1質量流量、及び第2質量流量及び比重測定手段により測定される比重に基づいて、前記混合ガスの熱量を前記目標熱量に、流量を目標流量に調整する第5制御指令を生成する第5制御手段を備え、
前記流量調整手段が、前記第5制御手段に生成される前記第5制御指令受けて、前記増熱用燃料ガス供給系統を通流する前記増熱用燃料ガスの流量を調整する熱量調整装置。
A main fuel gas supply system for flowing main fuel gas in a predetermined pressure state; and a heat increase fuel gas supply system for flowing heat increase fuel gas mixed in the main fuel gas in a predetermined pressure state; A mixed gas supply system through which a mixed gas in which the main fuel gas is mixed with the fuel gas for increasing heat flows, and a heat quantity for adjusting the mixed gas led to the downstream side of the mixed gas supply system to a target heat quantity An adjustment device,
A flow rate adjusting means for adjusting a flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system;
A first mass flow rate measuring means for measuring a first mass flow rate that is a mass flow rate of the mixed gas having a target heat amount required for the mixed gas after the heat increase is provided in the mixed gas supply system,
The main fuel gas supply system is provided with a second mass flow rate measuring means for measuring a second mass flow rate which is a mass flow rate of the main fuel gas having the main fuel gas calorific value required for the main fuel gas flowing through the main fuel gas supply system. Prepared,
Furthermore, it comprises specific gravity measuring means for measuring the specific gravity of the main fuel gas flowing through the main fuel gas supply system,
Based on the first mass flow rate measured by the first mass flow rate measurement unit and the second mass flow rate measurement unit and the specific gravity measured by the second mass flow rate and specific gravity measurement unit, the heat quantity of the mixed gas is determined as the target. A fifth control means for generating a fifth control command for adjusting the flow rate to the target flow rate in the amount of heat;
A calorific value adjusting device, wherein the flow rate adjusting means receives the fifth control command generated by the fifth control means and adjusts the flow rate of the heat increasing fuel gas flowing through the heat increasing fuel gas supply system.
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Citations (6)

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JPH08105338A (en) * 1994-10-05 1996-04-23 Yanmar Diesel Engine Co Ltd Control mechanism of auxiliary chamber type gas engine
JP2002364396A (en) * 2001-06-05 2002-12-18 Tokico Ltd Fuel mixing and filling system
JP2004316529A (en) * 2003-04-15 2004-11-11 Tokyo Gas Co Ltd Gas fuel feeding mechanism
JP2005171975A (en) * 2003-12-15 2005-06-30 Mitsubishi Heavy Ind Ltd Combustion control method and combustion control device in gas engine
JP2005256674A (en) * 2004-03-10 2005-09-22 Tokyo Gas Co Ltd Gas engine and method for controlling the same
JP2010059900A (en) * 2008-09-05 2010-03-18 Toho Gas Co Ltd Gas mixing device used in electric power generation system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08105338A (en) * 1994-10-05 1996-04-23 Yanmar Diesel Engine Co Ltd Control mechanism of auxiliary chamber type gas engine
JP2002364396A (en) * 2001-06-05 2002-12-18 Tokico Ltd Fuel mixing and filling system
JP2004316529A (en) * 2003-04-15 2004-11-11 Tokyo Gas Co Ltd Gas fuel feeding mechanism
JP2005171975A (en) * 2003-12-15 2005-06-30 Mitsubishi Heavy Ind Ltd Combustion control method and combustion control device in gas engine
JP2005256674A (en) * 2004-03-10 2005-09-22 Tokyo Gas Co Ltd Gas engine and method for controlling the same
JP2010059900A (en) * 2008-09-05 2010-03-18 Toho Gas Co Ltd Gas mixing device used in electric power generation system

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