JP2534418B2 - Calorimeter - Google Patents

Calorimeter

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Publication number
JP2534418B2
JP2534418B2 JP3335696A JP33569691A JP2534418B2 JP 2534418 B2 JP2534418 B2 JP 2534418B2 JP 3335696 A JP3335696 A JP 3335696A JP 33569691 A JP33569691 A JP 33569691A JP 2534418 B2 JP2534418 B2 JP 2534418B2
Authority
JP
Japan
Prior art keywords
gas
fuel gas
calorimeter
flow meter
flow rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP3335696A
Other languages
Japanese (ja)
Other versions
JPH05142066A (en
Inventor
一光 温井
実 瀬戸
直基 松原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
OOBARU KK
Tokyo Gas Co Ltd
Original Assignee
OOBARU KK
Tokyo Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by OOBARU KK, Tokyo Gas Co Ltd filed Critical OOBARU KK
Priority to JP3335696A priority Critical patent/JP2534418B2/en
Publication of JPH05142066A publication Critical patent/JPH05142066A/en
Application granted granted Critical
Publication of JP2534418B2 publication Critical patent/JP2534418B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Measuring Temperature Or Quantity Of Heat (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Description

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

【0001】[0001]

【技術分野】本発明は、熱量計、より詳細には、熱式流
量計と層流流量計とを直列に接続して熱式流量計の出力
を一定にする条件で層流流量計の標準状態における圧力
損失を検知することにより、燃料ガスの熱量を前記損失
圧力の関数として計測し燃料ガス中に含まれる特定のガ
ス成分の濃度に基づいて熱量を補正する簡易で正確な燃
料ガスの熱量計に関する。
TECHNICAL FIELD The present invention relates to a calorimeter, and more particularly to a standard laminar flow meter under the condition that a thermal flow meter and a laminar flow meter are connected in series to make the output of the thermal flow meter constant. By detecting the pressure loss in the state, the calorific value of the fuel gas is measured as a function of the loss pressure, and the calorific value is corrected based on the concentration of a specific gas component contained in the fuel gas. Regarding the total.

【0002】[0002]

【従来技術】燃料ガスおよび天然ガスは、その製造出荷
時において熱量および燃焼性を検知記録することが法的
に規定されており、この規定に基づいて混合ガスの熱量
を計測する熱量計が定められている。代表的な熱量計と
してユンカース式流水熱量計がある。この熱量計は、混
合ガスの燃料を空気と共に完全に燃焼させ、燃焼して生
じた廃ガスを最初のガス温度迄冷却して生成水蒸気を凝
縮させ、発生した熱の総量を熱量計に流れる水に吸収さ
せることにより、一定の混合ガス試料に対応する流水量
と、該流水の流入口および流出口における温度の温度差
とを乗算し、この乗算結果から総熱量を求めるという原
理である。
2. Description of the Related Art Fuel gas and natural gas are legally stipulated to detect and record the amount of heat and combustibility at the time of manufacturing and shipping, and a calorimeter for measuring the amount of heat of a mixed gas is stipulated based on this stipulation. Has been. A typical calorimeter is the Junkers-type running water calorimeter. This calorimeter completely burns the mixed gas fuel together with air, cools the waste gas produced by combustion to the initial gas temperature, condenses the generated steam, and collects the total amount of generated heat into the water flowing through the calorimeter. The principle is that the amount of flowing water corresponding to a fixed mixed gas sample is multiplied by the temperature difference between the temperature at the inlet and the outlet of the flowing water, and the total amount of heat is obtained from the multiplication result.

【0003】この熱量計は、基準熱量計として使用され
ているが、試験においては、水温と室温との温度差を±
0.5℃の範囲内で一致させるとか、1回の測定時間内
における水の温度変化を0.05℃以内に保つことが条
件とされる等、測定環境においての規定が厳しく、ま
た、測定の応答性も悪いので精度試験には適しているが
生産ラインでの使用に適さないため、別に速応形の熱量
計を使用することも認められており、通常、出荷時の熱
量の測定は、速応形の熱量計により連続的に行われてい
る。速応形の熱量計は、燃料ガスおよび空気を各々流量
計により計量して混合し、これをバーナで燃焼させ、燃
焼して生じた排ガスの温度と、燃焼用空気のバーナ入口
における温度とを熱電対等の温度検出器により検出して
各々の温度差と燃料ガスの空気に対する比重とを検知し
て、試料ガスの総発熱量と、該試料ガスの空気に対する
比重の平方根との比であるウォッペ指数(W.Iと呼
ぶ)を求め、被検燃料ガスの熱量をW.Iと試料ガスの
空気に対する比重の平方根との積として算出するもので
ある。その他の熱量検知方法に、混合ガスの熱量と、密
度とが比例関係にあるとの実験結果に基づいて、混合ガ
スの密度計測結果から熱量を算出することも試みられて
いる。
This calorimeter is used as a reference calorimeter, but in the test, the temperature difference between the water temperature and room temperature is ±
The conditions for measurement are strict, such as matching within 0.5 ° C and keeping the temperature change of water within 0.05 ° C within one measurement time. Since it is not suitable for use in a production line because it has a poor response, it is also approved to use a quick response type calorimeter because it is not suitable for use in a production line. , Is continuously performed by a quick response calorimeter. The fast-response type calorimeter measures the fuel gas and the air by metering them with a flow meter, mixes them, burns them with a burner, and burns them with the temperature of the exhaust gas and the temperature of the combustion air at the burner inlet. Detecting with a temperature detector such as a thermocouple, each temperature difference and the specific gravity of the fuel gas with respect to the air are detected, and the Woppe which is the ratio of the total calorific value of the sample gas to the square root of the specific gravity of the sample gas with respect to the air. An index (referred to as W.I) is obtained, and the heat quantity of the fuel gas to be tested is calculated as W.I. It is calculated as the product of I and the square root of the specific gravity of the sample gas with respect to air. As another heat quantity detection method, it has been attempted to calculate the heat quantity from the density measurement result of the mixed gas based on the experimental result that the heat quantity of the mixed gas and the density have a proportional relationship.

【0004】しかし、上述した速応形の熱量計は、高精
度な基準熱量計であるユンカース式流水形熱量計に代わ
る実用形の熱量計であるが、長時間の使用において測定
値がドリフトするため計測精度が低く1日の連続運転時
間に2回の割合で測定値を補正している。この補正操作
は煩わしいものであり、また、密度を検知する方法にお
いては、密度計が、通常、高価であり安価、簡易に熱量
を求めることはできなかった。これに対し、本出願人
は、下記の簡易な熱量計を提案した。
However, the above-described quick-response calorimeter is a practical calorimeter that replaces the Junkers-type running-water calorimeter, which is a highly accurate reference calorimeter, but its measured values drift when used for a long time. Therefore, the measurement accuracy is low, and the measured value is corrected twice a day during continuous operation time. This correction operation is troublesome, and in the method of detecting the density, the density meter is usually expensive and inexpensive, and the calorific value cannot be easily obtained. On the other hand, the applicant has proposed the following simple calorimeter.

【0005】特願平2−205378号における「熱量
計」は、燃料ガスの流路に、該燃料ガスの質量流量信号
を出力する熱式流量計と、該熱式流量計の出力を一定と
するように流量を制御する制御手段と、前記燃料ガスの
温度と圧力とを検知し標準状態における体積流量を差圧
信号として出力する層流流量計とを直列に接続し、前記
燃料ガスの熱量を前記差圧信号の逆数に比例した量とし
て演算出力する構成をもったものである。通常、都市ガ
スはメタンガスを主成分とする天然ガスであるが、都市
ガスを移送する場合には天然ガスをベースガスとしてプ
ロパンガス又はブタンガス等の高熱量の炭化水素ガスを
混合して熱量調整する。しかし、ある特定の燃料ガスの
中には、水素ガス、又は炭酸ガスを含むものがある。該
ベースガスの中に水素ガス又は炭酸ガスの濃度が一定量
含まれている場合は、混合した実ガスで校正することが
可能である。しかし、ベースガス中の水素ガス、炭酸ガ
スが不定量の場合は、熱量と差圧の相関がくずれ、熱量
計測定精度が低下するという問題点があった。
The "calorimeter" in Japanese Patent Application No. 2-205378 is a thermal type flow meter which outputs a mass flow rate signal of the fuel gas to a flow path of the fuel gas, and a constant output of the thermal type flow meter. And a laminar flow meter that detects the temperature and pressure of the fuel gas and outputs the volumetric flow rate in a standard state as a differential pressure signal, are connected in series, and the heat quantity of the fuel gas is controlled. Is calculated and output as an amount proportional to the reciprocal of the differential pressure signal. Usually, city gas is natural gas whose main component is methane gas, but when transferring city gas, heat amount is adjusted by mixing high calorific hydrocarbon gas such as propane gas or butane gas with natural gas as a base gas. . However, some specific fuel gases include hydrogen gas or carbon dioxide gas. When the base gas contains a certain amount of hydrogen gas or carbon dioxide, it is possible to calibrate with a mixed actual gas. However, when hydrogen gas and carbon dioxide gas in the base gas are indeterminate, there is a problem that the correlation between the calorific value and the differential pressure is lost and the calorimeter measurement accuracy is lowered.

【0006】[0006]

【目的】本発明は、上述のごとき実情に鑑みてなされた
もので、燃料ガスに含まれる水素ガス、炭酸ガス等のガ
ス濃度の量に影響されることなく高精度に燃料ガスの熱
量を計測できる簡易な熱量計を提供することを目的とす
るものである。
[Purpose] The present invention has been made in view of the above situation, and measures the calorific value of a fuel gas with high accuracy without being affected by the amount of gas concentration of hydrogen gas, carbon dioxide gas, etc. contained in the fuel gas. The purpose is to provide a simple calorimeter that can be used.

【0007】[0007]

【構成】本発明は、上記目的を達成するために、燃料ガ
スの流路に、該燃料ガスの質量流量信号を出力する熱式
流量計と、該熱式流量計の出力を一定とするように流量
を制御する制御手段と、前記燃料ガスの温度と圧力とを
検知し標準状態における体積流量を差圧信号として出力
する層流流量計と、前記燃料ガスに含まれる特定のガス
濃度に応じたガス濃度信号を出力するガス検知器とを直
列に接続し、前記燃料ガスの熱量を前記差圧信号の逆数
に比例して演算し、演算した熱量を前記ガス濃度信号に
基づいて補正する演算器とから構成したことを特徴とす
るもので、以下、本発明の実施例に基づいて説明する。
According to the present invention, in order to achieve the above object, a thermal type flow meter for outputting a mass flow rate signal of the fuel gas and a constant output of the thermal type flow meter are provided in a flow path of the fuel gas. A control means for controlling the flow rate, a laminar flow meter for detecting the temperature and pressure of the fuel gas and outputting the volumetric flow rate in a standard state as a differential pressure signal, and a laminar flow meter according to a specific gas concentration contained in the fuel gas. And a gas detector that outputs a gas concentration signal are connected in series, the calorific value of the fuel gas is calculated in proportion to the reciprocal of the differential pressure signal, and the calculated calorific value is corrected based on the gas concentration signal. It is characterized in that it is configured with a container, and will be described below based on an embodiment of the present invention.

【0008】図1は、本発明の熱量計における一実施例
を説明するための構成ブロック図で、図中、1は燃料ガ
ス流路、2は減圧弁、3はフィルタ、4は圧力計、5は
コントロールバルブ、6は熱式流量計、7は層流流量
計、8は差圧伝送器、9は温度計、10は圧力計、11
はガス検知器、12は演算器(表示器付)、13はPI
D(比例、積分、微分)制御器である。
FIG. 1 is a structural block diagram for explaining an embodiment of a calorimeter of the present invention. In the figure, 1 is a fuel gas passage, 2 is a pressure reducing valve, 3 is a filter, 4 is a pressure gauge, 5 is a control valve, 6 is a thermal type flow meter, 7 is a laminar flow meter, 8 is a differential pressure transmitter, 9 is a thermometer, 10 is a pressure gauge, 11
Is a gas detector, 12 is a calculator (with display), and 13 is PI
It is a D (proportional, integral, derivative) controller.

【0009】図示において熱量を測定するための燃料ガ
スは減圧弁2とフィルタ3とを介して大気圧近傍の低圧
で清浄な燃料ガスとなってコントロールバルブ5と熱式
流量計6と層流流量計7とを通って流出する。熱式流量
計6は、周知のように層流で流通する測定管にヒータを
巻回して混合ガスを加熱し、測定管の前後流において混
合ガスが熱交換されて生ずる温度差を抵抗値変化として
ブリッジ回路に組込んで電圧信号として検知するもの
で、出力電圧Vは V=K1・Cp・ρ・Q (1) (K1:定数、Cpは定圧比熱、ρは測定ガス密度、Q
は体積流量)であり、出力電圧Vは、質量流量ρ・Qと
定圧比熱Cpとに比例した線形出力となる。
In the figure, the fuel gas for measuring the amount of heat becomes clean fuel gas at a low pressure near atmospheric pressure via the pressure reducing valve 2 and the filter 3, and becomes a control valve 5, a thermal type flow meter 6, a laminar flow rate. It flows out through a total of 7. As is well known, the thermal flow meter 6 heats a mixed gas by winding a heater around a measuring tube that flows in a laminar flow, and changes a resistance value by a temperature difference caused by heat exchange of the mixed gas in a front-back flow of the measuring tube. Is incorporated in a bridge circuit and detected as a voltage signal. The output voltage V is V = K 1 · Cp · ρ · Q (1) (K 1 : constant, Cp is constant pressure specific heat, ρ is measured gas density, Q
Is a volumetric flow rate), and the output voltage V is a linear output proportional to the mass flow rate ρ · Q and the constant pressure specific heat Cp.

【0010】層流流量計7は周知のように低レイノルズ
(Re)数で流通する流体の体積流量Qが、該流体の流
通する流路の圧力損失ΔPに比例することを利用した流
量計であり、大気圧近傍の圧力のガスの体積流量Qは Q≒K2ΔP/μ(K2:定数、μ:燃料ガスの粘度)(2) であらわされる。
As is well known, the laminar flow meter 7 is a flow meter that utilizes the fact that the volumetric flow rate Q of a fluid flowing at a low Reynolds (Re) number is proportional to the pressure loss ΔP of a flow path of the fluid. Then, the volumetric flow rate Q of the gas at a pressure near the atmospheric pressure is expressed by Q≈K 2 ΔP / μ (K 2 : constant, μ: viscosity of fuel gas) (2).

【0011】一方、燃料ガスの発熱量H(Kcal/N
3)は燃料ガスの密度ρに比例し、粘度μおよび定圧
比熱Cpの逆数に比例することが知られている。(前記
出願特許明細書) 即ち、ρ=K3H (K3:定数) (3) μ=K4/H (K4:定数) (4) Cp=K5/H(K5:定数) (5) であり、(1)乃至(5)で熱式流量計の出力Vを一定
とすると H=KΔP (K:定数) (6) が得られる。
On the other hand, the calorific value H (Kcal / N) of the fuel gas
It is known that m 3 ) is proportional to the density ρ of the fuel gas and to the inverse of the viscosity μ and the constant pressure specific heat Cp. (The above-mentioned patent specification) ρ = K 3 H (K 3 : constant) (3) μ = K 4 / H (K 4 : constant) (4) Cp = K 5 / H (K 5 : constant) (5) and when the output V of the thermal type flow meter is constant in (1) to (5), H = KΔP (K: constant) (6) is obtained.

【0012】コントロールバルブ5は熱式流量計6の出
力を一定の値にするため燃料ガスの流量を制御する弁装
置であり、演算器12の設定値に基づいてPID制御器
13を介して駆動される。また、層流流量計7の差圧Δ
Pは差圧伝送器8で測定され、燃料ガス流路1の温度T
および、絶対圧力Pを各々温度計9、絶対圧力計10で
検知し、演算器12で体積流量Qが演算される。前記演
算器12においては、式(1)乃至(6)に基づいて燃
料ガスの熱量Hが演算されて出力し表示されるが、更に
前記熱量Hに対し、ガス検知器11より検知されたガス
濃度に応じて熱量Hの補正が演算される。
The control valve 5 is a valve device for controlling the flow rate of the fuel gas in order to make the output of the thermal type flow meter 6 constant, and is driven via the PID controller 13 based on the set value of the calculator 12. To be done. In addition, the differential pressure Δ of the laminar flow meter 7
P is measured by the differential pressure transmitter 8 and is the temperature T of the fuel gas flow path 1.
Also, the absolute pressure P is detected by the thermometer 9 and the absolute pressure gauge 10, respectively, and the volume flow rate Q is calculated by the calculator 12. In the calculator 12, the heat quantity H of the fuel gas is calculated based on the equations (1) to (6) and is output and displayed. Further, for the heat quantity H, the gas detected by the gas detector 11 is calculated. The correction of the heat quantity H is calculated according to the concentration.

【0013】燃料ガス中に、水素ガス又は炭酸ガスが含
まれると前述の熱量と密度との比例定数に変化を与え
る。ガス検知器11は、前記ガス濃度に応じて熱量を補
正するためのセンサであるから、前記ガスの濃度に応じ
た信号を出力するものであれば、検出方法は問わない。
例えば、周知のガス検知器には、測定気体の比例伝導率
(空気基準)の相異を利用して基準となる気体と伝導率
を比較する熱伝導形ガス検知器とか、光の屈折率を利用
して基準気体との間にモアレ縞を形成し、該モアレ縞の
縞密度からガス濃度を検知する光干渉ガス濃度計等があ
る。これらのガス濃度に基づいて燃料ガス熱量を補正す
ることにより高精度の燃料ガス熱量を検知することがで
きる。
When hydrogen gas or carbon dioxide gas is contained in the fuel gas, the proportional constant of the heat quantity and the density is changed. Since the gas detector 11 is a sensor for correcting the amount of heat according to the gas concentration, any detection method may be used as long as it outputs a signal according to the gas concentration.
For example, known gas detectors include a heat conduction type gas detector that compares the conductivity with a reference gas by utilizing the difference in the proportional conductivity (air reference) of the measurement gas, or the refractive index of light. There is an optical interference gas densitometer or the like that forms a moire fringe with a reference gas by utilizing it and detects the gas concentration from the fringe density of the moire fringe. By correcting the fuel gas heat quantity based on these gas concentrations, it is possible to detect the fuel gas heat quantity with high accuracy.

【0014】[0014]

【効果】以上の説明から明らかなように、本発明によれ
ば、燃料ガスの熱量を簡易な熱式流量計と層流流量計等
とからなる流量計を用いて構成し、更に、該熱量計を構
成するための関係式に影響を与える特定のガスのガス濃
度を検知して補正を加えるため簡易で高精度な熱量計を
提供できる。
As is apparent from the above description, according to the present invention, the calorific value of the fuel gas is configured by using a flowmeter including a simple thermal type flowmeter and a laminar flowmeter, and the calorific value is further increased. A simple and highly accurate calorimeter can be provided because the gas concentration of a specific gas that affects the relational expression for configuring the meter is detected and corrected.

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

【図1】 本発明の熱量計における一実施例を説明する
ための構成ブロック図である。
FIG. 1 is a configuration block diagram for explaining an embodiment of a calorimeter of the present invention.

【符号の説明】[Explanation of symbols]

1…燃料ガス流路、2…減圧弁、3…フィルタ、4…圧
力計、5…コントロールバルブ、6…熱式流量計、7…
層流流量計、8…差圧伝送器、9…温度計、10…絶対
圧力計、11…ガス検知器、12…演算器(表示器
付)、13…PID(比例、積分、微分)制御器。
1 ... Fuel gas flow path, 2 ... Pressure reducing valve, 3 ... Filter, 4 ... Pressure gauge, 5 ... Control valve, 6 ... Thermal flow meter, 7 ...
Laminar flow meter, 8 ... Differential pressure transmitter, 9 ... Thermometer, 10 ... Absolute pressure gauge, 11 ... Gas detector, 12 ... Computer (with display), 13 ... PID (proportional, integral, derivative) control vessel.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 燃料ガスの流路に、該燃料ガスの質量流
量信号を出力する熱式流量計と、該熱式流量計の出力を
一定とするように流量を制御する制御手段と、前記燃料
ガスの温度と圧力とを検知し標準状態における体積流量
を差圧信号として出力する層流流量計と、前記燃料ガス
に含まれる特定のガス濃度に応じたガス濃度信号を出力
するガス検知器とを直列に接続し、前記燃料ガスの熱量
を前記差圧信号の逆数に比例して演算し、演算した熱量
を前記ガス濃度信号に基づいて補正する演算器とから構
成したことを特徴とする熱量計。
1. A thermal type flow meter for outputting a mass flow rate signal of the fuel gas to a flow path of the fuel gas, a control means for controlling the flow rate so that the output of the thermal type flow meter is constant, and A laminar flow meter that detects the temperature and pressure of the fuel gas and outputs the volumetric flow rate in a standard state as a differential pressure signal, and a gas detector that outputs a gas concentration signal according to a specific gas concentration contained in the fuel gas. Is connected in series, the heat quantity of the fuel gas is calculated in proportion to the reciprocal of the differential pressure signal, and the calculated heat quantity is corrected based on the gas concentration signal. Calorimeter.
JP3335696A 1991-11-25 1991-11-25 Calorimeter Expired - Fee Related JP2534418B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3335696A JP2534418B2 (en) 1991-11-25 1991-11-25 Calorimeter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3335696A JP2534418B2 (en) 1991-11-25 1991-11-25 Calorimeter

Publications (2)

Publication Number Publication Date
JPH05142066A JPH05142066A (en) 1993-06-08
JP2534418B2 true JP2534418B2 (en) 1996-09-18

Family

ID=18291468

Family Applications (1)

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JP3335696A Expired - Fee Related JP2534418B2 (en) 1991-11-25 1991-11-25 Calorimeter

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Country Link
JP (1) JP2534418B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1164361A1 (en) * 2000-06-14 2001-12-19 Abb Research Ltd. Gasmeter
JP5184983B2 (en) * 2007-07-19 2013-04-17 理研計器株式会社 Calorimetry method and calorimeter
CN104034751A (en) * 2014-06-11 2014-09-10 中国计量学院 PID (proportion integration differentiation) control-based closed in-cavity natural convection heat transfer device and using method thereof
CN105466605A (en) * 2015-11-13 2016-04-06 北京京源水仪器仪表有限公司 Heat meter with working state monitoring function and monitoring method thereof

Also Published As

Publication number Publication date
JPH05142066A (en) 1993-06-08

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