JPS5923815A - Device for producing atmosphere gas - Google Patents

Device for producing atmosphere gas

Info

Publication number
JPS5923815A
JPS5923815A JP13428082A JP13428082A JPS5923815A JP S5923815 A JPS5923815 A JP S5923815A JP 13428082 A JP13428082 A JP 13428082A JP 13428082 A JP13428082 A JP 13428082A JP S5923815 A JPS5923815 A JP S5923815A
Authority
JP
Japan
Prior art keywords
gas
concn
endothermic
combustion
concentration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP13428082A
Other languages
Japanese (ja)
Other versions
JPS6058287B2 (en
Inventor
Takuji Katayama
片山 拓二
Toyoji Kitajima
北島 豊司
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro 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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP13428082A priority Critical patent/JPS6058287B2/en
Publication of JPS5923815A publication Critical patent/JPS5923815A/en
Publication of JPS6058287B2 publication Critical patent/JPS6058287B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
    • C21D1/76Adjusting the composition of the atmosphere
    • C21D1/763Adjusting the composition of the atmosphere using a catalyst

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Furnace Details (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

PURPOSE:To provide a titled production device by which an atmosphere gas having a prescribed concn. of CO over a wide range is obtained even if there is a fluctuation in the consumption, etc. of the atmosphere gas and the concn. of CO fluctuates by controlling the fluctuation in the concn. of CO in the atmosphere gas by adjusting the addition rate of an endothermic type gas contg. much CO. CONSTITUTION:The gas formed by combustion from a combustion chamber 2 in an exothermic type gas production device 1 is subjected to cooling 3 then to removal 4 of H2O and CO2 by adsorption to make NX which is an exothermic type gas and is supplied into a mixer 5. On the other hand, a gaseous mixture composed of fuel such as methane, propane or the like and air is heated with a retort 9 contg. a catalyst in an endothermic gas production device 7, by which the gas is modified 8. The modified gas is cooled 10 and is supplied as an RX gas which is an endothermic gas to the mixer 5. The NX gas and RX gas are mixed in the mixer to form the atmosphere gas having a prescribed concn. of CO and said gas is supplied 6 to a heat treatment furnace, etc. A flow rate control valve 16 is controlled to open or close by the signal from a measuring device 17 for concn. of CO provided on the downstream of the part where a supply pipe 6 is communicated with a by-pass line 15, whereby the concn. of CO in the atmosphere gas in the pipe 6 is controlled to a prescribed value.

Description

【発明の詳細な説明】 本発明は、雰囲気ガス製造装置、さらに詳しくは、消費
量の変O)があっても常に安定したCO含有量を確保す
ることのできる雰囲気ガス製造装置に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an atmospheric gas production device, and more particularly to an atmospheric gas production device that can always ensure a stable CO content even if there is a change in consumption. .

炭素鋼、合金鋼を熱処理する場合、雰囲気ガスを使用す
るが、近年、熱処理技術の向上、品質」−の要求により
厳密な雰囲気ガスのCO濃度制朗1か要求される。
When heat treating carbon steel and alloy steel, atmospheric gas is used, but in recent years, improvements in heat treatment technology and demands for quality have required strict control of the CO concentration of the atmospheric gas.

ところて、雰囲気ガスを発熱型ガス発生装置fj’?で
得る場合、一般に第1図に示すように雰囲気ガス中のC
O7農度は、使用ガス量の変化に伴う流量変化により吸
市塔の吸、#能力が変動することにより、ガス流量の増
加にともない、CO濃度も増加する傾向があること、お
よび1吸着剤の種類、品質のバラツキ、温度、圧力、使
用期間、1及仰剤の(1f生条件等による吸着能力の変
動に起因して、常に厳密なCO濃度を維持することは非
常に困難であった。
By the way, atmospheric gas is generated by a heat-generating gas generator fj'? In general, as shown in Figure 1, C in the atmospheric gas is
The O7 rate is based on the fact that the CO concentration tends to increase as the gas flow rate increases, as the adsorption capacity of the absorption tower fluctuates due to changes in the flow rate due to changes in the amount of gas used. It was extremely difficult to maintain a precise CO concentration at all times due to variations in adsorption capacity due to variations in type, quality, temperature, pressure, period of use, raw conditions of the agent, etc. .

これを解決するだめに、ガス発生装置からの雰囲気ガス
中のCOa度を測定することによりガス発生条件を制御
する方法も行なわれているが、CO濃度を高める必盟か
ある場合には、燃焼生成ガス中にススか発生するととも
に■I2濃ヴが高くなるきいう欠点を生ずる。
In order to solve this problem, a method is being used to control the gas generation conditions by measuring the COa concentration in the atmospheric gas from the gas generator, but if it is necessary to increase the CO concentration, combustion Soot is generated in the generated gas, and the I2 concentration increases.

本発明は、1jij記従来の欠点を除去するだめになさ
れたもので、発熱型ガス発生装量からの生成ガスと1汲
熱型ガス発生装置からの生成ガスを混合器て混僑・し、
所定COa度の雰囲気ガスとし、4丈用量の変化等によ
り雰囲気ガス中のCO濃度か変動すれは、バイパス路か
らCOa度の高い吸熱型ガス発生装置1qからの生成ガ
スを添加して常に最適な00濃度に制御するとともに、
吸熱型ガス発生装置1“11”の変成炉における熱源を
発熱型ガス発生装置Wtからの燃・1か生成ガスの一部
で行なうようにして省エネルギーを図った雰囲気ガス製
造装置を提供しようとするものである。
The present invention has been made in order to eliminate the drawbacks of the prior art as described in 1.1.
The atmosphere gas has a predetermined COa degree, and if the CO concentration in the atmosphere gas fluctuates due to changes in the amount of COa, etc., the produced gas from the endothermic gas generator 1q with a high COa degree is added from the bypass path to always maintain the optimum value. While controlling the concentration to 00,
An object of the present invention is to provide an atmospheric gas production device that saves energy by using a part of the combustion gas from an exothermic gas generator Wt as a heat source in a shift furnace of an endothermic gas generator 1 "11". It is something.

つきに、木発1]I]を一実施例である図面にしだがっ
て説明する。
Finally, Kibatsu 1]I] will be explained with reference to a drawing which is an example.

第2図において、1は発熱型ガス発生装量で、高負荷燃
焼を行なう燃焼室2L、冷却塔33よひl汲イ′1装置
f:4.4とからなり、燃焼室2からの燃焼生成ガ刈」
冷却された後(汲佇装置4てそのI■20とC02を除
去され、発熱型ガスであるNXガス(CO:1.8シロ
、CO3,005几112°■096、N2  残り)
となり、混合器5に供給される。
In Fig. 2, reference numeral 1 denotes the exothermic gas generation capacity, which consists of a combustion chamber 2L for performing high-load combustion, a cooling tower 33 and a pumping device f: 4.4. "Garage generation"
After being cooled (the I20 and C02 are removed by the pumping device 4, the exothermic gas NX gas (CO: 1.8 kg, CO3,005 112° ■096, N2 remains)
and is supplied to the mixer 5.

7は吸熱型ガス発生装動て、変成炉8および冷却器10
からなり、メタン・プロパン等の燃料と空気上の混合ガ
スが触媒を内蔵するレトルト9て加熱されて変成し、冷
却器10て冷却されて1汲熱型ガスであるR Xガス(
CO: 24K II2: 33.4!、16、CH4
: 0,496、CO2096、N2:残り)となり、
前記混合器5へ供給される。そして混合器5て+iff
記NXガスとRXガスとか混合され、所定CO画濃度雰
囲気ガスとなって、雰囲気ガス供給管6により熱処理炉
等に供給される。
7 is an endothermic gas generator, a shift furnace 8 and a cooler 10;
A mixed gas of fuel such as methane or propane and air is heated in a retort 9 containing a catalyst and transformed, and then cooled in a cooler 10 to produce R
CO: 24K II2: 33.4! ,16,CH4
: 0,496, CO2096, N2: remaining),
The mixture is supplied to the mixer 5. And mixer 5+if
The NX gas and the RX gas are mixed to form an atmospheric gas having a predetermined CO image concentration, which is supplied to a heat treatment furnace or the like through an atmospheric gas supply pipe 6.

なお、11はNXガスとRXガスとの混合比率を制r」
する比率調整器、12−脱水器である。
In addition, 11 controls the mixing ratio of NX gas and RX gas.
12-Dehydrator.

そして、曲記斐成炉8のレトルト9を加熱する熱源とし
て、前記燃焼室2からの燃焼生成ガスの一部分を変成炉
8に分岐供給し、レトルト9を加熱した後、燃焼生成ガ
スは燃焼生成ガス供給”4; 13の冷却器13aを経
てIJ’J 、′ic!吸百装)H4に1共給される。
Then, as a heat source for heating the retort 9 of the conversion furnace 8, a part of the combustion gas from the combustion chamber 2 is branched and supplied to the shift furnace 8, and after heating the retort 9, the combustion gas is converted to the combustion gas. Gas supply 4; 1 is co-supplied to IJ'J, 'ic! suction unit) H4 through 13 coolers 13a.

詮た、Orf記分岐燃焼生成ガスJi!幻、変成が58
のh” 温により開閉される流量制御ブT14により制
が11され、常に変成炉8 li所定炉温に保持される
I read the Orf branch combustion generated gas Ji! Illusion and transmutation are 58
The flow rate control valve T14, which is opened and closed depending on the temperature of the converter 8.

1、5 &;j前記供給管6と脱水器12からの生成ガ
ス供給管とバイパスするバイパス路で、このバイパス路
15にCJ流、iV1制御介16が設けられている。
1, 5 &;j A bypass path that bypasses the supply pipe 6 and the produced gas supply pipe from the dehydrator 12, and this bypass path 15 is provided with a CJ flow and iV1 control system 16.

1だ、前記供給管6のバイパス路15との連通部より下
流に一1GO濃度測定器17が設けられ、前記流量器m
11介16はRfJ記CO濃度測定器17からの(l−
i ′fJにより開閉制御されるようになっている。
1, a GO concentration measuring device 17 is provided downstream from the communication portion of the supply pipe 6 with the bypass path 15, and the flow rate device m
11 and 16 are (l-
Opening/closing is controlled by i'fJ.

しだかつて、い才、使用雰囲気ガスの使用JJ!Lか増
大すること等の理由により吸着装置4の吸百能力か変動
し、CO濃度が所定値より低くなると、この・仄態をC
O濃度測定器17で検出して流ill制6111介16
を開とし、供給管6中の雰囲気ガスにおけるCO濃度を
所定値にするように制ω11することになる。なお、実
操業において供給管6の出L1流11j、を]00靜/
11  とすれば、吸熱型ガス発生装動7出[−1流計
−20扉/11以下であればよい。似し、特に高CO濃
度の雰囲気ガスを必要とする場合には、吸熱型ガス発生
/汁を50 nl/I+とすることもある。
JJ's skill and use of atmosphere gas! If the adsorption capacity of the adsorption device 4 fluctuates due to an increase in the CO concentration and the CO concentration becomes lower than a predetermined value, this
Detected by O concentration measuring device 17 and flow control 6111-16
is opened, and the CO concentration in the atmospheric gas in the supply pipe 6 is controlled to a predetermined value by controlling ω11. In addition, in actual operation, the output L1 flow 11j of the supply pipe 6 is set to ]00/
11, it is sufficient that the endothermic gas generator has 7 outputs [-1 flowmeter-20 doors/11 or less]. Similarly, if an atmospheric gas with a particularly high CO concentration is required, the endothermic gas generation/juice may be 50 nl/I+.

以上の説明で明らかなように、本発明にかかる雰囲気ガ
ス製造装動によれば、雰囲気ガス中のCO?農反のf!
+11Iを、C0−hlの多い吸熱型ガスの添加量の調
整により制御J11するため、雰囲気ガスの消費り。
As is clear from the above explanation, according to the atmospheric gas production device according to the present invention, CO in the atmospheric gas? Anti-agriculture f!
Since +11I is controlled by adjusting the amount of endothermic gas added with a large amount of C0-hl, atmospheric gas is consumed.

等にgiのかあり、GO濃度が変!IIIJしCも、広
範囲にわたって所定CO画濃度雰囲気ガスを1!1・る
仁とかできる。また、吸熱型ガス発生装置i”fの熱+
JI:i lこ、発熱型ガス発生装置からの高温燃焼生
成ガスの−1114を使用し、l吸熱型ガス発生装置の
加熱用燃料を必要としないため省エネルギーを図ること
ができる。
There is gi in etc., and the GO concentration is strange! IIIJ and C can also reduce the atmospheric gas concentration to 1:1 over a wide range. In addition, the heat of the endothermic gas generator i”f +
JI:il This uses -1114 of the high-temperature combustion generated gas from the exothermic gas generator, and does not require heating fuel for the endothermic gas generator, so energy can be saved.

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

第1図は、発熱型ガス発生装置におけるC o濃度とガ
ス流計との関係を示すグラフで、第2図り」本発明にか
かる雰囲気ガス製)(5装置の概略図−C8る。 1・・発熱型ガス発生装置M、2・・・燃焼′ゲ、3・
・・冷却塔、4・・・1汲百装首、5・・混合4.6・
・・′、1y囲気ガス供給管、7・・・吸熱型ガス発生
装置l″1)゛、8 ・変成炉、9・・レトルト、10
・・・冷却器、13・・・燃焼生成ガス1JIH給愼・
、i 3 a  ・冷却器、15・・バイパス路、16
・・・流量制御弁、17・・・CO濃度測定器。
Figure 1 is a graph showing the relationship between the Co concentration and the gas flow meter in an exothermic gas generator;・Exothermic gas generator M, 2... combustion 'ge, 3.
・・Cooling tower, 4・1 100 heads, 5・・Mixture 4.6・
...', 1y Surrounding gas supply pipe, 7... Endothermic gas generator l''1)゛, 8 ・Transformation furnace, 9... Retort, 10
・・・Cooler, 13...Combustion generated gas 1JIH pumping・
, i 3 a - Cooler, 15... Bypass path, 16
...Flow rate control valve, 17...CO concentration measuring device.

Claims (1)

【特許請求の範囲】[Claims] (1)高負荷燃焼を行なう燃焼室、冷却塔および”)I
t、−i’f装置i<tからなる発熱型ガス発生装置と
、前記燃焼室からの燃焼生成ガスの一部を熱源とする変
成力iおよび冷却器からなる吸熱型ガス発生装置と、前
記変成炉の熱源として使用された燃焼生成ガスを前記灰
石装置に供給する供給管と、前記両ガス発生装置を出た
生成ガスを混合して所定雰囲気ガスとする混島滞と、r
′J[I記混合雰囲気ガス中のCO濃1身を測定するC
O濃度測定器と、前記吸熱型ガス発生装ばからの生成ガ
スを前記CO濃度測定器より」−、i& l+Jに供給
するバイパス路と、このバイパス路に設けられ前記CO
濃度測定器により制御される流垣制両弁と、から構成し
たことを特徴とする雰囲気ガス製造装置。
(1) Combustion chamber for high-load combustion, cooling tower and ") I
t, -i'f device i<t; an endothermic gas generator comprising a transformer power i and a cooler using part of the combustion generated gas from the combustion chamber as a heat source; a supply pipe that supplies the combustion generated gas used as a heat source of the conversion furnace to the ashstone device; a mixed island stagnation that mixes the generated gas exiting from both of the gas generators to form a predetermined atmospheric gas;
'J[I Measuring CO concentration in a mixed atmospheric gas C
an O concentration measuring device, a bypass path for supplying the generated gas from the endothermic gas generation device to the CO concentration measuring device, and a bypass path provided in this bypass path to
An atmospheric gas production device characterized by comprising: a flow barrier control valve controlled by a concentration measuring device;
JP13428082A 1982-07-30 1982-07-30 Atmospheric gas production equipment Expired JPS6058287B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13428082A JPS6058287B2 (en) 1982-07-30 1982-07-30 Atmospheric gas production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13428082A JPS6058287B2 (en) 1982-07-30 1982-07-30 Atmospheric gas production equipment

Publications (2)

Publication Number Publication Date
JPS5923815A true JPS5923815A (en) 1984-02-07
JPS6058287B2 JPS6058287B2 (en) 1985-12-19

Family

ID=15124586

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13428082A Expired JPS6058287B2 (en) 1982-07-30 1982-07-30 Atmospheric gas production equipment

Country Status (1)

Country Link
JP (1) JPS6058287B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007031667A1 (en) * 2005-09-16 2007-03-22 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for preventing formation of carbon monoxide during a gas quenching operation
JP2009156513A (en) * 2007-12-26 2009-07-16 Daido Plant Kogyo Kk Endothermic gas generating device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007031667A1 (en) * 2005-09-16 2007-03-22 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for preventing formation of carbon monoxide during a gas quenching operation
FR2890979A1 (en) * 2005-09-16 2007-03-23 Air Liquide METHOD FOR PREVENTING THE FORMATION OF CARBON MONOXIDE DURING A GAS TREATMENT OPERATION
JP2009156513A (en) * 2007-12-26 2009-07-16 Daido Plant Kogyo Kk Endothermic gas generating device

Also Published As

Publication number Publication date
JPS6058287B2 (en) 1985-12-19

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