JP2000074331A - Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system - Google Patents

Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system

Info

Publication number
JP2000074331A
JP2000074331A JP10240088A JP24008898A JP2000074331A JP 2000074331 A JP2000074331 A JP 2000074331A JP 10240088 A JP10240088 A JP 10240088A JP 24008898 A JP24008898 A JP 24008898A JP 2000074331 A JP2000074331 A JP 2000074331A
Authority
JP
Japan
Prior art keywords
exhaust gas
combustion
regenerator
burner
steam
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.)
Pending
Application number
JP10240088A
Other languages
Japanese (ja)
Inventor
Shingo Takao
信吾 高雄
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP10240088A priority Critical patent/JP2000074331A/en
Publication of JP2000074331A publication Critical patent/JP2000074331A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Gas Burners (AREA)
  • Air Supply (AREA)

Abstract

PROBLEM TO BE SOLVED: To largely improve an overall thermal efficiency by effectively utilizing a sensible heat of an exhaust gas. SOLUTION: In the thermal storage burner system for exhausting burned exhaust gas 21 from a burner B1 or B2 through a thermal storage unit R1 or R2 at time of non-burning by switching paired two burners B1, B2 at the each predetermined time, for alternately burning the burners B1, B2, and for supplying combustion air 12 to the burner B1 or B2 via the unit R1 or R2 at the time of burning; the gas 21 is elevated at its temperature, thermally converting a sensible heat absorbed via the unit R1 or R2 of the gas into steam at a serial two stages to be recovered, driving a blower 30 of the air by steam heat recovered at a high temperature stage, driving a regenerator 25 of dehumidified liquid by the steam heat recovered at a low temperature stage, and dehumidifying combustion gas 18 and/or the air 12 by using the dehumidified liquid regenerated by the regenerator.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は燃料ガスと燃焼用空
気をバーナに供給して燃焼させる蓄熱バーナシステムの
排ガス高温化による総合熱効率向上方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for improving the overall thermal efficiency of a heat storage burner system in which fuel gas and combustion air are supplied to a burner and burned by raising the temperature of exhaust gas.

【0002】[0002]

【従来の技術】従来、対をなす二つのバーナを所定時間
ごとに切り替えて交互に燃焼させ、燃焼時には蓄熱体を
通して前記バーナへ燃焼用空気を供給し、非燃焼時には
前記バーナから蓄熱体を通して燃焼排ガスを排出する蓄
熱バーナシステムは特開昭6―200321号公報に開
示され公知の技術となっている。
2. Description of the Related Art Conventionally, two burners forming a pair are switched alternately at predetermined time intervals and burned alternately. Combustion air is supplied to the burner through a heat storage during combustion, and combustion is performed from the burner through a heat storage during non-combustion. A heat storage burner system for discharging exhaust gas is disclosed in Japanese Patent Application Laid-Open No. 6-200321 and is a known technology.

【0003】[0003]

【発明が解決しようとする課題】鋼材加熱炉等として用
いる従来の蓄熱バーナシステムでは、蓄熱体を経由して
吸引した顕熱(250℃程度)のある排ガスを未利用で
放出していた。本発明の目的は、排ガスの顕熱を有効に
利用してシステムの総合熱効率を大幅に向上させること
ができ、また回収された熱を使って燃焼システムの効率
も同時に上げることができる蓄熱バーナシステムの排ガ
ス高温化による総合熱効率向上方法を提供することにあ
る。
In a conventional heat storage burner system used as a steel heating furnace or the like, exhaust gas having sensible heat (about 250 ° C.) sucked through a heat storage body is released without being used. SUMMARY OF THE INVENTION It is an object of the present invention to provide a heat storage burner system capable of significantly improving the overall thermal efficiency of a system by effectively utilizing the sensible heat of exhaust gas, and simultaneously increasing the efficiency of a combustion system by using recovered heat. It is an object of the present invention to provide a method for improving overall thermal efficiency by increasing the temperature of exhaust gas.

【0004】[0004]

【課題を解決するための手段】前記の目的を達成するた
めに、本発明の請求項1による蓄熱バーナシステムの排
ガス高温化による総合熱効率向上方法は、対をなす二つ
のバーナを所定時間ごとに切り替えて交互に燃焼させ、
燃焼時には蓄熱体を通して前記バーナへ燃焼用空気を供
給し、非燃焼時には前記バーナから蓄熱体を通して燃焼
排ガスを排出する蓄熱バーナシステムにおいて、前記排
ガスを高温化し、該排ガスの蓄熱体を経由して吸引した
顕熱を直列2段階で蒸気に熱変換して回収し、高温段で
回収された蒸気熱で燃焼用空気の送風機を駆動し、低温
段で回収された蒸気熱で除湿液の再生器を駆動し、この
除湿液再生器で再生された除湿液を用いて燃料ガス及び
/又は燃焼用空気の除湿を行うことを特徴とする。
In order to achieve the above object, a method for improving the overall thermal efficiency by increasing the temperature of exhaust gas in a heat storage burner system according to claim 1 of the present invention, comprises the steps of: Switch and burn alternately,
In a heat storage burner system that supplies combustion air to the burner through the heat storage during combustion and discharges combustion exhaust gas from the burner through the heat storage during non-combustion, the temperature of the exhaust gas is increased, and the exhaust gas is suctioned through the heat storage. The sensible heat is converted into steam in two stages in series and collected.The steam heat collected in the high-temperature stage drives the combustion air blower, and the steam heat collected in the low-temperature stage forms a dehumidifier regenerator. The fuel cell system is driven to dehumidify the fuel gas and / or combustion air using the dehumidified liquid regenerated by the dehumidified liquid regenerator.

【0005】また、本発明の請求項2においては、対を
なす二つのバーナを所定時間ごとに切り替えて交互に燃
焼させ、燃焼時には蓄熱体を通して前記バーナへ燃焼用
空気を供給し、非燃焼時には前記バーナから蓄熱体を通
して燃焼排ガスを排出する蓄熱バーナシステムにおい
て、前記排ガスを高温化し、該排ガスの蓄熱体を経由し
て吸引した顕熱を直列2段階で蒸気に熱変換して回収
し、高温段で回収された蒸気熱で燃焼用空気の送風機を
駆動すると共に燃料ガス及び/又は燃焼用空気の予熱を
行い、低温段で回収された蒸気熱で除湿液の再生器を駆
動し、この除湿液再生器で再生された除湿液を用いて燃
料ガス及び/又は燃焼用空気の除湿を行うことを特徴と
する。
According to a second aspect of the present invention, two burners forming a pair are alternately burned by switching at predetermined intervals, and combustion air is supplied to the burner through a heat storage during combustion, and combustion is performed during non-combustion. In a heat storage burner system for discharging combustion exhaust gas from the burner through a heat storage material, the exhaust gas is heated to a high temperature, and the sensible heat sucked through the heat storage material of the exhaust gas is converted into steam in two stages in series and collected. The steam heat recovered in the stage drives the combustion air blower and preheats the fuel gas and / or combustion air, and the steam heat recovered in the low-temperature stage drives the dehumidifier regenerator. The fuel gas and / or combustion air is dehumidified by using the dehumidified liquid regenerated by the liquid regenerator.

【0006】以上のように、本発明においては蓄熱バー
システムの排ガスを高温化し、この高温排ガスから2段
階の温度レベルで回収した各蒸気を燃焼用空気の送風機
駆動動力、燃料ガス及び/又は燃焼用空気の予熱熱源、
燃料ガス及び/又は燃焼用空気の除湿再生用熱源に用い
るので、排ガスの最終温度を除湿再生器の戻り温度レベ
ルまで下げることが可能となり、総合の熱利用効率が大
幅に向上する。また、予熱および駆動エネルギーの削減
により燃焼システムの効率も同時に上げることが可能と
なる。
As described above, in the present invention, the exhaust gas of the heat storage bar system is heated to a high temperature, and the steam recovered from the high temperature exhaust gas at two temperature levels is used to drive the blower driving power of the combustion air, the fuel gas and / or the combustion gas. Air preheating heat source,
Since it is used as a heat source for dehumidifying and regenerating fuel gas and / or combustion air, the final temperature of exhaust gas can be reduced to the return temperature level of the dehumidifying regenerator, and the overall heat utilization efficiency is greatly improved. In addition, the efficiency of the combustion system can be increased at the same time by reducing the preheating and the driving energy.

【0007】[0007]

【発明の実施の形態】以下、本発明を図面に示す実施形
態に基づいて具体的に説明する。この実施例はスラブ、
パイプ等を加熱する熱風炉を蓄熱バーナシステムとした
適用例を示すものであって、図面では火炎7を噴射する
バーナB1が燃焼状態にあり、燃焼排ガス21は非燃焼
側のバーナB2、蓄熱体R2、燃焼排ガスのバルブV4
を通して排気されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below based on embodiments shown in the drawings. This embodiment is a slab,
This shows an application example in which a hot blast stove for heating pipes and the like is used as a heat storage burner system. In the drawing, a burner B1 for injecting a flame 7 is in a combustion state, and a combustion exhaust gas 21 is a non-combustion side burner B2, a heat storage element. R2, combustion exhaust valve V4
Has been exhausted through.

【0008】この状態では燃料ガス18のバルブV1と
燃焼排ガス18のバルブV4と燃焼用空気12のバブル
V5が開、燃料ガス18のバルブV2と燃焼排ガス18
のバルブV2と燃焼用空気12のバブルV6が閉となっ
ている。
In this state, the valve V1 of the fuel gas 18, the valve V4 of the combustion exhaust gas 18 and the bubble V5 of the combustion air 12 are opened, and the valve V2 of the fuel gas 18 and the combustion exhaust gas 18 are opened.
The valve V2 and the bubble V6 of the combustion air 12 are closed.

【0009】前記バーナB1での燃焼は、コントローラ
等で設定される時間続行され、燃焼切替え時間に達した
時点で、前記バルブV1, V4,V5が閉められ、且つ
前記バルブV2, V3,V6が開けられて、バーナB2
での燃焼に切り替えられる。
The combustion in the burner B1 continues for a time set by a controller or the like. When the combustion switching time is reached, the valves V1, V4 and V5 are closed, and the valves V2, V3 and V6 are closed. Opened, burner B2
Can be switched to combustion.

【0010】以上説明したように、本実施例の対象とす
る燃焼システムは、対をなす二つのバーナB1,B2を
所定時間ごとに切り替えて交互に燃焼させ、燃焼時には
蓄熱体R1又はR2を通して前記バーナB1又はB2へ
燃焼用空気12を供給し、非燃焼時には前記バーナB2
又はB1から蓄熱体R2又はR1を通して燃焼排ガス2
1を排出する蓄熱式のバーナシステムであって、前記排
ガス21をその温度が従来の設定温度(例えば、250
℃)より高い温度(例えば、300℃)になるように高
温化している。
As described above, in the combustion system according to the present embodiment, the two burners B1 and B2 forming a pair are switched at predetermined time intervals and burned alternately. At the time of combustion, the burners B1 and B2 pass through the heat accumulator R1 or R2. The combustion air 12 is supplied to the burner B1 or B2.
Or flue gas 2 from B1 through regenerator R2 or R1
1 is a regenerative burner system which discharges the exhaust gas 21 at a conventional set temperature (for example, 250 ° C.).
℃) to a higher temperature (for example, 300 ℃).

【0011】そして、前記排ガス21の排出経路に前記
排ガス21の蓄熱体R2又はR1を経由して吸引した顕
熱を直列2段階で蒸気に熱変換して回収する熱交換器2
2を設置し、この熱交換器22の高温段22aで回収さ
れた180℃程度の蒸気熱で燃焼用空気の蒸気作動式送
風機30を駆動すると共に燃料ガス及び燃焼用空気の予
熱器28を作動させて燃料ガス18及び燃焼用空気12
の予熱を行う。
A heat exchanger 2 for converting the sensible heat sucked into the exhaust gas 21 through the heat storage material R2 or R1 of the exhaust gas 21 into steam in two stages in series and recovering it.
2, the steam-operated blower 30 for combustion air is driven by the steam heat of about 180 ° C. collected in the high-temperature stage 22a of the heat exchanger 22, and the preheater 28 for fuel gas and combustion air is operated. The fuel gas 18 and the combustion air 12
Perform preheating.

【0012】また、前記熱交換器22の低温段22bで
回収された120℃程度の蒸気熱で除湿液の再生器25
を駆動し、この除湿液再生器25で再生された除湿液を
燃料ガス供給経路18aに組み込まれた除湿機26と燃
焼用空気供給経路12aに組み込まれた除湿機27に循
環ライン25a,25bを介して循環させて、水分を含
む燃焼用空気12及び燃料ガス18の除湿を行うように
構成している。
The dehumidifying liquid regenerator 25 is heated by the steam heat of about 120 ° C. recovered in the low-temperature stage 22b of the heat exchanger 22.
And the circulation lines 25a and 25b are connected to a dehumidifier 26 incorporated in the fuel gas supply path 18a and a dehumidifier 27 incorporated in the combustion air supply path 12a by using the dehumidified liquid regenerated by the dehumidified liquid regenerator 25. The combustion air 12 and the fuel gas 18 containing moisture are dehumidified by being circulated.

【0013】なお、前記熱交換器22の高温段の蒸気循
環路と低温段の蒸気循環路には蒸気循環用のポンプ23
a,23bが組み込まれている。前記除湿機26, 27
は、高濃度かつ低温度の塩化リチウム溶液(除湿液)と
水分を含む燃料ガス18及び燃焼用空気12を直接接触
させることにより、水分を燃料ガス18及び燃焼用空気
12から除湿液に移動させて除湿する従来公知のもので
あって、この除湿により低濃度になった除湿液は除湿液
再生器25に循環移送して加熱し、大気と直接接触させ
ることにより水分を除湿液から空気中に移動させて高濃
度に濃縮・再生される。
The high-temperature steam circulation path and the low-temperature steam circulation path of the heat exchanger 22 have a steam circulation pump 23.
a and 23b are incorporated. The dehumidifier 26, 27
Moves the moisture from the fuel gas 18 and the combustion air 12 to the dehumidifying solution by directly contacting the fuel gas 18 containing the moisture and the combustion air 12 with a high concentration and low temperature lithium chloride solution (dehumidifying solution). The dehumidifying solution, which is conventionally known to be dehumidified by the dehumidifying method, is circulated and transferred to the dehumidifying solution regenerator 25 to be heated, and is brought into direct contact with the atmosphere to remove moisture from the dehumidifying solution into the air. It is moved and concentrated and regenerated to a high concentration.

【0014】以上述べた実施例では、排ガス21の最終
温度を100℃レベルまで下げることができるため、高
温化による温度差(約150℃相当)の熱を有効に利用
でき、また回収熱を予熱にまわすことでシステムの総合
熱効率は大幅に向上する。更に、回収された熱を使って
燃焼用空気及び燃料ガスの除湿と送風機30の駆動を行
うことにより、バーナシステムの熱効率も上げることが
できる。
In the embodiment described above, since the final temperature of the exhaust gas 21 can be lowered to the level of 100 ° C., the heat of the temperature difference (corresponding to about 150 ° C.) due to the high temperature can be effectively used, and the recovered heat can be preheated. The overall thermal efficiency of the system is greatly improved. Further, by using the recovered heat to dehumidify the combustion air and fuel gas and drive the blower 30, the thermal efficiency of the burner system can be increased.

【0015】なお、前記実施例は燃料ガス18及び燃焼
用空気12の両方を除湿し且つ予熱する場合について説
明したが、燃焼用空気12又は燃料ガス18のいずれか
一方を除湿し且つ予熱するように構成してもよいし、ま
た予熱器28については請求項1に示すように省略する
ことも可能である。
Although the above embodiment has been described with respect to the case where both the fuel gas 18 and the combustion air 12 are dehumidified and preheated, either the combustion air 12 or the fuel gas 18 is dehumidified and preheated. The preheater 28 may be omitted as shown in claim 1.

【0016】[0016]

【発明の効果】以上説明したように、本発明の方法によ
れば、排ガスの顕熱を有効に利用してシステムの総合熱
効率を大幅に向上させることができ、また回収された熱
を使って燃焼システムの効率も同時に上げることができ
るという効果を奏する。
As described above, according to the method of the present invention, the total thermal efficiency of the system can be significantly improved by effectively utilizing the sensible heat of the exhaust gas, and the recovered heat can be used. This has the effect of increasing the efficiency of the combustion system at the same time.

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

【図1】本発明における蓄熱バーナシステムの排ガス高
温化による総合熱効率向上方法の実施例を示す回路図。
FIG. 1 is a circuit diagram showing an embodiment of a method for improving overall thermal efficiency by increasing the temperature of exhaust gas in a heat storage burner system according to the present invention.

【符号の説明】[Explanation of symbols]

7…火炎、12…燃焼用空気、12a…燃焼用空気の供
給経路、18…燃料ガス、18a…燃料ガスの供給経
路、21…燃焼排ガス、B1, B2…バーナ、R1, R
2…蓄熱体、V1, V2…燃料ガスのバルブ、V3, V
4…燃焼排ガスのバルブ、V5, V6…燃焼用空気のバ
ルブ、22…熱交換器、25…除湿液再生器、26,2
7…除湿機、28…予熱器、30…送風機。
7: Flame, 12: Combustion air, 12a: Combustion air supply path, 18: Fuel gas, 18a: Fuel gas supply path, 21: Combustion exhaust gas, B1, B2: Burner, R1, R
2: heat storage element, V1, V2: fuel gas valve, V3, V
4: Valve of combustion exhaust gas, V5, V6: Valve of combustion air, 22: Heat exchanger, 25: Dehumidified liquid regenerator, 26, 2
7 ... dehumidifier, 28 ... preheater, 30 ... blower.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 対をなす二つのバーナを所定時間ごとに
切り替えて交互に燃焼させ、燃焼時には蓄熱体を通して
前記バーナへ燃焼用空気を供給し、非燃焼時には前記バ
ーナから蓄熱体を通して燃焼排ガスを排出する蓄熱バー
ナシステムにおいて、前記排ガスを高温化し、該排ガス
の蓄熱体を経由して吸引した顕熱を直列2段階で蒸気に
熱変換して回収し、高温段で回収された蒸気熱で燃焼用
空気の送風機を駆動し、低温段で回収された蒸気熱で除
湿液の再生器を駆動し、この除湿液再生器で再生された
除湿液を用いて燃料ガス及び/又は燃焼用空気の除湿を
行うことを特徴とする蓄熱バーナシステムの排ガス高温
化による総合熱効率向上方法。
1. A pair of two burners are switched at predetermined time intervals and burned alternately, and combustion air is supplied to the burner through a regenerator during combustion, and combustion exhaust gas is passed through the regenerator from the burner during non-combustion. In the heat storage burner system to be discharged, the exhaust gas is heated to a high temperature, and the sensible heat sucked through the heat storage body of the exhaust gas is converted into steam in two stages in series and collected, and is burned by the steam heat collected in the high temperature stage The dehumidifier regenerator is driven by the steam heat recovered in the low-temperature stage, and the dehumidifier regenerated by the dehumidifier regenerator is used to dehumidify the fuel gas and / or combustion air. A method for improving the overall thermal efficiency by increasing the temperature of exhaust gas in a heat storage burner system.
【請求項2】 対をなす二つのバーナを所定時間ごとに
切り替えて交互に燃焼させ、燃焼時には蓄熱体を通して
前記バーナへ燃焼用空気を供給し、非燃焼時には前記バ
ーナから蓄熱体を通して燃焼排ガスを排出する蓄熱バー
ナシステムにおいて、前記排ガスを高温化し、該排ガス
の蓄熱体を経由して吸引した顕熱を直列2段階で蒸気に
熱変換して回収し、高温段で回収された蒸気熱で燃焼用
空気の送風機を駆動すると共に燃料ガス及び/又は燃焼
用空気の予熱を行い、低温段で回収された蒸気熱で除湿
液の再生器を駆動し、この除湿液再生器で再生された除
湿液を用いて燃料ガス及び/又は燃焼用空気の除湿を行
うことを特徴とする蓄熱バーナシステムの排ガス高温化
による総合熱効率向上方法。
2. A pair of two burners are switched at predetermined time intervals and burned alternately. During combustion, combustion air is supplied to the burner through a regenerator, and during non-combustion, combustion exhaust gas is passed from the burner through a regenerator. In the heat storage burner system to be discharged, the exhaust gas is heated to a high temperature, and the sensible heat sucked through the heat storage body of the exhaust gas is converted into steam in two stages in series and collected, and is burned by the steam heat collected in the high temperature stage Drives the air blower and preheats the fuel gas and / or combustion air, drives the dehumidifier regenerator with the steam heat recovered at the low temperature stage, and regenerates the dehumidifier with this dehumidifier regenerator. A method for improving the overall thermal efficiency of a heat storage burner system by increasing the temperature of exhaust gas, wherein dehumidification of fuel gas and / or combustion air is performed using the gas.
JP10240088A 1998-08-26 1998-08-26 Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system Pending JP2000074331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10240088A JP2000074331A (en) 1998-08-26 1998-08-26 Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10240088A JP2000074331A (en) 1998-08-26 1998-08-26 Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system

Publications (1)

Publication Number Publication Date
JP2000074331A true JP2000074331A (en) 2000-03-14

Family

ID=17054317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10240088A Pending JP2000074331A (en) 1998-08-26 1998-08-26 Method for improving overall thermal efficiency by exhaust gas temperature elevating of thermal storage burner system

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102563684A (en) * 2012-01-12 2012-07-11 亿恒节能科技江苏有限公司 Fuel gas circulated tail gas refrigerating fuel gas air independent dehumidification heating system
KR20160078633A (en) * 2014-12-24 2016-07-05 재단법인 포항산업과학연구원 Regenerator of combustion furnace and Furnace having the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102563684A (en) * 2012-01-12 2012-07-11 亿恒节能科技江苏有限公司 Fuel gas circulated tail gas refrigerating fuel gas air independent dehumidification heating system
KR20160078633A (en) * 2014-12-24 2016-07-05 재단법인 포항산업과학연구원 Regenerator of combustion furnace and Furnace having the same
KR101644536B1 (en) * 2014-12-24 2016-08-02 재단법인 포항산업과학연구원 Furnace

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