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JP4090178B2 - High temperature regenerator - Google Patents
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JP4090178B2 - High temperature regenerator - Google Patents

High temperature regenerator Download PDF

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Publication number
JP4090178B2
JP4090178B2 JP2000054874A JP2000054874A JP4090178B2 JP 4090178 B2 JP4090178 B2 JP 4090178B2 JP 2000054874 A JP2000054874 A JP 2000054874A JP 2000054874 A JP2000054874 A JP 2000054874A JP 4090178 B2 JP4090178 B2 JP 4090178B2
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Japan
Prior art keywords
double
liquid
temperature regenerator
header
inner shell
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JP2000054874A
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JP2001241804A (en
Inventor
伯一 久保田
唯人 小林
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Sanyo Electric Co Ltd
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Sanyo Electric 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • 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
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

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  • Sorption Type Refrigeration Machines (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、吸収冷凍機の高温再生器に関するものである。
【0002】
【従来の技術】
この種の高温再生器としては、例えば特開平10−197100号公報に記載されているように、内シェル1と外シェル2との間の空間3と、内シェル1を上下に貫通して配管した多数の液管4とに注入した吸収液を、表面燃焼バーナ5により内シェル1の内側に生成する火炎6とその燃焼ガスにより加熱し、吸収液に吸収されていた冷媒を蒸発分離し、吸収液の濃度を高めて吸収液の再生を行うようにした構造のものが周知である。
【0003】
そして、このような構成の高温再生器においては、火炎6が短く形成される表面燃焼プレート7を混合室8の前面に装備した表面燃焼バーナ5を使用して、装置の小型化を図ると共に、燃焼を短期間で完結させてNOxの生成を抑えている。
【0004】
【発明が解決しようとする課題】
上記構成の高温再生器の場合、可燃性ガスと燃焼用空気が混合室で混合され、その混合気が表面燃焼プレートの無数の小孔を通過してその表面側で燃焼する構造であるため、熱応力を受ける表面燃焼プレートにひび割れや、位置ズレが生じて混合気が漏れると、混合室まで逆火して爆発し、大事故になる危険ある。
【0005】
このため、表面燃焼バーナに装着する表面燃焼プレートは、熱応力を繰り返し受けてもひび割れなどが生じないように作る必要があるが、セラミックスで作られることの多い表面燃焼プレートには、材質面から大型化に限界があるため、高温再生器の大容量化が難しく、したがって吸収冷凍機を大容量化することができないと云った問題点があり、この点の解決が課題となっていた。
【0006】
【課題を解決するための手段】
上記課題を解決するため本発明は、バーナと、バーナの火炎が内側に形成され、燃焼ガスが通過する内シェルと、内シェルとの間に吸収液を収容する外シェルと、内シェルを上下に貫通して配管され吸収液を通過させる液管群とを備えた二重缶体を水平面内に複数並設し、各二重缶体の内シェルと外シェルとの間の空間に連通する吸収液用入口ヘッダーと出口ヘッダーを設けると共に、各内シェルの非火炎形成側内側終端部同士を連通する排気ヘッダーを設けるようにした第1の構成の高温再生器と、
【0007】
前記第1の構成の高温再生器において、各二重缶体の内シェルと外シェルとの間の、吸収液用出口ヘッダーの液出口より低い部分の空間同士を、吸収液用入口ヘッダー・出口ヘッダー以外で連通するようにした第2の構成の高温再生器と、
【0008】
前記第1または第2の構成の高温再生器において、吸収液用出口ヘッダーまたは何れか一つの二重缶体に設けた吸収液検出手段の出力情報に基づいて、高温再生器に流入する吸収液の量を制御するようにした第3の構成の高温再生器と、
【0009】
前記第1〜第3何れかの構成の高温再生器において、各二重缶体に付設したバーナの燃焼量を同量に制御するようにした第4の構成の高温再生器と、
を提供するものである。
【0010】
【発明の実施の形態】
以下、図1に基づいて本発明の一実施形態を詳細に説明する。なお、理解を容易にするため、これらの図においても前記図2において説明した部分と同様の機能を有する部分には、同一の符号を付した。
【0011】
例示した本発明の高温再生器100は、内シェル1を備えた外シェル2を同一水平面内に複数、例えば2個並設し、それぞれの同じ側の一端に表面燃焼バーナ5を内シェル1の内側に臨ませて設置したものである。すなわち、前記図2で説明した従来の高温再生器と同様の二重缶体9を2個並設した構成となっている。
【0012】
表面燃焼バーナ5が設置された側の二重缶体9の下部には、二つの二重缶体9で共用する1個の液入口ヘッダー10を設置し、その液入口ヘッダー10に図示しない吸収冷凍機の吸収器から冷媒を吸収して吸収液濃度を下げた吸収液が吸収液ポンプにより注入口11から強制注入され、液入口ヘッダー10を介して二重缶体9それぞれの空間3の下部側に略均等に流入し、その流入した吸収液がそれぞれの二重缶体9の各液管4(図1では示していない)内にあって加熱され、沸騰して勢い良く上昇する気液混合流体の引き込み作用によって各液管4に入り、液管4それぞれの管壁を介して次々に加熱され続けるように構成してある。
【0013】
また、二重缶体9の表面燃焼バーナ5が設置されていない側の中段部には、二つの二重缶体9で共用する1個の液出口ヘッダー12を設置し、液入口ヘッダー10から各二重缶体9の空間3に強制注入され、それぞれの液管4の管壁などを介して加熱され、冷媒を蒸発分離して吸収液濃度が高まった吸収液が、この1個の液出口ヘッダー12で合流し、図示しない吸収冷凍機の低温再生器に向けて送り出せるように構成してある。なお、液出口ヘッダー12の液出口12Aは、内シェル1の上端より所定寸法だけ高い位置に設置して、各二重缶体9で吸収液が内シェル1、すなわち液管4の上端より高い位置まで収容できるようにしてある。
【0014】
また、二重缶体9の表面燃焼バーナ5が設置されていない側の上部には、二つの二重缶体9で共用する1個の蒸気出口ヘッダー13を設置し、液入口ヘッダー10から各二重缶体9の空間3に強制注入され、それぞれの液管4の管壁などを介して加熱されて吸収液から蒸発した冷媒蒸気が、この蒸気出口ヘッダー13で合流し、低温再生器に向けて送り出せるように構成してある。
【0015】
また、二重缶体9の表面燃焼バーナ5が設置されていない側の内シェル1の終端部同士を、排気ヘッダー14によって連通し、そこに排気ダクト15を連結して、各二重缶体9の表面燃焼バーナ5による燃焼によって生成された燃焼ガスを合流させて排気できるように構成してある。
【0016】
また、二重缶体9同士の隣接する空間3同士が連通するように連通管16を二箇所に設置している。2本の連通管16は、何れも液出口ヘッダー12の液出口12Aより少し低い位置に設置して、それぞれの空間3に収容した吸収液の行き来を可能にしてある。
【0017】
また、液出口ヘッダー12の、液出口12Aよりは低く内シェル1の上端よりは高い位置に液面センサ18を設置し、液出口ヘッダー12内にある吸収液の液面を検出して、制御器19に出力するようにしてある。
【0018】
制御器19は、液面センサ18が検出して出力する情報に基づいて、図示しない吸収冷凍機の吸収液ポンプをオン/オフ制御したり回転数制御して、吸収器で冷媒を吸収して吸収液濃度を下げた吸収液を液入口ヘッダー10の注入口11から二重缶体9それぞれに強制注入し、高温再生器100内にある吸収液の量(液面)を一定または所定の範囲に制御にする。
【0019】
また、この制御器19は、二つの表面燃焼バーナ5の火力が同一となるように、二つの混合室8には同量の可燃性ガスと燃焼用空気を供給する。
【0020】
なお、本発明は上記実施形態に限定されるものではないので、特許請求の範囲に記載の趣旨から逸脱しない範囲で各種の変形実施が可能である。
【0021】
例えば、吸収液の液面を検出する液面センサ18は、液出口ヘッダー12ではなく、何れか一方の二重缶体9に設置するようにしても良い。
【0022】
また、3個以上の二重缶体9を並設して一層の大容量化を図ることなども可能である。
【0023】
【発明の効果】
以上説明したように、本発明はバーナを備えた二重缶体を水平面内に複数並設して構成する高温再生器であるので、表面燃焼プレートの大容量化が困難であっても、製造可能な大きさの表面燃焼プレートを複数並設して大容量化するものであるから、NOxの生成が少ない表面燃焼プレートを使用した高温再生器の大容量化が容易であり、したがって吸収冷凍機の大容量化も容易に行える。
【0024】
また、各二重缶体の内シェルと外シェルとの間の空間に連通する吸収液用入口ヘッダーと出口ヘッダーを設けると共に、各内シェルの非火炎形成側内側終端部同士を連通する排気ヘッダーを設けた高温再生器であるので、配管構造が簡単になると共に、二重缶体毎に設けるバーナの発熱量が相違し、冷媒蒸気の発生量に違いが生じても、吸収液の液面レベルは出口ヘッダーを介して調節されるし、燃焼ガスの熱を回収するタイプの吸収冷凍機にする際の熱交換機構も簡単になる。
【0025】
また、各二重缶体の内シェルと外シェルとの間の、吸収液用出口ヘッダーの液出口より低い部分の空間同士を、吸収液用入口ヘッダー・出口ヘッダー以外で連通させる請求項2の発明によれば、各二重缶体の内シェルと外シェルとの間に収容して加熱し、冷媒を蒸発分離している吸収液の液面は一層一致し易くなる。
【0026】
また、吸収液用出口ヘッダーまたは何れか一つの二重缶体に設けられた吸収液検出手段の出力情報に基づいて、高温再生器に流入する吸収液の量を制御する請求項3の発明と、各二重缶体に付設したバーナの燃焼量を同量に制御する請求項4の発明によれば、制御が一層簡単になると共に、各二重缶体の内シェルと外シェルとの間にある吸収液の液面も一層一致し易くなる。
【図面の簡単な説明】
【図1】この発明の一実施形態を示す説明図で、(A)は平面図、(B)は側面図である。
【図2】従来技術を示す説明図で、(A)は水平断面図、(B)は垂直断面図である。
【符号の説明】
1 内シェル
2 外シェル
3 空間
4 液管
5 表面燃焼バーナ
6 火炎
7 表面燃焼プレート
8 混合室
9 二重缶体
10 液入口ヘッダー
11 注入口
12 液出口ヘッダー
12A 液出口
13 蒸気出口ヘッダー
14 排気ヘッダー
15 排気ダクト
16 連通管
17 連通管
18 液面センサ
19 制御器
100 高温再生器
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a high-temperature regenerator for an absorption refrigerator.
[0002]
[Prior art]
As this type of high-temperature regenerator, as described in, for example, Japanese Patent Laid-Open No. 10-197100, a space 3 between the inner shell 1 and the outer shell 2 and a pipe that penetrates the inner shell 1 vertically. The absorbing liquid injected into the numerous liquid pipes 4 is heated by the flame 6 generated inside the inner shell 1 by the surface combustion burner 5 and its combustion gas, and the refrigerant absorbed in the absorbing liquid is evaporated and separated. The thing of the structure which raised the density | concentration of absorption liquid and was made to reproduce | regenerate absorption liquid is known.
[0003]
And in the high temperature regenerator of such a structure, while using the surface combustion burner 5 which equips the front of the mixing chamber 8 with the surface combustion plate 7 in which the flame 6 is formed shortly, while aiming at size reduction of an apparatus, Combustion is completed in a short period of time to suppress generation of NOx.
[0004]
[Problems to be solved by the invention]
In the case of the high-temperature regenerator having the above configuration, the combustible gas and the combustion air are mixed in the mixing chamber, and the mixed gas passes through countless small holes of the surface combustion plate and burns on the surface side. If the air-fuel mixture leaks due to cracks or misalignment in the surface combustion plate that is subjected to thermal stress, there is a risk of a backfire and explosion to the mixing chamber, causing a major accident.
[0005]
For this reason, the surface combustion plate to be mounted on the surface combustion burner must be made so that it will not crack even if it is repeatedly subjected to thermal stress, but the surface combustion plate, which is often made of ceramics, Since there is a limit to the increase in size, there is a problem that it is difficult to increase the capacity of the high-temperature regenerator, and therefore the capacity of the absorption refrigerator cannot be increased.
[0006]
[Means for Solving the Problems]
In order to solve the above problems, the present invention is directed to a burner, an inner shell in which a flame of the burner is formed, a combustion gas passes through, an outer shell that contains an absorbent between the inner shell, and an inner shell A plurality of double cans that are piped through the pipe and have a liquid tube group that allows the absorption liquid to pass therethrough are juxtaposed in a horizontal plane, and communicate with the space between the inner shell and the outer shell of each double can. A high-temperature regenerator having a first configuration in which an inlet header for absorbing liquid and an outlet header are provided, and an exhaust header that communicates the inner end portions of the non-flame forming side of each inner shell is provided;
[0007]
In the high-temperature regenerator having the first configuration, the space between the inner shell and the outer shell of each double can body is lower than the liquid outlet of the outlet header for absorbing liquid, and the inlet header and outlet for absorbing liquid A high-temperature regenerator having a second configuration that communicates with other than the header;
[0008]
In the high temperature regenerator of the first or second configuration, the absorbing liquid flowing into the high temperature regenerator based on the output information of the absorbing liquid detecting means provided in the outlet header for absorbing liquid or any one of the double cans A high temperature regenerator of a third configuration that controls the amount of
[0009]
In the high temperature regenerator of any one of the first to third configurations, a high temperature regenerator of the fourth configuration configured to control the combustion amount of the burner attached to each double can body to the same amount;
Is to provide.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described in detail with reference to FIG. In order to facilitate understanding, in these drawings, parts having the same functions as those described with reference to FIG.
[0011]
The illustrated high temperature regenerator 100 includes a plurality of, for example, two outer shells 2 provided with an inner shell 1 in the same horizontal plane, and a surface combustion burner 5 at one end of each same side. It was installed facing the inside. That is, two double cans 9 similar to the conventional high-temperature regenerator described in FIG. 2 are arranged side by side.
[0012]
One liquid inlet header 10 shared by the two double can bodies 9 is installed below the double can body 9 on the side where the surface combustion burner 5 is installed, and the liquid inlet header 10 has an absorption (not shown). Absorbed liquid whose absorption liquid concentration has been reduced by absorbing refrigerant from the absorber of the refrigerator is forcibly injected from the injection port 11 by the absorption liquid pump, and below the space 3 of each of the double can bodies 9 via the liquid inlet header 10. The gas-liquid which flows into the side substantially evenly, and the absorbed liquid which flows in is in each liquid pipe | tube 4 (not shown in FIG. 1) of each double can body 9, is heated, boils, and rises vigorously Each liquid pipe 4 is entered by the drawing action of the mixed fluid and is continuously heated through the respective pipe walls of the liquid pipe 4.
[0013]
In addition, a single liquid outlet header 12 shared by the two double can bodies 9 is installed in the middle portion of the double can body 9 on the side where the surface combustion burner 5 is not installed. The absorption liquid which is forcedly injected into the space 3 of each double can 9 and heated via the pipe wall of each liquid pipe 4 to evaporate and separate the refrigerant and the concentration of the absorption liquid is increased. It merges at the outlet header 12 and is configured to be sent out toward a low-temperature regenerator of an absorption refrigerator (not shown). The liquid outlet 12A of the liquid outlet header 12 is installed at a position higher than the upper end of the inner shell 1 by a predetermined dimension, and the absorption liquid is higher than the upper end of the inner shell 1, that is, the liquid pipe 4 in each double can body 9. It can be accommodated up to the position.
[0014]
In addition, one steam outlet header 13 shared by the two double can bodies 9 is installed on the upper portion of the double can body 9 on the side where the surface combustion burner 5 is not installed. Refrigerant vapor that has been forcedly injected into the space 3 of the double can 9 and heated from the tube walls of the respective liquid tubes 4 and evaporated from the absorption liquid joins at the vapor outlet header 13 and is supplied to the low-temperature regenerator. It is configured so that it can be sent out.
[0015]
Further, the end portions of the inner shell 1 on the side where the surface combustion burner 5 of the double can body 9 is not installed are communicated with each other by an exhaust header 14, and an exhaust duct 15 is connected thereto to connect each double can body. The combustion gas generated by the combustion by the surface combustion burner 5 is joined so that it can be exhausted.
[0016]
Moreover, the communication pipe | tube 16 is installed in two places so that the adjacent spaces 3 of the double can bodies 9 may communicate. Each of the two communication pipes 16 is installed at a position slightly lower than the liquid outlet 12 </ b> A of the liquid outlet header 12, so that the absorption liquid stored in each space 3 can be moved back and forth.
[0017]
Further, a liquid level sensor 18 is installed at a position lower than the liquid outlet 12A of the liquid outlet header 12 and higher than the upper end of the inner shell 1, and the liquid level of the absorbing liquid in the liquid outlet header 12 is detected and controlled. The data is output to the device 19.
[0018]
Based on the information detected and output by the liquid level sensor 18, the controller 19 performs on / off control or rotation speed control of an absorption liquid pump of an absorption refrigerator (not shown) to absorb the refrigerant with the absorber. Absorbing liquid whose concentration of absorbing liquid is lowered is forcibly injected into each of the double cans 9 from the inlet 11 of the liquid inlet header 10, and the amount (liquid level) of the absorbing liquid in the high-temperature regenerator 100 is constant or within a predetermined range. To control.
[0019]
The controller 19 supplies the same amount of combustible gas and combustion air to the two mixing chambers 8 so that the heating powers of the two surface combustion burners 5 are the same.
[0020]
In addition, since this invention is not limited to the said embodiment, various deformation | transformation implementation is possible in the range which does not deviate from the meaning as described in a claim.
[0021]
For example, the liquid level sensor 18 for detecting the liquid level of the absorbing liquid may be installed not in the liquid outlet header 12 but in any one of the double cans 9.
[0022]
It is also possible to increase the capacity further by arranging three or more double cans 9 side by side.
[0023]
【The invention's effect】
As described above, the present invention is a high-temperature regenerator constructed by arranging a plurality of double can bodies equipped with burners in a horizontal plane, so that even if it is difficult to increase the capacity of the surface combustion plate, it is manufactured. Since a plurality of surface combustion plates of a possible size are arranged side by side to increase the capacity, it is easy to increase the capacity of a high-temperature regenerator using a surface combustion plate that generates little NOx, and therefore an absorption refrigerator Can be easily increased in capacity.
[0024]
In addition, an inlet header and an outlet header for absorbing liquid that communicate with the space between the inner shell and the outer shell of each double can body are provided, and an exhaust header that communicates between the non-flame forming side inner terminal portions of each inner shell The high-temperature regenerator is provided with a high-temperature regenerator, so that the piping structure is simplified, the heat generation amount of the burner provided for each double can body is different, and even if there is a difference in the generation amount of refrigerant vapor, the liquid level of the absorbing liquid The level is adjusted through the outlet header, and the heat exchange mechanism in the type of absorption refrigerator that recovers the heat of the combustion gas is simplified.
[0025]
Further, the space between the inner shell and the outer shell of each double can that is lower than the liquid outlet of the absorbent outlet header is communicated with other than the absorbent inlet and outlet headers. According to the invention, the liquid level of the absorbing liquid which is accommodated between the inner shell and the outer shell of each double can body and heated to evaporate and separate the refrigerant becomes easier to match.
[0026]
Further, the invention according to claim 3, wherein the amount of absorbing liquid flowing into the high-temperature regenerator is controlled based on the output information of the absorbing liquid detecting means provided in the absorbing liquid outlet header or any one of the double cans. According to the invention of claim 4 which controls the combustion amount of the burner attached to each double can body to the same amount, the control is further simplified, and between the inner shell and the outer shell of each double can body. The liquid level of the absorption liquid in the layer is also more easily matched.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing an embodiment of the present invention, in which (A) is a plan view and (B) is a side view.
2A and 2B are explanatory views showing a conventional technique, in which FIG. 2A is a horizontal sectional view and FIG. 2B is a vertical sectional view.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Inner shell 2 Outer shell 3 Space 4 Liquid pipe 5 Surface combustion burner 6 Flame 7 Surface combustion plate 8 Mixing chamber 9 Double can body 10 Liquid inlet header 11 Inlet 12 Liquid outlet header 12A Liquid outlet 13 Steam outlet header 14 Exhaust header 15 Exhaust duct 16 Communication pipe 17 Communication pipe 18 Liquid level sensor 19 Controller 100 High temperature regenerator

Claims (4)

バーナと、バーナの火炎が内側に形成され、燃焼ガスが通過する内シェルと、内シェルとの間に吸収液を収容する外シェルと、内シェルを上下に貫通して配管され吸収液を通過させる液管群とを備えた二重缶体を水平面内に複数並設し、各二重缶体の内シェルと外シェルとの間の空間に連通する吸収液用入口ヘッダーと出口ヘッダーを設けると共に、各内シェルの非火炎形成側内側終端部同士を連通する排気ヘッダーを設けたことを特徴とする高温再生器。A burner, a burner flame is formed inside, an inner shell through which combustion gas passes, an outer shell that contains the absorbent between the inner shell, and a pipe that passes vertically through the inner shell and passes through the absorbent A plurality of double cans having a liquid tube group to be arranged are arranged side by side in a horizontal plane, and an inlet header and an outlet header for absorbing liquid communicating with a space between the inner shell and the outer shell of each double can body are provided. In addition, a high-temperature regenerator comprising an exhaust header that communicates the non-flame forming side inner terminal portions of the inner shells. 各二重缶体の内シェルと外シェルとの間の、吸収液用出口ヘッダーの液出口より低い部分の空間同士が、吸収液用入口ヘッダー・出口ヘッダー以外で連通されたことを特徴とする請求項1記載の高温再生器。The space between the inner shell and the outer shell of each double can body, which is lower than the liquid outlet of the absorbent outlet header, is communicated with other than the absorbent inlet header and outlet header. The high temperature regenerator according to claim 1. 吸収液用出口ヘッダーまたは何れか一つの二重缶体に設けられた吸収液検出手段の出力情報に基づいて、高温再生器に流入する吸収液の量が制御されることを特徴とする請求項1または2記載の高温再生器。The amount of the absorption liquid flowing into the high-temperature regenerator is controlled based on output information of the absorption liquid detection means provided in the absorption liquid outlet header or any one of the double can bodies. The high temperature regenerator according to 1 or 2. 各二重缶体に付設されたバーナの燃焼量が同量に制御されることを特徴とする請求項1〜3何れかに記載の高温再生器。The high-temperature regenerator according to any one of claims 1 to 3, wherein the combustion amount of the burner attached to each double can body is controlled to the same amount.
JP2000054874A 2000-02-29 2000-02-29 High temperature regenerator Expired - Fee Related JP4090178B2 (en)

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