JP3732924B2 - High temperature regenerator - Google Patents

High temperature regenerator Download PDF

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Publication number
JP3732924B2
JP3732924B2 JP19269797A JP19269797A JP3732924B2 JP 3732924 B2 JP3732924 B2 JP 3732924B2 JP 19269797 A JP19269797 A JP 19269797A JP 19269797 A JP19269797 A JP 19269797A JP 3732924 B2 JP3732924 B2 JP 3732924B2
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JP
Japan
Prior art keywords
combustion
heating chamber
temperature regenerator
liquid
exhaust port
Prior art date
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Expired - Fee Related
Application number
JP19269797A
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Japanese (ja)
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JPH1137604A (en
Inventor
伯一 久保田
仁志 鹿沼
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.)
Sanyo Electric Co Ltd
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Sanyo Electric 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
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Priority to JP19269797A priority Critical patent/JP3732924B2/en
Publication of JPH1137604A publication Critical patent/JPH1137604A/en
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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の構造に関する。
【0002】
【従来の技術】
吸収冷凍機(吸収冷温水機などと呼ばれるものを含む)に設けられる従来の高温再生器においては、
▲1▼燃焼・加熱室に立設する液管の本数を減らして製造コストを削減する。
【0003】
▲2▼吸収液の流動制御を容易にする。
【0004】
などの観点から、長い液管を使用していたため、左右方向の寸法より上下方向の寸法の方を大きくなっている。
【0005】
このため、図4に示したように、高温再生器100と共に吸収冷凍機を構成する低温再生器200と凝縮器300を収納した上胴400と、蒸発器500と吸収器600を収納した下胴700の下方に潜り込ませることが困難で、止むなくその側方に配設していたため、設置のための広い床面積が必要であった。
【0006】
【発明が解決しようとする課題】
したがって、吸収冷凍機の設置床面積を削減するために、吸収液の流動を損ねることなく、高温再生器の高さを低く抑えて上胴と下胴の下方に潜り込ませることができるようにする必要があった。
【0007】
【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、少なくとも上下および左右両側方が二重壁構造の炉壁によって囲繞形成された燃焼・加熱室と、この燃焼・加熱室に立設されて二重壁の上部空隙部と下部空隙部とを連通する複数の液管と、前記上部空隙部と前記下部空隙部とを連通する左右両側空隙部と、燃焼・加熱室の前方に液管に臨んで横向きに設置された面状火炎型バーナと、燃焼・加熱室の後方に開設された排気口とを有して構成され、この面状火炎型バーナが生成する火炎と、排気口に向かって流れる燃焼ガスとで、器内に注入した吸収液を加熱濃縮する吸収冷凍機の高温再生器において、燃焼・加熱室は上下方向より左右方向の寸法を大きく形成して高さ方向の寸法を抑え、その左右方向の中央部に面状火炎型バーナを設置し、且つ、前記排気口側に位置する前記左右両側空隙部の上方に吸収液が流下する流入口が開設するようにした第1の構成の高温再生器
を提供するものである。
【0010】
【発明の実施の形態】
以下、本発明になる高温再生器100の一実施形態を、図1および図2に基づいて説明する。
【0011】
1は、上下方向より左右方向の寸法の方が大きく形成された燃焼・加熱室であり、その上下と左右の両側方は二重壁によって囲繞されている。
【0012】
燃焼・加熱室1の前方にはバーナ設置口2が開口し、後方には排気口3が開口している。なお、バーナ設置口2は、燃焼・加熱室1の左右方向の中央部に開口し、バーナ設置口2にそれ自体は従来周知の面状火炎型バーナ4が、燃焼面が横向きになるように設置されている。
【0013】
また、燃焼・加熱室1には多数の液管5が立設されて、二重壁の上部空隙6と下部空隙7とを連通し、二重壁の上部空隙6・下部空隙7・右側部空隙8・左側部空隙9などに注入した吸収液が加熱時に対流できるようになっている。
【0014】
そして、上部空隙6は、その左右方向の中央部分が上方に拡大形成されて、液ヘッダー10を形成し、この液ヘッダー10の排気口3側上部に蒸気流出口11が開口し、排気口3側中段部に吸収液流出口12が開口し、液ヘッダー10となっていない両側の上部空隙6部分に吸収液流入口13が開口している。
【0015】
したがって、吸収液流入口13から吸収液をポンプ圧を利用して注入し、面状火炎型バーナ4に点火すると、面状火炎型バーナ4の表面に面状の火炎が形成され、生成した高温の燃焼ガスは燃焼・加熱室1を通って排気口3から排出される際に、液管5の管壁と、上部空隙6・下部空隙7・右側部空隙8・左側部空隙9それぞれにおいても内壁を介して加熱されるが、温度分布を比較すると、面状火炎型バーナ4側と排気口3側では火炎を形成して燃焼している面状火炎型バーナ4側が高くて排気口3側が低く、中央部と側壁部側の左右方向では火炎を形成して燃焼している面状火炎型バーナ4側が高くて側壁側が低いので、矢印で示したように、排気口3側から面状火炎型バーナ4側に、側壁部側から中央部側にと吸収液は対流するので、温度が上昇した吸収液だけが液ヘッダー10に入り、そこに開口している吸収液流出口12から排出される。
【0016】
特に、火炎が直接当たったり、火炎の輻射熱を受けることになる面状火炎型バーナ4の前方に位置する液管5では最大の加熱作用が生じ、これら液管5の内部では吸収液が沸騰し、生成する気泡のポンプ作用が加わると共に、液ヘッダー10が上方に延設されているので、この部分に向かう強い上昇流が発生し、これに伴って吸収液流入口12から注入された温度の低い吸収液は、主にその近傍の右側部空隙8・左側部空隙9を沈降して全体の対流を促進するので、高温再生器100全体でも腐食性の吸収液が部分的に滞留したり、偏流することがなくなり、壁面の腐食が抑制される。
【0017】
そして、左右方向の中央寄りで面状火炎型バーナ4側に立設された液管5内において沸騰する吸収液から蒸発分離された冷媒の蒸気は、液ヘッダー10の上部側に溜り、上方に開口した蒸気流出口11から排出される。
【0018】
なお、液管5は、バーナ設置口2の側に密に立設される第1の液管群5Aと、排気口3の側に粗に立設される第2の液管群5Bとに分けて立設され、第1の液管群5Aと第2の液管群5Bとの間には液管5が立設されないて燃焼促進空間14が設けられている。
【0019】
このため、面状火炎型バーナ4が生成する火炎と燃焼ガスは、第1の液管群5Aにおいて吸収液に速やかに放熱して温度が下がるため、高温燃焼時に増加すると云われるNOxの生成量が顕著に減少し、その後は燃焼促進空間14においてさらなる温度低下を抑制して燃焼を促進し、低温燃焼時に増加すると云われるCOの発生を抑えたのち、第2の液管群5Bに放熱して排気される。
【0020】
上記構成の高温再生器100は、高さが低いため、例えば図3に示したように低温再生器200と凝縮器300を収納した上胴400と、蒸発器500と吸収器600を収納した下胴700の下方に潜り込ませることが可能であり、所要床面積が小さくなるので、設置場所を選定する際の自由度が増える。
【0021】
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。
【0022】
例えば、液管群を5A、5Bと分離配設することなく、連続配設した高温再生器とす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、本発明の高温再生器によれば、高さを抑えても吸収液の強い対流が起こって局部的に滞留すると云ったことがない。したがって、低温再生器と凝縮器を収納した上胴と、蒸発器と吸収器を収納した下胴の下方に潜り込ませることが可能であり、吸収冷凍機の所要床面積が小さくなるので、設置場所を選定する際の自由度が増えると云った特長がある。
【図面の簡単な説明】
【図1】 正面から見た一実施形態の説明図である。
【図2】 側方から見た一実施形態の説明図である。
【図3】 本発明の高温再生器を用いて構成した吸収冷凍機の説明図で、(A)は正面から見た図、(B)は上方から見た図、(C)は側方から見た図である。
【図4】 従来技術の高温再生器を用いて構成した吸収冷凍機の説明図で、(A)は正面から見た図、(B)は上方から見た図、(C)は側方から見た図である。
【符号の説明】
1 燃焼・加熱室
2 バーナ設置口
3 排気口
4 面状火炎型バーナ
5 液管
5A 第1液管群
5B 第2液管群
6 上部空隙
7 下部空隙
8 右側部空隙
9 左側部空隙
10 液ヘッダー
11 蒸気流出口
12 吸収液流出口
13 吸収液流入口
14 燃焼促進空間
100 高温再生器
200 低温再生器
300 凝縮器
400 上胴
500 蒸発器
600 吸収器
700 下胴
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to the structure of a high-temperature regenerator of an absorption refrigerator.
[0002]
[Prior art]
In conventional high-temperature regenerators installed in absorption refrigerators (including those called absorption cold / hot water machines)
(1) Reduce the production cost by reducing the number of liquid pipes installed in the combustion / heating chamber.
[0003]
(2) Facilitates the flow control of the absorbent.
[0004]
In view of the above, since a long liquid pipe is used, the dimension in the vertical direction is larger than the dimension in the horizontal direction.
[0005]
Therefore, as shown in FIG. 4, the upper cylinder 400 that houses the low-temperature regenerator 200 and the condenser 300 that constitute the absorption refrigerator together with the high-temperature regenerator 100, and the lower cylinder that houses the evaporator 500 and the absorber 600. Since it was difficult to sneak under 700, and it was disposed on the side of it, a large floor area was required for installation.
[0006]
[Problems to be solved by the invention]
Therefore, in order to reduce the installation floor area of the absorption refrigerator, the height of the high-temperature regenerator can be kept low without being lost in the flow of the absorption liquid and can be buried under the upper and lower bodies. There was a need.
[0007]
[Means for Solving the Problems]
In order to solve the above-described problems, the present invention provides a combustion / heating chamber that is surrounded by a furnace wall having a double wall structure at least on the upper and lower sides and the left and right sides, and an upper portion of the double wall that is erected in the combustion / heating chamber. A plurality of liquid pipes communicating with the gap and the lower gap, left and right side gaps communicating with the upper gap and the lower gap , and installed sideways facing the liquid pipe in front of the combustion / heating chamber. A planar flame type burner, and an exhaust port opened behind the combustion / heating chamber, the flame generated by the planar flame type burner, and the combustion gas flowing toward the exhaust port, In the high-temperature regenerator of an absorption refrigerator that heats and concentrates the absorption liquid injected into the chamber, the combustion / heating chamber is formed to have a larger dimension in the left-right direction than in the vertical direction, thereby suppressing the height dimension. planar-flame burner is placed in the center of, and, the exhaust The first configuration of the high-temperature regenerator inlet for upwardly absorbing liquid of said right and left side gap portion flows down positioned on the mouth side was made to establish
Is to provide.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the high-temperature regenerator 100 according to the present invention will be described with reference to FIGS. 1 and 2.
[0011]
Reference numeral 1 denotes a combustion / heating chamber having a dimension in the left-right direction larger than that in the up-down direction, and the upper and lower sides and the left and right sides are surrounded by double walls.
[0012]
A burner installation port 2 is opened in front of the combustion / heating chamber 1, and an exhaust port 3 is opened in the rear. The burner installation port 2 is opened at the center in the left-right direction of the combustion / heating chamber 1, and the burner installation port 2 itself has a well-known planar flame type burner 4 so that the combustion surface faces sideways. is set up.
[0013]
In addition, a large number of liquid pipes 5 are erected in the combustion / heating chamber 1 to connect the upper cavity 6 and the lower cavity 7 of the double wall to the upper cavity 6, the lower cavity 7, and the right side of the double wall. The absorbing liquid injected into the gap 8 and the left side gap 9 can be convected during heating.
[0014]
The upper gap 6 is formed such that a central portion in the left-right direction is enlarged upward to form a liquid header 10. A vapor outlet 11 is opened on the upper side of the liquid header 10 on the exhaust port 3 side. The absorbing liquid outlet 12 is opened in the middle side portion of the side, and the absorbing liquid inlet 13 is opened in the upper gap 6 portions on both sides which are not the liquid header 10.
[0015]
Accordingly, when the absorbing liquid is injected from the absorbing liquid inlet 13 using the pump pressure and the planar flame type burner 4 is ignited, a planar flame is formed on the surface of the planar flame type burner 4 and the generated high temperature is generated. When the combustion gas is discharged from the exhaust port 3 through the combustion / heating chamber 1, the liquid pipe 5, the upper gap 6, the lower gap 7, the right side gap 8, and the left side gap 9, respectively. Although heated through the inner wall, when comparing the temperature distribution, the planar flame burner 4 side that burns by forming a flame on the planar flame burner 4 side and the exhaust port 3 side is high and the exhaust port 3 side is heated. Since the sheet flame type burner 4 side that is burning and forming a flame is high in the left and right direction at the center and the side wall side, the side flame side is high and the side wall side is low. Since the absorbent convects from the side wall portion side to the central portion side on the mold burner 4 side, Only absorbent degrees rises enters the liquid header 10, which is discharged from the absorption liquid flow outlet 12 which opens into.
[0016]
In particular, the maximum heating action occurs in the liquid pipes 5 positioned in front of the planar flame type burner 4 that directly hits the flame or receives the radiant heat of the flame, and the absorbing liquid boils inside these liquid pipes 5. In addition to the pumping action of the generated bubbles, the liquid header 10 is extended upward, so that a strong upward flow toward this portion is generated, and the temperature of the liquid injected from the absorbing liquid inlet 12 is accordingly increased. Since the low absorption liquid mainly sinks the right side gap 8 and the left side gap 9 in the vicinity thereof to promote the entire convection, the corrosive absorption liquid partially stays in the high temperature regenerator 100 as a whole. The drift does not occur and corrosion of the wall surface is suppressed.
[0017]
The refrigerant vapor evaporated and separated from the absorbing liquid boiling in the liquid pipe 5 erected on the planar flame type burner 4 side near the center in the left-right direction is accumulated on the upper side of the liquid header 10 and is It is discharged from the open steam outlet 11.
[0018]
The liquid pipe 5 is divided into a first liquid pipe group 5A that is densely installed on the burner installation port 2 side and a second liquid pipe group 5B that is roughly installed on the exhaust port 3 side. A combustion promoting space 14 is provided between the first liquid pipe group 5A and the second liquid pipe group 5B so that the liquid pipe 5 is not erected.
[0019]
For this reason, the flame and combustion gas generated by the planar flame type burner 4 quickly dissipate heat to the absorbing liquid in the first liquid tube group 5A and the temperature drops, so that the amount of NOx generated that is said to increase during high-temperature combustion After that, in the combustion promoting space 14, the temperature is further suppressed in the combustion promoting space 14 to suppress the generation of CO, which is said to increase during the low temperature combustion, and then is radiated to the second liquid pipe group 5 </ b> B. Exhausted.
[0020]
Since the high temperature regenerator 100 having the above configuration is low in height, for example, as shown in FIG. 3, the upper body 400 containing the low temperature regenerator 200 and the condenser 300, and the lower part containing the evaporator 500 and the absorber 600. It is possible to sink under the trunk 700, and the required floor area is reduced, so that the degree of freedom in selecting the installation location is increased.
[0021]
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.
[0022]
For example, a high-temperature regenerator that is continuously arranged without separating the liquid tube group from 5A and 5B can be used.
[0023]
【The invention's effect】
As described above, according to the high-temperature regenerator of the present invention, even if the height is suppressed, strong convection of the absorbing liquid has occurred and it has never been said that it is locally retained. Therefore, it is possible to sink under the upper cylinder containing the low-temperature regenerator and the condenser and the lower cylinder containing the evaporator and the absorber, and the floor area required for the absorption refrigerator is reduced. There is a feature that the degree of freedom in selecting is increased.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram of an embodiment as viewed from the front.
FIG. 2 is an explanatory diagram of an embodiment as viewed from the side.
FIG. 3 is an explanatory view of an absorption refrigerator constructed using the high-temperature regenerator of the present invention, where (A) is a view from the front, (B) is a view from above, and (C) is from the side. FIG.
FIG. 4 is an explanatory view of an absorption refrigerator constructed using a high-temperature regenerator of the prior art, (A) is a view from the front, (B) is a view from above, and (C) is from the side. FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Combustion / heating chamber 2 Burner installation port 3 Exhaust port 4 Plane flame type burner 5 Liquid pipe 5A 1st liquid pipe group 5B 2nd liquid pipe group 6 Upper space | gap 7 Lower space | gap 8 Right side space | gap 9 Left side space | gap 10 Liquid header 11 Steam outlet 12 Absorbing liquid outlet 13 Absorbing liquid inlet 14 Combustion promoting space 100 High temperature regenerator 200 Low temperature regenerator 300 Condenser 400 Upper body 500 Evaporator 600 Absorber 700 Lower body

Claims (1)

少なくとも上下および左右両側方が二重壁構造の炉壁によって囲繞形成された燃焼・加熱室と、この燃焼加熱室に立設されて二重壁の上部空隙部と下部空隙部とを連通する複数の液管と、前記上部空隙部と前記下部空隙部とを連通する左右両側空隙部と、燃焼・加熱室の前方に液管に臨んで横向きに配置された面状火炎型バーナと、燃焼・加熱室の後方に開設された排気口とを有して構成され、この面状火炎型バーナが形成する火炎と、排気口に向かって流れる燃焼ガスとで、器内に注入した吸収液を加熱濃縮する吸収冷凍機の高温再生器において、
燃焼・加熱室は上下方向より左右方向の寸法を大きく形成して高さ方向の寸法を抑え、その左右方向の中央部に面状火炎型バーナを配置し、且つ、前記排気口側に位置する上部外壁の前記左右両側空隙部の上方に吸収液が流下する流入口が開設されたことを特徴とする高温再生器。
A combustion / heating chamber that is surrounded by a furnace wall having a double wall structure at least on the top and bottom and on both the left and right sides, and a plurality of pipes that are erected in the combustion heating chamber and communicate with the upper gap portion and the lower gap portion of the double wall Liquid pipe, left and right side gaps communicating with the upper gap and the lower gap, a planar flame type burner disposed sideways facing the liquid pipe in front of the combustion / heating chamber, It has an exhaust port opened at the rear of the heating chamber, and heats the absorption liquid injected into the chamber with the flame formed by this planar flame burner and the combustion gas flowing toward the exhaust port In the high-temperature regenerator of the absorption refrigerator to be concentrated,
The combustion / heating chamber is formed larger in the left-right direction than in the vertical direction to suppress the height dimension , and a planar flame burner is disposed at the center in the left-right direction, and is located on the exhaust port side. A high-temperature regenerator characterized in that an inlet through which the absorbent flows down is formed above the left and right gaps on the upper outer wall .
JP19269797A 1997-07-17 1997-07-17 High temperature regenerator Expired - Fee Related JP3732924B2 (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19269797A JP3732924B2 (en) 1997-07-17 1997-07-17 High temperature regenerator

Publications (2)

Publication Number Publication Date
JPH1137604A JPH1137604A (en) 1999-02-12
JP3732924B2 true JP3732924B2 (en) 2006-01-11

Family

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