JPH07117318B2 - Vertical high-temperature regenerator for gas absorption chiller / heater - Google Patents

Vertical high-temperature regenerator for gas absorption chiller / heater

Info

Publication number
JPH07117318B2
JPH07117318B2 JP17327189A JP17327189A JPH07117318B2 JP H07117318 B2 JPH07117318 B2 JP H07117318B2 JP 17327189 A JP17327189 A JP 17327189A JP 17327189 A JP17327189 A JP 17327189A JP H07117318 B2 JPH07117318 B2 JP H07117318B2
Authority
JP
Japan
Prior art keywords
heater
liquid
liquid pipe
temperature regenerator
gas absorption
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
JP17327189A
Other languages
Japanese (ja)
Other versions
JPH0339873A (en
Inventor
茂吉 黒沢
茂 中村
努 小津
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.)
Tokyo Gas Co Ltd
Original Assignee
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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP17327189A priority Critical patent/JPH07117318B2/en
Publication of JPH0339873A publication Critical patent/JPH0339873A/en
Publication of JPH07117318B2 publication Critical patent/JPH07117318B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はガス吸収冷温水機用縦型高温再生装置に関する
ものである。
TECHNICAL FIELD The present invention relates to a vertical high temperature regenerator for a gas absorption chiller / heater.

(従来技術と問題点) 従来のガス吸収冷温水機の高温再生装置は、第1図に示
す通り、炉筒部と煙管部を、別々に有した炉筒煙管型の
装置が通常使用されていた。かかる装置は、ブラストバ
ーナによる燃焼ガスを臭化リチウム稀溶液溜内の煙管部
に流すことによって熱交換し、臭化リチウム溶液を沸騰
させ、濃溶液と冷媒蒸気を発生させる装置である。かか
る従来装置は、横長であるため設置スペースが大きく、
占有容積も大きいことに加え、溶液保有量が多く、負荷
応答性が遅い。また横長型のため、炎長の長いブラスト
バーナを使用しなければならず、かかるバーナは騒音値
が高く、定期点検が必要でコスト高の欠点である。更
に、炉筒部と煙管部、即ち燃焼室と熱交換部が別個に構
成されているので、従来装置を前提としたコンパクト化
の改良は困難であった。本発明者等は、試行錯誤を繰り
返しながら、従来装置の改良には難点があることを知
り、全く別の角度から発想して本発明に到達したもので
ある。
(Prior Art and Problems) As a conventional high-temperature regenerator for a gas absorption chiller-heater, as shown in FIG. 1, a furnace tube smoke tube type apparatus having a furnace tube section and a smoke tube section separately is usually used. It was Such an apparatus is an apparatus for causing heat exchange by flowing combustion gas from a blast burner to a smoke pipe section in a lithium bromide dilute solution reservoir to boil the lithium bromide solution to generate a concentrated solution and a refrigerant vapor. Since such a conventional device is horizontally long, the installation space is large,
In addition to occupying a large volume, it also has a large amount of solution and has a slow load response. Further, since it is a horizontally long type, it is necessary to use a blast burner having a long flame length, and such a burner has a high noise value, requires periodic inspections, and is a disadvantage of high cost. Further, since the furnace tube portion and the smoke tube portion, that is, the combustion chamber and the heat exchange portion are separately configured, it is difficult to improve the compactness of the conventional apparatus. While repeating trial and error, the inventors of the present invention have found that there is a difficulty in improving the conventional device, and arrived at the present invention by thinking from a completely different angle.

(発明の構成) 第2図及び第3図に於いて、符号1は被加熱液壁2で構
成した筒状体であって、この筒状体1は上端に排気口3
を有し、且つその内部には、前記被加熱液壁2と連通す
る液管4を、縦方向に斜目に交差するように配置すると
共に、前記液管4にはフィン5を取着け、前記筒状体1
下端にはバーナ6を設置した構成である。第2項記載の
ものは、第1項記載の液管4は、液管上部位置に於いて
斜目交差するように構成したものである。
(Structure of the Invention) In FIGS. 2 and 3, reference numeral 1 is a tubular body constituted by a heated liquid wall 2, and the tubular body 1 has an exhaust port 3 at its upper end.
And a liquid pipe 4 communicating with the heated liquid wall 2 is disposed inside the liquid pipe 4 so as to intersect the slant in the longitudinal direction, and fins 5 are attached to the liquid pipe 4. The tubular body 1
A burner 6 is installed at the lower end. According to the second aspect, the liquid pipe 4 according to the first aspect is configured such that the liquid pipe 4 crosses obliquely at the upper position of the liquid pipe.

(作用) バーナ6に於いて燃焼が開始すると、燃焼ガスは、被加
熱液壁2と液管4を加熱しつつ上昇する。
(Operation) When combustion starts in the burner 6, the combustion gas rises while heating the heated liquid wall 2 and the liquid pipe 4.

かかる際、液管4は縦方向に斜目に交差させて配管して
あるので、その熱交換は直交型となり、加熱効率が格段
に向上する。即ち、液管4は前記した通り、縦方向に斜
目に交差させて配管してあるので、伝熱面積が大きくな
る上、上昇する燃焼ガスはその液管によって乱流状態が
形成され、加熱効率を飛躍的に向上させる。かかる液管
はその上部位置に於いて斜目交差させると、下部位置の
空間に於いて、燃焼ガスが急冷されず、その結果、完全
燃焼状態で、前記した通りの熱交換を行なうことができ
る利点がある。加えて、液管4を斜目に構成してあるの
で、管内気ほうが管内から容易にぬける利点もある。
At this time, since the liquid pipe 4 is piped so as to cross the slant in the vertical direction, the heat exchange becomes orthogonal and the heating efficiency is remarkably improved. That is, as described above, since the liquid pipe 4 is arranged so as to intersect the slant in the vertical direction in the vertical direction, the heat transfer area is increased, and the rising combustion gas is turbulently formed by the liquid pipe to heat the combustion gas. Greatly improve efficiency. When such a liquid pipe is crossed obliquely at the upper position, the combustion gas is not rapidly cooled in the space at the lower position, and as a result, the heat exchange as described above can be performed in the complete combustion state. There are advantages. In addition, since the liquid pipe 4 is formed in a slanted shape, there is an advantage that the air inside the pipe can be easily removed from the inside of the pipe.

このように、燃焼室と熱交換部が一体化した構成である
上、前記した通り、加熱効率が向上するので、一層のコ
ンパクト化が達成できる。実際に、従来装置と比較し
て、設置面積に於いて、7割〜8割、占有容積に於い
て、2割〜3割の大きさで構成することができた。ま
た、装置自体を縦型とすることにより、通常使用されて
いる短炎バーナを使用することができ、維持管理が容易
であると共に極端な低騒音化が達成できる。また、縦長
構成により設置面積の低減化が実現できる。
As described above, since the combustion chamber and the heat exchange section are integrated with each other and the heating efficiency is improved as described above, further compactness can be achieved. In fact, compared with the conventional device, the size of the installation area was 70 to 80%, and the occupied volume was 20 to 30%. Further, by making the apparatus itself vertical, it is possible to use a short-flame burner that is normally used, and it is possible to easily maintain and manage and to achieve extremely low noise. Further, the vertically long structure can reduce the installation area.

(発明の効果) 本発明は以上の通り、再生装置を独特の構成にすること
によって、コンパクト化を図ることができると同時に、
騒音が少なく、維持管理をほとんど不要として、低コス
トの再生装置を提供することができる外、設置面積を低
減できる一大利点を有するものである。
(Effects of the Invention) As described above, according to the present invention, by making the playback device have a unique configuration, it is possible to achieve compactness and at the same time,
In addition to providing a low-cost reproducing device with little noise and requiring almost no maintenance, it has a great advantage that the installation area can be reduced.

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

第1図(A),(B)は従来装置の説明図、第2図は本
発明装置の斜視的説明図、第3図は同縦断的説明図であ
る。 符号1……筒状体、2……被加熱液壁、3……排気口、
4……液管、5……フィン、6……バーナ、7……液導
入口。
1 (A) and 1 (B) are explanatory views of a conventional device, FIG. 2 is a perspective explanatory view of the device of the present invention, and FIG. 3 is a longitudinal explanatory view thereof. Reference numeral 1 ... Cylindrical body, 2 ... Liquid wall to be heated, 3 ... Exhaust port,
4 ... Liquid pipe, 5 ... Fin, 6 ... Burner, 7 ... Liquid inlet.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】被加熱液壁で構成し、上部に排気口を設け
た筒状体内に、前記被加熱液壁と連通する液管を、縦方
向に斜目交差するように配管すると共に、前記管液には
フィンを取着け、前記筒状体下部にはバーナを設置した
ガス吸収冷温水機用縦型高温再生装置。
1. A liquid pipe communicating with the liquid wall to be heated is arranged in a cylindrical body having a liquid wall to be heated and provided with an exhaust port at an upper part thereof, so that the liquid pipe is crossed at a slant in the vertical direction. A vertical high-temperature regenerator for a gas absorption chiller-heater, in which fins are attached to the pipe liquid and a burner is installed in the lower portion of the tubular body.
【請求項2】第1項記載の液管は、液管に上部位置に於
いて斜目交差するように構成したガス吸収冷温水機用縦
型高温再生装置
2. A vertical high-temperature regenerator for a gas absorption chiller / heater, wherein the liquid pipe according to claim 1 is constructed so as to cross the liquid pipe at an oblique position at an upper position.
JP17327189A 1989-07-05 1989-07-05 Vertical high-temperature regenerator for gas absorption chiller / heater Expired - Fee Related JPH07117318B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17327189A JPH07117318B2 (en) 1989-07-05 1989-07-05 Vertical high-temperature regenerator for gas absorption chiller / heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17327189A JPH07117318B2 (en) 1989-07-05 1989-07-05 Vertical high-temperature regenerator for gas absorption chiller / heater

Publications (2)

Publication Number Publication Date
JPH0339873A JPH0339873A (en) 1991-02-20
JPH07117318B2 true JPH07117318B2 (en) 1995-12-18

Family

ID=15957357

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17327189A Expired - Fee Related JPH07117318B2 (en) 1989-07-05 1989-07-05 Vertical high-temperature regenerator for gas absorption chiller / heater

Country Status (1)

Country Link
JP (1) JPH07117318B2 (en)

Also Published As

Publication number Publication date
JPH0339873A (en) 1991-02-20

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