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JP3089534B2 - Absorption chiller / heater - Google Patents
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JP3089534B2 - Absorption chiller / heater - Google Patents

Absorption chiller / heater

Info

Publication number
JP3089534B2
JP3089534B2 JP07067280A JP6728095A JP3089534B2 JP 3089534 B2 JP3089534 B2 JP 3089534B2 JP 07067280 A JP07067280 A JP 07067280A JP 6728095 A JP6728095 A JP 6728095A JP 3089534 B2 JP3089534 B2 JP 3089534B2
Authority
JP
Japan
Prior art keywords
tray
absorber
evaporator
solution
temperature
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 - Lifetime
Application number
JP07067280A
Other languages
Japanese (ja)
Other versions
JPH08261588A (en
Inventor
正治 野牧
雅彦 渥美
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.)
Yazaki Corp
Original Assignee
Yazaki Corp
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 Yazaki Corp filed Critical Yazaki Corp
Priority to JP07067280A priority Critical patent/JP3089534B2/en
Publication of JPH08261588A publication Critical patent/JPH08261588A/en
Application granted granted Critical
Publication of JP3089534B2 publication Critical patent/JP3089534B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • 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

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、上部にトレイを内設し
た蒸発器及び吸収器を備えてなる吸収冷温水機に係り、
特に蒸発器トレイ及び吸収器トレイの水平精度を向上し
冷凍能力を安定するのに好適な吸収冷温水機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller / heater having an evaporator and an absorber having a tray provided therein.
Particularly, the present invention relates to an absorption chiller / heater suitable for improving the horizontal accuracy of the evaporator tray and the absorber tray and stabilizing the refrigerating capacity.

【0002】[0002]

【従来の技術】従来の吸収冷温水機においては、図6に
示すように、高温再生器1で加熱された希溶液を冷媒蒸
気と中間濃溶液とに分離する分離器2と、中間濃溶液を
希溶液と熱交換させて降温する高温溶液熱交換器3と、
降温した中間濃溶液を冷媒蒸気で再度加熱し濃溶液を生
成する低温再生器6と、この濃溶液を希溶液と熱交換さ
せて降温する低温溶液熱交換器4と、冷媒蒸気を液冷媒
に凝縮する凝縮器7と、上部に蒸発器トレイ8aを内設
し蒸発器トレイ8aより液冷媒を滴下して蒸発する蒸発
器8と、上部に吸収器トレイ9aを内設し吸収器トレイ
9aより低温溶液熱交換器4からの濃溶液を滴下し蒸発
器8で蒸発した冷媒蒸気を吸収させて希溶液を生成する
吸収器9と、吸収器9に接続し希溶液を吸入する溶液循
環ポンプ5とを備えてなる構成である。
2. Description of the Related Art In a conventional absorption chiller / heater, as shown in FIG. 6, a separator 2 for separating a dilute solution heated by a high-temperature regenerator 1 into refrigerant vapor and an intermediate concentrated solution, A high-temperature solution heat exchanger 3 for exchanging heat with a dilute solution to lower the temperature;
A low-temperature regenerator 6 that reheats the cooled intermediate concentrated solution with refrigerant vapor to generate a concentrated solution, a low-temperature solution heat exchanger 4 that heat-exchanges the concentrated solution with a dilute solution, and cools the refrigerant vapor to liquid refrigerant. A condenser 7 for condensing, an evaporator 8 in which an evaporator tray 8a is provided in the upper part and a liquid refrigerant is dropped from the evaporator tray 8a to evaporate, and an absorber tray 9a is provided in the upper part and the evaporator tray 9a is provided. An absorber 9 for dropping a concentrated solution from the low-temperature solution heat exchanger 4 and absorbing the refrigerant vapor evaporated in the evaporator 8 to generate a dilute solution, and a solution circulation pump 5 connected to the absorber 9 for sucking the dilute solution This is a configuration including:

【0003】蒸発器8と吸収器9の上部には、液冷媒を
滴下させる蒸発器トレイ8a及び濃溶液を滴下させる吸
収器トレイ9aが取付けられており、これらの蒸発器ト
レイ8a及び吸収器トレイ9aは、上面が開放されたコ
字状の箱型に形成されているとともに、底面に多数の孔
が穿設されていて上面より流入した濃溶液又は液冷媒が
所定の高さに溜められた後、その液柱圧により多数の孔
を経由して蒸発器8又は吸収器9のコイル8b,9bの
上にほぼ均等に滴下し散布させる構造になっている。蒸
発器トレイ8a又は吸収器トレイ9aがほぼ水平に保た
れていない場合は、各トレイ内の液面の高さが不均一に
なり、滴下量が不均一になって冷凍能力に大きく影響す
る。
[0003] Above the evaporator 8 and the absorber 9, an evaporator tray 8a for dropping liquid refrigerant and an absorber tray 9a for dropping a concentrated solution are mounted. These evaporator tray 8a and absorber tray are provided. 9a is formed in a U-shaped box shape with an open upper surface, and has a large number of holes formed in the bottom surface, and a concentrated solution or liquid refrigerant flowing from the upper surface is stored at a predetermined height. Thereafter, the liquid column pressure is applied to the coil 8b of the evaporator 8 or the coil 9b of the absorber 9 through a number of holes so as to be almost uniformly dropped and sprayed. If the evaporator tray 8a or the absorber tray 9a is not kept substantially horizontal, the height of the liquid level in each tray becomes uneven, and the amount of dripping becomes uneven, greatly affecting the refrigerating capacity.

【0004】吸収冷温水機の水平据付けは、底面11a
を基準面として取付けられた水平基準板12を利用して
行われるが、底面11aは、蒸発器トレイ8a及び吸収
器トレイ9aより寸法的に隔てられた間接的な平面であ
って水平面を形成し難いため、水平基準板12の基準面
になり難く蒸発器トレイ8a及び吸収器トレイ9aの水
平度の精度が悪化するため、冷凍能力不足が発生し易
い。
[0004] The horizontal installation of the absorption chiller / heater is performed by the bottom 11a.
The bottom surface 11a is an indirect plane that is dimensionally separated from the evaporator tray 8a and the absorber tray 9a and forms a horizontal plane. Since the evaporator tray 8a and the absorber tray 9a are not easily formed on the reference surface of the horizontal reference plate 12 and the accuracy of the horizontality of the evaporator tray 8a and the absorber tray 9a is deteriorated, the refrigeration capacity is likely to be insufficient.

【0005】[0005]

【発明が解決しようとする課題】従来の吸収冷温水機に
あっては、蒸発器トレイ及び吸収器トレイの水平精度が
悪いため、液冷媒又は濃溶液の滴下量が不均一になって
冷凍能力不足が発生し易い問題点がある。
In the conventional absorption chiller / heater, since the horizontal accuracy of the evaporator tray and the absorber tray is poor, the drop amount of the liquid refrigerant or the concentrated solution becomes non-uniform, so that the refrigerating capacity is reduced. There is a problem that shortage easily occurs.

【0006】本発明の目的は、蒸発器トレイ及び吸収器
トレイの水平精度を向上し、冷凍能力の低下を防止する
ことのできる吸収冷温水機を提供することにある。
An object of the present invention is to provide an absorption chiller / heater capable of improving the horizontal accuracy of an evaporator tray and an absorber tray and preventing a decrease in refrigeration capacity.

【0007】[0007]

【課題を解決するための手段】前記の目的を達成するた
め、本発明に係る吸収冷温水機は、希溶液を加熱する高
温再生器と、希溶液を冷媒蒸気と中間濃溶液とに分離す
る分離器と、中間濃溶液を希溶液と熱交換させて降温す
る高温溶液熱交換器と、降温した中間濃溶液を冷媒蒸気
で再度加熱し濃溶液を得る低温再生器と、この濃溶液を
希溶液と熱交換させて降温する低温溶液熱交換器と、冷
媒蒸気を液冷媒に凝縮する凝縮器と、上部に蒸発器トレ
イを内設し蒸発器トレイより液冷媒を滴下して蒸発する
蒸発器と、上部に吸収器トレイを内設し吸収器トレイよ
り低温溶液熱交換器からの濃溶液を滴下し蒸発器で蒸発
した冷媒蒸気を吸収させて希溶液を生成する吸収器と、
蒸発器トレイ及び吸収器トレイの水平基準面を備えてな
る吸収冷温水機において、蒸発器と吸収器とを共通仕切
を介して一つの容器に収容するとともに、共通仕切より
複数の凸部を容器の底面を貫通して突出させ、水平基準
面を、それぞれの凸部の底辺に形成した構成とする。
In order to achieve the above object, an absorption chiller / heater according to the present invention separates a dilute solution into a refrigerant vapor and an intermediate concentrated solution by heating a dilute solution. A separator, a high-temperature solution heat exchanger that heat-exchanges the intermediate concentrated solution with a dilute solution, lowers the temperature, a low-temperature regenerator that reheats the cooled intermediate concentrated solution with refrigerant vapor to obtain a concentrated solution, and dilutes the concentrated solution. A low-temperature solution heat exchanger that exchanges heat with the solution to lower the temperature, a condenser that condenses the refrigerant vapor into a liquid refrigerant, and an evaporator that has an evaporator tray inside and evaporates by dropping the liquid refrigerant from the evaporator tray An absorber in which an absorber tray is provided in the upper part, a concentrated solution from the low-temperature solution heat exchanger is dropped from the absorber tray, and the refrigerant vapor absorbed by the evaporator is absorbed to generate a dilute solution;
In an absorption chiller / heater provided with a horizontal reference plane of an evaporator tray and an absorber tray, an evaporator and an absorber are housed in one container via a common partition, and a plurality of convex portions are formed in the container by the common partition. And projecting through the bottom surface of the projection, and a horizontal reference plane is formed on the bottom side of each projection.

【0008】そして容器は中空円筒状に形成されるとと
もに、共通仕切は円環状に形成され、それぞれの凸部
は、共通仕切を周方向に複数等分して形成されている構
成でもよい。
The container may be formed in a hollow cylindrical shape, the common partition may be formed in an annular shape, and each projection may be formed by dividing the common partition into a plurality in the circumferential direction.

【0009】[0009]

【作用】本発明によれば、容器内に収容した蒸発器と吸
収器との共通仕切の底辺に設けた複数の突起を水平基準
面とし、この水平基準面で容器の水平を保持した状態で
水平基準板を取付け、この水平基準板と同一レベルに蒸
発器トレイと吸収器トレイとを配設することによって、
蒸発器トレイと吸収器トレイの水平据付け精度が向上さ
れる。
According to the present invention, a plurality of projections provided on the bottom side of the common partition between the evaporator and the absorber housed in the container are used as a horizontal reference plane, and the horizontal reference plane holds the container horizontally. By installing a horizontal reference plate and arranging the evaporator tray and the absorber tray at the same level as this horizontal reference plate,
Horizontal installation accuracy of the evaporator tray and the absorber tray is improved.

【0010】[0010]

【実施例】本発明の一実施例を図1〜図3を参照しなが
ら説明する。図1〜図3に示すように、希溶液を加熱す
る高温再生器1と、希溶液を冷媒蒸気と中間濃溶液とに
分離する分離器2と、中間濃溶液を希溶液と熱交換させ
て降温する高温溶液熱交換器3と、降温した中間濃溶液
を冷媒蒸気で再度加熱し濃溶液を生成する低温再生器6
と、この濃溶液を希溶液と熱交換させて降温する低温溶
液熱交換器4と、冷媒蒸気を液冷媒に凝縮する凝縮器7
と、上部に蒸発器トレイ8aを内設し蒸発器トレイ8a
より液冷媒を滴下して蒸発する蒸発器8と、上部に吸収
器トレイ9aを内設し吸収器トレイ9aより低温溶液熱
交換器4からの濃溶液を滴下し蒸発器8で蒸発した冷媒
蒸気を吸収させて希溶液を生成する吸収器9と、吸収器
9に接続し希溶液を循環する溶液循環ポンプ5とを備え
てなる吸収冷温水機であって、蒸発器8と吸収器9とを
円環状の共通仕切10を介して中空円筒状の一つの容器
11に収容するとともに、共通仕切10より複数の凸部
10aを容器11の底面11aを貫通して突出させ、そ
れぞれの凸部10aの底辺を蒸発器トレイ8a及び吸収
器トレイ9aの水平基準面に形成した構成である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to FIGS. As shown in FIGS. 1 to 3, a high-temperature regenerator 1 for heating a dilute solution, a separator 2 for separating the dilute solution into refrigerant vapor and an intermediate concentrated solution, and a heat exchange between the intermediate concentrated solution and the dilute solution are performed. A high-temperature solution heat exchanger 3 for lowering the temperature, and a low-temperature regenerator 6 for reheating the cooled intermediate concentrated solution with refrigerant vapor to generate a concentrated solution.
And a low-temperature solution heat exchanger 4 for heat-exchanging the concentrated solution with a dilute solution to lower the temperature, and a condenser 7 for condensing refrigerant vapor into liquid refrigerant.
And an evaporator tray 8a is provided inside the evaporator tray 8a.
An evaporator 8 that drip and evaporates a liquid refrigerant, and an absorber tray 9a provided in the upper part, and a refrigerant vapor evaporated by the evaporator 8 by dropping a concentrated solution from the low-temperature solution heat exchanger 4 from the absorber tray 9a. And a solution circulation pump 5 connected to the absorber 9 for circulating the dilute solution. The evaporator 8 and the absorber 9 Is accommodated in one hollow cylindrical container 11 via an annular common partition 10, and a plurality of convex portions 10 a are protruded from the common partition 10 through the bottom surface 11 a of the container 11, and each convex portion 10 a Is formed on the horizontal reference plane of the evaporator tray 8a and the absorber tray 9a.

【0011】蒸発器8と吸収器9の上部には、液冷媒を
滴下させる蒸発器トレイ8a及び濃溶液を滴下させる吸
収器トレイ9aが取付けられており、これらの蒸発器ト
レイ8a及び吸収器トレイ9aは、上面が開放されたコ
字状の箱型断面を有しかつ円環状に形成されているとと
もに、底面に多数の孔が穿設されていて上面より流入し
た液冷媒又は濃溶液が所定の高さに溜められた後、その
液柱圧により多数の孔を経由して蒸発器8又は吸収器9
の円環状のコイル8b,9bの上にほぼ均等に滴下し散
布させるようになっている。そして図4及び図5に示す
ように、半径方向に設けられた複数のトレイ固定板8
c,9cに挿通されて周方向が固定されるとともに、下
面がトレイ固定板8d,9dにより支持されている。ま
たトレイ固定板8d,9dと離間してコイル固定板8
e,9eが配設され、コイル固定板8e,9eには、所
定のピッチでスペーサー8f,9fが上下方向に設けら
れ、上下方向複数列のコイル8b,9bを挟持するよう
になっている。
Above the evaporator 8 and the absorber 9, an evaporator tray 8a for dropping liquid refrigerant and an absorber tray 9a for dropping a concentrated solution are mounted. These evaporator tray 8a and absorber tray are provided. 9a has a U-shaped box-shaped cross section with an open upper surface, is formed in an annular shape, and has a large number of holes formed in the bottom surface. Of the evaporator 8 or absorber 9 through a number of holes due to the liquid column pressure.
Are almost uniformly dropped and sprayed on the annular coils 8b and 9b. As shown in FIGS. 4 and 5, a plurality of tray fixing plates 8 provided in the radial direction are provided.
c and 9c, the circumferential direction is fixed, and the lower surface is supported by tray fixing plates 8d and 9d. Further, the coil fixing plate 8 is separated from the tray fixing plates 8d and 9d.
e, 9e are provided, and spacers 8f, 9f are provided in the coil fixing plates 8e, 9e in a vertical direction at a predetermined pitch so as to sandwich the coils 8b, 9b in plural rows in the vertical direction.

【0012】共通仕切10は、蒸発器8と吸収器9とを
仕切るように容器11とほぼ同心円状に内設してあり、
かつ円周上をほぼ3等分して設けた3個の凸部10aの
底面を水平基準面に加工してある。これらの凸部10a
の底面を水平面上に搭載することにより共通仕切10が
ほぼ垂直に立設される。そしてコイル8b,9bを配列
した後、蒸発器トレイ8a及び吸収器トレイ9aの底面
のレベルに水平基準板12を容器11の側壁に固定す
る。ついで水平基準板12の位置と一致させて蒸発器ト
レイ8a及び吸収器トレイ9aを配設し、トレイ固定板
8c,9cを挿通して固定した後、トレイ固定板8c,
9cの両端を共通仕切10の上端に固着することによ
り、蒸発器トレイ8a及び吸収器トレイ9aがほぼ水平
に保持される。
The common partition 10 is provided substantially concentrically with the container 11 so as to partition the evaporator 8 and the absorber 9 from each other.
In addition, the bottom surfaces of the three convex portions 10a provided by dividing the circumference into approximately three equal parts are machined into a horizontal reference plane. These convex portions 10a
The common partition 10 is erected substantially vertically by mounting the bottom surface of the common partition on a horizontal plane. After arranging the coils 8b and 9b, the horizontal reference plate 12 is fixed to the side wall of the container 11 at the level of the bottom surface of the evaporator tray 8a and the absorber tray 9a. Next, the evaporator tray 8a and the absorber tray 9a are arranged in alignment with the position of the horizontal reference plate 12, and the tray fixing plates 8c, 9c are inserted and fixed.
By fixing both ends of 9c to the upper end of the common partition 10, the evaporator tray 8a and the absorber tray 9a are held substantially horizontally.

【0013】本実施例によれば、蒸発器トレイ及び吸収
器トレイがほぼ水平に保持されるため、蒸発器トレイ及
び吸収器トレイ内に溜められる液冷媒又は濃溶液の液面
がほぼ水平になり、底面の多数の孔までの液柱圧が等し
くなって、どの孔からも液冷媒又は濃溶液がほぼ一様に
滴下するようになり、蒸発器及び吸収器のコイルに一様
に散布される結果、コイル上の液膜厚さがほぼ一様にな
って液膜厚さの不均一又は滴下量の不均一による冷凍能
力の低下が防止され、冷凍能力が安定する。
According to the present embodiment, since the evaporator tray and the absorber tray are held substantially horizontally, the liquid surface of the liquid refrigerant or the concentrated solution stored in the evaporator tray and the absorber tray becomes substantially horizontal. , The liquid column pressures to many holes on the bottom surface are equal, and the liquid refrigerant or the concentrated solution drops almost uniformly from any of the holes, and is evenly distributed to the coils of the evaporator and the absorber. As a result, the liquid film thickness on the coil becomes substantially uniform, and a decrease in the refrigerating capacity due to the non-uniform liquid film thickness or the non-uniform dropping amount is prevented, and the refrigerating capacity is stabilized.

【0014】[0014]

【発明の効果】本発明によれば、蒸発器トレイ及び吸収
器トレイがほぼ水平に保持されるため、液冷媒又は濃溶
液の滴下量の不均一による冷凍能力の低下が防止され、
冷凍能力が安定する効果がある。
According to the present invention, since the evaporator tray and the absorber tray are held substantially horizontally, a decrease in the refrigeration capacity due to the non-uniform dripping amount of the liquid refrigerant or the concentrated solution is prevented,
This has the effect of stabilizing the refrigeration capacity.

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

【図1】本発明の一実施例を示す構成図である。FIG. 1 is a configuration diagram showing one embodiment of the present invention.

【図2】図1の要部を示す断面図である。FIG. 2 is a sectional view showing a main part of FIG.

【図3】図2のA矢視図である。FIG. 3 is a view as viewed from an arrow A in FIG. 2;

【図4】図2のB矢視図である。FIG. 4 is a view taken in the direction of arrow B in FIG. 2;

【図5】図2の斜視図である。FIG. 5 is a perspective view of FIG. 2;

【図6】従来の技術を示す図である。FIG. 6 is a diagram showing a conventional technique.

【符号の説明】[Explanation of symbols]

1 高温再生器 2 分離器 3 高温溶液熱交換器 4 低温溶液熱交換器 5 溶液循環ポンプ 6 低温再生器 7 凝縮器 8 蒸発器 8a 蒸発器トレイ 9 吸収器 9a 吸収器トレイ 10 共通仕切 10a 凸部 11 容器 12 水平基準板 DESCRIPTION OF SYMBOLS 1 High temperature regenerator 2 Separator 3 High temperature solution heat exchanger 4 Low temperature solution heat exchanger 5 Solution circulation pump 6 Low temperature regenerator 7 Condenser 8 Evaporator 8a Evaporator tray 9 Absorber 9a Absorber tray 10 Common partition 10a Convex part 11 container 12 horizontal reference plate

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F25B 15/00 F25B 37/00 F25B 39/02 Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) F25B 15/00 F25B 37/00 F25B 39/02

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 希溶液を加熱する高温再生器と、該希溶
液を冷媒蒸気と中間濃溶液とに分離する分離器と、該中
間濃溶液を前記希溶液と熱交換させて降温する高温溶液
熱交換器と、降温した中間濃溶液を前記冷媒蒸気で再度
加熱し濃溶液を得る低温再生器と、この濃溶液を前記希
溶液と熱交換させて降温する低温溶液熱交換器と、前記
冷媒蒸気を液冷媒に凝縮する凝縮器と、上部に蒸発器ト
レイを内設し該蒸発器トレイより前記液冷媒を滴下して
蒸発する蒸発器と、上部に吸収器トレイを内設し該吸収
器トレイより前記低温溶液熱交換器からの前記濃溶液を
滴下し前記蒸発器で蒸発した冷媒蒸気を吸収させて希溶
液を生成する吸収器と、前記蒸発器トレイ及び前記吸収
器トレイの水平基準面を備えてなる吸収冷温水機におい
て、前記蒸発器と前記吸収器とを共通仕切を介して一つ
の容器に収容するとともに、該共通仕切より複数の凸部
を前記容器の底面を貫通して突出させ、前記水平基準面
を、それぞれの凸部の底辺に形成したことを特徴とする
吸収冷温水機。
1. A high-temperature regenerator for heating a dilute solution, a separator for separating the dilute solution into refrigerant vapor and an intermediate concentrated solution, and a high-temperature solution for lowering the temperature by exchanging the intermediate concentrated solution with the dilute solution. A heat exchanger, a low-temperature regenerator that reheats the cooled intermediate concentrated solution with the refrigerant vapor to obtain a concentrated solution, a low-temperature solution heat exchanger that exchanges heat of the concentrated solution with the dilute solution to lower the temperature, and the refrigerant A condenser for condensing the vapor into a liquid refrigerant, an evaporator tray provided at an upper portion, an evaporator for dropping the liquid refrigerant from the evaporator tray to evaporate, and an absorber at an upper portion provided with an absorber tray. An absorber that drops the concentrated solution from the low-temperature solution heat exchanger from the tray and absorbs the refrigerant vapor evaporated by the evaporator to generate a dilute solution; and a horizontal reference surface of the evaporator tray and the absorber tray. In the absorption chiller-heater comprising: The container and the absorber are accommodated in a single container through a common partition, and a plurality of convex portions penetrate through the bottom surface of the container and protrude from the common partition, and the horizontal reference surface is positioned at the base of each convex portion. An absorption chiller / heater characterized by being formed in.
【請求項2】 容器は中空円筒状に形成されるととも
に、共通仕切は円環状に形成され、それぞれの凸部は、
前記共通仕切を周方向に複数等分して形成されているこ
とを特徴とする請求項1記載の吸収冷温水機。
2. The container is formed in a hollow cylindrical shape, and the common partition is formed in an annular shape.
2. The absorption chiller / heater according to claim 1, wherein the common partition is formed by dividing the common partition into a plurality in the circumferential direction.
JP07067280A 1995-03-27 1995-03-27 Absorption chiller / heater Expired - Lifetime JP3089534B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07067280A JP3089534B2 (en) 1995-03-27 1995-03-27 Absorption chiller / heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07067280A JP3089534B2 (en) 1995-03-27 1995-03-27 Absorption chiller / heater

Publications (2)

Publication Number Publication Date
JPH08261588A JPH08261588A (en) 1996-10-11
JP3089534B2 true JP3089534B2 (en) 2000-09-18

Family

ID=13340410

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07067280A Expired - Lifetime JP3089534B2 (en) 1995-03-27 1995-03-27 Absorption chiller / heater

Country Status (1)

Country Link
JP (1) JP3089534B2 (en)

Also Published As

Publication number Publication date
JPH08261588A (en) 1996-10-11

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