JP3089533B2 - Absorption chiller / heater - Google Patents
Absorption chiller / heaterInfo
- Publication number
- JP3089533B2 JP3089533B2 JP07067279A JP6727995A JP3089533B2 JP 3089533 B2 JP3089533 B2 JP 3089533B2 JP 07067279 A JP07067279 A JP 07067279A JP 6727995 A JP6727995 A JP 6727995A JP 3089533 B2 JP3089533 B2 JP 3089533B2
- Authority
- JP
- Japan
- Prior art keywords
- tray
- evaporator
- absorber
- 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 - Fee Related
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 8
- 239000006096 absorbing agent Substances 0.000 claims description 61
- 239000003507 refrigerant Substances 0.000 claims description 34
- 239000007788 liquid Substances 0.000 claims description 28
- 238000005192 partition Methods 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000001704 evaporation Methods 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 238000003466 welding Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、上部にトレイを内設し
た吸収器及び蒸発器を備えてなる吸収冷温水機に係り、
特に吸収器トレイ及び蒸発器トレイの水平を保持して固
定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 provided with an absorber and an evaporator having a tray installed in the upper part thereof.
In particular, the present invention relates to an absorption chiller / heater suitable for stabilizing the refrigerating capacity by holding and fixing the horizontal level of the absorber tray and the evaporator tray.
【0002】[0002]
【従来の技術】従来の吸収冷温水機においては、図8〜
図12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
度加熱し濃溶液を得る低温再生器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とを備えてなる構成であっ
て、蒸発器8と吸収器9とを共通仕切10を介して一つ
の容器11に収容し、蒸発器トレイ8a及び吸収器トレ
イ9aをほぼ水平に支持する固定板8i,9iを設け、
それぞれの固定板8i,9iの一端を共通仕切10に溶
接w等で係合するとともに、それぞれの固定板8i,9
iの上部を蒸発器トレイ8a及び吸収器トレイ9aのト
レイ固定板8h,9hに溶接w等で係合している。2. Description of the Related Art In a conventional absorption chiller / heater, FIGS.
As shown in FIG. 12, a high-temperature regenerator 1 for heating a dilute solution
A separator 2 that separates the dilute solution into a refrigerant vapor and an intermediate concentrated solution, a high-temperature solution heat exchanger 3 that exchanges heat between the intermediate concentrated solution and the dilute solution and lowers the temperature, A low-temperature regenerator 6 for heating again to obtain a concentrated solution, a low-temperature solution heat exchanger 4 for exchanging heat of the concentrated solution with a dilute solution, and a condenser 7 for condensing refrigerant vapor into a liquid refrigerant; Evaporator 8 which has a built-in tray 8a and evaporates by dropping liquid refrigerant from the evaporator tray 8a, and a concentrated solution from the low-temperature solution heat exchanger 4 which has an absorber tray 9a provided above and which has an absorber tray 9a. And a solution circulation pump 5 connected to the absorber 9 to circulate the dilute solution, comprising: an absorber 9 for absorbing the refrigerant vapor evaporated by the evaporator 8 to generate a dilute solution; The evaporator 8 and the absorber 9 are housed in one container 11 via a common partition 10. Evaporator tray 8a and the fixed plate 8i which substantially horizontally supports the absorber tray 9a, provided 9i,
One end of each fixed plate 8i, 9i is engaged with the common partition 10 by welding w or the like, and each fixed plate 8i, 9i is engaged.
The upper part of i is engaged with the tray fixing plates 8h, 9h of the evaporator tray 8a and the absorber tray 9a by welding w or the like.
【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ようになっている。蒸
発器トレイ8a及び吸収器トレイ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 causes the droplets to be almost uniformly dropped and sprayed onto the coils 8b, 9b of the evaporator 8 or the absorber 9 via a large number of holes. If the evaporator tray 8a and the absorber tray 9a are not kept substantially horizontal, the height of the liquid level in each tray will be uneven, and the dripping amounts will be uneven, greatly affecting the refrigerating capacity.
【0004】蒸発器トレイ8a及び吸収器トレイ9aの
一端は、共通仕切10に固定されかつ下端が固定板8
i,9iに固定されていて吸収器8及び蒸発器9のセル
空間に浮いた状態になっているため、蒸発器トレイ8a
及び吸収器トレイ9aの他端はコイル8b,9bの自重
により若干、下側へ落ち込む状態になり、蒸発器トレイ
8a及び吸収器トレイ9aも同様にして下がってしまう
ため水平度が変化し、蒸発器トレイ8a及び吸収器トレ
イ9a内の液面の高さが不均一になり、滴下量が不均一
になって冷凍能力が不安定となる。[0004] One end of the evaporator tray 8a and one end of the absorber tray 9a are fixed to the common partition 10 and the lower end is fixed to the fixing plate 8.
i, 9i and floating in the cell space of the absorber 8 and the evaporator 9, the evaporator tray 8a
Also, the other end of the absorber tray 9a is slightly lowered due to the weight of the coils 8b, 9b, and the evaporator tray 8a and the absorber tray 9a are similarly lowered, so that the horizontality is changed and the evaporation is changed. The heights of the liquid levels in the container tray 8a and the absorber tray 9a become uneven, the dripping amounts become uneven, and the refrigerating capacity becomes unstable.
【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
コイルの自重により低下し、濃溶液又は液冷媒の滴下量
が不均一になって冷凍能力が不安定となる問題点があ
る。In the conventional absorption chiller / heater, the horizontal accuracy of the evaporator tray and the absorber tray is reduced by the weight of the coil, and the amount of dripping of the concentrated solution or liquid refrigerant becomes uneven. As a result, the refrigeration capacity becomes unstable.
【0006】本発明の目的は、蒸発器トレイ及び吸収器
トレイの水平精度の低下を防止し、冷凍能力を安定する
ことのできる吸収冷温水機を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide an absorption chiller / heater capable of preventing a decrease in horizontal accuracy of an evaporator tray and an absorber tray and stabilizing a refrigerating 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、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し、蒸発器トレイ及び吸
収器トレイの少なくともいずれか一方をほぼ水平に保持
するトレイ固定板を設け、それぞれのトレイ固定板の一
端を共通仕切に固着するとともに、それぞれのトレイ固
定板を蒸発器コイル及び吸収器コイルの少なくともいず
れか一方のコイル固定板より離間して配置した構成とす
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, A low-temperature solution heat exchanger that exchanges heat with a low-temperature solution heat exchanger, a condenser that condenses the refrigerant vapor into a liquid refrigerant, an evaporator that has an evaporator tray installed in the upper part, and a liquid refrigerant is dropped from the evaporator tray and evaporated. , An absorber tray is provided in the upper part, and a concentrated solution from the low-temperature solution heat exchanger is dropped from the absorber tray, and an absorber that absorbs the refrigerant vapor evaporated by the evaporator to generate a dilute solution is provided. In a chiller / heater, one evaporator and one absorber are connected via a common partition. A tray fixing plate housed in a container and holding at least one of the evaporator tray and the absorber tray substantially horizontally is provided, and one end of each tray fixing plate is fixed to a common partition, and each tray fixing plate is fixed. At least one of the evaporator coil and the absorber coil is separated from the coil fixing plate.
【0008】[0008]
【作用】本発明によれば、蒸発器トレイ及び吸収器トレ
イのトレイ固定板を、コイル固定板より分離して容器の
共通仕切で支持し、蒸発器コイル又は吸収器コイルの自
重量がかからないようにしたため、吸収器トレイ及び蒸
発器トレイの水平精度が向上され、蒸発器トレイ及び吸
収器トレイ内の液面の高さが均一になり、液冷媒又は濃
溶液の蒸発器又は吸収器への滴下量が均一になって冷凍
能力が安定する。According to the present invention, the tray fixing plates of the evaporator tray and the absorber tray are separated from the coil fixing plate and supported by the common partition of the container so that the weight of the evaporator coil or the absorber coil is not applied. As a result, the horizontal accuracy of the absorber tray and the evaporator tray is improved, the liquid level in the evaporator tray and the absorber tray becomes uniform, and the liquid refrigerant or the concentrated solution is dropped onto the evaporator or the absorber. The amount becomes uniform and the refrigerating capacity becomes stable.
【0009】[0009]
【実施例】本発明の一実施例を図1〜図5を参照しなが
ら説明する。図1〜図5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得る低温再生器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
る吸収冷温水機であって、蒸発器8と吸収器9とを共通
仕切10を介して一つの容器11に収容し、蒸発器トレ
イ8a及び吸収器トレイ9aの少なくともいずれか一方
をほぼ水平に保持するトレイ固定板8d,9dを設け、
それぞれのトレイ固定板8d,9dの少なくともいずれ
か一方の一端を共通仕切10に溶接w等で固着するとと
もに、それぞれのトレイ固定板を蒸発器コイル8b及び
吸収器コイル9bの少なくともいずれか一方のコイル固
定板8e,9eより離間して配置した構成とする。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 5, a high-temperature regenerator 1 for heating a dilute solution, a separator 2 for separating the dilute solution into a refrigerant vapor and an intermediate concentrated solution, and heat exchange of the intermediate concentrated solution with the dilute solution A high-temperature solution heat exchanger 3 for lowering the temperature, a low-temperature regenerator 6 for reheating the cooled intermediate concentrated solution with refrigerant vapor to obtain a concentrated solution,
A low-temperature solution heat exchanger 4 for heat-exchanging the concentrated solution with a dilute solution and lowering the temperature; a condenser 7 for condensing refrigerant vapor into a liquid refrigerant;
The evaporator 8 is provided with an evaporator tray 8a at the upper part, and a liquid refrigerant is dropped from the evaporator tray 8a to evaporate. The evaporator 8 is provided with an absorber tray 9a at the upper part. Absorber 9 comprising an absorber 9 for dropping a concentrated solution and absorbing a refrigerant vapor evaporated in an evaporator 8 to generate a dilute solution, and a solution circulation pump 5 connected to the absorber 9 for sucking the dilute solution. A water machine, a tray for holding an evaporator 8 and an absorber 9 in one container 11 via a common partition 10 and holding at least one of an evaporator tray 8a and an absorber tray 9a substantially horizontally. Fixing plates 8d and 9d are provided,
At least one end of each of the tray fixing plates 8d and 9d is fixed to the common partition 10 by welding w or the like, and each tray fixing plate is fixed to at least one of the evaporator coil 8b and the absorber coil 9b. It is configured to be arranged apart from the fixing plates 8e, 9e.
【0010】そして図6及び図7に示すように、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及び吸収器9の円環状のコイル8
b,9bの上にほぼ均等に滴下し散布されるようになっ
ている。蒸発器トレイ8a及び吸収器トレイ9aは、半
径方向に設けられた複数のトレイ固定板8c,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の上端面により支持され、トレイ固定板
8c,9cの下端がトレイ固定板8d,9dの上部に溶
接w等で固着されている。またトレイ固定板8d,9d
がコイル固定板8e,9eとコイル8b,9bの長さ方
向に離間されており、またコイル固定板8e,9eの上
端面が蒸発器トレイ8a及び吸収器トレイ9aの下面よ
り離間されているとともに、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。As shown in FIGS. 6 and 7, an evaporator tray 8a for dropping the liquid refrigerant and an absorber tray 9a for dropping the concentrated solution are mounted above the evaporator 8 and the absorber 9. The evaporator tray 8a and the absorber tray 9a have a U-shaped box-shaped cross section with an open upper surface, are formed in an annular shape, and have a large number of holes formed in the bottom surface. After the liquid refrigerant or concentrated solution flowing from the upper surface is stored at a predetermined height, the liquid column pressure causes the annular coils 8 of the evaporator 8 and the absorber 9 to pass through a number of holes.
b and 9b are almost uniformly dropped and sprayed. The evaporator tray 8a and the absorber tray 9a are inserted through a plurality of tray fixing plates 8c, 9c provided in the radial direction and fixed in the circumferential direction, and the lower surface is supported by the upper end surfaces of the tray fixing plates 8d, 9d. The lower ends of the tray fixing plates 8c and 9c are fixed to the upper portions of the tray fixing plates 8d and 9d by welding w or the like. Also, tray fixing plates 8d, 9d
Are separated from the coil fixing plates 8e, 9e in the longitudinal direction of the coils 8b, 9b, and the upper end surfaces of the coil fixing plates 8e, 9e are separated from the lower surfaces of the evaporator tray 8a and the absorber tray 9a. The spacers 8f and 9f are provided in the vertical direction at a predetermined pitch so as to sandwich the coils 8b and 9b in a plurality of rows in the vertical direction.
【0011】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されてお
り、トレイ固定板8c,9cの一端を固定している。そ
してトレイ固定板8c,9cの下端を固定したトレイ固
定板8d,9dをコイル固定板8e,9eより離間し、
コイル固定板8e,9eの上端面を蒸発器トレイ8a及
び吸収器トレイ9aの底面より隙間aを開ける。この隙
間aによりトレイ固定板8c,9cの他端がコイル8
b,9bの自重により下がった場合でも、トレイ8a,
9aが水平を保ち、トレイ8a,9a内の液面が絶えず
均一に維持される。The common partition 10 is provided substantially concentrically with the container 11 so as to partition the evaporator 8 and the absorber 9, and fixes one end of the tray fixing plates 8c and 9c. Then, the tray fixing plates 8d, 9d to which the lower ends of the tray fixing plates 8c, 9c are fixed are separated from the coil fixing plates 8e, 9e,
A gap a is opened from the bottom surfaces of the evaporator tray 8a and the absorber tray 9a on the upper end surfaces of the coil fixing plates 8e and 9e. Due to the gap a, the other ends of the tray fixing plates 8c and 9c
b, 9b, the tray 8a,
9a is kept horizontal, and the liquid levels in the trays 8a, 9a are constantly maintained.
【0012】本実施例によれば、蒸発器トレイ及び吸収
器トレイの少なくともいずれか一方が、蒸発器コイル又
は吸収器コイルの自重に影響されることなくほぼ水平に
保持されるため、蒸発器トレイ又は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
もほぼ均一に液冷媒又は濃溶液が滴下するようになり、
コイルに一様に散布される結果、コイル上の液膜厚さが
等しくなって冷凍能力が安定する。According to this embodiment, at least one of the evaporator tray and the absorber tray is held substantially horizontally without being affected by the weight of the evaporator coil or the absorber coil. Or, the liquid surface of the liquid refrigerant or concentrated solution stored in the absorber tray becomes almost horizontal, the liquid column pressures to many holes on the bottom surface become equal, and the liquid refrigerant or concentrated solution is almost uniformly discharged from any hole. Began to drip,
As a result of being uniformly spread on the coil, the liquid film thickness on the coil becomes equal and the refrigerating capacity is stabilized.
【0013】[0013]
【発明の効果】本発明によれば、蒸発器コイル又は吸収
器コイルの自重による蒸発器トレイ又は吸収器トレイの
歪が防止されて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不安定が防止
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 or the absorber tray is prevented from being distorted due to the weight of the evaporator coil or the absorber coil and is held almost horizontally, the amount of the liquid refrigerant or the concentrated solution dropped is reduced. Instability of the refrigeration capacity due to unevenness of the refrigeration is prevented, and the refrigeration capacity is stabilized.
【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の蒸発器の要部を示す断面図である。FIG. 2 is a sectional view showing a main part of the evaporator of FIG.
【図3】図2の側面図である。FIG. 3 is a side view of FIG. 2;
【図4】図1の吸収器の要部を示す断面図である。FIG. 4 is a sectional view showing a main part of the absorber of FIG.
【図5】図4の側面図である。FIG. 5 is a side view of FIG. 4;
【図6】図1の容器の横断面図である。FIG. 6 is a cross-sectional view of the container of FIG.
【図7】図6の斜視図である。FIG. 7 is a perspective view of FIG. 6;
【図8】従来の技術を示す図である。FIG. 8 is a diagram showing a conventional technique.
【図9】図8の蒸発器を示す断面図である。FIG. 9 is a sectional view showing the evaporator of FIG. 8;
【図10】図9の側面図である。FIG. 10 is a side view of FIG. 9;
【図11】図8の吸収器を示す断面図である。FIG. 11 is a sectional view showing the absorber of FIG. 8;
【図12】図11の側面図である。FIG. 12 is a side view of FIG. 11;
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 8b 蒸発器コイル 8c トレイ固定板 8d トレイ固定板 8e コイル固定板 9 吸収器 9a 吸収器トレイ 9b 吸収器コイル 9c トレイ固定板 9d トレイ固定板 9e コイル固定板 10 共通仕切 11 容器 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 8b Evaporator coil 8c Tray fixing plate 8d Tray fixing plate 8e Coil fixing plate 9 Absorber 9a Absorber tray 9b Absorber coil 9c Tray fixing plate 9d Tray fixing plate 9e Coil fixing plate 10 Common partition 11 Container
───────────────────────────────────────────────────── 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 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) F25B 15/00 F25B 37/00 F25B 39/02
Claims (1)
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、降温した前記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、該濃溶液を前記
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
つの容器に収容し、前記蒸発器トレイ及び前記吸収器ト
レイの少なくともいずれか一方をほぼ水平に保持するト
レイ固定板を設け、それぞれのトレイ固定板の一端を前
記共通仕切に固着するとともに、それぞれのトレイ固定
板を蒸発器コイル及び吸収器コイルの少なくともいずれ
か一方のコイル固定板より離間して配置したことを特徴
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 with the dilute solution to lower the temperature, and A condenser for condensing the refrigerant vapor into a liquid refrigerant; an evaporator for evaporating the liquid refrigerant from the evaporator tray by evaporating the liquid refrigerant from the evaporator tray; and an absorbing tray for evaporating the liquid refrigerant from the evaporator tray to the upper part. An absorber for dropping the concentrated solution from the low-temperature solution heat exchanger from the container tray and absorbing a refrigerant vapor evaporated by the evaporator to generate a dilute solution, wherein the evaporator comprises: And the absorber are housed in one container via a common partition, A tray fixing plate that holds at least one of the evaporator tray and the absorber tray substantially horizontally is provided, one end of each tray fixing plate is fixed to the common partition, and each tray fixing plate is attached to the evaporator. An absorption chiller / heater characterized by being arranged apart from a coil fixing plate of at least one of a coil and an absorber coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07067279A JP3089533B2 (en) | 1995-03-27 | 1995-03-27 | Absorption chiller / heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07067279A JP3089533B2 (en) | 1995-03-27 | 1995-03-27 | Absorption chiller / heater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08261587A JPH08261587A (en) | 1996-10-11 |
| JP3089533B2 true JP3089533B2 (en) | 2000-09-18 |
Family
ID=13340381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP07067279A Expired - Fee Related JP3089533B2 (en) | 1995-03-27 | 1995-03-27 | Absorption chiller / heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3089533B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5036360B2 (en) * | 2007-03-22 | 2012-09-26 | 大阪瓦斯株式会社 | Absorption refrigerator |
-
1995
- 1995-03-27 JP JP07067279A patent/JP3089533B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08261587A (en) | 1996-10-11 |
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| Date | Code | Title | Description |
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| LAPS | Cancellation because of no payment of annual fees |