JP2957112B2 - Regenerator for absorption refrigeration system - Google Patents

Regenerator for absorption refrigeration system

Info

Publication number
JP2957112B2
JP2957112B2 JP7219951A JP21995195A JP2957112B2 JP 2957112 B2 JP2957112 B2 JP 2957112B2 JP 7219951 A JP7219951 A JP 7219951A JP 21995195 A JP21995195 A JP 21995195A JP 2957112 B2 JP2957112 B2 JP 2957112B2
Authority
JP
Japan
Prior art keywords
medium
case
concentration
low
temperature regenerator
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
JP7219951A
Other languages
Japanese (ja)
Other versions
JPH0961011A (en
Inventor
克也 大島
泰平 林
佐登志 内藤
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.)
Rinnai Corp
Original Assignee
Rinnai 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 Rinnai Corp filed Critical Rinnai Corp
Priority to JP7219951A priority Critical patent/JP2957112B2/en
Publication of JPH0961011A publication Critical patent/JPH0961011A/en
Application granted granted Critical
Publication of JP2957112B2 publication Critical patent/JP2957112B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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]

【発明の属する技術分野】この発明は、臭化リチウムな
どの水溶液を吸収液として用いた吸収式冷凍装置の冷凍
機本体に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigerator main body of an absorption refrigerating apparatus using an aqueous solution such as lithium bromide as an absorbing solution.

【0002】[0002]

【従来の技術】吸収式冷凍装置の冷凍機本体は、加熱タ
ンクの頂部から上方に延設した中濃度吸収液仕切筒の外
周に縦型円筒状の冷媒蒸気回収筒を配した高温再生器を
備える。冷媒蒸気回収筒の外に縦筒状の低温再生器ケー
スを設け、低温再生器ケースの外に縦筒状の蒸発・吸収
ケースを形成した同心的または偏心的多重筒構造を有す
る。中濃度吸収液仕切筒、冷媒蒸気回収筒、低温再生器
ケースおよび蒸発・吸収ケースの間の環状隙間には、底
板があてがわれ、当接面が気密状態に溶接される。
2. Description of the Related Art A refrigerator body of an absorption refrigeration system is a high-temperature regenerator in which a vertical cylindrical refrigerant vapor recovery cylinder is arranged on the outer periphery of a medium-concentration absorption liquid partition cylinder extending upward from the top of a heating tank. Prepare. It has a concentric or eccentric multi-cylinder structure in which a vertical cylindrical low temperature regenerator case is provided outside the refrigerant vapor recovery cylinder, and a vertical cylindrical evaporation / absorption case is formed outside the low temperature regenerator case. A bottom plate is applied to an annular gap between the medium-concentration absorbing liquid partition cylinder, the refrigerant vapor recovery cylinder, the low-temperature regenerator case, and the evaporation / absorption case, and the contact surface is welded in an airtight state.

【0003】高温再生器では、バーナなどの加熱源で加
熱された低濃度吸収液を170℃前後に加熱・沸騰さ
せ、中濃度吸収液仕切筒内で冷媒蒸気と160℃前後の
中濃度吸収液とを生成させている。冷媒蒸気回収筒内で
は、壁面の熱交換により凝縮した冷媒液が底に溜まる。
この冷媒液は90℃前後であり、冷媒液流路を通じて圧
力差により凝縮器に供給される。
In a high-temperature regenerator, a low-concentration absorbing liquid heated by a heating source such as a burner is heated and boiled to about 170 ° C., and refrigerant vapor and a medium-concentration absorbing liquid of about 160 ° C. are separated in a medium-concentration absorbing liquid partition tube. And is generated. In the refrigerant vapor recovery cylinder, the refrigerant liquid condensed by heat exchange on the wall surface accumulates at the bottom.
This refrigerant liquid is around 90 ° C., and is supplied to the condenser by a pressure difference through the refrigerant liquid flow path.

【0004】[0004]

【発明が解決しようとする課題】冷媒蒸気回収筒の底に
溜まる冷媒液は、低温度であり、沸騰または蒸発するこ
とがないことが望ましい。しかるに、コンパクト化のた
め、寸法の短縮が求められており、中濃度吸収液仕切筒
内の中濃度吸収液の液面と冷媒蒸気回収筒の底の距離を
大きく取ることが困難となっている。
It is desirable that the refrigerant liquid accumulated at the bottom of the refrigerant vapor recovery cylinder has a low temperature and does not boil or evaporate. However, for compactness, it is required to reduce the size, and it is difficult to increase the distance between the liquid surface of the medium concentration absorbing liquid in the medium concentration absorbing liquid partition and the bottom of the refrigerant vapor recovery cylinder. .

【0005】このため、冷媒蒸気回収筒の底に溜まる冷
媒液を中濃度吸収液からの伝熱により再沸騰させる。こ
れによって、中濃度吸収液仕切筒内は、熱を奪われて沸
騰エネルギーの損失が生じ、低濃度吸収液の沸騰による
蒸気冷媒の分離が妨げられる。この結果、冷凍装置は、
熱効率が低下して冷凍能力が低下する問題が生じてい
る。
For this reason, the refrigerant liquid accumulated at the bottom of the refrigerant vapor recovery cylinder is re-boiled by the heat transfer from the medium-concentration absorption liquid. As a result, heat is deprived in the middle-concentration absorbent partition, causing a loss of boiling energy, thereby preventing the separation of the vapor refrigerant due to the boiling of the low-concentration absorbent. As a result, the refrigeration system
There is a problem that the thermal efficiency is reduced and the refrigerating capacity is reduced.

【0006】この発明の目的は、冷凍機本体の体格の増
大を招かず、中濃度吸収液仕切筒内の中濃度吸収液の熱
が、冷媒蒸気回収筒の底に溜まった冷媒液に伝達して冷
媒液が沸騰または蒸発し、熱の損失が生じて冷凍能力が
低下することを防止できる再生器の提供にある。
SUMMARY OF THE INVENTION It is an object of the present invention to transfer the heat of the medium-concentration absorbing liquid in the medium-concentration absorbing liquid partition to the refrigerant liquid accumulated at the bottom of the refrigerant vapor recovery cylinder without increasing the size of the refrigerator body. It is an object of the present invention to provide a regenerator capable of preventing a refrigerant liquid from boiling or evaporating and causing a loss of heat to reduce a refrigerating capacity.

【0007】[0007]

【課題を解決するための手段】この発明の吸収式冷凍装
置の再生器は、加熱タンクおよび該加熱タンクから上方
に延設された中濃度吸収液仕切筒、および該中濃度吸収
液仕切筒の外周に配された冷媒蒸気回収筒を有する高温
再生器と、前記冷媒蒸気回収筒の外周に設けられた縦型
円筒状の低温再生器ケースと、前記低温再生器ケースの
外周に配された縦型円筒状の蒸発・吸収ケースと、前記
蒸発・吸収ケースの上方に配された凝縮器ケースと、前
記冷媒蒸気回収筒、低温再生器ケース、および蒸発・吸
収ケースの下端に溶接された底板とを有する吸収式冷凍
装置の再生器において、前記中濃度吸収液仕切筒は、前
記加熱タンクの沸騰口から延設された内筒と、該内筒の
上端に溶接された上端と、前記底板に溶接された下端と
を有し、前記内筒との間に断熱隙間を形成する外筒とか
らなることを特徴とする。
SUMMARY OF THE INVENTION A regenerator for an absorption refrigeration apparatus according to the present invention comprises a heating tank, a medium-concentration absorbing liquid partition extending upward from the heating tank, and a medium-concentration absorbing liquid partition. A high-temperature regenerator having a refrigerant vapor recovery cylinder disposed on an outer periphery thereof; a vertical cylindrical low-temperature regenerator case provided on the outer periphery of the refrigerant vapor recovery cylinder; and a vertical disposed on an outer periphery of the low-temperature regenerator case. A cylindrical evaporating / absorbing case, a condenser case disposed above the evaporating / absorbing case, a refrigerant vapor recovery cylinder, a low-temperature regenerator case, and a bottom plate welded to a lower end of the evaporating / absorbing case. In the regenerator of an absorption refrigeration apparatus having the above, the medium-concentration absorbent partition is an inner cylinder extending from a boiling port of the heating tank, an upper end welded to an upper end of the inner cylinder, and a bottom plate. Said inner cylinder having a welded lower end and Characterized by comprising the outer tube which forms an insulating gap between the.

【0008】請求項2に記載の再生器は、前記冷媒蒸気
回収筒の底部の近傍の前記中濃度吸収液仕切筒の内周壁
に断熱層を形成したことを特徴とする。請求項3に記載
の再生器は、前記断熱層は、樹脂層であることを特徴と
する。
A regenerator according to a second aspect of the present invention is characterized in that a heat insulating layer is formed on an inner peripheral wall of the middle concentration absorbing liquid partition near the bottom of the refrigerant vapor recovery cylinder. A regenerator according to a third aspect is characterized in that the heat insulating layer is a resin layer.

【0009】[0009]

【発明の作用・効果】この吸収式冷凍装置の再生器は、
中濃度吸収液仕切筒を、内筒と、該内筒の上端に上端が
溶接され底板に下端が溶接されるとともに、内筒との間
に断熱隙間を形成する外筒とで形成したので、高温度の
中濃度吸収液の熱が冷媒蒸気回収筒の底に滞留した冷媒
液へ伝達することを阻止できる。このため、冷媒液の蒸
発を低減でき、運転効率が向上する。
The regenerator of this absorption refrigeration system is:
Since the medium-concentration absorbing liquid partition cylinder was formed of an inner cylinder and an outer cylinder forming an adiabatic gap between the inner cylinder and the lower end thereof being welded to the upper end thereof and the lower end thereof being welded to the bottom plate, It is possible to prevent the heat of the high-temperature medium-concentration absorbing liquid from being transmitted to the refrigerant liquid remaining at the bottom of the refrigerant vapor recovery cylinder. For this reason, the evaporation of the refrigerant liquid can be reduced, and the operation efficiency is improved.

【0010】請求項2の構成では、中濃度吸収液仕切筒
の内面に断熱層を張り、二重筒と同様の効果を得てい
る。請求項3の構成では、断熱層を耐熱性および耐蝕性
に優れた樹脂製とし、耐久性を向上させている。
According to the second aspect of the present invention, a heat insulating layer is provided on the inner surface of the intermediate-concentration absorbing liquid partition cylinder, and the same effect as the double cylinder is obtained. In the configuration of the third aspect, the heat insulating layer is made of a resin having excellent heat resistance and corrosion resistance, thereby improving durability.

【0011】[0011]

【発明の実施の形態】図1は、吸収式冷凍装置の冷凍機
本体100を示す。吸収式冷凍装置200は、図2に示
す如く、冷凍機本体100とクーリングタワー(冷却
塔)CTとからなり、クーリングユニット(室内機)C
Uが付設され空調装置を構成している。冷凍機本体10
0は、図示しないスタンドにより支持された縦に立設さ
れている。
FIG. 1 shows a refrigerator main body 100 of an absorption refrigeration system. As shown in FIG. 2, the absorption refrigeration system 200 includes a refrigerator main body 100 and a cooling tower (cooling tower) CT, and a cooling unit (indoor unit) C
U is attached to form an air conditioner. Refrigerator body 10
Numeral 0 stands upright supported by a stand (not shown).

【0012】冷凍機本体100は、低濃度吸収液を加熱
・沸騰させ、中濃度吸収液と冷媒蒸気とに分離するため
の高温再生器1を下部に備える。高温再生器1は、下方
に加熱源としてのガスバーナBが配置された加熱タンク
11、加熱タンク11から上方に延設され上端が開口し
たステンレス製円筒からなる中濃度吸収液仕切筒12、
および中濃度吸収液仕切筒12の外周に偏心して配設さ
れたステンレス製で縦型円筒状の気密性容器からなる冷
媒蒸気回収筒10を有する。
The refrigerator main body 100 is provided with a high-temperature regenerator 1 for heating and boiling the low-concentration absorbing liquid to separate it into medium-concentration absorbing liquid and refrigerant vapor. The high-temperature regenerator 1 includes a heating tank 11 in which a gas burner B as a heating source is disposed below, a medium-concentration absorbing liquid partition tube 12 formed of a stainless steel cylinder extending upward from the heating tank 11 and having an open upper end,
And a refrigerant vapor recovery cylinder 10 composed of a stainless steel vertical cylindrical airtight container disposed eccentrically on the outer periphery of the medium concentration absorbent partition cylinder 12.

【0013】中濃度吸収液仕切筒12は、下部121に
冷媒が蒸発して中濃度となった中濃度吸収液が滞留して
おり、上端開口122から沸騰した吸収液(冷媒蒸気)
が冷媒蒸気回収筒10の内部に吹き出している。1A
は、動揺している中濃度吸収液の平均的液面を示す。冷
媒蒸気回収筒10の外周には、熱効率を向上させる作用
を有する低温再生器2が設けられている。
In the medium-concentration absorbent partition 12, a medium-concentration absorbent having a medium concentration due to evaporation of the refrigerant is retained in a lower portion 121, and an absorbent (refrigerant vapor) boiled from an upper end opening 122.
Blows out into the refrigerant vapor recovery cylinder 10. 1A
Indicates the average liquid level of the oscillating medium concentration absorption liquid. A low-temperature regenerator 2 having a function of improving thermal efficiency is provided on the outer periphery of the refrigerant vapor recovery cylinder 10.

【0014】低温再生器2は、ステンレス製で縦型円筒
状を呈し、天井に冷媒蒸気出口21が開口するととも
に、前記中濃度吸収液仕切筒12と同心的に配置された
低温再生器ケース20を備える。低温再生器ケース20
は低圧であり、高圧である中濃度吸収液仕切筒12の下
部121から、中濃度吸収液流路L1 により熱交換器H
を介して中濃度吸収液が供給される。
The low-temperature regenerator 2 is made of stainless steel, has a vertical cylindrical shape, has a refrigerant vapor outlet 21 opened in the ceiling, and has a low-temperature regenerator case 20 arranged concentrically with the medium-concentration absorbent partition 12. Is provided. Low temperature regenerator case 20
Is a low-pressure, high-pressure medium-absorbent partition 12 from the lower part 121 of the medium-concentrated absorbent flow path L1 through the heat exchanger H.
Is supplied via the medium.

【0015】低温再生器ケース20内の中濃度吸収液
は、前記冷媒蒸気回収筒10の外周面を熱源として再蒸
発し、高濃度吸収液と冷媒蒸気に分離される。低温再生
器2の外周には、ステンレス製で縦型円筒形の気密性容
器からなる蒸発・吸収ケース30が同心的に設置されて
いる。蒸発・吸収ケース30内には、内周側に吸収器3
が設けられ、外周側に蒸発器4が設置されている。
The medium-concentration absorbent in the low-temperature regenerator case 20 re-evaporates using the outer peripheral surface of the refrigerant vapor recovery cylinder 10 as a heat source, and is separated into a high-concentration absorbent and refrigerant vapor. On the outer periphery of the low-temperature regenerator 2, an evaporating / absorbing case 30 made of stainless steel and formed of a vertical cylindrical airtight container is concentrically installed. Inside the evaporating / absorbing case 30, the absorber 3
And an evaporator 4 is provided on the outer peripheral side.

【0016】低温再生器2の外周で、かつ蒸発・吸収ケ
ース30の上方には、ステンレス製で縦型円筒形の気密
性容器からなる凝縮器ケース50が同心的に設置され、
内部に冷却コイル51が配設された凝縮器5が構成され
ている。
On the outer periphery of the low-temperature regenerator 2 and above the evaporating / absorbing case 30, a condenser case 50 made of a stainless steel vertical cylindrical airtight container is installed concentrically.
The condenser 5 in which the cooling coil 51 is disposed is configured.

【0017】吸収器3は、蒸発・吸収ケース30内の内
側部分に縦型円筒状に巻設した冷却コイル31を配置
し、その上方に該冷却コイル31に高濃度吸収液を散布
するための高濃度吸収液散布具32を装着してなる。蒸
発器4は、蒸発・吸収ケース30内の外側部分に、縦型
円筒状に巻設した蒸発コイル41を配置し、その上方に
冷媒液散布具42を配してなる。
The absorber 3 is provided with a cooling coil 31 wound in a vertical cylindrical shape inside an evaporating / absorbing case 30 and for spraying a high-concentration absorbing liquid to the cooling coil 31 above the cooling coil 31. A high-concentration absorbent sprayer 32 is attached. The evaporator 4 has an evaporator coil 41 wound in a vertical cylindrical shape disposed on an outer portion inside the evaporator / absorber case 30, and a refrigerant liquid disperser 42 disposed above the evaporator coil 41.

【0018】高温再生器1、低温再生器2、吸収器3、
蒸発器4および凝縮器5は、同心的に配されるととも
に、図1に示す如く、下端が底板6に一体に溶接されて
縦型円筒形の冷凍機本体100を形成している。中濃度
吸収液仕切筒12は、下端が加熱タンク11の頂部に開
口した筒状の沸騰口13に嵌合・溶接された内筒14
と、該内筒14に微小隙間15を隔てて同軸配置され、
上端が内筒14の上端に外嵌・溶接されるとともに、下
端が底板6の上面に設けた中央段部60に外嵌・溶接さ
れた外筒16とからなる。
A high-temperature regenerator 1, a low-temperature regenerator 2, an absorber 3,
The evaporator 4 and the condenser 5 are arranged concentrically, and as shown in FIG. 1, the lower end is integrally welded to the bottom plate 6 to form a vertical cylindrical refrigerator main body 100. The intermediate-concentration absorbent partition tube 12 has an inner tube 14 fitted and welded to a cylindrical boiling port 13 having a lower end opened at the top of the heating tank 11.
And coaxially arranged in the inner cylinder 14 with a minute gap 15 therebetween,
The upper end is externally fitted and welded to the upper end of the inner cylinder 14, and the lower end is formed of the outer cylinder 16 fitted and welded to the central step portion 60 provided on the upper surface of the bottom plate 6.

【0019】底板6は、ステンレス板をプレスして一体
成形されており、内側段61を介して上方に突き出た中
央部62を有する。中央部62には、中濃度吸収液仕切
筒12の内筒14が挿通する挿通穴63が設けられてい
る。挿通穴63には、円周状に90度の間隔で4つの支
持爪64が突設されており、内筒14の下部外周壁を支
持して同心を保っている。挿通穴63の外周には、前記
中央段部60が形成されており、前記外筒16の下端が
外嵌・溶接されている。
The bottom plate 6 is integrally formed by pressing a stainless steel plate, and has a central portion 62 protruding upward through an inner step 61. The central portion 62 is provided with an insertion hole 63 through which the inner cylinder 14 of the intermediate-concentration absorbing liquid partition cylinder 12 is inserted. Four support claws 64 are projected from the insertion hole 63 circumferentially at 90 ° intervals, and support the lower outer peripheral wall of the inner cylinder 14 to maintain concentricity. The central step portion 60 is formed on the outer periphery of the insertion hole 63, and the lower end of the outer cylinder 16 is externally fitted and welded.

【0020】内側段61には、冷媒蒸気回収筒10の下
端が外嵌・溶接されている。内側段61の外周には、環
状の低温再生器底65を介して外側段66が形成され、
低温再生器ケース20の下端が外嵌・溶接されている。
外側段66から下方に筒部67が延設され、該筒部67
の下端からは水平方向に円環状の鍔部68が設けられて
いる。蒸発・吸収ケース30の下端には水平方向に短寸
のフランジ状縁33が設けられており、鍔部68の外周
とフランジ状縁33の外周とが溶接されている。
The lower end of the refrigerant vapor recovery cylinder 10 is externally fitted and welded to the inner step 61. An outer stage 66 is formed on the outer periphery of the inner stage 61 via an annular low-temperature regenerator bottom 65,
The lower end of the low-temperature regenerator case 20 is externally fitted and welded.
A cylindrical portion 67 extends downward from the outer step 66, and the cylindrical portion 67
An annular flange 68 is provided in the horizontal direction from the lower end. A short flange 33 in the horizontal direction is provided at the lower end of the evaporating / absorbing case 30. The outer periphery of the flange 68 and the outer periphery of the flange 33 are welded.

【0021】加熱タンク11内は、バーナBでの加熱で
低濃度吸収液が沸騰しており、温度は170℃程度とな
っている。中濃度吸収液仕切筒12の下部121内の中
濃度吸収液は160℃程度になっている。冷媒蒸気回収
筒10と中濃度吸収液仕切筒12との間の冷媒蒸気回収
筒10の底1Bは、液化した冷媒液が溜まる冷媒液受け
部となって、冷媒流路L3 で低圧の凝縮器5に連通して
いる。この液冷媒は、90℃となっており、凝縮器5内
で再蒸発し、冷却コイル51で冷却され再液化する。
In the heating tank 11, the low-concentration absorbing liquid is boiled by heating with the burner B, and the temperature is about 170 ° C. The medium concentration absorbent in the lower part 121 of the medium concentration absorbent partition 12 is at about 160 ° C. The bottom 1B of the refrigerant vapor recovery cylinder 10 between the refrigerant vapor recovery cylinder 10 and the medium-concentration absorption liquid partitioning cylinder 12 serves as a refrigerant liquid receiving portion for storing liquefied refrigerant liquid, and a low-pressure condenser is provided in the refrigerant flow path L3. 5 is connected. This liquid refrigerant is at 90 ° C., re-evaporates in the condenser 5, is cooled by the cooling coil 51 and is re-liquefied.

【0022】冷媒蒸気回収筒10の底1B内の冷媒液
が、中濃度吸収液仕切筒12の下部121内の中濃度吸
収液からの伝熱で再沸騰ないし再蒸発すると、ベーパー
ロックにより凝縮器5への冷媒液の流出が円滑にできな
くなる。これを防止するためには、冷媒蒸気回収筒10
の底1Bに溜まった冷媒液への中濃度吸収液仕切筒12
の下部121内の中濃度吸収液からの伝熱を阻止する必
要がある。
When the refrigerant liquid in the bottom 1B of the refrigerant vapor recovery cylinder 10 re-boils or re-evaporates due to heat transfer from the medium-concentration absorbing liquid in the lower part 121 of the medium-concentration absorbing liquid partitioning cylinder 12, the condenser is operated by vapor lock. 5 cannot flow smoothly. In order to prevent this, the refrigerant vapor recovery cylinder 10
Partitioning tube 12 for medium-concentration absorbent into refrigerant liquid accumulated in bottom 1B
It is necessary to prevent heat transfer from the medium-concentration absorbing liquid in the lower part 121.

【0023】この実施例では、中濃度吸収液仕切筒12
を、下端が加熱タンク11の沸騰口13に嵌合・溶接さ
れた内筒14と、該内筒14に微小隙間15を隔てて同
軸配置され、上端が内筒14の上端に外嵌・溶接される
とともに、下端が底板6の上面に設けた中央段部60に
外嵌・溶接された外筒16とで形成している。
In this embodiment, the intermediate concentration absorbent partition 12
An inner cylinder 14 whose lower end is fitted and welded to the boiling port 13 of the heating tank 11, and is coaxially arranged with a small gap 15 between the inner cylinder 14 and an upper end is externally fitted and welded to the upper end of the inner cylinder 14. In addition, the lower end is formed by an outer cylinder 16 fitted and welded to a central step portion 60 provided on the upper surface of the bottom plate 6.

【0024】これにより、中濃度吸収液仕切筒12によ
る熱伝導路を長くして、熱伝導の低減を図っている。な
お、微小隙間15の下方は、前記4つの支持爪64以外
の部分が開放しており、微小隙間15が内筒14と外筒
16との間の空気断熱層として作用する際に、膨張空気
の逃し穴として作用する。
As a result, the heat conduction path of the intermediate-concentration liquid partitioning tube 12 is lengthened to reduce heat conduction. Below the minute gap 15, portions other than the four support claws 64 are open, and when the minute gap 15 acts as an air insulation layer between the inner cylinder 14 and the outer cylinder 16, the expanded air Acts as an escape hole.

【0025】吸収器3の底部と加熱タンク11の底部と
の間は、吸収器3から排出された低濃度吸収液を、高温
再生器1の加熱タンク11に帰還させるための低濃度吸
収液流路L2 で連結されている。低濃度吸収液流路L2
には、熱交換器Hおよび吸収液ポンプP1 が介装されて
いる。
Between the bottom of the absorber 3 and the bottom of the heating tank 11, a low-concentration absorbing liquid flow for returning the low-concentration absorbing liquid discharged from the absorber 3 to the heating tank 11 of the high-temperature regenerator 1. It is connected by road L2. Low concentration absorbent flow path L2
Is provided with a heat exchanger H and an absorbent pump P1.

【0026】低温再生器2の上部は気液分離部22とな
っており、該気液分離部22は凝縮器5の上部と隙間5
Aを介して連通している。中濃度吸収液仕切筒12の下
部121は、前記中濃度吸収液流路L1 で低温再生器2
の頂部または底部(図では頂部)に連通している。低温
再生器2の高濃度吸収液受け部23は、熱交換器Hを介
して高濃度吸収液流路L4 により、高濃度吸収液散布具
32へ連結されている。
The upper part of the low-temperature regenerator 2 is a gas-liquid separator 22. The gas-liquid separator 22 is located between the upper part of the condenser 5 and the gap 5.
It communicates via A. The lower part 121 of the intermediate-concentration absorbent partition 12 is connected to the low-temperature regenerator 2 through the medium-concentration absorbent flow path L1.
Communicate with the top or bottom (the top in the figure). The high-concentration absorbent receiving section 23 of the low-temperature regenerator 2 is connected to the high-concentration absorbent sprayer 32 via the heat exchanger H by a high-concentration absorbent flow path L4.

【0027】凝縮器5の下部と蒸発器4の蒸発コイル4
1の上方に設置された冷媒液散布具42とは、オリフィ
ス付き電磁弁V1 が介装された冷媒液供給路L5 で連通
してある。冷媒は、蒸発コイル41の表面に冷媒液散布
具42から滴下された後、蒸発コイル41から気化熱を
奪って蒸発し、内部を流れる熱媒体としての冷温水を冷
却する。
The lower part of the condenser 5 and the evaporator coil 4 of the evaporator 4
The refrigerant liquid dispersing device 42 installed above 1 is connected to a refrigerant liquid supply passage L5 in which a solenoid valve V1 with an orifice is interposed. After the refrigerant is dropped from the refrigerant liquid sprayer 42 onto the surface of the evaporating coil 41, the refrigerant takes away heat of vaporization from the evaporating coil 41, evaporates, and cools cold and hot water as a heat medium flowing inside.

【0028】この際に発生する蒸気冷媒は、冷却コイル
31の表面で高濃度吸収液散布具32から滴下された高
濃度吸収液に吸収される。冷媒を吸収して低濃度になっ
た吸収液は、前記低濃度吸収液流路L2 を経て吸収液ポ
ンプP1 により、加熱タンク11に戻される。
The vapor refrigerant generated at this time is absorbed by the high concentration absorbing liquid dropped from the high concentration absorbing liquid sprayer 32 on the surface of the cooling coil 31. The absorption liquid having a low concentration by absorbing the refrigerant is returned to the heating tank 11 by the absorption liquid pump P1 through the low concentration absorption liquid flow path L2.

【0029】冷却コイル31は冷却コイル51に接続
し、さらに冷却塔CTと冷却水循環路34で接続してあ
り、冷却水ポンプP2 により冷却水が、冷却塔CT→冷
却コイル31→冷却コイル51→冷却塔CTの順に循環
している。蒸発コイル41は、冷温水ポンプP3 を有す
る冷温水循環路43で室内機CUに接続されている。
The cooling coil 31 is connected to the cooling coil 51, and further connected to the cooling tower CT via the cooling water circulation path 34. The cooling water is supplied by the cooling water pump P2 to the cooling tower CT → the cooling coil 31 → the cooling coil 51 → It circulates in the order of the cooling tower CT. The evaporating coil 41 is connected to the indoor unit CU through a cold / hot water circulation path 43 having a cold / hot water pump P3.

【0030】吸収器3から排出された低温度の低濃度吸
収液は、吸収液ポンプP1 で熱交換器Hに供給され、高
濃度吸収液および中濃度吸収液と熱交換して加熱された
後、加熱タンク11に帰還され、再び加熱され沸騰す
る。
The low-temperature low-concentration absorbent discharged from the absorber 3 is supplied to the heat exchanger H by the absorbent pump P1 and is heated after exchanging heat with the high-concentration absorbent and the medium-concentration absorbent. Is returned to the heating tank 11 and again heated and boiled.

【0031】中濃度吸収液仕切筒12内の中濃度吸収液
は高温度であり、熱交換器H内で低濃度吸収液と熱交換
され、冷却された後、圧力差により低温再生器2に供給
される。低温再生器2に生成した高濃度吸収液は、熱交
換器Hで低濃度吸収液と熱交換されて低温になり、高濃
度吸収液散布具32に圧力差で供給される。
The medium-concentration absorbing liquid in the medium-concentration absorbing liquid partition 12 has a high temperature, and is exchanged with the low-concentration absorbing liquid in the heat exchanger H. After being cooled, the medium is supplied to the low-temperature regenerator 2 by a pressure difference. Supplied. The high-concentration absorbent generated in the low-temperature regenerator 2 exchanges heat with the low-concentration absorbent in the heat exchanger H to become low in temperature, and is supplied to the high-concentration absorbent sprayer 32 with a pressure difference.

【0032】図3は他の実施例を示す。この実施例で
は、高温再生器1は、加熱タンク11の沸騰口13に連
結した揚液管18を有する。中濃度吸収液仕切筒12
は、加熱タンク11の延長部である揚液管18の下部に
中濃度吸収液仕切筒12の下端が外嵌・溶接され、上方
に延設されている。
FIG. 3 shows another embodiment. In this embodiment, the high-temperature regenerator 1 has a liquid pumping pipe 18 connected to the boiling port 13 of the heating tank 11. Medium concentration absorbent partition 12
The lower end of the medium-concentration absorbent partition 12 is externally fitted and welded to the lower part of the pumping pipe 18 which is an extension of the heating tank 11, and extends upward.

【0033】中濃度吸収液仕切筒12の下部の内周面に
は、フッ素樹脂製の筒体からなる断熱層7が設けられて
いる。断熱層7は、揚液管18と中濃度吸収液仕切筒1
2との間に溜まった中濃度吸収液の熱が、冷媒蒸気回収
筒10の底1Bに溜まった冷媒液へ伝熱することを阻止
している。
A heat insulating layer 7 made of a fluororesin cylinder is provided on the inner peripheral surface of the lower part of the intermediate-concentration liquid partitioning cylinder 12. The heat-insulating layer 7 is composed of the pumping pipe 18 and the medium-concentration absorbing liquid partition 1.
2 prevents the heat of the medium-concentration absorption liquid accumulated between the refrigerant vapors from being transferred to the refrigerant liquid accumulated at the bottom 1B of the refrigerant vapor recovery cylinder 10.

【0034】断熱層7は、フッ素樹脂製の筒体に限ら
ず、内周面にフッ素樹脂等の樹脂をコーティングしても
よく、セラミック製の筒体またはセラミックコーティン
グを採用してもよい。
The heat insulating layer 7 is not limited to a cylindrical body made of a fluororesin, but may be coated with a resin such as a fluororesin on the inner peripheral surface, or may be a cylindrical body made of a ceramic or a ceramic coating.

【0035】この実施例においても、中濃度吸収液仕切
筒12を内筒14と外筒16によって構成し、下方が開
放した微小隙間15を空気断熱層とすれば、さらに伝熱
を低減できる。なお、図1に示す実施例においても、中
濃度吸収液仕切筒12の下部の内周面に断熱層7を設け
ることにより、冷媒蒸気回収筒10の底1Bに溜まった
冷媒液の沸騰・蒸発防止効果がさらに向上できる。
Also in this embodiment, if the middle-concentration absorbing liquid partitioning cylinder 12 is constituted by the inner cylinder 14 and the outer cylinder 16 and the minute gap 15 opened downward is an air heat insulating layer, the heat transfer can be further reduced. In the embodiment shown in FIG. 1, the heat insulating layer 7 is provided on the inner peripheral surface of the lower part of the medium-concentration absorbing liquid partition 12 so that the refrigerant liquid accumulated on the bottom 1B of the refrigerant vapor recovery tube 10 boils and evaporates. The prevention effect can be further improved.

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

【図1】吸収式冷凍装置の冷凍機本体の断面図である。FIG. 1 is a sectional view of a refrigerator main body of an absorption refrigerator.

【図2】吸収式冷凍装置の概念図である。FIG. 2 is a conceptual diagram of an absorption refrigeration apparatus.

【図3】他の実施例の冷凍機本体の断面図である。FIG. 3 is a sectional view of a refrigerator main body according to another embodiment.

【符号の説明】[Explanation of symbols]

100 冷凍機本体 200 吸収式冷凍装置 1 高温再生器 2 低温再生器 3 吸収器 4 蒸発器 5 凝縮器 6 底板 7 断熱層 10 冷媒蒸気回収筒 11 加熱タンク 12 中濃度吸収液仕切筒 13 沸騰口 14 内筒 15 微小隙間 16 外筒 20 低温再生器ケース 30 蒸発・吸収ケース 50 凝縮器ケース 61 内側段 63 挿通穴 66 外側段 67 筒部 1B 底部 DESCRIPTION OF SYMBOLS 100 Refrigerator main body 200 Absorption refrigeration apparatus 1 High temperature regenerator 2 Low temperature regenerator 3 Absorber 4 Evaporator 5 Condenser 6 Bottom plate 7 Heat insulation layer 10 Refrigerant vapor recovery cylinder 11 Heating tank 12 Medium concentration absorption liquid partition 13 Boiling port 14 Inner cylinder 15 Micro gap 16 Outer cylinder 20 Low temperature regenerator case 30 Evaporation / absorption case 50 Condenser case 61 Inner step 63 Insertion hole 66 Outer step 67 Tube part 1B Bottom part

フロントページの続き (56)参考文献 特開 平2−263068(JP,A) 特開 平7−190554(JP,A) 特開 平7−43032(JP,A) (58)調査した分野(Int.Cl.6,DB名) F25B 33/00 F25B 15/00 303 Continuation of front page (56) References JP-A-2-263068 (JP, A) JP-A-7-190554 (JP, A) JP-A-7-43032 (JP, A) (58) Fields investigated (Int) .Cl. 6 , DB name) F25B 33/00 F25B 15/00 303

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 加熱タンクおよび該加熱タンクから上方
に延設された中濃度吸収液仕切筒、および該中濃度吸収
液仕切筒の外周に配された冷媒蒸気回収筒を有する高温
再生器と、 前記冷媒蒸気回収筒の外周に設けられた縦型円筒状の低
温再生器ケースと、 前記低温再生器ケースの外周に配された縦型円筒状の蒸
発・吸収ケースと、 前記蒸発・吸収ケースの上方に配された凝縮器ケース
と、 前記冷媒蒸気回収筒、低温再生器ケース、および蒸発・
吸収ケースの下端に溶接された底板とを有する吸収式冷
凍装置の再生器において、 前記中濃度吸収液仕切筒は、前記加熱タンクの沸騰口か
ら延設された内筒と、該内筒の上端に溶接された上端
と、前記底板に溶接された下端とを有し、前記内筒との
間に断熱隙間を形成する外筒とからなることを特徴とす
る再生器。
A high-temperature regenerator having a heating tank, a medium-concentration absorbent partition extending upward from the heating tank, and a refrigerant vapor recovery cylinder disposed on an outer periphery of the medium-concentration absorbent partition; A vertical cylindrical low-temperature regenerator case provided on the outer periphery of the refrigerant vapor recovery cylinder; a vertical cylindrical evaporator / absorber case disposed on the outer periphery of the low-temperature regenerator case; A condenser case disposed above, the refrigerant vapor recovery cylinder, a low-temperature regenerator case, and an evaporator
In a regenerator of an absorption refrigerating apparatus having a bottom plate welded to a lower end of an absorption case, the medium-concentration absorption liquid partition tube includes an inner cylinder extending from a boiling port of the heating tank, and an upper end of the inner cylinder. A regenerator having an upper end welded to the inner plate and an outer tube having a lower end welded to the bottom plate and forming an adiabatic gap with the inner tube.
【請求項2】 加熱タンクおよび該加熱タンクから上方
に延設された中濃度吸収液仕切筒、および該中濃度吸収
液仕切筒の外周に配された冷媒蒸気回収筒を有する高温
再生器と、 前記冷媒蒸気回収筒の外周に設けられた縦型円筒状の低
温再生器ケースと、 前記低温再生器ケースの外周に配された縦型円筒状の蒸
発・吸収ケースと、 前記蒸発・吸収ケースの上方に配された凝縮器ケース
と、 前記冷媒蒸気回収筒、低温再生器ケース、および蒸発・
吸収ケースの下端に溶接された底板とを有する吸収式冷
凍装置の再生器において、 前記冷媒蒸気回収筒の底部の近傍の前記中濃度吸収液仕
切筒の内周壁に断熱層を形成したことを特徴とする再生
器。
A high-temperature regenerator having a heating tank, a medium-concentration absorbent partition extending upward from the heating tank, and a refrigerant vapor recovery cylinder disposed on the outer periphery of the medium-concentration absorbent partition; A vertical cylindrical low-temperature regenerator case provided on the outer periphery of the refrigerant vapor recovery cylinder; a vertical cylindrical evaporator / absorber case disposed on the outer periphery of the low-temperature regenerator case; A condenser case disposed above, the refrigerant vapor recovery cylinder, a low-temperature regenerator case, and an evaporator
In a regenerator of an absorption refrigerating apparatus having a bottom plate welded to a lower end of an absorption case, a heat insulating layer is formed on an inner peripheral wall of the medium concentration absorption liquid partition near a bottom of the refrigerant vapor recovery cylinder. And a regenerator.
【請求項3】 請求項2において、前記断熱層は、樹脂
層であることを特徴とする再生器。
3. The regenerator according to claim 2, wherein the heat insulating layer is a resin layer.
JP7219951A 1995-08-29 1995-08-29 Regenerator for absorption refrigeration system Expired - Fee Related JP2957112B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7219951A JP2957112B2 (en) 1995-08-29 1995-08-29 Regenerator for absorption refrigeration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7219951A JP2957112B2 (en) 1995-08-29 1995-08-29 Regenerator for absorption refrigeration system

Publications (2)

Publication Number Publication Date
JPH0961011A JPH0961011A (en) 1997-03-07
JP2957112B2 true JP2957112B2 (en) 1999-10-04

Family

ID=16743602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7219951A Expired - Fee Related JP2957112B2 (en) 1995-08-29 1995-08-29 Regenerator for absorption refrigeration system

Country Status (1)

Country Link
JP (1) JP2957112B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5903548B2 (en) * 2011-04-22 2016-04-13 パナソニックIpマネジメント株式会社 COOLING DEVICE, ELECTRONIC DEVICE WITH THE SAME, AND ELECTRIC CAR

Also Published As

Publication number Publication date
JPH0961011A (en) 1997-03-07

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