JPS59501279A - Power unit for absorption heat exchange system - Google Patents

Power unit for absorption heat exchange system

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Publication number
JPS59501279A
JPS59501279A JP58502624A JP50262483A JPS59501279A JP S59501279 A JPS59501279 A JP S59501279A JP 58502624 A JP58502624 A JP 58502624A JP 50262483 A JP50262483 A JP 50262483A JP S59501279 A JPS59501279 A JP S59501279A
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JP
Japan
Prior art keywords
power unit
chamber
pipe
wall
reservoir
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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.)
Pending
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JP58502624A
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Japanese (ja)
Inventor
ウイルキンソン・ウイリアム・エツチ
Original Assignee
バッテル・メモリアル・インステイチュ−ト
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Application filed by バッテル・メモリアル・インステイチュ−ト filed Critical バッテル・メモリアル・インステイチュ−ト
Priority claimed from PCT/US1983/001056 external-priority patent/WO1984000413A1/en
Publication of JPS59501279A publication Critical patent/JPS59501279A/en
Pending legal-status Critical Current

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    • 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

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 吸収熱交換システム用パワーユニット 技術分野 本発明は吸収熱交換/ステム用の、発生器と凝縮器とを組み合わせたパワーユニ ット、て関する。より詳しくは、本発明(I′i吸収ヒートボノプシステムある いは吸収冷凍システムのいづれかと共に使用する装置に関する。[Detailed description of the invention] Power unit for absorption heat exchange system Technical field The present invention provides a combined generator and condenser power unit for absorption heat exchange/stem. Regarding the cut. More specifically, the present invention (I'i absorption heat bonop system) or an apparatus for use with any absorption refrigeration system.

本装置は垂直方向の中央パイプを囲む、複数の共@線関係に位置したパイプを含 む。各パイプは中央パイプを囲む次のチャンバと隣接する環状のチャンバを形成 するに十分、中心Sがら漸次大きくされている。AiJ記チャ/ハは中央パイプ ならび(C該パイプを囲む複数のパイプVこ接続された部材(/二よって上端お よびF端で閉鎖されている。中央パイプの内部へ熱を提供するよう襖ふり1位1 値しでいるっ直径が最大のハ゛イブの外面をて冷却流体が接月虫する。Lうic −g−る装置か設けられている。チャツバの内壁上の吸収剤から冷媒全脱着し、 チャンバ・′り外鍔上の冷媒テ、疑耀するよう環状チャンバの内壁・\冷媒と吸 収剤力)らなる1、@液全排ITする装置も設(ケられている。吸収熱交換/ス テムの適尚な9素へ循環下るよう、?分課と吸収剤がしなる@仮と1脅媒とか別 ・−にチャツバの底部で集められる。っ王として、化学浴液の種々の濃度間にお ける熱交換により作動する吸収冷凍/ステムにおいては、伝熱速度と、伝熱効率 とか極めて重要である。//+凍化学薬剤か搬送される装置の形態を変えること が当該/ステムにおける伝熱速度や伝熱効率に重要な影響をも1こらす。The device includes a plurality of co-located pipes surrounding a vertical central pipe. nothing. Each pipe forms an annular chamber adjacent to the next chamber surrounding the central pipe The center S is gradually enlarged to the extent that it is sufficient to do so. AiJkicha/ha is the central pipe and (C a plurality of pipes surrounding the pipe V) connected members (/2, so the upper end and and closed at the F end. Fusumafuri 1st 1 to provide heat to the inside of the central pipe The cooling fluid engrafts the outer surface of the hive with the largest possible diameter. Lic -g- equipment is provided. The refrigerant is completely desorbed from the absorbent on the inner wall of the chatuba, It is suspected that the refrigerant on the outer rim of the chamber is absorbed by the refrigerant on the inner wall of the annular chamber. 1. A device for completely discharging the liquid is also installed. Absorption heat exchange/steam So that it circulates down to the appropriate 9 elements of tem? Division and absorbent are flexible @kari and 1 threat medium and other -Collected at the bottom of the chatuba. As a general rule, there are differences between various concentrations of chemical bath solutions. In absorption refrigeration systems that operate by heat exchange, the heat transfer rate and heat transfer efficiency are It is extremely important. //+Changing the form of the device in which the cryochemical agent is transported This also has an important effect on the heat transfer rate and heat transfer efficiency in the stem.

伝統的に、吸収冷凍システムにおいては、発生器かリザーバ全含み、該リザーバ において、冷媒浴液ペアj才、チュー)に熱を通すか、あるいはリザーバの容器 の底部や側部に熱を加えることにより熱か力口えられる。ロース他(Lowet h et c、l lの米圃侍許第3.495,420号は吸収7ステム用の典 型的な装置を示している。Traditionally, in absorption refrigeration systems, either the generator or the reservoir is fully contained; In a refrigerant bath, heat is passed through a pair of refrigerant baths, or in a reservoir container. Heat can be removed by applying heat to the bottom or sides of the device. Lowet et al. U.S. Farm Bureau Permit No. 3.495,420 for h,etc,l is the standard for absorption 7 stems. It shows a typical device.

1だ、mJ記特許しては、リザーバ状の凝、湘器か隣接隔置位置(で設けられて いる。発生器のチャンバ(てお・いて冷媒は然発し、1疑陥器チヤン・\へ運ば れるっこの従来のシステム!/I:お−いては、発生器に加えら汎た熱は著しく 無駄にさ几、リザーバ内の浴液の大部分(て対して効率よく供給さ几ない。同様 (′i:、凝嬬器に対する冷却も有効に使用さ本発明の説明において、パワーユ ニット金出入りする、容器を明確(て区別することか重要である。し1こがって 、不明能書で・は、米国に寂C・する吸収/ステム【関する規格設定団体である 、吸収磯熾に関するA 5IiRAE枝術委員会(8,31(ASHRAE T echnical Convnittee 07+A、bsorption M ac1日、ves’Jの表示を採用する。それらの表示1j: A、5HRAE の1979年度7版設備便覧(Equip−m、eηt Handbookl  14章からの以下の引用に示されている。1, MJ's patent states that a reservoir-like condensate is provided in an adjacent spaced position. There is. The refrigerant spontaneously emitted from the generator chamber and was transported to the suspect chamber. Reruko's traditional system! /I: In some cases, the heat added to the generator is significant. Most of the bath liquid in the reservoir is wasted (as opposed to being efficiently supplied). ('i: Cooling of the condenser is also effectively used. In the description of the present invention, the power unit is It is important to clearly distinguish the container where the knitted gold goes in and out. , in an unknown document, is a standard-setting organization related to absorption/stem , A5IiRAE Branch Committee on Absorption (8, 31 (ASHRAE T electrical Convnittee 07+A, bsorption M On the ac1st day, the display of ves'J is adopted. Their display 1j: A, 5HRAE 1979 7th Edition Equipment Handbook (Equip-m, eηt Handbook) This is illustrated in the following quotation from Chapter 14:

[吸収技術分野にお(げろ用語の困乱を避ける1こめに、ASHRAE技術委員 会8.3は吸収剤−冷媒浴液に対して以下の標準用語を推奨する。薄い吸収剤と は吸収器内で冷媒を吸収ずみで、冷媒に対する親和力の弱い@液である。濃い吸 収剤とは発生器において冷媒を放出ずみなので4冷媒に対する親和力の強い浴液 である」 ハツチM記念研究所(Battelle Memorial In5ti−1u te)の子会社であるハツチlし開発会社<BattelleDevelopm ent Corporationlに譲渡さ、aた、1980手8月31日出願 の%願第177,695号において、吸収システムにおいて、熱交換器の形態に ょる貢1駄を指向した改良が開示されている。前記開示お裏ひその延長、あるい は部分的な延長のいづれかを本明細書では参考として一部採用している。[In order to avoid the confusion of terminology in the field of absorption technology, ASHRAE technical committee member Society 8.3 recommends the following standard terminology for absorbent-refrigerant bath liquids: with thin absorbent has already absorbed the refrigerant in the absorber and is a @liquid with a weak affinity for the refrigerant. thick suction Absorbent is a bath liquid that has a strong affinity for the 4 refrigerants because it has already released the refrigerant in the generator. is” Battelle Memorial Institute (In5ti-1u) Battelle Development is a subsidiary of Battelle Develop. Assigned to Ent Corporation, filed on August 31, 1980. No. 177,695, in the form of a heat exchanger in an absorption system. Improvements are disclosed that are aimed at reducing the burden on customers. An extension of the above-mentioned disclosure secrets, or Any of the partial extensions are hereby incorporated in part by reference.

本発明は吸収システムにおける熱又換装置の改良である。本発明においては、発 生器および凝縮器は本明細書で「パワーユニット」と称する単段あるいは多段ユ ニットとして組み合わさ1ている。このパワーユニットトイう呼称の由来は高温 (駆動)エネルギが供給される、システムの高圧側にある冷凍システムの二種類 の要素7!:組み合せたことに関係する。蒸発器および吸収器全音む、当該シス テムの他の部分は相対的に低圧で作動する。The present invention is an improvement to a heat exchanger in an absorption system. In the present invention, The generator and condenser may be a single-stage or multi-stage unit, referred to herein as a "power unit". It is combined as a knit. The origin of the name “power unit toy” is high temperature. Two types of refrigeration systems, on the high pressure side of the system, where (driving) energy is supplied Element 7! :Relates to a combination. evaporator and absorber, the system Other parts of the system operate at relatively low pressures.

本発明の目的は発生器と凝縮器とを、−万の作動部分が他方の作動部分全形成し 、一方の熱伝導が龍万の熱伝導と一体となるように一部を他方と一体化するよう 組み4 1)[59−50127’1(3)合わせる装置と構造の形態を提供す ることである。本発明の別の目的は、配置と構造を簡素化することに、r、す、 最小のヌペースとコストで適度の伝熱効率を提供するようパワーユニットを多段 化するこさである。The object of the invention is to combine a generator and a condenser in such a way that one working part forms the entire working part of the other. , so that one part is integrated with the other so that the heat conduction on one side is integrated with the heat conduction on the other side. Combination 4 1) [59-50127'1 (3) Providing the form of the combining device and structure Is Rukoto. Another object of the invention is to simplify the arrangement and structure of r, s, Multi-stage power unit to provide moderate heat transfer efficiency with minimum space and cost It is difficult to change.

本発明のその1mの特徴や目的は以下の図面ならびに説明および請求の範囲から 明らかとなるう図面の簡単な説明 第1図は典型的な従来技術に↓る吸収冷凍システムにおいて本発明を実施した概 略図、 第2図は本発明iCよる装置の部分断側面図、第3図は第2図の平面3−3から みた断平面図である。The features and objects of this invention can be understood from the following drawings, description and claims. A brief explanation of the drawing that will be clear Figure 1 shows an overview of the present invention implemented in a typical prior art absorption refrigeration system. Schematic diagram, FIG. 2 is a partially sectional side view of the device according to the invention iC, and FIG. 3 is taken from the plane 3-3 of FIG. FIG.

本発明を実施する最良の形態 第1図を参照すれば、発生器11、凝縮器12、蒸発器13、膨張弁14、吸収 器15、ポンプ16、お工び護熱器17を含む、従来の吸収冷凍/力ロ熱システ ム1゜が概シロ図示されている。本発明によるパワーユニットは従来のシステム 10iCi−ける発生器11と1凝縮器12の@能を夫施し、かつm人台わせる 。点緋が、パワーユニット30に組み合わさ几た該システム1oの部分を囲む。BEST MODE FOR CARRYING OUT THE INVENTION Referring to FIG. 1, a generator 11, a condenser 12, an evaporator 13, an expansion valve 14, an absorber A conventional absorption refrigeration/forced heat system including 1° is shown schematically. The power unit according to the invention is similar to the conventional system. A generator 11 and a condenser 12 capable of generating 10 iCi are used, and m people are installed. . A dotted scarlet surrounds the part of the system 1o that is combined with the power unit 30.

従来の吸収710熱/R却システムの作動は周矧であって、そ几以上の説明はほ とんど要しない。典型的な7ステムにおいては、水が、度々「浴液ペア」と亦窟 れる、臭化リチウムと水との@液中に分解した(ダ媒でちる。水(は該システム を通して種々の度合で臭化リチウム溶液中に吸収され、加熱および冷却幼果を提 供するよう吸収熱が添加されたり抽出され1こ9する。The operation of the conventional absorption 710 heat/R-rejection system is so detailed that little further explanation is necessary. I don't really need it. In a typical 7 stem, water is often combined with a "bath liquid pair". It is decomposed into a liquid of lithium bromide and water. is absorbed into the lithium bromide solution to varying degrees through the heating and cooling of the young fruit. Absorbed heat is added or extracted to serve the purpose.

溶液ペアは導管20を介して発生器へ入りそこで熱を加えられる。供給された熱 が蓄圧し、冷媒の水を蒸気の形で脱着し、該蒸気は配管23を介して凝縮器12 へ送られる。そこで、外気の冷却により水蒸気を液体に凝縮し、液体は配管22 と膨張弁14を介して送られ、蒸発器13で熱が吸収される。冷凍システムに2 いては、蒸発器13で吸収される熱は4卸負荷からのものである。The solution pair enters the generator via conduit 20 where it is heated. heat supplied accumulates pressure, desorbs the refrigerant water in the form of steam, and the steam passes through the pipe 23 to the condenser 12. sent to. Therefore, the water vapor is condensed into liquid by cooling the outside air, and the liquid is transferred to the pipe 22. The heat is sent through the expansion valve 14, and the heat is absorbed by the evaporator 13. 2 for the refrigeration system In this case, the heat absorbed by the evaporator 13 is from four loads.

低圧蒸気は配管24を通して吸収器15へ送られ、そこで大気の冷却により臭化 リチウム溶液が水蒸気を脱着できる。次いで、浴液ペアはポンプ16により復熱 器17へ送られる。復熱器は対流交換器であって、配管18を介して発生器11 から送られてくる吸収剤の臭化リチウムが配管19を介して吸収器15への途中 で浴液ペアを加熱する。The low-pressure steam is sent through pipe 24 to absorber 15, where it is brominated by atmospheric cooling. Lithium solutions can desorb water vapor. Next, the bath liquid pair is recuperated by the pump 16. It is sent to the container 17. The recuperator is a convection exchanger, which connects the generator 11 via piping 18. Lithium bromide, an absorbent sent from the Heat the bath solution pair.

加熱サイクル((おいては、吸収器15および(11こは)凝縮器12で供給さ れた冷却作用が加熱負荷であるっ第2図を参照すれば、本発明による燃焼管式の 吸収パワーユニットは、垂直方向の「燃焼室」の中央柱状パイプ部材31を含み 、該部材31は、典型的にはパルス燃焼器である熱源33か貫通して突出する、 弁軸線関係の開口を備えた端板32を下端で有する。第2の柱状パイプ部材34 が弁軸線関係で前記の中央パイプ部材31を囲んで、1=−9、前記パイプ部材 34は、上端の、外方に延び、半径方向に位置した閉鎖プレート35と、類似の 下端閉鎖プレート36 &てより中央の柱状パイプ部材31の外面に接続され、 第1の環状脱着チャンバ37を形成している。The heating cycle (in which the absorber 15 and (11) are supplied by the condenser 12) The cooling effect of the combustion tube type according to the present invention is a heating load. The absorption power unit includes a vertical "combustion chamber" central columnar pipe member 31. , the member 31 projects through a heat source 33, typically a pulse combustor. It has an end plate 32 at its lower end with an opening in relation to the valve axis. Second columnar pipe member 34 surrounds the central pipe member 31 in relation to the valve axis, 1=-9, the pipe member 34 has a top, outwardly extending, radially located closure plate 35 and a similar The lower end closing plate 36 & the end are connected to the outer surface of the central columnar pipe member 31, A first annular desorption chamber 37 is formed.

本発明を構成する各種要素は概ね共@線関係に配置され、「内側」と称する部材 は中心@線に対してより近接した1則のものである。The various elements constituting the present invention are generally arranged in a co-linear relationship, and are referred to as "inner" members. is a law closer to the center @ line.

ワツンヤ状の上端閉鎖プレート35は、導管20を介して復熱器17からの冷媒 と吸収41の溶液21を通す開口を有する。導管20の端部にあるペンド38あ るいはその他の装置により冷媒と吸収剤の溶液21が中央の柱状パイプ部材31 の外面へ拡散する。下端の閉鎖プレート36には仕切40が設けられ、該仕切4 0か環状チャンバ37の底部を内側リザーバ41と外−II ’Jザーハ42に 分割する。The upper end closing plate 35 in the shape of a bow allows the refrigerant from the recuperator 17 to flow through the conduit 20. and an opening through which the solution 21 of the absorption 41 passes. Pend 38 at the end of conduit 20 The refrigerant and absorbent solution 21 is transferred to the central columnar pipe member 31 by using another device. diffuses to the outer surface of the The closure plate 36 at the lower end is provided with a partition 40 , the partition 4 0 or the bottom of the annular chamber 37 into the inner reservoir 41 and the outer-II 'J Zaha 42 To divide.

別の上端の外方、C延ひ、半径方向に位置した閉鎖プレート45と、類似の下端 の閉鎖プレー)46tζより第3の柱状パイプ部材44が第2の柱状パイプ部材 34を共融線方向に囲んで取り付けられており、第2の環状脱着チャンバ47を 形成する。上端の閉鎖プレート45は、チャンバ47をチャンバ37の内側リザ ーバ41に接続する導管48が通過する開口を有する。ある場合には、ポンプ4 3((よってチャンバ間の差圧が上昇し、導管48内の部分的に濃くされた冷媒 と吸収剤の溶液を上昇させる。チャンバ47内の導管48の上端にあるベンド4 9あるいはその他の装置が、内側リザーノX41からの部分的に濃くされたtや 媒と吸収剤との浴液を第2のバイブ部材34の外面50上に拡散させる。a C-extending, radially located closure plate 45 outwardly of another upper end and a similar lower end; (closing play) From 46tζ, the third columnar pipe member 44 is the second columnar pipe member 34 in the eutectic line direction, and is attached to the second annular desorption chamber 47. Form. A closure plate 45 at the top end closes the chamber 47 to the inner reservoir of the chamber 37. It has an opening through which a conduit 48 connecting to the server 41 passes. In some cases, pump 4 3((Thus the differential pressure between the chambers increases and the partially enriched refrigerant in conduit 48 and rise the absorbent solution. Bend 4 at the upper end of conduit 48 in chamber 47 9 or other devices may be used to detect partially darkened t or A bath of medium and absorbent is diffused onto the outer surface 50 of the second vibrator member 34 .

チャンバ47の下端閉鎖プレート46も仕切53により同様(で内部1の環状リ ザーバ51と外“叫の環状リザーバ52v′C分割さ。1する。導管18が内側 リザーバ51を復熱器17に接子させる。チャツバ37の外側リザーバ42とチ ャンバ47の外用リザーバ52とは減圧装置94と導管22により相互に接侵さ れ、次いで導管92により膨張4f14に接侵されている。The lower end closing plate 46 of the chamber 47 is also closed by the partition 53 (and the annular ring of the interior 1 The reservoir 51 and the external annular reservoir 52v'C are divided.1.The conduit 18 is inside The reservoir 51 is attached to the recuperator 17. Chatuba 37 outer reservoir 42 and chi The external reservoir 52 of the chamber 47 is in mutual contact with the pressure reducing device 94 and the conduit 22. The conduit 92 then penetrates the expansion 4f14.

第3の柱状バイブ部材44の外面(では、例えばフィン55のような複式の輻射 面を設けることができる。The outer surface of the third columnar vibe member 44 (for example, A surface can be provided.

チーヤ/・\37の内部の中央の柱状パイプ部材31の表面39には全体的に半 1万同に位置し、外方、かつ上方に突13した面:う延長部材か取す付りすら汎 で2す、該部材は基本′3−. L/C、、突起56を形成するスリットを一汀 する。同様に、第2の柱状・くイブ部材の面50上で、チャンバ!47の内部に は全体旧Qζ半匝方同・、・口位置し、外方かつ上方に突出した間延長部材、即 ち突起56か取9けけられている。The surface 39 of the central columnar pipe member 31 inside the A surface located at 13 points and protruding outward and upwards: Even the attachment of the extension member is universal. 2, the member is basically '3-. L/C, the slit that forms the protrusion 56 do. Similarly, on the surface 50 of the second columnar/squive member, the chamber! Inside 47 The whole old Qζ is located in the same way, and the extension member protrudes outward and upward. There are 56 protrusions and 9 holes.

図示の好適実施1夕1]にあ・いては、前記の間延長部材5Gはチャツバ37. 47の1部近くに取りけけられ、仕切40.53の近ぐ1でそ几ぞnらせん状に 中央および第2の柱状パイプ部材の周りに巻かれている。別の構造においては、 フィン(まパイプの壁自体から削り出してもよい。In the illustrated preferred embodiment 1/1], the above-mentioned space extension member 5G is the chatuba 37. It is installed near part 47, and it is arranged in a spiral shape near partition 40.53. It is wrapped around the central and second columnar pipe members. In another structure, Fins (may also be carved from the pipe wall itself).

本発明の典型的な作動において・1才、パルス燃焼器の焔が中央のパイプ部材3 ]の内側あるいは下方で燃現し、パイプを高温1で加熱する。復熱器17から冷 媒/吸収剤6液21が導管20を介してチャンバ、37へ、そして外面39上へ 導入さ汎ると、@改21干の水成方が脱着さ几、分離して蒸気となり、次いで第 2のパイプ部材34の低温面上で凝゛遁する。面ラエ長部材56.ま加熱面を1 膨張させ、薄いフィルム状から水(!:冷媒を極めて効果的VC蒸発しやすくす る。In a typical operation of the present invention, when the flame of the pulse combustor is 1 year old, the flame of the pulse combustor is ] and heats the pipe to a high temperature of 1. Cold from recuperator 17 Medium/absorbent 6 liquid 21 is passed through conduit 20 to chamber 37 and onto external surface 39. When it is widely introduced, the water of @kai21dried is desorbed, separated and becomes steam, and then the second It condenses on the cold surface of the pipe member 34 of No. 2. Surface length member 56. The heating surface is 1 It expands and transforms the water (!: refrigerant into a thin film) into an extremely effective VC, making it easier to evaporate. Ru.

浴液21はリザーバ41(て集められる壕で、面39と突起56に沿って下方へ 徐々:て流nるにつれて〆1媒が薄くなる。濃くさ、7′L1こ溶液は導管48 、入口49そ介して面50上・\汲み上げられ、そこから下方−\、かつオ]の 突起56上そ流几る。脱着つ5行わ几、水蒸気つ)放出されて、リザーバ51に 集められさら(C塵くさユに、容(沙から出ていく。今や濃くされた水と臭化リ チウム5r)@孜(・寸導管18、復熱S17、配管19そ介して説屑器]5へ 2里ば几る。The bath liquid 21 is collected in a reservoir 41 and flows downward along the surface 39 and the protrusion 56. Gradually: The first medium becomes thinner as it flows. Concentration, 7'L1 This solution is conduit 48 , is pumped up through the inlet 49 onto the surface 50, and from there downward -\, katsuo] The protrusion 56 flows upwardly. After the desorption process is carried out, water vapor is released into the reservoir 51. The water and bromide solution are now thickened and the water and bromide are collected. Chiumu 5r) @ Kei (・Dimension pipe 18, recuperation S17, pipe 19 and explanation waste container] Go to 5 It takes 2 ri.

前述の尤う((、チャツバ37と・17で脱着が行われている間、第2のパイプ 34の内壁と第3のパイプ44の内壁は説着か行われている反対側の壁や突起上 りも冷1こいため、それらの内壁上で凝縮が同時に行わ肚る。冷却作用源は、面 延長フィン55を備え1こ第3のパイプ44の外壁である。大気、ある”のはあ る場合(lこは、ンヤクソト(図示せずフ内のg状冷却剤(例えば水)がフィン 55と壁に近接、かつ接触して通され、ノでワーユニット30の中心から熱を徐 々に外方へ抽出するつ凝縮が行われるにつれて、水がチャツバ37.47の外壁 上を流下し、それぞれ外1ull リザーzX42と52こ集められ、そこから 導管22.92を介して膨張弁14へ運ばれる。While the above-mentioned ((, Chatuba 37 and ・17) are being attached and detached, the second pipe The inner wall of pipe 34 and the inner wall of third pipe 44 are connected to the wall or protrusion on the opposite side where the persuasion is being performed. Since the walls are also cold, condensation occurs simultaneously on their inner walls. The cooling source is The outer wall of the third pipe 44 is provided with an extension fin 55. There is an atmosphere (In this case, if the coolant (e.g. water) in the fin (not shown) is 55 and in close contact with the wall, the heat is removed from the center of the warping unit 30. As the water is extracted outwards and condensed, the water builds up on the outer walls of the chatuba. Flowing down from above, 1ull of lither zX42 and 52 were collected, and from there It is conveyed to the expansion valve 14 via conduit 22.92.

%トンの/争凍駆力を1共するよう、吸収熱交換/ステムで溝底、かつ作動しつ る典型的な図示パワーユニットにおける特徴は以下の通りである。In order to share the freezing driving force of % tons, the absorption heat exchanger/stem is installed at the bottom of the groove and continues to operate. Features of a typical illustrated power unit are as follows.

中上・バ′イブー1905ミリ(菟インチ)の440(外径17.15ミリ(0 ,675イノチ)−内径12.52ミリ(0,493インチ))第2のパイプ− 31,50ミリ(11Aインチ)の≠40(外年4216ミリ(166イノナ) −内作35.05ミリ(1,:38インチ))第3のパイプ−63,5ミ’J( 1’;インチ)チューフッ′14ゲージ(外径635ミリ(2,5インチツー内 径59.28ミリ(2,334イノチラ) 閉鎖部材の間におけるパイプの長さ−1,7メートル(5,5フイート) このパワーユニット30へは、臭[ヒリチウムの濃度か58己4%の臭化リチウ ム7/水の薄い溶液が、約155.6℃(312下)の温度で中上・/クイズ3 1の外面39へ送0 人される。この薄い・@液は面延長部斑56上を流下し、約166.7℃(33 2下)の温度で、臭化リチウムの濃度が60%%1で部分的して濃くされて、リ ザーノス41を介してチャンバ37から出ていくつ第2(つ/ぐイブ34の内壁 上で水の凝縮物が集1す、約107.8°C(226”置の温度で導管22を介 して底部6て分いてリサー/12を介してチャフ〕・37から出てのく。部分的 Cで濃くされた臭化リチウム溶液(ま(濃度臭化リチウー60”/ 、% 0− F tで)約90℃(194下)の温度で渠2のノぐイブ347)外壁50へ導 管48を介して運ばnる。面砥長部材56を流下した後、濃い浴液(ま、約94 4℃t 202 ’F )の温度で、かつ臭化リチウム畏1i62.1%で底部 に設けた導管18を介してリザー・\51を通ってチャン/X47 :6−ら出 ていくつこの時、帳(、でお【ハて;ま磐、夜、、ま児童iて脱着さ几1こ儂い 浴液である。【影陥物(ζ7に〕43.3℃(110°F)0温度て第3のパイ プ44の内壁上に桑めら1′LX底部01ノザーハ52を通して、導管92を介 してチマノノ\47カ)ら出ていく。冷却水か、rり却フィン55を含む第3の ノ〈イブ44の外側を、約29.4℃(85下)の温度で循環する。Nakagami/Ba'ibu 1905 mm (菟inch) 440 (outer diameter 17.15 mm (0 , 675 inch) - inner diameter 12.52 mm (0,493 inch)) second pipe - 31,50 mm (11 A inch) ≠ 40 (4216 mm (166 Inona)) - Internally made 35.05 mm (1,:38 inch)) Third pipe - 63,5 mm (38 inches) 1' inch) Chufu '14 gauge (outer diameter 635 mm (2.5 inch inner diameter) Diameter 59.28 mm (2,334 millimeters) Length of pipe between closure members - 1.7 meters (5.5 feet) This power unit 30 is supplied with an odor [the concentration of lithium is 58% and 4% lithium bromide]. Mu7/A dilute solution of water is at a temperature of about 155.6°C (below 312)./Quiz 3 0 to the outer surface 39 of 1 Become a person. This thin @ liquid flows down on the surface extension part spot 56 and is approximately 166.7°C (33°C). At a temperature of 2), the concentration of lithium bromide is partially concentrated to 60%%1, The inner wall of the second tube 34 exits from the chamber 37 via the Water condensate collects at the top of the pipe 22 at a temperature of about 107.8°C Then it separates from the bottom part 6 and comes out from the chaff]・37 via the ricer/12. Partial Lithium bromide solution (concentration lithium bromide 60”/ , % 0- Ft) at a temperature of approximately 90°C (below 194), the pipe 2's nog 347) is guided to the outer wall 50. Conveyed via tube 48. After flowing down the surface polishing member 56, a thick bath liquid (approx. At a temperature of 4°C 202'F), and at a temperature of 62.1% of lithium bromide, the bottom It passes through the reservoir \51 through the conduit 18 provided in the At this time, at night, the child was wearing and undressing for just a little while. It is a bath liquid. [Shadow object (on ζ7]) 43.3℃ (110℃) 3rd pie at 0 temperature Pass the mulberry plate 1'LX bottom part 01 nose plate 52 onto the inner wall of the pipe 44 and connect it via the conduit 92. Then Chimanono \47ka) and others left. The cooling water or the third The outside of the nozzle 44 is circulated at a temperature of about 29.4° C. (below 85° C.).

チャンバ47を出ていく爵、夜の2畳度は第2.ス古第3図に示す2段式パワー ユニットにおいて臭でヒリチウム濃度か58%%から62.1%ぽで増加してい る。つこのことは、この程度の寸度と容量の吸収装置に2し^て□・ま例外的に 貝好なものと考えられる。The duke leaves chamber 47, and the night is 2 tatami degrees. Two-stage power shown in Figure 3 In the unit, the concentration of hylithium increased from 58% to 62.1% due to odor. Ru. This is exceptionally true for an absorber of this size and capacity. It is considered to be a shellfish.

11 本発明によるパワーユニットの共軸線関係の密閉構造はスペースとエイ・ルギの 節約上特に効率的、かつ効果的であることが判る。熱は密閉スペース内で発生す るので唯一の逃げは構造体の外部に向かってであって、(全ての燃焼系統に2け る損失である頂部を通しての排出以外)熱は有利に使用でさる。逆にいえば、冷 却作用のための最大面積が外側パイプ44とフィン55の周りから得られる。11 The coaxial line-related sealed structure of the power unit according to the present invention saves space and energy. It turns out to be particularly efficient and effective in terms of savings. Heat is generated in confined spaces. The only escape is towards the outside of the structure (2-key for all combustion systems). The heat can be advantageously used (other than exhaust through the top, which is a loss of energy). Conversely, cold The maximum area for cooling is available around the outer pipe 44 and fins 55.

本発明による装置は、各種の主要パイプ、チャンバおよびチャンバの壁の中心@ 線が垂耳位置で示さnている。The device according to the invention can be applied to various main pipes, chambers and the center of the walls of the chamber @ The line is shown in the floppy position.

この概ね垂直位置において装置ならひにシステムは最も効果的に作動するものと 考えられている。しかしながら、甲ノし細線か垂直方向に対して傾斜するにつわ て、システムの作動はその効率性が徐々(・て下がることを理屏丁べきである。The equipment system operates most effectively in this generally vertical position. It is considered. However, when the instep line is slanted to the vertical direction, Therefore, the operation of the system should be subject to a gradual decline in its efficiency.

ある傾斜位置に2いては、下側での脱着と・凝縮2よび上側のこの脱着と凝縮と がかけ離れることによってそれらの作用を1代下させ、装置の作動効率を低下さ せる。前述のような傾斜度を決定することは、当該技術分野における専問家の経 常的な実験上の問題であって、本発明は使用者側に容認される程度1で垂直方向 に対して傾斜した7ステムも包含し、かつ適用される意図である。At a certain inclined position 2, the desorption and condensation on the lower side and this desorption and condensation on the upper side occur. If the values are far apart, their effects will be lowered by one generation, and the operating efficiency of the device will be reduced. let Determining the slope as described above is a matter of experience for experts in the field. As a matter of routine experimentation, the present invention is capable of 7 stems angled relative to the 7 stems are also intended to be included and applied.

柱状パイプと環状チャツバを使用した形態は構造が簡単であって、例えば各接接 続し1こ鋼パイプのような一般に入手可能か、製作さ九る材料で簡単に製作され る。・らせん状に巻かれ・1こ面・延長部材、5.6は環状チャンノ′X37. 47のスペースを利用する上で特に有効である。The configuration using columnar pipes and circular chatuba has a simple structure, for example, each connection Easily fabricated from commonly available or fabricated materials such as continuous steel pipe. Ru.・Wound in a spiral shape・One side・Extension member, 5.6 is an annular channel X37. This is particularly effective in utilizing 47 spaces.

間延長部材を備えた独特の共畑線関係の形態のために、延長部材の蒸発面と、チ ャンバの外壁の凝縮面との間の蒸気の移動距離は均一で極めて短い。このため、 この形式の装置の熱効率を向上させる。Due to the unique form of co-field line relationship with the extension member, the evaporation surface of the extension member and the chi The distance traveled by the vapor to and from the condensing surface of the outer wall of the chamber is uniform and very short. For this reason, Improves the thermal efficiency of this type of equipment.

前記の形態のために、パルス燃焼器33の形態で、例外的に高度の熱入力を典型 的に提供できる。この手段により、パワーユニットの中心で驚くべきほどの高温 を発生させることができ、パワーユニットは冷却作用を行う該ユニット7)周囲 を用いて効果的に取扱うことができる。Due to the configuration described above, an exceptionally high heat input is typical in the form of a pulse combustor 33. can be provided. By this means, surprisingly high temperatures can be achieved at the center of the power unit. 7) Surroundings of the unit can be effectively handled using

また、前記の形態とその伝熱効率の良さのため、ホットスポットつ問題が排除さ れるか、最小とされる。この種の装置に2いて:は、高伝熱速度を試み1こ場合 、脱着工程VC>いて沸騰が起ることは稀で;まない。臭化リチウム2よひその 他典型的な浴rLを使用して沸騰が起ると、伝熱面シでわ1こり撹拌や、温度差 が発生する。・これら「ホットスポット」は全体の効率を低下させ、慈父換器が つくられている材料に悪影響を与える高度に腐蝕性の雰囲気をつくる。1だ、ホ ットスポットは溶y、を結晶化させ、通路を詰らせたり、装置の作動を1今止さ せる。Also, due to the above-mentioned morphology and its good heat transfer efficiency, hot spot problems are eliminated. or minimized. 2. In this type of equipment: try high heat transfer rate 1. , boiling rarely occurs during the desorption process. Lithium bromide 2 If boiling occurs using a typical bath rL, the heat transfer surface may become wrinkled, stirring may occur, or temperature differences may occur. occurs.・These “hot spots” reduce overall efficiency and reduce the Creates a highly corrosive atmosphere that adversely affects the materials of which it is made. 1, ho Spots can crystallize molten fluid, which can clog passageways or stop equipment from working. let

本発明による装置においては、@液ペアがチャンバの内面のらせん状の壁を流下 するにつ几て最高温の点に導液ペア刀S徐々に近づくためホットスポットは排除 される。In the device according to the invention, the @liquid pair flows down the helical wall of the inner surface of the chamber. Hot spots are eliminated as the liquid guiding pair sword S gradually approaches the point with the highest temperature. be done.

本発明による装置は、多段吸収冷凍システムにおける発生器と凝羅器とを、各々 の云熱壁が他方の極めて効率的な成分として作用する1個の「パワーユニット」 へ組み合わせることが判る。The device according to the present invention is a device for each of the generator and condenser in a multi-stage absorption refrigeration system. One "power unit" in which one thermal wall acts as a highly efficient component of the other. It turns out that it can be combined with

本明細書で図示し、かつ説明した本発明の典型的な好適実施例は2段式のユニッ トである。本発明の概念を利用して、内用1[パイプ31と外側パイプ44との 間に、別の段階を共軸線関係で追加することができる。追加の各段階は当該シス テムの高圧側において@液と−り媒の分離を増すことにより該システムの効率を 向上させる機会を提供する。The exemplary preferred embodiment of the invention illustrated and described herein is a two-stage unit. It is. Utilizing the concept of the present invention, internal use 1 [pipe 31 and outer pipe 44] In between, another stage can be added in coaxial relationship. Each additional step is Increase the efficiency of the system by increasing the separation of liquid and medium on the high pressure side of the system. Provide opportunities to improve.

本発明の好適実施例を不明!wB書において説明してきたが、本発明の基本をな す基本原理から逸脱すうことなく、図示し、かつ説明し1こ構造において種々の 変更、修正か可能なことか理解される。し1こかって、この種の変更や修正は、 請求の範囲あるいは合理的なその均等概念により必然的に修正される以外大発明 の精神と範囲に含ぼれるものと見做される。The preferred embodiment of the invention is unknown! As explained in the wB book, the basics of the present invention are Without departing from the basic principles of It is understood that changes, modifications or possible changes are possible. However, this kind of change or correction is Major inventions other than those necessarily modified by the scope of the claims or their reasonable equivalents be considered to be within the spirit and scope of

Claims (1)

【特許請求の範囲】 〔1〕隣接するパイプの内壁と外壁との間で空間を提供するよう、漸次大きくさ れた直径と寸法を有する複数の概ね共軸線方向に位置したパイプを含む、吸収熱 交換システム用のパワーユニットにおいて、 α、中空の、垂直方向の中央パイプと。 b、前記中央バイプンら外方に延ひ、外側のパイプと接続され、−万か前記中央 パイプを囲む次のチャンバき隣接する概ね環状のチャンバそ形成する上方と下方 の閉鎖部材と。 C9中央パイプに熱を提供する手段と。 d、最大直径のパイプの外面と廣触するようCや却At体を提供する手段と。 e、概ね環状のチャンバの内壁上へとや媒さ吸収剤の・容液を排出し吸収41] をきむ該、@徹から冷媒を悦看し、かつ前記チャンバの外壁上でtや媒を梁組さ せる手段と。 f、概ね環状のチャンバにお(ハて冷媒と浴孜を別々に集める手段と。 g、別々に集めた(答、没を一万のチャンバから次の隣接する漸次直径の大きい チャンバへ運び、最大直径のチャンバから該浴液を排出する手段と:ん、別々に 集められた冷媒を前記チャンバから運ぶ手段と。 を含む、吸収熱交換7ステム用のパワーユニット。 5 (2)請求の範囲第1項に記載のパワーユニット:cおいて、前記閉鎖部材は前 記ユニットの長手方向!!ilImに対して概ね半径方向に位置したフランツで あるパワーユニット。 (3)請求の範囲第1項に記載のパワーユニン:・に2いて、前記パイプは断面 形状が円形であるパワーユニット。 (4) 請求の範囲第1項に記載のパワーユニット・、4:、おいて、内側パイ プは、その外面に沿って、前記端部閉鎖部材の間で間隔をあけて、全体的に半径 方向に位置し、外方および上方に突出した1延長部材を■するパワーユニット。 (5) 請Zの範囲第4項に記載のパワーユニットにおいて、前記1延長部材( は基本的に突起を形成するスリットを有するパワーユニット。 (6)請求の範囲第5項に記載のパワーユニットにおいて、前記面延長部財は端 部閉鎖部材の間でらせん状に前記パイプの外面に位置し、かつ取り付けられるパ ワーユニットっ (7)請求の範囲第4項に記載のパワーユニットに2いて、外側パイプの外側に 1延長部材を設けること)でより冷却元本の効果が向上するパワーユニット。 (8)請求の範囲第4頂:C記載のパワーユニットに分いて、冷却元本を供給し 冷却作淘を提供する装置が水ジャケットであるパワーユニット。 〔9〕吸収冷凍システムの中心軸の周りで全体的に対称の構造である、吸収熱交 換システム用のパワーユニットにお1ハて、 16 a、外壁と内壁とで構成さ店その中へ燃焼生成物の流れを導くよう位置した燃料 燃焼による燃焼器を受入れるよう形成さnた燃焼チャンバ部材であって、その外 壁面に沿って中ノし・軸線の方向に間隔をおいて、全体的に半径方向に位置し外 方に突出した1延長部材の面を有し、端部が前記外面から外方に突出し、半径方 向(・こ形成された1閉鎖部材を含む、中央配置の燃焼チャンバ部材と。 b、前記J燃焼チャンバ部材を囲み、該チャンバ部材の外壁刀Sら隔置され、前 記閉鎖部射に取り付けられた第1の脱着チャンバ部材であって、その外壁に沿っ て両端の間で間隔をあけて中)し・@線の方向((延ひ、全体的に半径方向に位 置し、外方(C突出した面延長部材の而を有し、端部か前記外壁面から外方に突 ・出し、半径方向に形成されfこ閉鎖部材を含む第1の脱着チャツバ部材と。 C0前記燃焼チャンバ部材と前記第1轍着チャンバ部拐との間に形成された第1 の脱着チャツバであって、一端で入口開口を、反対側の端部で仕切を有し、該仕 切は外壁に対して全対向(/こ平行、刀・っ閉鎖部材に対して垂直方向に位置し 前記第1脱着チャツバの端部そ内側リザーバと外側リザーバに分割しており、各 リザーバからの出口開口を・備えている第1の脱着チャンバと。 d、前記第1の脱着チャンバ部材を囲み、その外壁17 特表昭59−5012 79 (2)つ)ら隔置され、前記閉鎖部桐に取り付けられている第2の脱着チ ャンバ部材と。 e 前記第1の脱着チャンバ部材さ前記第2の脱着チャツバ部材の間に形成され た第2の脱着チャンバであって、一端(C入口開口を、反対側]の端部)で仕切 を有し、該仕切は外壁に対して全′本的に平行で、かつ閉鎖部材(・て対して垂 直に位置(〜で男2の脱着チャツバの端部そ内側リザーバと外測リザーバに分割 して分り、各リザーバからの一口開口を17ζた第2の脱着チャンバ。 とを含む、吸収熱交換システム用パワーユニット。 (10,請求のQ囲第9頂(C記数のパワーユニット(・こ寂いて、第1の脱着 チャンバの内1i111チャツバと第2の脱滑チf/ハへの入口との間には流体 連通装置が設けら才しているパワーユニット。 (旬 請求の化囲第9項に記載のパワーユニット・ておいて、面メ匹長部材の面 か、基本的に突起を形成するスリンI−を有するパワーユニット。 (D請求の範囲第11項に記載のパワーユニットにおいて、1延長部材の面が端 部閉鎖部材の間で5ぜん状に外面に回置し、かつ取り付けられているパワーユニ ット。 ■[Claims] [1] Gradually increase the size to provide space between the inner and outer walls of adjacent pipes. a plurality of generally coaxially located pipes having diameters and dimensions that In power units for replacement systems, α, with a hollow, vertical central pipe; b. extending outward from said central pipe and being connected to an outer pipe; Surrounding the pipe are adjacent generally annular chambers forming upper and lower chambers. with a closing member. and a means for providing heat to the C9 central pipe. d. means for providing a C or attenuated member in wide contact with the outer surface of the pipe of maximum diameter; e. Draining and absorbing the medium-absorbent liquid onto the inner wall of the generally annular chamber 41] The refrigerant is fed from @Toru, and the t and medium are placed on the outer wall of the chamber. and the means to do so. f. a generally annular chamber (with means for separately collecting the refrigerant and bath water; g, collected separately (Answer: 10,000 chambers from the next adjacent progressively larger diameter and means for conveying the bath liquid to the chamber and draining the bath liquid from the largest diameter chamber, separately. means for conveying collected refrigerant from the chamber; A power unit for 7 stems with heat absorption and exchange, including 5 (2) In the power unit according to claim 1, in c, the closing member is Longitudinal direction of the unit! ! Franz located approximately radially to ilIm A power unit. (3) The power unit according to claim 1: In 2, the pipe has a cross section A power unit with a circular shape. (4) The power unit according to claim 1. a generally radial radius along an outer surface thereof and spaced between said end closure members; ■ A power unit including an extension member located in the direction and protruding outward and upward. (5) In the power unit according to claim 4, the first extension member ( is basically a power unit that has a slit that forms a protrusion. (6) In the power unit according to claim 5, the surface extension part is an end a patch located and attached to the outer surface of the pipe in a spiral manner between the closing members; War unit (7) In the power unit according to claim 4, 1. A power unit that improves the cooling effect by providing an extension member. (8) Fourth aspect of claim: Supplying cooling principal separately to the power unit described in C. A power unit whose cooling device is a water jacket. [9] Absorption heat exchanger has an overall symmetrical structure around the central axis of the absorption refrigeration system. Put one on the power unit for the conversion system, 16 a. A fuel outlet comprising an outer wall and an inner wall and positioned to direct the flow of combustion products thereinto. A combustion chamber member configured to receive a combustor for combustion, the member comprising: At intervals along the wall surface in the direction of the center and axis, generally located radially and outwardly. one extension member has a surface projecting in the direction, an end projecting outwardly from said outer surface, and a radial direction a centrally disposed combustion chamber member including a closure member formed in opposite directions; b, surrounding the combustion chamber member J, spaced apart from the outer wall S of the chamber member, and a first desorption chamber member attached to the closure section; spaced between the ends) and @line direction ((extending, generally radially positioned) and has a surface extension member that protrudes outward (C), with the end thereof protruding outward from the outer wall surface. - a first removable chatuba member formed in a radial direction and including a closure member; C0 a first rutting chamber member formed between the combustion chamber member and the first rutting chamber part; a removable chatuba having an inlet opening at one end and a partition at the opposite end; The cut is completely opposite to the outer wall (parallel to / and perpendicular to the closing member) The end of the first detachable chatuba is divided into an inner reservoir and an outer reservoir. a first desorption chamber comprising an outlet opening from the reservoir; d, the outer wall 17 surrounding the first desorption chamber member; 79 (2) second detachable chips spaced apart from each other and attached to the closing part paulownia; With chamber parts. e. formed between the first desorption chamber member and the second desorption chamber member; a second desorption chamber partitioned at one end (an end opposite to the C inlet opening); , the partition is entirely parallel to the outer wall and perpendicular to the closing member. The end of the detachable chatuba of the man 2 is divided into an inner reservoir and an outer reservoir at the direct position (~) A second desorption chamber with 17 ζ openings from each reservoir. Power unit for absorption heat exchange system, including. (10, Q box 9th peak of claim (C number power unit A fluid is provided between the chamber 1i111 chatuba and the inlet to the second de-sliding channel f/c. A power unit equipped with a communication device. (In the case of the power unit described in Clause 9 of the claim, Or a power unit having a sulin I- which basically forms a protrusion. (D In the power unit according to claim 11, the surface of one extension member is an end The power unit is rotated on the outer surface in a five-ring shape between the closing members, and is attached to the power unit. t. ■
JP58502624A 1982-07-12 1983-07-08 Power unit for absorption heat exchange system Pending JPS59501279A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US397620CHEDE 1982-07-12
PCT/US1983/001056 WO1984000413A1 (en) 1982-07-12 1983-07-08 Power unit for absorption heat exchange system

Publications (1)

Publication Number Publication Date
JPS59501279A true JPS59501279A (en) 1984-07-19

Family

ID=22175341

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58502624A Pending JPS59501279A (en) 1982-07-12 1983-07-08 Power unit for absorption heat exchange system

Country Status (1)

Country Link
JP (1) JPS59501279A (en)

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