JPS58200966A - Absorption cold and hot water machine - Google Patents
Absorption cold and hot water machineInfo
- Publication number
- JPS58200966A JPS58200966A JP8350982A JP8350982A JPS58200966A JP S58200966 A JPS58200966 A JP S58200966A JP 8350982 A JP8350982 A JP 8350982A JP 8350982 A JP8350982 A JP 8350982A JP S58200966 A JPS58200966 A JP S58200966A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- low
- regenerator
- heat source
- heat
- 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.)
- Pending
Links
Landscapes
- 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】
本発明は、−重二重効用吸収冷凍幽(二吸収ヒートポン
プ@能Y備え、低温熱源再生器りの高温水ン取り出せる
ようにした吸収冷温水Mζ:関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption cold/hot water Mζ which is equipped with a dual-effect absorption refrigeration system (dual absorption heat pump @ function Y, and is capable of extracting high-temperature water from a low-temperature heat source regenerator).
従来、−重二重効用吸収令凍機においては、夏191等
令水2要時に、工場排温水等の低温熱1原を有効梱用し
つつ冷媒と吸収液との循環による冷凍サイクルχ形成せ
しめて蒸発器に収納した伝熱管から冷水を取り・旧−冬
藺等温水必要時(二、灯油等の・ご焼ガスY加熱・原と
する高温再生器に温水器Y付設し、該温水器と高温再生
器とY循1素する冷媒の#縮熱で温水器(二収納した温
水管から温水Y取り出丁よう(=シている。Conventionally, in double-effect absorption refrigerating machines, a refrigeration cycle χ is formed by circulating refrigerant and absorption liquid while effectively using one source of low-temperature heat, such as factory waste water, when 191st grade water is required in summer. At least take cold water from the heat exchanger tube stored in the evaporator, and when isothermal water is needed (2. Heat the kerosene, etc., burnt gas Y, attach a water heater Y to the high-temperature regenerator used as the source, and use the hot water The hot water is extracted from the hot water pipes stored in the water heater (2) by the heat condensation of the refrigerant flowing through the vessel and the high-temperature regenerator.
19rる従来の吸収冷温水機は、温水必要時には工場!
−+に温水等の低温熱#ゲ有効に利用していない欠点?
有している。The conventional absorption chiller/heater is a factory when you need hot water!
−+ Low-temperature heat such as hot water #ge Is it a disadvantage of not using it effectively?
have.
本発明は、所る点(二鑑み、此種−東二献効用吸収冷凍
1(:おいて、低温熱、悼乞、高温再生器で発生させた
令媒蒸気の凝縮熱により加熱した後蒸発4に収納した伝
熱管および低温熱源再生器に収納した熱、4jp、管I
;fJIcaせしめ、吸収器に収納した水雷から低温熱
源温度以上の温水Y取り吊子よう(二低温熱諒再生器、
凝縮器、蒸発器、咥収器支び溶液熱交換器を接続して吸
収ヒートポンプサイクルを形成せしめる切替機構を備え
た構成ゲ採ることにより、温水必要時(−おいても排温
水等の低温熱紳馨有効利用し、しかも低温熱源より高温
の温水ン得られる吸収冷温水機Y提供することY目的と
したものである。The present invention has a certain point (in view of this, this type of absorption refrigeration). Heat exchanger tubes stored in 4 and heat stored in low temperature heat source regenerator, 4jp, tube I
fJIca, the hot water above the low-temperature heat source temperature is collected from the torpedo stored in the absorber (two low-temperature heat regenerators,
By adopting a configuration equipped with a switching mechanism that connects a condenser, evaporator, absorber support, and solution heat exchanger to form an absorption heat pump cycle, low-temperature heat such as waste hot water can be The object of the present invention is to provide an absorption chiller/heater that utilizes water effectively and can obtain hot water at a higher temperature than a low temperature heat source.
以下、本発明の実施例を図面(二基いて説明する。Embodiments of the present invention will be described below with reference to the drawings.
(8G)は器内ζ:熱轢管fllt’収納し、該熱源管
に151Et!iせしめる排温水等の低温熱源Y加熱源
として稀液から冷媒を分離する低温熱源再生器、(HG
)は燃焼ガスや高温蒸気等の高温熱源Y加熱源として中
間液から冷媒χ加熱分離する高温再生器、(LG)は前
記高温再生器(H())で分離された冷媒蒸気χfP4
#とじて、濃度の高い中間液を史(;加熱分離する低温
再生器、(0)は前記各占生器(8G)(HG)(LO
)から流入する冷媒を器内に収納した冷却管(21で冷
却して凝縮させる凝−器、(31は前記凝lli!i器
tCaからの液冷媒Y器内に収納した伝熱’Ih3+に
散布して気化させる蒸発器、囚は前記低温熱*再生器(
SG)、高温再生器(HG)、低温再生器(LG)にお
いて冷媒が分離された吸収液を器内(=収納した水管(
4)(−散布して気化冷媒を吸収する吸収器、(5)及
び(6)は溶液熱斐換器であり、これらは冷媒導管(7
1,41冷媒液流下管(8)、第1冷媒ポンプ(9)Y
有する冷媒液管01%41溶液ポンプ+111有する稀
液管(13、第2溶液ポンプlI3′1に:有する中間
液[U41f15、濃液管・IF3及び第1バイパス溶
液管0ηにて配管接続されて冷媒と吸収液の循環(二よ
る冷凍サイクルを形成し、lk−発器(燭(二収納した
伝熱管(3)から冷水を得る一直二重効用吸収冷凍機Y
構成している。(8G) is stored in the vessel ζ: heat track tube fllt', and the heat source tube contains 151Et! A low-temperature heat source regenerator (HG
) is a high-temperature regenerator that heats and separates the refrigerant χ from the intermediate liquid as a high-temperature heat source Y such as combustion gas or high-temperature steam, and (LG) is the refrigerant vapor χfP4 separated in the high-temperature regenerator (H()).
# A low-temperature regenerator that heats and separates the high-concentration intermediate liquid, (0) indicates each spacer (8G) (HG) (LO
) A condenser that cools and condenses the refrigerant flowing in from the cooling pipe (21), (31 is a condenser that cools and condenses the refrigerant flowing from the condenser tCa) to the heat transfer 'Ih3+ stored in the liquid refrigerant Y vessel from the condenser tCa. An evaporator that disperses and vaporizes the vapor, and a low-temperature heat * regenerator (
SG), high-temperature regenerator (HG), and low-temperature regenerator (LG), the absorption liquid from which the refrigerant has been separated is stored inside the vessel (= water pipe (
4) (- an absorber for absorbing vaporized refrigerant by dispersion, (5) and (6) are solution heat exchangers, which are connected to the refrigerant conduit (7)
1, 41 refrigerant liquid flow pipe (8), first refrigerant pump (9) Y
Refrigerant liquid pipe with 01% 41 solution pump + 111 dilute liquid pipe with Circulation of refrigerant and absorption liquid (to form a refrigeration cycle with two
It consists of
σ岨ま前記高温再生器(HG)i二付設した補助熱交換
器で、該熱交換器の上部には冷媒導管(7:の分岐冷媒
導管f’7’l接続し、下部には高温再生器(HG)l
二連結されたドレン管11v接続して高温再生器(HG
)と補助熱交換器illとの間!冷媒が循環できるよう
に形成されている。The high temperature regenerator (HG) i2 is attached to the auxiliary heat exchanger, and the upper part of the heat exchanger is connected to the refrigerant conduit (branch refrigerant conduit f'7'l of 7), and the lower part is connected to the high temperature regenerator (HG). Vessel (HG)l
Connect the two connected drain pipes 11v to the high temperature regenerator (HG).
) and the auxiliary heat exchanger ill! Designed to allow refrigerant to circulate.
(11は三方弁(1)Y介して前記熱源管(1)(−配
設したバイパス熱源管で、該バイパス熱源管の一部1に
:@紀禰助熱父換器tllli二収納している。(至)
は削紀伝黙w(3)と熱源管+11とt連結した連絡管
で、該連絡管及び伝熱w(31には夫々開閉弁(6)及
び+61が配設されており、これらの開閉χ切替えるこ
とにより伝熱管(31に冷水又は低温熱myhvtすよ
うにしている。(11 is a bypass heat source tube installed through the three-way valve (1) Y to the heat source tube (1) (-), and part 1 of the bypass heat source tube: @Kine auxiliary heat exchanger tllli2 is stored. There is. (To)
is a connecting pipe connected to the heat source pipe +11 and the connecting pipe w(3), and the connecting pipe and the heat transfer w(31) are provided with on-off valves (6) and +61, respectively, and these opening/closing χ By switching, cold water or low-temperature heat is supplied to the heat transfer tube (31).
(81は第2冷媒ポンプ(211ン有する第2冷媒液流
下管、(1fIは第6溶液ポンプ・nt有する第2バイ
パス溶液管である。そして、((11は冷媒導管(7)
(=、lflは第1冷媒液流下w(8)に、Iglは低
温熱#再生器(8G)から高温再生器(HG)(−至る
中間液管+411−1lh)は高温再生器(HG)から
低温再生器(LG)に至る中間液管n5 +二、(il
ハ濃液tDE91−1(jl)1 $2冷媒液流下f
(81+二、並びC二(k)は第2バイパス浴液管面′
に、夫々備えた開閉弁で、これらの開閉Y切替えること
(二より冷媒と吸収液の循環!切替える。(81 is a second refrigerant liquid flow down pipe having a second refrigerant pump (211), (1fI is a second bypass solution pipe having a sixth solution pump), and ((11 is a refrigerant conduit (7)
(=, lfl is the first refrigerant liquid downstream w (8), Igl is the low temperature heat # from the regenerator (8G) to the high temperature regenerator (HG) (- intermediate liquid pipe +411-1lh) is the high temperature regenerator (HG) Intermediate liquid pipe n5 +2, (il
C Concentrated liquid tDE91-1 (jl) 1 $2 Refrigerant liquid flow f
(81+2, line C2(k) is the second bypass bath liquid pipe surface'
Then, use the on-off valves provided for each to switch between opening and closing (circulation of refrigerant and absorption liquid!).
(4)は吸収器(A+に収納した本管で、該水@(−は
温度検出器C241に:備えており、また伝熱管(3)
(二も@:蔓検出器12s’P備えている。のは高温再
生器(HG)への加熱借制御弁である。■は、冷温切替
スイyすt21v介して+1+J記温[y検出器124
)若しくは(2艶からの信号(二より、加熱針制御弁の
の開度を調節すると共C;第1、$27’?I媒ポンプ
(9)Qυ、第1、$2、第5溶液ポンプ1111t1
3tηの夫々Y発停させる制御器である。(4) is the main pipe stored in the absorber (A+), the water @ (- is in the temperature detector C241: equipped, and the heat transfer tube (3)
(Two also @: Equipped with a vine detector 12s'P. is a heating control valve to the high temperature regenerator (HG).■ is a +1+J temperature recording [y detector 124
) or (Signal from 2) Adjust the opening of the heating needle control valve and C; 1st, $27'? I medium pump (9) Qυ, 1st, $2, 5th solution Pump 1111t1
This is a controller that starts and stops each Y of 3tη.
次(−1貼る構成の吸収冷温水機の運転動作(二ついて
説明する。Next (-1 Operation operation of an absorption chiller/heater with a pasting configuration (two explanations will be given).
(イ)冷水必要時の運転動作
冷水必釦には、弁(・)Y開き弁(blv閉じて、例え
ば冷房用の冷水負荷側熱交換器(図示せず)と接続され
ている伝熱@ [3+ 4m冷水′Ik:流通させ、三
方弁(&)のバイパス熱#’!(11側流路を閉じて、
例えば工場廃熱源と接続されている熱源管(1)に低温
熱源ン流通させ、かつ冷却水IF +21及び水t (
41(二冷却水Y[し、また高温再生器(HG)Y加熱
する。(b) Operation behavior when chilled water is required The cold water must button has a valve (・) Y open valve (blv closed, for example, a heat transfer @ connected to a chilled water load side heat exchanger (not shown) for cooling) [3+4m cold water 'Ik: Flow, bypass heat of three-way valve (&) #'! (Close the flow path on the 11th side,
For example, a low temperature heat source is passed through a heat source pipe (1) connected to a factory waste heat source, and cooling water IF +21 and water t (
41 (2 cooling water Y [and also heats the high temperature regenerator (HG) Y.
同峙(=、冷温切替スイツデf27Lvo接点1:接続
し、ポンプ191G1113Y作動セL、166 、!
: 共1m弁!(11、ffl、(gl、Fhl及び(
1)乞開き、かつポンプ121J及び1涛の作@Y停止
し、弁tjl及び(kl ’t’閉じて運転する。Same side (=, cold/hot switching switch f27Lvo contact 1: Connect, pump 191G1113Y operation set L, 166,!
: Both 1m valve! (11, ffl, (gl, Fhl and (
1) Open the pump and stop pump 121J and 1st operation @Y, close valve tjl and (kl 't') and operate.
而して、吸収液は、吸収器fAlから管11邊、ポンプ
(Ill、 !11カ、溶液熱交換器)61、’tn力
、低温熱θ再生5(8())、Wl′I41、ポンプ0
、管04、弁(g+、堂04)溶液熱交換器(5)、管
11高温再生器(HG)、肯0つ、溶液熱交換器(5)
、ttts、弁(h)、管119、低温再生器(L()
)、管aS、弁(1)、WaS、溶液熱交換器(61,
1iae’v経て吸収器tAlへ還流して循環する。尚
、吸収器体)から低温熱源再生器(8G)へ達した吸収
液の一部は管a′7)へ分流し、該雪と管11eとの後
続部Cユおいて低温再生器(LG)からの吸収液と再び
合流する。Therefore, the absorption liquid is transferred from the absorber fAl to the pipe 11, the pump (Ill, !11, solution heat exchanger) 61, 'tn force, low temperature heat θ regeneration 5 (8 ()), Wl'I41, pump 0
, pipe 04, valve (g+, door 04) solution heat exchanger (5), pipe 11 high temperature regenerator (HG), no 0, solution heat exchanger (5)
, ttts, valve (h), pipe 119, low temperature regenerator (L()
), pipe aS, valve (1), WaS, solution heat exchanger (61,
1iae'v and then refluxed to the absorber tAl for circulation. A part of the absorption liquid that has reached the low-temperature heat source regenerator (8G) from the absorber body) is diverted to the pipe a'7), and is transferred to the low-temperature regenerator (LG ) is recombined with the absorption liquid from ).
低温熱源再生器(8G)及び低温再生器(LG)で吸収
液から分離された冷媒は器内のe縮器tel鑑二おいて
凝縮され、また高温再生器(HG)で分離された冷媒は
管(71、低温再生器(LG)、’!+71゜弁+(1
1、管(7)を経て凝縮器tc+に至り該凝縮器におい
て凝縮される。凝縮器(C1(二おいて凝縮された冷媒
は管(8)、弁15)、!(8)、ポンプ(9)、管(
In’経て蒸発器[El内の伝熱管(3)に散布されて
気化する。そして気化冷媒は吸収器(AICおいて再び
吸収され、冷媒の循環がtIP返される。The refrigerant separated from the absorption liquid in the low-temperature heat source regenerator (8G) and the low-temperature regenerator (LG) is condensed in the internal e-condenser, and the refrigerant separated in the high-temperature regenerator (HG) is Pipe (71, low temperature regenerator (LG), '! + 71° valve + (1
1. It reaches the condenser tc+ through the pipe (7) and is condensed in the condenser. Condenser (C1 (2), condensed refrigerant is pipe (8), valve 15), ! (8), pump (9), pipe (
Through In', it is distributed to the heat exchanger tube (3) in the evaporator [El] and vaporized. The vaporized refrigerant is then absorbed again in the absorber (AIC) and the refrigerant circulation is returned tIP.
このような冷媒と吸収液との循4(二よる冷凍サイクル
が形成され、蒸発器tgl内で冷媒液が気化する際の吸
熱作用C二より伝熱管(31から冷水Y取り出す一龜二
重効用吸収冷[′WAが構成される。A refrigeration cycle is formed in which the refrigerant and the absorbing liquid circulate (4) in this manner, and the heat absorption effect when the refrigerant liquid is vaporized in the evaporator (TGL) C2 takes out cold water Y from the heat transfer tube (31). Absorption cooling ['WA is constructed.
冷水負荷が増大すると冷水取り出し温度が上昇し始める
ので、温闇検出器鉋の信号(二より加熱酸制御弁(@)
の開文χ増し、高温再生器(HG)への加熱11に:増
大させ、冷媒分離Wk?増加させると共1:吸吸収液質
r高めて冷凍能力ゲ同上せしめ、冷水取り出し温度ン下
げて負荷1ユ見合う冷水を取り出す。As the cold water load increases, the cold water outlet temperature begins to rise, so the signal from the temperature detector plane (secondary heating acid control valve (@)
Increased opening χ, heating to high temperature regenerator (HG) 11: Increased, refrigerant separation Wk? When the temperature is increased to 1, the absorption and absorption liquid quality r is increased to increase the refrigerating capacity, and the cold water takeout temperature is lowered to take out cold water corresponding to the load of 1 unit.
尚、冷水負荷が小さく、低温熱源再生器(8G)の駆動
のみで十分な場合は高温再生器()IG)への加熱を停
止して、所謂−重効用吸収冷凍礪として冷凍運転するこ
とも可能であり、また低温熱#l?rA1fが低下ぎて
、吸収液から冷媒を分離する能力カ1不忙する場合(:
は、低温熱源再生器(8G)への低温熱源の供給?停止
し、高温再生器(HG)及び低温再生!(LG)の駆動
(二よる折開二重効用吸収冷凍機としての冷凍遼(転χ
行なうこともiiJ能である。In addition, if the chilled water load is small and it is sufficient to drive the low temperature heat source regenerator (8G), heating to the high temperature regenerator (2G) may be stopped and refrigeration operation may be performed as a so-called heavy-effect absorption refrigeration tank. Is it possible and also low temperature heat #l? If rA1f is too low and the ability to separate the refrigerant from the absorbing liquid is insufficient (:
Is it supplying low temperature heat source to low temperature heat source regenerator (8G)? Stop, high temperature regenerator (HG) and low temperature regeneration! (LG) drive (refrigeration Liao as a folding double effect absorption refrigerator
It is also iiJ Noh to do something.
(σ)温水必要時の運転動作
温水必要時(二は、弁(θ)!閉じて弁11)l Y開
ま、三方弁(alの低温熱源入口流路ll!lt閉じて
バイパス熱#管(11…11流路χ開き、低温熱I!A
ン該バイパス熱諒管を介して補助熱交換器(lに通した
後、熱源管(1)(−低温熱源を流通させると共C;連
絡管艷を介して伝熱肯(3)(−低温熱fIA1に:流
通させ、冷却水管+21+−冷却水を流し、かつ水管(
4)χ例えば暖房用の温水負荷側熱9換器(図示せず)
と接続して温水!流し、また高温再生器(HG)1に:
加熱する。同時(−1冷温切替スイ7デ罰ンH接点に接
続し、ポンプ(910υ12+) ?3を作動せしめる
と共に弁1jl及び(k)7開き、かつポンプ0の作動
を停出し、弁(al、 (fl、tgl、(bl及び(
1)を閉じて運転する。(σ) Operation behavior when hot water is required When hot water is required (2, valve (θ)! Close and valve 11) l Y open, three-way valve (al low temperature heat source inlet flow path ll! lt close and bypass heat # pipe (11...11 flow path χ open, low temperature heat I!A
After passing through the auxiliary heat exchanger (L) through the bypass heat exchanger, the heat source tube (1) (-) passes the low temperature heat source through the heat transfer tube (3) (- Low-temperature heat fIA1: Let it flow, let the cooling water flow through the cooling water pipe +21+-, and connect the water pipe (
4) χ For example, hot water load side heat exchanger 9 for heating (not shown)
Connect to hot water! Sink and also to high temperature regenerator (HG) 1:
Heat. At the same time (-1 cold/hot switching switch 7 is connected to contact H), pump (910υ12+) ?3 is activated, valves 1jl and (k) 7 are opened, and pump 0 is deactivated, valves (al, ( fl, tgl, (bl and (
1) Close and operate.
而して、低温熱源は高温再生器(HG)からの冷媒蒸気
の熱により補助熱交換器aS Cおいて加熱昇温され、
低温熱1tl杏生器(8G)の冷媒分離能力及び蒸発器
tElの冷媒気化能力が同上する。The low-temperature heat source is heated and heated in the auxiliary heat exchanger aSC by the heat of the refrigerant vapor from the high-temperature regenerator (HG),
The refrigerant separation capacity of the low-temperature heat generator (8G) and the refrigerant vaporization capacity of the evaporator tEl are the same as above.
そして、吸収液は、吸収器体から管1t21.ポンプ0
υ、管0載溶液熱交換器(61、管・1z、低温熱譚書
生5(S())、qir+i、ポンプQ7J、管r+7
1、弁(k)、11!ML管(161、溶液熱交換器(
6)、管用ン経て吸収器(〜に還流して循環する。Then, the absorption liquid is transferred from the absorber body to the pipe 1t21. pump 0
υ, tube 0 solution heat exchanger (61, tube 1z, low temperature heat exchanger 5 (S()), qir+i, pump Q7J, tube r+7
1, valve (k), 11! ML tube (161, solution heat exchanger (
6) It is refluxed and circulated through the pipe to the absorber (~).
また、低温熱源再生器(8G)で吸収液から分離された
冷媒は器内の凝縮器+01?−おいて凝縮されてf#冷
媒となり、この冷媒は管(鎖、ポンプ+211.!(8
1、弁1jl、!(81、ポンプ(9)、堂1101経
て蒸発器[11内の伝軌管(:(1に散布されて気化す
る。そして気化冷媒は吸収器体において再び吸収され、
冷媒の循環が繰退される。このような冷媒と吸収液との
循環による吸収ヒートポンプサイクルが形成され、騨1
Fン器(A)内で冷媒が吸収液に吸収される際の放熱作
用により水管(4)から温水ン取り出す吸収ヒートポン
プが構成される。Also, the refrigerant separated from the absorption liquid in the low-temperature heat source regenerator (8G) is transferred to the condenser +01 in the vessel. - is condensed into f# refrigerant, which is piped (chain, pump +211.! (8
1, valve 1jl,! (81, pump (9), through the hall 1101, the transmission pipe (:(1) in the evaporator [11] is sprayed and vaporized.Then, the vaporized refrigerant is absorbed again in the absorber body,
Refrigerant circulation is retracted. An absorption heat pump cycle is formed by circulating the refrigerant and absorption liquid, and
An absorption heat pump is constructed that takes out hot water from the water pipe (4) by the heat radiation effect when the refrigerant is absorbed by the absorption liquid in the fan unit (A).
温水f’を荷が増大すると温水取り出し温度が低下し始
めるので、温丈検出器′禎からの信号(二より加熱華刑
仰弁tel力PJ4叶乞増し、高温再生器(H())か
らの冷媒分離はr41mlやすと共(−冷媒蒸気温度t
高めて、低温艷係をより加熱昇温し、低温熱源再生器(
8G)の令媒分離能力言い代えれば・汐収液の濃縮カン
同上せしめると共に蒸発器(Elでの仝、嘩気化す!増
やすこと(:より、吸収器(A1での冷W吸収l全増大
させて放熱作用χ同上せしめ、温水H■り出し温度?上
げて、負荷に見合う温水ン収り出す。As the load of hot water f' increases, the hot water take-out temperature begins to drop, so a signal from the temperature sensor (from the second heating control valve tel PJ4 to the high temperature regenerator (H)) is output. The refrigerant separation is r41ml and (-refrigerant vapor temperature t
The low temperature heat source regenerator (
In other words, increase the refrigerant separation capacity of the evaporator (El) and increase the refrigerant separation capacity of the absorber (A1). The heat dissipation effect χ is increased, and the temperature of the hot water H is raised to draw out the hot water suitable for the load.
折る構成の吸収ヒートポンプ(−おいては、低温熱!@
肉生器(8G)及び凝縮器(01側内田より蒸発器(E
l及び吸収器内側内圧の方が高い状萼で厚転され、かつ
吸収器内において吸収液が冷媒χ吸収−rる際(二発生
する熱で温水?昇温するものであるから、低昌熱掠温ず
以Eの温水Y取り出すことができる。例えば、断る吸収
ヒートポンプにおいては、80〜90℃の低温熱#を供
給することによつ〔,400℃以Eの温水又は蒸気を取
り・男し得る。Absorption heat pump with foldable configuration (low-temperature heat! @
Meat generator (8G) and condenser (evaporator (E) from Uchida on 01 side
When the internal pressure inside the absorber is higher than that of the calyx, and when the absorption liquid absorbs the refrigerant χ in the absorber (2), the heat generated raises the temperature of the hot water. For example, in an absorption heat pump, by supplying low-temperature heat of 80 to 90℃, hot water or steam with a temperature of 400℃ or higher can be extracted. I can be a man.
以りのように、本発明吸収冷温水醗は、工場排温水等の
低温熱源を利用する一重二市効用吸収令凍機において、
低温熱#Y1高温高温再生付設した補助熱交換器で冷媒
蒸気により加熱した後伝熱管及びへAつ管(二流通せし
める切替機構と、低温熱諒J4−4生器、19編器、蒸
発器、吸収器及び溶液熱交換器ケ接続して吸収ヒートポ
ンプサイクルを形成せしめる切替機構とV*えて水管か
ら漏水を収り出すよう)−シたものであるから、冷水必
娑時1m水必要時のいずれの場合も低温熱源を有効利用
でき、かつ、温水必要時に低温熱源温度以上の高温水?
得ることができるものである。As described above, the absorption chilled/hot water bottle of the present invention can be used in a single/two-city absorption chiller that utilizes a low-temperature heat source such as factory waste water.
Low temperature heat #Y1 High temperature regeneration After heating with refrigerant vapor in the auxiliary heat exchanger attached, heat transfer tube and A-tube (switching mechanism that allows two flows, low temperature heat generator J4-4 generator, 19 knitting machine, evaporator , a switching mechanism that connects the absorber and solution heat exchanger to form an absorption heat pump cycle. In either case, can a low-temperature heat source be used effectively, and when hot water is needed, is there high-temperature water that is higher than the low-temperature heat source temperature?
It is something that can be obtained.
内面1・ま本発明の一実施例を示す回路41!成概略説
明図である。
・ (8G)・・・低温熱源再生器、(HG)・・・高
温再生器、(L())・・・低温再生器、(0)・・・
凝縮器、(El・・・蒸発器、囚・−・吸収器、(1)
・・・熱源管、of・・・バイパスPP4Ill管、(
31・・・伝熱管、14)・・・本管、(51t61・
−・溶液熱交換器、181・・・@2冷媒液隠下管、1
イ・・・第2バイパス浴液肯、11国・・・補助熱交換
器、(21・−・連絡管、Qυ・−・第2冷媒ポンプ、
(23・・・@5溶液ポンプ、1゛)優円・・・温度検
出器1.酌・・・1,1j倒器、イ浄・・・冷温切柊ス
イ7j、lal・・・三方弁、(bl(dltel(f
ltgl(hl[il[k)−3M閉弁、/ −・・加
熱1制御弁。
出願人 三洋電m株式会社外−1名Inner surface 1. A circuit 41 showing an embodiment of the present invention! FIG.・ (8G)...Low temperature heat source regenerator, (HG)...High temperature regenerator, (L())...Low temperature regenerator, (0)...
Condenser, (El... evaporator, absorber, (1)
...Heat source tube, of...Bypass PP4Ill tube, (
31...Heat transfer tube, 14)...Main pipe, (51t61・
-・Solution heat exchanger, 181...@2 Refrigerant liquid concealment tube, 1
A...Second bypass bath liquid pump, 11 countries...Auxiliary heat exchanger, (21...Connection pipe, Qυ...Second refrigerant pump,
(23...@5 solution pump, 1゛) Yuen...Temperature detector 1. Cup...1,1j down vessel, ijo...cold and warm Kirihiragi sui 7j, lal...three-way valve, (bl(dltel(f)
ltgl(hl[il[k)-3M valve closed, /-...Heating 1 control valve. Applicant: 1 person outside Sanyo Denki M Co., Ltd.
Claims (1)
熱fIj、角生器、悌燐ガス等の高温熱源を加熱綻とす
る高温再生器、該再生器で分離された冷媒蒸気を加熱源
−iする低温再生器、凝縮器、蒸発器、吸収器及び溶液
熱交換器を接続して冷凍サイクルχ形成せしめ、蒸発器
(:収納した伝熱管から冷水を取り出すようにした一重
二重効用吸収冷凍機において、低温熱#ン、前記高温再
生器に付設した補助熱交換器で冷媒蒸気により加熱した
後蒸発器に収納した伝熱管および低温熱源再生器に収納
した熱源肯に15を通せしめ、前記吸収器に収納した本
管から低温熱源温度以上の温水を取り出すようC二回記
低温熱源再生器、凝縮器、蒸発器、吸収器及び溶液熱交
換器1に:接続して吸収ヒートポンプサイクルY形1戊
せしめる切替a*y1′備えたことY特徴とする吸収冷
温水機。(1) A high-temperature regenerator that uses a low-temperature heat source such as factory waste water as a heating source, a high-temperature heat source such as a horn generator, or a high-temperature heat source such as phosphorus gas, and refrigerant vapor separated by the regenerator. A low-temperature regenerator, a condenser, an evaporator, an absorber, and a solution heat exchanger are connected to form a refrigeration cycle (chi), and the evaporator (a single-duplex system that takes out cold water from a housed heat transfer tube) In an effective absorption refrigerator, a low temperature heat tube is heated by refrigerant vapor in an auxiliary heat exchanger attached to the high temperature regenerator, and then 15 is passed through a heat transfer tube stored in an evaporator and a heat source stored in a low temperature heat source regenerator. Then, connect the absorption heat pump to the low-temperature heat source regenerator, condenser, evaporator, absorber, and solution heat exchanger 1 to take out hot water above the low-temperature heat source temperature from the main pipe stored in the absorber. An absorption chiller/heater characterized by having a cycle Y type 1 switching a*y1'.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8350982A JPS58200966A (en) | 1982-05-17 | 1982-05-17 | Absorption cold and hot water machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8350982A JPS58200966A (en) | 1982-05-17 | 1982-05-17 | Absorption cold and hot water machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58200966A true JPS58200966A (en) | 1983-11-22 |
Family
ID=13804448
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8350982A Pending JPS58200966A (en) | 1982-05-17 | 1982-05-17 | Absorption cold and hot water machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58200966A (en) |
-
1982
- 1982-05-17 JP JP8350982A patent/JPS58200966A/en active Pending
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