JPH02203166A - Absorption type refrigerator - Google Patents

Absorption type refrigerator

Info

Publication number
JPH02203166A
JPH02203166A JP2293689A JP2293689A JPH02203166A JP H02203166 A JPH02203166 A JP H02203166A JP 2293689 A JP2293689 A JP 2293689A JP 2293689 A JP2293689 A JP 2293689A JP H02203166 A JPH02203166 A JP H02203166A
Authority
JP
Japan
Prior art keywords
refrigerant
absorption liquid
evaporator
absorption
absorber
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
Application number
JP2293689A
Other languages
Japanese (ja)
Inventor
Masayuki Daino
大能 正之
Masahiro Furukawa
雅裕 古川
Toshiyuki Kaneko
敏之 金子
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2293689A priority Critical patent/JPH02203166A/en
Publication of JPH02203166A publication Critical patent/JPH02203166A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To improve the wettability of cooling in a heat transfer tube, to scatter refrigerant substantially uniformly to the heat transfer tube, and further to prevent refrigerant evaporating temperature from decreasing in an evaporator by mixing absorption liquid of a specific range by weight concentration in refrigerant scattered by the evaporator. CONSTITUTION:Since absorption liquid of a range of 0.2 - 4% by weight concentration is mixed in the refrigerant of an evaporator 4, the surface tension of the refrigerant is reduced. Thus, even if oil, etc. is adhered to the outer surface of a heat transfer tube 22A at the time of starting operating of an absorption refrigerator, wettability of the refrigerant on the outer surface of the tube 22A can be improved, the wettability on a tray 18A is improved to scatter the refrigerant substantially uniformly to the tube 22A, thereby preventing the refrigerant evaporating temperature from decreasing in the evaporator 4 when the absorption liquid concentration is high. Thus, the heat exchanging rate of the tube 22A is improved to improve refrigerating capacity. The absorption liquid concentration can be calculated by a controller 25 based on a signal from a specific weight detector 34 provided at the evaporator 4 at the time of operating the refrigerator, and a refrigerant control valve 31 and the absorption liquid control valve 33 are controlled based on the absorption liquid concentration.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は冷媒に水を用い、吸収液に塩類溶液である臭化
リチウム溶液を用いた吸収冷凍機に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to an absorption refrigerator that uses water as a refrigerant and a lithium bromide solution, which is a salt solution, as an absorption liquid.

(ロ)従来の技術 例えば特公昭62−48148号公報には、蒸発器内の
冷媒液中の吸収液濃度と、蒸発器内の冷媒液量との間に
特定の濃度・液量関係を定め、きらにこの濃度・液量関
係に基づいて許容濃度範囲を定め、吸収液濃度及び冷媒
液量を検出し、吸収液検出濃度が許容濃度範囲の上限を
超えたときに、蒸発器内の冷媒の一部を吸収液サイクル
側へ流し、吸収液検出濃度が許容濃度範囲の下限より小
さくなったときに、吸収溶液の一部を蒸発器内の冷媒液
中に混入する吸収冷凍装置が開示されている。
(b) Conventional technology For example, Japanese Patent Publication No. 62-48148 defines a specific concentration/liquid amount relationship between the absorption liquid concentration in the refrigerant liquid in the evaporator and the amount of refrigerant liquid in the evaporator. , Kirani determines the permissible concentration range based on this concentration/liquid volume relationship, detects the absorption liquid concentration and refrigerant liquid volume, and when the detected absorption liquid concentration exceeds the upper limit of the permissible concentration range, the refrigerant in the evaporator is An absorption refrigeration system is disclosed in which a part of the absorption solution is flowed to the absorption liquid cycle side, and a part of the absorption solution is mixed into the refrigerant liquid in the evaporator when the detected concentration of the absorption liquid becomes smaller than the lower limit of the allowable concentration range. ing.

り八)発明が解決しようとする課題 上記従来の技術において、吸収冷凍機の運転開始初期な
どに吸収液濃度が低く例えば0 、1 wt%である場
合には、冷媒液の表面張力が増加し、蒸発器での吸収液
の滴下が均一でなくなり、さらに蒸発器の伝熱管表面上
での濡れ性が悪くなり、伝熱管での熱交換率が悪くなり
、冷凍能力が低下する虞れがあった。又、吸収剤濃度が
高い場合には、蒸発器での冷媒蒸発温度が低下し、蒸発
器での冷媒蒸発が抑制され、冷凍能力が低下するという
問題が発生していた。
8) Problems to be Solved by the Invention In the conventional technology described above, when the absorption liquid concentration is low, for example, 0.1 wt%, at the beginning of operation of the absorption refrigerator, the surface tension of the refrigerant liquid increases. , the dripping of the absorption liquid in the evaporator will not be uniform, and the wettability on the surface of the heat transfer tube of the evaporator will deteriorate, the heat exchange rate in the heat transfer tube will deteriorate, and there is a risk that the refrigerating capacity will decrease. Ta. Furthermore, when the concentration of the absorbent is high, the refrigerant evaporation temperature in the evaporator is lowered, evaporation of the refrigerant in the evaporator is suppressed, and the refrigerating capacity is lowered.

本発明は蒸発器の吸収液濃度を所定濃度に保ち、冷凍能
力を向上させることを目的とする。
An object of the present invention is to maintain the absorption liquid concentration in the evaporator at a predetermined concentration and improve the refrigerating capacity.

り二)課題を解決するための手段 本発明は上記課題を解決するために、吸収器(5)、再
生器(1) 、 (2)、凝縮器(3)、及び蒸発器<
4)をそれぞれ配管接続し、冷媒に水、吸収液に臭化リ
チウム溶液を使用し、蒸発器に設けられた熱交換器の伝
熱管(22A)に冷媒を散布する吸収冷凍機において、
蒸発器(4)で散布される冷媒に重量濃度で0.2%な
いし4%の範囲の吸収液を混入したことを特徴とする吸
収冷凍機を提供するものである。
2) Means for Solving the Problems In order to solve the above problems, the present invention provides an absorber (5), a regenerator (1), (2), a condenser (3), and an evaporator.
4) are connected to each other via piping, water is used as the refrigerant, lithium bromide solution is used as the absorption liquid, and the refrigerant is sprayed onto the heat exchanger tube (22A) of the heat exchanger provided in the evaporator.
The present invention provides an absorption refrigerator characterized in that the refrigerant sprayed in the evaporator (4) is mixed with an absorption liquid having a weight concentration in the range of 0.2% to 4%.

又、吸収器(5)、再生器(1) 、 (2)、凝縮器
(3)、及び伝熱管(22A)を有した蒸発器(4)を
それぞれ配管接続し、冷媒に水、吸収液に臭化リチウム
溶液を使用した吸収冷凍機において、吸収器(5)と蒸
発器(4)との間に吸収器から蒸発器へ吸収液を導く吸
収液送り管(32)を設け、この吸収液送り管(32)
の途中に吸収液調節弁(33)を設け、かつ、蒸発器(
4)と吸収器(5)との間に蒸発器くべ)から吸収器(
5)へ冷媒を導く冷媒送り管(30〉を設け、この冷媒
送り管(30)の途中に冷媒調節弁(31)を設け、蒸
発器(4)に冷媒の比重を検出する検出器(34)を設
け、更にこの検出器(34)から信号を入力し、比重、
或いは密度から冷媒の吸収液濃度を算出して吸収液濃度
に基づいて吸収液調節弁(33)、及び冷媒調節弁(3
1)を制御し、蒸発器の冷媒中の吸収液の重量濃度を0
.2%ないし4%の範囲に制御する制御装置(35)を
設けたことを特徴とする吸収冷凍機を提供するものであ
る。
In addition, the absorber (5), regenerators (1), (2), condenser (3), and evaporator (4) with heat transfer tubes (22A) are connected to each other via piping, and the refrigerant is water and absorption liquid. In an absorption refrigerator using a lithium bromide solution, an absorption liquid feed pipe (32) is provided between the absorber (5) and the evaporator (4) to guide the absorption liquid from the absorber to the evaporator. Liquid feed pipe (32)
An absorption liquid control valve (33) is provided in the middle of the evaporator (
4) and the absorber (5) from the evaporator pipe) to the absorber (
A refrigerant feed pipe (30) is provided to guide the refrigerant to the refrigerant feed pipe (30), a refrigerant control valve (31) is provided in the middle of the refrigerant feed pipe (30), and a detector (34) for detecting the specific gravity of the refrigerant is provided in the evaporator (4). ), further input a signal from this detector (34), and determine the specific gravity,
Alternatively, the absorption liquid concentration of the refrigerant is calculated from the density, and the absorption liquid adjustment valve (33) and the refrigerant adjustment valve (3) are operated based on the absorption liquid concentration.
1) to reduce the weight concentration of the absorbing liquid in the refrigerant of the evaporator to 0.
.. The present invention provides an absorption refrigerating machine characterized in that it is equipped with a control device (35) that controls the temperature within the range of 2% to 4%.

更に、吸収器り5)、再生器(1) 、 (2)、凝縮
器(3)、及び伝熱管(22A)を有した蒸発器(4)
をそれぞれ配管接続し、冷媒に水、吸収液に臭化リチウ
ム溶液を使用した吸収冷凍機において、吸収器(5)と
蒸発器(4〉との間に吸収器(5)から蒸発器(4)へ
吸収液を導く吸収液送り管(32)を設け、この吸収液
送り管(32)の途中に吸収液調節弁〈33)を設け、
かつ、蒸発器(4)と吸収器(5)との間に蒸発器(4
)から吸収器(5)へ冷媒を導く冷媒送り管(30)を
設け、この冷媒送り管り30)の途中に冷媒調節弁(3
1)を設け、蒸発器(4)に内圧を検出する圧力検出器
(37)と冷媒蒸発温度を検出する温度検出器(38)
とを設け、更に温度検出器(38)と圧力検出器(37
)とから信号を入力し、蒸発器(4)の内圧から冷媒蒸
発温度を算出し、この算出した冷媒蒸発温度と検出した
冷、媒蒸発温度との差に基づいて冷媒調節弁を制御し、
蒸発器(4)の冷媒中の吸収液の重量濃度を0.2%な
いし4%の範囲に制御する制御装置を設けたことを特徴
とする吸収冷凍機を提供するものである。
Furthermore, an evaporator (4) having an absorber 5), a regenerator (1), (2), a condenser (3), and a heat transfer tube (22A).
In an absorption refrigerator that uses water as the refrigerant and lithium bromide solution as the absorption liquid, the absorber (5) is connected to the evaporator (4) between the absorber (5) and the evaporator (4). ) is provided, and an absorption liquid control valve (33) is provided in the middle of this absorption liquid feed pipe (32),
An evaporator (4) is provided between the evaporator (4) and the absorber (5).
) to the absorber (5), and a refrigerant control valve (3) is provided in the middle of this refrigerant feed pipe 30).
1), a pressure detector (37) for detecting the internal pressure and a temperature detector (38) for detecting the refrigerant evaporation temperature are provided in the evaporator (4).
Furthermore, a temperature sensor (38) and a pressure sensor (37) are provided.
), calculates the refrigerant evaporation temperature from the internal pressure of the evaporator (4), and controls the refrigerant control valve based on the difference between the calculated refrigerant evaporation temperature and the detected refrigerant evaporation temperature,
The present invention provides an absorption refrigerator characterized in that it is equipped with a control device that controls the weight concentration of the absorption liquid in the refrigerant of the evaporator (4) within a range of 0.2% to 4%.

(ホ)作用 蒸発器<4)の冷媒中の吸収液の重量濃度が0.2%な
いし4%の範囲であり、冷媒の表面張力が減少し、吸収
冷凍機の運転開始時等に伝熱管(22A)の外表面に油
等が付着している場合にも、伝熱管(22A)外表面で
の冷媒の濡れ性が向上し、伝熱管(22A )の外表面
にほぼ均一に冷媒が流れ、又、蒸発器(4)での冷媒蒸
発温度の低下を防止し、伝熱管(22A)での熱交換率
を向上させることが可能になる。
(e) The weight concentration of the absorption liquid in the refrigerant of the action evaporator <4) is in the range of 0.2% to 4%, and the surface tension of the refrigerant decreases, so that when the absorption refrigerator starts operating, etc. Even if oil or the like adheres to the outer surface of the heat exchanger tube (22A), the wettability of the refrigerant on the outer surface of the heat exchanger tube (22A) is improved, and the refrigerant flows almost uniformly on the outer surface of the heat exchanger tube (22A). Furthermore, it is possible to prevent a decrease in the refrigerant evaporation temperature in the evaporator (4) and improve the heat exchange rate in the heat exchanger tubes (22A).

又、吸収冷凍機の運転時、蒸発器(4)に設けられた比
重検出器(34)により冷媒の比重が検出され、この比
重に基づいて制御装置(35〉で算出された冷媒の吸収
液濃度に基づいて吸収液送り管(32〉の吸収液調節弁
(33)、及び冷媒送り管(30)の冷媒調節弁(31
〉が制御され、吸収液濃度が高いときには冷媒送り管(
30)を介して冷媒が吸収器(5)へ送られ吸収液濃度
が低下し、吸収液濃度が低いときには吸収液送り管(3
2)を介して吸収液が蒸発器(4)へ送られ、冷媒中の
吸収液の重量濃度が0.2%ないし4%の範囲に制御さ
れ、伝熱管(22A)の外表面での冷媒の濡れ性が向上
し、伝熱管(22A)での熱交換率を向上させることが
可能になる。
Also, when the absorption refrigerator is operating, the specific gravity of the refrigerant is detected by the specific gravity detector (34) provided in the evaporator (4), and the refrigerant absorption liquid calculated by the control device (35) based on this specific gravity is detected. Based on the concentration, the absorption liquid control valve (33) of the absorption liquid feed pipe (32) and the refrigerant control valve (31) of the refrigerant feed pipe (30) are
〉 is controlled, and when the absorption liquid concentration is high, the refrigerant feed pipe (
The refrigerant is sent to the absorber (5) via the absorber (5) and the absorbent concentration decreases.When the absorbent concentration is low, the absorbent feed pipe (30)
2), the absorption liquid is sent to the evaporator (4), and the weight concentration of the absorption liquid in the refrigerant is controlled in the range of 0.2% to 4%, and the refrigerant on the outer surface of the heat transfer tube (22A) is The wettability of the heat exchanger tube (22A) is improved, and the heat exchange rate in the heat exchanger tube (22A) can be improved.

更に、吸収冷凍機の運転時、蒸発器(4)に設けられた
圧力検出器(37)からの信号に基づいて冷媒蒸発温度
が算出され、この冷媒蒸発温度と冷媒温度検出器(38
)が検出した冷媒蒸発温度との差に基づいて吸収液調節
弁(33)、及び冷媒調節弁(31)が制御され、冷媒
の吸収液濃度が上昇し、上記温度差が大きくなったとき
には冷媒が冷媒送り管り30)を介して吸収器(5)へ
送られ吸収液濃度が低下しし、又、冷媒の吸収液濃度が
低下し、上記温度差が小さくなったときには吸収液が吸
収液送り管(32〉を介して蒸発器(4)へ送られ、冷
媒中の吸収液の重量濃度が0.2%ないし4%の範囲に
制御され、伝熱管(22A>外表面での冷媒の濡れ性が
向上し、蒸発器での熱交換率を向上きせることが可能に
なる。
Furthermore, during operation of the absorption refrigerator, the refrigerant evaporation temperature is calculated based on the signal from the pressure detector (37) provided in the evaporator (4), and the refrigerant evaporation temperature and the refrigerant temperature detector (38) are calculated.
), the absorption liquid control valve (33) and the refrigerant control valve (31) are controlled based on the difference between the refrigerant evaporation temperature and the refrigerant evaporation temperature detected by the refrigerant. is sent to the absorber (5) via the refrigerant feed pipe 30), and the concentration of the absorption liquid decreases.Also, when the concentration of the absorption liquid of the refrigerant decreases and the above temperature difference becomes small, the absorption liquid becomes the absorption liquid. The absorption liquid is sent to the evaporator (4) via the feed pipe (32), and the weight concentration of the absorption liquid in the refrigerant is controlled within the range of 0.2% to 4%. The wettability is improved and it becomes possible to improve the heat exchange rate in the evaporator.

(へ)実施例 以下、本発明の一実施例を図面に基づいて詳細に説明す
る。
(F) Example Hereinafter, an example of the present invention will be described in detail based on the drawings.

第1図に示したものは二重効用吸収冷凍機であり、冷媒
に水(H,O)、吸収剤(吸収液)に臭化リチウム(L
iBr)溶液、を使用したものである。ここで、臭化リ
チウム溶液には界面活性剤として例えばオクチルアルコ
ールが僅かに含まれている。
The one shown in Figure 1 is a dual-effect absorption refrigerator, with water (H, O) used as the refrigerant and lithium bromide (L) used as the absorbent (absorbing liquid).
iBr) solution. Here, the lithium bromide solution contains a small amount of octyl alcohol as a surfactant, for example.

第1図において、(1)はガスバーナ(IB)を備えた
高温再生器、(2)は低温再生器、(3)は凝縮器、り
4)は蒸発器、(5)は吸収器、(6)は低温熱交換器
、(7)は高温熱交換器、(8)ないしく12)は吸収
液配管、(15)は吸収液ポンプ、(16〉ないしく1
8)は冷媒配管、<19)は冷媒ポンプ、(20)はガ
スバーナ(IB)に接続されたガス配管、(21)は加
熱量制御弁、(22)は冷水配管であり、それぞれは第
1図に示したように配管接続されている。そして、冷媒
配管(18)の冷媒流出側には冷媒散布ト1/イ(18
A)が設けられ、このトレイ(18A)の下方に冷水配
管(22)の蒸発器熱交換器である伝熱管(22A)が
設けられている。又、(25)は冷却水配管であり、こ
の冷却水配管〈25)の途中には吸収器熱交換器(26
)、及び凝縮器熱交換器<27)が設けられている。
In Figure 1, (1) is a high temperature regenerator equipped with a gas burner (IB), (2) is a low temperature regenerator, (3) is a condenser, (4) is an evaporator, (5) is an absorber, ( 6) is a low temperature heat exchanger, (7) is a high temperature heat exchanger, (8) or 12) is an absorption liquid piping, (15) is an absorption liquid pump, (16> or 1)
8) is a refrigerant pipe, <19) is a refrigerant pump, (20) is a gas pipe connected to a gas burner (IB), (21) is a heating amount control valve, and (22) is a cold water pipe, each of which is connected to the first The piping is connected as shown in the figure. A refrigerant distribution tray (18) is provided on the refrigerant outlet side of the refrigerant pipe (18).
A) is provided, and a heat exchanger tube (22A) which is an evaporator heat exchanger for a cold water pipe (22) is provided below this tray (18A). Also, (25) is a cooling water pipe, and an absorber heat exchanger (26) is installed in the middle of this cooling water pipe (25).
), and a condenser heat exchanger <27).

さらに、第1図において、冷媒を蒸発器(4)に循環さ
せるための冷媒配管(18)の冷媒ポンプ(19)吐出
側と吸収器(5)の下部との間には冷媒送り管(30)
が配管され、この冷媒送や管り30)の途中には冷媒調
節弁(31)が設けられている。又、吸収液配管(8)
の吸収液ポンプ(15)吐出側と冷媒配’If(18)
の冷媒ポンプ(19)の吸入側との間には、吸収液送り
管(32)が配管され、この吸収液送り管(32)の途
中には吸収液調節弁(33)が設けられている。又、(
34)は蒸発器(4)の冷媒液溜め(4A)に取り付け
られ、冷媒液溜め(4A)に溜った冷媒の比重を検出す
る比重検出器である。更に、(35〉は比重検出器(3
4)、冷媒調節弁(31)、及び吸収液調節弁(33)
に接続された制御装置であり、この制御装置(35)は
比重検出器(34)からの信号に基づいて動作し、冷媒
中の吸収液濃度を算出し、吸収液濃度に基づいて冷媒調
節弁(31)、及び吸収液調節弁(33)へ信号を出力
し、それぞれの調節弁(31) 、 (33)は制御装
置(35)により制御される。
Furthermore, in FIG. 1, a refrigerant feed pipe (30 )
A refrigerant control valve (31) is provided in the middle of this refrigerant conveyance or pipe 30). Also, absorption liquid piping (8)
Absorption liquid pump (15) discharge side and refrigerant distribution 'If (18)
An absorption liquid feed pipe (32) is installed between the suction side of the refrigerant pump (19) and an absorption liquid control valve (33) is provided in the middle of this absorption liquid feed pipe (32). . or,(
34) is a specific gravity detector that is attached to the refrigerant reservoir (4A) of the evaporator (4) and detects the specific gravity of the refrigerant accumulated in the refrigerant reservoir (4A). Furthermore, (35> is a specific gravity detector (3
4), refrigerant control valve (31), and absorption liquid control valve (33)
This control device (35) operates based on the signal from the specific gravity detector (34), calculates the absorption liquid concentration in the refrigerant, and controls the refrigerant control valve based on the absorption liquid concentration. (31) and an absorption liquid control valve (33), and each control valve (31) and (33) is controlled by a control device (35).

以下、上記吸収冷凍機の動作について説明する。ここで
、吸収冷凍機の運転時には従来の吸収冷凍機と同様に各
配管を冷媒、及び吸収液が循環する。そして、冷媒液溜
め(4A)に溜った冷媒が冷媒配管(18)を流れてト
レイ(18A)から伝熱管(22A)に散布され、伝熱
管(22)内を流れる冷水が冷媒の気化熱により冷却き
れる。ここで、吸収冷凍機の設置後、初めての運転開始
時には、各調節弁(31) 、 (33)を閉本させて
おき、冷媒液溜め(4A)が満杯で負荷が100%のと
きに、冷媒中の吸収液の濃度が重量濃度で例えば1%に
なるように吸収液を冷媒に混入する。そして、吸収液を
冷媒に上記のように混入することにより、伝熱管(22
A>の外表面に油等が付着していた場合にも、伝熱管(
22A)外表面の冷媒の濡れ性が向上し、冷媒が伝熱管
(22A)の外表面はぼ全面にわたり流れる。又、冷媒
散布トレイ(18A)での濡れ性が向上し、伝熱管(2
2A)へほぼ均一に冷媒が散布される。この結果、伝熱
管(22A)での熱交換率が向上する。そして、第2図
の吸収液の重量濃度(以下吸収液濃度という)に対する
冷凍能力の実験結果にて明らかなように、冷媒に吸収液
を1%混入させた場合には純冷媒での冷凍能力を100
%とすると、103%まで冷凍能力が上昇する。そして
、吸収液濃度が0.2%ないし4%の範囲で冷凍能力が
純冷媒の場合より高くなる。
The operation of the absorption refrigerator will be explained below. Here, when the absorption refrigerator is in operation, the refrigerant and the absorption liquid circulate through each pipe as in the conventional absorption refrigerator. The refrigerant accumulated in the refrigerant reservoir (4A) flows through the refrigerant pipe (18) and is sprayed from the tray (18A) to the heat transfer tube (22A), and the cold water flowing inside the heat transfer tube (22) is caused by the heat of vaporization of the refrigerant. It can be cooled completely. Here, when starting operation for the first time after installing the absorption chiller, each control valve (31) and (33) are closed, and when the refrigerant reservoir (4A) is full and the load is 100%, The absorption liquid is mixed into the refrigerant so that the concentration of the absorption liquid in the refrigerant is, for example, 1% by weight. Then, by mixing the absorption liquid into the refrigerant as described above, the heat exchanger tube (22
Even if there is oil etc. on the outer surface of the heat exchanger tube (
22A) The wettability of the refrigerant on the outer surface is improved, and the refrigerant flows over almost the entire outer surface of the heat exchanger tube (22A). In addition, the wettability of the refrigerant distribution tray (18A) is improved, and the heat transfer tube (2
Refrigerant is almost uniformly distributed to 2A). As a result, the heat exchange efficiency in the heat exchanger tube (22A) is improved. As is clear from the experimental results of the refrigerating capacity with respect to the weight concentration of the absorption liquid (hereinafter referred to as absorption liquid concentration) in Figure 2, when 1% of the absorption liquid is mixed in the refrigerant, the refrigerating capacity of the pure refrigerant increases. 100
%, the freezing capacity increases to 103%. When the absorption liquid concentration is in the range of 0.2% to 4%, the refrigerating capacity becomes higher than in the case of pure refrigerant.

又、吸収冷凍機の運転開始後、冷媒中の吸収液濃度が低
下し、0.2%より低くなったときには比重検出器(3
4)からの信号に基づいて制御装置(35)が動作し、
吸収液調節弁(33)へ信号を出力し、吸収液調節弁(
33)が僅かに開く。そして、吸収液が吸収液送り管(
32)を介して冷媒配管(18)へ流れ、冷媒とともに
冷媒ポンプ(19)から吐出され伝熱管(22A)に散
布される。このため、冷媒液溜め(4A)の冷媒中の吸
収液濃度が上昇する。その後、比重検出器(34)から
の信号に基づいて制御装置(35)が動作し、吸収液濃
度が算出され、冷媒中の吸収液濃度が0.2%以上にな
り、4%より高くなった場合には制御装置(35)が動
作し吸収液調節弁(33)が閉じ、冷媒への吸収液の混
入が停止する。さらに、制御装置(35)からの信号に
基づいて冷媒調節弁(31)が開き、吸収液が混入して
いる冷媒が冷媒送り管(30)を介して吸収器(5)へ
流れ、吸収液が吸収器(5)へ戻され吸収液濃度が低下
する。そして、吸収液濃度が低下し、0.2%より低く
なったときには上記と同様に吸収液調節弁(33)が開
き蒸発器(4〉へ吸収液が送られる。以上のように、吸
収液濃度を0.2%ないし4%に保つことにより、伝熱
管(22A)での冷媒の濡れ性の向上、及びトレイ(1
8A)から伝熱管(22A)への冷媒散布の均一化が図
られる。
In addition, after the absorption refrigerating machine starts operating, if the absorption liquid concentration in the refrigerant decreases and becomes lower than 0.2%, the specific gravity detector (3
The control device (35) operates based on the signal from 4),
A signal is output to the absorption liquid control valve (33), and the absorption liquid control valve (
33) opens slightly. Then, the absorption liquid is transferred to the absorption liquid feed pipe (
32) to the refrigerant pipe (18), and is discharged together with the refrigerant from the refrigerant pump (19) and sprayed onto the heat exchanger tubes (22A). Therefore, the concentration of the absorption liquid in the refrigerant in the refrigerant reservoir (4A) increases. Thereafter, the control device (35) operates based on the signal from the specific gravity detector (34) and calculates the concentration of the absorbent, and when the concentration of the absorbent in the refrigerant becomes 0.2% or higher and higher than 4%. In this case, the control device (35) operates and the absorption liquid control valve (33) closes, stopping the absorption liquid from being mixed into the refrigerant. Further, the refrigerant control valve (31) opens based on a signal from the control device (35), and the refrigerant mixed with the absorption liquid flows to the absorber (5) via the refrigerant feed pipe (30), and the absorption liquid is returned to the absorber (5) and the concentration of the absorbent decreases. Then, when the absorption liquid concentration decreases and becomes lower than 0.2%, the absorption liquid control valve (33) opens in the same way as above and the absorption liquid is sent to the evaporator (4>. By keeping the concentration between 0.2% and 4%, the wettability of the refrigerant in the heat exchanger tube (22A) is improved and the refrigerant in the tray (1
8A) to the heat exchanger tubes (22A) can be uniformly distributed.

又、吸収液濃度の変化に基づいて吸収液調節弁(33)
、及び冷媒調節弁(31)の開度を変え、吸収器(5)
から蒸発器(4)へ流れる吸収液の量、及び蒸発器<4
)から吸収器(5)へ流れる吸収液を含んだ冷媒の量を
制御することにより、吸収液濃度をほぼ1%に制御する
ことにより、伝熱管(22A )での濡れ性が一層向上
し、トレイ(18A)からの冷媒散布がさらに均一にな
る。
In addition, the absorption liquid control valve (33)
, and by changing the opening degree of the refrigerant control valve (31), the absorber (5)
The amount of absorption liquid flowing from to the evaporator (4) and the evaporator <4
) by controlling the amount of refrigerant containing the absorption liquid flowing from the absorber (5) to the absorption liquid concentration to approximately 1%, the wettability in the heat transfer tube (22A) is further improved. Refrigerant distribution from the tray (18A) becomes more uniform.

上記実施例によれば、蒸発器(4)の冷媒中に重量濃度
で0.2%ないし4%の範囲の吸収液が混入しているた
め、冷媒の表面張力が減少し、吸収冷凍機の運転開始時
に伝熱管(22A )の外表面に油等が付着している場
合にも伝熱管(22A>外表面での冷媒の濡れ性を向上
させることができ、又、トレイ(18A)での濡れ性が
向上し冷媒をほぼ均一に伝熱管(22A >へ散布する
ことができ、更に、吸収液濃度が高いときに起こる蒸発
器(4)での冷媒蒸発温度の低下を肪止し、伝熱管(2
2A)での熱交換率が向上し、冷凍能力を向上させるこ
とができる。
According to the above embodiment, since the absorption liquid with a weight concentration in the range of 0.2% to 4% is mixed in the refrigerant of the evaporator (4), the surface tension of the refrigerant decreases, and the absorption refrigerating machine Even if oil or the like adheres to the outer surface of the heat exchanger tube (22A) at the start of operation, it is possible to improve the wettability of the refrigerant on the outer surface of the heat exchanger tube (22A). The wettability is improved, and the refrigerant can be almost uniformly distributed to the heat transfer tubes (22A). Furthermore, the drop in refrigerant evaporation temperature in the evaporator (4) that occurs when the absorption liquid concentration is high is suppressed, and the transfer is improved. Heat pipe (2
The heat exchange rate in 2A) is improved, and the refrigeration capacity can be improved.

又、吸収冷凍機の運転時、蒸発器(4〉に設けられた比
重検出器(34〉からの信号に基づいて吸収液濃度が制
御装置(35)にて算出され、吸収液濃度に基づいて冷
媒調節弁(31)及び吸収液調節弁(33)が制御きれ
るため、吸収器(5)から蒸発器(4)へ流れる吸収液
、及び蒸発器(4)から吸収器(5)へ流れる吸収液を
含んだ冷媒を調節し、吸収液濃度を0゜2%ないし4%
の範囲に保つことにより、吸収冷凍機の運転中の冷凍能
力を向上させることができる。
Furthermore, when the absorption refrigerator is in operation, the concentration of the absorption liquid is calculated by the control device (35) based on the signal from the specific gravity detector (34) installed in the evaporator (4), and the concentration of the absorption liquid is calculated based on the concentration of the absorption liquid. Since the refrigerant control valve (31) and the absorption liquid control valve (33) can be fully controlled, the absorption liquid flowing from the absorber (5) to the evaporator (4) and the absorption liquid flowing from the evaporator (4) to the absorber (5) Adjust the refrigerant containing the liquid, and adjust the absorption liquid concentration from 0°2% to 4%.
By maintaining the temperature within this range, the refrigerating capacity of the absorption refrigerator during operation can be improved.

ここで、上記実施例では比重検出器(34)からの信号
に基づいて吸収液濃度を算出したが、冷媒液溜め(4A
)に例えば超音波密度センサー(超音波密度と温度とに
より吸収液の濃度を求めるもの)を設け、このセンサー
からの信号に基づいて制御装置く35)が動作し、各調
節弁(31) 、 (33)の制御を行うようにした場
合にも同様な作用効果を得ることができる。又、各調節
弁<31) 、 (33)の開閉制御をタイマーを用い
て所定間隔ごとに行っても良い。
Here, in the above embodiment, the absorption liquid concentration was calculated based on the signal from the specific gravity detector (34), but the refrigerant liquid reservoir (4A
) is provided with, for example, an ultrasonic density sensor (which determines the concentration of the absorbent liquid based on ultrasonic density and temperature), and the control device (35) operates based on the signal from this sensor, and each of the control valves (31), Similar effects can be obtained when the control (33) is performed. Further, the opening and closing control of each of the control valves <31) and (33) may be performed at predetermined intervals using a timer.

又、他の実施例において第1図に破線にて示したように
蒸発器(4)に蒸発圧力を検出する圧力検出器(37)
を設け、さらに冷媒液溜め(4A)に冷媒温度検出器(
冷媒蒸発温度検出器)(38)を設け、蒸発器(4)内
の圧力から冷媒温度(冷媒蒸発温度)を算出し、実測し
た冷媒温度と比較する。ここで、純冷媒の場合、蒸発器
(4)の圧力から求めた冷媒温度と実測した冷媒温度と
の差はないが、冷媒への吸収液の混入の度合により上記
温度差が大きくなる。そして、冷媒中の吸収液濃度が4
%のときには上記温度差は0.5℃であった。従って、
上記温度差が045℃より大きくなったときに冷媒調節
弁(31)を開き、吸収液を含んだ冷媒を吸収器〈5)
へ戻すことにより、吸収液濃度を4%以下に抑えること
ができ、比較的安価な圧力計、及び温度計を用いて伝熱
管(22A)外表面での冷媒の濡れ性を向上させること
ができ、又、吸収液濃度の上昇に伴う・蒸発器(4)で
の熱交換率の低下を回避することができる。尚、上記の
ように蒸発器(4)の蒸発圧力と冷媒温度を検出し、算
出した冷媒温度と実測した冷媒温度との差に基づいて冷
媒調節弁<31)を制御する場合には、吸収液調節弁(
33)を手動弁とし、吸収冷凍機の運転開始時に吸収液
調節弁(33)を開き、吸収液濃度が0.2%ないし4
%の範囲になるように吸収液を冷媒へ混入することによ
り、吸収冷凍機の運転開始時の伝熱管(22A)等の冷
媒の濡れ性の向上を図り、冷凍能力の向上を図ることが
できる。
In another embodiment, a pressure detector (37) for detecting the evaporation pressure is installed in the evaporator (4) as shown by the broken line in FIG.
A refrigerant temperature detector (4A) is installed in the refrigerant reservoir (4A).
A refrigerant evaporation temperature detector) (38) is provided to calculate the refrigerant temperature (refrigerant evaporation temperature) from the pressure inside the evaporator (4) and compare it with the actually measured refrigerant temperature. Here, in the case of pure refrigerant, there is no difference between the refrigerant temperature determined from the pressure of the evaporator (4) and the actually measured refrigerant temperature, but the temperature difference increases depending on the degree of mixing of the absorption liquid into the refrigerant. Then, the absorption liquid concentration in the refrigerant is 4
%, the temperature difference was 0.5°C. Therefore,
When the above temperature difference becomes larger than 045℃, the refrigerant control valve (31) is opened and the refrigerant containing the absorption liquid is transferred to the absorber <5>.
By returning it to Furthermore, it is possible to avoid a decrease in the heat exchange rate in the evaporator (4) due to an increase in the concentration of the absorbent. In addition, when the evaporation pressure and refrigerant temperature of the evaporator (4) are detected as described above and the refrigerant control valve <31) is controlled based on the difference between the calculated refrigerant temperature and the actually measured refrigerant temperature, the absorption Liquid control valve (
33) is a manual valve, and the absorption liquid control valve (33) is opened when the absorption refrigerator starts operating, and the absorption liquid concentration is between 0.2% and 4%.
By mixing the absorption liquid into the refrigerant so that the absorption liquid falls within the range of .

(ト)発明の効果 本発明は以上のように構成された吸収冷凍機であり、蒸
発器で散布される冷媒中に重量濃度で0.2%ないし4
%の範囲の吸収液を混入しているため、冷媒の表面張力
が減少し、吸収冷凍機の設置後の運転開始時等に蒸発器
の伝熱管外表面に油等が付着している場合にも、伝熱管
での冷却の濡れ性を向上させることができ、又、伝熱管
へほぼ均一に冷媒を散布することができ、更に、蒸発器
での冷媒蒸発温度の低下を防止でき、この結果、蒸発器
での熱交換率を向上し、冷凍能力を向上させることがで
きる。
(G) Effects of the Invention The present invention is an absorption refrigerating machine configured as described above, in which the weight concentration of the refrigerant sprayed in the evaporator is 0.2% to 4%.
% of absorption liquid, the surface tension of the refrigerant decreases, and if oil, etc. adheres to the outer surface of the heat transfer tube of the evaporator when starting operation after installation of the absorption refrigerator, etc. It is also possible to improve the wettability of cooling in the heat exchanger tubes, to distribute the refrigerant almost uniformly to the heat exchanger tubes, and to prevent the refrigerant evaporation temperature from decreasing in the evaporator. , it is possible to improve the heat exchange rate in the evaporator and improve the refrigeration capacity.

又、蒸発器の冷媒の比重又は密度から吸収液濃度を算出
し、吸収液濃度に基づいて吸収液調節弁、及び冷媒調節
弁を制御し、冷媒中の吸収液の重量濃度を0.2%ない
し4%の範囲に制御することにより、吸収冷凍機の運転
中に、吸収液濃度が変化した場合にも、蒸発器の伝熱管
等の冷媒の濡れ性を向上させることができ、又、蒸発器
での冷媒蒸発温度の低下を防止でき、この結果冷凍源力
を向上させることができる。
Also, the absorption liquid concentration is calculated from the specific gravity or density of the refrigerant in the evaporator, and the absorption liquid control valve and the refrigerant control valve are controlled based on the absorption liquid concentration, and the weight concentration of the absorption liquid in the refrigerant is reduced to 0.2%. By controlling it within the range of 4% to 4%, even if the absorption liquid concentration changes during operation of the absorption refrigerator, it is possible to improve the wettability of the refrigerant in the heat transfer tubes of the evaporator, etc. It is possible to prevent the refrigerant evaporation temperature from decreasing in the container, and as a result, the power of the refrigeration source can be improved.

更に、蒸発器の内圧から冷媒蒸発温度を算出し、この冷
媒蒸発温度と実測の冷媒蒸発温度との差に基づいて冷媒
調節弁を制御し、冷媒中の吸収液の重量濃度を0.2%
ないし4%の範囲に制御することにより、比較的安価な
検出器を用いて伝熱管での冷媒の濡れ性を向上させるこ
とができると共に、蒸発器での熱交換率の低下を回避す
ることができる。
Furthermore, the refrigerant evaporation temperature is calculated from the internal pressure of the evaporator, and the refrigerant control valve is controlled based on the difference between this refrigerant evaporation temperature and the measured refrigerant evaporation temperature, and the weight concentration of the absorption liquid in the refrigerant is reduced to 0.2%.
By controlling the refrigerant to a range of 4% to 4%, it is possible to improve the wettability of the refrigerant in the heat exchanger tubes using a relatively inexpensive detector, and to avoid a decrease in the heat exchange rate in the evaporator. can.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例を示す吸収冷凍機の回路構成
図、第2図は吸収液濃度と冷凍能力との関係図である。 (1)・・・高温再生器、 (2)・・・低温再生器、
 (3)・・・凝縮器、 (4)・・・蒸発器、 (5
)・・・吸収器、 (30)・・・冷媒送り管、 (3
1)・・・冷媒調節弁、 (32)・・・吸収液送り管
、 り33)・・・吸収液調節弁、 (34)・・・比
重検出器、 (35)・・・制御装置、 (37)・・
・圧力検出器、 (38)・・・冷媒温度検出器。
FIG. 1 is a circuit diagram of an absorption refrigerator showing an embodiment of the present invention, and FIG. 2 is a diagram showing the relationship between absorption liquid concentration and refrigerating capacity. (1)...High temperature regenerator, (2)...Low temperature regenerator,
(3)... Condenser, (4)... Evaporator, (5
)...Absorber, (30)...Refrigerant feed pipe, (3
1)...refrigerant control valve, (32)...absorption liquid feed pipe, 33)...absorption liquid control valve, (34)...specific gravity detector, (35)...control device, (37)...
・Pressure detector, (38)...Refrigerant temperature detector.

Claims (1)

【特許請求の範囲】  1、吸収器、再生器、凝縮器、及び伝熱管を有した蒸
発器をそれぞれ配管接続し、冷媒に水、吸収液に臭化リ
チウム溶液を使用し、蒸発器に設けられた熱交換器の伝
熱管に冷媒を散布する吸収冷凍機において、蒸発器で散
布される冷媒に重量濃度で0.2%ないし4%の範囲の
吸収液を混入したことを特徴とする吸収冷凍機。  2、吸収器、再生器、凝縮器、及び伝熱管を有した蒸
発器をそれぞれ配管接続し、冷媒に水、吸収液に臭化リ
チウム溶液を使用した吸収冷凍機において、吸収器と蒸
発器との間に吸収器から蒸発器へ吸収液を導く吸収液送
り管を設け、この吸収液送り管の途中に吸収液調節弁を
設け、かつ、蒸発器と吸収器との間に蒸発器から吸収器
へ冷媒を導く冷媒送り管を設け、この冷媒送り管の途中
に冷媒調節弁を設け、蒸発器に冷媒の比重、或いは密度
を検出する検出器を設け、更にこの検出器から信号を入
力し、比重、或いは密度から冷媒の吸収液濃度を算出し
て吸収液濃度に基づいて吸収液調節弁、及び冷媒調節弁
を制御し、蒸発器の冷媒中の吸収液の重量濃度を0.2
%ないし4%の範囲に制御する制御装置を設けたことを
特徴とする吸収冷凍機。  3、吸収器、再生器、凝縮器、及び伝熱管を有した蒸
発器をそれぞれ配管接続し、冷媒に水、吸収液に臭化リ
チウム溶液を使用した吸収冷凍機において、吸収器と蒸
発器との間に吸収器から蒸発器へ吸収液を導く吸収液送
り管を設け、この吸収液送り管の途中に吸収液調節弁を
設け、かつ、蒸発器と吸収器との間に蒸発器から吸収器
へ冷媒を導く冷媒送り管を設け、この冷媒送り管の途中
に冷媒調節弁を設け、蒸発器に内圧を検出する圧力検出
器と冷媒蒸発温度を検出する温度検出器とを設け、更に
温度検出器と圧力検出器とから信号を入力し、蒸発器の
内圧から冷媒蒸発温度を算出し、この算出した冷媒蒸発
温度と検出した冷媒蒸発温度との差に基づいて冷媒調節
弁を制御し、蒸発器の冷媒中の吸収液の重量濃度を0.
2%ないし4%の範囲に制御する制御装置を設けたこと
を特徴とする吸収冷凍機。
[Scope of Claims] 1. An absorber, a regenerator, a condenser, and an evaporator having a heat transfer tube are connected to each other through piping, and water is used as a refrigerant and a lithium bromide solution is used as an absorption liquid. In an absorption refrigerating machine that sprays a refrigerant into the heat transfer tubes of a heat exchanger, an absorption liquid having a weight concentration of 0.2% to 4% is mixed into the refrigerant sprayed in the evaporator. refrigerator. 2. In an absorption refrigerator that uses water as a refrigerant and lithium bromide solution as an absorption liquid, the absorber, regenerator, condenser, and evaporator with heat transfer tubes are connected through piping. An absorption liquid feed pipe is provided between the absorber and the absorber to guide the absorption liquid from the absorber to the evaporator, and an absorption liquid control valve is provided in the middle of this absorption liquid feed pipe, and between the evaporator and the absorber, the absorption liquid is A refrigerant feed pipe is provided to guide the refrigerant to the refrigerant, a refrigerant control valve is provided in the middle of the refrigerant feed pipe, a detector is provided in the evaporator to detect the specific gravity or density of the refrigerant, and a signal is input from this detector. , calculate the absorption liquid concentration of the refrigerant from the specific gravity or density, control the absorption liquid control valve and the refrigerant control valve based on the absorption liquid concentration, and set the weight concentration of the absorption liquid in the refrigerant of the evaporator to 0.2.
An absorption refrigerating machine characterized in that it is equipped with a control device that controls the temperature within the range of % to 4%. 3. In an absorption refrigerator that uses water as the refrigerant and lithium bromide solution as the absorption liquid, the absorber, regenerator, condenser, and evaporator with heat transfer tubes are connected through piping. An absorption liquid feed pipe is provided between the absorber and the absorber to guide the absorption liquid from the absorber to the evaporator, and an absorption liquid control valve is provided in the middle of this absorption liquid feed pipe, and between the evaporator and the absorber, the absorption liquid is A refrigerant feed pipe is provided to guide the refrigerant to the refrigerant, a refrigerant control valve is provided in the middle of the refrigerant feed pipe, a pressure detector to detect the internal pressure and a temperature detector to detect the refrigerant evaporation temperature are provided in the evaporator, and a temperature detector is provided to detect the refrigerant evaporation temperature. Inputting signals from the detector and the pressure detector, calculating the refrigerant evaporation temperature from the internal pressure of the evaporator, and controlling the refrigerant control valve based on the difference between the calculated refrigerant evaporation temperature and the detected refrigerant evaporation temperature, The weight concentration of the absorption liquid in the refrigerant of the evaporator is set to 0.
An absorption refrigerating machine characterized by being provided with a control device that controls the temperature within a range of 2% to 4%.
JP2293689A 1989-01-31 1989-01-31 Absorption type refrigerator Pending JPH02203166A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2293689A JPH02203166A (en) 1989-01-31 1989-01-31 Absorption type refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2293689A JPH02203166A (en) 1989-01-31 1989-01-31 Absorption type refrigerator

Publications (1)

Publication Number Publication Date
JPH02203166A true JPH02203166A (en) 1990-08-13

Family

ID=12096518

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2293689A Pending JPH02203166A (en) 1989-01-31 1989-01-31 Absorption type refrigerator

Country Status (1)

Country Link
JP (1) JPH02203166A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008202873A (en) * 2007-02-21 2008-09-04 Daikin Ind Ltd Absorption refrigeration system
JP2019027626A (en) * 2017-07-27 2019-02-21 株式会社日立製作所 Absorption freezing machine
CN113175772A (en) * 2020-01-24 2021-07-27 矢崎能源系统公司 Absorption refrigerator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS613960A (en) * 1984-06-15 1986-01-09 三洋電機株式会社 Absorption refrigerator
JPS6248148A (en) * 1985-08-27 1987-03-02 Nec Corp Communication system with highest priority in loop network

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS613960A (en) * 1984-06-15 1986-01-09 三洋電機株式会社 Absorption refrigerator
JPS6248148A (en) * 1985-08-27 1987-03-02 Nec Corp Communication system with highest priority in loop network

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008202873A (en) * 2007-02-21 2008-09-04 Daikin Ind Ltd Absorption refrigeration system
JP2019027626A (en) * 2017-07-27 2019-02-21 株式会社日立製作所 Absorption freezing machine
CN113175772A (en) * 2020-01-24 2021-07-27 矢崎能源系统公司 Absorption refrigerator
CN113175772B (en) * 2020-01-24 2022-07-05 矢崎能源系统公司 Absorption refrigerator

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