JPH0280879A - Temperature differential valve - Google Patents

Temperature differential valve

Info

Publication number
JPH0280879A
JPH0280879A JP23131588A JP23131588A JPH0280879A JP H0280879 A JPH0280879 A JP H0280879A JP 23131588 A JP23131588 A JP 23131588A JP 23131588 A JP23131588 A JP 23131588A JP H0280879 A JPH0280879 A JP H0280879A
Authority
JP
Japan
Prior art keywords
temperature
fluid
valve
valve member
refrigerant
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
JP23131588A
Other languages
Japanese (ja)
Inventor
Shotaro Wakita
脇田 祥太郎
Junzo Sakamoto
坂本 淳三
Shiro Igarashi
史郎 五十嵐
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries 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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP23131588A priority Critical patent/JPH0280879A/en
Publication of JPH0280879A publication Critical patent/JPH0280879A/en
Pending legal-status Critical Current

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  • Temperature-Responsive Valves (AREA)

Abstract

PURPOSE:To automatically keep a temperature difference between fluids within a designated temperature range by automatically driving a valve member by the first and second temperature sensing springs made of a shape memory alloy, which have sensed the temperature of both fluids to change the flow ratio between both fluids. CONSTITUTION:The acting force Fx of the first temperature sensing spring 10 which is made of a shape memory alloy and deformed on sensing the temperature Tx of the first fluid X and the acting force Fy of the second temperature sensing spring 20 adapted to deform on sensing the temperature Ty of the second fluid Y are loaded on a valve member 6, and the opening Gx of the first valve passage portion 16 and the opening Gy of the second valve passage portion 26 are regulated to decide the flow rate Sx, Sy of both fluids X, Y. For example, in case of applying the valve to a distribution valve of a refrigerating unit, though the first fluid X passes through the first evaporating coil 41 in the refrigerating unit and the second fluid Y passes through the second evaporating coil 42, the valve member 6 is displaced in either direction to reduce a temperature difference DELTAT between both cooling media X, Y. Thus, various apparatus to which both the first and second fluids are supplied can be operated with the maximum efficiency.

Description

【発明の詳細な説明】 (産業上の利用分野) 本願発明は流量の変化に応じて温度が変化する第1、第
2両流体のそれぞれの温度を検知して、核内流体の温度
差か所定温度範囲内に収まるように該両流体の流量比を
制御するために使用されろ温度差動弁に関するものであ
る。
Detailed Description of the Invention (Industrial Application Field) The present invention detects the respective temperatures of the first and second fluids whose temperatures change according to changes in flow rate, and detects the temperature difference between the fluids in the core. The present invention relates to a temperature differential valve used to control the flow rate ratio of both fluids so as to stay within a predetermined temperature range.

(従来の技術) 従来、例えは蒸発器に複数系統の蒸発コイルか組込まれ
ている冷凍装置においては、蒸発器の各蒸発コイルに分
配する冷媒の流量比か適切てないと、各蒸発コイルごと
に過熱度が異なり、蒸発器全体としての最高の冷却能力
を発揮さU−ることかできない。
(Prior art) Conventionally, for example, in a refrigeration system in which multiple systems of evaporator coils are incorporated in the evaporator, if the flow rate ratio of refrigerant distributed to each evaporator coil of the evaporator is not appropriate, each evaporator coil The degree of superheat is different between the two, and the maximum cooling capacity of the evaporator as a whole cannot be achieved.

又、1つの冷凍装置て多室の冷暖房を行うような空調ノ
ステムにおけるように、各室に設置されている室内機へ
の冷媒分配を均等に行う必要かある場合に、それか適切
に行イつれないと、各室ごとに冷暖房能力か一定せず不
都合か生じる。
In addition, when it is necessary to evenly distribute the refrigerant to the indoor units installed in each room, such as in an air conditioning system where one refrigeration system cools and heats multiple rooms, it is necessary to distribute the refrigerant evenly to the indoor units installed in each room. If not, the heating and cooling capacity will vary from room to room, which can be inconvenient.

従来、冷凍装置における冷媒分配器としては種々の形態
のちのがある(たとえば実開昭57−167377号公
報)が、その多くは複数系統の蒸発コイルなりあるいは
室内機なりへ単に一定比率で冷媒を分配するた(」の機
能しか有せず、蒸発器の各蒸発コイルやあるいは各室内
機の需要に応じて冷媒の流量比を調節する機能を有する
ものは見当らない。
Conventionally, there are various types of refrigerant distributors in refrigeration equipment (for example, Japanese Utility Model Application No. 57-167377), but most of them simply distribute refrigerant at a fixed ratio to multiple systems of evaporator coils or indoor units. It only has the function of distributing the refrigerant, and there is no one that has the function of adjusting the flow rate ratio of the refrigerant according to the demand of each evaporator coil of the evaporator or each indoor unit.

(発明が解決しようとする課題) 本願発明は、」−記の冷凍装置中の冷媒分配器のように
、複数系統を流通オろ流体の流量比を制御するにあたり
、それぞれの系統の流体の温度を検知し、各流体間の温
度差が自動的に所定温度範囲内に収まるように(一系統
の流体が他系統の流体に対して過度に温度上冒したり、
あるいは温度降下したりすることのないように)してそ
れらの流体が流通する各種機器が全体としてもっとも高
効率で機能し得るようにしようとするものであり、しか
もその場合に、各流体の温度を検知する手段と、その温
度に対応じて各流体の流量比を制御する手段とを1つの
ケーノング内に収納一体化して、その取扱い(各種機器
に対する着脱作業等)を容易にし得るようにしようとす
るものである。
(Problems to be Solved by the Invention) The present invention provides a method for controlling the flow rate ratio of the filtrate fluid flowing through multiple systems, such as the refrigerant distributor in the refrigeration equipment described in ``-'', by controlling the temperature of the fluid in each system. is detected, and the temperature difference between each fluid is automatically kept within a predetermined temperature range.
The aim is to ensure that the various devices through which these fluids flow can function with the highest overall efficiency by ensuring that the temperature of each fluid does not drop. A means for detecting the temperature and a means for controlling the flow rate ratio of each fluid according to the temperature can be housed and integrated in one caning so that its handling (installation and removal work for various devices, etc.) can be made easier. That is.

(課題を解決するたぬの手段) 本件出願では、上記の課題を解決するための手段として
、請求項第1項の発明においては、第1図及び第2図に
例示する如く、流量Sxの変化にしたがって温度TXが
変化する第1の流体Xを通過せしめる第1流体通路14
と流量syの変化にしたがって温度’h”yか変化する
第2の流体Yを通過せしめる第2流体通路24とを有す
るケーシング5と、該ケーシング5内で変位して前記第
1流体通路14を流通する第1流体Xと前記第2流体通
路24を流通する第2流体Yの流量比Sx/Syを変化
さ且る作用をする弁部材6と、前記第1流体通路14中
に置かれて前記弁部材6をイ」勢するとともに前記第1
流体Xの温度Txに感応じて該弁部材6に対する作用力
Fxが変化する形状記憶合金製の第1の感温バネIOと
、前記第2流体通路24中に置かれて前記弁部材6を(
=1勢するとともに前記第2流体Yの温度1゛yに感応
じて該弁部材6に対する作用力Fyが変化する形状記憶
合金製の第2の感温バネ20をそなえるとともに、前記
第1の感温バネ10と第2の感温バネ20は前記第1流
体Xの温度Txと第2流体Yの温度TVの差温ΔTを一
定の温度範囲内に維持するように前記弁部+A6による
前記第1、第2両流体x、yの流量比制御を行うべく該
弁部材6に対するそれぞれの温度−作用力特性を規定(
7ていることを特徴どしている。
(Unlikely means for solving the problem) In the present application, as a means for solving the above problem, in the invention of claim 1, as illustrated in FIGS. 1 and 2, the flow rate Sx is A first fluid passage 14 through which a first fluid X whose temperature TX changes according to the change in temperature passes through it.
and a second fluid passage 24 through which a second fluid Y whose temperature 'h''y changes as the flow rate sy changes; a valve member 6 which acts to change the flow rate ratio Sx/Sy of the first fluid X flowing through the second fluid passage 24 and the second fluid Y flowing through the second fluid passage 24; While pushing the valve member 6 upward, the first
A first temperature-sensitive spring IO made of a shape memory alloy whose acting force Fx on the valve member 6 changes depending on the temperature Tx of the fluid (
= 1 force, and a second temperature-sensitive spring 20 made of a shape memory alloy that changes the acting force Fy on the valve member 6 in accordance with the temperature 1y of the second fluid Y; The temperature sensitive spring 10 and the second temperature sensitive spring 20 are operated by the valve portion +A6 so as to maintain the temperature difference ΔT between the temperature Tx of the first fluid X and the temperature TV of the second fluid Y within a certain temperature range. In order to control the flow rate ratio of both the first and second fluids x and y, the respective temperature-acting force characteristics for the valve member 6 are defined (
7.

又、請求項第2項の発明においては、第1の流体Xど第
2の流体Yが冷凍装置にお(Jろ2系統の第1、第2の
蒸発コイル41.42を通過する第1、第2の分岐冷媒
流であり、第1の感温バネ10と第2の感温バネ20を
前記2系統の蒸発コイル4+、42通過後の各分岐冷媒
流の温度TX、Tyを感知する如くしたことを特徴とし
ている。
In addition, in the invention of claim 2, the first fluid , which is a second branched refrigerant flow, and senses the temperature TX, Ty of each branched refrigerant flow after passing through the two systems of evaporator coils 4+, 42 through the first temperature-sensing spring 10 and the second temperature-sensing spring 20. It is characterized by what happened.

さらに、請求項第3項の発明においては、グーソング5
内の第1流体通路14が第1蒸発コイル41へ向う湿り
状態の第2両分岐冷媒流X1の往路となる往路部14.
 Aと該第1蒸発コイル41から還流オろ乾き状態の第
2両分岐冷媒流X1の復路となる復路部14Bとに分割
されるとともに同ケーシング5内の第2流体通路24が
第2蒸発コイル42へ向う湿り状態の第2分岐冷媒流Y
、の往路となる往路部24Aと該第2蒸発コイル42か
ら還流する乾き状態の第2分岐冷媒流Y、の復路となる
復路部24 Bどに分割されており、且つ第1、第2の
各感温バネ10.20をそれぞれの流体通路14.24
の各復路部14 B 、 24. Bに、又弁部+A’
 6を前記第1、第2各流体通路14.24の各往路部
+ 4 A、24△にあって前記各感温バネ10.20
が感知する各乾き状態の第1、第2両分岐冷媒流X、、
Y、の温度Tx、Tyに応じて前記第1、第2の両流体
通路14.24の各往路部14A、24Aを通過する湿
り状態の第1、第2両分岐冷媒流X1、、y 、の流量
比Sx/Syを制御する如くしていることを特徴として
いるとしている。
Furthermore, in the invention of claim 3, the Goo Song 5
The first fluid passage 14 in the outgoing path portion 14 is the outgoing path of the wet second branched refrigerant flow X1 toward the first evaporator coil 41.
A and a return path section 14B, which is the return path of the second branched refrigerant flow X1 in a recirculated or dry state from the first evaporator coil 41, and the second fluid passage 24 in the casing 5 is connected to the second evaporator coil. A wet second branch refrigerant flow Y toward 42
, and a return path section 24B, which is the return path of the dry second branch refrigerant flow Y flowing back from the second evaporator coil 42. Each temperature sensitive spring 10.20 is connected to a respective fluid passage 14.24.
Each return portion 14B, 24. B, valve part +A'
6 is located at each outgoing path portion of the first and second fluid passages 14.24 + 4 A, 24△ and each of the temperature sensitive springs 10.20
Both the first and second branch refrigerant flows X in each dry state sensed by
The wet first and second branch refrigerant flows X1, y, which pass through the outgoing portions 14A and 24A of the first and second fluid passages 14.24 according to the temperatures Tx and Ty of Y, respectively. It is said that the feature is that the flow rate ratio Sx/Sy of is controlled.

(作 用) 本願の請求項第1項の発明においては、第1流体Xの温
度TXを感知して変形する形状記憶合金製の第1の感温
バネ10の作用力Fxと第2流体Yの温度’ryを感知
して変形する第2の感温バネ20の作用力Fyとが弁部
材6に負荷され、上記両件用力Fx、Fyのバランスす
るところで第1流体Xの流量を制御する第1弁通路部1
6の開度GXと第2流体Yの流量を制御する第2弁通路
部26の開度Gyが規定される。そして、その開度Gx
Gyに応じて両流体X、Yの流量sx、syか決定され
る。
(Function) In the invention of claim 1 of the present application, the acting force Fx of the first temperature-sensitive spring 10 made of a shape memory alloy that deforms by sensing the temperature TX of the first fluid X and the second fluid Y The acting force Fy of the second temperature-sensitive spring 20, which deforms upon sensing the temperature 'ry, is applied to the valve member 6, and the flow rate of the first fluid First valve passage section 1
The opening degree GX of 6 and the opening degree Gy of the second valve passage section 26 that controls the flow rate of the second fluid Y are defined. And its opening Gx
The flow rates sx and sy of both fluids X and Y are determined according to Gy.

第1流体Xの温度Txと第2流体Yの温度Tyが相対的
に変化し、その差温ΔTに変化が生じると、それまで弁
部材6に負荷されていた2つの感温バネの作用力Fx、
Fyのバランスか崩れ、弁部材6が変位せしめられる。
When the temperature Tx of the first fluid X and the temperature Ty of the second fluid Y change relatively and a change occurs in the temperature difference ΔT, the acting force of the two temperature-sensitive springs that was previously loaded on the valve member 6 Fx,
Fy becomes unbalanced and the valve member 6 is displaced.

それに伴って両弁通路部16.26の開度Gx、Gyが
変化して両流体X、Yの流ff1sx、syか変化する
か、その流量変化は第1、第2両流体X、Yの温度差Δ
Tを小さくさせる方向に向けて生じろ。
Along with this, the opening degrees Gx and Gy of both the valve passages 16.26 change, and the flows ff1sx and sy of both the fluids X and Y change. Temperature difference Δ
Produce in the direction that makes T smaller.

次に、本願の請求項第2項の発明は、上記請求項第1項
の発明を冷凍装置の分配弁に適用した場合に関するもの
で、第1流体Xは冷凍装置における第1蒸発コイル/1
1を通過し、第2流体Yは第2蒸発コイル42を通過す
る。ずなわち、第1感温バネ10と第2感ldIバネ2
0はそれぞれ蒸発コイル通過後のガス冷媒X、Yに接触
してその温度TXTyの変化に応じて変形し、弁部f、
A6に対する作用力が変化する。その作用力の変化は、
その作用力の変化によって弁部材6がいづれかの方向に
変位し、その変位に応じて両冷媒X、Yの流量比が変化
し、さらにその流量比の変化にしたがって両冷媒X、Y
の温度差Δ′Fが小さくなるような方向に生じる。
Next, the invention of claim 2 of the present application relates to the case where the invention of claim 1 is applied to a distribution valve of a refrigeration system, and the first fluid
1, and the second fluid Y passes through the second evaporator coil 42. That is, the first temperature sensitive spring 10 and the second temperature sensitive spring 2
0 contact the gas refrigerants X and Y after passing through the evaporator coils and deform according to the change in temperature TXTy, and the valve parts f,
The acting force on A6 changes. The change in the acting force is
The valve member 6 is displaced in either direction due to the change in the acting force, and the flow rate ratio of both refrigerants X and Y changes according to the displacement, and further, the flow rate ratio of both refrigerants X and Y changes according to the change in the flow rate ratio.
occurs in the direction in which the temperature difference Δ'F becomes smaller.

次に、本願の請求項第3項の発明は、第1.第2各流体
(冷媒)x、yが流通する流体通路14.24をそれぞ
れ、蒸発器4の各蒸発コイル41,42へ至るまての湿
り状態の冷媒が通過する往路部14A、24Aと、蒸発
器4の各蒸発コイル4142通過後の乾き状態の冷媒が
通過する復路部14 B、24 Bとに分け、蒸発器4
通過後の乾き状態の冷媒の温度’I”、x、Tyを検知
して、蒸発器4へ供給される湿り状態の冷媒の流量比S
X/SYを制御しようとするものである。オなイっち、
この請求項第3項の発明によれば、蒸発器4の各蒸発コ
イル41.42通過後の乾き状態の冷媒の温度状態に対
応じて、それらの各蒸発コイル4142へ供給される湿
り状態の圧縮機の流量をそれぞれの蒸発コイル41,4
2の入[」側において加減しようとするものである。
Next, the invention of claim 3 of the present application is as follows. Outgoing path portions 14A and 24A through which wet refrigerant passes through fluid passages 14 and 24 through which second fluids (refrigerants) x and y flow, respectively, to reach the evaporator coils 41 and 42 of the evaporator 4; The evaporator 4 is divided into return path sections 14B and 24B through which dry refrigerant passes after passing through each evaporator coil 4142 of the evaporator 4.
The temperature 'I'', x, Ty of the dry refrigerant after passing through is detected, and the flow rate ratio S of the wet refrigerant supplied to the evaporator 4 is determined.
The purpose is to control X/SY. It's so hot,
According to the invention of claim 3, the temperature of the dry refrigerant after passing through each of the evaporator coils 41 and 42 of the evaporator 4 corresponds to the temperature of the wet refrigerant supplied to each of the evaporator coils 4142. The flow rate of the compressor is adjusted to each evaporator coil 41, 4.
This is an attempt to make adjustments on the input side of 2.

(発明の効果) 本願の請求項第1項の発明の温度差動弁によれば、量弁
を流通する第1、第2の両流体X、Yは、それぞれの温
度T x 、 T yの変化にしたかってその流量比か
制御されるから、何らかの原因で両方の流体X、Yの間
に流量の不均衡が生じ、それによって両流体x、y間の
温度差か許容限度をこえろような状況が生じた場合でも
、両流体X、Yの温度を感知した形状記憶合金製の第1
、第2の両惑星バネ10.20が自動的に弁部材6を駆
動して両流体X、Yの流量比を変化させるので、上記の
ような両流体x、y間の流量の不均衡は自動的に修正さ
れる。したがって第1、第2両流体の供給をう(プる各
種機器、たとえば冷凍装置の蒸発器4や、多室型空調装
置の各室内機などはそれぞれ最高効率で運転可能となる
。
(Effects of the Invention) According to the temperature differential valve of the invention set forth in claim 1 of the present application, both the first and second fluids X and Y flowing through the volume valve have their respective temperatures T x and T y. Since the flow rate ratio is controlled depending on the change, if for some reason an imbalance occurs in the flow rates between both fluids X and Y, the temperature difference between the two fluids Even if the situation arises, the first one made of shape memory alloy that senses the temperature of both fluids X and Y
, the second planetary spring 10.20 automatically drives the valve member 6 to change the flow rate ratio of both fluids X and Y, so that the imbalance in the flow rates between both fluids x and y as described above Corrected automatically. Therefore, various devices that rely on the supply of both the first and second fluids, such as the evaporator 4 of the refrigeration system and the indoor units of the multi-room air conditioner, can each operate at maximum efficiency.

次に、本願の請求項第2項の発明では、」二足請求項第
1項の発明の効果が特に冷凍装置の蒸発器4において効
果的に実現するものである。
Next, in the invention of claim 2 of the present application, the effect of the invention of claim 1 is particularly effectively realized in the evaporator 4 of the refrigeration system.

又、本願の請求項第3項の発明では、蒸発器4の各蒸発
コイル41.42通過後の各系統の乾き状態の冷媒の温
度を感知して、それぞれの蒸発コイル41.42へ供給
される湿り状態の冷媒の流量比を各蒸発コイル/II、
42の入口側で制御するものであるから、流量比の不均
衡是正が迅速に行イつれるという効果かある。
Further, in the invention of claim 3 of the present application, the temperature of the dry refrigerant in each system after passing through each evaporator coil 41, 42 of the evaporator 4 is sensed, and the temperature of the dry refrigerant is supplied to each evaporator coil 41, 42. The flow rate ratio of the wet refrigerant is determined by each evaporator coil/II,
Since the control is performed on the inlet side of 42, it has the effect that the imbalance in the flow rate ratio can be quickly corrected.

(実施例) 以下、第1図ないし第4図を参照して本願各発明の好適
な実施例を説明する。
(Embodiments) Hereinafter, preferred embodiments of each invention of the present application will be described with reference to FIGS. 1 to 4.

第1図は、請求項第1項及び第2項の各発明に対応する
実施例の温度差動弁を示すものであり、ここでは同温度
差動弁は冷凍装置の蒸発器における2系統の蒸発コイル
を流通する冷媒の流量比を制御するために使用されてい
る。
FIG. 1 shows a temperature differential valve according to an embodiment corresponding to the inventions of claims 1 and 2. Here, the temperature differential valve is used in two systems in an evaporator of a refrigeration system. It is used to control the flow rate ratio of refrigerant flowing through the evaporator coil.

第1図において符号1け圧縮機、2は凝縮器、3は膨張
弁又(Jキャピラリーチコーブ等の減圧装置、4は蒸発
器を示している。蒸発器4には2系統の蒸発コイル/1
1.42が組込まれており、減圧装置3通過後の減圧液
冷媒がこの2系統の第1蒸発コイル41及び第2蒸発コ
イル42に分流して蒸発器4を通過づ−ろ。請求項第1
項の発明の実施例にかかる温度差動弁50は、蒸発器4
と圧縮機1の間に介設されて蒸発器4の第1蒸発コイル
41を通過する第1の冷媒分岐流(請求項第1項、第2
項中の第1流体に該当する)Xの流量SXと蒸発器4の
第2蒸発コイル42を通過する第2の冷媒分岐流(請求
項第1項、第2項中の第2流体に該当する)Yの流量S
yの比Sx/Syを制御する。
In Fig. 1, the number 1 is a compressor, 2 is a condenser, 3 is an expansion valve or a pressure reducing device such as a J capillary reach cove, and 4 is an evaporator. 1
1.42 is incorporated, and the reduced pressure liquid refrigerant after passing through the pressure reducing device 3 is divided into the first evaporator coil 41 and the second evaporator coil 42 of these two systems and passes through the evaporator 4. Claim 1
The temperature differential valve 50 according to the embodiment of the invention in section
A first refrigerant branch flow that is interposed between the compressor 1 and the compressor 1 and passes through the first evaporator coil 41 of the evaporator 4.
The second refrigerant branch flow passing through the second evaporator coil 42 of the evaporator 4 (corresponding to the second fluid in the first and second claims) ) Y flow rate S
The ratio Sx/Sy of y is controlled.

第1冷媒分岐流Xと第2冷媒分岐流Yは温度差動弁50
で合流して圧縮機Iへ還流する。
The first refrigerant branch flow X and the second refrigerant branch flow Y are controlled by a temperature differential valve 50.
The two converge and flow back to compressor I.

上記の温度差動弁50の構造と作用を第1図、第2図を
併用して説明すると、この温度差動弁50は筒形のケー
シング5の両端に第1冷媒分岐流Xが流入する第1人口
ボート11と第2冷媒分岐流Yが流入する第2人口ボー
ト21を有し、さらにその中間部に第11第2両冷媒分
岐流が合流して流出する出口ボート31を有している。
The structure and operation of the temperature differential valve 50 will be explained with reference to FIGS. 1 and 2. In the temperature differential valve 50, the first refrigerant branch flow X flows into both ends of the cylindrical casing 5. It has a second artificial boat 21 into which the first artificial boat 11 and the second refrigerant branch flow Y flow, and further has an outlet boat 31 in the middle thereof through which both the eleventh and second refrigerant branch flows merge and flow out. There is.

ケーンアク5内には出口ポート3Iに対向する位置に弁
部材6が収容されてケーシング5内を第1人ロボート1
1と出口ボート31の間に形成される第1流体通路14
と第2人L1ボート21と出口ボート31の間に形成さ
れる第2流体通路24とに区画している。
A valve member 6 is housed in the cane ac 5 at a position facing the outlet port 3I, and the first robot 1 is inserted into the casing 5.
1 and the outlet boat 31 .
and a second fluid passage 24 formed between the second person L1 boat 21 and the exit boat 31.

弁部44’ Gの両端には第1弁体部61と第2弁体部
62の2つの弁体部が形成されている。ケーシング5内
の一方の第1流体通路14内には一方の第1弁体部61
に対向して第1弁座部15が形成され、この第1弁体部
61と第1弁座部15との間に第1冷媒分岐流Xか流通
する第1弁通路部16が形成され、他方の第2流体通路
24内には他方の第2弁体部62に対向して第2弁座部
25が形成され、この第2弁体部62と第2弁座部25
どの間に第2冷媒分岐流Yが流通する第2弁通路部26
が形成されている。これらの第1、第2の2つの弁通路
部16.26は、弁部材6の変位によってその開度GX
、Gyが変化せしめられる。すなわち、この両弁通路部
16.26は弁部材6の変位に応じてその一方の開度G
X(又はGy)が大きくなれば、他方の開度Gy(又は
GX)が小さくなるという関係にあり、弁部材6の変位
にしたがってそれぞれの弁通路部16.26を流通する
両冷媒分岐流X、Yの流量比SX/SYを変化させる如
く作用オろ。
Two valve body parts, a first valve body part 61 and a second valve body part 62, are formed at both ends of the valve part 44'G. One first valve body portion 61 is disposed within one first fluid passage 14 in the casing 5.
A first valve seat portion 15 is formed opposite to the first valve body portion 61 and a first valve passage portion 16 through which the first refrigerant branch flow X flows is formed between the first valve body portion 61 and the first valve seat portion 15. A second valve seat portion 25 is formed in the other second fluid passage 24 facing the other second valve body portion 62, and the second valve body portion 62 and the second valve seat portion 25
a second valve passage section 26 through which the second refrigerant branch flow Y flows;
is formed. The opening degree GX of these two first and second valve passage sections 16.26 is changed by the displacement of the valve member 6.
, Gy are changed. That is, the opening degree G of one of the two valve passage portions 16.26 changes depending on the displacement of the valve member 6.
As X (or Gy) increases, the opening degree Gy (or GX) of the other side decreases. , Y to change the flow rate ratio SX/SY.

ケーシング5の第11第2の各流体通路1424にはそ
れぞれ弁部材6を付勢するためのバネ(第1感温バネI
Oと第2感温バネ20)か設けられている。これらの各
感温バネ10.20は、所定の温度領域内では温度の変
化にともなって変形)〜、それに応じて弁部材6に対す
る作用力(FxFy)か変化オろような特性をイ」与さ
れた形状記憶合金て作られている。
Each of the eleventh and second fluid passages 1424 of the casing 5 is provided with a spring (first temperature-sensitive spring I) for biasing the valve member 6.
O and a second temperature-sensitive spring 20) are provided. Each of these temperature-sensitive springs 10, 20 has characteristics such that the force (FxFy) applied to the valve member 6 changes accordingly. It is made from a shape memory alloy.

第1図及び第2図において符号45は第1感温バネl0
Z)一端を位置決めする有孔のバネ受板、46(J第2
感温バネ20の一端を位置決めする有孔のバネ受板であ
り、Iy11〜L IBはそれぞれ冷媒配管を示してい
る。
In FIGS. 1 and 2, reference numeral 45 indicates the first temperature-sensitive spring l0.
Z) Perforated spring receiving plate for positioning one end, 46 (J second
This is a perforated spring receiving plate that positions one end of the temperature-sensitive spring 20, and Iy11 to LIB each indicate a refrigerant pipe.

第2図及び第3図は、」二足の第1感温バネ10及び第
2感温バネ20の各作用力(Fx、Fy)の変化と第1
弁通路部16の開度Gxならびに第2弁通路部26の開
度cyの変化の関係を示す説明図である。
FIGS. 2 and 3 show the changes in the acting forces (Fx, Fy) of the first and second temperature-sensing springs 10 and 20, and the
FIG. 2 is an explanatory diagram showing the relationship between changes in the opening degree Gx of the valve passage section 16 and the opening degree cy of the second valve passage section 26;

第1図及び第2図において、第1感温バネ10は蒸発器
4の第1蒸発コイル41通過後の第1冷媒分岐流(第1
流体)Xと接触して温度Tx=Txの状態にある。さら
に第2感温バネ20は蒸発器4の第2蒸発コイル42通
過後の第2冷媒分岐流(第2流体)Yと接触して温度T
 ”l ”” T Y lの状態にある。又、弁部材6
は任意の乱点S。からストロークS u= S L+、
の位置にあり、そのとき、第1弁通路部16は開度G 
X= G x、、第2弁通路部26は開度G Y ” 
G )’ +に設定される。
1 and 2, the first temperature-sensitive spring 10 is connected to a first refrigerant branch flow after passing through the first evaporator coil 41 of the evaporator 4.
It is in contact with fluid (fluid) X and is in a state of temperature Tx=Tx. Furthermore, the second temperature-sensitive spring 20 comes into contact with the second branched refrigerant flow (second fluid) Y after passing through the second evaporator coil 42 of the evaporator 4, and the temperature T
"l"" T Y l state. Also, the valve member 6
is an arbitrary random point S. From stroke S u= S L+,
, and at that time, the first valve passage section 16 has an opening degree G
X=G x, the second valve passage section 26 has an opening degree G Y ”
G)' +.

第2図において符号10′は温度Tx=Tx+の状態下
にある第1感温バネ10の自由状態(自由長さ(lX=
QX、)を示し、符号20′は温度’ry′ryIの状
態下にある第2感温ノくネ20の自由状態(自由長さ(
ly=uy+)を示している。
In FIG. 2, reference numeral 10' indicates the free state (free length (lX=
QX, ), and 20' indicates the free state (free length (
ly=uy+).

これらの各バネ10.20はケーシング5内に組込まれ
た状態ではそれぞれ自由状態から圧縮されて、第1感温
バネ10はケーノング内長さ(lxmuxm、(そのと
きの圧縮量(C1xn)= nxn、= (lx。
Each of these springs 10 and 20 is compressed from its free state when it is assembled in the casing 5, and the first temperature-sensitive spring 10 has a canon inner length (lxmuxm, (amount of compression at that time (C1xn) = nxn , = (lx.

−Ilxm、)、第2感温バネ20はケーソンク内長さ
uym−σym+(そのときの圧縮量(σyn) =(
lyn+(l Y+−fl ym+)となる。
- Ilxm, ), the second temperature-sensitive spring 20 has a caissonk inner length uym - σym + (amount of compression at that time (σyn) = (
lyn+(l Y+-fl ym+).

」−紀行温度状態にある各バネ10.20の)<ネ定数
(Kx、KOを第1感温バネlOについてはKxKx+
(温度TX−T X +において)、第2感温ノくネ2
0Eつい”i:L:LKy=Ky+(?W度T V−”
 Tyeニおし)で)とすると、それぞれの温度状態に
おいて、各バネ10.20が弁部材6に負荷する作用力
(ノクネ定数×バネ圧縮量)は次のj;うになる。
”-KxKx+ for the first temperature-sensitive spring lO
(at temperature TX - TX +), second temperature sensing node 2
0E just "i:L:LKy=Ky+(?W degree T V-"
In each temperature state, the acting force (Nokune constant x spring compression amount) that each spring 10.20 loads on the valve member 6 is as follows.

第1感温バネ10の作用力(Fx−・FX1)F XI
 = K XI X (l X11+Kx+X(ux+
    nxm+)  ・  ・  ・  ・ (])
第2感温バネ20の作用力(F y= F y+)F’
/+ =Ky+X 1lyn Ky+X(見yl−旦ym+)・・・・(2)そ1.て
、この両バネ10.20のそれぞれの作用力F x(F
 XI)、 F y(−P y+)が、F X l =
 P y の関係になるところで弁部kA6が停止せしめられ、そ
の位置に対応じて第1、第2各弁通路部1626の開度
Gが決定される(開度Gx=Gx、、GyGy+)。
Acting force of the first temperature-sensitive spring 10 (Fx-・FX1) F XI
= K XI X (l X11+Kx+X(ux+
nxm+) ・ ・ ・ ・ (])
Acting force of the second temperature-sensitive spring 20 (F y=F y+)F'
/+ =Ky+X 1lyn Ky+X (seeyl-tanym+)...(2) Part 1. Then, the acting force F x (F
XI), F y (-P y+) is F X l =
The valve part kA6 is stopped when the relationship P y is reached, and the opening degree G of each of the first and second valve passage parts 1626 is determined according to that position (opening degree Gx=Gx, , GyGy+).

なお、本実施例では、本願発明を適用して、第1感温バ
ネ10と第2感温ノ\ネ20は所定の温度領域において
は温度変化にしたがって変形(自由長さαX、αyが変
化)し、且つバネ定数K x 、 K yが変化する形
状記憶合金を使用している。
In this embodiment, by applying the present invention, the first temperature-sensitive spring 10 and the second temperature-sensitive spring 20 are deformed (the free lengths αX and αy are changed) according to temperature changes in a predetermined temperature range. ) and uses a shape memory alloy whose spring constants K x and K y change.

すなわち、これらの第1、第2各感温バネ1020は、
それぞれ特定の温度ごとに特定の7\ネ定数と特定の自
由長さ(換言すればケーシング5内でのバネ圧縮量)を
有することになり、したがって特定の温度ごとに弁部材
6に対する作用力特性(バネ特性)を有することになる
。
That is, these first and second temperature-sensitive springs 1020 are as follows:
Each has a specific spring constant and a specific free length (in other words, the amount of spring compression within the casing 5) for each specific temperature, and therefore the acting force characteristics on the valve member 6 for each specific temperature. (spring characteristics).

第3図において(I、)は第1の感温バネ10の、温度
T x= T、 XIにおけるバネ特性線図、(I2)
は同温度T x= T X2(T x2> T x+)
i:おける同バネノバネ特性線図、(I3)は同温度T
 x= T X3(T X3< T x)にお(Jろ同
バネのバネ特性線図を示している。
In FIG. 3, (I,) is a spring characteristic diagram of the first temperature-sensitive spring 10 at temperature T x = T, XI, (I2)
is the same temperature T x = T x2 (T x2 > T x+)
i: The characteristic diagram of the spring at the same temperature, (I3) is the same temperature T
x= T X3 (T X3 < T

又、(■、)は第2感温バネ20の温度T V −’ 
T ”/ 1におけるバネ特性線図、(■、)は同温度
T y= T V2(Ty2>Tx1)にお(Jる同バ
ネのバネ特性線図、(■、)は同温度T y= T Y
3(T Y3< T Y1)におけろ同バネのバネ特性
線図を示している。
Moreover, (■,) is the temperature T V −' of the second temperature-sensitive spring 20
The spring characteristic diagram at T ''/1, (■,) is the spring characteristic diagram of the same spring at the same temperature Ty = T V2 (Ty2>Tx1), (■,) is the spring characteristic diagram at the same temperature Ty = T TY
3 (T Y3 < T Y1).

なお、第1図、第2図に示す温度差動弁50においては
、弁部材6に対する作用力は第1感温バネ10と、第2
感温バネ20とては相互に反対方向に作用するため、第
3図に示すそれらのバネ特性線図の傾斜が相−りに逆向
きとなっている。
In the temperature differential valve 50 shown in FIGS. 1 and 2, the acting force on the valve member 6 is caused by the first temperature-sensitive spring 10 and the second
Since the temperature sensitive springs 20 act in opposite directions, the slopes of their spring characteristic diagrams shown in FIG. 3 are in opposite directions.

第1図及び第2図において、第1冷媒分岐流(第1流体
)Xの温度Tx=Txい第2冷媒分岐流(第2流体)Y
の温度T V = T Y +の状態で弁部材6かス1
− ローフS u= S ul (第1弁通路部16の
開度GXG X、、第2弁通路部26の開度Gy=Gy
+)で静止しているとする。このとき、弁部材6に負荷
されている2つのバネのイ乍用力(Fx、Fy)を、第
1感温バネ10についてはFx=Pxい第2感温バネ2
0についてはF Y ” F Y tとすると、それら
の作用力FX、F)+は、 Fx、=Fy の関係にあり(第3図、点1)、の状態)、そのとき弁
部材6はス1−ローク5u=Su+の位置にある。
In FIGS. 1 and 2, the temperature of the first refrigerant branch flow (first fluid)
When the temperature of the valve member 6 is T V = T Y +,
- Loaf S u = S ul (opening degree GXG X of the first valve passage section 16, opening degree Gy of the second valve passage section 26 = Gy
+) and is at rest. At this time, the forces (Fx, Fy) of the two springs loaded on the valve member 6 are calculated as Fx=Px for the first temperature-sensitive spring 10 and
When F Stroke 1 - Stroke 5u = Su+ position.

このとき、第1冷媒分岐流(第1流体)Xの温度TX1
と第2冷媒分岐流(第2流体)Yの温度TY+の差Δ′
rはTXI  Txl−ΔT、で、この差温△T1は、
当初から設定されている所定の許容温度範囲T c内に
ある。
At this time, the temperature TX1 of the first refrigerant branch flow (first fluid)
and the temperature TY+ of the second refrigerant branch flow (second fluid) Y
r is TXI Txl−ΔT, and this temperature difference ΔT1 is
It is within the predetermined allowable temperature range Tc that has been set from the beginning.

次に、上記第1、第2両流体X、Yの差温△T(仮に、
Txl<Tylとする)が、たとえば第2蒸発コイル4
2側にお(ジる吸熱負荷増大にともなう第2冷媒分岐流
(第2流体)Yの温度上昇(T y= T y+−”T
yJにより拡大変化(ΔT−ΔT、−ΔT2sS、−3
2)L、それにともなって、第2感温バネ20のバネ特
性が変化、すなわち、同バネ20のバネ特性線図が第3
図上の(II、)から(■、)に移行したとする(この
とき、第1冷媒分岐流(第1流体)Xの温度はTxlの
まま変化がない、したか−)で第1感温バネ10につい
てけ特性線図(1,)のままバネ特性に変化かないとす
る)。
Next, the temperature difference ΔT between the first and second fluids X and Y (temporarily,
Txl<Tyl), for example, the second evaporator coil 4
The temperature rise of the second refrigerant branch flow (second fluid) Y due to the increase in the heat absorption load on the second side (T y=T
Expansion change due to yJ (ΔT−ΔT, −ΔT2sS, −3
2) L, the spring characteristics of the second temperature-sensitive spring 20 change accordingly, that is, the spring characteristics diagram of the second temperature-sensitive spring 20 changes to the third temperature-sensitive spring 20.
Suppose that the transition occurs from (II,) to (■,) in the diagram (at this time, the temperature of the first refrigerant branch flow (first fluid) X remains Txl and does not change, right?). Assume that there is no change in the spring characteristics as shown in the characteristic diagram (1,) for the warm spring 10).

この場合、第2感温バネ20はその温度上4により弁部
材6に対4−る作用力が増大し、該弁部材6を、第1感
温バネ10の作用力に抗して当該第1感温バネ10を圧
縮オる方向に変位させ、同弁部材6をΔSL+またり変
位させた位置(Su2)において新たな釣合状態に移行
−七ろ(第3図中、点]〕2の状態)。
In this case, the second temperature-sensitive spring 20 has an increased acting force on the valve member 6 due to its temperature, and the second temperature-sensitive spring 20 acts on the valve member 6 against the acting force of the first temperature-sensitive spring 10. 1 Displace the temperature-sensitive spring 10 in the direction of compression and shift the valve member 6 to a new balanced state at the position (Su2) where it is displaced by ΔSL+ - Shichiro (point in Figure 3)] 2 condition).

弁部材6がΔSu2だけ右行変位すると、それにともな
って第1弁通路部I6の開度OXがGx、からOX2に
減少して第1蒸発コイル41側の冷媒分流量を減少させ
る一方で第2弁通路部26の開度Gyh<Gy+からG
x2に増大し、第2蒸発コイル42への冷媒分流量を増
加さ且、第2冷媒分岐流(第2流体)Yの温度−1−昇
を抑制する。その結果、第G 1、第2両流体X、Yの差温ΔTを所定の温度範囲Tc
内に収れんさせる。
When the valve member 6 is displaced to the right by ΔSu2, the opening degree OX of the first valve passage portion I6 decreases from Gx to OX2, reducing the refrigerant branch flow rate on the first evaporator coil 41 side, while reducing the second valve passage portion I6. Opening degree of the valve passage section 26 Gyh<Gy+ to G
x2, increasing the refrigerant branch flow rate to the second evaporator coil 42 and suppressing the temperature -1 rise of the second refrigerant branch flow (second fluid) Y. As a result, the temperature difference ΔT between the G1 and second fluids X and Y is set within a predetermined temperature range Tc.
Converge within.

なお、」−記とは逆に第2蒸発コイル42側での吸熱量
減少等により、第1冷媒分岐流(第1流体)Xの温度は
T x +のままで、第2冷媒分岐流(第2流体)Yの
温度Tyが低下(Ty=−’1.”y+−”Fy3)し
た場合は、第3図中の点P3の状態で両バネl0120
の作用力(Fx3. F Y3)がバランスし、弁部十
オ6をSuaまで左行変位させる(第1弁通路部16の
開度GXがOX、からGL3に増大して第1蒸発コイル
/II側の冷媒分流量を増大さ且る−・方で、第2弁通
路部26側の開度GyがGY+からGx3に減少し、そ
れによって第2蒸発コイル42への冷媒分流量が減少し
、第2冷媒分岐流Yの温度TYを上昇させる)。このよ
うにして第11第2両流体XYの温度バランスがt(B
持される。
In addition, contrary to the description in "-", due to a decrease in the amount of heat absorbed on the second evaporator coil 42 side, etc., the temperature of the first refrigerant branch flow (first fluid) X remains T x +, and the temperature of the second refrigerant branch flow ( When the temperature Ty of the second fluid) Y decreases (Ty=-'1."y+-"Fy3), both springs l0120 in the state of point P3 in FIG.
The acting force (Fx3. Increasing the refrigerant division flow rate on the II side, the opening degree Gy of the second valve passage portion 26 side decreases from GY+ to Gx3, thereby reducing the refrigerant division flow rate to the second evaporator coil 42. , increasing the temperature TY of the second refrigerant branch Y). In this way, the temperature balance of both the eleventh and second fluids XY is maintained at t(B
held.

なお、第3図において点P 4(T X= T X4 
T YTY4)は点P 1(Tx=Tx+、 Ty=T
y+)を基準として、(T X4 > T XI、TY
t−’TV+)の場合の各バネの作用力のバランス状態
、点P s(T x= T X5T y1”、Y:、)
は(T X5< T X、、T l/、=−T y+)
の場合、点P6(Tx=’f”x6.Ty−Tye)は
(Txe<TXI、T y e < Ty1)の場合、
点P 7(T X −TX7. T y−’r )”r
)はTX?> T X l、i’、” Y 7 > T
 Y + )の場合、点P 8(T x= T X8′
ry ”’I”Ys)は(Tx8<’rXI、TYe>
TY+)の場合、点P 9(T x= T X9. T
 y= ’I’ y9)は(Tx9 > ′r X l
、Tys < T y + )の場合の各バネ間の作用
力のバランス状態をそれぞれ示している。
In addition, in Fig. 3, point P 4 (T X = T
TYTY4) is the point P1 (Tx=Tx+, Ty=T
y+) as a reference, (T X4 > T XI, TY
Balance state of the acting force of each spring in the case of t-'TV+), point P s (T x = T X5T y1'', Y:,)
is (Tx5<Tx,,Tl/,=-Ty+)
In the case of , the point P6 (Tx='f''x6.Ty-Tye) is (Txe<TXI, Tye<Ty1),
Point P 7 (T X −TX7.T y−'r )”r
) is TX? > T X l, i'," Y 7 > T
Y + ), then point P 8 (T x = T
ry "'I"Ys) is (Tx8<'rXI,TYe>
TY+), point P 9 (T x= T
y = 'I' y9) is (Tx9 >'r X l
, Tys < Ty + ), the balance state of the acting force between each spring is shown.

4−記名状態の1つの例として、点P7の状態について
説明オろと、この状態は点P1の状態に比へれば、第1
流体Xの温度T”Xも第2流体Yの温度T yもともに
上昇した場合を示しているが、この場合は第1、第2両
流体X、Yの温度差ΔTΔ1′7それ自体は小さいため
、その差温△1゛7を所定温度範囲Tc内に収れんさU
るための第1、第2両弁通路部+6,26開度Gx、G
yの変化量、すなわち、弁部材6の変位量(ΔSu−Δ
S u7)は小さくてよいことを示している。
4-As an example of the registered state, let us explain the state of point P7.This state is compared to the state of point P1.
This shows a case where both the temperature T''X of the fluid X and the temperature Ty of the second fluid Y have increased, but in this case, the temperature difference ΔTΔ1'7 between the first and second fluids X and Y is itself small. Therefore, the temperature difference △1゛7 is converged within the predetermined temperature range Tc.
Both the first and second valve passages + 6, 26 opening degrees Gx, G
The amount of change in y, that is, the amount of displacement of the valve member 6 (ΔSu−Δ
This shows that S u7) may be small.

又、」―紀行状態のもう1つの例として、点P8の状態
について説明すると、この状態は点P、の状態に比へれ
ば、第1冷媒分岐流(第1流体)Xの温度Txは低下(
Tx=Tx8<Tx+)しているにもかかわらず、第2
蒸発コイル42側での熱負荷の増加が大きくて第2冷媒
分岐流(第2流体)Yの温度TYが」−昇(Ty=Ty
a>Ty+)した場合を示しているが、この場合は、第
11第2両流体X、Yの温度差ΔT−△T8が大きくな
っているため、その差温ΔT8を所定温度範囲Tc内に
収れんさせるための第1、第2両弁通路部16.26の
開度GXayの調整量、すなわち弁部材6の変位量(Δ
SuΔS u8)が上記開度Gx減少、Gy増加の方向
に大きくなる(第1蒸発コイル4I側に比して第2蒸発
コイル42側への冷媒分流量か極端に大きくなる)こと
を示している。
Furthermore, as another example of the traveling state, the state at point P8 will be explained. If this state is compared to the state at point P, the temperature Tx of the first refrigerant branch flow (first fluid) X is Decrease (
Although Tx=Tx8<Tx+), the second
The increase in heat load on the evaporator coil 42 side is large, and the temperature TY of the second refrigerant branch flow (second fluid) Y increases (Ty=Ty
a>Ty+), but in this case, the temperature difference ΔT−ΔT8 between the 11th and 2nd fluids X and Y is large, so the temperature difference ΔT8 is kept within the predetermined temperature range Tc. The amount of adjustment of the opening degree GXay of both the first and second valve passage portions 16.26 for convergence, that is, the amount of displacement of the valve member 6 (Δ
SuΔS u8) increases in the direction of the above-mentioned opening Gx decrease and Gy increase (the refrigerant divided flow rate to the second evaporator coil 42 side becomes extremely large compared to the first evaporator coil 4I side). .

第4図は、請求項第3項の発明に対応する実施例を示す
もので、同図中、符号lは圧縮機、2は凝縮器、3は減
圧装置、4は蒸発器、I72.〜I7,9は冷媒配管を
示している。蒸発器4には2系統の第1蒸発コイル41
と第2蒸発コイル42とが組込まれている。
FIG. 4 shows an embodiment corresponding to the invention of claim 3, in which reference numeral 1 is a compressor, 2 is a condenser, 3 is a pressure reducing device, 4 is an evaporator, I72. - I7, 9 indicate refrigerant piping. The evaporator 4 has two systems of first evaporator coils 41.
and a second evaporator coil 42 are incorporated.

この実施例で使用される温度差動弁は、減圧装置3通過
後の冷媒を2系統の分岐流に分割して流通させるような
通路構成を有している。すなわち、第4図図示の温度差
動弁50は、大別してケーシング5と、冷媒流を第1冷
媒分岐流と第2冷媒分岐流に分割する弁部材6と、該弁
部材6に作用力を伺与゛4−ろ2つの感温バネ10.2
0とからなっており、該ケーシング5には、減圧装置3
通過後の湿り状態の冷媒Wが流入する主入ロポート31
と、第1冷媒分岐流X(蒸発器4の第1蒸発コイル41
へ向う湿り状態の冷媒X+)が流出する第1分岐流第1
出1月ボート17と、同第1冷媒分岐流X(湿り状態の
冷媒X、)が蒸発器4の第1蒸発コイル41通過後に乾
き状態の冷媒X、となって流入する第1分岐流入ロボー
ト18と、同乾き状態の冷媒分岐流X2か流出する第1
分岐流第2出ロボート19と、第2冷媒分岐流Y(蒸発
器4の第2蒸発コイル7I2へ向う湿り状態の冷媒Y、
)が流1)鴇ケる第2分岐流第1出日ボー)・27と、
同第2冷媒分岐流Y(湿り状態の冷媒Y、)が蒸発器4
の第2蒸発コイル42通過後に乾き状態の冷媒Y2とな
って流入する第2分岐流入ロボート28と、同乾き状態
の冷媒分岐流Y2が流出する第2分岐流第2出ロボート
29とを有している。
The temperature differential valve used in this embodiment has a passage structure that divides the refrigerant after passing through the pressure reducing device 3 into two branched flows and allows them to flow. That is, the temperature differential valve 50 shown in FIG. Two temperature-sensitive springs 10.2
0, and the casing 5 includes a pressure reducing device 3.
Main inlet port 31 into which the wet refrigerant W flows after passing through
and the first refrigerant branch flow X (the first evaporator coil 41 of the evaporator 4
The first branch flow from which the wet refrigerant
A first branch inflow robot into which the first refrigerant branch flow X (wet refrigerant X) flows as dry refrigerant X after passing through the first evaporator coil 41 of the evaporator 4. 18 and the same dry refrigerant branch flow X2 flows out from the first
The second branched flow robot 19 and the second branched refrigerant flow Y (wet refrigerant Y heading toward the second evaporator coil 7I2 of the evaporator 4,
) ga flow 1) Tokikeru 2nd branch flow 1st dehibo) ・27 and,
The second refrigerant branch flow Y (wet refrigerant Y) is transferred to the evaporator 4
It has a second branch inflow robot 28 into which the dry refrigerant Y2 flows after passing through the second evaporator coil 42, and a second branch flow second outflow robot 29 through which the dry refrigerant branch flow Y2 flows out. ing.

第4図図示の温度差動弁50では弁部材6は、主入ロボ
ート31から流入する気液混合で湿り状態の冷媒を第1
分岐流第1出ロボート17へ向う第1冷媒分岐流X (
X 、)と第2分岐流第1出1」ボート27へ向う第2
冷媒分岐Mty(y、)とに分流させ、且つその流量比
を制御する作用をする。
In the temperature differential valve 50 shown in FIG.
Branch flow First refrigerant branch flow X toward the first output robot 17 (
X ,) and the second branch stream 1st exit 1'' 2nd heading towards boat 27
The refrigerant branches Mty(y,) and controls the flow rate ratio thereof.

以」二のように、この実施例では第1冷媒分岐流Xのた
めの第1流体通路14は、減圧装置3から蒸発器4の第
1蒸発コイル41へ向う湿り状態の第1冷媒分岐流X 
(X 、)が流通する往路部14Aと、蒸発器4の第1
蒸発コイル41通過後の乾き状態の第1冷媒分岐流X 
(X 、)が流通する復路部14Bとに区画され、又、
第2冷媒分岐流Yのための第2流体通路24は、蒸発器
4の第2蒸発コイル42へ向う湿り状態の第2冷媒分岐
流Y (Y 、)が流通する往路部2/IAと、蒸発器
4の第2蒸発コイル42通過後の乾き状態の第2冷媒分
岐イY(Y2)が流通する復路部24 Bとに区画され
ている。
As described above, in this embodiment, the first fluid passage 14 for the first branched refrigerant flow X
(X,) flows through the outgoing path section 14A and the first
Dry first refrigerant branch flow X after passing through the evaporator coil 41
(X,) is divided into a return route section 14B through which
The second fluid passage 24 for the second branched refrigerant flow Y includes an outgoing path portion 2/IA through which a wet second branched refrigerant flow Y (Y,) toward the second evaporator coil 42 of the evaporator 4 flows; The second refrigerant branch A (Y2) in a dry state after passing through the second evaporator coil 42 of the evaporator 4 is divided into a return path section 24B and a return path section 24B.

第1流体通路往路部+ 4. Aの途中には弁部材6の
一方の弁体部(第1弁体部)61に対向する位置におい
て弁座部(第1弁座部)15が形成されており、この第
1弁体部6Iと第1弁座部15との間に湿り状態の第1
冷媒分岐流X (X t)の通路となる弁通路部(第1
弁通路部)16が形成されている。
First fluid passageway section+4. A valve seat portion (first valve seat portion) 15 is formed in the middle of A at a position facing one valve body portion (first valve body portion) 61 of the valve member 6, and this first valve body portion 6I and the first valve seat part 15 in a wet state.
Valve passage section (first
A valve passage portion) 16 is formed.

又、第2流体通路往路部24. Aの途中には弁部材6
のもう一方の弁体部(第2弁体部)62に対向する位置
において弁座部(第2弁座部)25が形成されており、
この第2弁体部62と第2弁座部25との間に湿り状態
の第2冷媒分岐流y (y 1)の通路となる弁通路部
(第2弁通路部)26が形成されている。
Also, the second fluid passage outward path portion 24. There is a valve member 6 in the middle of A.
A valve seat portion (second valve seat portion) 25 is formed at a position facing the other valve body portion (second valve body portion) 62,
A valve passage portion (second valve passage portion) 26 is formed between the second valve body portion 62 and the second valve seat portion 25, and serves as a passage for the wet second refrigerant branch flow y (y 1). There is.

この第4図図示の温度差動弁50においては、弁部材6
に作用力を付与オろ形状記憶合金製の第1、第2の感温
バネ10.20は、第1感温バネ10については第1流
体通路14の復路部14Bに、又第2感温バネ20につ
いては第2流体通路24の復路部24. Bにそれぞれ
配置される。
In the temperature differential valve 50 shown in FIG.
The first and second temperature-sensitive springs 10.20 made of a shape memory alloy are applied to the return path 14B of the first fluid passage 14 for the first temperature-sensing spring 10, and to the return path 14B of the first fluid passage 14. Regarding the spring 20, the return path 24 of the second fluid passage 24. They are placed in B respectively.

一方、弁部材6には第1流体通路復路部1413に達す
る第10ノド63と第2流体通路復路部24Bに達する
第20ヅド64が付設されていて、弁部材6は第10ツ
ト63を介して第1感温バネ10より作用ツノFXを受
けるとともに、第20ツト64を介して第2感温バネ2
0より作用力Fyを受けるようにされている。
On the other hand, the valve member 6 is provided with a tenth throat 63 that reaches the first fluid passage return passage portion 1413 and a twentieth throat 64 that reaches the second fluid passage return passage portion 24B. It receives the action horn FX from the first temperature-sensitive spring 10 through the 20th horn 64, and receives the action horn FX from the second temperature-sensing spring 2 through the 20th horn 64.
It is adapted to receive an acting force Fy from 0.

すなわち、この第4図図示の温度差動弁50では、弁部
材6は、乾き状態の第1冷媒分岐流X(X、)と接触し
その温度Txの変化にしたがって作用力Fxか変化する
第1感温バネ10と同しく乾き状態の第2冷媒分岐流Y
(Y2)と接触しその温度Tyの変化にしたがって作用
力Fyが変化する第2感温バネ20の両者から作用力を
う()て変位し、その変位にしたがって湿り状態の第1
冷媒分岐流X (X 、)の流量SXと同しく湿り状態
の第2冷媒分岐流y (y 、)の流m S yとの比
Sx/Syを制御するように作用するものである。
That is, in the temperature differential valve 50 shown in FIG. 4, the valve member 6 contacts the dry first refrigerant branch flow 1 The second refrigerant branch flow Y in a dry state like the temperature-sensitive spring 10
(Y2) and whose acting force Fy changes according to the change in temperature Ty, is displaced by the acting force () from both of them, and according to the displacement, the first temperature sensitive spring 20 in a wet state
It acts to control the ratio Sx/Sy between the flow rate SX of the refrigerant branch flow X (X,) and the flow m S y of the second refrigerant branch flow y (y,) which is also wet.

このように、蒸発器4の入口側において各冷媒分岐流x
、yの流量比制御を行う場合は、第1、第2両感温バネ
10.20で両流体X、Yの温度TxTyのアンバラン
スを感知してからその是正、すなわち第1、第2両流体
X、Yの流量比SX/Syの制御までに要する時間が短
かくてすみ、制御系の応答性及び精度が向」−する。
In this way, on the inlet side of the evaporator 4, each refrigerant branch flow x
, y, first and second temperature sensing springs 10.20 detect the imbalance in the temperatures TxTy of both fluids X and Y, and then correct the imbalance. The time required to control the flow rate ratio SX/Sy of fluids X and Y is shortened, and the responsiveness and accuracy of the control system are improved.

この第4図図示の温度差動弁50において、第1、第2
各感温バネ10.20がその温度の変化にしたがって弁
部材6に対する作用力Fx、FYを変化させ、それにし
たがって第1、第2両流体XYの流量比SX/SYを制
御するに至る過程は第1図図示の温度差動弁50の場合
と同様であるのでその説明!J省略する。
In the temperature differential valve 50 shown in FIG.
The process in which each temperature-sensitive spring 10.20 changes the acting force Fx, FY on the valve member 6 according to the change in temperature, and controls the flow rate ratio SX/SY of the first and second fluids XY accordingly is as follows. This is the same as the case of the temperature differential valve 50 shown in FIG. 1, so let's explain it! J is omitted.

第4図において、仮想線で示ず配管り、 3o 、 1
.−3は、乾き状態の第1、第2各冷媒分岐流X 2 
、 Y 2の主流(x 7.、y 2.)を温度差動弁
50をバイパスして直接圧縮機Iへ還流さ■るためのバ
イパス配管を示している。このようなノ\イパス配管L
3゜■731を設置′、lた場合は、乾き状態の第1、
第2各冷媒分岐流X7.Y2はその一部X 2 、+ 
Y 22が第1、第2感温バネ10.20の制御用流体
として温度差動弁50の第1流体通路14の復路部14
. B又は第2流体通路24の復路部24Bへ供給され
、残余の主流部分X、1.Y2+は直接圧縮機1へ吸入
される。
In Fig. 4, piping not shown by imaginary lines, 3o, 1
.. -3 is the first and second refrigerant branch flow X 2 in a dry state
, Y2 (x7., y2.) bypassing the temperature differential valve 50 and directly returning it to the compressor I. This kind of path piping L
When installing 3゜■731, install the first one in a dry state,
Second respective refrigerant branch flow X7. Y2 is part of X 2 , +
Y 22 is the return path portion 14 of the first fluid passage 14 of the temperature differential valve 50 as a control fluid for the first and second temperature sensitive springs 10.20.
.. B or the return path 24B of the second fluid passage 24, and the remaining mainstream portion X, 1. Y2+ is directly sucked into the compressor 1.

なお、」二足各実施例の説明においては、第1、第2の
両流体X、Yはいづれも単一の蒸発器4の中の2系統の
蒸発コイル/II、42を流通ずる場合について説明し
たが、本願各発明は、1基の冷凍装置に複数の室内機を
接続してなる多室型空調装置において異なる室の室内機
に対して冷媒を分流させるような場合にも実施し得るも
のである。
In addition, in the description of each embodiment, it is assumed that both the first and second fluids X and Y flow through two systems of evaporator coils/II and 42 in a single evaporator 4. Although described above, each invention of the present application can also be implemented in a case where refrigerant is divided into indoor units in different rooms in a multi-room air conditioner in which a plurality of indoor units are connected to one refrigeration system. It is something.

この場合は、第1図、第4図に示す各蒸発コイル41.
42がそれぞれ各室内機に付設される蒸発器に該当する
ことになる。
In this case, each evaporator coil 41 shown in FIG. 1 and FIG.
42 corresponds to the evaporator attached to each indoor unit.

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

第1図は本願の請求項第1項及び第2項の発明の実施例
に該当する温度差動弁を使用した冷凍装置の冷媒回路図
、第2図及び第3図は同温度差動弁の作動説明図、第4
図は本願の請求項第3項の発明の実施例に該当する温度
差動弁を使用した冷凍装置の冷媒回路図である。 1・・・・・圧縮機 2・・・・・凝縮器 3・・・・・減圧装置 4・・・・・蒸発器 5・・・・・ケーシング ロ・・・・・弁部材 lO・・・・第1感温バネ 14・・・・第1流体通路 14A・・・第1流体通路往路部 14+3・・・第1流体通路復路部 16・・・・第1弁通路部 20・・・・第2感温バネ 24・・・・第2t&体通路 24 A・・・第2流体通路往路部 24I3・・・第2流体通路復路部 26・・・・第2弁通路部 41・・・・第1蒸発コイル 42 ・ ・第2蒸発コイル
Fig. 1 is a refrigerant circuit diagram of a refrigeration system using a temperature differential valve corresponding to an embodiment of the invention of claims 1 and 2 of the present application, and Fig. 2 and 3 are the same temperature differential valve. Operation explanatory diagram, 4th
The figure is a refrigerant circuit diagram of a refrigeration system using a temperature differential valve according to an embodiment of the invention set forth in claim 3 of the present application. 1... Compressor 2... Condenser 3... Pressure reducing device 4... Evaporator 5... Casing roller... Valve member lO... ...First temperature-sensitive spring 14...First fluid passage 14A...First fluid passage outward path section 14+3...First fluid passage return path section 16...First valve passage section 20...・Second temperature-sensitive spring 24...Second t & body passage 24 A...Second fluid passage outward path part 24I3...Second fluid passage return path part 26...Second valve passage part 41...・First evaporator coil 42 ・・Second evaporator coil

Claims (1)

【特許請求の範囲】 1、流量(Sx)の変化にしたがって温度(Tx)が変
化する第1の流体(X)を通過せしめる第1流体通路(
14)と流量(Sy)の変化にしたがって温度(Ty)
が変化する第2の流体(Y)を通過せしめる第2流体通
路(24)とを有するケーシング(5)と、該ケーシン
グ(5)内で変位して前記第1流体通路(14)を流通
する第1流体(X)と前記第2流体通路(24)を流通
する第2流体(Y)の流量比(Sx/Sy)を変化させ
る作用をする弁部材(6)と、前記第1流体通路(14
)中に置かれて前記弁部材(6)を付勢するとともに前
記第1流体(X)の温度(Tx)に感応して変形し該弁
部材(6)に対する作用力(Fx)が変化する形状記憶
合金製の第1の感温バネ(10)と、前記第2流体通路
(24)中に置かれて前記弁部材(6)を付勢するとと
もに前記第2流体(Y)の温度(Ty)に感応して変形
し該弁部材(6)に対する作用力(Fy)が変化する形
状記憶合金製の第2の感温バネ(20)をそなえるとと
もに、前記第1の感温バネ(10)と第2の感温バネ(
20)は前記第1流体(X)の温度(Tx)と第2流体
(Y)の温度(Ty)の差温(ΔT)が一定の温度範囲
内に維持されるように前記弁部材(6)による前記第1
、第2両流体(X、Y)の流量比制御が行われるべく該
弁部材(6)に対するそれぞれの温度−作用力特性が規
定されていることを特徴とする温度差動弁。 2、第1の流体(X)と第2の流体(Y)が冷凍装置に
おける2系統の第1、第2の蒸発コイル(41、42)
を通過する第1、第2の分岐冷媒流であり、第1の感温
バネ(10)と第2の感温バネ(20)が前記2系統の
蒸発コイル(41、42)通過後の各分岐冷媒流の温度
(Tx、Ty)を感知する如くされた請求項第1項記載
の温度差動弁。 3、ケーシング(5)内の第1流体通路(14)が第1
蒸発コイル(41)へ向う湿り状態の第1分岐冷媒流(
X_1)の往路となる往路部(14A)と該第1蒸発コ
イル(41)から還流する乾き状態の第1分岐冷媒流(
X_2)の復路となる復路部(14B)とに分割される
とともに同ケーシング(5)内の第2流体通路(24)
が第2蒸発コイル(42)へ向う湿り状態の第2分岐冷
媒流(Y_1)の往路となる往路部(24A)と該第2
蒸発コイル(42)から還流する乾き状態の第2分岐冷
媒流(Y_2)の復路となる復路部(24B)とに分割
されており、且つ第1、第2の各感温バネ(10、20
)がそれぞれの流体通路(14、24)の各復路部(1
4B、24B)に又弁部材(6)が前記第1、第2各流
体通路(14、24)の各往路部(14A、24A)に
あって前記各感温バネ(10、20)が感知する各乾き
状態の第1、第2分岐冷媒流(X_2、Y_2)の温度
(Tx、Ty)に応じて前記第1、第2の両流体通路(
14、24)の各往路部(14A、24A)を通過する
湿り状態の第1、第2両分岐冷媒流(X_1、Y_1)
の流量比(Sx/Sy)を制御する如くされていること
を特徴とする請求項第2項記載の温度差動弁。
[Claims] 1. A first fluid passage (
14) and temperature (Ty) according to changes in flow rate (Sy).
a casing (5) having a second fluid passageway (24) through which a second fluid (Y) is changed; and a second fluid passageway (24) that is displaced within the casing (5) and flows through the first fluid passageway (14). a valve member (6) that acts to change the flow rate ratio (Sx/Sy) of the first fluid (X) and the second fluid (Y) flowing through the second fluid passage (24); and the first fluid passage (14
) to bias the valve member (6) and deform in response to the temperature (Tx) of the first fluid (X), changing the acting force (Fx) on the valve member (6). A first temperature-sensitive spring (10) made of a shape memory alloy is placed in the second fluid passage (24) to bias the valve member (6) and adjust the temperature (Y) of the second fluid (Y). A second temperature-sensitive spring (20) made of a shape memory alloy that deforms in response to temperature (Ty) and changes the acting force (Fy) on the valve member (6) is provided, and the first temperature-sensitive spring (10) ) and the second temperature-sensitive spring (
20) is the valve member (6) so that the temperature difference (ΔT) between the temperature (Tx) of the first fluid (X) and the temperature (Ty) of the second fluid (Y) is maintained within a certain temperature range. ) according to the first
, a temperature differential valve characterized in that respective temperature-acting force characteristics are defined for the valve member (6) so that flow rate ratio control of both second fluids (X, Y) is performed. 2. The first fluid (X) and the second fluid (Y) are connected to two systems of first and second evaporator coils (41, 42) in the refrigeration system.
The first and second branched refrigerant flows pass through the first and second temperature-sensitive springs (10) and the second temperature-sensitive springs (20), respectively, after passing through the two systems of evaporator coils (41, 42). 2. A temperature differential valve according to claim 1, wherein the temperature differential valve is adapted to sense the temperature (Tx, Ty) of the branched refrigerant stream. 3. The first fluid passage (14) in the casing (5) is the first
A wet first branch refrigerant flow (
The dry first branch refrigerant flow (
A second fluid passage (24) in the casing (5) is divided into a return passage section (14B) which is the return passage of X_2).
The outgoing path portion (24A) is the outgoing path of the wet second branch refrigerant flow (Y_1) heading toward the second evaporator coil (42);
The second branch refrigerant flow (Y_2) in a dry state returns from the evaporator coil (42).
) of each return path (1) of each fluid passage (14, 24).
4B, 24B), a valve member (6) is located in each outgoing path portion (14A, 24A) of the first and second fluid passages (14, 24), and each temperature-sensitive spring (10, 20) senses the temperature. Both the first and second fluid passages (
Both first and second branch refrigerant flows (X_1, Y_1) in a wet state pass through each outgoing path section (14A, 24A) of 14, 24)
3. The temperature differential valve according to claim 2, wherein the temperature differential valve is configured to control a flow rate ratio (Sx/Sy) of the temperature differential valve.
JP23131588A 1988-09-14 1988-09-14 Temperature differential valve Pending JPH0280879A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23131588A JPH0280879A (en) 1988-09-14 1988-09-14 Temperature differential valve

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23131588A JPH0280879A (en) 1988-09-14 1988-09-14 Temperature differential valve

Publications (1)

Publication Number Publication Date
JPH0280879A true JPH0280879A (en) 1990-03-20

Family

ID=16921707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23131588A Pending JPH0280879A (en) 1988-09-14 1988-09-14 Temperature differential valve

Country Status (1)

Country Link
JP (1) JPH0280879A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994012920A1 (en) * 1992-11-25 1994-06-09 Toto Ltd. Hot water/cold water mixing apparatus and hot water/cold water mixing method
JP2012097617A (en) * 2010-10-29 2012-05-24 Fujitsu Ltd Thermal actuator, shutter mechanism, and cooling system using the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994012920A1 (en) * 1992-11-25 1994-06-09 Toto Ltd. Hot water/cold water mixing apparatus and hot water/cold water mixing method
US5511723A (en) * 1992-11-25 1996-04-30 Toto Ltd. Combination faucet and method of mixing hot water with cold water
JP2012097617A (en) * 2010-10-29 2012-05-24 Fujitsu Ltd Thermal actuator, shutter mechanism, and cooling system using the same

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