JPH04187993A - Heat conveying device - Google Patents
Heat conveying deviceInfo
- Publication number
- JPH04187993A JPH04187993A JP31905890A JP31905890A JPH04187993A JP H04187993 A JPH04187993 A JP H04187993A JP 31905890 A JP31905890 A JP 31905890A JP 31905890 A JP31905890 A JP 31905890A JP H04187993 A JPH04187993 A JP H04187993A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- gas
- refrigerant
- receiver
- receivers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims description 79
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 239000003507 refrigerant Substances 0.000 description 27
- 239000013526 supercooled liquid Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
Landscapes
- Central Heating Systems (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、熱媒体とした冷媒を加熱する時の圧力上昇を
利用して熱を利用側に移動させる熱搬送装置に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a heat transfer device that transfers heat to a user side by utilizing the pressure increase when heating a refrigerant as a heat medium.
従来の技術
冷媒をバーナ等の燃焼熱で加熱し、蒸発する冷媒の圧力
を利用して冷媒を循環させる熱駆動型の熱搬送方式を行
うため、単一の受液器に満たされた液冷媒を間欠的に冷
媒加熱器に供給するとともに、間欠的に供給する周期を
冷媒の物性値に合わせて搬送熱量に合わせて設定してい
た。Conventional technology A liquid refrigerant filled in a single liquid receiver uses a heat-driven heat transfer system that heats the refrigerant with combustion heat from a burner and uses the pressure of the evaporating refrigerant to circulate the refrigerant. was intermittently supplied to the refrigerant heater, and the period of intermittent supply was set in accordance with the physical properties of the refrigerant and the amount of heat transferred.
上記熱搬送方式において受液器の有効内容積をv (C
:d)熱媒の潜熱Δi (kcal/kg) 、液冷媒
の密度ρ(g/ cj) 、開閉弁の開閉作動回数N(
サイクル/h)、熱搬送I Q (kca I/ h
) とすると、となり、熱搬送量Qを大きくするには受
液器の内容積■を大きくするか、開閉作動回数Nを大き
くするか、液冷媒の密度を大きくするかの方法があろう
発明が解決しようとする課題
しかし、受液器の内容積■を大きくすること、および開
閉作動回数Nを大きくするには、受液器を満液にする時
間Toff (開閉弁の閉時間)あるいは受液器内の液
冷媒を完全に流出させる時間Ton(開閉弁の開時間〕
のいずれか、あるいは両方を小さくして作動周期Ts
= Ton+Toffを小さくする必要があり、放熱器
の放熱能力あるいは冷媒管路の圧力損失抵抗上課題があ
った。In the above heat transfer method, the effective internal volume of the liquid receiver is v (C
:d) Latent heat Δi (kcal/kg) of heating medium, density ρ (g/cj) of liquid refrigerant, number of opening/closing operations of the on-off valve N(
cycles/h), heat transfer IQ (kca I/h
) Then, in order to increase the heat transfer amount Q, there are methods to increase the internal volume of the liquid receiver, increase the number of opening/closing operations N, or increase the density of the liquid refrigerant. However, in order to increase the internal volume of the liquid receiver and the number of opening/closing operations N, it is necessary to increase the time Toff (closing time of the on-off valve) to fill the liquid receiver Time for the liquid refrigerant in the liquid container to completely flow out Ton (opening time of the on-off valve)
The operating period Ts is reduced by reducing either or both of
= Ton+Toff had to be made small, and there was a problem with the heat dissipation ability of the radiator or the pressure loss resistance of the refrigerant pipeline.
本発明はこのような課題を解決するもので、熱搬送装置
の熱搬送能力を向上させ、より大容量の熱を搬送させる
ことを目的とする。The present invention solves these problems, and aims to improve the heat transfer ability of a heat transfer device and transfer a larger amount of heat.
課題を解決するための手段
上記課題を解決するために本発明の熱搬送装置は、熱媒
加熱機とその上方に設けた気液分離器を配管接続した環
状通路と、前記気液分離器の上方に設けた複数の受液器
と、各々の受液器と気液分離器を接続する複数の第1逆
止弁と、熱媒加熱機の熱媒の出口側と前記複数の受液器
とを接続する均圧管に設けた複数の開閉弁と、前記気液
分離器と放熱器を接続する熱媒往管と、前記複数の受液
器の上流側に設けた複数の第2逆止弁と前記放熱器を連
結する熱媒復管と、前記複数の開閉弁を開閉制御する制
御装置を設けた構成としたものであ作用
本発明の熱搬送装置は上記した構成により、複数の受液
器の開閉弁を順次開閉させて熱媒を受液器に流入あるい
は流出させて気液分離器に液状の冷媒を供給し、個々の
受液器での作動周期Tsを短くせずに、複数の受液器に
よる気液分離器への液冷媒の供給量を増加させることに
よって大容量の熱搬送を実現させるものである。Means for Solving the Problems In order to solve the above-mentioned problems, the heat transfer device of the present invention has an annular passage connecting a heat medium heating machine and a gas-liquid separator provided above it with piping, and a heat transfer device of the present invention. a plurality of liquid receivers provided above, a plurality of first check valves connecting each liquid receiver and the gas-liquid separator, a heating medium outlet side of the heating medium heater and the plurality of liquid receivers; a plurality of on-off valves provided in a pressure equalizing pipe connecting the gas-liquid separator and the radiator, a plurality of second non-return valves provided on the upstream side of the plurality of liquid receivers; The heat transfer device of the present invention is configured to include a heat medium return pipe that connects the valve and the radiator, and a control device that controls opening and closing of the plurality of on-off valves. The on-off valves of the liquid vessels are sequentially opened and closed to cause the heat medium to flow into or out of the liquid receiver to supply liquid refrigerant to the gas-liquid separator, without shortening the operating cycle Ts of each liquid receiver. By increasing the amount of liquid refrigerant supplied to the gas-liquid separator by a plurality of liquid receivers, large-capacity heat transfer is realized.
実施例
以下本発明の実施例を受液器を2個として第1図で説明
する。1は熱媒加熱機、2は熱媒加熱機1の上方に設け
た気液分離器、3は熱媒加熱機1と気液分離器2を環状
に配管接続した環状通路、4.4′は気液分離器2の上
方に設けた受液器、5.5′は受液器4.4′と気液分
離器2とを接続する管路に設けた第1逆止弁、6.6′
は熱媒加熱器1の熱媒出口側と受液器4.4′とを接続
する均圧管7に設けた開閉弁、8は送風機9を有する放
熱器、10は気液分離器2と放熱器8を連結する熱媒往
管、11.11’は受液器4.4′の上流側に設けた第
2逆止弁、12は放熱器8と第2逆止弁11.11′を
連結する熱媒復管、13は熱媒加熱器1に設けたバーナ
、14はバーナ13への燃料の流量制御部、15は環状
通路3の熱媒加熱機lの熱媒出口側に設けた温度検知器
、16は開閉弁6.6′、温度検知器15、流量制御部
14と電気的に接続された制御装置である。EXAMPLE Hereinafter, an example of the present invention will be described with reference to FIG. 1, assuming that there are two liquid receivers. 1 is a heating medium heating device, 2 is a gas-liquid separator provided above the heating medium heating device 1, 3 is an annular passageway in which the heating medium heating device 1 and the gas-liquid separator 2 are connected in an annular manner by piping; 4.4'5.5' is a liquid receiver provided above the gas-liquid separator 2; 5.5' is a first check valve provided in a pipe connecting the liquid receiver 4.4' and the gas-liquid separator 2; 6. 6′
1 is an on-off valve provided in a pressure equalizing pipe 7 connecting the heat medium outlet side of the heat medium heater 1 and the liquid receiver 4.4', 8 is a radiator having a blower 9, and 10 is a gas-liquid separator 2 and a heat radiator. 11.11' is a second check valve provided upstream of the liquid receiver 4.4', and 12 is a heat medium outgoing pipe connecting the radiator 8 and the second check valve 11.11'. A connecting heating medium return pipe, 13 is a burner provided in the heating medium heater 1, 14 is a fuel flow rate control unit to the burner 13, and 15 is installed on the heating medium outlet side of the heating medium heating machine 1 in the annular passage 3. A temperature sensor 16 is a control device electrically connected to the on-off valve 6.6', the temperature sensor 15, and the flow rate control section 14.
上記構成において、熱媒加熱機lでバーナ13の燃焼熱
で加熱された熱媒である冷媒はガスと液の混合した2相
状態で気液分離器2に流入し、液冷媒は気液分離器2の
下方より再び熱媒加熱器1に流入する。一方、気液分離
器2に流入した2相状態の冷媒のうちガス冷媒は気液分
離器2の上方部に開孔した熱媒往管10を通り放熱器8
で送J!II!9の運転で利用側に放熱し凝縮液化して
さらに過冷却液となる。複数の受液器4.4′に設けた
開閉弁のうち少なくとも1個が閉となった時に放熱器8
で過冷却液となった液冷媒は熱媒復管12を通って閉と
なった開閉弁6.6′のいずれかに対応する受液器4.
4′のいずれかにその対応する第2逆止弁11.11’
のいずれかを通って流入し、受液器内のガス冷媒を過冷
却液冷媒により冷却凝縮させることにより、受液器内を
液冷媒で満たす。次に液冷媒で満液となった受液器に対
応する開閉弁を制御装置16により開成せしめで受液器
と気液分離器2とを均圧管7により連通させ、受液器内
の液冷媒を重力により第1逆止弁を通って気液分離器2
内へ流入させる。この1つの受液器での流入流出を他の
受液器でも時間をズラして順次実施し、1個の受液器で
の開閉の1周期に要する時間を短縮することなく、気液
分離器2への受液器からの液冷媒の供給量を増大するこ
とができる。また、複数の受液器4.4′・・・を気液
努離器2の上方に配置することにより、気液分離H2内
の液冷媒面高さに影響されることなく受液器4.4′・
・・内の液冷媒を落下流入させることができ、開閉弁6
.6′・・・の開閉制御が容易になる効果がある。さら
に、受液器への流入時間(開閉弁の閉時間Toff)を
長くできるため過冷却液の過冷却度を小さく設定できる
ようになり、放熱器の放熱能力を低減できるようになり
、放熱器の低コスト、小型化ができる。In the above configuration, the refrigerant, which is a heating medium heated by the combustion heat of the burner 13 in the heating medium heater 1, flows into the gas-liquid separator 2 in a two-phase state in which gas and liquid are mixed, and the liquid refrigerant is separated into gas and liquid. The heat medium flows into the heat medium heater 1 again from below the vessel 2 . On the other hand, among the two-phase refrigerant that has flowed into the gas-liquid separator 2, the gas refrigerant passes through the heating medium outgoing pipe 10 that is opened in the upper part of the gas-liquid separator 2, and passes through the radiator 8.
Send it to J! II! In operation 9, heat is radiated to the user side, condensed and liquefied, and further becomes supercooled liquid. When at least one of the on-off valves provided in the plurality of liquid receivers 4.4' is closed, the radiator 8
The liquid refrigerant, which has become a supercooled liquid, passes through the heat medium return pipe 12 and enters the liquid receiver 4. which corresponds to either of the closed on-off valves 6.6'.
4' and its corresponding second check valve 11.11'
The gas refrigerant in the receiver is cooled and condensed by the supercooled liquid refrigerant, thereby filling the receiver with liquid refrigerant. Next, the control device 16 opens the on-off valve corresponding to the liquid receiver filled with liquid refrigerant, and the liquid receiver and the gas-liquid separator 2 are communicated through the pressure equalization pipe 7, and the liquid in the liquid refrigerant is The refrigerant is passed through the first check valve by gravity to the gas-liquid separator 2.
Let it flow inside. This inflow and outflow in one liquid receiver is carried out sequentially in other liquid receivers at different times, and gas-liquid separation can be achieved without shortening the time required for one cycle of opening and closing in one liquid receiver. The amount of liquid refrigerant supplied to the container 2 from the liquid receiver can be increased. In addition, by arranging the plurality of liquid receivers 4,4'... above the gas-liquid separator 2, the liquid receivers 4, 4'... .4′・
The liquid refrigerant inside can be allowed to fall and flow in, and the on-off valve 6
.. This has the effect of facilitating opening/closing control of 6'.... Furthermore, since the inflow time to the liquid receiver (closing time Toff of the on-off valve) can be lengthened, the degree of supercooling of the supercooled liquid can be set small, and the heat dissipation capacity of the radiator can be reduced. can be made low-cost and compact.
発明の効果
以上のように本発明の熱搬送装置によれば、気液分離器
の上方に設けた複数の受液器とその受液器に対応する複
数の開閉弁の開閉制御を行うものであるから、次のよう
な作用効果を有する。Effects of the Invention As described above, according to the heat transfer device of the present invention, it is possible to control the opening and closing of a plurality of liquid receivers provided above a gas-liquid separator and a plurality of on-off valves corresponding to the liquid receivers. Because of this, it has the following effects.
(1) より大容量の熱搬送ができるようになり、シ
ステムの応用範囲が大きくなる。(1) It becomes possible to transport a larger amount of heat, increasing the range of application of the system.
(2)気液分離器の上方に配した複数の受液器により安
定した液冷媒の供給ができ、システムの信較性が向上す
る。(2) A plurality of liquid receivers placed above the gas-liquid separator allows stable supply of liquid refrigerant, improving system reliability.
(3)熱搬送能力を大きくしない場合は、放熱器の小型
化、低コスト化ができる。(3) If the heat transfer capacity is not increased, the radiator can be made smaller and lower in cost.
図面は本発明の一実施例を示す熱搬送装置の構成回であ
る。
1・・・・・・熱媒加熱機、2・・・・・・気液分離器
、3・・・・・・環状通路、4.4′・・・・・・受液
器、5.5′・・・・・・第1逆止弁、6.6′・・・
・・・開閉弁、7・・・・・・均圧管、8・・・・・・
放熱器、lO・・・・・・熱媒往管、11.11′・・
・・・・第2逆止弁、12・・・・・・熱媒復管、16
・・・・・・制御装置。The drawing shows the configuration of a heat transfer device showing an embodiment of the present invention. 1... Heat medium heater, 2... Gas-liquid separator, 3... Annular passage, 4.4'... Liquid receiver, 5. 5'...First check valve, 6.6'...
...Opening/closing valve, 7...Pressure equalization pipe, 8...
Heat radiator, lO... Heat medium outgoing pipe, 11.11'...
...Second check valve, 12... Heat medium return pipe, 16
······Control device.
Claims (1)
た環状通路と、前記気液分離器の上方に設けた複数の受
液器と、この受液器の各々と気液分離器を接続する複数
の第1逆止弁と、熱媒加熱機の熱媒の出口側と前記複数
の受液器とを接続する均圧管に設けた複数の開閉弁と、
前記気液分離器と放熱器を接続する熱媒往管と、前記複
数の受液器の上流側に設けた複数の第2逆止弁と前記放
熱器を連結する熱媒復管と、前記複数の開閉弁を開閉制
御する制御装置とを設けた熱搬送装置。An annular passage connecting a heat medium heater and a gas-liquid separator provided above the heat medium heater, a plurality of liquid receivers provided above the gas-liquid separator, and each of the liquid receivers and the gas-liquid separator. a plurality of first check valves connecting the heating medium, and a plurality of on-off valves provided in pressure equalizing pipes connecting the heating medium outlet side of the heating medium heater and the plurality of liquid receivers;
a heat medium return pipe that connects the gas-liquid separator and the radiator; a heat medium return pipe that connects the radiator to a plurality of second check valves provided upstream of the plurality of liquid receivers; A heat transfer device equipped with a control device that controls opening and closing of a plurality of on-off valves.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31905890A JPH04187993A (en) | 1990-11-21 | 1990-11-21 | Heat conveying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31905890A JPH04187993A (en) | 1990-11-21 | 1990-11-21 | Heat conveying device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04187993A true JPH04187993A (en) | 1992-07-06 |
Family
ID=18106033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31905890A Pending JPH04187993A (en) | 1990-11-21 | 1990-11-21 | Heat conveying device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04187993A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997009570A1 (en) * | 1995-09-08 | 1997-03-13 | Daikin Industries, Ltd. | Heat transfer apparatus |
-
1990
- 1990-11-21 JP JP31905890A patent/JPH04187993A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997009570A1 (en) * | 1995-09-08 | 1997-03-13 | Daikin Industries, Ltd. | Heat transfer apparatus |
US6116035A (en) * | 1995-09-08 | 2000-09-12 | Daikin Industries, Ltd. | Heat transfer device |
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