JPH0316588B2 - - Google Patents
Info
- Publication number
- JPH0316588B2 JPH0316588B2 JP9833785A JP9833785A JPH0316588B2 JP H0316588 B2 JPH0316588 B2 JP H0316588B2 JP 9833785 A JP9833785 A JP 9833785A JP 9833785 A JP9833785 A JP 9833785A JP H0316588 B2 JPH0316588 B2 JP H0316588B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- reservoir
- boiling point
- liquid
- compartment
- 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.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 87
- 238000009835 boiling Methods 0.000 claims description 29
- 239000007788 liquid Substances 0.000 description 34
- 239000012530 fluid Substances 0.000 description 10
- 230000000630 rising effect Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000005856 abnormality Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、非共沸混合冷媒を使用した熱ポンプ
装置のうち、その冷媒組成を可変にする手段とし
て用いられる冷媒精溜装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a refrigerant rectification device used as a means for varying the refrigerant composition of a heat pump device using a non-azeotropic mixed refrigerant.
従来の技術
非共沸混合冷媒を用いた熱ポンプ装置に使用さ
れている従来の冷媒精溜装置には、たとえば第2
図に示すものがある。第2図において、1は冷媒
精溜塔、2は塔頂貯溜器、3は塔底貯溜器、4は
冷却源、5は加熱源、6は低沸点冷媒液、7は高
沸点冷媒液、8,9は塔頂貯溜器2と冷媒精溜塔
1を接続する配管、10は低沸点冷媒液6また
は、高沸点冷媒液7を抽出する抽出管で、熱ポン
プ装置の主回路へそれぞれの冷媒液を導く。11
は逆に、冷媒を熱ポンプ装置の主回路より冷媒精
溜塔1へ導く抽入管である。12は、冷媒精溜塔
1内を落下する冷媒液、13は同内を上昇する冷
媒ガスである。14は冷媒精溜塔1内に充填され
ている充填材である。Prior Art Conventional refrigerant rectifiers used in heat pump devices using non-azeotropic mixed refrigerants include, for example, a second
There is one shown in the figure. In FIG. 2, 1 is a refrigerant rectification column, 2 is a top reservoir, 3 is a bottom reservoir, 4 is a cooling source, 5 is a heating source, 6 is a low boiling point refrigerant liquid, 7 is a high boiling point refrigerant liquid, 8 and 9 are pipes connecting the tower top reservoir 2 and the refrigerant rectification column 1, and 10 is an extraction pipe for extracting the low boiling point refrigerant liquid 6 or the high boiling point refrigerant liquid 7, and each of them is connected to the main circuit of the heat pump device. Directs refrigerant liquid. 11
Conversely, it is an inlet pipe that leads the refrigerant from the main circuit of the heat pump device to the refrigerant rectification column 1. 12 is a refrigerant liquid falling inside the refrigerant rectification column 1, and 13 is a refrigerant gas rising therein. Reference numeral 14 denotes a filler filled in the refrigerant rectification column 1.
上記構成において、その作用は以下のようであ
る。高沸点冷媒液7中の低沸点成分が加熱源5に
よつて沸騰し、そのガス成分は、冷媒精溜塔1内
を上昇する。一方、低沸点冷媒液6中の高沸点成
分は、配管8を通つて、冷媒精溜塔1内を下降す
る。冷媒精溜塔1内には、充填材14が充填され
ている。ここで上昇する冷媒ガス13と、下降す
る冷媒液12とは、充填材14の表面で、熱交換
を行ない上昇する冷媒ガス13の成分は冷媒精溜
塔1内を上昇するにつれ、低沸点成分に富んだガ
スとなり、配管9を通つて冷却源4により液化さ
れて、より低沸点成分に富んだ液となつて塔頂貯
溜器2に溜まる。また、下降する冷媒液12は、
同様に熱交換により下降するにつれ、より高沸点
成分に富んだ液となり、塔底貯溜器3に溜まる。
したがつて、熱ポンプ装置の主回路より冷媒を抽
入管11を通して導入し、上記の作用をさせるこ
とによつて、導入した冷媒を高沸点冷媒液と低沸
点冷媒液に分離して貯溜することができ、主回路
の必要性に応じて、高沸点冷媒液7、あるいは低
沸点冷媒液6を抽出管10を通して主回路へ戻す
ことができ、熱ポンプ装置の主回路内を所望の組
成の冷媒に変えることができる。 In the above configuration, the operation is as follows. The low boiling point components in the high boiling point refrigerant liquid 7 are boiled by the heating source 5, and the gas components rise within the refrigerant rectification column 1. On the other hand, the high boiling point components in the low boiling point refrigerant liquid 6 pass through the pipe 8 and descend within the refrigerant rectification column 1 . A filler 14 is filled in the refrigerant rectification column 1 . Here, the rising refrigerant gas 13 and the falling refrigerant liquid 12 exchange heat on the surface of the filler 14, and as the rising refrigerant gas 13 rises in the refrigerant rectification column 1, the lower boiling point components The resulting gas is liquefied by the cooling source 4 through the pipe 9, and becomes a liquid rich in low-boiling components, which accumulates in the top reservoir 2. Furthermore, the descending refrigerant liquid 12 is
Similarly, as the liquid descends due to heat exchange, the liquid becomes richer in high-boiling components and accumulates in the bottom reservoir 3.
Therefore, the refrigerant is introduced from the main circuit of the heat pump device through the extraction pipe 11, and the introduced refrigerant is separated into a high boiling point refrigerant liquid and a low boiling point refrigerant liquid and stored by causing the above action. Depending on the needs of the main circuit, the high boiling point refrigerant liquid 7 or the low boiling point refrigerant liquid 6 can be returned to the main circuit through the extraction pipe 10, allowing a refrigerant of a desired composition to flow through the main circuit of the heat pump device. can be changed to
発明が解決しようとする問題点
熱ポンプ用冷媒精溜装置内には、上記のように
冷媒精溜塔内を上昇するガスと、下降する液の両
者が存在し、この両者の流れが全く逆の方向であ
るため、上昇するガス量(あるいはガス流速)が
著しく大きくなると、下降するはずの液の流れを
妨げてしまういわゆるフラツデイングという現象
が起こつた。これは、加熱源の熱量が著しく大き
い時などによく起こり、この現象が起こると冷媒
精溜装置本来の作用をしなくなり、低沸点冷媒液
と高沸点冷媒液に分離して貯溜できなくなる等の
問題点があつた。Problems to be Solved by the Invention In the refrigerant rectification device for a heat pump, there are both the gas rising in the refrigerant rectification column and the liquid flowing down, and the flows of these two are completely opposite. Therefore, if the rising amount of gas (or gas flow rate) becomes significantly large, a so-called flattening phenomenon occurs, which obstructs the flow of liquid that should be falling. This often occurs when the amount of heat from the heating source is extremely large, and when this phenomenon occurs, the refrigerant rectifier no longer functions as it should, and the refrigerant liquid is separated into low-boiling point and high-boiling point refrigerant liquids, which cannot be stored. There was a problem.
そこで、本発明は冷媒精溜装置の本来の機能は
保つたまま、きわめて簡単な構成で、従来の問題
点であつたフラツデイング現象を防止する熱ポン
プ用冷媒精溜装置を提供することを目的とする。 Therefore, an object of the present invention is to provide a refrigerant rectifying device for a heat pump that has an extremely simple configuration and prevents the flooding phenomenon, which has been a problem in the past, while maintaining the original function of the refrigerant rectifying device. do.
問題点を解決するための手段
上記問題点を解決する本発明の技術的手段は、
塔頂貯溜器内と塔底貯溜器内との各々に、その容
積が可変な隔室を設け、各々の隔室同志を配管接
続し、その内部の流体が隔室間を行き来できるよ
うにしたものである。Means for Solving the Problems The technical means of the present invention for solving the above problems are as follows:
A compartment with a variable volume is provided in each of the tower top reservoir and the tower bottom reservoir, and each compartment is connected with piping so that the fluid inside the compartment can go back and forth between the compartments. It is something.
作 用
上記構成によれば、安定した運転の状態にあつ
て塔底貯溜器内の圧力に変動が生じると塔底貯溜
器内の隔室の容積が急変し、内部の流体が配管を
通して塔頂貯溜器内の隔室に流入、あるいは、塔
底貯溜器内へ流入することにより、塔頂貯溜器内
の隔室の容積も急変し、その内部の圧力が塔底貯
溜器内の隔室内の圧力と釣り合うところで落ち着
く。この時、塔頂貯溜器内の圧力と塔底貯溜器内
の圧力は、圧力変動が起こる前の状態のように、
うまくバランスしており、常に安定な運転ができ
るものである。Effect According to the above configuration, when the pressure inside the tower bottom reservoir fluctuates during stable operation, the volume of the compartment in the tower bottom reservoir changes suddenly, and the internal fluid flows through the piping to the top of the tower. By flowing into the compartment in the reservoir or into the bottom reservoir, the volume of the compartment in the top reservoir changes suddenly, and the internal pressure increases to the level in the compartment in the bottom reservoir. It settles down when it balances the pressure. At this time, the pressure in the top reservoir and the pressure in the bottom reservoir are the same as before the pressure fluctuation occurs.
It is well balanced and allows stable operation at all times.
実施例
第1図は、本発明による熱ポンプ用冷媒精溜装
置の一実施例を示す構成図である。第1図におい
て番号15〜28の各構成部品は、第2図におけ
る番号1〜14の各構成部品とそれぞれ対応し、
同じ機能を持つ。29は、塔底貯溜器17内に設
けられた容積可変の下部隔室であり、中に流体3
0が入つている。31は塔頂貯溜器16内に設け
られた容積可変の上部隔室であり、下部隔室29
と上部隔室31は、配管32で接続され流体30
が行き来できるようになつている。Embodiment FIG. 1 is a configuration diagram showing an embodiment of a refrigerant rectification device for a heat pump according to the present invention. Each component numbered 15 to 28 in FIG. 1 corresponds to each component numbered 1 to 14 in FIG. 2,
have the same functionality. 29 is a lower compartment with a variable volume provided in the bottom reservoir 17, and the fluid 3 is contained therein.
It contains 0. 31 is an upper compartment with a variable volume provided in the top reservoir 16, and a lower compartment 29
and the upper compartment 31 are connected by a pipe 32 and a fluid 30
It is now possible to come and go.
以上のように構成された冷媒精溜装置において
その作用特にフラツデイングの発生を防止する作
用について説明する。なお、冷媒精溜装置を運転
して低沸点冷媒液と高沸点冷媒液に分離して貯溜
される等の基本的な説明は、従来例と同様であ
る。 The functions of the refrigerant rectifying apparatus constructed as described above, particularly the function of preventing the occurrence of flooding, will be explained. The basic explanation of operating the refrigerant rectifier to separate and store low-boiling point refrigerant liquid and high-boiling point refrigerant liquid is the same as in the conventional example.
加熱源19で加熱された高沸点冷媒液が沸騰
し、発生した低沸点成分ガスが冷媒情溜塔15内
の充填材28の間を通つて上昇し、塔頂貯溜器1
6から配管22を通つて落下する冷媒液26と対
向して流れる。もし、冷媒ガス27が多量に上昇
していく場合には、落下するはずの冷媒液26
が、上昇するガスに打ち勝つて落下することは困
難になり、冷媒ガス27と共に上昇してしまい、
最終的には、塔頂貯溜器16から全く液が落下し
ない状態になる。いわゆるフラツデイング現象が
起こる。この現象が起きる時には、冷媒ガス27
の発生量が多大となるため、塔頂貯溜器26内圧
力と塔底貯溜器17内圧力との差が急に大きくな
ることが知られている。すなわち、第3図に示す
ように、冷媒精溜塔15内の冷媒ガス流速を横軸
に、塔頂貯溜器16内圧力と塔底貯溜器17内圧
力との差圧を縦軸にとると、ガス流速に対し差圧
が急に上昇する点Pが存在し、これは、フラツデ
イング点と一般に呼ばれている。また点Qは、ロ
ーデイング点と呼ばれ、差圧が上昇する前の点で
ある。(参考文献「蒸溜工学ハンドブツク」P374
佐野司郎著)。冷媒精溜塔が正常な運転をするの
は、点Pより左側の領域、望ましくは、点Qより
左側の領域で、この領域においては、塔頂貯溜器
16内圧力と塔底貯溜器17内圧力との差圧は非
常に小さく、ガス流速の変化に対する差圧の変化
も小さい。したがつて、冷媒精溜塔が正常な運転
をしている時には、下部隔室29および上部隔室
31は、自己張力によつてほとんど動かずその内
部にある流体30も移動しない。一方、冷媒精溜
塔内に異常が起こり、冷媒ガス27の発生量が多
大になると、ガス流速が増大し、先に述べた第3
図のQ点にまで達すると急に差圧がP点まで増加
する。この時、自己張力よりも、塔頂貯溜器17
内圧力と流体30の圧力との差圧の方が大きくな
り、下部隔室29は、その容積を少くする方向へ
(第1図矢印方向へ)収縮する。それに伴つて内
部の流体30は、配管32を通つて上部隔室31
内に流入し、上部隔室31は、その容積を大きく
する方向(第1図矢印方向)へ拡張し、上部隔室
31内圧力と下部隔室29内圧力が均衡するとこ
ろで止まる。上部隔室31のこのような動きによ
り、塔頂貯溜器16内の実容積(上部隔室31を
除く)が減少することになり、塔頂貯溜器16内
圧力が、正常な運転時に比較して増加する。した
がつて、配管23を通つて上昇してくる冷媒ガス
の速度は急激に減少し、また、低沸点冷媒液20
の液面は低下しようとするので、配管22を通つ
て低沸点冷媒液20が急激に落下していく。落下
した液は、速度の減少した上昇する冷媒ガスに打
ち勝つて、無理なく塔底貯溜器17内に溜まる。
こうすることにより、塔底貯溜器17内にあり、
さかんに冷媒ガスを発生している高沸点冷媒液の
温度が下がつて、沸騰が押さえられ、正常な動作
に戻る。正常な動作になれば、塔底貯溜器17内
圧力と塔頂貯溜器16内圧力との差圧が縮まり、
今度は逆に上部隔室31から下部隔室29へ流体
30が配管32を通つて移動し、圧力の均衡を保
つて正常な位置に戻る。このような作用により、
冷媒精溜塔を常に安定な運転に保つことができ
る。 The high boiling point refrigerant liquid heated by the heating source 19 boils, and the generated low boiling point component gas rises through the space between the packing materials 28 in the refrigerant distillation tower 15 and reaches the top reservoir 1.
The refrigerant liquid 26 flows oppositely from the refrigerant liquid 26 falling through the pipe 22 from the refrigerant 6 . If the refrigerant gas 27 rises in large quantities, the refrigerant liquid 26 that should fall
However, it becomes difficult to overcome the rising gas and fall, and it rises together with the refrigerant gas 27,
Eventually, no liquid will fall from the top reservoir 16. A so-called flattening phenomenon occurs. When this phenomenon occurs, the refrigerant gas 27
It is known that the difference between the pressure inside the tower top reservoir 26 and the pressure inside the tower bottom reservoir 17 suddenly becomes large because the amount of gas generated becomes large. That is, as shown in FIG. 3, if the refrigerant gas flow rate in the refrigerant rectification column 15 is plotted on the horizontal axis, and the pressure difference between the pressure in the top reservoir 16 and the pressure in the bottom reservoir 17 is plotted on the vertical axis, then , there is a point P where the differential pressure suddenly increases with respect to the gas flow rate, and this is generally called the flattening point. Further, point Q is called a loading point, and is a point before the differential pressure increases. (Reference “Distillation Engineering Handbook” P374
Written by Shiro Sano). The refrigerant rectification column operates normally in the region to the left of point P, preferably in the region to the left of point Q. In this region, the pressure inside the tower top reservoir 16 and the inside pressure in the bottom reservoir 17 are The differential pressure is very small, and the change in differential pressure with respect to changes in gas flow rate is also small. Therefore, when the refrigerant rectification tower is operating normally, the lower compartment 29 and the upper compartment 31 hardly move due to their own tension, and the fluid 30 inside them does not move either. On the other hand, if an abnormality occurs in the refrigerant rectification tower and a large amount of refrigerant gas 27 is generated, the gas flow rate increases and the third
When reaching point Q in the figure, the differential pressure suddenly increases to point P. At this time, rather than self-tension, the top reservoir 17
The pressure difference between the internal pressure and the pressure of the fluid 30 becomes larger, and the lower compartment 29 contracts in the direction of decreasing its volume (in the direction of the arrow in FIG. 1). Accordingly, the internal fluid 30 passes through the pipe 32 to the upper compartment 31.
The upper compartment 31 expands in the direction of increasing its volume (in the direction of the arrow in FIG. 1), and stops when the internal pressure of the upper compartment 31 and the internal pressure of the lower compartment 29 are balanced. Due to this movement of the upper compartment 31, the actual volume inside the tower top reservoir 16 (excluding the upper compartment 31) decreases, and the pressure inside the tower top reservoir 16 becomes lower than that during normal operation. increases. Therefore, the velocity of the refrigerant gas rising through the pipe 23 decreases rapidly, and the low boiling point refrigerant liquid 20
As the liquid level of the refrigerant 20 tends to decrease, the low boiling point refrigerant liquid 20 rapidly falls through the pipe 22. The fallen liquid overcomes the rising refrigerant gas whose velocity has decreased and accumulates in the tower bottom reservoir 17 without difficulty.
By doing this, in the tower bottom reservoir 17,
The temperature of the high-boiling refrigerant liquid, which is actively generating refrigerant gas, drops, suppressing boiling, and returning to normal operation. When the operation is normal, the pressure difference between the pressure inside the tower bottom reservoir 17 and the pressure inside the tower top reservoir 16 is reduced.
This time, the fluid 30 moves in the opposite direction from the upper compartment 31 to the lower compartment 29 through the pipe 32 and returns to its normal position with the pressure balanced. Due to this effect,
The refrigerant rectification column can always be kept in stable operation.
発明の効果
以上述べたように、本発明の熱ポンプ用冷媒精
溜装置は、その塔頂貯溜器内と塔底貯溜器内に容
積が可変である上部隔室と下部隔室を設け、それ
を配管で接続して内部の流体が行ききできるよう
にしたことにより、従来の冷媒精溜装置につきも
ののフラツデイングという問題点を、きわめて簡
単な構成で防止することができ、冷媒精溜装置を
常に安定した正常な動作で運転できる効果があ
る。Effects of the Invention As described above, the refrigerant rectifying device for a heat pump of the present invention includes an upper compartment and a lower compartment whose volumes are variable in the top reservoir and the bottom reservoir. By connecting the refrigerant rectifiers with piping to allow the internal fluid to flow, it is possible to prevent the problem of flooding, which is common in conventional refrigerant rectification equipment, with an extremely simple configuration, and the refrigerant rectification equipment can be used at all times. It has the effect of allowing stable and normal operation.
第1図は本発明の一実施例における熱ポンプ用
冷媒精溜装置の構成図、第2図は従来の熱ポンプ
用冷媒精溜装置の構成図、第3図は冷媒精溜塔内
ガス流速と、塔頂貯溜器内圧力と塔底貯溜器内圧
力との差圧の関係を示した特性図である。
1,15……冷媒精溜塔、2,16……塔頂貯
溜器、3,17……塔底貯溜器、12,26……
冷媒液、13,27……冷媒ガス、29……下部
隔室、30……流体、31……上部隔室、32…
…配管。
Fig. 1 is a block diagram of a refrigerant rectifier for a heat pump according to an embodiment of the present invention, Fig. 2 is a block diagram of a conventional refrigerant rectifier for a heat pump, and Fig. 3 is a flow rate of gas in the refrigerant rectifier. FIG. 2 is a characteristic diagram showing the relationship between the pressure inside the tower top reservoir and the pressure inside the bottom reservoir. 1,15...Refrigerant rectification column, 2,16...Tower top reservoir, 3,17...Tower bottom reservoir, 12,26...
Refrigerant liquid, 13, 27... Refrigerant gas, 29... Lower compartment, 30... Fluid, 31... Upper compartment, 32...
…Piping.
Claims (1)
冷媒を貯溜する塔底貯溜器と、前記塔頂貯溜器に
上部を接続し、前記塔底貯溜器に下部を接続し、
低沸点冷媒若しくは高沸点冷媒またはこれらの混
合冷媒を流入する配管を有する冷媒精溜塔とを備
え、前記塔頂貯溜器内に容積可変の上部隔室を設
け、前記塔底貯溜器内に容積可変の下部隔室を設
け、前記上部隔室と下部隔室とを接続した熱ポン
プ用冷媒精溜装置。1. A tower top reservoir for storing a low boiling point refrigerant, a tower bottom reservoir for storing a high boiling point refrigerant, an upper part connected to the tower top reservoir, and a lower part connected to the tower bottom reservoir,
a refrigerant rectification column having piping into which a low-boiling point refrigerant, a high-boiling point refrigerant, or a mixed refrigerant thereof flows in; an upper compartment with a variable volume is provided in the tower top reservoir; A refrigerant rectifying device for a heat pump, which has a variable lower compartment and connects the upper compartment and the lower compartment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60098337A JPS61256163A (en) | 1985-05-09 | 1985-05-09 | Refrigerant rectifier for heat pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60098337A JPS61256163A (en) | 1985-05-09 | 1985-05-09 | Refrigerant rectifier for heat pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61256163A JPS61256163A (en) | 1986-11-13 |
| JPH0316588B2 true JPH0316588B2 (en) | 1991-03-05 |
Family
ID=14217085
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60098337A Granted JPS61256163A (en) | 1985-05-09 | 1985-05-09 | Refrigerant rectifier for heat pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61256163A (en) |
-
1985
- 1985-05-09 JP JP60098337A patent/JPS61256163A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61256163A (en) | 1986-11-13 |
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