JPS6160348B2 - - Google Patents
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- Publication number
- JPS6160348B2 JPS6160348B2 JP56055956A JP5595681A JPS6160348B2 JP S6160348 B2 JPS6160348 B2 JP S6160348B2 JP 56055956 A JP56055956 A JP 56055956A JP 5595681 A JP5595681 A JP 5595681A JP S6160348 B2 JPS6160348 B2 JP S6160348B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- piston
- flow rate
- valve
- gas cycle
- 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
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- Control Of Positive-Displacement Pumps (AREA)
Description
【発明の詳細な説明】
本発明は作業物質に気体を使用したいわゆるガ
スサイクル冷凍装置に関し、特にそのピストン駆
動方法を従来形式のものに対比して著しく安定化
し、エネルギ効率の高い冷凍装置を得ることを目
的としている。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a so-called gas cycle refrigeration system that uses gas as a working substance, and in particular, the piston drive method thereof is significantly stabilized compared to conventional types, and a refrigeration system with high energy efficiency is obtained. The purpose is to
ガスサイクル冷凍装置としては種々の方式のも
のが知られているが、大別すれば膨脹機のピスト
ンの往復運動をクランク装置によつて行わせる方
式と、気体の圧力によつて行わせる方式とがあ
る。クランク装置によつて機械的にピストンを往
復運動せしめる方式は大型で高価であり、摺動
部、回転部に油潤滑を必要とするため油蒸気の作
動気体への混入を完全に遮断することが困難であ
り、冷凍能力が低下するおそれがある。気体圧力
によつてピストンを往復運動させる方式は小型化
が容易であり、低価格とすることができるが、ピ
ストンの往復運動のストロークを制御することが
困難であり、シリンダ端壁にピストンが衝突する
不具合が生じて音、振動などが発生するおそれが
あり、各部品、例えば固定絞り弁などについて高
い精度が要求される。 Various types of gas cycle refrigeration systems are known, but they can be roughly divided into two types: one in which the reciprocating motion of the piston of the expander is performed by a crank device, and the other in which the reciprocating movement of the piston of the expander is performed by gas pressure. There is. Mechanically reciprocating the piston using a crank device is large and expensive, and requires oil lubrication for sliding and rotating parts, making it impossible to completely prevent oil vapor from entering the working gas. This is difficult, and there is a risk that the refrigeration capacity will decrease. The method of reciprocating the piston using gas pressure is easy to downsize and can be made at low cost, but it is difficult to control the stroke of the reciprocating movement of the piston, and the piston may collide with the cylinder end wall. There is a risk that problems may occur, resulting in noise, vibration, etc., and high precision is required for each component, such as a fixed throttle valve.
本発明によれば、膨脹機がシリンダ内で往復動
するピストンの一方端面によつて限定される第1
の可変容積空間として限定され、該ピストンの他
方端面が2分割されてそれぞれシリンダとの間に
第2および第3の空間を限定しており、該第2お
よび第3の空間には圧縮機の吐出側および吸入側
の導管がそれぞれ流量可変の絞り弁を介して接続
されている、ガスサイクル冷凍装置が提供され
る。 According to the present invention, the expander has a first space defined by one end surface of the piston that reciprocates within the cylinder.
The other end surface of the piston is divided into two to define second and third spaces between the piston and the cylinder, and the second and third spaces contain the compressor. A gas cycle refrigeration system is provided in which conduits on the discharge side and on the suction side are each connected via a variable flow rate throttle valve.
望ましい本発明の実施例において、絞り弁の流
量が温度追従性をもつて変化する如くし、これに
よつてピストンにそのときの温度に最適の制御力
を与えることが可能となり、ピストンとシリンダ
端壁との衝突を防ぎ且つ冷凍出力を増大すること
ができる。 In a preferred embodiment of the invention, the flow rate of the throttle valve is made to vary in accordance with the temperature, thereby making it possible to provide the piston with an optimum control force for the current temperature, and to provide the piston with the cylinder end. Collisions with walls can be prevented and refrigeration output can be increased.
以下図面を参照して本発明の作用、効果につい
て述べる。 The functions and effects of the present invention will be described below with reference to the drawings.
第1図は例えば特許第807732号(特公昭50−
18626号)に示す従来方式のガスサイクル冷凍装
置を示す略図である。ピストン11の一方の端面
はシリンダ9内に第1の可変容積空間10を限定
しており、その他方の端面は2分割されて大径端
面および小径端面を形成し、大径端面はシール1
2,14によつてシリンダ9内に第2の空間13
を限定し、小径端面はシリンダ9に連設する小径
のシリンダ内に第3の空間15を限定する。空間
13,15はそれぞれ固定絞り弁18,19を有
する流体導管16,17を介して圧縮機1の吐出
側導管2、吸入側導管3にそれぞれ接続されてい
る。 Figure 1 shows, for example, Patent No. 807732
18626) is a schematic diagram showing a conventional gas cycle refrigeration system. One end surface of the piston 11 defines a first variable volume space 10 within the cylinder 9, and the other end surface is divided into two to form a large diameter end surface and a small diameter end surface, and the large diameter end surface defines a first variable volume space 10 within the cylinder 9.
A second space 13 is created in the cylinder 9 by 2 and 14.
The small-diameter end face defines a third space 15 within the small-diameter cylinder connected to the cylinder 9. The spaces 13, 15 are connected to the discharge conduit 2 and the suction conduit 3 of the compressor 1 via fluid conduits 16, 17 having fixed throttle valves 18, 19, respectively.
ピストン11が図の最下方位置にあるとき低圧
切換弁5は閉じており、高圧切換弁4が開いて、
高圧気体は流体導管6、蓄冷器7、冷凍出力取出
用熱交換器8を経て第1の空間10に導入され
る。ピストン11の空間10に面する端面に作用
する気体圧力による力がピストン11の空間1
3,15に面する端面に作用する気体圧力による
力よりも大となつてピストン11は上昇する。ピ
ストン11の上昇運動は固定絞り弁18,19の
流れ抵抗によつて空間13,15の内部圧力が上
昇することによつて制限される。ピストン11が
その最上方位置附近に達すると高圧切換弁4が閉
じ、低圧切換弁5が開く。空間10内の気体は圧
縮機1に吸入されて低圧となり、ピストン11に
は下降力が与えられる。固定絞り弁18,19の
流体抵抗のためピストン11の下降力は弱められ
る。ピストン11の往復運動速度は固定絞り弁1
8,19の流体抵抗の度合によつて定められ、冷
凍出力は熱交換器8から取出される。 When the piston 11 is at the lowest position in the figure, the low pressure switching valve 5 is closed and the high pressure switching valve 4 is open.
The high-pressure gas is introduced into the first space 10 through the fluid conduit 6, the regenerator 7, and the heat exchanger 8 for extracting refrigeration output. The force due to the gas pressure acting on the end face of the piston 11 facing the space 10 causes the space 1 of the piston 11 to
The piston 11 rises as the force becomes larger than the force due to the gas pressure acting on the end faces facing the pistons 3 and 15. The upward movement of the piston 11 is limited by the increase in internal pressure in the spaces 13, 15 due to the flow resistance of the fixed throttle valves 18, 19. When the piston 11 reaches near its uppermost position, the high pressure switching valve 4 closes and the low pressure switching valve 5 opens. The gas in the space 10 is sucked into the compressor 1 and has a low pressure, and a downward force is applied to the piston 11. Due to the fluid resistance of the fixed throttle valves 18, 19, the downward force of the piston 11 is weakened. The reciprocating speed of the piston 11 is determined by the fixed throttle valve 1.
The refrigeration power is taken from the heat exchanger 8, determined by the degree of fluid resistance at 8 and 19.
第2図は本発明の望ましい実施例を示す概略図
であり、第1図と同様な部分は同一参照数字で示
し、その詳細な説明は省略する。前述説明によつ
て明かの如くピストン11の移動は空間10の圧
力と空間13,15の圧力との差によつて生じ、
ピストン11の移動速度は絞り弁の流体抵抗によ
つて定まる。近年この形式の冷凍装置として1段
型で室温から液体水素温度まで(300K〜20K)
冷凍を行うことが要求されるようになり、従つて
冷凍出力取出用熱交換器8および空間10の温度
は300K〜20Kの範囲で変化する必要がある。20K
の状態のときと300Kの状態のときとの温度の比
は300/20=15であり、従つて空間10内で膨脹
する流体の最も低温時と室温時との比が15とな
る。高圧及び低圧切換弁4,5、導管6、蓄冷器
7、冷凍出力取出用熱交換器8を通つて流れる流
体の抵抗は室温時に対比して低温時は著しく高く
なり、その結果空間10内の圧力上昇および圧力
減少の速度が低温時には室温時に比して小とな
る。絞り弁18,19を一定に保つと低温時に速
度制御が過大となり、所望の低温が達成できな
い。 FIG. 2 is a schematic diagram showing a preferred embodiment of the present invention, and parts similar to those in FIG. 1 are designated by the same reference numerals, and detailed explanation thereof will be omitted. As is clear from the above description, the movement of the piston 11 is caused by the difference between the pressure in the space 10 and the pressure in the spaces 13 and 15.
The speed of movement of the piston 11 is determined by the fluid resistance of the throttle valve. In recent years, this type of refrigeration equipment is a one-stage type that can be used from room temperature to liquid hydrogen temperature (300K to 20K).
It has become necessary to perform refrigeration, and therefore the temperature of the heat exchanger 8 for extracting the refrigeration output and the space 10 needs to vary in the range of 300K to 20K. 20K
The ratio of the temperatures between the state of . The resistance of the fluid flowing through the high-pressure and low-pressure switching valves 4 and 5, the conduit 6, the regenerator 7, and the refrigeration output extraction heat exchanger 8 is significantly higher at low temperatures than at room temperature, and as a result, the The rates of pressure increase and pressure decrease are smaller at low temperatures than at room temperature. If the throttle valves 18 and 19 are kept constant, speed control becomes excessive at low temperatures, making it impossible to achieve the desired low temperature.
本発明の望ましい実施例によれば、第2図に示
す如く絞り弁18′,19′は空間10の温度を感
知する感温部20,21によつて制御される流量
可変絞り弁である。感温部20,21はシリンダ
9の低温端又は熱交換器8にろう付け、ボルト付
け等により熱接触抵抗のないように取付けられ、
温度変化に追従して運動する弁棒22,23の先
端にニードル弁体29が設けられている。第3図
において感温部20,21は熱伝導性の高い且つ
熱膨脹係数の大きい材料、例えばアルミニウム等
から作られ、弁棒22,23は比較的熱伝導性の
低い材料、例えばステンレス鋼製とする。なおニ
ードル弁体29には最小流量を確保する逃がし溝
30が設けてあるが勿論これは対応する弁座27
に設けてもよい。なお第3図において25は圧縮
機1の吐出側、吸入側導間に連結される通路、2
6は流体導管16,17に対応する又は連結され
る通路、28は望ましくはシリンダ9の外壁の一
部、24は弁棒22,23のためのシースであ
る。感温部20,21の長さ、材質、ニードル弁
27,29の寸法を適切に定めることにより流量
可変絞り弁18′,19′を空間10又は熱交換器
8の温度に応答して適当に、自動的に制御して温
度低下に伴つて弁開口を大とすることができ、室
温から所望冷凍温度に至るまでの間そのときの温
度について最適の冷凍出力を得ることができる。
ピストンの運動を温度に関連して制御することが
できるからピストンがシリンダ端壁に衝突した
り、ストロークが不足したりすることがない。 According to a preferred embodiment of the present invention, the throttle valves 18' and 19' are variable flow rate throttle valves controlled by temperature sensing sections 20 and 21 that sense the temperature of the space 10, as shown in FIG. The temperature sensing parts 20 and 21 are attached to the low temperature end of the cylinder 9 or the heat exchanger 8 by brazing, bolting, etc. so as to avoid thermal contact resistance.
A needle valve element 29 is provided at the tip of the valve rods 22, 23 that move in accordance with temperature changes. In FIG. 3, the temperature sensing parts 20 and 21 are made of a material with high thermal conductivity and a large coefficient of thermal expansion, such as aluminum, and the valve stems 22 and 23 are made of a material with relatively low thermal conductivity, such as stainless steel. do. Note that the needle valve body 29 is provided with a relief groove 30 to ensure a minimum flow rate, but of course this is provided with the corresponding valve seat 27.
may be provided. In addition, in FIG. 3, 25 is a passage connected between the discharge side and the suction side conductor of the compressor 1;
6 is a passage corresponding to or connected to the fluid conduits 16, 17, 28 is preferably a part of the outer wall of the cylinder 9, and 24 is a sheath for the valve stems 22, 23. By appropriately determining the length and material of the temperature sensing parts 20 and 21 and the dimensions of the needle valves 27 and 29, the variable flow rate restricting valves 18' and 19' can be adjusted appropriately in response to the temperature of the space 10 or the heat exchanger 8. The valve opening can be automatically controlled to increase in size as the temperature decreases, and the optimal refrigeration output can be obtained for the temperature from room temperature to the desired refrigeration temperature.
Since the movement of the piston can be controlled in relation to temperature, the piston does not collide with the cylinder end wall or lack a stroke.
尚前記実施例に於て弁18′,19′の両者を温
度変化に応じて流量を変化させるものとして説明
したが、両者の内の一方のみを温度変化に応じて
流量を変化せしめるものとしても、従来装置に比
してエネルギ効率を上昇せしめることが可能であ
る。 In the above embodiment, both the valves 18' and 19' were described as ones that change the flow rate according to temperature changes, but it is also possible to use only one of the valves 18' and 19' as one that changes the flow rate according to temperature changes. , it is possible to increase energy efficiency compared to conventional devices.
上述実施例において感温部は熱膨脹、収縮する
金属棒を使用したが、気体又は液体圧ベローズ等
の如き温度変化によりニードル弁体29を長さ方
向に変位せしめる手段によつて代替することもで
き、弁開度を外部的に調節可能としてこれと感温
部とを電気的に接続することもできる。なお最大
弁開度を制限することにより、達成最低温度を制
限することができる。 In the above-described embodiment, a metal rod that expands and contracts thermally is used as the temperature-sensing section, but it may be replaced by a means for displacing the needle valve body 29 in the length direction by a change in temperature, such as a gas or liquid pressure bellows. It is also possible to make the valve opening degree externally adjustable and electrically connect this to the temperature sensing section. Note that by limiting the maximum valve opening degree, the lowest temperature that can be achieved can be limited.
本発明によるガスサイクル冷凍装置は機構が簡
単で信頼性が高く、小型で安価であり、効率が高
く振動が小である。 The gas cycle refrigeration apparatus according to the present invention has a simple mechanism, high reliability, small size, low cost, high efficiency, and low vibration.
第1図は従来のガスサイクル冷凍装置の一例を
示す概略図。第2図は本発明による冷凍装置の概
略図。第3図は流量可変絞り弁の概略断面図。
1:圧縮機、4,5:高圧、低圧切換弁、9:
シリンダ、11:ピストン、10:第1の可変容
積空間、13,15:第2、第3の空間、1
8′,19′:流量可変絞り弁、20,21:感温
部。
FIG. 1 is a schematic diagram showing an example of a conventional gas cycle refrigeration system. FIG. 2 is a schematic diagram of a refrigeration system according to the present invention. FIG. 3 is a schematic cross-sectional view of the variable flow rate restrictor. 1: Compressor, 4, 5: High pressure, low pressure switching valve, 9:
Cylinder, 11: Piston, 10: First variable volume space, 13, 15: Second and third spaces, 1
8', 19': Variable flow rate throttle valve, 20, 21: Temperature sensing section.
Claims (1)
リンダ内で往復動するピストンの一方端面によつ
て限定される第1の可変容積空間として限定され
ており、前記ピストンの他方の端面が2分割され
てそれぞれシリンダとの間に第2および第3の空
間を限定しており、該第2および第3の空間には
圧縮機の吐出側および吸入側の導管がそれぞれ流
量可変の絞り弁を介して接続され少くともその一
方が前記第1の可変容積空間の温度に対応して流
量が変化することを特徴とする前記ガスサイクル
冷凍装置。 2 前記絞り弁が温度追従性をもつて長さ方向に
変化する熱伝導性の高い熱膨脹係数の大きい感温
部を設けた弁棒に連接したニードル弁部の開度を
温度同調変化させ絞り弁流量が温度追従変化する
ことを特徴とする特許請求の範囲第1項記載のガ
スサイクル冷凍装置。 3 前記絞り弁がニードル弁であつて温度変化に
応じて変位を生ずる手段によりニードル弁体を長
さ方向に変位せしめることにより流量を可変とな
されていることを特徴とする特許請求の範囲第1
項記載のガスサイクル冷凍装置。[Scope of Claims] 1. In a gas cycle refrigeration system, an expander is defined as a first variable volume space defined by one end surface of a piston that reciprocates within a cylinder, and the other end surface of the piston is defined as a first variable volume space. is divided into two to define second and third spaces between each cylinder, and in the second and third spaces, conduits on the discharge side and suction side of the compressor are respectively connected to variable flow rate throttles. The gas cycle refrigeration system is characterized in that the flow rate of at least one of the valves is changed in response to the temperature of the first variable volume space connected through a valve. 2. The throttle valve is a throttle valve in which the opening degree of a needle valve part connected to a valve stem is provided with a temperature sensing part having high thermal conductivity and a large coefficient of thermal expansion that changes in the length direction with temperature followability. 2. The gas cycle refrigeration system according to claim 1, wherein the flow rate changes according to temperature. 3. Claim 1, characterized in that the throttle valve is a needle valve, and the flow rate is made variable by displacing the needle valve body in the longitudinal direction using means for generating displacement in response to temperature changes.
The gas cycle refrigeration device described in Section 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5595681A JPS57169565A (en) | 1981-04-14 | 1981-04-14 | Gas cycle refrigerating plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5595681A JPS57169565A (en) | 1981-04-14 | 1981-04-14 | Gas cycle refrigerating plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57169565A JPS57169565A (en) | 1982-10-19 |
| JPS6160348B2 true JPS6160348B2 (en) | 1986-12-20 |
Family
ID=13013523
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5595681A Granted JPS57169565A (en) | 1981-04-14 | 1981-04-14 | Gas cycle refrigerating plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57169565A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6378863U (en) * | 1986-11-10 | 1988-05-25 | ||
| JPS6378864U (en) * | 1986-11-10 | 1988-05-25 | ||
| US9080794B2 (en) * | 2010-03-15 | 2015-07-14 | Sumitomo (Shi) Cryogenics Of America, Inc. | Gas balanced cryogenic expansion engine |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5557673A (en) * | 1978-10-23 | 1980-04-28 | Japanese National Railways<Jnr> | Motive power absorption controller for expansion engine |
| JPS5634070A (en) * | 1979-08-28 | 1981-04-06 | Sumitomo Heavy Industries | Reciprocating expansion engine for very low temperature |
-
1981
- 1981-04-14 JP JP5595681A patent/JPS57169565A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57169565A (en) | 1982-10-19 |
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