JPS5993161A - Refrigerator - Google Patents
RefrigeratorInfo
- Publication number
- JPS5993161A JPS5993161A JP57201452A JP20145282A JPS5993161A JP S5993161 A JPS5993161 A JP S5993161A JP 57201452 A JP57201452 A JP 57201452A JP 20145282 A JP20145282 A JP 20145282A JP S5993161 A JPS5993161 A JP S5993161A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- valve
- compressor
- temperature
- condenser
- 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
- 238000005057 refrigeration Methods 0.000 claims description 16
- 239000003638 chemical reducing agent Substances 0.000 claims description 8
- 239000003507 refrigerant Substances 0.000 description 16
- 238000001816 cooling Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 6
- 238000009833 condensation Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 210000004907 gland Anatomy 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明はニアコンディショナー等に利用する冷凍装置に
関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigeration system used in near conditioners and the like.
従来例の構成とその問題点
従来この種の冷凍装置においてd、圧縮機の0N−OF
F 運転により所定の温度に冷却する方法がとられてい
る。そして、この0N−OFF運転では起動後、冷凍装
置内の圧力、冷媒分布状態が定常運転状態に達するまで
の非定常運転による低効率運転が生じるので、連続運転
時の冷凍能力の80%程度の冷却能力しか発揮されてい
ない。Configuration of conventional example and its problems In conventional refrigeration equipment of this type, d, ON-OF of compressor
A method of cooling to a predetermined temperature through F operation is used. In this 0N-OFF operation, after startup, low efficiency operation occurs due to unsteady operation until the pressure inside the refrigeration equipment and the refrigerant distribution state reach a steady operating state, so about 80% of the refrigeration capacity during continuous operation occurs. Only the cooling capacity is demonstrated.
この問題点の改良として第3図に示すように圧縮機10
1.圧力三方弁102.凝縮器103.圧力三方弁10
4.減圧器106.蒸発器106゜を順次環状に接続し
、前記圧力三方弁102のバイパス管107を圧縮機1
o1と蒸発器106との間に接続し、圧力三方弁102
は入口部108の圧力が所定の圧力以上となると入口部
108−出口部109への主回路を開略し、バイパス部
110を閉路する。逆に、入1」部の108圧力が所定
値以下となると入口部108−バイパス部110の回路
を開略し、出口部109を閉路するものである。また、
圧カニ方弁104は入口管111の圧力が所定の圧力以
上となると回路を開略し、所定の正分県下となると閉路
するものがある。この冷凍装置による圧力変化は第4図
に示すように、圧縮機101の運転中は圧力三方弁10
2の入口部108の圧力Pdは所定値Pdoより高く、
壕だ、圧カニ方弁104の入口管111の圧力PCも所
定値PCOより高い。従って、冷媒は圧縮器101−圧
力三方弁入口部108−回出[1部1OCa−凝縮器1
03−圧カニ方弁104−減圧器105−蒸発器106
−圧縮機101へと流れ、バイノ々ス管107は閉路さ
れ、定常冷却回路が形成されている。そして、冷却運転
が停止すると高圧側圧力は低下して行き、先ず、圧カニ
方弁入1:l簀111圧力P。が所定値P。。より低く
なり圧カニ方弁104の回路が閉路する。次いで圧力三
方邦人11部108の圧力Pdが所定値Pd0より低下
し、圧力三方弁102の主回路を閉路し、74747回
路107を開路する。従って、凝縮器103内の圧力は
ほぼ所定値P。。を維持し、圧縮機101内の圧力は蒸
発器106の圧力P8 とバランスし、圧縮機101
内の冷媒は全て蒸発器106へと流入する。再起動時は
先ず圧縮機101の運転により蒸発器106内に滞留す
る冷媒を吸引し、圧縮機101内の圧力が上昇する。こ
れにより圧力三方弁入口部108の圧力Pd も徐々
に上昇し、所定値Pdoより高くなると圧力三方弁10
2の主回路を開路し、バイパス回路107を回路するた
め、高圧冷媒が凝縮器103へと流入し、圧カニ方弁入
口管111の圧力PCが徐々に上列して所定値Po0よ
り高くなると回路を開略し、冷却運転状態となる。この
時、凝縮器103内の冷媒は運転中より若干少ない状態
で維持され、圧力三方弁104の回路後比較的速やかに
定常冷却運転状態に達する。つ捷りこの冷凍装置では起
動後圧縮機101内が定割となるまで(略1分)及び凝
縮器103内が定常となる寸で(略0,5分)が非定常
運転となるだけで従来の略6分に比較してKとなってい
るため、熱交換器能力の95%′iで発揮できることが
確脇できている。As an improvement to this problem, a compressor 10 as shown in FIG.
1. Pressure three-way valve 102. Condenser 103. Pressure three-way valve 10
4. Pressure reducer 106. The evaporators 106° are sequentially connected in an annular manner, and the bypass pipe 107 of the pressure three-way valve 102 is connected to the compressor 1.
o1 and the evaporator 106, the pressure three-way valve 102
When the pressure at the inlet section 108 exceeds a predetermined pressure, the main circuit from the inlet section 108 to the outlet section 109 is opened, and the bypass section 110 is closed. Conversely, when the pressure at the inlet 108 becomes less than a predetermined value, the circuit from the inlet 108 to the bypass section 110 is opened and the outlet 109 is closed. Also,
Some of the pressure crab valves 104 open the circuit when the pressure of the inlet pipe 111 exceeds a predetermined pressure, and close the circuit when the pressure reaches a predetermined predetermined pressure. As shown in FIG. 4, the pressure change caused by this refrigeration equipment is caused by
The pressure Pd at the inlet portion 108 of No. 2 is higher than the predetermined value Pdo,
The pressure PC of the inlet pipe 111 of the pressure crab valve 104 is also higher than the predetermined value PCO. Therefore, the refrigerant is compressor 101 - pressure three-way valve inlet 108 - recirculation [1 part 1 OCa - condenser 1
03-Pressure crab valve 104-Pressure reducer 105-Evaporator 106
- The air flows to the compressor 101, and the binoculars pipe 107 is closed, forming a steady cooling circuit. Then, when the cooling operation is stopped, the pressure on the high pressure side decreases, and first, the pressure on the crab side valve enters 1:1 in the tank 111 pressure P. is the predetermined value P. . The pressure becomes lower and the circuit of the pressure crab valve 104 is closed. Next, the pressure Pd of the pressure three-way Japanese 11 section 108 falls below the predetermined value Pd0, the main circuit of the pressure three-way valve 102 is closed, and the 74747 circuit 107 is opened. Therefore, the pressure inside the condenser 103 is approximately the predetermined value P. . is maintained, the pressure inside the compressor 101 is balanced with the pressure P8 of the evaporator 106, and the pressure inside the compressor 101 is balanced with the pressure P8 of the evaporator 106.
All the refrigerant inside flows into the evaporator 106. At the time of restart, first, the compressor 101 is operated to suck the refrigerant remaining in the evaporator 106, and the pressure inside the compressor 101 increases. As a result, the pressure Pd at the pressure three-way valve inlet 108 also gradually increases, and when it becomes higher than a predetermined value Pdo, the pressure three-way valve 108
2 is opened and the bypass circuit 107 is connected, high-pressure refrigerant flows into the condenser 103, and the pressure PC of the pressure crab inlet pipe 111 gradually rises and becomes higher than the predetermined value Po0. Open the circuit and enter cooling operation mode. At this time, the refrigerant in the condenser 103 is maintained at a slightly lower level than during operation, and the steady cooling operation state is reached relatively quickly after the pressure three-way valve 104 is circuited. In this refrigeration system, after startup, the only unsteady operation is until the inside of the compressor 101 becomes constant (approximately 1 minute) and when the inside of the condenser 103 becomes steady (approximately 0.5 minutes). Since it is K compared to about 6 minutes in the conventional case, it is certain that the heat exchanger can perform at 95%'i of its capacity.
しかし、この冷凍装置に於いても可能省エネルギー率2
0%の内の16%しか効果を発揮できておらず、高価な
弁を使用する割には効果の少ないという欠点を有してい
る。However, even with this refrigeration system, the possible energy saving rate is 2.
It is only 16% effective out of 0%, and has the drawback of being ineffective despite the use of expensive valves.
発明の目的
上記欠点に鑑み、本発明は圧縮機の運転、停止による温
度変化により適確に瞬時作動する弁装置により起動後の
非定常運転をほとんどOとし、約10Q%の効率を発揮
する冷凍装置を提供せんとするものである。Purpose of the Invention In view of the above-mentioned drawbacks, the present invention provides a refrigeration system that achieves an efficiency of approximately 10Q% by reducing unsteady operation after startup to almost zero using a valve device that operates accurately and instantaneously due to temperature changes caused by the start and stop of the compressor. The aim is to provide the equipment.
発明の構成
上記目的を達成するため、本発明は圧縮機の吸入管温度
相当圧力と凝縮圧力との圧力差で弁を開閉し、凝縮圧力
が吸入管温度相当圧力より所定値以上高い時に弁を開放
する差圧弁を凝縮器と減圧器との間に設けることにより
弁開閉動作の迅速化を言するものである。Structure of the Invention In order to achieve the above object, the present invention opens and closes a valve based on the pressure difference between the pressure corresponding to the suction pipe temperature of the compressor and the condensing pressure, and opens and closes the valve when the condensing pressure is higher than the pressure equivalent to the suction pipe temperature by a predetermined value or more. By providing a differential pressure valve that opens between the condenser and the pressure reducer, the valve opening and closing operations can be made faster.
実施例の説明
以下に本発明の一実施例について添付図面に従い説明す
る。DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings.
図に於て、1は圧縮機、2は凝縮器、3は差圧弁、4は
減圧器、5は蒸発器である。圧縮機1はロータリータイ
プであり、内部機械室6にはサタンヨンバルプを有して
いないため蒸発器6と圧縮機1との間に逆止弁7を介在
して順次環状に接続して冷凍装置を構成している。差圧
弁3は先端に感熱筒8を有する導圧管9を設けた上部ケ
ーゾング10と入口管11.出口管12を有する下部ケ
ーゾング13とで外殻14を形成し、内部を圧力応動素
子16vCて上部を感圧室16.下部を弁室17とに区
画している。In the figure, 1 is a compressor, 2 is a condenser, 3 is a differential pressure valve, 4 is a pressure reducer, and 5 is an evaporator. The compressor 1 is a rotary type, and the internal machine room 6 does not have a satanyong valve. Therefore, a check valve 7 is interposed between the evaporator 6 and the compressor 1, and the evaporator 6 and the compressor 1 are sequentially connected in an annular manner. configuring the device. The differential pressure valve 3 includes an upper casing 10 having a pressure guiding pipe 9 having a heat-sensitive cylinder 8 at its tip, and an inlet pipe 11. A lower casing 13 having an outlet pipe 12 forms an outer shell 14, a pressure responsive element 16vC is formed inside, and a pressure sensitive chamber 16 is formed above. The lower part is divided into a valve chamber 17.
感圧室16内には冷凍装置の冷媒と同一の凝縮ガスを充
填しており、弁室17には人1コ管11と出に1管12
との回路を開閉する弁装置18を備えている。弁装置1
8はブロック19の上面中央に形成した弁座2oとホル
ダー21内に収納しプこボール弁22より構成し、下部
ケーゾング13とホルダ−21外周との間にバネ23を
圧縮状態で備え、このバネ23の付勢力にてスペーサ2
4を介してホルダー21を前記圧力応動素子16下面中
央に押圧している。従って、ボール弁22は圧力応動素
子15の変位に連動して上下し、弁装置18を開閉する
ものである。ブロック19外周と下部ケーシング13は
調整ネジ25で螺合せしめられ、弁装置18の開閉を決
定する感圧室16と弁室17との差圧の調整を行ない、
調整ネジ25をローイ:Jけにより気密々閉している。The pressure sensitive chamber 16 is filled with the same condensed gas as the refrigerant in the refrigeration system, and the valve chamber 17 is filled with one tube 11 for one person and one tube 12 for one person.
It is equipped with a valve device 18 that opens and closes a circuit with. Valve device 1
8 consists of a valve seat 2o formed at the center of the upper surface of the block 19 and a ball valve 22 housed in a holder 21. A spring 23 is provided in a compressed state between the lower casing ring 13 and the outer periphery of the holder 21. Spacer 2 due to the biasing force of spring 23
4, the holder 21 is pressed against the center of the lower surface of the pressure responsive element 16. Therefore, the ball valve 22 moves up and down in conjunction with the displacement of the pressure responsive element 15 to open and close the valve device 18. The outer periphery of the block 19 and the lower casing 13 are screwed together with an adjustment screw 25 to adjust the differential pressure between the pressure sensitive chamber 16 and the valve chamber 17, which determines the opening and closing of the valve device 18.
The adjusting screw 25 is closed air-tight by tightening it.
この実施例においては弁装置18の開閉差圧がOKp/
cdl となるよう調整しである。In this embodiment, the opening/closing differential pressure of the valve device 18 is OKp/
Adjust it so that it is cdl.
また、感熱筒8は圧縮機1と逆止弁7との間の吸入配管
26の一部と交熱的に装着している。つまり、差圧弁3
の感圧室16内は逆止弁7と圧縮機1との間の吸入配管
26の温度Tll に相当する圧力が作用し、弁室17
内は凝縮温度T。に相当する圧力が作用しており、この
差圧が所定値(OKp/crA )になったとき弁装置
18は開閉される。換言すれば、吸入配管26の温度T
、>凝縮温度T。のときに差圧弁3の弁装置18は開路
し、吸入配管温度T8≦凝縮温度Tcのときに前記弁装
置1日は閉路するよう構成している。Further, the heat-sensitive cylinder 8 is attached to a part of the suction pipe 26 between the compressor 1 and the check valve 7 for heat exchange. In other words, the differential pressure valve 3
A pressure corresponding to the temperature Tll of the suction pipe 26 between the check valve 7 and the compressor 1 acts inside the pressure sensitive chamber 16,
Inside is condensation temperature T. A pressure corresponding to is acting on the valve device 18, and when this differential pressure reaches a predetermined value (OKp/crA), the valve device 18 is opened and closed. In other words, the temperature T of the suction pipe 26
, >condensation temperature T. At this time, the valve device 18 of the differential pressure valve 3 is opened, and when the suction pipe temperature T8≦condensation temperature Tc, the valve device 18 is configured to be closed for the rest of the day.
上記構成による動作について温度を基準に説明する。圧
縮機1の運転中は凝縮器2には圧縮機1で圧縮された高
温、高圧ガスが凝縮し、その温度T0は、通常周囲温度
より約5〜1Qdeg高い温度となる。The operation of the above configuration will be explained based on temperature. During operation of the compressor 1, the high temperature, high pressure gas compressed by the compressor 1 is condensed in the condenser 2, and its temperature T0 is usually about 5 to 1 Qdeg higher than the ambient temperature.
一方、圧縮機1の吸入配管26には蒸発器6で熱交換さ
れ、蒸発温度より過熱されたガスが流れているが、その
温度T8 は周囲温度より5〜10deg低い温度とな
っており一部2図のようにTc> Tgであるため差圧
弁3の弁装置18は開路されている。次に圧縮機1が停
止すると凝縮器2の放熱により凝縮温度T0 は低下す
るが、このときも高圧側圧力は凝縮@度T。に相当する
圧ツノである。と同時に圧縮機1の機械室6の油膜シー
ルが破れ、圧縮機1内の高温冷媒が機械室6を逆流して
吸入配管26へと流入する。このとき逆止弁7は冷媒流
の停止に伴ない閉路している/こめ、第2図のように吸
入配管26a腺Tllは急激に上昇し、凝縮温度T。よ
りも高くなる。これは凝縮温度Tc よりはるかに温
度の高い圧縮機1内の高温ガスが流入するだめである。On the other hand, gas that has undergone heat exchange in the evaporator 6 and has been superheated to the evaporation temperature is flowing through the suction pipe 26 of the compressor 1, but the temperature T8 is 5 to 10 degrees lower than the ambient temperature and some As shown in FIG. 2, since Tc>Tg, the valve device 18 of the differential pressure valve 3 is opened. Next, when the compressor 1 stops, the condensation temperature T0 decreases due to heat radiation from the condenser 2, but at this time too, the high pressure side pressure is condensed @ degrees T. It is a pressure horn corresponding to . At the same time, the oil film seal in the machine room 6 of the compressor 1 is broken, and the high-temperature refrigerant in the compressor 1 flows backward through the machine room 6 and into the suction pipe 26 . At this time, the check valve 7 is closed due to the stoppage of the refrigerant flow, and as shown in FIG. 2, the suction pipe 26a gland Tll rapidly rises to the condensing temperature T. be higher than This is due to the inflow of high temperature gas in the compressor 1 whose temperature is much higher than the condensation temperature Tc.
従って、圧縮機1が停止すると速やかに第2図のように
吸入配管温度Ts>凝縮6’P度T。となり、差圧弁3
の弁装置18は閉路する。Therefore, as soon as the compressor 1 stops, as shown in FIG. 2, the suction pipe temperature Ts>condensation 6'P degree T. Therefore, differential pressure valve 3
The valve device 18 is closed.
弁装置18の閉路により凝縮器2内の冷媒が減圧器4及
び蒸発器6へと流入することはなく、凝縮器2内は運転
中、停止中共に同一状態に維持されている。圧縮機1に
おいても同様で、運転中圧縮機1内の高圧冷媒は停止中
に機械室6より吸入配管26を逆止弁7まで逆流するが
その量は微少であり、圧縮機1内の冷媒は運転中、停止
中共にほぼ同一状態である。従って、停止後起動すると
高圧側にはすみやかに充分な冷媒が分布しているため、
即定常運転状態となシ、凝縮器2.蒸発器5共に約10
0%の熱交換能力を発揮でき、非常に高効率な冷却運転
を可能としている。By closing the valve device 18, the refrigerant in the condenser 2 does not flow into the pressure reducer 4 and the evaporator 6, and the inside of the condenser 2 is maintained in the same state both during operation and during stoppage. The same applies to the compressor 1, and the high-pressure refrigerant in the compressor 1 during operation flows backwards from the machine room 6 through the suction pipe 26 to the check valve 7 while the compressor 1 is stopped, but the amount is very small, and the refrigerant in the compressor 1 is in almost the same state both during operation and when stopped. Therefore, when starting after stopping, sufficient refrigerant is quickly distributed on the high pressure side, so
Immediately enter steady operation condition, condenser 2. Approximately 10 evaporators (5 and 5)
It can exhibit 0% heat exchange capacity, making extremely highly efficient cooling operation possible.
発明の効果
以上の説明からも明らかなように、本発明は圧縮機と圧
縮機の吸入側に接続した逆止弁間に装着した感熱筒の温
度に相当する圧力と凝縮器圧力との差圧にて圧力応動素
子を変位せしめ、この圧力応動素子の変位により開閉す
る弁装置を凝縮器と減圧器間に設けたものであるから、
運転中は通常の冷凍サイクルを構成し、そして、停止と
ほとA7ど同時に弁装置を閉路するため凝縮器内冷媒が
停止中に減少することがない。丑だ、停止中、1[縮機
から逆流する冷媒は逆止弁で止められ、蒸発器へと流入
することなく、運転中と同一状態を維持していると共に
、圧縮機吸入管と圧縮機内も同一圧力にバランスしてい
る。従って、圧縮機は圧力がバランスした状態で起動す
るため、従来とはとんど同じ起動性能であり、しかも、
起動時から冷凍装置全体が運転中と同一の冷媒状態であ
り、即定常運転状態が発揮され、従来比約20%up。Effects of the Invention As is clear from the above explanation, the present invention is capable of reducing the pressure difference between the pressure corresponding to the temperature of the heat-sensitive tube installed between the compressor and the check valve connected to the suction side of the compressor and the condenser pressure. A valve device is provided between the condenser and the pressure reducer, which opens and closes according to the displacement of the pressure-responsive element.
During operation, a normal refrigeration cycle is configured, and the valve device is closed almost at the same time as A7 is stopped, so the refrigerant in the condenser does not decrease during stoppage. During stoppage, 1. The refrigerant flowing back from the compressor is stopped by a check valve, and does not flow into the evaporator, maintaining the same state as during operation, and the compressor suction pipe and inside the compressor. are also balanced to the same pressure. Therefore, the compressor starts with the pressure balanced, so the starting performance is almost the same as before.
From the time of startup, the entire refrigeration system is in the same refrigerant state as during operation, and a steady state of operation is achieved immediately, an increase of about 20% compared to conventional systems.
高効率化が図れるものである。This allows for high efficiency.
第1図は本発明の一実施例である冷凍装置の概略図、第
2図は第1図の冷凍装置の要部温度変化図、第3図は従
来改良型冷凍装置の概略図、第4図は第3図の装置にお
ける圧力変化特性図である。
1・・・・・・圧縮機、2・・・・・凝縮器、3・・・
・・・差圧弁、4・・・・・・減圧器、5・・・・・・
蒸発器、7・・・・・・逆止弁、8・°°・・・感熱筒
、11・・・・・・入口l管、12・・・・・・出[−
1管、16・・・・・・圧力応動素子、16・・・・・
・感圧室、17・・・・・弁室、18・・・・・・弁装
置。
代理人の氏名 弁理士 中 尾 敏 男 はが1名第1
図
第2図
一時間
第 3 区
第4図
−H仔rMEjFig. 1 is a schematic diagram of a refrigeration system according to an embodiment of the present invention, Fig. 2 is a temperature change diagram of main parts of the refrigeration system shown in Fig. 1, Fig. 3 is a schematic diagram of a conventional improved refrigeration system, and Fig. 4 is a schematic diagram of a conventional improved refrigeration system. The figure is a pressure change characteristic diagram in the apparatus of FIG. 3. 1... Compressor, 2... Condenser, 3...
...Differential pressure valve, 4...Reducer, 5...
Evaporator, 7...Check valve, 8.°°...Thermosensitive tube, 11...Inlet l pipe, 12...Output [-
1 tube, 16... Pressure responsive element, 16...
-Pressure sensitive chamber, 17...valve chamber, 18...valve device. Name of agent: Patent attorney Toshio Nakao (1st person)
Figure 2 Figure 2 1 hour 3rd section Figure 4 - H child rMEj
Claims (1)
次環状に接続して構成し、前記差圧弁は圧力応動素子に
て内部を感圧室と弁室の2室の気密に区画され、前記感
圧室には外部に延在する感熱筒を備え、かつ内部に凝縮
性ガスを充填し、一方前記弁室には入口管、出口管を有
し、両管の間に前記圧力応動素子の応位により開閉する
弁装置を備え、前記感熱筒を前記圧縮機と前記逆止弁間
にて熱又換状態に装着し、前記差圧弁内の前記弁室圧力
が前記感圧室圧力より所定値以上の時に前記弁装置を開
略する冷凍装置。A compressor, a condenser, a differential pressure valve, a pressure reducer, an evaporator, and a check valve are sequentially connected in an annular manner. The pressure-sensitive chamber is equipped with a heat-sensitive cylinder extending outside and is filled with condensable gas, while the valve chamber has an inlet pipe and an outlet pipe, and a pipe is provided between the two pipes. The valve device is provided with a valve device that opens and closes according to the response of the pressure responsive element, the heat sensitive tube is installed between the compressor and the check valve in a heat exchange state, and the valve chamber pressure in the differential pressure valve is A refrigeration system that opens the valve device when the pressure in the pressure chamber is higher than a predetermined value.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57201452A JPS5993161A (en) | 1982-11-16 | 1982-11-16 | Refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57201452A JPS5993161A (en) | 1982-11-16 | 1982-11-16 | Refrigerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5993161A true JPS5993161A (en) | 1984-05-29 |
Family
ID=16441318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57201452A Pending JPS5993161A (en) | 1982-11-16 | 1982-11-16 | Refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5993161A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0518615A (en) * | 1991-07-12 | 1993-01-26 | Mitsubishi Electric Corp | Freezer refrigerator |
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| JPH10163013A (en) * | 1996-11-29 | 1998-06-19 | Hokuriku Electric Ind Co Ltd | Method for trimming resistor |
| JP2002156358A (en) * | 2000-11-20 | 2002-05-31 | Matsushita Electric Ind Co Ltd | Biosensor, notification device, and measurement device |
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| EP2051072A2 (en) * | 2007-10-19 | 2009-04-22 | HMD BioMedical Inc. | Test strip identification function and test instrument using the same |
| JP2009231359A (en) * | 2008-03-19 | 2009-10-08 | Hitachi Ltd | Thick-film resistor |
| JP2010524001A (en) * | 2007-04-12 | 2010-07-15 | ホーム ダイアグナスティックス,インコーポレーテッド | Error detection and elimination in diagnostic test systems |
| JP2010525373A (en) * | 2007-04-27 | 2010-07-22 | アボット ダイアベティス ケア インコーポレイテッド | Test strip identification using conductive patterns |
| JP2011075411A (en) * | 2009-09-30 | 2011-04-14 | Gunze Ltd | Apparatus for measurement of substrate component quantity of specimen, biosensor, and measurement display device |
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1982
- 1982-11-16 JP JP57201452A patent/JPS5993161A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10163013A (en) * | 1996-11-29 | 1998-06-19 | Hokuriku Electric Ind Co Ltd | Method for trimming resistor |
| JP2002156358A (en) * | 2000-11-20 | 2002-05-31 | Matsushita Electric Ind Co Ltd | Biosensor, notification device, and measurement device |
| JP2009031309A (en) * | 2001-09-28 | 2009-02-12 | Arkray Inc | Concentration measuring device |
| JP2008527341A (en) * | 2005-01-12 | 2008-07-24 | エフ ホフマン−ラ ロッシュ アクチェン ゲゼルシャフト | New electrode design for biosensors |
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| JP2010524001A (en) * | 2007-04-12 | 2010-07-15 | ホーム ダイアグナスティックス,インコーポレーテッド | Error detection and elimination in diagnostic test systems |
| JP2010525373A (en) * | 2007-04-27 | 2010-07-22 | アボット ダイアベティス ケア インコーポレイテッド | Test strip identification using conductive patterns |
| EP2051072A2 (en) * | 2007-10-19 | 2009-04-22 | HMD BioMedical Inc. | Test strip identification function and test instrument using the same |
| JP2009231359A (en) * | 2008-03-19 | 2009-10-08 | Hitachi Ltd | Thick-film resistor |
| JP2011075411A (en) * | 2009-09-30 | 2011-04-14 | Gunze Ltd | Apparatus for measurement of substrate component quantity of specimen, biosensor, and measurement display device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0518615A (en) * | 1991-07-12 | 1993-01-26 | Mitsubishi Electric Corp | Freezer refrigerator |
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