JP2001074325A - Two-stage compression type freezing and refrigerating system - Google Patents
Two-stage compression type freezing and refrigerating systemInfo
- Publication number
- JP2001074325A JP2001074325A JP24751599A JP24751599A JP2001074325A JP 2001074325 A JP2001074325 A JP 2001074325A JP 24751599 A JP24751599 A JP 24751599A JP 24751599 A JP24751599 A JP 24751599A JP 2001074325 A JP2001074325 A JP 2001074325A
- Authority
- JP
- Japan
- Prior art keywords
- stage compression
- compression element
- low
- pressure
- stage
- 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.)
- Granted
Links
- 230000006835 compression Effects 0.000 title claims abstract description 324
- 238000007906 compression Methods 0.000 title claims abstract description 324
- 238000007710 freezing Methods 0.000 title claims abstract description 41
- 230000008014 freezing Effects 0.000 title claims abstract description 41
- 238000005057 refrigeration Methods 0.000 claims description 90
- 238000001704 evaporation Methods 0.000 abstract description 38
- 238000007599 discharging Methods 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 62
- 230000008020 evaporation Effects 0.000 description 21
- 230000000694 effects Effects 0.000 description 13
- 239000007788 liquid Substances 0.000 description 13
- 238000010586 diagram Methods 0.000 description 10
- 238000004891 communication Methods 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 239000010687 lubricating oil Substances 0.000 description 8
- 230000010349 pulsation Effects 0.000 description 5
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000013021 overheating Methods 0.000 description 4
- 238000012937 correction Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000001050 lubricating effect Effects 0.000 description 3
- 238000005461 lubrication Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 101000801109 Homo sapiens Transmembrane protein 131 Proteins 0.000 description 1
- 102100033700 Transmembrane protein 131 Human genes 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/13—Economisers
Landscapes
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、2つの圧縮要素を
持つ二段圧縮機を備えた二段圧縮冷凍冷蔵装置に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a two-stage compression refrigeration apparatus having a two-stage compressor having two compression elements.
【0002】[0002]
【従来の技術】冷凍機器分野において、低温熱源および
高温熱源確保の一環として、高圧縮比運転に適した多段
圧縮機を用いた二段圧縮冷凍装置が提案されている。従
来の二段圧縮冷凍装置として、例えば特開平5−133
368号公報に示されているものがある。2. Description of the Related Art In the field of refrigeration equipment, a two-stage compression refrigeration system using a multi-stage compressor suitable for high compression ratio operation has been proposed as part of securing a low-temperature heat source and a high-temperature heat source. As a conventional two-stage compression refrigeration system, for example, Japanese Patent Application Laid-Open No. 5-133
No. 368 is disclosed.
【0003】以下、図面を参照しながら上記従来の二段
圧縮冷凍装置の一例について説明する。Hereinafter, an example of the conventional two-stage compression refrigeration system will be described with reference to the drawings.
【0004】図11は従来の二段圧縮機を使用した二段
圧縮冷凍サイクルの配管系統図である。FIG. 11 is a piping diagram of a two-stage compression refrigeration cycle using a conventional two-stage compressor.
【0005】図11において、1は二段圧縮機で、2は
凝縮器、3は第1膨張弁、4は気液分離機、5は第2膨
張弁、6は蒸発器、7はアキュムレータであり、これら
が順次配管により接続されている。8は密閉容器であ
り、密閉容器8内の上部空間にはモーター9、その下部
には二段圧縮機構10が配置され、その外周部および底
部が油溜11として構成されている。二段圧縮機構10
は、上部の高段圧縮要素12と下部の低段圧縮要素13
と両圧縮要素(12,13)の間に配置された平板形状
の中板14とからなる。15は第1偏心部15aと第2
偏心部15bを持つクランクシャフトであり、モーター
9のローター9aに固定されている。16、17はクラ
ンクシャフト15の第1偏心部15aと第2偏心部15
bに装着された第1ピストンおよび第2ピストンであ
る。高段圧縮要素12の気筒容積は、低段圧縮要素13
の気筒容積の約45〜65%に設定されている。低段圧
縮要素13の吐出側と高段圧縮要素12の吸入側とは連
通路18を介して連通している。19は冷媒インジェク
ション通路であり、連通路18と気液分離機4の下流側
とを連通している。In FIG. 11, 1 is a two-stage compressor, 2 is a condenser, 3 is a first expansion valve, 4 is a gas-liquid separator, 5 is a second expansion valve, 6 is an evaporator, and 7 is an accumulator. Yes, these are sequentially connected by piping. Reference numeral 8 denotes an airtight container. A motor 9 is disposed in an upper space in the airtight container 8, and a two-stage compression mechanism 10 is disposed below the motor 9, and an outer peripheral portion and a bottom portion thereof are configured as an oil reservoir 11. Two-stage compression mechanism 10
Are the upper stage compression element 12 and the lower stage compression element 13
And a flat plate-shaped middle plate 14 disposed between the compression elements (12, 13). 15 is the first eccentric portion 15a and the second
It is a crankshaft having an eccentric portion 15b, which is fixed to the rotor 9a of the motor 9. Reference numerals 16 and 17 denote a first eccentric portion 15a and a second eccentric portion 15 of the crankshaft 15.
b shows a first piston and a second piston mounted on the b. The cylinder capacity of the high-stage compression element 12 is
Is set to about 45 to 65% of the cylinder capacity of the cylinder. The discharge side of the low-stage compression element 13 communicates with the suction side of the high-stage compression element 12 via a communication passage 18. Reference numeral 19 denotes a refrigerant injection passage, which communicates the communication passage 18 with the downstream side of the gas-liquid separator 4.
【0006】以上のように構成された二段圧縮冷凍装置
について、以下その動作を説明する。[0006] The operation of the two-stage compression refrigeration system configured as described above will be described below.
【0007】モーター3によってクランクシャフト15
が回転すると、低段圧縮要素13はアキュームレータ7
から冷媒ガスを吸入して圧縮し、連通路18に吐出す
る。低段圧縮要素13から連通路18に吐出された冷媒
ガスは、冷媒インジェクション通路19からの冷媒ガス
と混合して、高段圧縮要素12の吸入側から吸入され、
再び圧縮される。高段圧縮要素12で圧縮された冷媒ガ
スは、密閉容器8内に一旦吐出された後に、配管を介し
て凝縮器2に送られる。凝縮器2で冷媒ガスは放熱して
凝縮されて液冷媒になった後、第1膨張弁3により減圧
される。そして、気液分離器4に流入し、一部はそこで
蒸発する。これにより、気液分離器4内底部には液冷媒
が貯溜され、気液分離器4内上部には一段膨張した飽和
ガス冷媒が溜まる。そして、気液分離器4内からは液冷
媒のみが第2膨張弁5方向に流出し、そこで減圧されて
蒸発器6に流入して蒸発する。このときに周囲から熱を
奪うことによって蒸発器6は冷却作用を発揮する。そし
て、蒸発器6を出た低温ガス冷媒はアキュームレータ7
を経て二段圧縮機1に帰還し、再び低段圧縮要素13に
吸入される。The crankshaft 15 is driven by the motor 3.
Rotates, the low-stage compression element 13
The refrigerant gas is sucked from the compressor, compressed, and discharged to the communication passage 18. The refrigerant gas discharged from the low-stage compression element 13 to the communication passage 18 mixes with the refrigerant gas from the refrigerant injection passage 19 and is sucked from the suction side of the high-stage compression element 12,
It is compressed again. The refrigerant gas compressed by the high-stage compression element 12 is once discharged into the closed vessel 8 and then sent to the condenser 2 via a pipe. The refrigerant gas radiates heat in the condenser 2 to be condensed into a liquid refrigerant, and then decompressed by the first expansion valve 3. Then, the gas flows into the gas-liquid separator 4 and a part thereof evaporates there. As a result, the liquid refrigerant is stored at the bottom inside the gas-liquid separator 4, and the saturated gas refrigerant that has expanded in one stage is stored at the top inside the gas-liquid separator 4. Then, only the liquid refrigerant flows out of the gas-liquid separator 4 in the direction of the second expansion valve 5, where it is depressurized, flows into the evaporator 6, and evaporates. At this time, the evaporator 6 exerts a cooling action by removing heat from the surroundings. Then, the low-temperature gaseous refrigerant leaving the evaporator 6 is supplied to the accumulator 7
Then, it is returned to the two-stage compressor 1 and is sucked into the low-stage compression element 13 again.
【0008】一方、気液分離器4内上部の飽和ガス冷媒
は、冷媒インジェクション通路19を経て連通路18に
流入する。そこで、低段圧縮要素13から吐出された冷
媒ガスの温度を下げるため、高段圧縮要素12が吸入す
る冷媒ガスの温度を下げることができ、効率を向上する
ことができる。また、高段圧縮要素12の吐出ガスの温
度も低くなるため、圧縮機の過熱を防止でき、潤滑油の
粘度低下による潤滑不良や潤滑油の劣化を防止できる。On the other hand, the saturated gas refrigerant in the upper part of the gas-liquid separator 4 flows into the communication passage 18 via the refrigerant injection passage 19. Therefore, since the temperature of the refrigerant gas discharged from the low-stage compression element 13 is reduced, the temperature of the refrigerant gas sucked by the high-stage compression element 12 can be reduced, and the efficiency can be improved. Further, since the temperature of the gas discharged from the high-stage compression element 12 is also reduced, overheating of the compressor can be prevented, and poor lubrication and deterioration of the lubricating oil due to a decrease in the viscosity of the lubricating oil can be prevented.
【0009】このように二段圧縮冷凍サイクルを使用し
た方が、一段圧縮冷凍サイクルを使用する場合よりも冷
凍サイクルの効率が向上し、圧縮機の信頼性が向上す
る。As described above, the use of the two-stage compression refrigeration cycle improves the efficiency of the refrigeration cycle and improves the reliability of the compressor as compared with the case of using the one-stage compression refrigeration cycle.
【0010】[0010]
【発明が解決しようとする課題】しかしながら上記従来
の構成では、二段圧縮冷凍サイクルを、例えば冷凍冷蔵
庫等の冷凍と冷蔵等の2つ以上の温度帯を必要とする装
置に適用する場合には、最も温度の低い冷凍室の庫内温
度が−18℃〜−22℃程度に設定されるため、蒸発器
6の蒸発温度はそれより低い約−30℃前後にする必要
があった。一方、蒸発温度が高いほど圧縮機の効率は高
くなるため、できるだけ蒸発温度を高く設計する必要が
あるが、前記した冷凍室の庫内温度の制限から蒸発温度
はある値以下に制限される。このため、庫内温度が3℃
〜7℃程度である冷蔵室の冷却にも、−30℃前後の蒸
発器6で冷却した低温の冷気を使用しなければならず、
蒸発温度が低いため冷却システムの効率が悪くなること
に加えて、冷蔵室庫内の温度制御の精度が悪くなると共
に庫内各部の温度が不均一になるという欠点があった。However, in the above-described conventional configuration, when the two-stage compression refrigeration cycle is applied to an apparatus requiring two or more temperature zones, such as freezing and refrigerating, for example, a refrigerator-freezer, etc. Since the temperature in the freezer compartment having the lowest temperature is set at about −18 ° C. to −22 ° C., the evaporation temperature of the evaporator 6 needs to be about −30 ° C. lower than that. On the other hand, the higher the evaporation temperature, the higher the efficiency of the compressor. Therefore, it is necessary to design the evaporation temperature as high as possible. However, the evaporation temperature is limited to a certain value or less due to the above-described limitation of the freezing room temperature. For this reason, the internal temperature is 3 ° C
For cooling the refrigerator compartment at about -7 ° C, low-temperature cold air cooled by the evaporator 6 at about -30 ° C must be used.
In addition to the low efficiency of the cooling system due to the low evaporating temperature, the accuracy of temperature control in the refrigerator compartment deteriorates and the temperature of each part in the refrigerator becomes uneven.
【0011】本発明は従来の課題を解決するもので、冷
凍冷蔵装置の冷凍室と冷蔵室の各庫内温度に適した蒸発
温度を持つ2つの蒸発器と二段圧縮機を備えることによ
り、各庫内の温度制御の精度を高めると共に庫内各部の
温度の均一化が図れ、更に高効率で消費電力が少なく、
また信頼性の高い二段圧縮冷凍冷蔵装置を提供すること
を目的とする。SUMMARY OF THE INVENTION The present invention solves the conventional problems, and comprises two evaporators and two-stage compressors each having an evaporating temperature suitable for the temperature in each of the freezing compartment and the refrigerator compartment of a freezing and refrigeration apparatus. The accuracy of temperature control in each chamber is improved, and the temperature of each section in the chamber can be made uniform, with higher efficiency and less power consumption.
It is another object of the present invention to provide a highly reliable two-stage compression refrigeration apparatus.
【0012】また、上記従来の構成は、蒸発器6のみで
冷却作用を得る必要があるために、気液分離器4から分
流する冷媒循環量は冷媒インジェクション通路19側よ
りも第2膨張弁5側の方が多くなる。そのため、二段圧
縮機1の高段圧縮要素12の気筒容積は低段圧縮要素1
3の気筒容積の約45〜65%に設定されている。この
二段圧縮機1を、冷凍冷蔵装置の冷凍室と冷蔵室の各庫
内温度に適した2つの蒸発器を持つ冷凍サイクルに適用
する場合には、高段圧縮要素12の気筒容積が低段圧縮
要素13の気筒容積よりかなり小さいために、冷蔵室用
の蒸発器の冷凍能力が小さくなり、冷凍室と冷蔵室を適
正に冷却することができない可能性があるという欠点が
あった。Further, in the above-mentioned conventional configuration, since it is necessary to obtain a cooling action only by the evaporator 6, the amount of the refrigerant circulated from the gas-liquid separator 4 is smaller than that of the refrigerant injection passage 19 in the second expansion valve 5. More on the side. Therefore, the cylinder capacity of the high-stage compression element 12 of the two-stage compressor 1 is
3 is set to about 45 to 65% of the cylinder capacity. When the two-stage compressor 1 is applied to a refrigeration cycle having two evaporators suitable for the temperatures in the freezing compartment and the freezing compartment of the refrigeration apparatus, the cylinder capacity of the high-stage compression element 12 is low. Since it is considerably smaller than the cylinder capacity of the stage compression element 13, the refrigerating capacity of the evaporator for the refrigerating compartment becomes small, and there is a disadvantage that the refrigerating compartment and the refrigerating compartment may not be properly cooled.
【0013】本発明の他の目的は、冷凍冷蔵装置の冷凍
室と冷蔵室の各庫内温度に適した蒸発温度を持つ2つの
蒸発器と二段圧縮機を備え、かつ高段圧縮要素の気筒容
積と低段圧縮要素の気筒容積の比率を適正にすることに
より、冷凍冷蔵装置の冷凍室と冷蔵室などの異なる温度
帯の庫内のどちらか一方が冷凍能力不足になったり、冷
凍能力過剰になること無く、各庫内を適正に冷却でき、
かつ高効率で消費電力の少ない二段圧縮冷凍冷蔵装置を
提供することを目的とする。Another object of the present invention is to provide a two-stage compressor and two evaporators each having an evaporating temperature suitable for the temperature in each of the freezing compartment and the refrigerating compartment of the freezing and refrigeration apparatus. By optimizing the ratio of the cylinder capacity to the cylinder capacity of the low-stage compression element, one of the freezer compartments in the freezer compartment and the refrigerating compartment in a different temperature zone, such as the freezer compartment, becomes insufficient in refrigeration capacity, Each chamber can be properly cooled without becoming excessive,
It is another object of the present invention to provide a two-stage compression refrigerating / cooling apparatus having high efficiency and low power consumption.
【0014】[0014]
【課題を解決するための手段】この目的を達成するため
に本発明は、密閉容器内にモーターと低段圧縮要素と高
段圧縮要素とを備えた二段圧縮機と、前記高段圧縮要素
の吐出側と配管接続した凝縮器と、前記凝縮器の出口側
と配管接続した中間圧用膨張装置と、前記低段圧縮要素
の吐出側ならびに前記高段圧縮要素の吸入側と共に連通
する中間圧用吸入パイプと、前記中間圧用膨張装置と前
記中間圧用吸入パイプとの間に配管接続された中間圧用
蒸発器と、前記凝縮器の出口側あるいは前記中間圧用膨
張装置の出口側と配管接続した低圧用膨張装置と、前記
低圧用膨張装置と前記二段圧縮機の低段圧縮要素の吸入
側との間に配管接続された低圧用蒸発器とからなり、前
記低段圧縮要素の吐出側と前記高段圧縮要素の吸入側と
が前記密閉容器内に連通した構成としたのである。SUMMARY OF THE INVENTION To achieve this object, the present invention provides a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container; A condenser connected to the discharge side of the condenser by a pipe, an expansion device for intermediate pressure connected to the outlet side of the condenser by a pipe, and an intermediate pressure suction communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element. A pipe, an intermediate-pressure evaporator connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe, and a low-pressure expansion connected to the outlet of the condenser or the outlet of the intermediate-pressure expansion device. And a low-pressure evaporator connected by piping between the low-pressure expansion device and the suction side of the low-stage compression element of the two-stage compressor, wherein the discharge side of the low-stage compression element and the high-stage The suction side of the compression element is in the closed container It was a structure in communication.
【0015】これにより、冷凍冷蔵装置の2つの蒸発器
はそれぞれ、冷凍室と冷蔵室等の各庫内温度に適した蒸
発温度にすることができ、各庫内の温度制御の精度が高
くなると共に庫内各部の温度の均一化が図れる。また、
特に中間圧用蒸発器の蒸発温度を高く設定できるため圧
縮機の効率が向上すると共に、各庫内を必要以上に温度
の低い冷気で冷却することが無いため冷凍サイクル全体
の効率が向上する。更に、密閉容器内が中間圧力になっ
ているため、低段圧縮要素ならびに高段圧縮要素のそれ
ぞれの圧縮室内と密閉容器内との圧力差が小さく、各圧
縮要素と密閉容器内の間での冷媒ガスの漏れ量を少なく
することができ、二段圧縮機の冷凍能力、ならびに効率
を向上することができる。Thus, the two evaporators of the freezing and refrigerating apparatus can be set to the evaporating temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room, respectively, and the accuracy of the temperature control in each of the internal refrigerators is improved. At the same time, the temperature of each part in the refrigerator can be made uniform. Also,
In particular, since the evaporation temperature of the intermediate-pressure evaporator can be set high, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. Furthermore, since the inside of the closed vessel is at an intermediate pressure, the pressure difference between the compression chamber of each of the low-stage compression element and the high-stage compression element and the inside of the closed vessel is small, and the pressure between each compression element and the inside of the closed vessel is small. The leakage amount of the refrigerant gas can be reduced, and the refrigeration capacity and efficiency of the two-stage compressor can be improved.
【0016】また、本発明は、密閉容器内にモーターと
低段圧縮要素と高段圧縮要素とを備えた二段圧縮機と、
前記高段圧縮要素の吐出側と配管接続した凝縮器と、前
記凝縮器の出口側と配管接続した中間圧用膨張装置と、
前記低段圧縮要素の吐出側ならびに前記高段圧縮要素の
吸入側と共に連通する中間圧用吸入パイプと、前記中間
圧用膨張装置と前記中間圧用吸入パイプとの間に配管接
続された中間圧用蒸発器と、前記凝縮器の出口側あるい
は前記中間圧用膨張装置の出口側と配管接続した低圧用
膨張装置と、前記低圧用膨張装置と前記二段圧縮機の低
段圧縮要素の吸入側との間に配管接続された低圧用蒸発
器とからなり、前記低段圧縮要素の吸入側が前記密閉容
器内に連通した構成としたのである。Further, the present invention provides a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container,
A condenser pipe-connected to the discharge side of the high-stage compression element, an intermediate-pressure expansion device pipe-connected to the outlet side of the condenser,
An intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element; and an intermediate-pressure evaporator pipe-connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe. A low-pressure expansion device pipe-connected to an outlet side of the condenser or an outlet side of the intermediate-pressure expansion device, and a pipe between the low-pressure expansion device and a suction side of a low-stage compression element of the two-stage compressor. A low-pressure evaporator is connected to the low-pressure compression element, and the suction side of the low-stage compression element communicates with the closed vessel.
【0017】これにより、冷凍冷蔵装置の2つの蒸発器
はそれぞれ、冷凍室と冷蔵室等の各庫内温度に適した蒸
発温度にすることができ、各庫内の温度制御の精度が高
くなると共に庫内各部の温度の均一化が図れる。また、
特に中間圧用蒸発器の蒸発温度を高く設定できるため圧
縮機の効率が向上すると共に、各庫内を必要以上に温度
の低い冷気で冷却することが無いため冷凍サイクル全体
の効率が向上する。更に、密閉容器内が低圧になってお
り、低圧用蒸発器から戻ってくる温度の低い冷媒ガスで
密閉容器内の各圧縮要素やモータを冷却できるので、各
圧縮要素の過熱を防止でき信頼性が向上すると共に、モ
ータの温度低下によりモータ効率を向上することができ
る。Thus, the two evaporators of the freezing and refrigerating apparatus can be set to the evaporating temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room, respectively, and the accuracy of the temperature control in each of the internal refrigerators is improved. At the same time, the temperature of each part in the refrigerator can be made uniform. Also,
In particular, since the evaporation temperature of the intermediate-pressure evaporator can be set high, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. Furthermore, since the pressure inside the sealed container is low, and each compression element and motor in the sealed container can be cooled by a low-temperature refrigerant gas returning from the low-pressure evaporator, overheating of each compression element can be prevented, and reliability can be prevented. And the motor efficiency can be improved by lowering the temperature of the motor.
【0018】また、本発明は、密閉容器内にモーターと
低段圧縮要素と高段圧縮要素とを備えた二段圧縮機と、
前記高段圧縮要素の吐出側と配管接続した凝縮器と、前
記凝縮器の出口側と配管接続した中間圧用膨張装置と、
前記低段圧縮要素の吐出側ならびに前記高段圧縮要素の
吸入側と共に連通する中間圧用吸入パイプと、前記中間
圧用膨張装置と前記中間圧用吸入パイプとの間に配管接
続された中間圧用蒸発器と、前記凝縮器の出口側あるい
は前記中間圧用膨張装置の出口側と配管接続した低圧用
膨張装置と、前記低圧用膨張装置と前記二段圧縮機の低
段圧縮要素の吸入側との間に配管接続された低圧用蒸発
器とからなり、前記高段圧縮要素の吐出側が前記密閉容
器内に連通した構成としたのである。Further, the present invention provides a two-stage compressor including a motor, a low-stage compression element and a high-stage compression element in a closed container,
A condenser pipe-connected to the discharge side of the high-stage compression element, an intermediate-pressure expansion device pipe-connected to the outlet side of the condenser,
An intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element; and an intermediate-pressure evaporator pipe-connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe. A low-pressure expansion device pipe-connected to an outlet side of the condenser or an outlet side of the intermediate-pressure expansion device, and a pipe between the low-pressure expansion device and a suction side of a low-stage compression element of the two-stage compressor. A low-pressure evaporator was connected, and the discharge side of the high-stage compression element was configured to communicate with the closed vessel.
【0019】これにより、冷凍冷蔵装置の2つの蒸発器
はそれぞれ、冷凍室と冷蔵室等の各庫内温度に適した蒸
発温度にすることができ、各庫内の温度制御の精度が高
くなると共に庫内各部の温度の均一化が図れる。また、
特に中間圧用蒸発器の蒸発温度を高く設定できるため圧
縮機の効率が向上すると共に、各庫内を必要以上に温度
の低い冷気で冷却することが無いため冷凍サイクル全体
の効率が向上する。更に、密閉容器内が高圧になってい
るため、圧力差により密閉容器内から低段圧縮要素なら
びに高段圧縮要素それぞれの圧縮室内への潤滑油の供給
が十分にでき、ピストンとシリンダー等の摺動部の潤滑
性が向上して信頼性を向上することができる。Thus, the two evaporators of the freezing and refrigerating apparatus can be set to the evaporating temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room, respectively, and the accuracy of the temperature control in each of the internal refrigerators is improved. At the same time, the temperature of each part in the refrigerator can be made uniform. Also,
In particular, since the evaporation temperature of the intermediate-pressure evaporator can be set high, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. Further, since the pressure in the closed vessel is high, lubricating oil can be sufficiently supplied from the inside of the closed vessel to the compression chambers of the low-stage compression element and the high-stage compression element by the pressure difference. The lubricity of the moving part is improved, and the reliability can be improved.
【0020】また、本発明は、低段圧縮要素の気筒容積
VLと高段圧縮要素の気筒容積VHの比VH/VLが
0.5〜1.3の範囲に設定された構成としたのであ
る。Further, in the present invention, the ratio VH / VL of the cylinder volume VL of the low-stage compression element to the cylinder volume VH of the high-stage compression element is set in the range of 0.5 to 1.3. .
【0021】これにより、冷凍冷蔵装置の2つの蒸発器
はそれぞれ、冷凍室と冷蔵室等の各庫内温度に適した蒸
発温度にすることができ、各庫内の温度制御の精度が高
くなると共に庫内各部の温度の均一化が図れる。また、
特に中間圧用蒸発器の蒸発温度を高く設定できるため圧
縮機の効率が向上すると共に、各庫内を必要以上に温度
の低い冷気で冷却することが無いため冷凍サイクル全体
の効率が向上する。更に、高段圧縮要素の気筒容積と低
段圧縮要素の気筒容積の比率を適正にすることにより、
冷凍冷蔵装置の冷凍室と冷蔵室などの異なる温度帯の庫
内のどちらか一方が冷凍能力不足になったり、冷凍能力
過剰になること無く、各庫内を適正に冷却でき、かつ高
効率で消費電力を少なくすることができる。また、高
圧、低圧、中間圧の各圧力に応じた気筒容積の比率にす
ることにより、モータの最大トルクとトルク変動を小さ
くすることができ、モータ効率の向上と振動低減ができ
る。Thus, the two evaporators of the freezing and refrigerating apparatus can be set to the evaporating temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room, respectively, and the accuracy of temperature control in each of the internal refrigerators is improved. At the same time, the temperature of each part in the refrigerator can be made uniform. Also,
In particular, since the evaporation temperature of the intermediate-pressure evaporator can be set high, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. Furthermore, by making the ratio of the cylinder volume of the high-stage compression element to the cylinder volume of the low-stage compression element appropriate,
Either the freezer compartment and the refrigerator compartment of the freezer compartment in different temperature zones, such as the freezer compartment, will not have insufficient freezing capacity or excess freezing capacity. Power consumption can be reduced. Further, by setting the ratio of the cylinder volume to each of the high pressure, the low pressure, and the intermediate pressure, the maximum torque and the torque fluctuation of the motor can be reduced, and the motor efficiency can be improved and the vibration can be reduced.
【0022】また、本発明は、中間圧用吸入パイプの密
閉容器内への開口部が高段側圧縮要素の吸入側にわずか
な隙間を介して連通する構成としたのである。Further, in the present invention, the opening of the suction pipe for the intermediate pressure into the closed vessel communicates with the suction side of the high-stage compression element through a small gap.
【0023】これにより、冷凍冷蔵装置の2つの蒸発器
はそれぞれ、冷凍室と冷蔵室等の各庫内温度に適した蒸
発温度にすることができ、各庫内の温度制御の精度が高
くなると共に庫内各部の温度の均一化が図れる。また、
特に中間圧用蒸発器の蒸発温度を高く設定できるため圧
縮機の効率が向上すると共に、各庫内を必要以上に温度
の低い冷気で冷却することが無いため冷凍サイクル全体
の効率が向上する。更に、中間圧用蒸発器から中間圧用
吸入パイプを通って密閉容器内に戻ってきた冷媒ガス
は、わずかな隙間を介して高段圧縮要素の吸入側に吸入
されるため、各圧縮要素やモータからの受熱の影響が小
さく、温度上昇が小さく抑えられる。そのため、吸入さ
れる冷媒ガスの密度が大きくなり、冷媒循環量が多くな
ると共に効率を向上することができる。更に、中間圧用
吸入パイプと高段圧縮要素の吸入側が直接接続される場
合に比べて、わずかな隙間があるために高段圧縮要素か
らの圧力脈動は密閉容器内に拡散し、中間圧用吸入パイ
プに伝わり難く、騒音の発生を防止できる。[0023] Thereby, the two evaporators of the freezing and refrigerating apparatus can be set to the evaporating temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room, respectively, and the accuracy of the temperature control in each of the internal refrigerators is improved. At the same time, the temperature of each part in the refrigerator can be made uniform. Also,
In particular, since the evaporation temperature of the intermediate-pressure evaporator can be set high, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. Further, the refrigerant gas returned from the intermediate-pressure evaporator into the closed vessel through the intermediate-pressure suction pipe is sucked into the suction side of the high-stage compression element through a small gap, so that each compression element and the motor The influence of the heat reception is small, and the temperature rise is suppressed to a small level. Therefore, the density of the refrigerant gas to be taken in increases, and the amount of circulating refrigerant increases, and the efficiency can be improved. Furthermore, compared with the case where the intermediate pressure suction pipe and the suction side of the high-stage compression element are directly connected, the pressure pulsation from the high-stage compression element diffuses into the closed vessel due to the slight gap, and the intermediate-pressure suction pipe It is difficult to transmit the noise, and the generation of noise can be prevented.
【0024】[0024]
【発明の実施の形態】本発明の請求項1に記載の発明
は、密閉容器内にモーターと低段圧縮要素と高段圧縮要
素とを備えた二段圧縮機と、前記高段圧縮要素の吐出側
と配管接続した凝縮器と、前記凝縮器の出口側と配管接
続した中間圧用膨張装置と、前記低段圧縮要素の吐出側
ならびに前記高段圧縮要素の吸入側と共に連通する中間
圧用吸入パイプと、前記中間圧用膨張装置と前記中間圧
用吸入パイプとの間に配管接続された中間圧用蒸発器
と、前記凝縮器の出口側あるいは前記中間圧用膨張装置
の出口側と配管接続した低圧用膨張装置と、前記低圧用
膨張装置と前記二段圧縮機の低段圧縮要素の吸入側との
間に配管接続された低圧用蒸発器とからなり、前記低段
圧縮要素の吐出側と前記高段圧縮要素の吸入側とが前記
密閉容器内に連通した構成としたものであり、冷凍冷蔵
装置の2つの蒸発器は、蒸発圧力がそれぞれ低圧と中間
圧になるため、冷凍室と冷蔵室等の各庫内温度に適した
蒸発器温度にそれぞれすることができ、各庫内の温度制
御の精度が高くなると共に庫内各部の温度の均一化が図
れる。また、特に中間圧用蒸発器の蒸発温度を高く設定
できることから、圧縮機の効率が向上すると共に、各庫
内を必要以上に温度の低い冷気で冷却することが無いた
め冷凍サイクル全体の効率が向上する。更に、低段圧縮
要素の吐出側と高段圧縮要素の吸入側とが密閉容器内に
連通しているため、密閉容器内が中間圧力になり、低段
圧縮要素ならびに高段圧縮要素のそれぞれの圧縮室内と
密閉容器内との圧力差が小さく、各圧縮要素と密閉容器
内の間での冷媒ガスの漏れ量を少なくすることができ、
二段圧縮機の冷凍能力、ならびに効率を向上することが
できるという作用を有する。DESCRIPTION OF THE PREFERRED EMBODIMENTS An invention according to claim 1 of the present invention is directed to a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, A condenser pipe-connected to the discharge side, an intermediate-pressure expansion device pipe-connected to the outlet side of the condenser, and an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element An intermediate-pressure evaporator pipe-connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe; and a low-pressure expansion device pipe-connected to the outlet side of the condenser or the outlet side of the intermediate-pressure expansion device. And a low-pressure evaporator piped between the low-pressure expansion device and the suction side of the low-stage compression element of the two-stage compressor, wherein the discharge side of the low-stage compression element and the high-stage compression The suction side of the element communicated with the closed container The two evaporators of the freezing and refrigeration system have low and intermediate evaporating pressures, respectively. Therefore, the evaporator temperatures should be suitable for the temperatures inside the freezer and refrigerator compartments. As a result, the accuracy of temperature control in each of the refrigerators can be improved, and the temperature of each part in the refrigerator can be made uniform. In addition, since the evaporation temperature of the evaporator for the intermediate pressure can be set higher, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each refrigerator is not cooled with unnecessarily low temperature air. I do. Further, since the discharge side of the low-stage compression element and the suction side of the high-stage compression element communicate with each other in the closed container, the inside of the closed container has an intermediate pressure, and each of the low-stage compression element and the high-stage compression element The pressure difference between the compression chamber and the closed container is small, and the amount of refrigerant gas leakage between each compression element and the closed container can be reduced,
This has the effect of improving the refrigerating capacity and efficiency of the two-stage compressor.
【0025】請求項2に記載の発明は、密閉容器内にモ
ーターと低段圧縮要素と高段圧縮要素とを備えた二段圧
縮機と、前記高段圧縮要素の吐出側と配管接続した凝縮
器と、前記凝縮器の出口側と配管接続した中間圧用膨張
装置と、前記低段圧縮要素の吐出側ならびに前記高段圧
縮要素の吸入側と共に連通する中間圧用吸入パイプと、
前記中間圧用膨張装置と前記中間圧用吸入パイプとの間
に配管接続された中間圧用蒸発器と、前記凝縮器の出口
側あるいは前記中間圧用膨張装置の出口側と配管接続し
た低圧用膨張装置と、前記低圧用膨張装置と前記二段圧
縮機の低段圧縮要素の吸入側との間に配管接続された低
圧用蒸発器とからなり、前記低段圧縮要素の吸入側が前
記密閉容器内に連通した構成としたものであり、冷凍冷
蔵装置の2つの蒸発器は、蒸発圧力がそれぞれ低圧と中
間圧になるため、冷凍室と冷蔵室等の各庫内温度に適し
た蒸発器温度にそれぞれすることができ、各庫内の温度
制御の精度が高くなると共に庫内各部の温度の均一化が
図れる。また、特に中間圧用蒸発器の蒸発温度を高く設
定できることから、圧縮機の効率が向上すると共に、各
庫内を必要以上に温度の低い冷気で冷却することが無い
ため冷凍サイクル全体の効率が向上する。更に、低段圧
縮要素の吸入側が密閉容器内に連通しているため、密閉
容器内が低圧になり、低圧用蒸発器から戻ってくる温度
の低い冷媒ガスで密閉容器内の各圧縮要素やモータを冷
却できるので、各圧縮要素の過熱を防止でき信頼性が向
上すると共に、モータの温度低下によりモータ効率を向
上することができるという作用を有する。According to a second aspect of the present invention, there is provided a two-stage compressor including a motor, a low-stage compression element and a high-stage compression element in a closed container, and a condenser connected to a discharge side of the high-stage compression element by piping. An intermediate-pressure expansion device pipe-connected to the outlet side of the condenser, an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element,
An intermediate-pressure evaporator pipe-connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe, and a low-pressure expansion device pipe-connected to the outlet side of the condenser or the outlet side of the intermediate-pressure expansion device, A low-pressure evaporator connected by piping between the low-pressure expansion device and the suction side of the low-stage compression element of the two-stage compressor, wherein the suction side of the low-stage compression element is communicated with the closed vessel. Since the two evaporators of the freezing and refrigeration system have low and intermediate evaporating pressures, respectively, the evaporator temperatures should be suitable for the temperatures in the freezer and refrigerator compartments. As a result, the accuracy of temperature control in each of the refrigerators can be improved, and the temperature of each part in the refrigerator can be made uniform. In addition, since the evaporation temperature of the evaporator for the intermediate pressure can be set higher, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each refrigerator is not cooled with unnecessarily low temperature air. I do. Furthermore, since the suction side of the low-stage compression element communicates with the closed container, the pressure in the closed container becomes low, and the low-temperature refrigerant gas returned from the low-pressure evaporator cools each compression element and motor in the closed container. Can be prevented, overheating of each compression element can be prevented, reliability can be improved, and motor efficiency can be improved by lowering the temperature of the motor.
【0026】請求項3に記載の発明は、密閉容器内にモ
ーターと低段圧縮要素と高段圧縮要素とを備えた二段圧
縮機と、前記高段圧縮要素の吐出側と配管接続した凝縮
器と、前記凝縮器の出口側と配管接続した中間圧用膨張
装置と、前記低段圧縮要素の吐出側ならびに前記高段圧
縮要素の吸入側と共に連通する中間圧用吸入パイプと、
前記中間圧用膨張装置と前記中間圧用吸入パイプとの間
に配管接続された中間圧用蒸発器と、前記凝縮器の出口
側あるいは前記中間圧用膨張装置の出口側と配管接続し
た低圧用膨張装置と、前記低圧用膨張装置と前記二段圧
縮機の低段圧縮要素の吸入側との間に配管接続された低
圧用蒸発器とからなり、前記高段圧縮要素の吐出側が前
記密閉容器内に連通した構成としたものであり、冷凍冷
蔵装置の2つの蒸発器は、蒸発圧力がそれぞれ低圧と中
間圧になるため、冷凍室と冷蔵室等の各庫内温度に適し
た蒸発器温度にそれぞれすることができ、各庫内の温度
制御の精度が高くなると共に庫内各部の温度の均一化が
図れる。また、特に中間圧用蒸発器の蒸発温度を高く設
定できることから、圧縮機の効率が向上すると共に、各
庫内を必要以上に温度の低い冷気で冷却することが無い
ため冷凍サイクル全体の効率が向上する。更に、高段圧
縮要素の吐出側が密閉容器内に連通しているため、密閉
容器内が高圧になり、圧力差により密閉容器内から低段
圧縮要素ならびに高段圧縮要素それぞれの圧縮室内への
潤滑油の供給が十分にでき、ピストンとシリンダー等の
摺動部の潤滑性が向上して信頼性を向上することができ
るという作用を有する。According to a third aspect of the present invention, there is provided a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, and a condenser connected to a discharge side of the high-stage compression element by piping. An intermediate-pressure expansion device pipe-connected to the outlet side of the condenser, an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element,
An intermediate-pressure evaporator pipe-connected between the intermediate-pressure expansion device and the intermediate-pressure suction pipe, and a low-pressure expansion device pipe-connected to the outlet side of the condenser or the outlet side of the intermediate-pressure expansion device, A low-pressure evaporator connected by piping between the low-pressure expansion device and a suction side of a low-stage compression element of the two-stage compressor, wherein a discharge side of the high-stage compression element is communicated with the closed vessel. Since the two evaporators of the freezing and refrigeration system have low and intermediate evaporating pressures, respectively, the evaporator temperatures should be suitable for the temperatures in the freezer and refrigerator compartments. As a result, the accuracy of temperature control in each of the refrigerators can be improved, and the temperature of each part in the refrigerator can be made uniform. In addition, since the evaporation temperature of the evaporator for the intermediate pressure can be set higher, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each refrigerator is not cooled with unnecessarily low temperature air. I do. Furthermore, since the discharge side of the high-stage compression element communicates with the inside of the closed vessel, the inside of the closed vessel becomes high pressure, and the pressure difference causes lubrication from the inside of the closed vessel to the compression chambers of the low-stage compression element and the high-stage compression element. It has an effect that the oil can be sufficiently supplied, the lubricating properties of the sliding parts such as the piston and the cylinder are improved, and the reliability can be improved.
【0027】請求項4に記載の発明は、請求項1あるい
は請求項2あるいは請求項3に記載の発明に、さらに、
低段圧縮要素の気筒容積VLと高段圧縮要素の気筒容積
VHの比VH/VLが0.5〜1.3の範囲に設定する
ように構成されたものであり、請求項1あるいは請求項
2あるいは請求項3に記載の発明の作用に加えて、高段
圧縮要素の気筒容積と低段圧縮要素の気筒容積の比率を
適正にすることにより、冷凍冷蔵装置の冷凍室と冷蔵室
などの異なる温度帯の庫内のどちらか一方が冷凍能力不
足になったり、冷凍能力過剰になること無く、各庫内を
適正に冷却でき、かつ高効率で消費電力を少なくすると
いう作用を有する。また、高圧、低圧、中間圧の各圧力
に応じた気筒容積の比率にすることにより、モータの最
大トルクとトルク変動を小さくすることができ、モータ
効率の向上と振動低減ができる。The invention described in claim 4 is the same as the invention described in claim 1, 2 or 3,
The ratio VH / VL of the cylinder volume VL of the low-stage compression element and the cylinder volume VH of the high-stage compression element is set to be in the range of 0.5 to 1.3, and is set forth in claim 1 or claim 2. In addition to the operation of the second or third aspect of the present invention, the ratio of the cylinder volume of the high-stage compression element to the cylinder volume of the low-stage compression element is made appropriate, so that the freezing room and the refrigerating room of the refrigerating and refrigerating device can be used. There is an effect that the inside of each refrigerator can be properly cooled, and the power consumption can be reduced with high efficiency, without any one of the refrigerators in different temperature zones becoming insufficient in refrigeration capacity or excessive in refrigeration capacity. Further, by setting the ratio of the cylinder volume to each of the high pressure, the low pressure, and the intermediate pressure, the maximum torque and the torque fluctuation of the motor can be reduced, and the motor efficiency can be improved and the vibration can be reduced.
【0028】請求項5に記載の発明は、中間圧用吸入パ
イプの密閉容器内への開口部が高段側圧縮要素の吸入側
にわずかな隙間を介して連通する構成としたものであ
り、請求項1に記載の発明の作用に加えて、中間圧用蒸
発器から中間圧用吸入パイプを通って密閉容器内に戻っ
てきた冷媒ガスは、わずかな隙間を介して高段圧縮要素
の吸入側に吸入されるため、各圧縮要素やモータからの
受熱の影響が小さく、温度上昇が小さく抑えられる。そ
のため、吸入される冷媒ガスの密度が大きくなり、冷媒
循環量が多くなると共に効率を向上することができる。
更に、中間圧用吸入パイプと高段圧縮要素の吸入側が直
接接続される場合に比べて、わずかな隙間があるために
高段圧縮要素からの圧力脈動は密閉容器内に拡散し、中
間圧用吸入パイプに伝わり難く、騒音が発生し難いとい
う作用を有する。According to a fifth aspect of the present invention, the opening of the intermediate-pressure suction pipe into the closed vessel communicates with the suction side of the high-stage compression element through a small gap. In addition to the function of the invention described in Item 1, the refrigerant gas returned from the intermediate pressure evaporator into the closed vessel through the intermediate pressure suction pipe is sucked into the suction side of the high-stage compression element through a small gap. Therefore, the influence of the heat received from each compression element and the motor is small, and the temperature rise is suppressed to a small level. Therefore, the density of the refrigerant gas to be taken in increases, and the amount of circulating refrigerant increases, and the efficiency can be improved.
Furthermore, compared with the case where the intermediate pressure suction pipe and the suction side of the high-stage compression element are directly connected, the pressure pulsation from the high-stage compression element diffuses into the closed vessel due to the slight gap, and the intermediate-pressure suction pipe It has an effect that it is hard to be transmitted to noise and noise is hardly generated.
【0029】[0029]
【実施例】以下、本発明による二段圧縮冷凍冷蔵装置の
実施例について、図面を参照しながら説明する。尚、従
来と同一構成については、同一符号を付して詳細な説明
を省略する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a two-stage compression refrigeration apparatus according to the present invention will be described below with reference to the drawings. The same components as those of the related art are denoted by the same reference numerals, and detailed description is omitted.
【0030】(実施例1)図1は本発明の実施例1によ
る二段圧縮冷凍冷蔵装置の冷媒回路図を示す。図2は同
実施例の二段圧縮冷凍冷蔵装置に使用する二段圧縮機の
平面断面図を示す。図3は同実施例の二段圧縮冷凍冷蔵
装置に使用する二段圧縮機の縦断面図を示す。図4は同
実施例の二段圧縮冷凍冷蔵装置における冷凍サイクルの
圧力−エンタルピ線図である。(Embodiment 1) FIG. 1 shows a refrigerant circuit diagram of a two-stage compression refrigeration apparatus according to Embodiment 1 of the present invention. FIG. 2 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment. FIG. 3 is a longitudinal sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment. FIG. 4 is a pressure-enthalpy diagram of a refrigeration cycle in the two-stage compression refrigeration apparatus of the embodiment.
【0031】図1、図2、図3、図4において、20は、
密閉容器21内にモーター22と低段圧縮要素23と高
段圧縮要素24とを備えた二段圧縮機である。25は高
段圧縮要素24の吐出側と配管接続した凝縮器であり、
26は凝縮器25の出口側と配管接続した中間圧用膨張
装置である。27は低段圧縮要素23の吐出側ならびに
高段圧縮要素24の吸入側と共に連通する中間圧用吸入
パイプであり、28は中間圧用膨張装置26と中間圧用
吸入パイプ27との間に配管接続された中間圧用蒸発器
である。29は凝縮器25の出口側と配管接続した低圧
用膨張装置であり、30は低圧用膨張装置29と二段圧
縮機20の低段圧縮要素23の吸入側との間に配管接続
された低圧用蒸発器である。低段圧縮要素23の吐出側
と高段圧縮要素24の吸入側は密閉容器21内に連通し
ている。In FIG. 1, FIG. 2, FIG. 3, and FIG.
This is a two-stage compressor including a motor 22, a low-stage compression element 23, and a high-stage compression element 24 in a closed container 21. 25 is a condenser connected to the discharge side of the high-stage compression element 24 by piping.
Reference numeral 26 denotes an intermediate pressure expansion device connected to the outlet side of the condenser 25 by piping. Reference numeral 27 denotes an intermediate pressure suction pipe which communicates with the discharge side of the low-stage compression element 23 and the suction side of the high-stage compression element 24, and 28 is connected between the intermediate-pressure expansion device 26 and the intermediate-pressure suction pipe 27. It is an intermediate pressure evaporator. Reference numeral 29 denotes a low-pressure expansion device connected to the outlet side of the condenser 25 by piping, and reference numeral 30 denotes a low-pressure expansion device connected by piping between the low-pressure expansion device 29 and the suction side of the low-stage compression element 23 of the two-stage compressor 20. Evaporator. The discharge side of the low-stage compression element 23 and the suction side of the high-stage compression element 24 communicate with each other in the closed casing 21.
【0032】低段圧縮要素23は、シリンダー31、ピ
ストン32、コンロッド33、吸入マフラー34、吐出
マフラー35等からなり、高段圧縮要素24も同様にシ
リンダー36、ピストン37、コンロッド38、吸入マ
フラー39、吐出マフラー40等からなる。モーター2
2は、クランクシャフト41に固定されたローター4
2、ステーター43により構成されている。クランクシ
ャフト41は偏心部41aを有し、偏心部41aとピス
トン32、37はそれぞれコンロッド33、38により
連結されている。42は密閉容器21に固定され、吸入
マフラー34と低圧用蒸発器30を連通する低圧用吸入
パイプである。43は密閉容器21に固定された吐出パ
イプであり、一端が吐出管44を介して吐出マフラー4
0に連通し、他端が配管を介して凝縮器25に連通して
いる。45は潤滑油で、密閉容器21の下部に貯溜して
いる。The low-stage compression element 23 includes a cylinder 31, a piston 32, a connecting rod 33, a suction muffler 34, a discharge muffler 35, and the like. The high-stage compression element 24 similarly has a cylinder 36, a piston 37, a connecting rod 38, and a suction muffler 39. , A discharge muffler 40 and the like. Motor 2
2 is a rotor 4 fixed to the crankshaft 41
2. It is composed of the stator 43. The crankshaft 41 has an eccentric portion 41a, and the eccentric portion 41a and the pistons 32 and 37 are connected by connecting rods 33 and 38, respectively. Reference numeral 42 denotes a low-pressure suction pipe that is fixed to the closed container 21 and communicates the suction muffler 34 and the low-pressure evaporator 30. Reference numeral 43 denotes a discharge pipe fixed to the closed container 21, one end of which is connected to the discharge muffler 4 through a discharge pipe 44.
0, and the other end is connected to the condenser 25 via a pipe. Reference numeral 45 denotes a lubricating oil, which is stored in a lower part of the closed container 21.
【0033】以上のように構成された密閉型圧縮機につ
いて、以下その動作を説明する。The operation of the hermetic compressor constructed as described above will be described below.
【0034】モーター22によってクランクシャフト4
1が回転すると、コンロッド33、38によりピストン
32、37はそれぞれシリンダー31、36内を往復運
動する。そして、低段圧縮要素23は、低圧用蒸発器3
0から低圧用吸入パイプ42、吸入マフラー34を介し
てシリンダー31内に冷媒ガスを吸入した後、中間圧ま
で圧縮して吐出マフラー35を介して密閉容器21内に
吐出する。吐出マフラー35から吐出された冷媒ガス
は、中間圧用吸入パイプ27から密閉容器21内に流入
する冷媒ガスと混合して、高段圧縮要素24の吸入マフ
ラー39からシリンダー36内に吸入され、再び圧縮さ
れる。高段圧縮要素24で圧縮された冷媒ガスは、吐出
マフラー40、吐出管44、吐出パイプ43を通って凝
縮器25に送られる。凝縮器25で冷媒ガスは放熱して
凝縮されて液冷媒になった後、2つの流路に分かれる。
一方は、中間圧用膨張装置26に流れて減圧され、中間
圧用蒸発器28に流入して蒸発する。このときに周囲か
ら熱を奪うことによって中間圧用蒸発器28は冷却作用
を発揮する。そして、中間圧用蒸発器28を出た冷媒ガ
スは中間圧用吸入パイプ27を経て二段圧縮機1に帰還
する。The motor 22 causes the crankshaft 4
When 1 rotates, the pistons 32 and 37 reciprocate in the cylinders 31 and 36 by the connecting rods 33 and 38, respectively. The low-stage compression element 23 is provided with the low-pressure evaporator 3.
After sucking the refrigerant gas into the cylinder 31 from 0 through the low-pressure suction pipe 42 and the suction muffler 34, the refrigerant gas is compressed to an intermediate pressure and discharged into the closed container 21 through the discharge muffler 35. The refrigerant gas discharged from the discharge muffler 35 is mixed with the refrigerant gas flowing into the closed vessel 21 from the intermediate pressure suction pipe 27, and is sucked into the cylinder 36 from the suction muffler 39 of the high-stage compression element 24, and compressed again. Is done. The refrigerant gas compressed by the high-stage compression element 24 is sent to the condenser 25 through the discharge muffler 40, the discharge pipe 44, and the discharge pipe 43. The refrigerant gas radiates heat in the condenser 25 to be condensed into a liquid refrigerant, and then splits into two flow paths.
One of them flows into the intermediate pressure expansion device 26 and is decompressed, and then flows into the intermediate pressure evaporator 28 and evaporates. At this time, by removing heat from the surroundings, the intermediate-pressure evaporator 28 exhibits a cooling action. Then, the refrigerant gas that has exited the intermediate-pressure evaporator 28 returns to the two-stage compressor 1 through the intermediate-pressure suction pipe 27.
【0035】凝縮器25からの他方の液冷媒は、低圧用
膨張装置29に流れて減圧され、低圧用蒸発器30に流
入して蒸発する。このときに周囲から熱を奪うことによ
って低圧用蒸発器28は冷却作用を発揮する。そして、
低圧用蒸発器30を出た冷媒ガスは低圧用吸入パイプ4
2を経て二段圧縮機1に帰還し、再び低段圧縮要素23
に吸入される。The other liquid refrigerant from the condenser 25 flows into the low-pressure expansion device 29 to be decompressed, flows into the low-pressure evaporator 30, and evaporates. At this time, the low-pressure evaporator 28 exerts a cooling action by removing heat from the surroundings. And
The refrigerant gas exiting the low-pressure evaporator 30 is supplied to the low-pressure suction pipe 4.
2 and returns to the two-stage compressor 1, and again the low-stage compression element 23
Inhaled.
【0036】また、潤滑油45はクランクシャフト41
の下端部から遠心力によって吸い上げられ、クランクシ
ャフト41の各摺動部を潤滑した後、偏心部41aの上
端部から遠心力によって飛散して、ピストン32、37
とシリンダー31、36の摺動部やコンロッド33、3
8の摺動部を潤滑する。The lubricating oil 45 is supplied to the crankshaft 41.
After being lifted up by the centrifugal force from the lower end of the eccentric part 41a and lubricating each sliding part of the crankshaft 41, it is scattered by the centrifugal force from the upper end of the eccentric part 41a, and the pistons 32, 37
And the sliding parts of the cylinders 31 and 36 and the connecting rods 33 and 3
8 are lubricated.
【0037】本実施例の冷凍サイクルは図4に示される
ように、中間圧用蒸発器28内の冷媒は中間圧に、低圧
用蒸発器30内の冷媒は低圧になる。この冷凍サイクル
を冷凍冷蔵装置に適用する場合、中間圧用蒸発器28を
冷蔵用に使用し、低圧用蒸発器30を冷凍用に使用す
る。そのため、冷凍室と冷蔵室等の各庫内温度に適した
蒸発器温度にそれぞれすることができる。例えば、冷蔵
室の温度を3℃〜7℃、冷凍室の温度を−18℃〜−2
2℃に設定する場合には、中間圧用蒸発器28の蒸発温
度を0℃〜−10℃程度に、低圧用蒸発器30の蒸発温
度を−25℃〜−35℃程度に設定することができ、各
庫内の温度と蒸発温度の差が小さいため、各庫内の温度
制御の精度が高くなると共に庫内各部の温度の均一化が
図れる。また、特に中間圧用蒸発器28の蒸発温度を高
く設定できることから、二段圧縮機20の効率が向上す
ると共に、各庫内を必要以上に温度の低い冷気で冷却す
ることが無いため冷凍サイクル全体の効率が向上する。In the refrigeration cycle of this embodiment, as shown in FIG. 4, the refrigerant in the intermediate-pressure evaporator 28 has an intermediate pressure, and the refrigerant in the low-pressure evaporator 30 has a low pressure. When this refrigeration cycle is applied to a refrigeration apparatus, the intermediate-pressure evaporator 28 is used for refrigeration, and the low-pressure evaporator 30 is used for refrigeration. Therefore, the temperature of the evaporator can be adjusted to the temperature in each of the freezer compartment and the refrigerator compartment. For example, the temperature of the refrigerator compartment is 3 ° C. to 7 ° C., and the temperature of the freezer compartment is −18 ° C. to −2.
When set to 2 ° C., the evaporation temperature of the intermediate pressure evaporator 28 can be set to about 0 ° C. to −10 ° C., and the evaporation temperature of the low pressure evaporator 30 can be set to about −25 ° C. to −35 ° C. Since the difference between the temperature in each storage and the evaporation temperature is small, the accuracy of temperature control in each storage is improved and the temperature of each part in the storage can be made uniform. In addition, since the evaporation temperature of the intermediate-pressure evaporator 28 can be set particularly high, the efficiency of the two-stage compressor 20 is improved, and the interior of each refrigerator is not cooled with unnecessarily low temperature cool air. Efficiency is improved.
【0038】更に、低段圧縮要素23の吐出側と高段圧
縮要素24の吸入側とが密閉容器20内に連通している
ため、密閉容器20内が中間圧力になり、低段圧縮要素
23ならびに高段圧縮要素24のそれぞれのシリンダー
31、36内と密閉容器21内との圧力差が小さく、各
圧縮要素と密閉容器21内の間での冷媒ガスの漏れ量を
少なくすることができ、二段圧縮機20の冷凍能力、な
らびに効率を向上することができる。Further, since the discharge side of the low-stage compression element 23 and the suction side of the high-stage compression element 24 communicate with each other in the closed container 20, the pressure in the closed container 20 becomes an intermediate pressure, and the low-stage compression element 23 In addition, the pressure difference between the inside of each of the cylinders 31 and 36 of the high-stage compression element 24 and the inside of the closed vessel 21 is small, and the amount of refrigerant gas leakage between each compression element and the inside of the closed vessel 21 can be reduced. The refrigeration capacity and efficiency of the two-stage compressor 20 can be improved.
【0039】以上のように本実施例の二段圧縮冷凍冷蔵
装置は、密閉容器21内にモーター22と低段圧縮要素
23と高段圧縮要素24とを備えた二段圧縮機20と、
高段圧縮要素24の吐出側と配管接続した凝縮器25
と、凝縮器25の出口側と配管接続した中間圧用膨張装
置26と、低段圧縮要素23の吐出側ならびに高段圧縮
要素24の吸入側と共に連通する中間圧用吸入パイプ2
7と、中間圧用膨張装置26と中間圧用吸入パイプ27
との間に配管接続された中間圧用蒸発器28と、凝縮器
25の出口側あるいは中間圧用膨張装置26の出口側と
配管接続した低圧用膨張装置29と、低圧用膨張装置2
9と二段圧縮機20の低段圧縮要素23の吸入側との間
に配管接続された低圧用蒸発器30とからなり、低段圧
縮要素23の吐出側と高段圧縮要素24の吸入側とが密
閉容器21内に連通した構成となっているので、各庫内
の温度制御の精度を高めると共に庫内各部の温度の均一
化が図れ、更に高効率で消費電力が少ない二段圧縮冷凍
冷蔵装置とすることができる。As described above, the two-stage compression refrigeration apparatus of the present embodiment comprises a two-stage compressor 20 having a motor 22, a low-stage compression element 23, and a high-stage compression element 24 in a closed container 21,
Condenser 25 connected to the discharge side of high-stage compression element 24 by piping
And an intermediate-pressure expansion device 26 connected to the outlet side of the condenser 25 by piping, and an intermediate-pressure suction pipe 2 communicating with the discharge side of the low-stage compression element 23 and the suction side of the high-stage compression element 24.
7, intermediate pressure expansion device 26 and intermediate pressure suction pipe 27
, A low-pressure expansion device 29 connected to the outlet of the condenser 25 or the outlet of the intermediate-pressure expansion device 26, and a low-pressure expansion device 2.
9 and a low-pressure evaporator 30 connected by piping between the two-stage compressor 20 and the suction side of the low-stage compression element 23. The discharge side of the low-stage compression element 23 and the suction side of the high-stage compression element 24. Are communicated with the inside of the closed container 21, so that the accuracy of temperature control in each refrigerator can be improved, the temperature of each part in the refrigerator can be made uniform, and the two-stage compression refrigeration with high efficiency and low power consumption can be achieved. It can be a refrigerator.
【0040】(実施例2)図5は本発明の実施例2によ
る二段圧縮冷凍冷蔵装置の冷媒回路図を示す。図6は同
実施例の二段圧縮冷凍冷蔵装置に使用する二段圧縮機の
平面断面図を示す。(Embodiment 2) FIG. 5 is a refrigerant circuit diagram of a two-stage compression refrigeration apparatus according to Embodiment 2 of the present invention. FIG. 6 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【0041】以下、図面を参照しながら説明するが、実
施例1と同一構成については、同一符号を付して詳細な
説明を省略する。 図5、図6において、46は、低段
圧縮要素47と高段圧縮要素48とを備えた二段圧縮機
である。49は低段圧縮要素47の吐出側ならびに高段
圧縮要素48の吸入側と共に連通する中間圧用吸入パイ
プである。50は密閉容器21に固定された低圧用吸入
パイプであり、低圧用蒸発器30と密閉容器21内を連
通している。また、低段圧縮要素47の吸入側は吸入マ
フラー51から密閉容器21内に連通している。52は
高段圧縮要素48の吸入マフラーであり、中間圧用吸入
パイプ49と連通している。53は吐出マフラー54と
吸入マフラー52を連通する連通管である。Hereinafter, description will be made with reference to the drawings, but the same components as those in the first embodiment are denoted by the same reference numerals, and detailed description thereof will be omitted. 5 and 6, reference numeral 46 denotes a two-stage compressor including a low-stage compression element 47 and a high-stage compression element 48. Reference numeral 49 denotes an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element 47 and the suction side of the high-stage compression element 48. Reference numeral 50 denotes a low-pressure suction pipe fixed to the closed container 21, and communicates the low-pressure evaporator 30 with the inside of the closed container 21. Further, the suction side of the low-stage compression element 47 communicates from the suction muffler 51 into the closed container 21. Reference numeral 52 denotes a suction muffler for the high-stage compression element 48, which communicates with a suction pipe 49 for intermediate pressure. A communication pipe 53 communicates the discharge muffler 54 and the suction muffler 52.
【0042】以上のように構成された二段圧縮冷凍冷蔵
装置について、以下その動作を説明する。The operation of the two-stage compression refrigerating and refrigerating apparatus configured as described above will be described below.
【0043】二段圧縮機46の内部構成以外は実施例1
と同じなので、本冷凍サイクルによる効果は実施例1と
ほぼ同様に得られる。すなわち、各庫内の温度制御の精
度を高めると共に庫内各部の温度の均一化が図れ、更に
高効率で消費電力を少なくすることができる。Embodiment 1 Except for the internal structure of the two-stage compressor 46
Therefore, the effect of the present refrigeration cycle can be obtained almost in the same manner as in the first embodiment. That is, it is possible to improve the accuracy of the temperature control in each of the refrigerators, to make the temperature of each part in the refrigerator uniform, and to further reduce power consumption with higher efficiency.
【0044】本実施例では、低段圧縮要素47の吸入側
が密閉容器21内に連通しているため、密閉容器21内
が低圧になり、低圧用蒸発器30から戻ってくる温度の
低い冷媒ガスで密閉容器21内の低段圧縮要素47、高
段圧縮要素48やモータ22を冷却できるので、各圧縮
要素47、48の過熱を防止でき信頼性が向上すると共
に、モータ22の温度低下によりモータ効率を向上する
ことができる。In this embodiment, since the suction side of the low-stage compression element 47 communicates with the inside of the closed vessel 21, the inside of the closed vessel 21 has a low pressure and the low-temperature refrigerant gas returning from the low-pressure evaporator 30. Can cool the low-stage compression element 47, the high-stage compression element 48, and the motor 22 in the closed container 21, so that the overheating of each compression element 47, 48 can be prevented, and the reliability is improved. Efficiency can be improved.
【0045】以上のように本実施例の二段圧縮冷凍冷蔵
装置は、密閉容器21内にモーター22と低段圧縮要素
47と高段圧縮要素48とを備えた二段圧縮機46と、
高段圧縮要素48の吐出側と配管接続した凝縮器28
と、凝縮器28の出口側と配管接続した中間圧用膨張装
置26と、低段圧縮要素47の吐出側ならびに高段圧縮
要素48の吸入側と共に連通する中間圧用吸入パイプ4
9と、中間圧用膨張装置26と中間圧用吸入パイプ49
との間に配管接続された中間圧用蒸発器28と、凝縮器
25の出口側あるいは中間圧用膨張装置26の出口側と
配管接続した低圧用膨張装置29と、低圧用膨張装置2
9と二段圧縮機46の低段圧縮要素47の吸入側との間
に配管接続された低圧用蒸発器30とからなり、低段圧
縮要素47の吸入側が密閉容器21内に連通した構成と
なっているので、各庫内の温度制御の精度を高めると共
に庫内各部の温度の均一化が図れ、更に高効率で消費電
力を少なくすることができ、更に二段圧縮機46の信頼
性を向上させ、モータ効率を向上することができる。As described above, the two-stage compression refrigeration apparatus of the present embodiment comprises a two-stage compressor 46 having the motor 22, the low-stage compression element 47 and the high-stage compression element 48 in the closed container 21,
Condenser 28 connected by piping to the discharge side of high-stage compression element 48
An intermediate-pressure expansion device 26 connected to the outlet side of the condenser 28 via a pipe, and an intermediate-pressure suction pipe 4 communicating with the discharge side of the low-stage compression element 47 and the suction side of the high-stage compression element 48.
9, intermediate pressure expansion device 26 and intermediate pressure suction pipe 49
, A low-pressure expansion device 29 connected to the outlet of the condenser 25 or the outlet of the intermediate-pressure expansion device 26, and a low-pressure expansion device 2.
9 and a low-pressure evaporator 30 connected to the suction side of the low-stage compression element 47 of the two-stage compressor 46 by piping. The suction side of the low-stage compression element 47 communicates with the closed vessel 21. Therefore, the accuracy of the temperature control in each of the refrigerators can be improved, the temperature in each of the refrigerators can be made uniform, the power consumption can be reduced with higher efficiency, and the reliability of the two-stage compressor 46 can be further improved. And motor efficiency can be improved.
【0046】(実施例3)図7は本発明の実施例3によ
る二段圧縮冷凍冷蔵装置の冷媒回路図を示す。図8は同
実施例の二段圧縮冷凍冷蔵装置に使用する二段圧縮機の
平面断面図を示す。(Embodiment 3) FIG. 7 shows a refrigerant circuit diagram of a two-stage compression refrigeration apparatus according to Embodiment 3 of the present invention. FIG. 8 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【0047】以下、図面を参照しながら説明するが、実
施例1と同一構成については、同一符号を付して詳細な
説明を省略する。図8、図9において、55は、低段圧
縮要素56と高段圧縮要素57とを備えた二段圧縮機で
ある。58は低段圧縮要素56の吐出側ならびに高段圧
縮要素57の吸入側と共に連通する中間圧用吸入パイプ
である。59は高段圧縮要素57の吸入マフラーであ
り、中間圧用吸入パイプ58と連通している。60は吐
出マフラー61と吸入マフラー59を連通する連通管で
ある。62は密閉容器21に固定された吐出パイプであ
り、一端が密閉容器21内に連通し、他端が配管を介し
て凝縮器25に連通している。また、高段圧縮要素57
の吐出側は吐出マフラー63から密閉容器21内に連通
している。Hereinafter, description will be made with reference to the drawings. However, the same components as those in the first embodiment are denoted by the same reference numerals, and detailed description is omitted. 8 and 9, reference numeral 55 denotes a two-stage compressor including a low-stage compression element 56 and a high-stage compression element 57. Reference numeral 58 denotes an intermediate-pressure suction pipe that communicates with the discharge side of the low-stage compression element 56 and the suction side of the high-stage compression element 57. Reference numeral 59 denotes a suction muffler for the high-stage compression element 57, which communicates with the suction pipe 58 for intermediate pressure. Reference numeral 60 denotes a communication pipe that connects the discharge muffler 61 and the suction muffler 59. Reference numeral 62 denotes a discharge pipe fixed to the closed container 21, one end of which is connected to the inside of the closed container 21, and the other end of which is connected to the condenser 25 via a pipe. Also, the high-stage compression element 57
Is communicated from the discharge muffler 63 into the closed container 21.
【0048】以上のように構成された二段圧縮冷凍冷蔵
装置について、以下その動作を説明する。The operation of the two-stage compression refrigerating / refrigerating apparatus configured as described above will be described below.
【0049】二段圧縮機55の内部構成以外は実施例1
と同じなので、本冷凍サイクルによる効果は実施例1と
ほぼ同様に得られる。すなわち、各庫内の温度制御の精
度を高めると共に庫内各部の温度の均一化が図れ、更に
高効率で消費電力を少なくすることができる。Embodiment 1 Except for the internal structure of the two-stage compressor 55,
Therefore, the effect of the present refrigeration cycle can be obtained almost in the same manner as in the first embodiment. That is, it is possible to improve the accuracy of the temperature control in each of the refrigerators, to make the temperature of each part in the refrigerator uniform, and to further reduce power consumption with higher efficiency.
【0050】本実施例では、高段圧縮要素57の吐出側
が密閉容器21内に連通しているため、密閉容器21内
が高圧になり、密閉容器21内の圧力がシリンダー3
1、36内の圧力よりも高くなる。そのため、クランク
シャフト41の偏心部41aからシリンダー31、36
部に飛散した潤滑油45は、圧力差によりシリンダー3
1、36とピストン32、37のそれぞれの隙間に流入
して、ピストン32、37とシリンダー31、36等の
摺動部の潤滑性が向上して信頼性を向上することができ
る。In this embodiment, since the discharge side of the high-stage compression element 57 communicates with the inside of the closed vessel 21, the pressure inside the closed vessel 21 becomes high, and
It becomes higher than the pressure in 1,36. Therefore, the cylinders 31 and 36 are moved from the eccentric portion 41a of the crankshaft 41.
The lubricating oil 45 scattered on the cylinder 3
The lubrication of the sliding parts such as the pistons 32 and 37 and the cylinders 31 and 36 can be improved by flowing into the gaps between the pistons 1 and 36 and the pistons 32 and 37, and the reliability can be improved.
【0051】以上のように本実施例の二段圧縮冷凍冷蔵
装置は、密閉容器21内にモーター22と低段圧縮要素
56と高段圧縮要素57とを備えた二段圧縮機55と、
高段圧縮要素57の吐出側と配管接続した凝縮器25
と、凝縮器25の出口側と配管接続した中間圧用膨張装
置26と、低段圧縮要素56の吐出側ならびに高段圧縮
要素57の吸入側と共に連通する中間圧用吸入パイプ5
8と、中間圧用膨張装置26と中間圧用吸入パイプ58
との間に配管接続された中間圧用蒸発器28と、凝縮器
25の出口側あるいは中間圧用膨張装置26の出口側と
配管接続した低圧用膨張装置29と、低圧用膨張装置2
9と二段圧縮機55の低段圧縮要素56の吸入側との間
に配管接続された低圧用蒸発器30とからなり、高段圧
縮要素57の吐出側が密閉容器21内に連通した構成と
なっているので、各庫内の温度制御の精度を高めると共
に庫内各部の温度の均一化が図れ、更に高効率で消費電
力を少なくすることができ、更に圧力差により密閉容器
21内から低段圧縮要素56ならびに高段圧縮要素57
それぞれのシリンダー31、36内への潤滑油45の供
給が十分にでき、ピストン32、37とシリンダー3
1、36等の摺動部の潤滑性が向上して信頼性を向上す
ることができる。As described above, the two-stage compression refrigeration apparatus of the present embodiment comprises a two-stage compressor 55 having the motor 22, the low-stage compression element 56 and the high-stage compression element 57 in the closed container 21,
Condenser 25 connected to the discharge side of high-stage compression element 57 by piping
An intermediate-pressure expansion device 26 connected to the outlet side of the condenser 25 with a pipe, and an intermediate-pressure suction pipe 5 communicating with the discharge side of the low-stage compression element 56 and the suction side of the high-stage compression element 57.
8, intermediate pressure expansion device 26 and intermediate pressure suction pipe 58
, A low-pressure expansion device 29 connected to the outlet of the condenser 25 or the outlet of the intermediate-pressure expansion device 26, and a low-pressure expansion device 2.
9 and a low-pressure evaporator 30 connected to the suction side of the low-stage compression element 56 of the two-stage compressor 55, wherein the discharge side of the high-stage compression element 57 communicates with the closed vessel 21. As a result, the accuracy of the temperature control in each of the refrigerators can be improved, and the temperature of each part in the refrigerator can be made uniform, and the power consumption can be reduced with higher efficiency. Stage compression element 56 and high stage compression element 57
The lubricating oil 45 can be sufficiently supplied into the respective cylinders 31 and 36, and the pistons 32 and 37 and the cylinder 3
The lubricating properties of the sliding portions such as 1 and 36 are improved, and the reliability can be improved.
【0052】(実施例4)図9は本発明の実施例4によ
る二段圧縮冷凍冷蔵装置に使用する二段圧縮機の縦断面
図を示す。(Embodiment 4) FIG. 9 is a longitudinal sectional view of a two-stage compressor used in a two-stage compression refrigeration apparatus according to a fourth embodiment of the present invention.
【0053】以下、図面を参照しながら説明するが、実
施例1あるいは実施例2あるいは実施例3と同一構成に
ついては、同一符号を付して詳細な説明を省略する。
図9において、64は、低段圧縮要素65と高段圧縮要
素66とを備えた二段圧縮機である。低段圧縮要素65
は、シリンダー66、ピストン67、コンロッド68、
吸入マフラー34、吐出マフラー35等からなり、高段
圧縮要素66も同様にシリンダー69、ピストン70、
コンロッド71、吸入マフラー39、吐出マフラー40
等からなる。低段圧縮要素65の気筒容積VLと高段圧
縮要素66の気筒容積VHの比VH/VLは0.5〜
1.3の範囲に設定されている。Hereinafter, description will be made with reference to the drawings. However, the same components as those in the first, second, or third embodiment will be denoted by the same reference numerals, and detailed description will be omitted.
In FIG. 9, reference numeral 64 denotes a two-stage compressor including a low-stage compression element 65 and a high-stage compression element 66. Low stage compression element 65
Is a cylinder 66, a piston 67, a connecting rod 68,
The high-stage compression element 66 includes a cylinder 69, a piston 70, a suction muffler 34, a discharge muffler 35, and the like.
Connecting rod 71, suction muffler 39, discharge muffler 40
Etc. The ratio VH / VL of the cylinder volume VL of the low-stage compression element 65 to the cylinder volume VH of the high-stage compression element 66 is 0.5 to
It is set in the range of 1.3.
【0054】以上のように構成された二段圧縮冷凍冷蔵
装置について、以下その動作を説明する。The operation of the two-stage compression refrigerating and refrigerating apparatus configured as described above will be described below.
【0055】二段圧縮機64の気筒容積の比VH/VL
以外は実施例1あるいは実施例2あるいは実施例3と同
じなので、本冷凍サイクルによる効果は実施例1あるい
は実施例2あるいは実施例3とほぼ同様に得られる。す
なわち、各庫内の温度制御の精度を高めると共に庫内各
部の温度の均一化が図れ、更に高効率で消費電力が少な
く、また信頼性を高くすることができる。The cylinder volume ratio VH / VL of the two-stage compressor 64
Except for the above, the present refrigeration cycle has substantially the same effects as those of the first, second, or third embodiment. That is, it is possible to improve the accuracy of temperature control in each of the refrigerators and to make the temperature of each part in the refrigerator uniform, to achieve higher efficiency, lower power consumption, and to increase reliability.
【0056】本実施例では、低段圧縮要素65の気筒容
積VLと高段圧縮要素69の気筒容積VHの比VH/V
Lは0.5〜1.3の範囲に設定しており、その効果を
以下に説明する。In the present embodiment, the ratio VH / V of the cylinder volume VL of the low-stage compression element 65 to the cylinder volume VH of the high-stage compression element 69
L is set in the range of 0.5 to 1.3, and the effect will be described below.
【0057】一般に冷凍冷蔵庫は、冷凍室の庫内容積に
対する冷蔵室の庫内容積の比率は、1.5〜4.0程度
になり冷蔵室の方が大きいが、冷凍室の方をより低温に
することから必要な冷凍能力はこの比率より小さくな
る。そのため、冷凍室の必要冷凍能力に対する冷蔵室の
必要冷凍能力の比は、0.5〜1.1程度になる。Generally, in a refrigerator, the ratio of the internal volume of the refrigerator to the internal volume of the freezer is about 1.5 to 4.0, which is larger in the refrigerator. , The required refrigerating capacity is smaller than this ratio. Therefore, the ratio of the required refrigerating capacity of the refrigerator to the required refrigerating capacity of the freezer is about 0.5 to 1.1.
【0058】例えば、パーシャル室等を含めた冷蔵室の
温度を−5℃〜7℃、冷凍室の温度を−22℃〜−18
℃に設定する場合には、中間圧用蒸発器28の蒸発温度
を−20℃〜0℃程度に、低圧用蒸発器30の蒸発温度
を−35℃〜−25℃程度に設定する。これらの蒸発温
度のときに、冷凍室と冷蔵室との冷凍能力の比率を前記
した0.5〜1.1にする場合には、発明者の検討によ
れば、低段圧縮要素65の気筒容積VLと高段圧縮要素
69の気筒容積VHの比VH/VLは0.5〜1.3に
すれば良いことが計算と実験から分かっている。For example, the temperature of the refrigerating compartment including the partial compartment is -5 ° C. to 7 ° C., and the temperature of the freezing compartment is -22 ° C. to -18.
When the temperature is set to ° C., the evaporation temperature of the intermediate pressure evaporator 28 is set to about −20 ° C. to 0 ° C., and the evaporation temperature of the low pressure evaporator 30 is set to about −35 ° C. to −25 ° C. When the ratio of the refrigerating capacity between the freezing compartment and the refrigerating compartment is set to 0.5 to 1.1 at these evaporation temperatures, according to the study of the inventor, the cylinder of the low-stage compression element 65 It is known from calculations and experiments that the ratio VH / VL between the volume VL and the cylinder volume VH of the high-stage compression element 69 should be set to 0.5 to 1.3.
【0059】VH/VLの値が小さ過ぎると、高段圧縮
側の冷媒循環量が減少し、中間圧用蒸発器28の冷凍能
力が小さくなって、冷蔵室の庫内温度が上昇する等の悪
影響が現れる。一方、VH/VLの値が大き過ぎると、
低段圧縮側の冷媒循環量が減少し、低圧用蒸発器30の
冷凍能力が小さくなって、冷凍室の庫内温度が上昇する
等の悪影響が現れる。If the value of VH / VL is too small, the amount of circulating refrigerant on the high-stage compression side decreases, the refrigerating capacity of the intermediate-pressure evaporator 28 decreases, and the temperature inside the refrigerator compartment rises. Appears. On the other hand, if the value of VH / VL is too large,
The amount of circulating refrigerant on the low-stage compression side is reduced, the refrigeration capacity of the low-pressure evaporator 30 is reduced, and adverse effects such as an increase in the temperature of the freezer compartment appear.
【0060】従って、高段圧縮要素66の気筒容積と低
段圧縮要素64の気筒容積の比率を適正にすることによ
り、冷凍冷蔵装置の冷凍室と冷蔵室などの異なる温度帯
の庫内のどちらか一方が冷凍能力不足になったり、冷凍
能力過剰になること無く、各庫内を適正に冷却でき、か
つ高効率で消費電力を少なくすることができる。Therefore, by making the ratio of the cylinder capacity of the high-stage compression element 66 to the cylinder volume of the low-stage compression element 64 appropriate, it is possible to use either the freezer compartment of the freezing and refrigeration system or the refrigerator compartment of a different temperature zone. It is possible to appropriately cool the inside of each refrigerator, to reduce the power consumption with high efficiency, without causing the refrigeration capacity to be insufficient or the refrigeration capacity to be excessive.
【0061】更に、圧縮機運転中において、高圧と中間
圧の差圧が中間圧と低圧の差圧より大きい場合は、高段
圧縮要素66の気筒容積を低段圧縮要素64の気筒容積
より小さくすることにより、高段圧縮要素66の圧縮に
必要なトルクと低段圧縮要素64の圧縮に必要なトルク
の差が小さくなり、モータ22の最大トルクとトルク変
動を小さくすることができ、モータ効率の向上と振動低
減ができる。この場合、各気筒容積の調整はピストン6
7、70の外径の変更により行う。また、逆に高圧と中
間圧の差圧が中間圧と低圧の差圧より小さい場合は、高
段圧縮要素66の気筒容積を低段圧縮要素64の気筒容
積より大きくすることにより、同様の効果が得られる。Further, when the differential pressure between the high pressure and the intermediate pressure is larger than the differential pressure between the intermediate pressure and the low pressure during the operation of the compressor, the cylinder volume of the high-stage compression element 66 is made smaller than the cylinder volume of the low-stage compression element 64. By doing so, the difference between the torque required to compress the high-stage compression element 66 and the torque required to compress the low-stage compression element 64 is reduced, and the maximum torque and torque fluctuation of the motor 22 can be reduced. And vibration can be reduced. In this case, adjustment of each cylinder volume is performed by the piston 6
This is performed by changing the outer diameter of 7, 70. On the other hand, when the differential pressure between the high pressure and the intermediate pressure is smaller than the differential pressure between the intermediate pressure and the low pressure, the same effect can be obtained by making the cylinder volume of the high-stage compression element 66 larger than the cylinder volume of the low-stage compression element 64. Is obtained.
【0062】以上のように本実施例の二段圧縮冷凍冷蔵
装置は、低段圧縮要素65の気筒容積VLと高段圧縮要
素66の気筒容積VHの比VH/VLが0.5〜1.3
の範囲に設定された構成となっているので、実施例1あ
るいは実施例2あるいは実施例3の効果に加えて、冷凍
冷蔵装置の冷凍室と冷蔵室などの異なる温度帯の庫内の
どちらか一方が冷凍能力不足になったり、冷凍能力過剰
になること無く、各庫内を適正に冷却でき、かつ高効率
で消費電力を少なくすることができる。また、高圧、低
圧、中間圧の各圧力に応じた気筒容積の比率にすること
により、モータ22の最大トルクとトルク変動を小さく
することができ、モータ効率の向上と振動低減ができ
る。As described above, in the two-stage compression refrigeration apparatus of this embodiment, the ratio VH / VL of the cylinder volume VL of the low-stage compression element 65 to the cylinder volume VH of the high-stage compression element 66 is 0.5-1. 3
, And in addition to the effects of the first or second or third embodiment, either the inside of the freezer compartment of the freezing and refrigeration apparatus and the refrigerator compartment of a different temperature zone, such as the refrigerating compartment. It is possible to appropriately cool the interiors of each refrigerator, to reduce the power consumption with high efficiency, without one of the refrigeration capacity becoming insufficient or the refrigeration capacity becoming excessive. Further, by setting the cylinder volume ratio according to each of the high pressure, the low pressure, and the intermediate pressure, the maximum torque and the torque fluctuation of the motor 22 can be reduced, and the motor efficiency can be improved and the vibration can be reduced.
【0063】(実施例5)図10は本発明の実施例5に
よる二段圧縮冷凍冷蔵装置に使用する二段圧縮機の平面
断面図を示す。(Embodiment 5) FIG. 10 is a plan sectional view of a two-stage compressor used in a two-stage compression refrigeration apparatus according to a fifth embodiment of the present invention.
【0064】以下、図面を参照しながら説明するが、実
施例1と同一構成については、同一符号を付して詳細な
説明を省略する。 図10において、72は、低段圧縮
要素23と高段圧縮要素73とを備えた二段圧縮機であ
る。74は低段圧縮要素23の吐出側ならびに高段圧縮
要素73の吸入側と共に連通する中間圧用吸入パイプで
ある。75は高段圧縮要素73の吸入マフラーである。
中間圧用吸入パイプ74の密閉容器21内への開口部が
高段側圧縮要素73の吸入マフラー75にわずかな隙間
を介して連通している。Hereinafter, description will be made with reference to the drawings. However, the same components as those in the first embodiment are denoted by the same reference numerals, and detailed description thereof will be omitted. In FIG. 10, reference numeral 72 denotes a two-stage compressor including a low-stage compression element 23 and a high-stage compression element 73. An intermediate pressure suction pipe 74 communicates with the discharge side of the low stage compression element 23 and the suction side of the high stage compression element 73. 75 is a suction muffler for the high-stage compression element 73.
The opening of the intermediate pressure suction pipe 74 into the closed container 21 communicates with the suction muffler 75 of the high-stage compression element 73 via a small gap.
【0065】以上のように構成された二段圧縮冷凍冷蔵
装置について、以下その動作を説明する。The operation of the two-stage compression refrigerating and refrigerating apparatus configured as described above will be described below.
【0066】二段圧縮機46の内部構成以外は実施例1
と同じなので、本冷凍サイクルによる効果は実施例1と
ほぼ同様に得られる。すなわち、各庫内の温度制御の精
度を高めると共に庫内各部の温度の均一化が図れ、更に
高効率で消費電力を少なくすることができる。Embodiment 1 Except for the internal structure of the two-stage compressor 46,
Therefore, the effect of the present refrigeration cycle can be obtained almost in the same manner as in the first embodiment. That is, it is possible to improve the accuracy of the temperature control in each of the refrigerators, to make the temperature of each part in the refrigerator uniform, and to further reduce power consumption with higher efficiency.
【0067】本実施例では、中間圧用吸入パイプ74の
密閉容器21内への開口部が高段側圧縮要素73の吸入
マフラー75にわずかな隙間を介して連通しているた
め、中間圧用蒸発器28から中間圧用吸入パイプ74を
通って密閉容器21内に戻ってきた冷媒ガスは、わずか
な隙間を介して高段圧縮要素73の吸入側にある吸入マ
フラー75に吸入される。そのため、冷媒ガスは、低段
圧縮要素23や高段圧縮要素73やモータ22からの受
熱の影響が小さく、温度上昇が小さく抑えられる。従っ
て、吸入される冷媒ガスの密度が大きくなり、冷媒循環
量が多くなると共に効率を向上することができる。In this embodiment, the opening of the intermediate pressure suction pipe 74 into the closed vessel 21 communicates with the suction muffler 75 of the high-stage compression element 73 through a small gap. The refrigerant gas that has returned from inside 28 into the closed casing 21 through the intermediate-pressure suction pipe 74 is drawn into the suction muffler 75 on the suction side of the high-stage compression element 73 through a small gap. Therefore, the influence of the heat received from the low-stage compression element 23, the high-stage compression element 73, and the motor 22 on the refrigerant gas is small, and the temperature rise is suppressed to be small. Therefore, the density of the sucked refrigerant gas increases, the refrigerant circulation amount increases, and the efficiency can be improved.
【0068】更に、中間圧用吸入パイプ74と高段圧縮
要素73の吸入側が直接接続される場合に比べて、わず
かな隙間があるために高段圧縮要素73からの圧力脈動
は密閉容器21内に拡散し、中間圧用吸入パイプ74に
伝わり難く、騒音の発生を防止できる。Further, as compared with the case where the suction pipe 74 for intermediate pressure and the suction side of the high-stage compression element 73 are directly connected, the pressure pulsation from the high-stage compression element 73 is It is difficult to diffuse and transmit to the suction pipe 74 for the intermediate pressure, so that generation of noise can be prevented.
【0069】以上のように本実施例の二段圧縮冷凍冷蔵
装置は、中間圧用吸入パイプ74の密閉容器21内への
開口部が高段側圧縮要素73の吸入側にわずかな隙間を
介して連通する構成となっているので、実施例1の効果
に加えて、中間圧用蒸発器28から中間圧用吸入パイプ
74を通って密閉容器21内に戻ってきた冷媒ガスは、
わずかな隙間を介して高段圧縮要素73の吸入側に吸入
されるため、各圧縮要素やモータ22からの受熱の影響
が小さく、温度上昇が小さく抑えられる。そのため、吸
入される冷媒ガスの密度が大きくなり、冷媒循環量が多
くなると共に効率を向上することができる。更に、高段
圧縮要素からの圧力脈動は密閉容器内に拡散し、中間圧
用吸入パイプに伝わり難く、騒音の発生を防止できる。As described above, in the two-stage compression refrigeration apparatus of this embodiment, the opening of the intermediate-pressure suction pipe 74 into the closed vessel 21 is provided with a small gap on the suction side of the high-stage compression element 73. Because of the communication configuration, in addition to the effect of the first embodiment, the refrigerant gas returned from the intermediate pressure evaporator 28 into the closed container 21 through the intermediate pressure suction pipe 74 is
Since the air is sucked into the suction side of the high-stage compression element 73 through a small gap, the influence of the heat received from each compression element and the motor 22 is small, and the temperature rise is suppressed to a small level. Therefore, the density of the refrigerant gas to be taken in increases, and the amount of circulating refrigerant increases, and the efficiency can be improved. Further, the pressure pulsation from the high-stage compression element is diffused into the closed vessel and is hardly transmitted to the intermediate-pressure suction pipe, so that generation of noise can be prevented.
【0070】[0070]
【発明の効果】以上説明したように請求項1に記載の発
明は、密閉容器内にモーターと低段圧縮要素と高段圧縮
要素とを備えた二段圧縮機と、前記高段圧縮要素の吐出
側と配管接続した凝縮器と、前記凝縮器の出口側と配管
接続した中間圧用膨張装置と、前記低段圧縮要素の吐出
側ならびに前記高段圧縮要素の吸入側と共に連通する中
間圧用吸入パイプと、前記中間圧用膨張装置と前記中間
圧用吸入パイプとの間に配管接続された中間圧用蒸発器
と、前記凝縮器の出口側あるいは中間圧用膨張装置の出
口側と配管接続した低圧用膨張装置と、前記低圧用膨張
装置と前記二段圧縮機の前記低段圧縮要素の吸入側との
間に配管接続された低圧用蒸発器とからなり、前記低段
圧縮要素の吐出側と前記高段圧縮要素の吸入側とが密閉
容器内に連通した構成となっているので、冷凍冷蔵装置
の2つの蒸発器はそれぞれ、冷凍室と冷蔵室等の各庫内
温度に適した蒸発温度にすることができ、各庫内の温度
制御の精度が高くなると共に庫内各部の温度の均一化が
図れる。また、特に中間圧用蒸発器の蒸発温度を高く設
定できるため圧縮機の効率が向上すると共に、各庫内を
必要以上に温度の低い冷気で冷却することが無いため冷
凍サイクル全体の効率が向上する。更に、密閉容器内が
中間圧力になっているため、低段圧縮要素ならびに高段
圧縮要素のそれぞれの圧縮室内と密閉容器内との圧力差
が小さく、各圧縮要素と密閉容器内の間での冷媒ガスの
漏れ量を少なくすることができ、二段圧縮機の冷凍能
力、ならびに効率を向上することができる。As described above, the first aspect of the present invention provides a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, A condenser pipe-connected to the discharge side, an intermediate-pressure expansion device pipe-connected to the outlet side of the condenser, and an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element An intermediate-pressure evaporator piped between the intermediate-pressure expansion device and the intermediate-pressure suction pipe, and a low-pressure expansion device piped to the outlet side of the condenser or the outlet side of the intermediate-pressure expansion device. A low-pressure evaporator connected between the low-pressure expansion device and the suction side of the low-stage compression element of the two-stage compressor, the discharge side of the low-stage compression element and the high-stage compression. The suction side of the element communicates with the closed container Therefore, the two evaporators of the freezing and refrigerating device can be set to the evaporating temperature suitable for the respective internal temperature of the freezing room and the refrigerating room, respectively, and the accuracy of the temperature control in each internal refrigerator is high. In addition, the temperature of each part in the refrigerator can be made uniform. Particularly, the efficiency of the compressor is improved because the evaporating temperature of the intermediate pressure evaporator can be set high, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. . Furthermore, since the inside of the closed vessel is at an intermediate pressure, the pressure difference between the compression chamber of each of the low-stage compression element and the high-stage compression element and the inside of the closed vessel is small, and the pressure between each compression element and the inside of the closed vessel is small. The leakage amount of the refrigerant gas can be reduced, and the refrigeration capacity and efficiency of the two-stage compressor can be improved.
【0071】また、請求項2に記載の発明は、密閉容器
内にモーターと低段圧縮要素と高段圧縮要素とを備えた
二段圧縮機と、前記高段圧縮要素の吐出側と配管接続し
た凝縮器と、前記凝縮器の出口側と配管接続した中間圧
用膨張装置と、前記低段圧縮要素の吐出側ならびに前記
高段圧縮要素の吸入側と共に連通する中間圧用吸入パイ
プと、前記中間圧用膨張装置と前記中間圧用吸入パイプ
との間に配管接続された中間圧用蒸発器と、前記凝縮器
の出口側あるいは前記中間圧用膨張装置の出口側と配管
接続した低圧用膨張装置と、前記低圧用膨張装置と前記
二段圧縮機の前記低段圧縮要素の吸入側との間に配管接
続された低圧用蒸発器とからなり、前記低段圧縮要素の
吸入側が前記密閉容器内に連通した構成となっているの
で、冷凍冷蔵装置の2つの蒸発器は、蒸発圧力がそれぞ
れ低圧と中間圧になるため、冷凍室と冷蔵室等の各庫内
温度に適した蒸発器温度にそれぞれすることができ、各
庫内の温度制御の精度が高くなると共に庫内各部の温度
の均一化が図れる。また、特に中間圧用蒸発器の蒸発温
度を高く設定できることから、圧縮機の効率が向上する
と共に、各庫内を必要以上に温度の低い冷気で冷却する
ことが無いため冷凍サイクル全体の効率が向上する。更
に、低段圧縮要素の吸入側が密閉容器内に連通している
ため、密閉容器内が低圧になり、低圧用蒸発器から戻っ
てくる温度の低い冷媒ガスで密閉容器内の各圧縮要素や
モータを冷却できるので、各圧縮要素の過熱を防止でき
信頼性が向上すると共に、モータの温度低下によりモー
タ効率を向上することができる。The invention according to claim 2 provides a two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, and a pipe connection between a discharge side of the high-stage compression element and a pipe. A condenser, an intermediate-pressure expansion device connected to the outlet of the condenser by piping, an intermediate-pressure suction pipe communicating with a discharge side of the low-stage compression element and a suction side of the high-stage compression element, and an intermediate-pressure suction pipe. An intermediate-pressure evaporator pipe-connected between an expansion device and the intermediate-pressure suction pipe; a low-pressure expansion device connected to the outlet of the condenser or the outlet of the intermediate-pressure expansion device; A low-pressure evaporator connected by piping between an expansion device and the suction side of the low-stage compression element of the two-stage compressor, wherein the suction side of the low-stage compression element communicates with the closed vessel. Refrigeration equipment Since the evaporating pressures of the two evaporators become low pressure and intermediate pressure, respectively, the evaporator temperatures suitable for the respective internal temperatures of the freezing room and the refrigerating room can be respectively set, and the accuracy of the temperature control in each internal compartment can be achieved. And the temperature of each part in the refrigerator can be made uniform. In addition, since the evaporation temperature of the evaporator for the intermediate pressure can be set higher, the efficiency of the compressor is improved, and the efficiency of the entire refrigeration cycle is improved because the inside of each refrigerator is not cooled with unnecessarily low temperature air. I do. Furthermore, since the suction side of the low-stage compression element communicates with the closed container, the pressure in the closed container becomes low, and the low-temperature refrigerant gas returned from the low-pressure evaporator cools each compression element and motor in the closed container. , Cooling of each compression element can be prevented, reliability can be improved, and motor efficiency can be improved by lowering the temperature of the motor.
【0072】また、請求項3に記載の発明は、密閉容器
内にモーターと低段圧縮要素と高段圧縮要素とを備えた
二段圧縮機と、前記高段圧縮要素の吐出側と配管接続し
た凝縮器と、前記凝縮器の出口側と配管接続した中間圧
用膨張装置と、前記低段圧縮要素の吐出側ならびに前記
高段圧縮要素の吸入側と共に連通する中間圧用吸入パイ
プと、前記中間圧用膨張装置と前記中間圧用吸入パイプ
との間に配管接続された中間圧用蒸発器と、前記凝縮器
の出口側あるいは前記中間圧用膨張装置の出口側と配管
接続した低圧用膨張装置と、前記低圧用膨張装置と前記
二段圧縮機の前記低段圧縮要素の吸入側との間に配管接
続された低圧用蒸発器とからなり、前記高段圧縮要素の
吐出側が密閉容器内に連通した構成となっているので、
冷凍冷蔵装置の2つの蒸発器はそれぞれ、冷凍室と冷蔵
室等の各庫内温度に適した蒸発温度にすることができ、
各庫内の温度制御の精度が高くなると共に庫内各部の温
度の均一化が図れる。また、特に中間圧用蒸発器の蒸発
温度を高く設定できるため圧縮機の効率が向上すると共
に、各庫内を必要以上に温度の低い冷気で冷却すること
が無いため冷凍サイクル全体の効率が向上する。更に、
密閉容器内が高圧になっているため、圧力差により密閉
容器内から低段圧縮要素ならびに高段圧縮要素それぞれ
の圧縮室内への潤滑油の供給が十分にでき、ピストンと
シリンダー等の摺動部の潤滑性が向上して信頼性を向上
することができる。The third aspect of the present invention provides a two-stage compressor including a motor, a low-stage compression element and a high-stage compression element in a closed container, and a pipe connection between a discharge side of the high-stage compression element and a pipe. A condenser, an intermediate-pressure expansion device connected to the outlet of the condenser by piping, an intermediate-pressure suction pipe communicating with a discharge side of the low-stage compression element and a suction side of the high-stage compression element, and an intermediate-pressure suction pipe. An intermediate-pressure evaporator pipe-connected between an expansion device and the intermediate-pressure suction pipe; a low-pressure expansion device connected to the outlet of the condenser or the outlet of the intermediate-pressure expansion device; A low-pressure evaporator connected to a pipe between the expansion device and the suction side of the low-stage compression element of the two-stage compressor, wherein the discharge side of the high-stage compression element communicates with the closed vessel. So
Each of the two evaporators of the freezing and refrigeration apparatus can be set to an evaporating temperature suitable for each internal temperature of the freezing room and the refrigerating room,
The accuracy of temperature control in each refrigerator is improved, and the temperature of each part in the refrigerator can be made uniform. Particularly, the efficiency of the compressor is improved because the evaporating temperature of the intermediate pressure evaporator can be set high, and the efficiency of the entire refrigeration cycle is improved because the inside of each compartment is not cooled with cold air having a lower temperature than necessary. . Furthermore,
Since the pressure inside the closed vessel is high, lubricating oil can be sufficiently supplied from the inside of the closed vessel to the compression chamber of each of the low-stage compression element and the high-stage compression element due to the pressure difference. And the reliability can be improved.
【0073】また、請求項4に記載の発明は、請求項1
あるいは請求項2あるいは請求項3に記載の発明に加え
て、低段圧縮要素の気筒容積VLと高段圧縮要素の気筒
容積VHの比VH/VLが0.5〜1.3の範囲に設定
された構成となっているので、更に、冷凍冷蔵装置の冷
凍室と冷蔵室などの異なる温度帯の庫内のどちらか一方
が冷凍能力不足になったり、冷凍能力過剰になること無
く、各庫内を適正に冷却でき、かつ高効率で消費電力を
少なくすることができる。また、高圧、低圧、中間圧の
各圧力に応じた気筒容積の比率にすることにより、モー
タの最大トルクとトルク変動を小さくすることができ、
モータ効率の向上と振動低減ができる。The invention described in claim 4 is the first invention.
Alternatively, in addition to the invention described in claim 2 or 3, the ratio VH / VL of the cylinder volume VL of the low-stage compression element to the cylinder volume VH of the high-stage compression element is set in the range of 0.5 to 1.3. In addition, since one of the refrigerators in different temperature zones such as the freezing room and the refrigerator compartment of the freezing and refrigerating device does not have insufficient refrigeration capacity or does not have excessive freezing capacity, The inside can be properly cooled, and the power consumption can be reduced with high efficiency. Also, by setting the ratio of the cylinder volume according to each of the high pressure, the low pressure, and the intermediate pressure, the maximum torque and torque fluctuation of the motor can be reduced,
Improves motor efficiency and reduces vibration.
【0074】また、請求項5に記載の発明は、請求項1
に記載の発明に加えて、中間圧用吸入パイプの密閉容器
内への開口部が高段側圧縮要素の吸入側にわずかな隙間
を介して連通する構成となっているので、更に、中間圧
用蒸発器から中間圧用吸入パイプを通って密閉容器内に
戻ってきた冷媒ガスは、わずかな隙間を介して高段圧縮
要素の吸入側に吸入されるため、各圧縮要素やモータか
らの受熱の影響が小さく、温度上昇が小さく抑えられ
る。そのため、吸入される冷媒ガスの密度が大きくな
り、冷媒循環量が多くなると共に効率を向上することが
できる。更に、高段圧縮要素からの圧力脈動は密閉容器
内に拡散し、中間圧用吸入パイプに伝わり難く、騒音の
発生を防止できる。The invention described in claim 5 is the first invention.
In addition to the above-mentioned invention, since the opening of the suction pipe for intermediate pressure into the closed vessel communicates with the suction side of the high-stage compression element via a small gap, the evaporation for intermediate pressure is further improved. The refrigerant gas returned from the compressor through the intermediate-pressure suction pipe into the closed vessel is drawn into the suction side of the high-stage compression element through a small gap, so the influence of the heat received from each compression element and motor It is small and the temperature rise is kept small. Therefore, the density of the refrigerant gas to be taken in increases, and the amount of circulating refrigerant increases, and the efficiency can be improved. Further, the pressure pulsation from the high-stage compression element is diffused into the closed vessel and is hardly transmitted to the intermediate-pressure suction pipe, so that generation of noise can be prevented.
【図1】本発明による二段圧縮冷凍冷蔵装置の実施例1
の冷媒回路図FIG. 1 is a first embodiment of a two-stage compression refrigeration apparatus according to the present invention.
Refrigerant circuit diagram
【図2】同実施例の二段圧縮冷凍冷蔵装置に使用する二
段圧縮機の平面断面図FIG. 2 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【図3】同実施例の二段圧縮冷凍冷蔵装置に使用する二
段圧縮機の縦断面図FIG. 3 is a longitudinal sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【図4】同実施例の二段圧縮冷凍冷蔵装置における冷凍
サイクルの圧力−エンタルピ線図FIG. 4 is a pressure-enthalpy diagram of a refrigeration cycle in the two-stage compression refrigeration apparatus of the embodiment.
【図5】本発明による二段圧縮冷凍冷蔵装置の実施例2
の冷媒回路図FIG. 5 is a second embodiment of a two-stage compression refrigeration apparatus according to the present invention.
Refrigerant circuit diagram
【図6】同実施例の二段圧縮冷凍冷蔵装置に使用する二
段圧縮機の平面断面図FIG. 6 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【図7】本発明による二段圧縮冷凍冷蔵装置の実施例3
の冷媒回路図FIG. 7 is a third embodiment of a two-stage compression refrigeration apparatus according to the present invention.
Refrigerant circuit diagram
【図8】同実施例の二段圧縮冷凍冷蔵装置に使用する二
段圧縮機の平面断面図FIG. 8 is a plan sectional view of a two-stage compressor used in the two-stage compression refrigeration apparatus of the embodiment.
【図9】本発明による二段圧縮冷凍冷蔵装置の実施例4
における二段圧縮機の縦断面図FIG. 9 is a fourth embodiment of a two-stage compression refrigeration apparatus according to the present invention.
Sectional view of a two-stage compressor in Japan
【図10】本発明による二段圧縮冷凍冷蔵装置の実施例
5における二段圧縮機の平面断面図FIG. 10 is a plan sectional view of a two-stage compressor in a fifth embodiment of a two-stage compression refrigeration apparatus according to the present invention.
【図11】従来の二段圧縮機を使用した二段圧縮冷凍サ
イクルの配管系統図FIG. 11 is a piping diagram of a two-stage compression refrigeration cycle using a conventional two-stage compressor.
20 二段圧縮機 21 密閉容器 22 モータ 23 低段圧縮要素 24 高段圧縮要素 25 凝縮器 26 中間圧用膨張装置 27 中間圧用吸入パイプ 28 中間圧用蒸発器 29 低圧用膨張装置 30 低圧用蒸発器 46 二段圧縮機 47 低段圧縮要素 48 高段圧縮要素 49 中間圧用吸入パイプ 55 二段圧縮機 56 低段圧縮要素 57 高段圧縮要素 58 中間圧用吸入パイプ 64 二段圧縮機 65 低段圧縮要素 66 高段圧縮要素 72 二段圧縮機 73 高段圧縮要素 74 中間圧用吸入パイプ DESCRIPTION OF SYMBOLS 20 Two-stage compressor 21 Closed container 22 Motor 23 Low-stage compression element 24 High-stage compression element 25 Condenser 26 Intermediate pressure expansion device 27 Intermediate pressure suction pipe 28 Intermediate pressure evaporator 29 Low pressure expansion device 30 Low pressure evaporator 46 2 Stage compressor 47 Low stage compression element 48 High stage compression element 49 Intermediate pressure suction pipe 55 Two stage compressor 56 Low stage compression element 57 High stage compression element 58 Intermediate pressure suction pipe 64 Two stage compressor 65 Low stage compression element 66 High Stage compression element 72 Two stage compressor 73 High stage compression element 74 Intermediate pressure suction pipe
【手続補正書】[Procedure amendment]
【提出日】平成11年9月24日(1999.9.2
4)[Submission date] September 24, 1999 (1999.9.2)
4)
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】特許請求の範囲[Correction target item name] Claims
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【特許請求の範囲】[Claims]
───────────────────────────────────────────────────── フロントページの続き (72)発明者 坪井 康祐 大阪府東大阪市高井田本通4丁目2番5号 松下冷機株式会社内 Fターム(参考) 3H076 AA04 AA38 BB21 BB31 BB32 BB35 BB43 CC28 CC91 CC92 CC94 CC99 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Kosuke Tsuboi 4-5-2-5 Takaida Hondori, Higashi-Osaka-shi, Osaka Matsushita Refrigerator Co., Ltd. F-term (reference) 3H076 AA04 AA38 BB21 BB31 BB32 BB35 BB43 CC28 CC91 CC92 CC94 CC99
Claims (5)
高段圧縮要素とを備えた二段圧縮機と、前記高段圧縮要
素の吐出側と配管接続した凝縮器と、前記凝縮器の出口
側と配管接続した中間圧用膨張装置と、前記低段圧縮要
素の吐出側ならびに前記高段圧縮要素の吸入側と共に連
通する中間圧用吸入パイプと、前記中間圧用膨張装置と
前記中間圧用吸入パイプとの間に配管接続された中間圧
用蒸発器と、前記凝縮器の出口側あるいは前記中間圧用
膨張装置の入口側と配管接続した低圧用膨張装置と、前
記低圧用膨張装置と前記二段圧縮機の低段圧縮要素の吸
入側との間に配管接続された低圧用蒸発器とからなり、
前記低段圧縮要素の吐出側と前記高段圧縮要素の吸入側
とが前記密閉容器内に連通した二段圧縮冷凍冷蔵装置。1. A two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, a condenser connected to a discharge side of the high-stage compression element by piping, An intermediate-pressure expansion device connected to the outlet side with a pipe, an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element, the intermediate-pressure expansion device and the intermediate-pressure suction pipe, An evaporator for intermediate pressure connected between the pipes, a low-pressure expansion device connected to the outlet side of the condenser or the inlet side of the expansion device for intermediate pressure, and the low-pressure expansion device and the two-stage compressor. A low-pressure evaporator connected to the piping between the low-stage compression element and the suction side,
A two-stage compression refrigeration apparatus in which a discharge side of the low-stage compression element and a suction side of the high-stage compression element communicate with the closed container.
高段圧縮要素とを備えた二段圧縮機と、前記高段圧縮要
素の吐出側と配管接続した凝縮器と、前記凝縮器の出口
側と配管接続した中間圧用膨張装置と、前記低段圧縮要
素の吐出側ならびに前記高段圧縮要素の吸入側と共に連
通する中間圧用吸入パイプと、前記中間圧用膨張装置と
前記中間圧用吸入パイプとの間に配管接続された中間圧
用蒸発器と、前記凝縮器の出口側あるいは前記中間圧用
膨張装置の入口側と配管接続した低圧用膨張装置と、前
記低圧用膨張装置と前記二段圧縮機の低段圧縮要素の吸
入側との間に配管接続された低圧用蒸発器とからなり、
前記低段圧縮要素の吸入側が前記密閉容器内に連通した
二段圧縮冷凍冷蔵装置。2. A two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed vessel, a condenser connected to a discharge side of the high-stage compression element by piping, An intermediate-pressure expansion device connected to the outlet side with a pipe, an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element, the intermediate-pressure expansion device and the intermediate-pressure suction pipe, An evaporator for intermediate pressure connected between the pipes, a low-pressure expansion device connected to the outlet side of the condenser or the inlet side of the expansion device for intermediate pressure, and the low-pressure expansion device and the two-stage compressor. A low-pressure evaporator connected to the piping between the low-stage compression element and the suction side,
A two-stage compression refrigeration apparatus in which the suction side of the low-stage compression element communicates with the inside of the closed container.
高段圧縮要素とを備えた二段圧縮機と、前記高段圧縮要
素の吐出側と配管接続した凝縮器と、前記凝縮器の出口
側と配管接続した中間圧用膨張装置と、前記低段圧縮要
素の吐出側ならびに前記高段圧縮要素の吸入側と共に連
通する中間圧用吸入パイプと、前記中間圧用膨張装置と
前記中間圧用吸入パイプとの間に配管接続された中間圧
用蒸発器と、前記凝縮器の出口側あるいは前記中間圧用
膨張装置の入口側と配管接続した低圧用膨張装置と、前
記低圧用膨張装置と前記二段圧縮機の低段圧縮要素の吸
入側との間に配管接続された低圧用蒸発器とからなり、
前記高段圧縮要素の吐出側が前記密閉容器内に連通した
二段圧縮冷凍冷蔵装置。3. A two-stage compressor having a motor, a low-stage compression element and a high-stage compression element in a closed container, a condenser connected to a discharge side of the high-stage compression element by piping, An intermediate-pressure expansion device connected to the outlet side with a pipe, an intermediate-pressure suction pipe communicating with the discharge side of the low-stage compression element and the suction side of the high-stage compression element, the intermediate-pressure expansion device and the intermediate-pressure suction pipe, An evaporator for intermediate pressure connected between the pipes, a low-pressure expansion device connected to the outlet side of the condenser or the inlet side of the expansion device for intermediate pressure, and the low-pressure expansion device and the two-stage compressor. A low-pressure evaporator connected to the piping between the low-stage compression element and the suction side,
A two-stage compression refrigeration unit in which a discharge side of the high-stage compression element communicates with the inside of the closed container.
要素の気筒容積VHの比VH/VLが0.5〜1.3の
範囲に設定された請求項1または請求項2または請求項3
に記載の二段圧縮冷凍冷蔵装置。4. The ratio VH / VL of the cylinder volume VL of the low-stage compression element and the cylinder volume VH of the high-stage compression element is set in a range of 0.5 to 1.3. Item 3
2. The two-stage compression freezing and refrigeration apparatus according to 1.
口部が高段側圧縮要素の吸入側にわずかな隙間を介して
連通する請求項1に記載の二段圧縮冷凍冷蔵装置。5. The two-stage compression refrigeration apparatus according to claim 1, wherein an opening of the intermediate-pressure suction pipe into the closed vessel communicates with a suction side of the high-stage compression element through a small gap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24751599A JP3847493B2 (en) | 1999-09-01 | 1999-09-01 | Two-stage compression refrigeration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24751599A JP3847493B2 (en) | 1999-09-01 | 1999-09-01 | Two-stage compression refrigeration system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001074325A true JP2001074325A (en) | 2001-03-23 |
| JP3847493B2 JP3847493B2 (en) | 2006-11-22 |
Family
ID=17164641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24751599A Expired - Fee Related JP3847493B2 (en) | 1999-09-01 | 1999-09-01 | Two-stage compression refrigeration system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3847493B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003001129A1 (en) * | 2001-06-26 | 2003-01-03 | Daikin Industries, Ltd. | Freezing device |
| JP2007232263A (en) * | 2006-02-28 | 2007-09-13 | Daikin Ind Ltd | Refrigeration equipment |
| US9121641B2 (en) | 2012-04-02 | 2015-09-01 | Whirlpool Corporation | Retrofittable thermal storage for air conditioning systems |
| US9188369B2 (en) | 2012-04-02 | 2015-11-17 | Whirlpool Corporation | Fin-coil design for a dual suction air conditioning unit |
| CN112964003A (en) * | 2021-01-23 | 2021-06-15 | 上海朗旦科技集团有限公司 | Control method of refrigerator using micro moving-magnetic type series two-stage linear compressor |
| CN115962121A (en) * | 2022-12-06 | 2023-04-14 | 珠海格力电器股份有限公司 | Double-cylinder two-stage compressor and refrigerating system with same |
-
1999
- 1999-09-01 JP JP24751599A patent/JP3847493B2/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003001129A1 (en) * | 2001-06-26 | 2003-01-03 | Daikin Industries, Ltd. | Freezing device |
| CN100353128C (en) * | 2001-06-26 | 2007-12-05 | 大金工业株式会社 | Freezing device |
| JP2007232263A (en) * | 2006-02-28 | 2007-09-13 | Daikin Ind Ltd | Refrigeration equipment |
| WO2007105440A1 (en) * | 2006-02-28 | 2007-09-20 | Daikin Industries, Ltd. | Refrigeration device |
| CN101384865B (en) * | 2006-02-28 | 2012-04-18 | 大金工业株式会社 | Refrigerating system |
| US9121641B2 (en) | 2012-04-02 | 2015-09-01 | Whirlpool Corporation | Retrofittable thermal storage for air conditioning systems |
| US9188369B2 (en) | 2012-04-02 | 2015-11-17 | Whirlpool Corporation | Fin-coil design for a dual suction air conditioning unit |
| US9863674B2 (en) | 2012-04-02 | 2018-01-09 | Whirlpool Corporation | Fin-coil design for dual suction air conditioning unit |
| CN112964003A (en) * | 2021-01-23 | 2021-06-15 | 上海朗旦科技集团有限公司 | Control method of refrigerator using micro moving-magnetic type series two-stage linear compressor |
| CN115962121A (en) * | 2022-12-06 | 2023-04-14 | 珠海格力电器股份有限公司 | Double-cylinder two-stage compressor and refrigerating system with same |
| CN115962121B (en) * | 2022-12-06 | 2025-09-19 | 珠海格力电器股份有限公司 | Double-cylinder double-stage compressor and refrigerating system with same |
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|---|---|
| JP3847493B2 (en) | 2006-11-22 |
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