JP2005257149A - Refrigerator - Google Patents

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Publication number
JP2005257149A
JP2005257149A JP2004068381A JP2004068381A JP2005257149A JP 2005257149 A JP2005257149 A JP 2005257149A JP 2004068381 A JP2004068381 A JP 2004068381A JP 2004068381 A JP2004068381 A JP 2004068381A JP 2005257149 A JP2005257149 A JP 2005257149A
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Prior art keywords
refrigerant
gas
liquid separator
compressor
heat insulating
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JP2004068381A
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Inventor
Toshimichi Hirata
俊通 平田
Haruyuki Yoshida
治之 吉田
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Sanyo Electric Co Ltd
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Sanyo Electric Co Ltd
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Priority to JP2004068381A priority Critical patent/JP2005257149A/en
Publication of JP2005257149A publication Critical patent/JP2005257149A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/05Compression system with heat exchange between particular parts of the system
    • F25B2400/052Compression system with heat exchange between particular parts of the system between the capillary tube and another part of the refrigeration cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/13Economisers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/23Separators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D23/00General constructional features
    • F25D23/003General constructional features for cooling refrigerating machinery

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  • Devices That Are Associated With Refrigeration Equipment (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To improve the cooling capacity of a freezing cycle of a refrigerator. <P>SOLUTION: This refrigerator 1 has a main body composed of a heat insulating casing 2, and comprises the freezing cycle for allowing a refrigerant of high temperature and high pressure discharged from a compressor 21 to be successively circulated to a radiator 23, expanding parts 24, 31 and an evaporator 16, and returned to the compressor. The sectioned inside of the refrigerator of the heat insulating casing is cooled by applying the evaporating action of the refrigerant by an evaporator of the freezing cycle, the expanding parts are constituted by a series circuit formed by successively connecting a first expanding part, a gas-liquid separator 18 and a second expanding part, a gas refrigerant in the gas-liquid separator is supplied to an intermediate pressure part 21c of the compressor, and the gas-liquid separator is covered by a heat insulating material. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、本体が断熱作用を有する断熱箱体で構成されているとともに、内部にコンプレッサから吐出される高温・高圧の冷媒が放熱器、膨張部、蒸発器を順次循環して再びコンプレッサに戻る冷凍サイクルを具備し、この冷凍サイクルの蒸発器で作動冷媒が蒸発する際の吸熱作用により区画された庫内を冷却することのできる冷蔵庫に関する。   In the present invention, the main body is constituted by a heat insulating box body having a heat insulating action, and high-temperature and high-pressure refrigerant discharged from the compressor is circulated through the radiator, the expansion unit, and the evaporator in order, and returns to the compressor again. The present invention relates to a refrigerator that includes a refrigeration cycle and that can cool a compartment partitioned by an endothermic action when a working refrigerant evaporates in an evaporator of the refrigeration cycle.

従来の冷蔵庫では、たとえば特許文献1の冷蔵庫では冷凍先サイクルが、圧縮機(コンプレッサに相当)、コンデンサ(放熱器に相当)、キャピラリー(キャピラリーチューブに相当)、冷却器(蒸発器に相当)を環状に接続して構成されていた。この際、キャピラリーチューブや膨張弁などの膨張部は一段のみである。   In a conventional refrigerator, for example, in the refrigerator disclosed in Patent Document 1, a refrigeration destination cycle includes a compressor (corresponding to a compressor), a condenser (corresponding to a radiator), a capillary (corresponding to a capillary tube), and a cooler (corresponding to an evaporator). It was configured to be connected in a ring. At this time, the expansion portion such as the capillary tube or the expansion valve is only one stage.

ところで、図2の P-h線図に示すように、キャピラリーチューブや膨張弁などの膨張部が膨張部24の一段のみであると、膨張部24で減圧された冷媒がそのまま全て蒸発器へ供給されるため冷却能力は図2に示すa−b間の冷却能力となる。膨張部を膨張部24および膨張部31の2段にすると、膨張部31の作用により冷媒の圧力を図2のcまで減圧することができ、その結果c−b間の冷却能力を得ることができる。そこで、本出願人は、冷蔵庫における冷凍サイクルの膨張部を二段にすることを検討した。しかしながら、膨張部を二段にするためには、第1膨張部24と第2膨張部31との間で一部の冷媒に蒸発作用を行わさせて冷媒を冷却させる必要があり、その結果ガス化した冷媒を分離させるための気液分離器18を設ける必要がある。そして、この気液分離器18を冷蔵庫に如何にして配置するかが問題となる。たとえば、冷蔵庫の機械室などに配置すると、コンプレッサや放熱器などからの熱が気液分離器18に侵入し、冷却効率が落ちる。
特開2002−286347号公報
By the way, as shown in the Ph diagram of FIG. 2, when the expansion part such as the capillary tube or the expansion valve is only one stage of the expansion part 24, all the refrigerant decompressed by the expansion part 24 is supplied to the evaporator as it is. Therefore, the cooling capacity is the cooling capacity between a and b shown in FIG. When the expansion part is in two stages, the expansion part 24 and the expansion part 31, the pressure of the refrigerant can be reduced to c in FIG. 2 by the action of the expansion part 31, and as a result, the cooling capacity between c and b can be obtained. it can. Therefore, the present applicant studied to make the expansion part of the refrigeration cycle in the refrigerator into two stages. However, in order to make the expansion part into two stages, it is necessary to cause some refrigerant to evaporate between the first expansion part 24 and the second expansion part 31 to cool the refrigerant, and as a result, the gas It is necessary to provide a gas-liquid separator 18 for separating the converted refrigerant. The problem is how to arrange the gas-liquid separator 18 in the refrigerator. For example, when it is disposed in a machine room of a refrigerator, heat from a compressor, a radiator or the like enters the gas-liquid separator 18 and cooling efficiency decreases.
JP 2002-286347 A

解決しようとする問題点は、冷蔵庫の冷凍サイクルの膨張部が一段で冷却能力が低い点であり、また、冷蔵庫の冷凍サイクルの膨張部を二段にした場合に、気液分離器を冷蔵庫の最適な場所に如何にして配置するかという点である。   The problem to be solved is that the expansion part of the refrigerator refrigeration cycle is one stage and the cooling capacity is low, and when the expansion part of the refrigerator refrigeration cycle is two stages, the gas-liquid separator is connected to the refrigerator. It is a point how to arrange in the most suitable place.

本発明の冷蔵庫(1)は、本体を断熱箱体(2)で構成し、コンプレッサ(21)から吐出される高温高圧の冷媒が、放熱器(23)、膨張部(24,31)、蒸発器(16)を順次循環してコンプレッサに戻る冷凍サイクルを具備し、この冷凍サイクルの蒸発器での冷媒の蒸発作用を用いて前記断熱箱体の区画される庫内を冷却すると共に、前記膨張部を第1膨張部、気液分離器(18)、および第2膨張部を順次直列に接続した直列回路で構成し、前記気液分離器中のガス冷媒を前記コンプレッサの中間圧部(21c)に供給し、かつ、前記気液分離器を断熱材で覆う。   The refrigerator (1) of the present invention has a main body constituted by a heat insulating box (2), and the high-temperature and high-pressure refrigerant discharged from the compressor (21) is a radiator (23), expansion parts (24, 31), evaporation. A refrigeration cycle that sequentially circulates through the vessel (16) and returns to the compressor, and cools the interior of the heat-insulated box body using the evaporation of refrigerant in the evaporator of the refrigeration cycle, and the expansion The first expansion section, the gas-liquid separator (18), and the second expansion section are sequentially connected in series, and the gas refrigerant in the gas-liquid separator is used as the intermediate pressure section (21c) of the compressor. And the gas-liquid separator is covered with a heat insulating material.

また、前記気液分離器が、断熱箱体の背面側を成す断熱材(2a)の中に配置されていることがある。
さらに、前記気液分離器が、蒸発器近傍の断熱材の中に配置されていることがある。
Moreover, the said gas-liquid separator may be arrange | positioned in the heat insulating material (2a) which comprises the back side of a heat insulation box.
Furthermore, the gas-liquid separator may be disposed in a heat insulating material near the evaporator.

そして、前記コンプレッサが、単一ケース内に圧縮要素を直列に2段接続した2段圧縮の構成を備えると共に、前記圧縮要素間の中間圧部に前記気液分離器からのガス冷媒を供給することがある。   The compressor has a two-stage compression configuration in which two compression elements are connected in series in a single case, and supplies the gas refrigerant from the gas-liquid separator to an intermediate pressure portion between the compression elements. Sometimes.

また、前記冷凍サイクルを循環する冷媒が、二酸化炭素、又は二酸化炭素を含有する冷媒であることがある。
さらに、前記冷凍サイクルの第1膨張部又は第2膨張部の少なくとも一方をキャピラリーチューブで構成することがある。
The refrigerant circulating in the refrigeration cycle may be carbon dioxide or a refrigerant containing carbon dioxide.
Furthermore, at least one of the first expansion section and the second expansion section of the refrigeration cycle may be configured with a capillary tube.

そして、前記冷凍サイクルの第1膨張部及び第2膨張部の両方をキャピラリーチューブで構成することがある。
また、前記気液分離器を前記コンプレッサより上方に配置することがある。
And both the 1st expansion part and the 2nd expansion part of the refrigerating cycle may be constituted with a capillary tube.
Further, the gas-liquid separator may be disposed above the compressor.

さらに、前記放熱器は放熱作用を有する複数の熱交換器に分割されて構成されていることがある。
そして、第1の膨張部中の冷媒と前記ガス冷媒とを熱交換させる構成を備えることがある。
Furthermore, the heat radiator may be divided into a plurality of heat exchangers having a heat radiation action.
And it may be provided with the structure which carries out heat exchange between the refrigerant in the 1st expansion part, and the gas refrigerant.

また、第2の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えることがある。
さらに、第1の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えることがある。
In addition, there may be a configuration in which heat exchange is performed between the refrigerant in the second expansion portion and the refrigerant discharged from the evaporator.
Furthermore, the refrigerant | coolant in a 1st expansion part and the structure which heat-exchanged the refrigerant | coolant which came out of the said evaporator may be provided.

本発明によれば、冷蔵庫の冷凍サイクルの膨張部を第1膨張部、気液分離器、および第2膨張部を順次直列に接続した直列回路で構成し、気液分離器中のガス冷媒をコンプレッサの中間圧部に供給しており、冷蔵庫の冷凍サイクルの冷却能力が向上する。しかも、第1膨張部と第2膨張部との間に設けられる気液分離器が断熱材で覆われている。その結果、気液分離器から第2膨張部に供給される冷媒への機械室からの発熱の影響を、断熱材で少なくすることができる。その結果、冷凍サイクルの冷却効率が向上する。   According to the present invention, the expansion part of the refrigeration cycle of the refrigerator is configured by a series circuit in which the first expansion part, the gas-liquid separator, and the second expansion part are sequentially connected in series, and the gas refrigerant in the gas-liquid separator is Supplying to the intermediate pressure part of the compressor improves the cooling capacity of the refrigeration cycle of the refrigerator. And the gas-liquid separator provided between the 1st expansion part and the 2nd expansion part is covered with the heat insulating material. As a result, the influence of heat generated from the machine room on the refrigerant supplied from the gas-liquid separator to the second expansion section can be reduced by the heat insulating material. As a result, the cooling efficiency of the refrigeration cycle is improved.

また、気液分離器が、断熱箱体の背面側を成す断熱材の中に配置されており、気液分離器の断熱を断熱箱体の断熱に用いる断熱材と共用することができ、分品点数の削減となり効率良い配置となる。   In addition, the gas-liquid separator is disposed in a heat insulating material that forms the back side of the heat insulating box, and the heat insulating of the gas liquid separator can be shared with the heat insulating material used for heat insulating the heat insulating box. The number of items is reduced and the arrangement is efficient.

さらに、気液分離器が、蒸発器近傍の断熱材の中に配置されており、蒸発器から断熱材を介して断熱箱体外へ漏れていた冷熱を気液分離器へ有効に供給でき、冷媒の冷却効率が上がる。
そして、コンプレッサが、単一ケース内に圧縮要素を直列に2段接続した2段圧縮の構成を備えると共に、前記圧縮要素間の中間圧部に気液分離器からのガス冷媒を供給しており、気液分離器からのガス冷媒を2段圧縮のコンプレッサの中間圧部から回収することができ、冷却能力を低下させること無くガス冷媒を再圧縮することができる。
Furthermore, the gas-liquid separator is arranged in the heat insulating material in the vicinity of the evaporator, and the cold heat leaking from the evaporator to the outside of the heat insulating box through the heat insulating material can be effectively supplied to the gas-liquid separator, Increases the cooling efficiency of the refrigerant.
The compressor has a two-stage compression configuration in which two compression elements are connected in series in a single case, and supplies gas refrigerant from the gas-liquid separator to the intermediate pressure portion between the compression elements. The gas refrigerant from the gas-liquid separator can be recovered from the intermediate pressure part of the two-stage compressor, and the gas refrigerant can be recompressed without reducing the cooling capacity.

また、冷凍サイクルを循環する冷媒が、二酸化炭素、又は二酸化炭素を含有する冷媒であるので、他の冷媒と比較して環境に良い。
さらに、冷凍サイクルの第1膨張部又は第2膨張部の少なくとも一方をキャピラリーチューブで構成しており、構成を簡単にすることができる。
そして、冷凍サイクルの第1膨張部及び第2膨張部の両方をキャピラリーチューブで構成しており、構成を簡単にすることができる。
In addition, since the refrigerant circulating in the refrigeration cycle is carbon dioxide or a refrigerant containing carbon dioxide, it is better for the environment than other refrigerants.
Furthermore, at least one of the first expansion section or the second expansion section of the refrigeration cycle is configured with a capillary tube, and the configuration can be simplified.
And both the 1st expansion | swelling part and 2nd expansion | swelling part of a refrigerating cycle are comprised with the capillary tube, and a structure can be simplified.

また、気液分離器をコンプレッサより上方に配置しており、コンプレッサの停止時に液冷媒を自重で貯留することができる。
さらに、放熱器は放熱作用を有する複数の熱交換器に分割されて構成されており、放熱を露付き防止等に利用できる。
そして、第1膨張部中の冷媒と前記ガス冷媒とを熱交換させており、ガス冷媒を第1膨張部中の冷媒で加熱することにより確実にガス化させることができる。
Further, the gas-liquid separator is disposed above the compressor, and the liquid refrigerant can be stored by its own weight when the compressor is stopped.
Furthermore, the heat radiator is configured by being divided into a plurality of heat exchangers having a heat radiation action, and the heat radiation can be used for preventing dew condensation.
And the refrigerant | coolant in a 1st expansion part and the said gas refrigerant are heat-exchanged, and it can gasify reliably by heating a gas refrigerant with the refrigerant | coolant in a 1st expansion part.

また、第2の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えており、蒸発器から出た冷媒を過熱することができる。
さらに、第1の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えており、蒸発器から出た冷媒を過熱することができる。
Moreover, the structure which heat-exchanges the refrigerant | coolant in a 2nd expansion part and the refrigerant | coolant which came out of the said evaporator is provided, and the refrigerant | coolant which came out of the evaporator can be overheated.
Furthermore, the refrigerant | coolant in the 1st expansion | swelling part and the structure which heat-exchanges the refrigerant | coolant which came out of the said evaporator are provided, and the refrigerant | coolant which came out of the evaporator can be overheated.

冷蔵庫の冷凍サイクルの冷却能力を向上させるという目的を、膨張部を第1膨張部および第2膨張部の2段設け、この第1膨張部と第2膨張部との間に気液分離器を設けて、この気液分離器でガス冷媒と液冷媒とに分け、気体状のガス冷媒をコンプレッサの中間圧部に戻すとともに、膨張部を2段にした際に設けられる気液分離器を断熱材で覆って断熱し、コンプレッサや放熱器などからの熱が気液分離器に侵入することを極力防止することで実現した。   For the purpose of improving the cooling capacity of the refrigeration cycle of the refrigerator, the expansion section is provided with two stages of the first expansion section and the second expansion section, and a gas-liquid separator is provided between the first expansion section and the second expansion section. The gas-liquid separator is divided into a gas refrigerant and a liquid refrigerant, the gaseous gas refrigerant is returned to the intermediate pressure part of the compressor, and the gas-liquid separator provided when the expansion part is arranged in two stages is insulated. It was realized by covering it with a material and insulating it to prevent heat from the compressor and radiator from entering the gas-liquid separator as much as possible.

次に、本発明における冷蔵庫の一実施例について、図1ないし図6を用いて説明する。図1は本発明における冷蔵庫の冷凍サイクルの冷媒回路図である。図2は図1の冷凍サイクルの P-h線図である。図3は冷蔵庫の断面図である。図4は冷蔵庫の斜視図である。図5、図6は冷凍サイクルの変形例である。なお、図4において、断熱箱体の一部が透視された状態で図示されている。   Next, an embodiment of the refrigerator according to the present invention will be described with reference to FIGS. FIG. 1 is a refrigerant circuit diagram of a refrigeration cycle of a refrigerator in the present invention. FIG. 2 is a Ph diagram of the refrigeration cycle of FIG. FIG. 3 is a sectional view of the refrigerator. FIG. 4 is a perspective view of the refrigerator. 5 and 6 show modified examples of the refrigeration cycle. In FIG. 4, a part of the heat insulating box is shown in a transparent state.

図3および図4において、家庭用の冷蔵庫1は、その本体である外郭が断熱効果を有する断熱材を備える断熱箱体2で構成されている。この断熱箱体2の内部空間(すなわち複数の区画に分割された庫内)は、設定温度の異なる複数の貯蔵室3(この実施例では5室、すなわち5区画)に仕切られており、各貯蔵室3は例えば冷蔵室、野菜室、アイス室、冷凍や冷蔵を選べるセレクト室や冷凍室などになっている。また、断熱箱体2の前面開口は、断熱効果を備える断熱扉4で開閉可能に閉じられている。そして、下側の貯蔵室3の奥側は、機械室11となっている。さらに、断熱箱体2の内部空間には、冷気が循環する冷気流路13が設けられ、この冷気流路13内には、蒸発器16および、この蒸発器16で冷却された冷気を各貯蔵室3に循環させる蒸発器用送風機17が設けられている。蒸発器16の近傍で背面側に位置する断熱壁2aには、中間圧用の気液分離器18が内蔵されている。また、この気液分離器18はコンプレッサ21の上方に位置し、コンプレッサ21の停止時に冷媒を貯留することができる。尚、蒸発器16は単一のものを用いて、冷凍用の冷気及び冷蔵用の冷気を生成しているが、蒸発温度の異なる複数の蒸発器から構成し、冷凍用及び冷蔵用に夫々専用の温度の冷気を生成するようにしても良い。放熱器23は単一の熱交換器であってよく、また冷蔵庫の前面開口周囲の露付きを防止する露付き防止ヒータとしての熱交換器、除霜水・ドレンの蒸発に用いるドレンパン用コンデンサ等に一部転用するなど複数の熱交換器の組み合わせで構成しても良い。従って、放熱器としてはプレートコンデンサ、マイクロフィンチューブ、フィンチューブコンデンサ、クレストコンデンサやフレームコンデンサなどが用いられる。   3 and 4, the household refrigerator 1 is configured by a heat insulating box 2 including a heat insulating material whose outer shell, which is a main body, has a heat insulating effect. The internal space of the heat insulation box 2 (that is, the interior divided into a plurality of compartments) is partitioned into a plurality of storage chambers 3 (in this embodiment, five compartments, that is, five compartments) having different set temperatures. The storage room 3 is, for example, a refrigerated room, a vegetable room, an ice room, a select room or a freezer room for selecting freezing or refrigeration. Moreover, the front opening of the heat insulation box 2 is closed by the heat insulation door 4 provided with the heat insulation effect so that opening and closing is possible. The inner side of the lower storage chamber 3 is a machine room 11. Further, in the internal space of the heat insulating box 2, a cold air flow path 13 through which the cold air circulates is provided. In the cold air flow path 13, an evaporator 16 and the cold air cooled by the evaporator 16 are stored. An evaporator blower 17 to be circulated in the chamber 3 is provided. A gas-liquid separator 18 for intermediate pressure is built in the heat insulating wall 2a located near the evaporator 16 on the back side. The gas-liquid separator 18 is located above the compressor 21 and can store the refrigerant when the compressor 21 is stopped. In addition, although the evaporator 16 produces | generates the cold air for freezing and the cold air for refrigeration using the single thing, it is comprised from several evaporators from which evaporation temperature differs, and each is dedicated for freezing and refrigeration. You may make it produce | generate the cold of the temperature. The radiator 23 may be a single heat exchanger, a heat exchanger as a dew prevention heater that prevents dew condensation around the front opening of the refrigerator, a drain pan condenser used for evaporating defrost water and drain, etc. It may be configured by a combination of a plurality of heat exchangers such as partially diverting to the above. Therefore, a plate capacitor, a micro fin tube, a fin tube capacitor, a crest capacitor, a frame capacitor, or the like is used as a heat radiator.

そして、機械室11には、コンプレッサ21などが設けられている。このコンプレッサ21は、上述の蒸発器16および気液分離器18などとともに冷媒配管で接続され、図1および図2に図示する冷凍サイクルを構成している。コンプレッサ21は二段圧縮式で、単一の密閉ケース内に第1圧縮部21aおよび第2圧縮部21bを直列に結合し2段圧縮を可能にしており、吸い込んだ気体状の冷媒を圧縮し、高温・高圧となった冷媒を、放熱器23に吐出する。そして、冷媒は放熱器23で温度が低下し、第1膨張部である第1キャピラリーチューブ24で減圧された後、中間圧に位置する気液分離器18内で一部が膨張(蒸発作用)し、気体状のガス冷媒と液体状の液冷媒とに分けられる。この際、冷媒の蒸発作用で液冷媒が冷却される。尚、第1膨張部の構成としては、予め想定される冷凍サイクルの動作に合わせて設計された第1キャピラリーチューブ24を用いているが、冷凍サイクルの負荷変動を考慮する必要がある場合は、絞り量を可変できる可動式の膨張機構を用いて予め定められたアルゴリズムに従ってこの絞り量を可変し冷凍サイクルの運転サイクルが最適、又は安定するように制御しても良いものである。   The machine room 11 is provided with a compressor 21 and the like. The compressor 21 is connected by a refrigerant pipe together with the evaporator 16 and the gas-liquid separator 18 described above, and constitutes the refrigeration cycle shown in FIGS. 1 and 2. The compressor 21 is a two-stage compression type. The first compression section 21a and the second compression section 21b are connected in series in a single sealed case to enable two-stage compression, and compresses the sucked gaseous refrigerant. Then, the high-temperature and high-pressure refrigerant is discharged to the radiator 23. Then, the temperature of the refrigerant is lowered by the radiator 23 and reduced in pressure by the first capillary tube 24 as the first expansion part, and then partially expanded (evaporation action) in the gas-liquid separator 18 located at the intermediate pressure. However, it is divided into a gaseous gas refrigerant and a liquid liquid refrigerant. At this time, the liquid refrigerant is cooled by the evaporation of the refrigerant. In addition, as the configuration of the first expansion section, the first capillary tube 24 designed in accordance with the operation of the refrigeration cycle assumed in advance is used, but when it is necessary to consider the load fluctuation of the refrigeration cycle, The throttle amount may be varied according to a predetermined algorithm using a movable expansion mechanism capable of varying the throttle amount, and may be controlled so as to optimize or stabilize the operation cycle of the refrigeration cycle.

そして、気液分離器18の気体状のガス冷媒は、気液分離器18から中間圧冷媒流路26を通って、コンプレッサ21の中間圧部21c(すなわち、第1圧縮部21aと第2圧縮部21bとの間の部分)に供給される。その際に、中間圧冷媒流路26を流れるガス冷媒は第1キャピラリーチューブ24を流れる冷媒と熱交換部27で熱交換を行い、第1キャピラリーチューブ24を流れる冷媒の冷却を向上させている。また、気液分離器18とコンプレッサ21の中間圧部21cを接続する中間圧冷媒流路26には、ガス冷媒の逆流(コンプレッサ21の停止時など)を防止する逆止弁28が設けられている。尚、コンプレッサ21にケース内部を中間圧に設計しているものを用いる場合は、中間圧冷媒流路26をコンプレッサ21のケース内にガス冷媒が供給できるように構成すればよい。このとき、第1圧縮部21aの吐出はケース内となり第2圧縮部21bの吸い込みはケース内となっている。   The gaseous gas refrigerant in the gas-liquid separator 18 passes through the intermediate-pressure refrigerant flow path 26 from the gas-liquid separator 18 and passes through the intermediate pressure portion 21c (that is, the first compression portion 21a and the second compression portion) of the compressor 21. To the portion 21b). At that time, the gas refrigerant flowing in the intermediate pressure refrigerant flow path 26 exchanges heat with the refrigerant flowing in the first capillary tube 24 in the heat exchanging unit 27, thereby improving the cooling of the refrigerant flowing in the first capillary tube 24. In addition, a check valve 28 is provided in the intermediate pressure refrigerant flow path 26 that connects the gas-liquid separator 18 and the intermediate pressure portion 21c of the compressor 21 to prevent a reverse flow of gas refrigerant (such as when the compressor 21 is stopped). Yes. In addition, when using the compressor 21 whose case interior is designed to have an intermediate pressure, the intermediate pressure refrigerant flow path 26 may be configured to supply gas refrigerant into the case of the compressor 21. At this time, the discharge of the first compression unit 21a is in the case, and the suction of the second compression unit 21b is in the case.

一方、気液分離器18の液冷媒は、第2膨張部である第2キャピラリーチューブ31で減圧された後蒸発器16に流入して蒸発する。この際、冷媒は蒸発器16周囲の空気を冷却しながら気化(蒸発)して冷却作用を奏する。この後、再びコンプレッサ21に吸い込まれ冷凍サイクルを循環することになる。さらに、蒸発器16からコンプレッサ21に流れる冷媒は、第2キャピラリーチューブ31を流れる冷媒と熱交換部33で熱交換を行い、蒸発器16へ供給される液冷媒の冷却を向上させている。尚、第2膨張部となる第2キャピラリーチューブ31も前記した第1膨張部と同様に設計されるものであり、また、同様に可動式の膨張機構に置き換えることができるものである。   On the other hand, the liquid refrigerant in the gas-liquid separator 18 is depressurized by the second capillary tube 31 which is the second expansion portion, and then flows into the evaporator 16 and evaporates. At this time, the refrigerant evaporates (evaporates) while cooling the air around the evaporator 16 and exhibits a cooling action. Thereafter, it is sucked into the compressor 21 again and circulated through the refrigeration cycle. Further, the refrigerant flowing from the evaporator 16 to the compressor 21 exchanges heat with the refrigerant flowing through the second capillary tube 31 at the heat exchanging unit 33, thereby improving the cooling of the liquid refrigerant supplied to the evaporator 16. The second capillary tube 31 serving as the second expansion portion is also designed in the same manner as the first expansion portion described above, and can be similarly replaced with a movable expansion mechanism.

そして、蒸発器16の冷却作用で冷却された空気は冷気となり、送風機17により冷気流路13を通って貯蔵室3に送風されて庫内を循環する。   Then, the air cooled by the cooling action of the evaporator 16 becomes cold air, and is blown by the blower 17 through the cold air flow path 13 to the storage chamber 3 and circulates in the warehouse.

冷蔵庫1はこの様に構成されているので、膨張部を第1キャピラリーチューブ24および第2キャピラリーチューブ31の二段で構成することができるとともに、気液分離器18を断熱箱体2の背面側の蒸発器16の近傍に位置する断熱壁2aに内蔵し機械室11からの熱の侵入を抑制し、また蒸発器16から断熱箱体2外へ漏れる冷気を利用することができる。したがって、冷凍サイクルの2段目膨張(減圧)効率を向上させ冷却量を増加させることができるとともに、気液分離器18を最適に配置することができる。
また、冷凍サイクルの各機器の設計は作動冷媒に二酸化炭素を用いて行なっている。その結果、図2のp−h線図では作動領域が亜臨界であるが、周囲温度によっては作動領域が超臨界に至る場合もある。尚、作動冷媒は二酸化炭素に限らず他の類似する冷媒を用いることも可能である。
Since the refrigerator 1 is configured in this way, the expansion portion can be configured in two stages of the first capillary tube 24 and the second capillary tube 31, and the gas-liquid separator 18 is arranged on the back side of the heat insulating box 2. It is built in the heat insulating wall 2a located in the vicinity of the evaporator 16 to suppress intrusion of heat from the machine room 11, and cool air leaking out of the heat insulating box 2 from the evaporator 16 can be used. Therefore, the second-stage expansion (decompression) efficiency of the refrigeration cycle can be improved and the amount of cooling can be increased, and the gas-liquid separator 18 can be optimally arranged.
In addition, each refrigeration cycle device is designed using carbon dioxide as a working refrigerant. As a result, in the ph diagram of FIG. 2, the operating region is subcritical, but depending on the ambient temperature, the operating region may become supercritical. The working refrigerant is not limited to carbon dioxide, and other similar refrigerants can be used.

また、気液分離器18の配置の変形例として、気液分離器18の周囲を断熱材で覆って、機械室11に配置することも可能である。この様に、気液分離器18を断熱材で覆うことにより周囲から断熱し、周囲温度の高い機械室11に配置しても、冷凍サイクルの効率が低下することを防止することができる。なお、従来、気液分離器が断熱材で覆われることは無かった。   Further, as a modified example of the arrangement of the gas-liquid separator 18, the gas-liquid separator 18 can be disposed in the machine room 11 by covering the periphery with a heat insulating material. In this way, even if the gas-liquid separator 18 is covered with a heat insulating material to be insulated from the surroundings and disposed in the machine room 11 having a high ambient temperature, it is possible to prevent the efficiency of the refrigeration cycle from being lowered. Conventionally, the gas-liquid separator has not been covered with a heat insulating material.

さらに、冷蔵庫の冷凍サイクルは、二段の膨張部を具備していれば、適宜変更可能であり、その冷凍サイクルの一変形例について、図5、図6を用いて説明する。
この図5に図示する変形例は、図1に図示する実施例と、熱交換部の個数および配置が異なっており、図5に図示する変形例では、1個の熱交換部36を具備し、この熱交換部36が第1キャピラリーチューブ24を流れる冷媒と、蒸発器16からコンプレッサ21に流れる冷媒とを熱交換させている。
Furthermore, the refrigeration cycle of the refrigerator can be appropriately changed as long as it has a two-stage expansion section, and a modified example of the refrigeration cycle will be described with reference to FIGS.
The modification shown in FIG. 5 is different from the embodiment shown in FIG. 1 in the number and arrangement of the heat exchange units. The modification shown in FIG. 5 includes one heat exchange unit 36. The heat exchanging unit 36 exchanges heat between the refrigerant flowing through the first capillary tube 24 and the refrigerant flowing from the evaporator 16 to the compressor 21.

また、この図6に示す変形例は、図1に図示する実施例と、熱交換部の個数および配置が異なっており、図6に図示する変形例では、1個の熱交換部37を具備し、この熱交換部37が放熱器23から出る冷媒と蒸発器16からコンプレッサ21に流れる冷媒とを熱交換させている。この際、夫々の冷媒の流れが対向するように構成されている。   Further, the modification shown in FIG. 6 differs from the embodiment shown in FIG. 1 in the number and arrangement of the heat exchange units, and the modification shown in FIG. 6 includes one heat exchange unit 37. The heat exchanging unit 37 exchanges heat between the refrigerant coming out of the radiator 23 and the refrigerant flowing from the evaporator 16 to the compressor 21. At this time, the refrigerant flows are configured to face each other.

以上、本発明の実施例を詳述したが、本発明は、前記実施例に限定されるものではなく、特許請求の範囲に記載された本発明の要旨の範囲内で、種々の変更を行うことが可能である。本発明の変更例を下記に例示する。
(1)実施例においては、気液分離器は蒸発器の背面側に位置する断熱壁内に配置されているが、他の断熱壁に配置することも可能である。
As mentioned above, although the Example of this invention was explained in full detail, this invention is not limited to the said Example, A various change is performed within the range of the summary of this invention described in the claim. It is possible. Examples of modifications of the present invention are illustrated below.
(1) In the embodiment, the gas-liquid separator is disposed in the heat insulating wall located on the back side of the evaporator, but may be disposed on another heat insulating wall.

(2)実施例においては、コンプレッサは二段圧縮であるが、気液分離器の気体状の冷媒を中間圧で戻すことができるならば、コンプレッサの形式や構造は適宜選択可能である。例えば、単一の圧縮部を有するがシリンダー又はローターハウジングの中間圧部に位置する場所へガスインジェクションが可能なインジェクションポートを備える構造のコンプレッサであっても良い。
(3)冷蔵庫の貯蔵室の形式、個数や配置は適宜変更可能である。たとえば、冷蔵室、冷凍室、氷温室、チルド、製氷室および野菜室などを適宜箇所に、適宜の個数配置することができる。
(2) In the embodiment, the compressor is two-stage compression. However, if the gaseous refrigerant of the gas-liquid separator can be returned at an intermediate pressure, the type and structure of the compressor can be selected as appropriate. For example, it may be a compressor having a single compression portion but having an injection port capable of gas injection into a location located at an intermediate pressure portion of a cylinder or rotor housing.
(3) The type, number and arrangement of the refrigerator storage room can be changed as appropriate. For example, an appropriate number of refrigeration rooms, freezing rooms, ice greenhouses, chilled, ice making rooms, vegetable rooms, and the like can be arranged at appropriate locations.

(4)実施例においては、膨張部はキャピラリーチューブで構成されているが、膨張弁で構成することも可能である。 (4) In the embodiment, the inflating part is constituted by a capillary tube, but it can also be constituted by an expansion valve.

冷蔵庫の冷凍サイクルの膨張部を第1膨張部および第2膨張部の2段設け、この第1膨張部と第2膨張部との間に気液分離器を設けて、この気液分離器で気体状のガス冷媒と液体状の液冷媒に分け、ガス冷媒をコンプレッサの中間圧部に戻すとともに、膨張部を2段にした際に設けられる気液分離器を断熱材で覆って断熱し、冷蔵庫の冷凍サイクルの冷却能力を向上させることができる。したがって、冷却能力を要求される冷蔵庫に適用することが最適である。   The expansion part of the refrigerating cycle of the refrigerator is provided with two stages of a first expansion part and a second expansion part, and a gas-liquid separator is provided between the first expansion part and the second expansion part. Dividing into gaseous gas refrigerant and liquid liquid refrigerant, returning the gas refrigerant to the intermediate pressure part of the compressor and covering the gas-liquid separator provided when the expansion part is made in two stages with a heat insulating material, The cooling capacity of the refrigeration cycle of the refrigerator can be improved. Therefore, it is optimal to apply to refrigerators that require cooling capacity.

図1は本発明における冷蔵庫の冷凍サイクルの冷媒回路図である。FIG. 1 is a refrigerant circuit diagram of a refrigeration cycle of a refrigerator in the present invention. 図2は図1の冷凍サイクルの P-h線図である。FIG. 2 is a Ph diagram of the refrigeration cycle of FIG. 図3は冷蔵庫の断面図である。FIG. 3 is a sectional view of the refrigerator. 図4は冷蔵庫の斜視図である。FIG. 4 is a perspective view of the refrigerator. 図5は冷凍サイクルの変形例である。FIG. 5 shows a modification of the refrigeration cycle. 図6は冷凍サイクルの変形例である。FIG. 6 shows a modification of the refrigeration cycle.

符号の説明Explanation of symbols

1 冷蔵庫
2 断熱箱体(冷蔵庫本体)
2a 断熱壁
16 蒸発器
18 気液分離器
21 コンプレッサ
21c コンプレッサの中間圧部
23 放熱器
24 第1キャピラリーチューブ(第1膨張部)
31 第2キャピラリーチューブ(第2膨張部)
1 Refrigerator 2 Insulation box (refrigerator body)
2a Heat insulation wall 16 Evaporator 18 Gas-liquid separator 21 Compressor 21c Intermediate pressure part 23 of compressor 23 Radiator 24 1st capillary tube (1st expansion part)
31 2nd capillary tube (2nd expansion part)

Claims (12)

本体を断熱箱体で構成し、コンプレッサから吐出される高温高圧の冷媒が、放熱器、膨張部、蒸発器を順次循環してコンプレッサに戻る冷凍サイクルを具備し、この冷凍サイクルの蒸発器での冷媒の蒸発作用を用いて前記断熱箱体の区画される庫内を冷却すると共に、
前記膨張部を第1膨張部、気液分離器、および第2膨張部を順次直列に接続した直列回路で構成し、
前記気液分離器中のガス冷媒を前記コンプレッサの中間圧部に供給し、
かつ、前記気液分離器を断熱材で覆うことを特徴とする冷蔵庫。
The main body is composed of a heat insulating box, and a high-temperature and high-pressure refrigerant discharged from the compressor has a refrigeration cycle that sequentially circulates through the radiator, expansion section, and evaporator and returns to the compressor. While cooling the inside of the compartment where the heat insulating box is partitioned using the evaporating action of the refrigerant,
The inflating part is constituted by a series circuit in which a first inflating part, a gas-liquid separator, and a second inflating part are sequentially connected in series,
Supplying the gas refrigerant in the gas-liquid separator to the intermediate pressure part of the compressor;
And the said gas-liquid separator is covered with a heat insulating material, The refrigerator characterized by the above-mentioned.
前記気液分離器が、前記断熱箱体の背面側を成す断熱材の中に配置されていることを特徴とする請求項1記載の冷蔵庫。 The refrigerator according to claim 1, wherein the gas-liquid separator is disposed in a heat insulating material forming a back side of the heat insulating box. 前記気液分離器が、前記蒸発器近傍の断熱材の中に配置されていることを特徴とする請求項2記載の冷蔵庫。 The refrigerator according to claim 2, wherein the gas-liquid separator is disposed in a heat insulating material in the vicinity of the evaporator. 前記コンプレッサは単一ケース内に圧縮要素を直列に2段接続した2段圧縮の構成を備えると共に、前記圧縮要素間の中間圧部に前記気液分離器からのガス冷媒を供給することを特徴とする請求項1乃至請求項3のいずれか1項記載の冷蔵庫。 The compressor includes a two-stage compression configuration in which two compression elements are connected in series in a single case, and supplies the gas refrigerant from the gas-liquid separator to an intermediate pressure portion between the compression elements. The refrigerator according to any one of claims 1 to 3. 前記冷凍サイクルを循環する冷媒は二酸化炭素、又は二酸化炭素を含有する冷媒であることを特徴とする請求項4記載の冷蔵庫。 The refrigerator according to claim 4, wherein the refrigerant circulating in the refrigeration cycle is carbon dioxide or a refrigerant containing carbon dioxide. 前記冷凍サイクルの第1膨張部又は第2膨張部の少なくとも一方をキャピラリーチューブで構成することを特徴とする請求項5記載の冷蔵庫。 6. The refrigerator according to claim 5, wherein at least one of the first expansion section and the second expansion section of the refrigeration cycle is configured by a capillary tube. 前記冷凍サイクルの第1膨張部及び第2膨張部の両方をキャピラリーチューブで構成することを特徴とする請求項5記載の冷蔵庫。 6. The refrigerator according to claim 5, wherein both the first expansion section and the second expansion section of the refrigeration cycle are configured by capillary tubes. 前記気液分離器を前記コンプレッサより上方に配置することを特徴とする請求項5記載の冷蔵庫。 6. The refrigerator according to claim 5, wherein the gas-liquid separator is disposed above the compressor. 前記放熱器は放熱作用を有する複数の熱交換器に分割されて構成されていることを特徴とする請求項5記載の冷蔵庫。 6. The refrigerator according to claim 5, wherein the heat radiator is divided into a plurality of heat exchangers having a heat radiation action. 第1の膨張部中の冷媒と前記ガス冷媒とを熱交換させる構成を備えることを特徴とする請求項6又は請求項7記載の冷蔵庫。 The refrigerator according to claim 6 or 7, comprising a configuration for exchanging heat between the refrigerant in the first expansion section and the gas refrigerant. 第2の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えることを特徴とする請求項6又は請求項7記載の冷蔵庫。 The refrigerator according to claim 6 or 7, further comprising a configuration for exchanging heat between the refrigerant in the second expansion section and the refrigerant discharged from the evaporator. 第1の膨張部中の冷媒と前記蒸発器から出た冷媒とを熱交換させる構成を備えることを特徴とする請求項6又は請求項7記載の冷蔵庫。
The refrigerator according to claim 6 or 7, further comprising a structure for exchanging heat between the refrigerant in the first expansion section and the refrigerant discharged from the evaporator.
JP2004068381A 2004-03-11 2004-03-11 Refrigerator Pending JP2005257149A (en)

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JP2010526985A (en) * 2007-05-14 2010-08-05 キャリア コーポレイション Refrigerant vapor compression system with flash tank economizer
JP2010181090A (en) * 2009-02-05 2010-08-19 Mitsubishi Electric Corp Gas liquid separator and refrigerating cycle device mounted with the same
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JP2007263487A (en) * 2006-03-29 2007-10-11 Sanyo Electric Co Ltd Refrigerating device
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JP2007263488A (en) * 2006-03-29 2007-10-11 Sanyo Electric Co Ltd Refrigerating device
JP2010531423A (en) * 2006-12-29 2010-09-24 キャリア コーポレイション Economizer heat exchanger
US8312737B2 (en) 2006-12-29 2012-11-20 Carrier Corporation Economizer heat exchanger
JP2010526985A (en) * 2007-05-14 2010-08-05 キャリア コーポレイション Refrigerant vapor compression system with flash tank economizer
JP2010181090A (en) * 2009-02-05 2010-08-19 Mitsubishi Electric Corp Gas liquid separator and refrigerating cycle device mounted with the same
JP2010210145A (en) * 2009-03-10 2010-09-24 Mitsubishi Electric Corp Gas-liquid separator and refrigerating cycle device mounted with the same
CN101776358A (en) * 2010-03-02 2010-07-14 浙江大学 Varied concentration mixed working medium auto-cascade refrigerator
EP2690376A1 (en) * 2012-07-24 2014-01-29 LG Electronics, Inc. Refrigerating cycle and refrigerator having the same
US9625181B2 (en) 2012-07-24 2017-04-18 Lg Electronics Inc. Refrigerator cycle system and refrigerator having the same including a gas-liquid separator and a liquid refrigerant remover
CN114183941A (en) * 2021-12-14 2022-03-15 珠海格力电器股份有限公司 Refrigerating system, control method and refrigerating equipment
CN114183941B (en) * 2021-12-14 2022-09-20 珠海格力电器股份有限公司 Refrigerating system, control method and refrigerating equipment

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