KR20040082457A - Heat exchanging accumulator - Google Patents

Heat exchanging accumulator Download PDF

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Publication number
KR20040082457A
KR20040082457A KR1020030016982A KR20030016982A KR20040082457A KR 20040082457 A KR20040082457 A KR 20040082457A KR 1020030016982 A KR1020030016982 A KR 1020030016982A KR 20030016982 A KR20030016982 A KR 20030016982A KR 20040082457 A KR20040082457 A KR 20040082457A
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South Korea
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pressure side
side refrigerant
pipe
low pressure
refrigerant
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KR1020030016982A
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Korean (ko)
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KR100950153B1 (en
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장길상
오세균
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한라공조주식회사
대한냉열공업 (주)
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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
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/006Accumulators
    • 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
    • F25B41/00Fluid-circulation arrangements
    • F25B41/40Fluid line arrangements
    • 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
    • F25B2400/051Compression system with heat exchange between particular parts of the system between the accumulator and another part of the cycle

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE: A heat exchange accumulator is provided to reduce the manufacturing cost by separating gas and liquid while exchanging heat at the same time. CONSTITUTION: A heat exchange accumulator includes a body cylinder(10), an upper cap(20) combined with an upper part of the body cylinder, a lower cap(30) combined with a lower part of the body cylinder, and a high pressure side refrigerant pipe(40) contained in the body cylinder. A low pressure side refrigerant inlet pipe(21) is combined with the upper cap, and a low pressure side refrigerant outflow pipe(31) is combined wit the lower cap, wherein one end(32) of the low pressure side refrigerant outflow pipe is extended to the inside of the body cylinder. The high pressure side refrigerant pipe is formed by winding a refrigerant tube(41) several times. A low pressure side refrigerant flowed into through the low pressure side refrigerant inlet pipe flows downward in association with the refrigerant tube of the high pressure side refrigerant pipe, exchanging heat with a high pressure side refrigerant flowing in the refrigerant tube. Only gaseous refrigerant among the low pressure side refrigerant accumulated at a bottom of an accumulator is moved out through the low pressure side refrigerant outflow pipe.

Description

열교환 어큐물레이터{HEAT EXCHANGING ACCUMULATOR}Heat exchange accumulator {HEAT EXCHANGING ACCUMULATOR}

본 발명은 열교환 어큐물레이터(Accumulator)에 관한 것으로, 특히 열교환과 동시에 냉매의 기액(氣液)분리가 이루어지는 구조의 열교환 어큐물레이터에 관한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchange accumulator, and more particularly, to a heat exchange accumulator having a structure in which gas-liquid separation of a refrigerant is performed simultaneously with heat exchange.

일반적으로 냉방을 위한 공조장치에서, 냉매는 압축기, 응축기, 팽창밸브, 증발기를 순환하는 냉동사이클을 순환는데, 압축기에 의해 임계상태를 초과하는 초임계상태로 압축되는 냉동사이클을 초임계(超臨界) 냉동사이클이라고 부른다.In general, in an air conditioner for cooling, a refrigerant circulates a refrigeration cycle circulating a compressor, a condenser, an expansion valve, and an evaporator, and supercritical the refrigeration cycle compressed by the compressor to a supercritical state exceeding a threshold state. It is called a refrigeration cycle.

상기 초임계 냉동사이클에 있어서는, 냉매가 압축된 이후에 대기 중으로 방열하는 과정에서 상변화를 겪지 않으므로 이때의 방열장치를 응축기 대신 가스냉각기로 불리운다.In the supercritical refrigeration cycle, since the phase change does not occur in the process of radiating heat into the atmosphere after the refrigerant is compressed, the heat radiating device at this time is called a gas cooler instead of a condenser.

도1은 초임계 냉동사이클의 p-h선도이다. 도1에 도시한 바와 같이, 기본 냉동사이클은 1 →2 →3 →4 과정을 순환하게 되는데, 냉방효과는 증발과정인 4 →1과정의 엔탈피(Enthalpy) 차이(△h1)에 따라 결정된다.1 is a p-h diagram of a supercritical refrigeration cycle. As shown in Figure 1, the basic refrigeration cycle is cycled 1 → 2 → 3 → 4, the cooling effect is determined according to the enthalpy difference (Δh1) of the process 4 → 1 evaporation process.

이러한 초임계 냉동사이클의 냉방성능을 향상시키기 위하여, 압축기로 들어가는 냉매와 응축기로부터 나오는 냉매사이에 열교환을 위한 열교환기를 설치하는 경우가 있다.In order to improve the cooling performance of such a supercritical refrigeration cycle, a heat exchanger for heat exchange may be installed between the refrigerant entering the compressor and the refrigerant coming out of the condenser.

이때의 냉동사이클은 1' →2' →3' →4'로 순환하게 되고, 냉방 성능은 4' →1과정의 엔탈피 차이(△h2)가 되어 상기의 엔탈피차이(△h1)보다 증가하게 된다.At this time, the refrigerating cycle is circulated from 1 '→ 2' → 3 '→ 4', and the cooling performance becomes enthalpy difference (△ h2) of 4 '→ 1 process, which is higher than the enthalpy difference (△ h1). .

또한, 압축성능을 향상시키기 위하여 기체상태의 냉매만을 압축기로 보내기 위한 어큐물레이터를 추가적으로 포함하는 경우도 있다.In addition, the accumulator may further include an accumulator for sending only a gaseous refrigerant to the compressor in order to improve compression performance.

도2는, 상기와 같이 열교환기와 어큐물레이터가 설치되는 종래의 초임계 냉동사이클의 계통도이다.2 is a system diagram of a conventional supercritical refrigeration cycle in which a heat exchanger and an accumulator are installed as described above.

도시한 바와 같이, 종래의 초임계 냉동사이클에는, 증발기로부터 나온 냉매로부터 기액을 분리하는 어큐물레이터와, 가스냉각기로부터 나온 냉매와 어큐물레이터로부터 나온 냉매사이에 열교환을 시키기 위한 열교환기가 설치된다.As shown, a conventional supercritical refrigeration cycle is provided with an accumulator for separating gas liquid from a refrigerant from an evaporator, and a heat exchanger for exchanging heat between a refrigerant from a gas cooler and a refrigerant from an accumulator.

이러한 종래의 초임계 냉동사이클을 구현하는 공조장치에 있어서, 도2에 도시한 바와 같이, 기액을 분리하는 어큐물레이터와 열교환을 위한 열교환기가 별개의 부품으로 설치되는 경우에는 제조원가가 상승하고 배관의 구성이 복잡하게 되는 문제점이 있었다.In the conventional air conditioning apparatus for implementing a supercritical refrigeration cycle, as shown in FIG. 2, when the accumulator separating gas and the heat exchanger for heat exchange are installed as separate parts, the manufacturing cost increases and There was a problem that the configuration is complicated.

또한, 일본특허공보 제1998-019421호에는 상기 어큐물레이터와 열교환기를 하나의 부품으로 구현한 열교환 어큐물레이터를 개시하고 있으나, 상기 열교환 어큐물레이터는 열교환 효율이 떨어지는 문제점이 있었으며, 냉매 중에 포함된 윤활유가 열교환 어큐물레이터의 내부에 축적되고 압축기에 유입되지 않음으로 인하여, 압축기의 효율이 떨어지거나 시징(Seizing) 등의 고장이 발생하는 경우가 있었다.In addition, Japanese Patent Application Laid-Open No. 1998-019421 discloses a heat exchange accumulator in which the accumulator and the heat exchanger are implemented as one component, but the heat exchange accumulator has a problem of inferior heat exchange efficiency and is included in the refrigerant. Since the lubricated oil accumulates inside the heat exchange accumulator and does not flow into the compressor, there is a case where the efficiency of the compressor decreases or a failure such as seizing occurs.

본 발명은 상기와 같은 문제점을 해결하기 위하여 안출된 것으로, 열교환과 동시에 기액분리가 가능하여 제조원가가 절감되고, 배관의 구성이 간단하게 되며,열교환 효율이 우수하고, 열교환 어큐물레이터에 축적되는 윤활유를 압축기에 적절하게 공급하는 구조의 열교환 어큐물레이터를 제공하는데 목적이 있다.The present invention has been made in order to solve the above problems, it is possible to separate the gas-liquid and heat exchange at the same time to reduce the manufacturing cost, simplify the configuration of the pipe, excellent heat exchange efficiency, the lubricating oil accumulated in the heat exchange accumulator It is an object of the present invention to provide a heat exchange accumulator having a structure in which is properly supplied to a compressor.

도1은, 초임계 냉동싸이클의 p-h선도이다.1 is a p-h diagram of a supercritical refrigeration cycle.

도2는, 종래의 초임계 냉동싸이클의 계통도이다.2 is a system diagram of a conventional supercritical refrigeration cycle.

도3은, 본 발명에 따른 열교환 어큐물레이터의 측단면도이다.3 is a side cross-sectional view of a heat exchange accumulator according to the present invention.

도4(a)는 도3의 원형배플의 평면도이고, 도4(b)는 도4(a)의 A-A 단면도이다.Fig. 4A is a plan view of the circular baffle of Fig. 3, and Fig. 4B is a sectional view taken along line A-A of Fig. 4A.

도5(a)는, 도1의 점선부분의 측단면도이고, 도5(b)는 스트레이너의 사시도이다.Fig. 5A is a side cross-sectional view of the dotted line in Fig. 1, and Fig. 5B is a perspective view of the strainer.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

10... 바디실린더(Body Cylinder), 20... 상부캡,10 ... Body Cylinder, 20 ... Upper Cap,

21... 저압측 냉매 유입파이프, 30... 하부캡,21 ... low pressure refrigerant inlet pipe, 30 ... lower cap,

31... 저압측 냉매 유출파이프, 40... 고압측 냉매관,31 ... low pressure refrigerant pipe, 40 high pressure refrigerant pipe,

41... 냉매튜브, 42... 소경부,41 refrigerant tube, 42 small diameter,

43... 대경부, 50... 원형배플(Baffle),43 ... large neck, 50 ... round baffle,

51... 유출홈, 60... 원통배플,51 ... spilled groove, 60 ... cylindrical baffle,

70... 윤활유공급부, 71... 오목부,70 ... lubricant supply, 71 ... recess,

72... 윤활유구멍, 73... 스트레이너(Strainer).72 ... Lube hole, 73 ... Strainer.

상기 목적을 달성하기 위해 본 발명에 따른 열교환 어큐물레이터는,In order to achieve the above object, a heat exchange accumulator according to the present invention,

바디실린더와; 상기 바디실린더의 상부에 결합되는 상부캡과; 상기 바디실린더의 하부에 결합되는 하부캡과; 상기 바디실린더의 내부에 수용되는 고압측 냉매관을 포함하는데,Body cylinders; An upper cap coupled to an upper portion of the body cylinder; A lower cap coupled to the lower portion of the body cylinder; It includes a high-pressure side refrigerant pipe accommodated in the body cylinder,

상기 상부캡에는 저압측 냉매 유입파이프가 결합되고, 상기 하부캡에는 저압측 냉매 유출파이프가 그 일단부가 상기 바디실린더의 내부까지 연장되도록 설치되며, 상기 고압측 냉매관은 냉매튜브가 수회 권취되어 형성되어,A low pressure side refrigerant inlet pipe is coupled to the upper cap, and a low pressure side refrigerant outlet pipe is installed at the lower cap such that one end thereof extends into the body cylinder, and the high pressure side refrigerant pipe is formed by winding a refrigerant tube several times. Became,

상기 저압측 냉매 유입파이프를 통하여 유입된 저압측 냉매는 상기 고압측 냉매관의 냉매튜브를 따라 아래쪽으로 유동하면서 상기 냉매튜브의 내부를 유동하는 고압측 냉매와 열교환되고, 상기 어큐물레이터의 하부에 축적된 저압측 냉매 중 기체상태의 냉매만이 상기 저압측 냉매 유출파이프를 통하여 유출되는 것을 특징으로 한다.The low pressure side refrigerant introduced through the low pressure side refrigerant inlet pipe exchanges heat with the high pressure side refrigerant flowing inside the refrigerant tube while flowing downward along the refrigerant tube of the high pressure side refrigerant pipe, Among the accumulated low pressure side refrigerants, only gaseous refrigerants are discharged through the low pressure side refrigerant outlet pipe.

또한, 상기 고압측 냉매관은, 냉매튜브가 2중으로 나선방향으로 권취되어 직경이 작은 소경부와 직경이 큰 대경부를 형성하는 것을 특징으로 한다.The high-pressure side refrigerant pipe is characterized in that the refrigerant tube is wound in a double direction in a spiral direction to form a small diameter portion having a small diameter and a large diameter portion having a large diameter.

또한, 상기 고압측 냉매관의 중앙에는 수직방향으로 하부가 개방된 원통배플이 설치되는 것이 바람직하다.In addition, it is preferable that a cylindrical baffle having an open lower portion in the vertical direction is installed at the center of the high-pressure side refrigerant pipe.

또한, 상기 상부캡과 바디하우징 사이에는 원형배플이 개재되고, 상기 원형배플에는 다수의 유출홈이 형성되는데, 상기 유출홈은 경사지도록 형성되고, 상기 고압측 냉매관의 소경부와 대경부 사이에 위치하도록 형성되는 것이 바람직하다.In addition, a circular baffle is interposed between the upper cap and the body housing, and a plurality of outflow grooves are formed in the round baffle, and the outflow grooves are formed to be inclined, between the small diameter portion and the large diameter portion of the high-pressure side refrigerant pipe. It is preferably formed to be located.

또한, 상기 하부캡과 결합된 저압측 냉매 유출파이프에는, 상기 유출파이프의 외주에 형성된 오목부와; 상기 오목부에 대응하는 유출파이프에 형성된 1개 이상의 윤활유구멍을 포함하는 윤활유공급부가 형성되며,In addition, the low-pressure side refrigerant outflow pipe coupled to the lower cap, the recess formed on the outer periphery of the outflow pipe; A lubricating oil supply part including at least one lubricating oil hole formed in the outflow pipe corresponding to the recess is formed,

상기 오목부에는 메시(Mesh)가 형성된 스트레이너가 설치되는 것이 바람직하다.Preferably, the recess is provided with a strainer on which a mesh is formed.

이하에서는 도면을 참조하여 본 발명에 따른 열교환 어큐물레이터의 실시예를 상세하게 설명한다.Hereinafter, with reference to the drawings will be described in detail an embodiment of the heat exchange accumulator according to the present invention.

도3은 본 발명에 따른 열교환 어큐물레이터의 측단면도이고, 도4는 도3의 원형배플의 평면도와 측단면도이며, 도5는 도3의 점선부분의 단면도와 스트레이너의 사시도이다.3 is a side cross-sectional view of the heat exchange accumulator according to the present invention, FIG. 4 is a plan view and a side cross-sectional view of the circular baffle of FIG. 3, and FIG. 5 is a cross-sectional view and a perspective view of a strainer of FIG.

본 발명에 따른 열교환 어큐물레이터는, 도3에 도시한 바와 같이, 바디실린더(10)와, 상기 바디실린더(10)의 상부에 결합되는 상부캡(20)과; 상기 바디실린더(10)의 하부에 결합되는 하부캡(30); 및 상기 바디실린더(10)의 내부에 수용되는 고압측 냉매관(40)을 포함한다.The heat exchange accumulator according to the present invention, as shown in Figure 3, the body cylinder 10, the upper cap 20 is coupled to the upper portion of the body cylinder 10; A lower cap 30 coupled to the lower portion of the body cylinder 10; And a high pressure side refrigerant pipe 40 accommodated in the body cylinder 10.

상기 상부캡(20)은 상기 바디실린더(10)에 용접 등의 수단으로 결합되는데, 그 상부에는 저압측의 냉매, 즉 증발기로부터의 냉매가 유입되는 저압측 냉매 유입파이프(21)가 상기 상부캡(20)의 내부와 소통되도록 결합된다.The upper cap 20 is coupled to the body cylinder 10 by means of welding or the like, and a lower pressure refrigerant inlet pipe 21 through which a refrigerant from a low pressure side, that is, a refrigerant from an evaporator, is introduced thereon. It is coupled to communicate with the interior of the (20).

또한, 상기 하부캡(30)도 상기 바디실린더(10)에 용접 등의 수단으로 결합되는데, 그 하부에는 저압측의 냉매가 유출되는 저압측 냉매 유출파이프(31)가 상기 하부캡(30)의 내부와 소통되도록 결합된다. 상기 저압측 냉매 유출파이프(31)의 일단부(32)는, 도3에 도시한 바와 같이, 상기 바디실린더(10)의 내부까지 연장되도록 설치되어 기체상태의 냉매만이 상기 유출파이프(31)를 통하여 유출되도록 한다.In addition, the lower cap 30 is also coupled to the body cylinder 10 by means of welding or the like, and a lower pressure side refrigerant outflow pipe 31 through which the refrigerant from the low pressure side flows out of the lower cap 30. Combined to communicate internally One end portion 32 of the low pressure side refrigerant outlet pipe 31 is installed to extend to the inside of the body cylinder 10, as shown in FIG. Allow outflow through.

상기 고압측 냉매관(40)의 내부에는 고압측의 냉매, 즉 가스냉각기를 통과한 냉매가 유동하는데 상기 고압측 냉매관(40)은, 도3에 도시한 바와 같이, 냉매튜브(41)가 수회 권취되어 형성된다. 즉, 상기 냉매튜브(41)가 2중으로 나선방향으로 권취되어 직경이 작은 소경부(42)와 직경이 큰 대경부(43)를 형성하게 되는데, 상기 냉매튜브(41)가 권취형성됨으로써 고압측 냉매가 저압측의 냉매와 열교환하는 열교환 길이가 연장되어 열교환 효율이 상승하게 된다. 여기에서, 상기 소경부(42)와 대경부(43)는 소정의 거리만큼 이격되어서 공간을 형성하게 된다.Inside the high-pressure side refrigerant pipe 40, a high-pressure side refrigerant, that is, a refrigerant passing through the gas cooler flows. The high-pressure side refrigerant pipe 40, as shown in Figure 3, the refrigerant tube 41 is It is wound up several times and formed. That is, the refrigerant tube 41 is wound in a double direction in a spiral direction to form a small diameter portion 42 having a small diameter and a large diameter portion 43 having a large diameter, and the refrigerant tube 41 is wound to form a high pressure side. The heat exchange length in which the refrigerant exchanges heat with the refrigerant on the low pressure side is extended, thereby increasing the heat exchange efficiency. Here, the small diameter portion 42 and the large diameter portion 43 are spaced by a predetermined distance to form a space.

도3에서는 상기 냉매튜브(41)가 2중으로 권취된 것을 도시하였지만, 1열로 권취되거나, 3열 이상으로 권취되는 것도 무방하다.3 shows that the refrigerant tube 41 is wound in two, but may be wound in one row or wound in three or more rows.

또한, 상기 상부캡(20)과 바디하우징(10) 사이에는 원형배플(50)이 개재되는데, 상기 원형배플(50)에는 원주방향으로 다수(도4(a)에서는 4개)의 유출홈(51)이 형성된다.In addition, a circular baffle 50 is interposed between the upper cap 20 and the body housing 10, and the circular baffle 50 has a plurality of outflow grooves (four in FIG. 4A) in the circumferential direction. 51) is formed.

상기 원형배플(50)은 상기 상부캡(20)과 바디실린더(10) 사이를 차단하고, 저압측 냉매 유입파이프(21)를 통해 상부캡(20) 내로 유입된 냉매를 상기 유출홈(51)을 통해서 바디실린더(10)의 내부로 유입되도록 한다.The circular baffle 50 cuts off between the upper cap 20 and the body cylinder 10, and the refrigerant flowing into the upper cap 20 through the low pressure refrigerant inlet pipe 21 is discharged into the outlet 51. Through the body cylinder 10 to be introduced.

상기 유출홈(51)은, 도4(b)에 도시한 바와 같이, 경사지도록 형성되는 것이 바람직한데, 상기 유출홈(51)은 상기 상부캡(20) 내로 유입된 저압측의 냉매가 나선운동을 하면서 바디실린더(10)의 내부로 유출되도록 하여, 나선방향으로 권취된 상기 고압측 냉매관(40)의 냉매튜브(41)를 따라 유동하는 것을 돕게 된다.The outflow groove 51 is preferably formed to be inclined, as shown in Figure 4 (b), the outflow groove 51 is a spiral movement of the refrigerant on the low pressure side flowed into the upper cap 20 By allowing it to flow into the interior of the body cylinder 10, it helps to flow along the refrigerant tube 41 of the high-pressure side refrigerant pipe 40 wound in a spiral direction.

상기 유출홈(51)은, 도3에 도시한 바와 같이, 고압측 냉매관(40)의 소경부(42)와 대경부(43) 사이에 위치하도록 형성되는 것이 바람직한데, 이는 상기 유출홈(51)을 통해 유출된 저압측 냉매가 상기 소경부(42)와 대경부(43) 사이의 공간에서 유동하여 열교환 면적이 증가되도록 하기 위한 것이다.As shown in FIG. 3, the outlet groove 51 is preferably formed between the small diameter portion 42 and the large diameter portion 43 of the high-pressure side refrigerant pipe 40. The low pressure side refrigerant flowing out through the 51) flows in the space between the small diameter portion 42 and the large diameter portion 43 to increase the heat exchange area.

또한, 상기 고압측 냉매관(40)의 내부에는 원통배플(60)이 추가적으로 설치되는 것이 바람직하다. 상기 원통배플(60)은, 그 하부가 개방되게 형성된 실린더 형상의 파이프로, 그 상단부는 상기 원형배플(50)의 하면과 접하도록 설치된다.In addition, it is preferable that the cylindrical baffle 60 is additionally installed inside the high-pressure side refrigerant pipe 40. The cylindrical baffle 60 is a cylindrical pipe formed so that its lower part is opened, and an upper end thereof is installed to contact the lower surface of the circular baffle 50.

상기 원통배플(60)은, 상기 고압측 냉매관(40)의 냉매튜브(41)를 따라 유동하는 저압측 냉매가 고압측 냉매관(40)의 중앙으로 스며들어 낙하하는 것을 방지하여, 저압측 냉매가 고압측 냉매관(40)을 따라 충분한 열교환이 이루어지도록 한다.The cylindrical baffle 60 prevents the low pressure side refrigerant flowing along the refrigerant tube 41 of the high pressure side refrigerant pipe 40 from penetrating into the center of the high pressure side refrigerant pipe 40 and falling down, thereby reducing the low pressure side. The refrigerant is allowed to undergo sufficient heat exchange along the high pressure side refrigerant pipe (40).

상기 하부캡(30)의 하부에 위치한 저압측 냉매 유출파이프(31)에는, 점선으로 도시한 바와 같이, 윤활유공급부(70)가 형성되는데, 상기 윤활유공급부(70)는 윤활유를 저장하기 위하여 유출파이프(31)의 일부분을 내측으로 함몰시켜 형성한 오목부(71)와 상기 오목부(71)에 대응하는 유출파이프(31)에 형성된 1개 이상의(도5에서는 1개만 도시)의 윤활유구멍(72)을 포함한다(도5(a) 참조).In the low pressure side refrigerant outlet pipe 31 positioned below the lower cap 30, a lubricating oil supply part 70 is formed as shown by a dotted line, and the lubricating oil supply part 70 is configured to store the lubricating oil in order to store the lubricating oil. Lubricating oil holes 72 of one or more (only one in FIG. 5) formed in the recess 71 formed by recessing a part of the 31 inwardly and the outflow pipe 31 corresponding to the recess 71. ) (See Fig. 5 (a)).

또한, 상기 오목부(71)의 외주에는 메쉬(Mesh)가 형성된 스트레이너(73)가설치되는데(도5(b) 참조), 상기 스트레이너(73)는 상기 윤활유구멍(71)에 유입되는 윤활유 중의 이물질을 차단하는 한편, 상기 오목부(71)를 덮음으로써 상기 오목부(71)와 상기 스트레이너(73)로 형성된 공간에 윤활유가 저장되도록 한다.In addition, a strainer 73 having a mesh is formed on the outer circumference of the concave portion 71 (see FIG. 5 (b)), and the strainer 73 is in the lubricant oil flowing into the lubricant oil hole 71. While blocking the foreign matter, the concave portion 71 is covered so that the lubricant is stored in the space formed by the concave portion 71 and the strainer 73.

상기 윤활유공급부(70)는 압축기에 유입되는 저압측의 냉매에 윤활유를 공급하여 압축기가 원활히 구동되도록 한다.The lubricating oil supply unit 70 supplies lubricating oil to the low pressure side refrigerant flowing into the compressor so that the compressor is smoothly driven.

상기 실시예의 작동과정을 설명하면, 저압측 유입파이프(21)를 통하여 저압측의 냉매가 상부캡(20)의 내부로 유입되는 한편, 고압측 냉매관(40)에는 고압측 냉매가 유입되어 냉매튜브(41)의 내부로 유동하게 된다.Referring to the operation of the above embodiment, the low pressure side refrigerant flows into the upper cap 20 through the low pressure side inlet pipe 21, while the high pressure side refrigerant flows into the high pressure side refrigerant pipe 40. It flows into the tube 41.

상기 상부캡(10) 내부로 유입된 저압측 냉매는 원형배플(50)의 유출홈(51)을 통하여 바디실린더(10) 내부로 유입되어 고압측 냉매관(40)의 냉매튜브(41)를 따라 나선방향으로 유동하게 된다. 이 때 상기 유출홈(51)의 경사진 형상이 저압측 냉매의 나선운동을 유도한다.The low pressure refrigerant introduced into the upper cap 10 is introduced into the body cylinder 10 through the outflow groove 51 of the circular baffle 50 to cool the refrigerant tube 41 of the high pressure refrigerant tube 40. As a result, they flow in a spiral direction. At this time, the inclined shape of the outflow groove 51 induces a spiral motion of the low pressure side refrigerant.

상기 냉매튜브(41)를 따라 나선 유동하는 저압측 냉매는 상기 냉매튜브(41)의 내부에서 유동하는 고압측 냉매와 열교환하게 되고, 이 과정 동안에 저압측 냉매는 대부분 기화하게 된다. 이 때, 원통배플(60)은 상기 저압측 냉매가 고압측 냉매관(40)의 하부에 이르기 전에 중앙으로 스며드는 것을 차단하여 효과적인 열교환이 이루어지도록 한다.The low pressure side refrigerant flowing spirally along the refrigerant tube 41 is heat-exchanged with the high pressure side refrigerant flowing in the refrigerant tube 41, and during this process, the low pressure side refrigerant is mostly vaporized. At this time, the cylindrical baffle 60 prevents the low pressure side refrigerant from seeping into the center before reaching the lower portion of the high pressure side refrigerant pipe 40 so that effective heat exchange is achieved.

상기 고압측 냉매관(40)의 하부에 도달한 저압측 냉매는 하부캡(30)의 상면에 축적되는데, 상기 냉매 중의 윤활유는 비중 차이로 인하여 가장 아래쪽에 축적된다.The low pressure refrigerant reaching the lower portion of the high pressure refrigerant pipe 40 accumulates on the upper surface of the lower cap 30, and the lubricant oil in the refrigerant accumulates at the lowermost portion due to the difference in specific gravity.

상기 축적된 저압측 냉매 중 기체성분은 저압측 유출파이프(31)의 일단부(32)를 통하여 유출되며, 이 때 윤활유공급부(70)의 윤활유구멍(72)를 통하여 유출되는 저압측 냉매에 윤활유를 공급할 수가 있다.The gas component of the accumulated low pressure side refrigerant flows out through one end 32 of the low pressure side outlet pipe 31, and at this time, lubricant oil is supplied to the low pressure side refrigerant flowing out through the lubricating oil hole 72 of the lubricating oil supply unit 70. Can be supplied.

본 발명에 따른 열교환 어큐물레이터에 의하면, 열교환과 동시에 기액분리가 가능하여 제조원가가 절감되고, 배관의 구성이 간단하게 된다.According to the heat exchange accumulator according to the present invention, the gas-liquid separation can be performed simultaneously with the heat exchange, thereby reducing the manufacturing cost and simplifying the construction of the pipe.

또한, 고압측 냉매와 저압측 냉매의 열교환 길이를 증가시켜 열교환 효율이 우수하고, 열교환 어큐물레이터 내부에 축적되는 윤활유를 유출되는 저압측 냉매에 공급하여 압축기를 적절하게 윤활하게 된다.In addition, the heat exchange length between the high pressure refrigerant and the low pressure refrigerant is increased, so that the heat exchange efficiency is excellent, and the lubricating oil accumulated in the heat exchange accumulator is supplied to the low pressure refrigerant that flows out to lubricate the compressor properly.

Claims (8)

바디실린더(Body Cylinder,10)와; 상기 바디실린더(10)의 상부에 결합되는 상부캡(20)과; 상기 바디실린더(10)의 하부에 결합되는 하부캡(30)과; 상기 바디실린더(10)의 내부에 수용되는 고압측 냉매관(40)을 포함하는 열교환 어큐물레이터(Accumulator)에 있어서,A body cylinder 10; An upper cap 20 coupled to an upper portion of the body cylinder 10; A lower cap 30 coupled to the lower portion of the body cylinder 10; In the heat exchange accumulator (Accumulator) comprising a high-pressure side refrigerant pipe 40 accommodated in the body cylinder 10, 상기 상부캡(20)에는 저압측 냉매 유입파이프(21)가 결합되고, 상기 하부캡(30)에는 저압측 냉매 유출파이프(31)가 그 일단부(32)가 상기 바디실린더(10)의 내부까지 연장되도록 설치되며, 상기 고압측 냉매관(40)은 냉매튜브(41)가 수회 권취되어 형성되어,The low pressure side refrigerant inlet pipe 21 is coupled to the upper cap 20, and the low pressure side refrigerant outlet pipe 31 is connected to the lower cap 30 at one end 32 of the body cylinder 10. It is installed to extend to, the high-pressure side refrigerant pipe 40 is formed by winding the refrigerant tube 41 several times, 상기 저압측 냉매 유입파이프(21)를 통하여 유입된 저압측 냉매는 상기 고압측 냉매관(40)의 냉매튜브(41)를 따라 아래쪽으로 유동하면서 상기 냉매튜브(41)의 내부를 유동하는 고압측 냉매와 열교환되고, 상기 어큐물레이터의 하부에 축적된 저압측 냉매 중 기체상태의 냉매만이 상기 저압측 냉매 유출파이프(31)를 통하여 유출되는 것을 특징으로 하는 열교환 어큐물레이터.The low pressure side refrigerant introduced through the low pressure side refrigerant inlet pipe 21 flows downward along the refrigerant tube 41 of the high pressure side refrigerant pipe 40 and flows inside the refrigerant tube 41. And a gaseous refrigerant of the low pressure side refrigerant accumulated in the lower portion of the accumulator is discharged through the low pressure side refrigerant outlet pipe (31). 제1항에 있어서,The method of claim 1, 상기 고압측 냉매관(40)은, 냉매튜브(41)가 2중으로 나선방향으로 권취되어 직경이 작은 소경부(42)와 직경이 큰 대경부(43)를 형성하는 것을 특징으로 하는 열교환 어큐물레이터.The high-pressure side refrigerant pipe 40, the refrigerant tube 41 is wound in a double direction in a spiral direction to form a small diameter portion 42 having a small diameter and a large diameter portion 43 having a large diameter Raider. 제1항에 있어서,The method of claim 1, 상기 상부캡(20)과 바디하우징(30) 사이에는 원형배플(Baffle,50)이 개재되고, 상기 원형배플(50)에는 다수의 유출홈(51)이 형성되는 것을 특징으로 하는 열교환 어큐물레이터.A heat exchange accumulator, characterized in that a circular baffle (50) is interposed between the upper cap (20) and the body housing (30), and a plurality of outlet grooves (51) are formed in the circular baffle (50). . 제1항에 있어서,The method of claim 1, 상기 고압측 냉매관(40)의 중앙에는 수직방향으로 하부가 개방된 원통배플(60)이 설치되는 것을 특징으로 하는 열교환 어큐물레이터.Heat exchange accumulator, characterized in that the center of the high-pressure side refrigerant pipe (40) is provided with a cylindrical baffle (60), the lower portion of which is opened in the vertical direction. 제3항에 있어서,The method of claim 3, 상기 유출홈(51)은, 경사지도록 형성되는 것을 특징으로 하는 열교환 어큐물레이터.The outflow groove 51 is heat exchange accumulator, characterized in that formed to be inclined. 제3항에 있어서,The method of claim 3, 상기 유출홈(51)은, 상기 고압측 냉매관(40)의 소경부(42)와 대경부(43) 사이에 위치하도록 형성되는 것을 특징으로 하는 열교환 어큐물레이터.The outflow groove 51 is formed to be located between the small diameter portion 42 and the large diameter portion 43 of the high-pressure side refrigerant pipe (40). 제1항에 있어서,The method of claim 1, 상기 하부캡(30)과 결합된 저압측 냉매 유출파이프(31)에는, 상기 유출파이프(31)의 외주에 형성된 오목부(71)와; 상기 오목부(71)에 대응하는 유출파이프(31)에 형성된 1개이상의 윤활유구멍(72)을 포함하는 윤활유공급부(70)가 형성되는 것을 특징으로 열교환 어큐물레이터.The low pressure side refrigerant outflow pipe 31 coupled to the lower cap 30 includes a recess 71 formed on an outer circumference of the outflow pipe 31; And a lubricating oil supply part (70) comprising at least one lubricating oil hole (72) formed in the outflow pipe (31) corresponding to the recess (71). 제6항에 있어서,The method of claim 6, 상기 오목부(71)에는 메시(Mesh)가 형성된 스트레이너(Strainer,73)가 설치되는 것을 특징으로 하는 열교환 어큐물레이터.The recess 71 is provided with a strainer 73 having a mesh formed therein.
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CN109405593A (en) * 2017-08-18 2019-03-01 显示器生产服务株式会社 A kind of heat exchanger and its manufacturing method and heat exchange module and its manufacturing method

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KR101980640B1 (en) * 2017-08-17 2019-05-23 주식회사 디엠에스 Mist recovery apparatus and substrate processing system using the same
US11992835B2 (en) * 2020-08-04 2024-05-28 Universal Analyzers Inc. Distillation probes and methods for sampling and conditioning a fluid

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