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KR100750375B1 - Combined cooling and heating system using 2-pass line wastewater heat recovery machine and heat pump - Google Patents

Combined cooling and heating system using 2-pass line wastewater heat recovery machine and heat pump Download PDF

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KR100750375B1
KR100750375B1 KR1020070040780A KR20070040780A KR100750375B1 KR 100750375 B1 KR100750375 B1 KR 100750375B1 KR 1020070040780 A KR1020070040780 A KR 1020070040780A KR 20070040780 A KR20070040780 A KR 20070040780A KR 100750375 B1 KR100750375 B1 KR 100750375B1
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water
heat
temperature
storage tank
hot water
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왕화식
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왕화식
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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
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • 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
    • F25B27/00Machines, plants or systems, using particular sources of energy
    • F25B27/02Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • 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
    • F25B30/00Heat pumps
    • 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
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D20/00Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
    • F28D20/0034Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using liquid heat storage material
    • 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
    • F25B2400/24Storage receiver heat
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

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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)
  • Combustion & Propulsion (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

본 발명은 냉수 및 온수를 이용한 시설에 알맞도록 열교환된 최적의 열원을 수냉식 히트펌프의 증발기 및 축열탱크에 공급함으로서, 냉수 및 온수를 이용한 시설에 사용할 수 있는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템에 관한 것이다. 본 발명의 주요구성은 원수가 저장되는 원수공급처와; 중온의 폐수가 저장되는 폐수공급처와; 원수가 냉각된 냉수가 저장되는 축냉탱크와; 원수공급처의 원수 및 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시켜 1차 온수로 변환시키고, 또한 폐열공급처의 폐수와 축냉탱크의 냉수의 혼합수를 원수공급처의 원수와 상호 열교환시켜 원수를 일정한 온도를 갖는 기준수로 변환시키는 폐수열회수기와; 폐수열회수기를 통과하면서 온도가 증가된 1차 온수가 저장되는 축열탱크와; 축열탱크에 저장된 1차 온수를 응축기로 유입시켜서 내부의 고온의 냉매와 열교환시켜 1차 온수의 온도를 고온으로 상승시켜 2차 온도로 변환시키고, 기준수를 증발기로 유입시켜 원수의 온도를 저온으로 하강시켜 냉수로 변환시키는 히트펌프와; 히트펌프를 통과한 고온의 2차 온수를 저장하는 온수탱크;를 포함하며 증발기를 통과한 냉수는 축냉탱크에 저장되는 것을 특징으로 한다.The present invention supplies an optimal heat source heat-exchanged to a facility using cold water and hot water to an evaporator and a heat storage tank of a water-cooled heat pump, thereby using a 2-pass line wastewater heat recovery unit and a heat pump that can be used in a facility using cold water and hot water. It relates to a cooling and heating combined use system. The main configuration of the present invention and the raw water supply source in which raw water is stored; A wastewater supply source for storing wastewater of medium temperature; A cold storage tank for storing cold water in which raw water is cooled; By exchanging the raw water of the raw water supply source and the waste water of the waste heat supply source mutually, the temperature of the raw water is increased to convert it into primary hot water. A wastewater heat recovery unit for converting the waste water into reference water having a constant temperature; A heat storage tank storing primary hot water having an increased temperature while passing through the waste water heat recovery unit; The primary hot water stored in the heat storage tank is introduced into the condenser and heat exchanged with the internal high temperature refrigerant to raise the temperature of the primary hot water to a high temperature and convert it to a secondary temperature. A heat pump which is lowered and converted into cold water; And a hot water tank storing high temperature secondary hot water passing through the heat pump, wherein the cold water passing through the evaporator is stored in the cold storage tank.

Description

2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템 {COOLING OR HEATING COMBINED SYSTEM USING 2-PASSLINE WASTE WATER EXCHANGER AND HEAT PUMP}COOLING OR HEATING COMBINED SYSTEM USING 2-PASSLINE WASTE WATER EXCHANGER AND HEAT PUMP}

도 1은 종래의 냉동기를 이용한 폐열회수시스템을 도시한 개략도 1 is a schematic diagram showing a waste heat recovery system using a conventional freezer

도 2는 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템 개략도.Figure 2 is a schematic diagram of a combined heating and cooling system using a heat pump and a two-pass line wastewater heat recovery of the present invention.

도 3은 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템의 난방시 흐름도.Figure 3 is a flow chart during heating of a combined heating and cooling system using a heat pump and a two-pass line wastewater heat recovery of the present invention.

도 4는 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템의 냉방시 흐름도.Figure 4 is a flow chart for cooling the cooling and cooling system using a two-pass line wastewater heat recovery and heat pump of the present invention.

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

1 : 온수공급처 2 : 폐수공급처1: hot water supply source 2: waste water supply source

3 : 폐수열회수기 4 : 제1폐열교환부3: wastewater heat recovery unit 4: the first waste heat exchanger

5 : 제2폐열교환부 6 : 히트펌프5: second waste heat exchanger 6: heat pump

7 : 응축기 8 : 축열탱크7: condenser 8: heat storage tank

9 : 온수탱크 9 : 온수를 이용한 시설9: hot water tank 9: facility using hot water

12 : 증발기 13 : 축냉탱크12: evaporator 13: cold storage tank

14 : 냉수를 이용한 시설14: Facility using cold water

본 발명은 2패스라인 폐수열회수기를 이용한 냉난방 겸용 히트펌프 시스템에 관한 것으로, 보다 상세하게는 냉수 및 온수를 이용한 시설조건에 알맞도록 열교환된 최적의 열원을 수냉식 히트펌프의 증발기 및 축열탱크에 공급함으로서, 사계절 냉수 및 온수를 이용한 시설에 사용할 수 있는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템에 관한 것이다.
이하, 본 발명에서 사용된 원수, 폐수, 1차 온수, 2차 온수, 기준수 및 2차 냉수는 각각 다음과 같이 정의한다. "원수'는 폐수열회수기에 공급되지 전의 물을 의미하고, "폐수"는 고온의 폐열을 갖는 물을 의미하고, "1차 온수"는 원수가 폐수열회수기에서 폐수와 열교환되어 온도가 증가된 물을 의미하고, "2차 온수"는 1차온수가 히트펌프의 응축기에서 가열되어 1차 온수보다 온도가 증가된 물을 의미하고, "기준수"는 원수가 폐수열회수기에서 폐수+냉수의 혼합수와 열교환하면서 약 12℃의 온도를 갖는 물을 의미하며, "냉수"는 기준수가 히트펌프의 증발기에서 냉각된 물을 의미한다.
The present invention relates to a combined heat and cooling heat pump system using a two-pass line wastewater heat recovery device, and more particularly, by supplying an optimal heat source heat-exchanged to a facility condition using cold water and hot water to an evaporator and a heat storage tank of a water-cooled heat pump. The present invention relates to a two-pass line wastewater heat recovery system that can be used for facilities using cold water and hot water for four seasons, and a heating / cooling system using a heat pump.
Hereinafter, raw water, waste water, primary hot water, secondary hot water, reference water and secondary cold water used in the present invention are defined as follows. "Raw water" means water before it is supplied to the wastewater heat recovery unit, "waste water" means water having high temperature waste heat, and "primary hot water" means water whose temperature is increased by heat exchange with waste water in the wastewater heat recovery machine. "Secondary hot water" refers to water in which the primary hot water is heated in the condenser of the heat pump to increase the temperature than the primary hot water, and "reference water" refers to the mixed water of wastewater + cold water in the wastewater heat recovery machine. By heat exchange means water having a temperature of about 12 ° C., and “cold water” means the water cooled in the evaporator of the heat pump.

일반적으로 목욕탕 및 사우나(찜질방) 등에서는 사용되고 버려지는 폐수로부터 폐수열회수기를 이용하여 열을 회수하여 에너지 절감을 하고 있다. 도 1은 대한민국등록특허 제10-574275호인 종래의 냉동기를 이용한 폐수열회수시스템의 개략도이다.In general, in baths and saunas (Jjimjilbang), energy is recovered by recovering heat from wastewater used and discarded using wastewater heat recovery machines. 1 is a schematic diagram of a waste water heat recovery system using a conventional freezer of Korea Patent No. 10-574275.

도 1에 도시된 바와 같이, 대한민국등록특허 제10-574275호의 폐수열회수시스템은 원수의 급수원(106)을 냉동기(102)의 증발기(117)에 연결하고, 상기 증발기(117)는 폐수열회수기(101)에 연결되며, 유입된 원수를 적정한 온도까지 하강시키도록 순환시킨다. 또한, 증발기(117)는 유체도관에 의해 압축기(114)에 연결되어 증발기를 통해 잠열을 가진 냉매를 고온 고압의 냉매로 압축함으로써 큰 열량을 갖 는다. 또한 압축기(114)는 도관에 의해 응축기(115)에 연결된다. 이와 같이 압축기(114)를 통과한 고온 고압의 냉매가 상기 응축기(115)를 통과하면서 폐수열회수기(101)를 통과한 원수와 열교환을 하게 되고, 열을 축적한 원수는 순환펌프(111)를 통해 축열탱크(103)에 저장되게 된다. 응축기(115)를 통과한 냉매는 팽창변(121)을 통과하면서 저온 저압으로 상변화를 일으킨 후에, 증발기(117)로 이동하여 원수를 냉각시킨다. 또한, 상기 폐수열회수기(101)는 목욕탕(120)등의 폐수 공급원(107)과 연결되어 폐열을 유입하게 된다. 이때, 상기 증발기(117)를 순환한 원수는 상기 폐수열회수기(101)를 통과하는 고온의 폐열로부터 열을 흡수하여 열을 가진 폐수으로 배출되고, 상기 폐열은 열을 빼앗기 후 폐열출구(108)를 통해 저온의 폐열로 배출되게 된다.1, the wastewater heat recovery system of the Republic of Korea Patent No. 10-574275 is connected to the water supply source 106 of the raw water to the evaporator 117 of the refrigerator 102, the evaporator 117 is a wastewater heat recovery machine ( 101) and circulates the incoming raw water to the appropriate temperature. In addition, the evaporator 117 is connected to the compressor 114 by a fluid conduit to have a large amount of heat by compressing the refrigerant having latent heat into the refrigerant of high temperature and high pressure through the evaporator. The compressor 114 is also connected to the condenser 115 by conduits. In this way, the high temperature and high pressure refrigerant passing through the compressor 114 passes through the condenser 115 to exchange heat with the raw water passing through the wastewater heat recovery 101, and the raw water accumulating heat is transferred through the circulation pump 111. The heat storage tank 103 is to be stored. The refrigerant passing through the condenser 115 causes a phase change at low temperature and low pressure while passing through the expansion valve 121, and then moves to the evaporator 117 to cool the raw water. In addition, the wastewater heat recovery unit 101 is connected to the wastewater supply source 107 such as the bath 120 to introduce waste heat. At this time, the raw water circulated through the evaporator 117 absorbs heat from the waste heat of high temperature passing through the waste water heat recovery unit 101 and is discharged to waste water having heat, and the waste heat is taken out of the waste heat outlet 108 after the heat is taken out. Through the waste heat of low temperature will be discharged.

상기 폐수열회수기(101)를 통과한 열원의 일부는 냉수분배기(113)를 통해 냉수로 목욕탕(120)에 공급될 수 있고, 나머지 일부는 상기 응축기(115)로 보내져서 열을 흡수하게 된다. 상기 축열탱크(103)에 저장된 온수는 온수탱크에 저장되어 목욕탕으로 공급되는 시스템이다.A portion of the heat source passing through the wastewater heat recovery unit 101 may be supplied to the bath 120 by cold water through the cold water distributor 113, and the other part may be sent to the condenser 115 to absorb heat. The hot water stored in the heat storage tank 103 is stored in the hot water tank is supplied to the bath.

상기와 같이 종래의 냉동기를 이용한 폐열회수시스템은 폐열을 냉동기(102)의 증발기(117)내부로 유입하는 대신에 열원을 증발기(117)로 유입하여 순환시키는 것과, 증발기(117)의 내부를 순환한 열원을 폐수열회수기(101) 내부로 통과시켜 순수 온수만을 생산하는 시스템으로, 목욕탕 및 사우나(찜질방)에서 냉방 및 난방(바닥난방시설 포함)은 전혀 사용할 수 없으며, 또한 사계절 온수생산 시 열원 공급온도가 5℃(동절기)~25℃(하절기)의 온도변화에 따라 용량제어가 안됨으로써, 냉동기 의 빈번한 고장 및 성능저하(또는 원하는 온수생산 안됨)가 발생되며, 하절기의 경우 폐열온도 34℃와 열원온도 25℃의 열교환 되어 얻어진 열량이 거의 없기 때문에 폐수열회수기의 역할이 상당히 미미하다. 그리고 기존의 냉동기의 경우 응축온도가 50℃인 R-22냉매를 사용함으로서, 일반적으로 목욕탕 및 사우나(찜질방)에서 요구하는 60℃의 온수를 공급하지 못함으로써, 보조열원인 보일러가 필요하다는 단점이 있다.As described above, in the waste heat recovery system using the conventional refrigerator, instead of introducing the waste heat into the evaporator 117 of the refrigerator 102, the heat source is introduced into the evaporator 117 and circulated, and the inside of the evaporator 117 is circulated. A system that produces only pure hot water by passing a heat source into the wastewater heat recovery machine 101. Cooling and heating (including floor heating facilities) are not available in baths and saunas. When capacity is not controlled according to the temperature change of 5 ℃ (winter) ~ 25 ℃ (summer), frequent failure of the refrigerator and deterioration of performance (or no desired hot water production) occurs.In summer, waste heat temperature 34 ℃ and heat source Since little heat is obtained by heat exchange at a temperature of 25 ° C, the role of the wastewater heat recovery machine is very small. In the case of the conventional refrigerator using the R-22 refrigerant with a condensation temperature of 50 ℃, it does not supply the hot water of 60 ℃ generally required in baths and saunas (jjimjilbang), the disadvantage of the need for a boiler as an auxiliary heat source have.

따라서, 현재까지 단일시스템을 이용하여 냉수 및 온수를 이용한 시설겸용 및 보조열원이 없는 시스템은 없으며, 냉동기 및 열교환기의 성능 향상과 빈번한 열교환기의 고장을 줄여 획기적인 에너지 절감을 크게 할 수 있는 시스템에 대한 요구가 지속적으로 있어왔다. Therefore, to date, there is no system without facility and auxiliary heat source using cold water and hot water by using a single system, and it is possible to improve the performance of refrigerator and heat exchanger and to reduce the breakdown of frequent heat exchanger. There has been a continuous demand.

본 발명은 상기와 같은 문제점들을 해결하기 위한 것으로, 냉수 및 온수를 이용한 시설 겸용 및 보조열원이 없는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템을 제공함에 있다.The present invention is to solve the above problems, to provide a combined cooling and heating system using a heat pump and a two-pass line waste water heat recovery system without the combined use of auxiliary water source and cold water and hot water.

본 발명의 다른 목적은 폐열을 회수 및 제거함으로서 최적의 열원을 응축기 및 증발기에 공급하여 열원의 온도에 관계없이 사계절 사용할 수 있는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템을 제공함에 있다. Another object of the present invention is to provide a cooling and heating combined system using a two-pass line wastewater heat recovery and heat pump that can be used for four seasons regardless of the temperature of the heat source by supplying the optimal heat source to the condenser and evaporator by recovering and removing the waste heat.

본 발명의 또다른 목적은 열원을 폐수열회수기를 거쳐 축열탱크에 공급된 중열원을 수냉식 히트펌프 응축기로 공급되어 냉매의 고온. 고압의 가스와 열교환된 중열원을 고열원을 생산하여 축열탱크에 다시 저장하여 온수를 이용한 시설에서 난방을 할 수 있는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템을 제공함에 있다.Still another object of the present invention is to supply a medium heat source supplied to a heat storage tank via a wastewater heat recovery device to a water-cooled heat pump condenser and a high temperature of a refrigerant. The present invention provides a dual-pass wastewater heat recovery system and a heating / cooling system using a heat pump that can heat a high-heat gas and heat-exchanged heavy heat source to produce a high heat source and store it in a heat storage tank for heating in a hot water facility.

본 발명의 또 다른 목적은 2패스라인 폐열회수기에서 냉방 및 난방에 최적의 온도로 열교환시킴으로써 빈번한 고장 및 성능 저하를 방지할 수 있는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템을 제공함에 있다.It is another object of the present invention to provide a dual-pass wastewater heat recovery system and a heating / cooling system using a heat pump that can prevent frequent failures and deterioration by exchanging heat at an optimal temperature for cooling and heating in the 2-pass line waste heat recovery system. .

상기와 같은 목적을 달성하기 위한 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템은, 원수가 저장되는 원수공급처와; 중온의 폐수가 저장되는 폐수공급처와; 상기 원수가 냉각된 냉수가 저장되는 축냉탱크와; 상기 원수공급처의 원수 및 상기 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시켜 1차 온수로 변환시키고, 또한 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합수를 상기 원수공급처의 원수와 상호 열교환시켜 상기 원수를 일정한 온도를 갖는 기준수로 변환시키는 폐수열회수기와; 상기 폐수열회수기를 통과하면서 온도가 증가된 1차 온수가 저장되는 축열탱크와; 상기 축열탱크에 저장된 1차 온수를 응축기로 유입시켜서 내부의 고온의 냉매와 열교환시켜 1차 온수의 온도를 고온으로 상승시켜 2차 온도로 변환시키고, 상기 기준수를 증발기로 유입시켜 원수의 온도를 저온으로 하강시켜 냉수로 변환시키는 히트펌프와; 상기 히트펌프를 통과한 고온의 2차 온수를 저장하는 온수탱크;를 포함하며 상기 증발기를 통과한 냉수는 상기 축냉탱크에 저장되는 것을 특징으로 한다.In order to achieve the above object, a two-pass line wastewater heat recovery system and a heating / cooling system using a heat pump include: a raw water supply source for storing raw water; A wastewater supply source for storing wastewater of medium temperature; A cold storage tank in which the cold water in which the raw water is cooled is stored; The raw water of the raw water supply source and the waste water of the waste heat supply source are mutually heat exchanged to increase the temperature of the raw water to convert it into primary hot water, and further, the mixed water of the waste water of the waste heat supply source and the cold water of the cold storage tank is mixed with the raw water of the raw water supply source. A wastewater heat recovery unit converting the raw water into reference water having a constant temperature by heat exchange with each other; A heat storage tank storing primary hot water having an increased temperature while passing through the waste water heat recovery unit; The primary hot water stored in the heat storage tank is introduced into a condenser to exchange heat with a high temperature refrigerant therein, thereby increasing the temperature of the primary hot water to a high temperature, converting it into a secondary temperature, and introducing the reference water into an evaporator to reduce the temperature of raw water. A heat pump that is lowered to a low temperature and converted into cold water; And a hot water tank for storing high temperature secondary hot water passing through the heat pump, wherein the cold water passing through the evaporator is stored in the cold storage tank.

바람직하게, 상기 폐수열회수기는 상기 원수공급처의 원수 및 상기 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시키는 제1폐열교환부와; 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합수를 상기 원수공급처의 원수와 상호 열교환시키는 제2폐수열교환부를 포함하는 것을 특징으로 한다.Preferably, the wastewater heat recovery unit includes: a first waste heat exchanger configured to increase the temperature of the raw water by mutually heat-exchanging the raw water of the raw water supply source and the wastewater of the waste heat supply source; And a second wastewater heat exchanger configured to mutually heat-exchange the mixed water of the wastewater of the waste heat supply source with the cold water of the cold storage tank.

바람직하게, 상기 원수공급처의 온도를 측정하는 제1온도센서와; 상기 제1온도센서에서 측정된 온도에 따라 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합비율을 조절하는 전자밸브를 더 포함하는 것을 특징으로 한다.Preferably, the first temperature sensor for measuring the temperature of the raw water supply destination; And a solenoid valve for controlling a mixing ratio of the wastewater of the waste heat supply destination and the cold water of the cold storage tank according to the temperature measured by the first temperature sensor.

바람직하게, 상기 축열탱크의 내부에서 수위를 측정하는 수위센서와; 상기 수위센서에서 측정된 수위가 최고수위이면 상기 축열탱크로 유입되는 1차 온수를 차단하는 차단밸브를 더 포함하는 것을 특징으로 한다.Preferably, the water level sensor for measuring the water level in the heat storage tank; If the water level measured by the water level sensor is the highest level, characterized in that it further comprises a shut-off valve for blocking the primary hot water flowing into the heat storage tank.

바람직하게, 상기 축열탱크의 내부에서 온도를 측정하는 제2온도센서를 더 포함하는 것을 특징으로 한다.Preferably, it further comprises a second temperature sensor for measuring the temperature in the heat storage tank.

바람직하게, 상기 응축기를 통과한 2차 온수가 기준온도 이상일 때에 상기 온수탱크로 이송되는 것을 특징으로 한다.Preferably, the secondary hot water passing through the condenser is characterized in that it is transferred to the hot water tank when the reference temperature or more.

바람직하게, 상기 온수탱크에 저장된 2차 온수는 난방시설에 공급되고, 상기 축냉탱크에 저장된 저온의 냉수는 냉방시설에 공급되는 것을 특징으로 한다.Preferably, the secondary hot water stored in the hot water tank is supplied to a heating facility, the cold water of low temperature stored in the storage tank is supplied to a cooling facility.

바람직하게, 상기 히트펌프는 수냉식 히트 또는 공랭식 히트펌프인 것을 특징으로 한다.Preferably, the heat pump is characterized in that the water-cooled heat or air-cooled heat pump.

도 2를 참조하여 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템에 대하여 자세히 살펴본다. 도 2는 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템 개략도이고, 도 3은 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템의 난방시 흐름도이며, 도 4는 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템의 냉방시 흐름도이다.With reference to Figure 2 looks at in detail with the two-pass line wastewater heat recovery and the combined heating and cooling system using a heat pump. 2 is a schematic diagram of a combined heating and cooling system using a two-pass wastewater heat recovery unit and a heat pump according to the present invention, and FIG. 3 is a flow chart of a heating and cooling system using a two-pass wastewater heat recovery unit and a heat pump according to the present invention. 2 is a flow chart for cooling the cooling and cooling system using a two-pass line wastewater heat recovery device and a heat pump of the present invention.

도 2에 도시된 바와 같이, 원수가 저장되는 원수공급처(1)와; 중온의 폐수가 저장되는 폐수공급처(2)와; 원수가 냉각된 냉수가 저장되는 축냉탱크(13)와; 상기 원수공급처의 원수 및 상기 폐열공급처(2)의 폐수를 상호 열교환시켜 원수의 온도를 증가시켜 1차 온수로 변환시키고, 또한 상기 원수공급처(1)의 원수 및 상기 폐열공급처(2)의 폐수와 상기 축냉탱크(13)의 냉수의 혼합수를 상호 열교환시켜 원수의 온도를 일정한 온도를 갖는 기준수로 변환시키는 폐수열회수기(3)와; 상기 폐수열회수기(3)를 통과하면서 온도가 증가된 1차 온수가 저장되는 축열탱크(8)와 상기 축열탱크(8)에 저장된 1차 온수를 응축기(7)로 유입시켜 내부의 고온의 냉매와 열교환시켜 1차 원수의 온도를 고온으로 상승시켜 2차 온수로 변환시키고, 상기 혼합수와 열교환된 기준수를 증발기(12)로 유입시켜 기준수의 온도를 저온으로 하강시켜 냉수로 변환시키는 히트펌프(6)와; 상기 히트펌프(6)를 통과한 고온의 2차 원수가 저장되는 온수탱크(9)로 이루어진다. 이때, 히트펌프(6)의 응축기(7)를 통과한 2차 온수의 온도가 기준 온도(60℃) 이하일 때에는 축열탱크(8)에 저장되어 순환되고, 기준 온도 이상일 때 온수탱크(9)로 이송되도록 설정할 수 있다.As shown in Figure 2, the raw water supply destination (1) for storing the raw water; A wastewater supply source (2) in which wastewater of medium temperature is stored; A cold storage tank 13 in which cold water cooled by raw water is stored; The raw water of the raw water supply source and the wastewater of the waste heat supply source 2 are mutually heat-exchanged to increase the temperature of the raw water to convert it into primary hot water, and furthermore, the raw water of the raw water supply source 1 and the wastewater of the waste heat supply source 2 and A wastewater heat recovery unit (3) for exchanging the mixed water of cold water of the cold storage tank (13) to convert the temperature of the raw water into reference water having a constant temperature; The heat storage tank 8 through which the waste water heat recoverer 3 is stored and the primary hot water of which temperature is increased is introduced to the condenser 7 by introducing the primary hot water stored in the heat storage tank 8 into a condenser 7. Heat pump to heat the temperature of the primary raw water to the high temperature to convert to the second hot water, the heat exchanged with the mixed water and the reference water exchanged into the evaporator 12 to lower the temperature of the reference water to low temperature to convert it into cold water (6); It consists of a hot water tank (9) for storing the high-temperature secondary raw water passing through the heat pump (6). At this time, when the temperature of the secondary hot water passing through the condenser 7 of the heat pump 6 is below the reference temperature (60 ° C.), it is stored and circulated in the heat storage tank 8, and when the temperature of the secondary hot water is higher than the reference temperature, it is transferred to the hot water tank 9. Can be set to be transported.

한편, 폐수열회수기(3)는 원수공급처의 원수 및 상기 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시켜 1차 온수로 변환시키는 제1폐열교환부(4)와 원수공급처의 원수 및 상기 폐열공급처(2)의 폐수와 상기 축냉탱크(13)의 냉수의 혼합수를 상호 열교환시켜 원수의 온도를 증가시켜 기준수로 변환시키는 제2폐수열교환부(5)로 이루어진다.Meanwhile, the wastewater heat recovery unit 3 exchanges heat between the raw water of the raw water supply source and the wastewater of the waste heat supply source to increase the temperature of the raw water and converts it into primary hot water, and the raw water and the waste heat of the raw water supply source. The second wastewater heat exchange part 5 converts the wastewater of the supply destination 2 and the mixed water of the cold water of the said cold storage tank 13 into mutually increasing the temperature of raw water, and converts it into a reference water.

또한, 원수공급처(1) 및 축열탱크(8)에는 온도를 측정하는 제1,2온도센서(56,38)가 부착되고, 상기 폐열공급처(2)의 폐수와 상기 축냉탱크(13)의 냉수의 혼합비율을 조절하기 위한 전자밸브(57,58)가 설치된다.In addition, the raw water supply unit 1 and the heat storage tank 8 are equipped with first and second temperature sensors 56 and 38 for measuring temperature, and the waste water of the waste heat supply unit 2 and the cold water of the cold storage tank 13. Solenoid valves (57, 58) for adjusting the mixing ratio of the.

또한, 축열탱크(8)의 내부에는 수위를 측정하는 수위센서(38)가 설치되고, 수위센서(38)에서 측정된 수위가 최고수위이면 상기 축열탱크(8)로 유입되는 1차 원수를 차단하는 차단밸브(39)와 축열탱크의 온도가 일정이상이면 온수탱크(9)로 배출시키는 압력펌프(42)가 더 설치된다.In addition, the water level sensor 38 for measuring the water level is installed inside the heat storage tank 8, and if the water level measured by the water level sensor 38 is the highest level, the primary raw water flowing into the heat storage tank 8 is blocked. If the temperature of the shut-off valve 39 and the heat storage tank is more than a predetermined pressure pump 42 for discharging to the hot water tank (9) is further installed.

이와 같이, 온수탱크(9)에 저장된 고온의 2차 원수는 난방시설(10)에 공급되고, 축냉탱크(13)에 저장된 저온의 냉수는 냉방시설(14)에 공급된다.As such, the high temperature secondary raw water stored in the hot water tank 9 is supplied to the heating facility 10, and the low temperature cold water stored in the storage cooling tank 13 is supplied to the cooling facility 14.

한편, 이러한 히트펌프(6)는 수냉식 히트펌프 또는 공냉식 히트펌프를 선택적으로 사용할 수 있다. 수냉식 히트펌프를 사용하면 여름철에 냉매의 온도가 높기 때문에 냉수의 온도를 낮추는데 효율이 낮으며, 공냉식 히트펌프를 사용하면 겨울철에 냉매의 온도가 너무 낮아 2차 온수의 온도를 높이는 효율이 낮아지는 문제가 있다.Meanwhile, the heat pump 6 may selectively use a water-cooled heat pump or an air-cooled heat pump. When water-cooled heat pump is used, the efficiency of lowering the temperature of cold water is low because the temperature of the refrigerant is high in summer, and when the air-cooled heat pump is used, the efficiency of raising the temperature of secondary hot water is low because the temperature of the refrigerant is too low in winter. There is.

이하, 본 발명에 따른 폐수열회수기를 이용한 수냉식 히트펌프의 동작에 대한 내용을 구체적으로 설명한다.Hereinafter, the details of the operation of the water-cooled heat pump using the waste water heat recovery according to the present invention will be described in detail.

(1) 온수생산 및 온수를 이용한 난방시설  (1) Hot water production and heating facilities using hot water

도 3에 도시된 바와 같이, 원수공급처(1)의 원수(동절기에는 약5℃이고, 환절기에는 약 15℃이며, 하절기에는 약 25℃의 온도를 갖는다.)는 제1도관(31)을 통해 폐수열회수기(3)의 제1폐열교환부(4)로 공급된다. 폐열공급처(2)의 약 32~34℃의 폐수는 제2도관(32)을 통해 폐수열회수기(3)의 제1폐열교환부(4)로 공급한다. 이에 따라 제1폐열교환부(4)에서 저온의 원수와 고온의 폐수가 서로 반대방향으로 진행하면서 제1도관(31)으로 공급된 원수와 열교환된다.As shown in FIG. 3, raw water of the raw water supply source 1 (about 5 ° C. in winter, about 15 ° C. in summer and about 25 ° C. in summer) is provided through the first conduit 31. It is supplied to the 1st waste heat exchange part 4 of the wastewater heat recovery machine 3. The wastewater at about 32 to 34 ° C. of the waste heat supply source 2 is supplied to the first waste heat exchanger 4 of the wastewater heat recovery machine 3 through the second conduit 32. Accordingly, in the first waste heat exchange unit 4, the raw water of the low temperature and the waste water of the high temperature travel in opposite directions to exchange heat with the raw water supplied to the first conduit 31.

제1폐열교환부(4)에서 서로 반대방향으로 진행하는 원수와 폐수는 열교환되며, 제1폐열교환부(4)를 통과한 온수는 온도가 증가된 1차 온수로서 제3도관(33)을 통해 축열탱크(8)에 저장된다. 제1폐열교환부(4)를 통과한 폐수는 온도가 감소되어 제4도관(34)을 통해 외부로 방류된다.In the first waste heat exchange unit 4, the raw water and the waste water flowing in opposite directions are exchanged with each other, and the hot water passing through the first waste heat exchange unit 4 is the primary hot water having an increased temperature. It is stored in the heat storage tank (8) through. The wastewater that has passed through the first waste heat exchanger 4 is reduced in temperature and discharged to the outside through the fourth conduit 34.

축열탱크(8)에 저장된 1차 온수는 제5도관(35)을 통해 수냉식 히트펌프(6)의 응축기(7)로 유입된다. 응축기(7) 수배관 입구로 유입된 30℃의 1차 온수는 히트펌프(6)의 냉매 배관에서 순환하는 냉매의 응축열(65℃)과 열교환되며, 열교환된 고온의 2차 온수는 제6도관(36)을 통해 축열탱크(8)에 다시 저장된다. 축열탱크(8)로 유입된 2차 온수는 축열탱크(8) 내의 1차 온수와 혼합되고 다시 히트펌프의 응축기(7)로 유입되어 열교환된다.Primary hot water stored in the heat storage tank (8) is introduced into the condenser (7) of the water-cooled heat pump (6) through the fifth conduit (35). The primary hot water at 30 ° C. introduced into the condenser (7) inlet is heat exchanged with the condensation heat (65 ° C.) of the refrigerant circulating in the refrigerant pipe of the heat pump (6). It is stored again in the heat storage tank (8) via (36). Secondary hot water introduced into the heat storage tank (8) is mixed with the primary hot water in the heat storage tank (8) and flows back into the condenser (7) of the heat pump to heat exchange.

이와 같이, 축열탱크와 응축기(7)를 반복적으로 순환되어 축열탱크의 내부의 온도가 약 60기준℃의 온도일 때에는 제7도관(37)을 통해 온수탱크(9)에 저장된다. 이때, 축열탱크(8)의 내부에서 수위를 측정하는 수위센서(38)에서 측정된 수위가 최고수위이면 차단밸브(39)가 오프(close)되어 제1폐열교환부(4)에서 축열탱크(8)로 유입되는 1차 온수가 차단된다. 또한, 응축기(7)에서 열교환된 2차 온수는 축열탱크(8)에 저장되지 않고 직접 온수탱크(9)에 저장될 수도 있다.As described above, the heat storage tank and the condenser 7 are repeatedly circulated to be stored in the hot water tank 9 through the seventh conduit 37 when the temperature of the heat storage tank is about 60 ° C. At this time, when the water level measured by the water level sensor 38 for measuring the water level in the heat storage tank 8 is the highest water level, the shutoff valve 39 is closed to close the heat storage tank (1) in the first waste heat exchanger (4). 8) The primary hot water flowing into is blocked. In addition, the secondary hot water heat exchanged in the condenser (7) may be stored directly in the hot water tank (9) instead of being stored in the heat storage tank (8).

온수탱크(9)에 저장된 2차 온수는 제8도관(40)을 통해 2차 온수가 사용되는 사용처(11)에 공급되거나 또는 제9도관(41)을 통해 난방시설(10)로 공급되어 난방에 사용될 수 있다. Secondary hot water stored in the hot water tank (9) is supplied to the place of use (11) where secondary hot water is used through the eighth conduit (40) or the heating facility (10) through the ninth conduit (41) to heat Can be used for

이것은 기존의 폐수열회수기를 이용한 온수생산 시스템에서 온수를 이용한 난방시설에서 난방을 구현할 수 있다는 것과, 보조열원인 (유류, 가스)보일러를 제거할 수 있는 특징을 가지고 있다.This has the characteristics that heating can be realized in a heating facility using hot water in a hot water production system using a conventional wastewater heat recovery system, and that the auxiliary heat source (oil, gas) boiler can be removed.

(2) 냉수생산 및 냉수를 이용한 냉방시설(2) Cooling facilities using cold water production and cold water

도 4에 도시된 바와 같이, 원수공급처(1)의 원수는 제11도관(51)을 통해 폐수열회수기의 제2폐열교환부(5)로 공급된다. 그리고, 폐열공급처(2)에 연결된 제12도관(52)과 축냉탱크에 연결된 제13도관(53)이 서로 결합되어 고온의 폐수와 저온의 냉수가 혼합된 혼합수는 제14도관(54)을 통해 제2폐열교환부(5)로 공급된다. 한편, 원수와 혼합수는 제2폐열교환부(5)에서 서로 반대방향으로 진행하면서 원수가 약 12℃의 온도를 갖는 기준수가 되도록 열교환된다. 제2폐열교환부(5)를 통과한 기준수는 제14도관(55)을 통해 히트펌프의 증발기(12)로 유입된다.As shown in FIG. 4, the raw water of the raw water supply source 1 is supplied to the second waste heat exchanger 5 of the wastewater heat recovery unit through the eleventh conduit 51. In addition, the twelfth conduit 52 connected to the waste heat supply source 2 and the thirteenth conduit 53 connected to the cold storage tank are coupled to each other so that the mixed water in which the hot waste water and the cold cold water are mixed is connected to the fourteenth conduit 54. It is supplied to the second waste heat exchanger (5) through. On the other hand, the raw water and the mixed water is heat-exchanged so that the raw water is a reference water having a temperature of about 12 ℃ while proceeding in the opposite direction in the second waste heat exchange unit (5). The reference water passing through the second waste heat exchanger 5 is introduced into the evaporator 12 of the heat pump through the fourteenth conduit 55.

이때, 원수공급처(1)에 설치된 제1온도센서(56)에서 측정된 원수의 온도에 따라 제12도관(52)과 제13도관(53)에 설치된 전자밸브(57,58)를 조절하여 혼합되는 폐수와 냉수의 비율이 조절된다. 즉, 열원공급처에서 공급되는 원수의 온도는 동절기(5℃), 환절기(15℃), 하절기(25℃)이며, 계절별 온도가 다른 원수를 히트펌프의 증발기에 바로 공급하게 되면, 동절기의 경우 원수의 온도가 너무 낮아 온수가 생산되지 않으며, 하절기의 경우 원수의 온도가 너무 높아 증발기 과열 현상에 의하여 제품 고장을 유발한다. 따라서, 동절기 경우 제1온도센서(56)에 의하여 측정된 원수 온도가 5℃인 경우 12℃의 원수온도를 만들기 위하여 축냉탱크(13)에서 유입되는 전자밸브(58)를 닫고, 폐수공급처(2)에서 공급되는 유량을 제어하여 혼합수의 온도를 높일 수 있으며, 반대로 하절기 경우 제1온도센서(56)에 의하여 측정된 원수 온도가 25℃인 경우 12℃의 원수온도를 만들기 위하여 폐수공급처(2)의 전자밸브(57)를 차단하고, 축냉탱크(13)의 전자밸브(58)를 제어하여 혼합수의 온도를 내림으로써 열교환된 기준수의 온도를 유지할 수 있다.At this time, mixing and adjusting the solenoid valves (57, 58) installed in the twelfth conduit (52) and the thirteenth conduit (53) according to the temperature of the raw water measured by the first temperature sensor (56) installed in the raw water supply source (1) The ratio of waste water to cold water is controlled. That is, the temperature of the raw water supplied from the heat source supply source is winter (5 ℃), season (15 ℃), summer (25 ℃), and when raw water having different temperature is directly supplied to the evaporator of the heat pump, the raw water in winter The temperature of the water is too low to produce hot water, and in summer, the temperature of raw water is too high, causing product failure due to overheating of the evaporator. Therefore, in the winter, when the raw water temperature measured by the first temperature sensor 56 is 5 ° C, the solenoid valve 58 flowing from the cold storage tank 13 is closed to make the raw water temperature of 12 ° C, and the wastewater supply source 2 The temperature of the mixed water can be increased by controlling the flow rate supplied from the wastewater. On the contrary, when the raw water temperature measured by the first temperature sensor 56 is 25 ° C. in summer, the waste water supply source 2 By closing the solenoid valve 57 of the ()) and controlling the solenoid valve 58 of the cold storage tank 13, the temperature of the mixed water can be maintained by lowering the temperature of the mixed water.

히트펌프의 증발기(12)로 유입된 약 12℃의 기준수는 히트펌프(6)의 냉매 배관에서 순환하는 냉매의 증발열과 열교환되어 약 7℃로 냉각되며, 냉수는 제16도관(59)을 통해 축냉탱크(13)에 저장된다. 축냉탱크(13)에 저장된 냉수는 제17도관(60)을 통해 냉방시설(4)로 공급되거나 또는 제18도관(61)을 통해 원수공급처(1)로 제공된다.The reference water of about 12 ° C introduced into the evaporator 12 of the heat pump is heat-exchanged with the heat of evaporation of the refrigerant circulating in the refrigerant pipe of the heat pump 6 to cool to about 7 ° C, and the cold water passes through the sixteenth conduit 59. Through the storage tank 13 is stored. The cold water stored in the cold storage tank 13 is supplied to the cooling facility 4 through the seventeenth conduit 60 or the raw water supply source 1 through the eighteenth conduit 61.

한편, 냉수를 이용한 냉방시설(4)은 냉수를 유입하여 냉방시설 내부의 팬을 이용하여 냉방하는 장치이다. 이것은 기존의 온수만 생산하던 시스템에서 증발기에서 생산된 냉수를 축냉탱크로 저장하여 냉방을 할 수 있는 시스템을 구현할 수 있다.On the other hand, the cooling facility (4) using cold water is a device for cooling by using a fan inside the cooling facility by introducing cold water. This can realize a system capable of cooling by storing the cold water produced by the evaporator in the cold storage tank in the system that was only producing hot water.

이상에서 살펴본 바와 같이, 본 발명의 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템은 사계절 냉수 및 온수를 이용한 시설을 겸용으로 사용할 수 있으며, 수냉식 히트펌프를 이용하여 별도의 동력없이 냉방시설 및 장치를 이용한 냉난방 사용 및 온수를 이용 난방시설을 통해 난방을 할 수 있는 큰 이점이 있다. As described above, the two-pass line wastewater heat recovery unit and the cooling and heating system using the heat pump of the present invention can be used as a facility using the four seasons cold water and hot water, and using the water-cooled heat pump to cool the cooling facilities and There is a big advantage that can be heated by heating and heating using the device using the heating and heating using the device.

또한, 2패스라인 폐열회수기에서 냉방 및 난방에 최적의 온도로 열교환되기 때문에 지나친 온도 차이로 인한 빈번한 고장 및 성능 저하를 방지할 수 있는 장점이 있다.In addition, since the heat exchange at the optimum temperature for cooling and heating in the 2-pass line waste heat recovery machine, there is an advantage that can prevent frequent failures and performance degradation due to excessive temperature difference.

또한, 폐수열회수기를 거쳐 축열탱크에 공급된 중열원을 수냉식 히트펌프 응축기로 공급되어 냉매의 고온. 고압의 가스와 열교환된 중열원을 고열원을 생산하여 축열탱크에 순환되기 때문에 적정 온도까지 온도를 올릴 수 있는 장점이 있다.In addition, the heavy heat source supplied to the heat storage tank via the waste water heat recovery machine is supplied to the water-cooled heat pump condenser to obtain a high temperature of the refrigerant. Since the heavy heat source heat-exchanged with high pressure gas is circulated in the heat storage tank by producing a high heat source, there is an advantage of raising the temperature to an appropriate temperature.

또한, 이는 보조열원인 보일러가 필요 없으므로, 전기에너지 외에 별도의 에너지를 사용하지 않아 에너지 절감을 획기적으로 줄일 수 있다.In addition, since it does not require a boiler as an auxiliary heat source, it does not use a separate energy other than electrical energy can significantly reduce energy savings.

Claims (9)

원수가 저장되는 원수공급처와; A raw water supply source for storing raw water; 중온의 폐수가 저장되는 폐수공급처와; A wastewater supply source for storing wastewater of medium temperature; 상기 원수가 냉각된 냉수가 저장되는 축냉탱크와; A cold storage tank in which the cold water in which the raw water is cooled is stored; 상기 원수공급처의 원수 및 상기 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시켜 1차 온수로 변환시키고, 또한 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합수를 상기 원수공급처의 원수와 상호 열교환시켜 상기 원수를 일정한 온도를 갖는 기준수로 변환시키는 폐수열회수기와; The raw water of the raw water supply source and the waste water of the waste heat supply source are mutually heat exchanged to increase the temperature of the raw water to convert it into primary hot water, and further, the mixed water of the waste water of the waste heat supply source and the cold water of the cold storage tank is mixed with the raw water of the raw water supply source. A wastewater heat recovery unit converting the raw water into reference water having a constant temperature by heat exchange with each other; 상기 폐수열회수기를 통과하면서 온도가 증가된 1차 온수가 저장되는 축열탱크와; A heat storage tank storing primary hot water having an increased temperature while passing through the waste water heat recovery unit; 상기 축열탱크에 저장된 1차 온수를 응축기로 유입시켜서 내부의 고온의 냉매와 열교환시켜 1차 온수의 온도를 고온으로 상승시켜 2차 온도로 변환시키고, 상기 기준수를 증발기로 유입시켜 원수의 온도를 저온으로 하강시켜 냉수로 변환시키는 히트펌프와; The primary hot water stored in the heat storage tank is introduced into a condenser to exchange heat with a high temperature refrigerant therein, thereby increasing the temperature of the primary hot water to a high temperature, converting it into a secondary temperature, and introducing the reference water into an evaporator to reduce the temperature of raw water. A heat pump that is lowered to a low temperature and converted into cold water; 상기 히트펌프를 통과한 고온의 2차 온수를 저장하는 온수탱크;를 포함하는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.And a hot water tank for storing the high temperature secondary hot water that has passed through the heat pump. 제1항에 있어서, 상기 폐수열회수기는 상기 원수공급처의 원수 및 상기 폐열공급처의 폐수를 상호 열교환시켜 원수의 온도를 증가시키는 제1폐열교환부와; 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합수를 상기 원수공급처의 원수와 상호 열교환시키는 제2폐수열교환부를 포함하는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템The wastewater heat recovery unit according to claim 1, further comprising: a first waste heat exchanger configured to increase the temperature of the raw water by mutually heat-exchanging the raw water of the raw water supply source and the wastewater of the waste heat supply source; And a second wastewater heat exchanger configured to mutually heat-exchange the mixed water of the wastewater of the waste heat supply source and the cold water of the cold storage tank with the raw water of the raw water supply source. 제1항에 있어서, 상기 히트펌프의 증발기를 통과한 냉수는 상기 축냉탱크에 저장되는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.The system of claim 1, wherein the cold water passing through the evaporator of the heat pump is stored in the cold storage tank. 제1항에 있어서, 상기 온수공급처의 온도를 측정하는 제1온도센서와; According to claim 1, A first temperature sensor for measuring the temperature of the hot water supply destination; 상기 제1온도센서에서 측정된 온도에 따라 상기 폐열공급처의 폐수와 상기 축냉탱크의 냉수의 혼합비율을 조절하는 전자밸브를 더 포함하는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.Combined with a two-pass line waste water heat recovery unit and a heat pump, characterized in that it further comprises an electromagnetic valve for controlling the mixing ratio of the waste water of the waste heat supply source and the cold water of the cold storage tank according to the temperature measured by the first temperature sensor. system. 제1항에 있어서, 상기 축열탱크의 내부에서 수위를 측정하는 수위센서와; The liquid crystal display of claim 1, further comprising: a water level sensor measuring a water level inside the heat storage tank; 상기 수위센서에서 측정된 수위가 최고수위이면 상기 축열탱크로 유입되는 1차 온수를 차단하는 차단밸브를 더 포함하는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.And a two-pass line wastewater heat recovery unit and a heat pump using a heat pump if the water level measured by the water level sensor is the highest level. 제1항에 있어서, 상기 축열탱크의 내부에서 온도를 측정하는 제2온도센서를 더 포함하는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.The system of claim 1, further comprising a second temperature sensor for measuring a temperature in the heat storage tank. 제1항에 있어서, 상기 히트펌프의 응축기를 통과한 2차 온수는 상기 축열탱크에 저장되고, 기준온도 이상일 때 상기 온수탱크로 이송되는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.According to claim 1, The second hot water passing through the condenser of the heat pump is stored in the heat storage tank, and is transferred to the hot water tank when the reference temperature or more, characterized in that the two-pass line waste water heat recovery and heating and cooling using the heat pump Combined system. 제1항에 있어서, 상기 온수탱크에 저장된 2차 온수는 난방시설에 공급되고, 상기 축냉탱크에 저장된 냉수는 냉방시설에 공급되는 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.The system of claim 1, wherein the secondary hot water stored in the hot water tank is supplied to a heating facility, and the cold water stored in the cold storage tank is supplied to a cooling facility. . 제1항에 있어서, 상기 히트펌프는 수냉식 히트펌프 또는 공랭식 히트펌프 중의 어느 하나인 것을 특징으로 하는 2패스라인 폐수열회수기와 히트펌프를 이용한 냉난방 겸용 시스템.The system of claim 1, wherein the heat pump is any one of a water-cooled heat pump and an air-cooled heat pump.
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