KR100353761B1 - Heat exchanger structure of condensing gas boiler - Google Patents

Heat exchanger structure of condensing gas boiler Download PDF

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KR100353761B1
KR100353761B1 KR1020000082072A KR20000082072A KR100353761B1 KR 100353761 B1 KR100353761 B1 KR 100353761B1 KR 1020000082072 A KR1020000082072 A KR 1020000082072A KR 20000082072 A KR20000082072 A KR 20000082072A KR 100353761 B1 KR100353761 B1 KR 100353761B1
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heat
heat exchanger
gas boiler
divided
auxiliary
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KR1020000082072A
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Korean (ko)
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KR20020052660A (en
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이돈형
허정선
정은찬
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주식회사 롯데기공
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/124Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and being formed of pins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/001Casings in the form of plate-like arrangements; Frames enclosing a heat exchange core
    • F28F9/002Casings in the form of plate-like arrangements; Frames enclosing a heat exchange core with fastening means for other structures

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Details Of Fluid Heaters (AREA)

Abstract

본 발명은 열교환을 위해 설치되는 메인 열교환기 및 보조 열교환기로 이루어진 열교환기를 2단 구조를 갖도록 하여 열교환시 외부로 방출·손실되는 열을 최소화할 수 있고 또한, 열교환 파이프에 결합된 방열핀의 불필요한 전열면적을 제거하여 방열핀 표면에서 발생되는 마찰저항을 줄여 배기성을 향상시켜 연소성이 우수하고 연소시 발생되는 배기가스 성분인 질소산화물(NOx) 발생을 억제할 수 있도록 한 콘덴싱 가스보일러의 열교환기 구조에 관한 것으로서, 버너의 점화·연소로 인해 발생되는 열을 흡열하여 난방 및 온수 공급을 위한 난방수를 가열시키는 메인 열교환부와 보조 열교환부로 이루어진 콘덴싱 가스보일러의 열교환기에 있어서, 상기 보조 열교환부가 중간에 소정의 갭이 발생되도록 상·하부몸체로 등분·분할됨에 따라, 열교환시 잠열 및 응축 잠열을 효율적으로 흡열함은 물론, 배기성과 연소성을 향상시켜 연소시 발생되는 배기가스에 함유된 유해성분인 질소산화물(NOx) 발생을 줄여 부식을 억제할 수 있으며, 또한, 흡열이 이루어지는 방열핀의 불필요한 전열면적을 축소시켜 냉각현상을 억제하여 열효율을 증대시킬 수 있어 최소량의 연료로 최대한의 열에너지를 얻을 수 있는 것이다.The present invention has a two-stage structure of a heat exchanger consisting of a main heat exchanger and an auxiliary heat exchanger installed for heat exchange, thereby minimizing heat released and lost during heat exchange, and also unnecessary heat transfer area of a heat radiation fin coupled to a heat exchange pipe. Of heat exchanger structure of condensing gas boiler to reduce the frictional resistance generated on the surface of radiating fins to improve the exhaust performance and to suppress the generation of nitrogen oxide (NOx), which is excellent in combustibility and combustion. In the heat exchanger of the condensing gas boiler comprising a main heat exchanger and an auxiliary heat exchanger for absorbing heat generated by ignition and combustion of a burner to heat the heating water for heating and hot water supply, the auxiliary heat exchanger has a predetermined gap in the middle. Heat is divided into equal parts and divided into upper and lower bodies so that In addition to efficiently absorbing heat and latent heat of condensation, and improving exhaustability and combustibility, corrosion can be suppressed by reducing the generation of nitrogen oxides (NOx), which are harmful components contained in the exhaust gases generated during combustion. By reducing the unnecessary heat transfer area of the heat sink fins, the cooling phenomenon can be suppressed to increase the thermal efficiency, thereby obtaining the maximum heat energy with the least amount of fuel.

Description

콘덴싱 가스보일러의 열교환기 구조{HEAT EXCHANGER STRUCTURE OF CONDENSING GAS BOILER}Heat Exchanger Structure of Condensing Gas Boiler {HEAT EXCHANGER STRUCTURE OF CONDENSING GAS BOILER}

본 발명은 콘덴싱 가스보일러의 열교환기 구조에 관한 것으로서, 보다 상세하게는 열교환을 위해 설치되는 메인 열교환기 및 보조 열교환기로 이루어진 열교환기를 2단 구조를 갖도록 하여 열교환시 외부로 방출·손실되는 열을 최소화할 수 있고 또한, 열교환 파이프에 결합된 방열핀의 불필요한 전열면적을 제거하여 방열핀 표면에서 발생되는 마찰저항을 줄여 배기성을 향상시켜 연소성이 우수하고 연소시 발생되는 배기가스 성분인 질소산화물(NOx) 발생을 억제할 수 있도록 한 콘덴싱 가스보일러의 열교환기 구조에 관한 것이다.The present invention relates to a heat exchanger structure of a condensing gas boiler, and more particularly, to a heat exchanger consisting of a main heat exchanger and an auxiliary heat exchanger installed for heat exchange to have a two-stage structure, thereby minimizing heat released and lost during heat exchange. In addition, by eliminating unnecessary heat transfer area of the heat sink fins coupled to the heat exchange pipe, it reduces frictional resistance generated on the surface of the heat sink fins to improve the exhaust performance, which is excellent in combustibility and generates NOx, an exhaust gas component generated during combustion. The heat exchanger structure of a condensing gas boiler which can be suppressed is related.

일반적으로, 가스보일러라 함은 일반가정이나 산업현장에서 난방 및 온수 공급을 위해 사용되는 것으로서, 크게 나누어 보면, 공급되는 연료(가스 또는 기름)를 점화·연소시키기 위한 연소기와, 연소장치에 의해 발생된 열량을 난방수에 전달하여 고온 상태가 되도록 하는 열교환기와, 고온상태로 열교환이 이루어진 난방수를 난방 및 온수공급을 위해 순환·공급시키는 난방배관으로 나눌 수 있으며, 연소시 사용되는 연료에 따라 가스보일러와 기름보일러로 구분되어 진다.In general, gas boilers are used for heating and hot water supply in general homes or industrial sites. In general, gas boilers are generated by a combustor and a combustion device for igniting and burning fuel (gas or oil). It can be divided into a heat exchanger that transfers the amount of heat to the heating water to make it into a high temperature state, and a heating pipe that circulates and supplies heating water that has been heat-exchanged at a high temperature state for heating and hot water supply. It is divided into boiler and oil boiler.

특히, 본 발명에서 다루고자 하는 것은 가스보일러의 열교환기에 관한 것으로서, 열교환기는 가스보일러에 있어 가장 핵심적인 기술로써, 최소한의 연료(가스)를 사용하여 최대한의 열효율을 얻기 위해 많은 연구개발이 이루어지고 있으며또한, 열교환시 발생되는 드레인[연소시 발생되는 배기가스에 함유된 부식성 성분인 질소산화물(NOx)이 용융됨]으로 인해 발생되는 부식현상에 따른 보일러의 수명단축이 가장 큰 문제점으로 대두되고 있다.In particular, the present invention deals with the heat exchanger of the gas boiler, the heat exchanger is the core technology for the gas boiler, a lot of research and development is made to obtain the maximum thermal efficiency using the least fuel (gas) In addition, shortening the life of the boiler due to the corrosion phenomenon caused by the drain generated during the heat exchange (NOx, which is a corrosive component contained in the exhaust gas generated during combustion) has emerged as the biggest problem. .

현재, 상기와 같은 문제점을 해소하기 위한 열교환기로는 특허 제 132742호(이하, 선행특허 1이라 함)와 특허 제 257573호9이하, 선행특허 2라 함)에 의해 알려진 바 있으며, 이에 따른 열교환기를 살펴보면, 먼저 선행특허 1에 따른 열교환기는 첨부 도면 도 1에 도시된 바와 같이, 통수관(11)의 외측 둘레에 다수의 핀(12a)을 설치한 주열교환부(1a)를 구성하고, 상기 통수관(11)에 있어서의 상기 주열교환부(1a)보다 상류측 부분이 되는 외측둘레에 다수의 핀(12b)을 설치한 부열교환부(1b)를 구성하며, 배기통로에 있어서의 연소장치의 하류측에 주열교환부(1a)와 부열교환부(1b)를 순차배치하여 설치하여 현열 및 잠열을 흡수하도록 한 열교환장치에 있어서, 상기 주열교환부(1a)의 핀(12a)을 동으로 형성함과 아울러 부열교환부(1b)의 통수관(11)이나 핀(12b)을 알루미늄재로 성형한 것이고, 선행특허 2는 첨부 도면 도 2에 도시된 바와 같이, 상하 배열된 열교환파이프(19)의 둘레에 브레이징 용접되어 현열을 흡수하는 현열부 핀(13)과 내부에 열매체가 흐르고 외부의 현열부 핀(13)으로부터 현열을 흡수하여 열매체에 전달하는 열교환파이프(19)로 구성되어 버너(18)에서 발생한 연소 현열을 흡수하는 상부의 현열 열교환부(20)와, 상하 배열된 열교환파이프(30)의 둘레에 브레이징 용접되어 잠열을 흡수하는 잠열부 핀(24)과 내부에 열매체가 흐르고 외부의 잠열부 핀(24)으로부터 잠열을 흡수하여 열매체에 전달하는 열교환파이프(30)로 구성되어 상기 현열 열교환부(20)에서열교환을 마친 현열의 잔열 및 응축시 발생하는 응축 잠열을 흡수하는 하부의 잠열 열교환부(22)가 구비된 것이다.At present, a heat exchanger for solving the above problems has been known by Patent No. 132742 (hereinafter referred to as Patent 1) and Patent No. 257573 9 or below, referred to as Patent 2). Looking at, first, the heat exchanger according to the prior patent 1 constitutes the main heat exchanger (1a) having a plurality of fins (12a) installed on the outer periphery of the water pipe (11), as shown in the accompanying drawings The sub-heat exchange part 1b which provided the some fin 12b in the outer periphery which becomes an upstream part of the said main heat exchange part 1a in the pipe 11 is comprised, and the combustion apparatus in an exhaust path In the heat exchanger in which the main heat exchanger (1a) and the subheat exchanger (1b) are arranged in the downstream side so as to absorb sensible and latent heat, the fins (12a) of the main heat exchanger (1a) are formed of copper. In addition, the water pipe 11 and the fin 12b of the sub-heat exchange part 1b are made of aluminum. As shown in FIG. 2, the prior patent 2 has a heat-sensing part pin 13 for absorbing sensible heat by brazing welding around a heat exchange pipe 19 arranged up and down, and a heat medium flowing therein, An upper sensible heat exchanger 20 configured to absorb sensible heat from the sensible heat fin 13 and transfer the sensible heat to the heat medium and absorb the combustion sensible heat generated by the burner 18, and a heat exchange pipe arranged up and down ( 30 is formed of a latent heat portion fin 24 for brazing welding absorbing latent heat and a heat exchanger pipe 30 for absorbing latent heat from an external latent heat portion pin 24 and transferring it to the heat medium. The latent heat exchanger 22 which absorbs the residual heat of the sensible heat and the latent heat of condensation generated during condensation is provided at the sensible heat exchanger 20.

따라서, 상기와 같은 선행특허 1은 주열교환부의 핀 재질을 동으로 하고 부열교환부의 통수관이나 핀을 알루미늄재로 하여 열교환시 발생되는 드레인에 따른 부식을 방지하고자 하는 것이고, 선행특허 2는 열교환이 이루어지는 열교환기를 현열 열교환부와 잠열 열교환부로 이루어지는 이중구조를 갖도록 하여 배기가스에 의해 외부로 방출되는 열손실을 줄이기 위한 것이다.Therefore, the prior patent 1 as described above is to prevent the corrosion caused by the drain generated during heat exchange by using the fin material of the main heat exchange part and the water pipe or fin of the sub-heat exchange part as aluminum material, and the prior patent 2 is It is to reduce the heat loss emitted to the outside by the exhaust gas by having a dual structure consisting of a sensible heat exchanger and a latent heat exchanger.

그러나, 상기와 같은 선행특허 1에서는 드레인 발생이 억제되어 이에 따른 부식현상을 방지할 수 있으나 열교환시 외부로 방출되어 손실되는 열량이 많아 열효율이 떨어지게 되는 단점을 갖게 되며, 선행특허 2에서는 열교환기를 이중구조로 이루어짐에 따라 열교환시 외부로 방출되는 열량을 최소화 할 수 있어 열효율을 높일 수 있다는 장점을 갖고 있으나, 드레인 발생으로 인해 부식이 우려되고 열교환시 흡열을 위한 핀에 대한 전열면적이 너무 커 배기성이 떨어지게 되어 배기성 및 연소성이 저하되는 폐단을 갖게 되었다.However, in the prior patent 1 as described above, drain generation is suppressed, thereby preventing corrosion, but there is a disadvantage in that thermal efficiency decreases due to a large amount of heat released and lost during heat exchange. The structure has the advantage of minimizing the amount of heat released to the outside during heat exchange, which has the advantage of increasing the thermal efficiency.However, there is concern about corrosion due to drain generation and the heat transfer area for fins for heat absorption during heat exchange is too large. As a result, it has a closed end in which exhaustability and combustibility are reduced.

본 발명은 상기와 같은 폐단점을 해소하기 위한 것으로서, 그 목적은 열교환기를 2단구조를 갖도록 하여 열교환시 잠열 및 응축 잠열을 효율적으로 흡열함은 물론, 배기성과 연소성을 향상시켜 연소시 발생되는 배기가스에 함유된 유해성분인 질소산화물(NOx) 발생을 줄여 부식을 억제할 수 있으며, 또한, 흡열이 이루어지는 방열핀의 전열면적을 축소시켜 냉각현상을 억제하여 열효율을 증대시킬 수 있어 최소량의 연료로 최대한의 열에너지를 얻을 수 있도록 된 새로운 형태의 콘덴싱 가스보일러의 열교환기 구조를 제공하고자 하는 것이다.The present invention is to solve the above-mentioned end point, the purpose is to have a heat exchanger having a two-stage structure to efficiently absorb the latent heat and condensation latent heat during heat exchange, as well as to improve the exhaustability and combustibility exhaust gas generated during combustion Corrosion can be suppressed by reducing the generation of nitrogen oxides (NOx), which are harmful components in the gas, and heat efficiency can be reduced by reducing the heat transfer area of the heat sink fins that absorb heat, thereby increasing the thermal efficiency. It is to provide a heat exchanger structure of a condensing gas boiler of a new type to obtain a thermal energy of.

이와 같은 목적을 달성하기 위하여, 본 발명은 버너의 점화·연소로 인해 발생되는 열을 흡열하여 난방 및 온수 공급을 위한 난방수를 가열시키는 메인 열교환부와 보조 열교환부로 이루어진 콘덴싱 가스보일러의 열교환기에 있어서, 상기 보조 열교환부가 중간에 소정의 갭이 발생되도록 상·하부몸체로 등분·분할된 특징을 갖는다.In order to achieve the above object, the present invention provides a heat exchanger of a condensing gas boiler comprising a main heat exchanger and an auxiliary heat exchanger for absorbing heat generated by ignition and combustion of a burner to heat heating water for heating and hot water supply. The auxiliary heat exchanger has a feature of being divided into upper and lower bodies so as to generate a predetermined gap in the middle.

이와 같은 본 발명에서, 상기 메인 열교환부가 갭을 갖도록 등분·분할된 특징을 갖는다.In the present invention as described above, the main heat exchanger has a feature that is divided into equal parts and divided so as to have a gap.

도 1은 선행특허 1에 따른 콘덴싱 가스보일러를 나타내는 개략도,1 is a schematic view showing a condensing gas boiler according to the prior patent 1,

도 2는 선행특허 2에 따른 콘덴싱 가스보일러를 나타내는 개략도,Figure 2 is a schematic diagram showing a condensing gas boiler according to the prior patent 2,

도 3은 본 발명에 따른 열교환기가 설치된 콘덴싱 가스보일러를 나타내는 개략도,3 is a schematic view showing a condensing gas boiler equipped with a heat exchanger according to the present invention;

도 4는 본 발명에 따른 열교환기의 보조 열교환부를 나타내는 확대 단면도,4 is an enlarged cross-sectional view showing an auxiliary heat exchanger of the heat exchanger according to the present invention;

도 5는 도 3의 A부에 대한 확대 사시도,5 is an enlarged perspective view of a portion A of FIG. 3;

도 6은 본 발명에 따른 열교환기의 방열핀에 대한 다른 실시예를 나타내는 개략도,6 is a schematic view showing another embodiment of the heat dissipation fin of the heat exchanger according to the present invention;

도 7은 본 발명에 따른 열교환기의 또 다른 실시예를 나타내는 개략도이다.7 is a schematic view showing another embodiment of a heat exchanger according to the present invention.

<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>

100:케이스 102:버너100: case 102: burner

103:연소실 104, 104', 104":방열핀103: combustion chamber 104, 104 ', 104 ": heat radiation fin

105:열교환파이프 110, 110':메인 열교환부105: heat exchange pipe 110, 110 ': main heat exchanger

120, 120':보조 열교환부 121, 121':상부몸체120, 120 ': Secondary heat exchanger 121, 121': Upper body

122, 122':하부몸체 130:열교환기122, 122 ': lower body 130: heat exchanger

G:갭(gap)G: gap

이하, 본 발명을 첨부된 도면에 의해 보다 상세하게 설명하면 다음과 같다.Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings.

도 3은 본 발명에 따른 열교환기가 설치된 콘덴싱 가스보일러를 나타내는 개략도로서, 보일러 케이스(100)의 상부에 공급된 가스를 점화·연소시키기 위한 버너(102)가 내설되고 그 하방으로 연소가 이루어지는 연소실(103) 아래로 다수개의 방열핀(104, 104')이 외주면에 결합된 열교환 파이프(105)가 일정 간격으로 나열된 메인 열교환부(110)와 보조 열교환부(120)로 이루어진 열교환기(130)가 내설되되, 상기 보조 열교환부(120)는 중간에 소정의 갭(G)이 발생되도록 상부몸체(121)와 하부몸체(122)로 등분·분할되어진 것을 나타내는 것이다.3 is a schematic view showing a condensing gas boiler provided with a heat exchanger according to the present invention, in which a combustion chamber in which a burner 102 for igniting and combusting a gas supplied to an upper portion of a boiler case 100 is installed and combustion is performed below the combustion chamber ( 103) A heat exchanger 130 including a main heat exchanger 110 and an auxiliary heat exchanger 120 having a plurality of heat dissipation fins 104 and 104 'coupled to an outer circumferential surface thereof is arranged at regular intervals. However, the auxiliary heat exchanger 120 indicates that the auxiliary heat exchanger 120 is equally divided and divided into the upper body 121 and the lower body 122 so that a predetermined gap G is generated in the middle.

도 4는 본 발명에 따른 열교환기의 보조 열교환부를 나타내는 확대 단면도로서, 횡방향으로 등간격을 이루며 외주면에 다수개의 방열핀(104)이 촘촘하게 결합된 열교환파이프(105)가 나열된 상부몸체(121)와 그 하방으로 소정의 갭(G)을 이루도록 설치된 하부몸체(122)로 이루어진 보조 열교환부(120)를 나타내는 것이다.Figure 4 is an enlarged cross-sectional view showing an auxiliary heat exchanger of the heat exchanger according to the present invention, the upper body 121 and the heat exchanger pipe 105 is a plurality of heat dissipation fins 104 are tightly coupled to the outer peripheral surface at equal intervals in the horizontal direction and It shows the secondary heat exchanger 120 made of a lower body 122 provided to form a predetermined gap (G) below.

이때, 열교환파이프(105)의 외주면에 결합된 방열핀(104)은 원판형상으로 각각 독립체로 구성된다.At this time, the heat dissipation fins 104 coupled to the outer circumferential surface of the heat exchange pipe 105 are each formed of an independent body in a disc shape.

도 5는 도 3의 A부에 대한 확대 사시도로서, 메인 열교환부(110) 및 보조 열교환부(120)의 열교환파이프(105)의 외주면에 원판형상으로 이루어지되, 각각 별개의 독립체로 구성된 방열핀(104)이 일정하게 등간격을 이루며 결합된 것을 나타내는 것이다.5 is an enlarged perspective view of part A of FIG. 3, wherein the heat dissipation fins are formed on the outer circumferential surface of the heat exchange pipe 105 of the main heat exchanger 110 and the auxiliary heat exchanger 120, respectively, each having a separate entity ( 104 is shown to be coupled at regular intervals.

이때, 열교환파이프(105)에 형성된 방열핀(104)은 열교환이 이루어 짐에 있어 불필요한 전열면적을 제거하기 위해 각각 별개의 독립체로 구성된 것이다.At this time, the heat radiation fins 104 formed on the heat exchange pipe 105 are each composed of a separate entity in order to remove unnecessary heat transfer area in the heat exchange.

도 6은 본 발명에 따른 열교환기의 방열핀에 대한 다른 실시예를 나타내는 개략도로서, 보조 열교환부(120)의 상부몸체(121)와 하부몸체(122) 외주면에 결합되는 방열핀(104")이 일체로 이루어지되, 상·하부몸체(121, 122) 중간부위에 횡방향으로 소정의 갭(G)이 형성된 것을 나타내는 것이다.6 is a schematic view showing another embodiment of the heat dissipation fin of the heat exchanger according to the present invention, in which the heat dissipation fin 104 ″ coupled to the outer circumferential surface of the upper body 121 and the lower body 122 of the auxiliary heat exchanger 120 is integrated. It consists of, but the upper and lower body (121, 122) in the middle portion of the predetermined gap (G) is formed in the transverse direction.

도 7은 본 발명에 따른 열교환기의 또 다른 실시예를 나타내는 개략도로서, 보일러 케이스(100)의 상부에 공급된 가스를 점화·연소시키기 위한 버너(102)가 내설되고 그 하방으로 연소가 이루어지는 연소실(103) 아래로 다수개의 방열핀(104')이 외주면에 결합된 열교환 파이프(105)가 일정 간격으로 나열된 메인 열교환부(110')와 보조 열교환부(120')가 소정거리 이격된 상태로 내설되되, 상기 메인 열교환부(110')는 중간에 소정의 갭(G)이 발생되도록 상부몸체(121')와 하부몸체(122')로 등분·분할되어진 열교환기(130)를 나타내는 것이다.7 is a schematic view showing another embodiment of a heat exchanger according to the present invention, in which a burner 102 for igniting and combusting a gas supplied to an upper portion of a boiler case 100 is installed, and a combustion chamber is burned below. The heat exchange pipe 105 having a plurality of heat dissipation fins 104 'coupled to the outer circumferential surface thereof is disposed below the main heat exchanger 110' and the auxiliary heat exchanger 120 ', which are arranged at regular intervals. However, the main heat exchanger 110 ′ represents the heat exchanger 130 divided into equal parts and divided into the upper body 121 ′ and the lower body 122 ′ so that a predetermined gap G is generated in the middle.

이와 같은 본 발명의 사용상태를 설명하면 다음과 같다.Referring to the use state of the present invention as follows.

도 3 내지 도 5에 도시된 바와 같이, 다수개의 방열핀(104)이 외주면에 결합된 열교환 파이프(105)가 일정 간격으로 나열된 메인 열교환부(110)와 보조 열교환부(120)가 소정거리 이격된 상태로 내설되되, 상기 보조 열교환부(120)는 중간에 소정의 갭(G)이 발생되도록 상부몸체(121)와 하부몸체(122)로 등분·분할되어진 열교환기(130)를 보일러 케이스(100)의 버너(102) 하방에 소정거리 이격된 상태로 내설된, 콘덴싱 가스보일러를 구비한 상태에서, 난방 및 온수공급을 위해 가스보일러를 구동시키게 되면, 버너(102)에 의해 공급된 가스가 점화되어 연소실(103)내에서 연소가 이루어지게 된다.As shown in FIGS. 3 to 5, a heat exchange pipe 105 having a plurality of heat dissipation fins 104 coupled to an outer circumferential surface thereof is spaced apart from the main heat exchanger 110 and the auxiliary heat exchanger 120 by a predetermined distance. The auxiliary heat exchanger 120 has a heat exchanger 130 divided into equal parts and divided into an upper body 121 and a lower body 122 so that a predetermined gap G is generated in the middle of the boiler case 100. When the gas boiler is driven for heating and hot water supply with a condensing gas boiler, which is insulated from the burner 102 under a predetermined distance, the gas supplied by the burner 102 is ignited. As a result, combustion occurs in the combustion chamber 103.

이와 같이, 가스가 연소됨에 따라 그 하방에 설치된 열교환기(130)에 열이 가해지게 되어 방열핀(104)에 의해 열교환파이프(105)로 순환·공급되는 난방수에 열교환이 이루어지게 되는 것으로, 메인 열교환기(110)에 의해 1차로 흡열되어 메인 열교환부(110)의 열교환파이프(105)를 통해 순환·공급되는 난방수의 열교환이 이루어지게 되고 그 하방에 설치된 보조 열교환기(120)에 의해 2차로 잠열 및 응축 잠열이 흡열되어 난방수의 열교환이 이루어지는 것이다.In this way, as the gas is burned, heat is applied to the heat exchanger 130 installed below the heat exchanger, so that heat exchange is made to the heating water circulated and supplied to the heat exchange pipe 105 by the heat dissipation fin 104. The heat is firstly absorbed by the heat exchanger 110 and heat exchange of the heating water circulated and supplied through the heat exchange pipe 105 of the main heat exchanger 110 is performed by the auxiliary heat exchanger 120 installed below. The latent heat and the latent heat of condensation are absorbed by the heat exchange.

이때, 잠열 및 응축 잠열이 열교환되는 보조 열교환부(120)는 소정의 갭(G)이 유지된 상태로 상부몸체(121)와 하부몸체(122)로 등분·분할된 상태이므로 2차 잠열을 흡열·열교환함에 있어 상부몸체(121)에 의해 1단계 흡열에 의한 열교환과 하부몸체(122)에 의한 2단계 흡열에 의한 열교환이 이루어지게 되므로 외부로 방출·손실되는 열량을 최소화 할 수 있어 열효율이 높게 되며, 상부몸체(121)와 하부몸체(122) 사이에 형성된 갭(G)에 의해 잠열을 흡열·열교환함에 있어 연소시 발생되는 배기가스의 방출 및 연소에 필요한 공기 공급을 위한 통풍이 원할하게 이루어지므로 배기성 및 연소성을 향상시켜 연소율을 높여 최소의 연소로 최대의 열량을 얻을 수 있고 또한, 연소성이 향상되므로 연소시 발생되는 배기가스에 함유된 질소산화물(NOx) 발생을 억제시킬 수 있어 이로 인한 부식현상을 예방할 수 있는 것이다.At this time, since the latent heat and the latent heat of condensation heat exchange part 120 is equally divided and divided into the upper body 121 and the lower body 122 while the predetermined gap G is maintained, endothermic secondary heat is absorbed. In the heat exchange, heat exchange is performed by the first stage endothermic by the upper body 121 and heat exchange by the second stage endothermic by the lower body 122, thereby minimizing the amount of heat released and lost to the outside, resulting in high thermal efficiency. By the gap G formed between the upper body 121 and the lower body 122, in endothermic heat exchange and heat exchange, the ventilation for exhausting the exhaust gas generated during combustion and supplying the air required for combustion is made smoothly. Therefore, it is possible to increase the combustion rate by improving the exhaustability and combustibility to obtain the maximum calorie value with minimum combustion, and to improve the combustibility, to suppress the generation of nitrogen oxides (NOx) contained in the exhaust gas generated during combustion. This would've caused that to prevent corrosion.

또한, 첨부 도면 도 6 및 7에 도시된 바와 같이, 보조 열교환부(120)의 상부몸체(121)와 하부몸체(122) 외주면에 결합되는 방열핀(104")을 일체로 이루어지도록 하되, 상·하부몸체(121, 122) 중간부위에 횡방향으로 소정의 갭(G)이 형성되도록 하거나(도 6참조) 가스의 점화·연소에 의해 1차로 열교환이 이루어지는 메인 열교환기(110')를 상기 보조 열교환기(120)와 마찬가지로 소정의 갭이 발생되도록 상·하부몸체(121', 122')로 등분·분할시키게 되면, 1차 열교환시 상부몸체(121')에 의해 1단계로 흡열·열교환이 이루어지고 하부몸체(122')에 의해 2단계로 흡열·열교환이 이루어진 후, 그 하방에 설치된 보조 열교환부(120')에 의해 2차 열교환이 이루어지도록 할 수도 있다.6 and 7, the heat dissipation fins 104 "coupled to the outer circumferential surface of the upper body 121 and the lower body 122 of the auxiliary heat exchanger 120 are integrally formed. The auxiliary heat exchanger 110 ′ may be formed such that a predetermined gap G is formed in the middle of the lower bodies 121 and 122 in the transverse direction (see FIG. 6), or the heat exchanger 110 ′ is primarily heat exchanged by ignition and combustion of gas. Like the heat exchanger 120, if the upper and lower bodies 121 'and 122' are equally divided and divided so as to generate a predetermined gap, the heat absorbing and heat exchange is performed in one step by the upper body 121 'during the first heat exchange. After the end body is endothermic and heat exchanged in two stages by the lower body 122 ′, the secondary heat exchange may be performed by the auxiliary heat exchanger 120 ′ installed below.

이와 같이, 난방 및 온수공급을 위해 난방수가 고온을 유지할 수 있도록 열교환이 이루어지는 열교환기(130)의 메인 열교환부(110, 110') 또는 보조 열교환부(120, 120')를 소정의 갭(G)이 형성되도록 상부몸체(121, 121')와 하부몸체(122, 122')로 등분·분할시켜 2단구조를 갖도록 하여 연소성 및 배기성을 향상시키고 외부로 방출·손실되는 열량을 최소화 할 수 있는 것이다.As such, the main heat exchanger 110, 110 ′ or the auxiliary heat exchanger 120, 120 ′ of the heat exchanger 130 in which the heat exchange is performed to maintain the high temperature of the heating water for heating and hot water supply may have a predetermined gap G. ) Is divided into upper and lower bodies 121 and 121 'and lower and lower bodies 122 and 122' so as to have a two-stage structure to improve combustibility and exhaustability, and to minimize the amount of heat released and lost to the outside. will be.

이와 같이, 본 발명에 따른 2단구조를 갖는 열교환기를 이용함에 따라, 열교환시 잠열 및 응축 잠열을 효율적으로 흡열함은 물론, 배기성과 연소성을 향상시켜 연소시 발생되는 배기가스에 함유된 유해성분인 질소산화물(NOx) 발생을 줄여 부식을 억제할 수 있으며, 또한, 흡열이 이루어지는 방열핀의 불필요한 전열면적을 축소시켜 냉각현상을 억제하여 열효율을 증대시킬 수 있어 최소량의 연료로 최대한의 열에너지를 얻을 수 있는 효과가 있다.As such, by using a heat exchanger having a two-stage structure according to the present invention, the latent heat and condensation latent heat during heat exchange can be efficiently absorbed as well as the harmful components contained in the exhaust gas generated during combustion by improving the exhaustability and combustibility. Corrosion can be suppressed by reducing the generation of NOx, and heat efficiency can be increased by reducing cooling phenomenon by reducing the unnecessary heat transfer area of the heat sink fins where endothermic heat is generated, so that maximum thermal energy can be obtained with the least amount of fuel. It works.

Claims (3)

버너(102)의 점화·연소로 인해 발생되는 열을 흡열하여 난방 및 온수 공급을 위한 난방수를 가열시키는 메인 열교환부(110)와 보조 열교환부(120)로 이루어진 콘덴싱 가스보일러의 열교환기에 있어서,In the heat exchanger of the condensing gas boiler consisting of a main heat exchanger 110 and an auxiliary heat exchanger 120 for absorbing heat generated by the ignition and combustion of the burner 102 to heat the heating water for heating and hot water supply, 상기 보조 열교환부(120)가 중간에 소정의 갭(G)이 발생되도록 상·하부몸체(121, 122)로 등분·분할되고 외주면에 독립체로 이루어진 방열핀(104')이 결합된 것을 특징으로 하는 콘덴싱 가스보일러의 열교환기 구조.The auxiliary heat exchanger 120 is divided into equal parts and divided into upper and lower bodies 121 and 122 so that a predetermined gap G is generated in the middle, and a heat dissipation fin 104 ′ composed of an independent body is coupled to an outer circumferential surface thereof. Heat exchanger structure of condensing gas boiler. 제 1항에 있어서, 보조 열교환부(120)의 상부몸체(121)와 하부몸체(122) 외주면에 일체으로 이루어지고 중간부위에 횡방향으로 소정의 갭(G)이 형성된 방열핀(104")이 결합된 것을 특징으로 하는 콘덴싱 가스보일러의 열교환기 구조.The heat dissipation fin 104 "of claim 1, wherein the heat dissipation fins 104" are formed integrally with the outer circumferential surface of the upper body 121 and the lower body 122 of the auxiliary heat exchanger 120, and a predetermined gap G is formed in the transverse direction in the middle portion. Heat exchanger structure of the condensing gas boiler, characterized in that coupled. 제 1항에 있어서, 상기 열교환기(130)는 소정의 갭(G)을 갖도록 상·하부몸체(121', 122')로 등분·분할된 메인 열교환부(110')와 보조 열교환부(120')로 이루어진 것을 특징으로 하는 콘덴싱 가스보일러의 열교환기 구조.The heat exchanger (130) according to claim 1, wherein the heat exchanger (130) and the auxiliary heat exchanger (120 ') are divided into equal parts and divided into upper and lower bodies (121', 122 ') to have a predetermined gap (G). Heat exchanger structure of the condensing gas boiler, characterized in that consisting of.
KR1020000082072A 2000-12-26 2000-12-26 Heat exchanger structure of condensing gas boiler KR100353761B1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010123247A3 (en) * 2009-04-20 2011-02-24 주식회사 경동나비엔 Heat exchanger

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59170787U (en) * 1983-04-27 1984-11-15 バブコツク日立株式会社 Heat exchange device with finned tubes
KR19990012110A (en) * 1997-07-26 1999-02-25 최병숙 Gas Boiler Condensing Heat Exchanger
KR19990070599A (en) * 1998-02-23 1999-09-15 김철병 Dual structure heat exchanger for condensing gas boiler
KR200219877Y1 (en) * 2000-09-18 2001-04-16 대성쎌틱주식회사 Condensing boiler heat exchanger
KR20020001465A (en) * 2000-06-28 2002-01-09 김철병 Condensing Type Heat Exchanger of Gas Boiler

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59170787U (en) * 1983-04-27 1984-11-15 バブコツク日立株式会社 Heat exchange device with finned tubes
KR19990012110A (en) * 1997-07-26 1999-02-25 최병숙 Gas Boiler Condensing Heat Exchanger
KR19990070599A (en) * 1998-02-23 1999-09-15 김철병 Dual structure heat exchanger for condensing gas boiler
KR20020001465A (en) * 2000-06-28 2002-01-09 김철병 Condensing Type Heat Exchanger of Gas Boiler
KR200219877Y1 (en) * 2000-09-18 2001-04-16 대성쎌틱주식회사 Condensing boiler heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010123247A3 (en) * 2009-04-20 2011-02-24 주식회사 경동나비엔 Heat exchanger
AU2010239899B2 (en) * 2009-04-20 2013-03-21 Kyungdong Navien Co., Ltd. Heat exchanger
EA019912B1 (en) * 2009-04-20 2014-07-30 Кюндон Навиен Ко., Лтд. Heat exchanger
US9250021B2 (en) 2009-04-20 2016-02-02 Kyungdong Navien Co., Ltd. Heat exchanger

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