KR20050120529A - Direct dry cleaning oven - Google Patents

Direct dry cleaning oven Download PDF

Info

Publication number
KR20050120529A
KR20050120529A KR1020040045904A KR20040045904A KR20050120529A KR 20050120529 A KR20050120529 A KR 20050120529A KR 1020040045904 A KR1020040045904 A KR 1020040045904A KR 20040045904 A KR20040045904 A KR 20040045904A KR 20050120529 A KR20050120529 A KR 20050120529A
Authority
KR
South Korea
Prior art keywords
heat
heat supply
drying
direct heating
combustion
Prior art date
Application number
KR1020040045904A
Other languages
Korean (ko)
Inventor
김영구
Original Assignee
김영구
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 김영구 filed Critical 김영구
Priority to KR1020040045904A priority Critical patent/KR20050120529A/en
Publication of KR20050120529A publication Critical patent/KR20050120529A/en

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00Domestic laundry dryers
    • D06F58/20General details of domestic laundry dryers 
    • D06F58/26Heating arrangements, e.g. gas heating equipment
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06FLAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00Domestic laundry dryers
    • D06F58/02Domestic laundry dryers having dryer drums rotating about a horizontal axis
    • D06F58/04Details 
    • 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
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B40/00Technologies aiming at improving the efficiency of home appliances, e.g. induction cooking or efficient technologies for refrigerators, freezers or dish washers

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

본 발명은 세탁물건조장치에 해당하는 열 공급 장치로 건조방식이 직접가열방식에 관한 것으로서 기존의 간접가열식에 비해 연료 절감 효율이 매우 높다. 직접 가열식은 연소후 배출되는 연소공기를 외부로 배출하지 않고 건조실 내부로 유입되는 것을 그 특징으로 직접가열식 방법에 관한 것이다.The present invention relates to a direct heating method of the drying method as a heat supply device corresponding to the laundry drying apparatus, and has a very high fuel saving efficiency compared to the conventional indirect heating method. The direct heating method relates to a direct heating method characterized in that the combustion air discharged after combustion is introduced into the drying chamber without discharged to the outside.

Description

세탁물건조기의 연료절감장치{direct dry cleaning oven} Direct dry cleaning oven for laundry dryers

본 발명은 세탁시설중 건조기의 건조 방법에 관한 것이다.The present invention relates to a drying method of a dryer in a laundry facility.

도 1은 일반적인 세탁시설의 건조장치를 나타낸 구성도이다. 도 1에 도시된 바와 같이 일반적인 건조장치는 크게 버너(101), 열공급장치(108), 건조실(104,105)로 구성되어 있으며 열교환기(102)에서 얻어진 열은 건조실(104,105)로 유입되어 세탁물 건조후 블로어(106,107)에의해 외부로 배기가 이루어진다.1 is a block diagram showing a drying apparatus of a general laundry facility. As shown in FIG. 1, a general drying apparatus includes a burner 101, a heat supply device 108, and drying chambers 104 and 105, and the heat obtained from the heat exchanger 102 flows into the drying chambers 104 and 105 after drying the laundry. Exhaust is made to the outside by the blowers 106 and 107.

도 2는 상기 기존 세탁물 건조장치의 간접가열식열 공급장치(205)를 설명한 것으로서 버너(201)에 의해 주입된 연료를 연소시키는 연소로(204), 연소된 뜨거운 공기의FIG. 2 illustrates the indirect heating type heat supply device 205 of the conventional laundry drying apparatus, and includes a combustion furnace 204 for burning fuel injected by the burner 201 and burned hot air.

열을 회수하는 열교환기(202)와 열 회수가 되지 않고 배출되는 연소공기의 배출구 Heat exchanger 202 for recovering heat and outlet of combustion air discharged without heat recovery

(203)로 상기 간접가열식 열공급장치가(205) 구성되며 열교환기(202)에서 회수되지 203, the indirect heating type heat supply device 205 is configured to recover the heat exchanger 202.

못한 열은 배출구(203)에 의해 외부로 배출되도록 구성되어있다.Unsuccessful heat is configured to be discharged to the outside by the outlet 203.

간접가열식은 열교환 효율이 40~50%에 불과해 연료의 소모가 많아 년간 연료비가 세탁물건조장치 1대당 약 일천오백만원이든다. 열회수 효율을 높이기 위해서는 열교환기(202)의 표면적과 부피가 증가하여야 하나, 열교환기의 표면적과 부피의 증가는 열교환기(202)의 제작비가 높아져 가격 경쟁력을 잃고 또한 건조장치를 건물내에 설치하는데 있어 그 부피가 커져 설치에 어려움이 있다.Indirect heating type heat exchange efficiency is only 40-50%, so the fuel consumption is high, the annual fuel cost is about 15 million Yuan per laundry dryer. In order to increase the heat recovery efficiency, the surface area and volume of the heat exchanger 202 must be increased. However, the increase in the surface area and volume of the heat exchanger results in a high manufacturing cost of the heat exchanger 202, which leads to a loss of price competitiveness and the installation of a drying apparatus in the building. Its bulkiness makes installation difficult.

본 발명은 상기 종래기술이 안고 있는 간접가열식 열공급방식은 열 회수율이 낮은 문제점을 해결하기 위하여 안출된 것으로 열 회수 효율의 극대화 뿐만 아니라 세탁 건조시간 단축 및 기존 대비 50%이상의 연료 절감 효과를 볼수 있으며 그 구조가 간단하여 매우 실용적이고 유용한 세탁물건조기의 열공급 방법을 제공하는 것을 그 목적으로 두고 있다.The present invention has been conceived in order to solve the problem of low heat recovery rate of the indirect heating type heat supply method of the prior art can not only maximize the heat recovery efficiency, but also reduce the drying time of washing and fuel savings of more than 50% compared to the conventional The object of the present invention is to provide a method of supplying heat to a laundry dryer that is simple in structure and very useful.

상기와 같은 목적을 달성하기 위하여 본 발명은 건조실 내에 열 공급방법이 직접가열식인 것을 그 특징으로 한다. 기존의 간접가열식은 연소된 열이 열교환기의 열 전도에 의해 일부 열회수는 되나 절반 이상의 열이 회수가 되지 않은 상태로 배출구(203)를 통해 외부로 배출되는데 비해, 본 발명의 직접 가열식 열공급장치는 배출구(303)에서 배출되어지는 폐열이 송풍기(403)에 의해 유입되는 공기(306)와 섞여 건조실(404,405)로 유입 시키게 되는 것으로서 외부로 열 에너지를 배출시키지 않고 모두 사용하는 열 공급방법이다.In order to achieve the above object, the present invention is characterized in that the heat supply method in the drying chamber is a direct heating type. In the conventional indirect heating type, the heat is burned out by heat conduction of the heat exchanger, but the heat is discharged to the outside through the outlet 203 in a state where at least half of the heat is not recovered. The waste heat discharged from the discharge port 303 is mixed with the air 306 introduced by the blower 403 to be introduced into the drying chambers 404 and 405, and is a heat supply method using all of them without discharging thermal energy to the outside.

상기의 직가열식 연소에있어 완전연소 되기 위해서는 버너(401)에서 점화된 연료와 버너블로어에서 유입된 공기가 연소로에서 500~1200℃로 0.2~3초간 연소가 가능하나, 효율적인 면과 경제적인 면에서 800~1000℃에서 0.5~2초간 연소하는 것이 In order to be completely burned in the direct heating combustion, the fuel ignited in the burner 401 and the air introduced from the burner blower can be burned for 0.2 to 3 seconds at 500 to 1200 ° C. in the combustion furnace, but it is efficient and economical. Burning at 800 ~ 1000 ℃ for 0.5 ~ 2 seconds

좋다. 열교환기효율이 낮아도 발생되어지는 열은 배출구(303)가 열 공급장치 내부에 있으므로 연소로(304)에서 발생한 모든 열이 건조실(404,405)로 유입된다. 그러므로 운전비용면에서 경제적이며 또한 열교환기가 작아도 되므로 제작적인 면에서도 경제적이다.good. Even though the heat exchanger efficiency is low, since the outlet 303 is inside the heat supply device, all the heat generated from the combustion furnace 304 is introduced into the drying chambers 404 and 405. It is therefore economical in terms of operating cost and economical in terms of production since the heat exchanger can be small.

상기 직접가열식 열공급장치(305)의 연료는 경유, 등유, LPG, LNG등을 연료로 사용할 수 있으나 좋기로는 청정연료인 LPG와LNG가 좋다.Fuel of the direct heating type heat supply device 305 may be diesel, kerosene, LPG, LNG, etc. as a fuel, but preferably LPG and LNG, which are clean fuels.

도 3은 상기의 직접가열식 열 공급장치를 설명하기 위한 개략적인 시스템 개요도로서, 송풍기(403)에 의해 건조실(404,405)로 유입되는 공기(306), 연료주입과 점화가 가능한 버너(301)에서 점화된 연료를 연소로(304)에서 완전 연소된 후 열교환기(302)를 통해 송풍기에 유입된 공기(306)에 열을 공급한다. 열공급은 연소로의 외벽을 스치며 가열되어지는 1차열과 연소배출구(302)에서 배출된 2차열로 구성되어지며, 연소로(304)는 두 공기가 충분히 혼합할 수 있도록 배플 역할을 한다. 이때 충분히 혼합된 공기(307)는 건조실 내부로 유입된다.FIG. 3 is a schematic system schematic diagram for explaining the above-described direct heating type heat supply device, and the air 306 introduced into the drying chamber 404 and 405 by the blower 403, and the ignition in the burner 301 capable of fuel injection and ignition. After the fuel is completely burned in the combustion furnace 304, heat is supplied to the air 306 introduced into the blower through the heat exchanger 302. The heat supply is composed of a primary heat that is heated and rubs the outer wall of the combustion furnace and a secondary heat discharged from the combustion outlet 302, and the combustion furnace 304 serves as a baffle to allow the two air to be sufficiently mixed. At this time, the sufficiently mixed air 307 is introduced into the drying chamber.

열교환기를 통해 열을 회수하는 간접가열식 열공급장치(205)는 열 회수효율이 45~50%정도로 열 회수율이 낮아 연료 소모가 높으나 본 발명에서 개발한 직접가열식 열공급장치(305)는 연소열을 전부 사용함으로써 열 회수 효율이 100%이므로 연료 소모를 최대로 낮추었다 또한 절반 용량의 버너를 사용하며, 작은 용량의 버너사용에 의해 연소실(204) 균열 발생이 적어 이로 인하여 발생되어지는 연소실(204) 교체 비용이 줄어 매우 실용적이다. The indirect heating type heat supply device 205 for recovering heat through the heat exchanger has a high heat recovery rate of about 45-50%, resulting in high fuel consumption, but the direct heating type heat supply device 305 developed in the present invention uses all the combustion heat. Since the heat recovery efficiency is 100%, the fuel consumption is reduced to the maximum. Also, a half-capacity burner is used, and the combustion chamber 204 is less likely to crack due to the use of a small-capacity burner, thereby reducing the cost of replacing the combustion chamber 204. Reduced is very practical.

도 1은 기존의 세탁물건조장치  1 is a conventional laundry drying apparatus

도 2는 기존 건조장치의 간접가열식 열공급장치  2 is an indirect heating type heat supply device of the existing drying apparatus

도 3은 직접가열식 열공급장치  3 is a direct heating heat supply device

도 4는 직접가열식 세탁물건조장치  4 is a direct heating laundry drying device

〈도면의 주요부분에 대한 부호의 설명〉  <Explanation of symbols for main parts of drawing>

101,201,301,401 : 버너 102,202,302,402 : 열교환기        101,201,301,401: Burner 102,202,302,402: Heat exchanger

103,203,303 : 연소배출구 104,105,404,405 : 건조실        103,203,303: combustion outlet 104,105,404,405: drying chamber

106,107 : 블로어 204,304 : 연소실         106,107: blower 204,304: combustion chamber

403 : 송풍기 108,205 : 간접가열식 열공급장치        403: Blower 108,205: Indirect heating type heat supply device

407,408 : 댐퍼 305,406 : 직접가열식 열공급장치        407,408: Damper 305,406: Direct heating type heat supply device

Claims (3)

송풍기(403)를 연소실(304)하단에 위치하며 연소실(304) 배출구(303)가 열공급장치(406)내부에 위치하고 배출구(303)로 배출 되어지는 연소열을 세탁물건조실(404,The blower 403 is positioned below the combustion chamber 304 and the combustion chamber 304 discharge port 303 is located inside the heat supply device 406 and discharges the combustion heat discharged to the discharge port 303 to the laundry drying chamber 404. 405)로 유입 되어지는 직접가열식 열공급방법을 특징으로하는 세탁물 건조장치 Laundry drying apparatus characterized by the direct heating type heat supply method introduced into 405 청구항 1에 있어서 직접가열식 열공급방법은 연료연소방식에 따라 직가열식 열연소방법, 직가열식 촉매연소방법 사용The direct heating type heat supply method according to claim 1 is used for direct heating type hot combustion method, direct heating type catalytic combustion method according to fuel combustion method 송풍기, 열공급장치, 건조덕트, 건조기로 구성되어지는 세탁물 건조장치에 있어서 송풍기(403)가 연소실(401)하단에 위치하고, 열공급장치(406) 하단부분과 건조실(404,405) 하단부분을 덕트로 연결하고 덕트중간에 여과필터와 댐퍼(407,408)를 설치하고 건조열을 재순환시키는 것을 특징으로 하는 세탁물 건조장치.In the laundry drying device consisting of a blower, a heat supply device, a drying duct, and a dryer, a blower 403 is located at the bottom of the combustion chamber 401, and a lower part of the heat supply device 406 and a lower part of the drying chamber 404 and 405 are connected by ducts. Laundry drying apparatus, characterized in that the filter installed in the middle of the duct and dampers (407,408) to recycle the drying heat.
KR1020040045904A 2004-06-19 2004-06-19 Direct dry cleaning oven KR20050120529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020040045904A KR20050120529A (en) 2004-06-19 2004-06-19 Direct dry cleaning oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020040045904A KR20050120529A (en) 2004-06-19 2004-06-19 Direct dry cleaning oven

Publications (1)

Publication Number Publication Date
KR20050120529A true KR20050120529A (en) 2005-12-22

Family

ID=37293023

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020040045904A KR20050120529A (en) 2004-06-19 2004-06-19 Direct dry cleaning oven

Country Status (1)

Country Link
KR (1) KR20050120529A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109790676A (en) * 2016-07-22 2019-05-21 三星电子株式会社 Dryer

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950009017U (en) * 1993-09-07 1995-04-19 코오롱엔지니어링 주식회사 Clothing dryer using waste heat of gas boiler
JPH08141289A (en) * 1994-11-17 1996-06-04 Sharp Corp Clothing dryer
KR20000007135A (en) * 1999-11-30 2000-02-07 송교섭 Drier with Heat-exchanger for heat-recovery
KR200256548Y1 (en) * 2001-01-04 2001-12-24 주영혁 Far Infrared Ray Dryer
KR200318377Y1 (en) * 2003-03-18 2003-06-28 지창환 A dryingmachine make use of recycling combustion heat

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950009017U (en) * 1993-09-07 1995-04-19 코오롱엔지니어링 주식회사 Clothing dryer using waste heat of gas boiler
JPH08141289A (en) * 1994-11-17 1996-06-04 Sharp Corp Clothing dryer
KR20000007135A (en) * 1999-11-30 2000-02-07 송교섭 Drier with Heat-exchanger for heat-recovery
KR200256548Y1 (en) * 2001-01-04 2001-12-24 주영혁 Far Infrared Ray Dryer
KR200318377Y1 (en) * 2003-03-18 2003-06-28 지창환 A dryingmachine make use of recycling combustion heat

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109790676A (en) * 2016-07-22 2019-05-21 三星电子株式会社 Dryer

Similar Documents

Publication Publication Date Title
CN101319788B (en) High performance fuel heat accumulation type condensation energy-saving boiler
CN206052380U (en) Textile cloth forming machine natural gas indirect heating apparatus
CN101338894A (en) Low-calorie fuel dual prewarming and thermal storage type energy-saving boiler
CN108343963A (en) A kind of controllable mixing disperse formula heat storage burner
CN103063044B (en) Rotary hearth furnace smoke waste heat utilization system and rotary hearth furnace fume afterheat Application way
CN102721276B (en) Energy-saving transformation system for ceramic kiln
CN209263628U (en) A kind of disperse formula renewable aluminum raw material accumulation of heat smelting furnace
KR20050120529A (en) Direct dry cleaning oven
CN115682434A (en) Gas water heater based on pulse combustion technology
CN101338906A (en) Low-grade fuel dual prewarming and thermal storage type condensation energy-saving boiler
CN212205063U (en) Hot-blast stove
CN209877355U (en) Intelligent temperature control type heating furnace
CN208652622U (en) A kind of temperature automatically controlled heating stove of environmental protection
CN212691792U (en) Direct-fired incinerator
CN202485204U (en) Double-air-blower double-control energy-saving air heater
KR200265150Y1 (en) a steam boiler
KR20050107673A (en) Paint booth by direct heating method for saving energy
CN205919293U (en) Gas energy -saving steam generator
CN201449007U (en) A turn-back flow coal burning hot air furnace
KR100441903B1 (en) Directly heating paint booth, saved energy
CN220556215U (en) High-efficient operation economizer of direct-fired gas boiler
CN210458060U (en) Exhaust gas recycling device
KR200184241Y1 (en) A water boiler
KR20090117554A (en) One body type combustion boiler for petro coke
CN203928384U (en) A kind of fume generating furnace that utilizes high efficiency smart burning to manufacture qualified drier

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E601 Decision to refuse application
E601 Decision to refuse application