MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM

A multi-stage separation heat-exchange type drying system according to the present invention is configured such that, if warm air (hereinafter 'first air') of waste heat discharged from a dryer (100) enters a heat exchange device (900) through a discharge line (110), the heat exchange devi...

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Hauptverfasser: WIE, Hyung Chul, LEE, Sang Ro, JANG, Se Gyeong
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LEE, Sang Ro
JANG, Se Gyeong
description A multi-stage separation heat-exchange type drying system according to the present invention is configured such that, if warm air (hereinafter 'first air') of waste heat discharged from a dryer (100) enters a heat exchange device (900) through a discharge line (110), the heat exchange device (900) performs a heat exchange so as to recover heat from the warm first air and supply the heat to outdoor cold air (hereinafter 'second air') and then discharge the heat. The heat exchange between the first air and the second air is performed by a heat medium, and the heat medium absorbs heat from the warm first air introduced to a first main body (300) by circulating throughout the first main body (300) and then is introduced to a second main body (400), and the heat medium introduced to the second main body (400) supplies heat to the cold second air. The first main body (300) and the second main body (400) of the heat exchange device (900) have structures corresponding to each other. That is, a plurality of first heat exchange blocks (700) of the first main body (300) are installed to be spaced from each other at a predetermined interval, and first vortex generating blocks (750) are installed between the first heat exchange blocks (700). Also, a plurality of second heat exchange blocks (800) of the second main body (400) are installed to be spaced apart from each other at a predetermined interval, and second vortex generating blocks (850) are installed between the second heat exchange blocks (800). The heat exchange occurs in a manner that the first heat exchange blocks (700) and the second heat exchange blocks (800) corresponding to each other, positioned up and down, exchange a heat medium therebetween. Un système de séchage du type à échange thermique avec séparation multi-étage selon la présente invention est configuré de telle sorte que, si de l'air chaud (désigné ci-après 'premier air') de chaleur perdue refoulé par un dispositif de séchage (100) pénètre dans un dispositif d'échange thermique (900) par une conduite de refoulement (110), le dispositif d'échange thermique (900) effectue un échange thermique de manière à récupérer la chaleur du premier air chaud et à transmettre la chaleur à l'air froid extérieur (désigné ci-après 'second air'), puis à évacuer la chaleur. L'échange de chaleur entre le premier air et le second air est effectué par un fluide caloporteur et le fluide caloporteur absorbe la chaleur du premier air chaud introduit dans un premier corp
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fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_WO2017090834A1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>WO2017090834A1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_WO2017090834A13</originalsourceid><addsrcrecordid>eNrjZDD3DfUJ8dQNDnF0d1UIdg1wDHIM8fT3U_BwdQzRdY1w9nD0A0qERAa4KrgERXr6uSsERwaHuPryMLCmJeYUp_JCaW4GZTfXEGcP3dSC_PjU4oLE5NS81JL4cH8jA0NzA0sDC2MTR0Nj4lQBAPayKVo</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM</title><source>esp@cenet</source><creator>WIE, Hyung Chul ; LEE, Sang Ro ; JANG, Se Gyeong</creator><creatorcontrib>WIE, Hyung Chul ; LEE, Sang Ro ; JANG, Se Gyeong</creatorcontrib><description>A multi-stage separation heat-exchange type drying system according to the present invention is configured such that, if warm air (hereinafter 'first air') of waste heat discharged from a dryer (100) enters a heat exchange device (900) through a discharge line (110), the heat exchange device (900) performs a heat exchange so as to recover heat from the warm first air and supply the heat to outdoor cold air (hereinafter 'second air') and then discharge the heat. The heat exchange between the first air and the second air is performed by a heat medium, and the heat medium absorbs heat from the warm first air introduced to a first main body (300) by circulating throughout the first main body (300) and then is introduced to a second main body (400), and the heat medium introduced to the second main body (400) supplies heat to the cold second air. The first main body (300) and the second main body (400) of the heat exchange device (900) have structures corresponding to each other. That is, a plurality of first heat exchange blocks (700) of the first main body (300) are installed to be spaced from each other at a predetermined interval, and first vortex generating blocks (750) are installed between the first heat exchange blocks (700). Also, a plurality of second heat exchange blocks (800) of the second main body (400) are installed to be spaced apart from each other at a predetermined interval, and second vortex generating blocks (850) are installed between the second heat exchange blocks (800). The heat exchange occurs in a manner that the first heat exchange blocks (700) and the second heat exchange blocks (800) corresponding to each other, positioned up and down, exchange a heat medium therebetween. Un système de séchage du type à échange thermique avec séparation multi-étage selon la présente invention est configuré de telle sorte que, si de l'air chaud (désigné ci-après 'premier air') de chaleur perdue refoulé par un dispositif de séchage (100) pénètre dans un dispositif d'échange thermique (900) par une conduite de refoulement (110), le dispositif d'échange thermique (900) effectue un échange thermique de manière à récupérer la chaleur du premier air chaud et à transmettre la chaleur à l'air froid extérieur (désigné ci-après 'second air'), puis à évacuer la chaleur. L'échange de chaleur entre le premier air et le second air est effectué par un fluide caloporteur et le fluide caloporteur absorbe la chaleur du premier air chaud introduit dans un premier corps principal (300) par circulation à travers le premier corps principal (300) et est ensuite introduit dans un second corps principal (400) et le fluide caloporteur introduit dans le second corps principal (400) transmet la chaleur au second air froid. Le premier corps principal (300) et le second corps principal (400) du dispositif d'échange thermique (900) présentent des structures correspondant l'une à l'autre. En d'autres termes, une pluralité de premiers blocs d'échange thermique (700) du premier corps principal (300) sont installés de manière à être espacés les uns des autres à un intervalle prédéterminé, et des premiers blocs de génération de tourbillons (750) sont installés entre les premiers blocs d'échange thermique (700). En outre, une pluralité de seconds blocs d'échange thermique (800) du second corps principal (400) sont installés de façon à être espacés les uns des autres à un intervalle prédéterminé, et des seconds blocs de génération de tourbillons (850) sont installés entre les seconds blocs d'échange thermique (800). L'échange thermique se produit de façon à ce que les premiers blocs d'échange thermique (700) et les seconds blocs d'échange thermique (800) correspondant les uns aux autres, disposés en haut et en bas, s'échangent un fluide caloporteur. 개시된 본 발명에 따른 다단 분리 열교환방식의 건조 시스템은, 건조기(100)에서 배출되는 폐열의 따뜻한 공기(이하 '제1공기'라 함)가 배출라인(110)을 통해 열교환 장치(900)로 유입되면, 열교환 장치(900)는 따뜻한 제1공기로부터 열을 회수하여 이를 외기의 차가운 공기(이하 '제2공기'라 함)로 공급 하도록 열교환 한 후 배출 시키게 된다. 상기 제1공기와 제2공기의 열교환은 열매체에 의해 이루어지게 되며, 열매체가 제1 본체(300)를 순환하여 제1 본체(300)로 유입되는 따뜻한 제1공기로부터 열을 흡수한 후 제2 본체(400)로 유입되고, 제2 본체(400)로 유입된 열매체는 차가운 제2공기에 열을 공급 하도록 한다. 열교환 장치(900)의 제1 본체(300)와 제2 본체(400)는 서로 대응되는 구조로 이루어진다. 즉 제1 본체(300)의 제1 열교환 블록(700)은 일정 간격을 두고 복수 개 설치되고 제1 열교환 블록(700) 사이에는 제1 와류발생 블록(750)이 각각 설치되고, 제2 본체(400)의 제2 열교환 블록(800) 역시 각각 일정 간격을 두고 복수 개 설치되고 제2 열교환 블록(800) 사이에는 제2 와류발생 블록(850)이 각각 설치된다, 그리고, 대응되는 상하 제1,2 열교환 블록(700,800)끼리 열매체를 주고받아 열교환을 하게 된다.</description><language>eng ; fre ; kor</language><subject>APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS ; BLASTING ; CHEMICAL RIPENING OF FRUIT OR VEGETABLES ; CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE ORHEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS ; CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS ; DRYING ; DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM ; FOODS OR FOODSTUFFS ; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC ; GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS ; HEAT EXCHANGE IN GENERAL ; HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT ; HEATING ; HUMAN NECESSITIES ; LIGHTING ; MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLESOR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR ; MECHANICAL ENGINEERING ; PEELING VEGETABLES OR FRUIT IN BULK ; PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT,VEGETABLES, EDIBLE SEEDS ; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS ; TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE ; THE PRESERVED, RIPENED, OR CANNED PRODUCTS ; THEIR TREATMENT, NOT COVERED BY OTHER CLASSES ; WEAPONS</subject><creationdate>2017</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20170601&amp;DB=EPODOC&amp;CC=WO&amp;NR=2017090834A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,309,781,886,25566,76549</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20170601&amp;DB=EPODOC&amp;CC=WO&amp;NR=2017090834A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>WIE, Hyung Chul</creatorcontrib><creatorcontrib>LEE, Sang Ro</creatorcontrib><creatorcontrib>JANG, Se Gyeong</creatorcontrib><title>MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM</title><description>A multi-stage separation heat-exchange type drying system according to the present invention is configured such that, if warm air (hereinafter 'first air') of waste heat discharged from a dryer (100) enters a heat exchange device (900) through a discharge line (110), the heat exchange device (900) performs a heat exchange so as to recover heat from the warm first air and supply the heat to outdoor cold air (hereinafter 'second air') and then discharge the heat. The heat exchange between the first air and the second air is performed by a heat medium, and the heat medium absorbs heat from the warm first air introduced to a first main body (300) by circulating throughout the first main body (300) and then is introduced to a second main body (400), and the heat medium introduced to the second main body (400) supplies heat to the cold second air. The first main body (300) and the second main body (400) of the heat exchange device (900) have structures corresponding to each other. That is, a plurality of first heat exchange blocks (700) of the first main body (300) are installed to be spaced from each other at a predetermined interval, and first vortex generating blocks (750) are installed between the first heat exchange blocks (700). Also, a plurality of second heat exchange blocks (800) of the second main body (400) are installed to be spaced apart from each other at a predetermined interval, and second vortex generating blocks (850) are installed between the second heat exchange blocks (800). The heat exchange occurs in a manner that the first heat exchange blocks (700) and the second heat exchange blocks (800) corresponding to each other, positioned up and down, exchange a heat medium therebetween. Un système de séchage du type à échange thermique avec séparation multi-étage selon la présente invention est configuré de telle sorte que, si de l'air chaud (désigné ci-après 'premier air') de chaleur perdue refoulé par un dispositif de séchage (100) pénètre dans un dispositif d'échange thermique (900) par une conduite de refoulement (110), le dispositif d'échange thermique (900) effectue un échange thermique de manière à récupérer la chaleur du premier air chaud et à transmettre la chaleur à l'air froid extérieur (désigné ci-après 'second air'), puis à évacuer la chaleur. L'échange de chaleur entre le premier air et le second air est effectué par un fluide caloporteur et le fluide caloporteur absorbe la chaleur du premier air chaud introduit dans un premier corps principal (300) par circulation à travers le premier corps principal (300) et est ensuite introduit dans un second corps principal (400) et le fluide caloporteur introduit dans le second corps principal (400) transmet la chaleur au second air froid. Le premier corps principal (300) et le second corps principal (400) du dispositif d'échange thermique (900) présentent des structures correspondant l'une à l'autre. En d'autres termes, une pluralité de premiers blocs d'échange thermique (700) du premier corps principal (300) sont installés de manière à être espacés les uns des autres à un intervalle prédéterminé, et des premiers blocs de génération de tourbillons (750) sont installés entre les premiers blocs d'échange thermique (700). En outre, une pluralité de seconds blocs d'échange thermique (800) du second corps principal (400) sont installés de façon à être espacés les uns des autres à un intervalle prédéterminé, et des seconds blocs de génération de tourbillons (850) sont installés entre les seconds blocs d'échange thermique (800). L'échange thermique se produit de façon à ce que les premiers blocs d'échange thermique (700) et les seconds blocs d'échange thermique (800) correspondant les uns aux autres, disposés en haut et en bas, s'échangent un fluide caloporteur. 개시된 본 발명에 따른 다단 분리 열교환방식의 건조 시스템은, 건조기(100)에서 배출되는 폐열의 따뜻한 공기(이하 '제1공기'라 함)가 배출라인(110)을 통해 열교환 장치(900)로 유입되면, 열교환 장치(900)는 따뜻한 제1공기로부터 열을 회수하여 이를 외기의 차가운 공기(이하 '제2공기'라 함)로 공급 하도록 열교환 한 후 배출 시키게 된다. 상기 제1공기와 제2공기의 열교환은 열매체에 의해 이루어지게 되며, 열매체가 제1 본체(300)를 순환하여 제1 본체(300)로 유입되는 따뜻한 제1공기로부터 열을 흡수한 후 제2 본체(400)로 유입되고, 제2 본체(400)로 유입된 열매체는 차가운 제2공기에 열을 공급 하도록 한다. 열교환 장치(900)의 제1 본체(300)와 제2 본체(400)는 서로 대응되는 구조로 이루어진다. 즉 제1 본체(300)의 제1 열교환 블록(700)은 일정 간격을 두고 복수 개 설치되고 제1 열교환 블록(700) 사이에는 제1 와류발생 블록(750)이 각각 설치되고, 제2 본체(400)의 제2 열교환 블록(800) 역시 각각 일정 간격을 두고 복수 개 설치되고 제2 열교환 블록(800) 사이에는 제2 와류발생 블록(850)이 각각 설치된다, 그리고, 대응되는 상하 제1,2 열교환 블록(700,800)끼리 열매체를 주고받아 열교환을 하게 된다.</description><subject>APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS</subject><subject>BLASTING</subject><subject>CHEMICAL RIPENING OF FRUIT OR VEGETABLES</subject><subject>CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE ORHEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS</subject><subject>CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS</subject><subject>DRYING</subject><subject>DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM</subject><subject>FOODS OR FOODSTUFFS</subject><subject>GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC</subject><subject>GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS</subject><subject>HEAT EXCHANGE IN GENERAL</subject><subject>HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT</subject><subject>HEATING</subject><subject>HUMAN NECESSITIES</subject><subject>LIGHTING</subject><subject>MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLESOR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR</subject><subject>MECHANICAL ENGINEERING</subject><subject>PEELING VEGETABLES OR FRUIT IN BULK</subject><subject>PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT,VEGETABLES, EDIBLE SEEDS</subject><subject>TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS</subject><subject>TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE</subject><subject>THE PRESERVED, RIPENED, OR CANNED PRODUCTS</subject><subject>THEIR TREATMENT, NOT COVERED BY OTHER CLASSES</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2017</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDD3DfUJ8dQNDnF0d1UIdg1wDHIM8fT3U_BwdQzRdY1w9nD0A0qERAa4KrgERXr6uSsERwaHuPryMLCmJeYUp_JCaW4GZTfXEGcP3dSC_PjU4oLE5NS81JL4cH8jA0NzA0sDC2MTR0Nj4lQBAPayKVo</recordid><startdate>20170601</startdate><enddate>20170601</enddate><creator>WIE, Hyung Chul</creator><creator>LEE, Sang Ro</creator><creator>JANG, Se Gyeong</creator><scope>EVB</scope></search><sort><creationdate>20170601</creationdate><title>MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM</title><author>WIE, Hyung Chul ; LEE, Sang Ro ; JANG, Se Gyeong</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_WO2017090834A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre ; kor</language><creationdate>2017</creationdate><topic>APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS</topic><topic>BLASTING</topic><topic>CHEMICAL RIPENING OF FRUIT OR VEGETABLES</topic><topic>CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE ORHEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS</topic><topic>CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS</topic><topic>DRYING</topic><topic>DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM</topic><topic>FOODS OR FOODSTUFFS</topic><topic>GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC</topic><topic>GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS</topic><topic>HEAT EXCHANGE IN GENERAL</topic><topic>HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT</topic><topic>HEATING</topic><topic>HUMAN NECESSITIES</topic><topic>LIGHTING</topic><topic>MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLESOR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR</topic><topic>MECHANICAL ENGINEERING</topic><topic>PEELING VEGETABLES OR FRUIT IN BULK</topic><topic>PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT,VEGETABLES, EDIBLE SEEDS</topic><topic>TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS</topic><topic>TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE</topic><topic>THE PRESERVED, RIPENED, OR CANNED PRODUCTS</topic><topic>THEIR TREATMENT, NOT COVERED BY OTHER CLASSES</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>WIE, Hyung Chul</creatorcontrib><creatorcontrib>LEE, Sang Ro</creatorcontrib><creatorcontrib>JANG, Se Gyeong</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>WIE, Hyung Chul</au><au>LEE, Sang Ro</au><au>JANG, Se Gyeong</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM</title><date>2017-06-01</date><risdate>2017</risdate><abstract>A multi-stage separation heat-exchange type drying system according to the present invention is configured such that, if warm air (hereinafter 'first air') of waste heat discharged from a dryer (100) enters a heat exchange device (900) through a discharge line (110), the heat exchange device (900) performs a heat exchange so as to recover heat from the warm first air and supply the heat to outdoor cold air (hereinafter 'second air') and then discharge the heat. The heat exchange between the first air and the second air is performed by a heat medium, and the heat medium absorbs heat from the warm first air introduced to a first main body (300) by circulating throughout the first main body (300) and then is introduced to a second main body (400), and the heat medium introduced to the second main body (400) supplies heat to the cold second air. The first main body (300) and the second main body (400) of the heat exchange device (900) have structures corresponding to each other. That is, a plurality of first heat exchange blocks (700) of the first main body (300) are installed to be spaced from each other at a predetermined interval, and first vortex generating blocks (750) are installed between the first heat exchange blocks (700). Also, a plurality of second heat exchange blocks (800) of the second main body (400) are installed to be spaced apart from each other at a predetermined interval, and second vortex generating blocks (850) are installed between the second heat exchange blocks (800). The heat exchange occurs in a manner that the first heat exchange blocks (700) and the second heat exchange blocks (800) corresponding to each other, positioned up and down, exchange a heat medium therebetween. Un système de séchage du type à échange thermique avec séparation multi-étage selon la présente invention est configuré de telle sorte que, si de l'air chaud (désigné ci-après 'premier air') de chaleur perdue refoulé par un dispositif de séchage (100) pénètre dans un dispositif d'échange thermique (900) par une conduite de refoulement (110), le dispositif d'échange thermique (900) effectue un échange thermique de manière à récupérer la chaleur du premier air chaud et à transmettre la chaleur à l'air froid extérieur (désigné ci-après 'second air'), puis à évacuer la chaleur. L'échange de chaleur entre le premier air et le second air est effectué par un fluide caloporteur et le fluide caloporteur absorbe la chaleur du premier air chaud introduit dans un premier corps principal (300) par circulation à travers le premier corps principal (300) et est ensuite introduit dans un second corps principal (400) et le fluide caloporteur introduit dans le second corps principal (400) transmet la chaleur au second air froid. Le premier corps principal (300) et le second corps principal (400) du dispositif d'échange thermique (900) présentent des structures correspondant l'une à l'autre. En d'autres termes, une pluralité de premiers blocs d'échange thermique (700) du premier corps principal (300) sont installés de manière à être espacés les uns des autres à un intervalle prédéterminé, et des premiers blocs de génération de tourbillons (750) sont installés entre les premiers blocs d'échange thermique (700). En outre, une pluralité de seconds blocs d'échange thermique (800) du second corps principal (400) sont installés de façon à être espacés les uns des autres à un intervalle prédéterminé, et des seconds blocs de génération de tourbillons (850) sont installés entre les seconds blocs d'échange thermique (800). L'échange thermique se produit de façon à ce que les premiers blocs d'échange thermique (700) et les seconds blocs d'échange thermique (800) correspondant les uns aux autres, disposés en haut et en bas, s'échangent un fluide caloporteur. 개시된 본 발명에 따른 다단 분리 열교환방식의 건조 시스템은, 건조기(100)에서 배출되는 폐열의 따뜻한 공기(이하 '제1공기'라 함)가 배출라인(110)을 통해 열교환 장치(900)로 유입되면, 열교환 장치(900)는 따뜻한 제1공기로부터 열을 회수하여 이를 외기의 차가운 공기(이하 '제2공기'라 함)로 공급 하도록 열교환 한 후 배출 시키게 된다. 상기 제1공기와 제2공기의 열교환은 열매체에 의해 이루어지게 되며, 열매체가 제1 본체(300)를 순환하여 제1 본체(300)로 유입되는 따뜻한 제1공기로부터 열을 흡수한 후 제2 본체(400)로 유입되고, 제2 본체(400)로 유입된 열매체는 차가운 제2공기에 열을 공급 하도록 한다. 열교환 장치(900)의 제1 본체(300)와 제2 본체(400)는 서로 대응되는 구조로 이루어진다. 즉 제1 본체(300)의 제1 열교환 블록(700)은 일정 간격을 두고 복수 개 설치되고 제1 열교환 블록(700) 사이에는 제1 와류발생 블록(750)이 각각 설치되고, 제2 본체(400)의 제2 열교환 블록(800) 역시 각각 일정 간격을 두고 복수 개 설치되고 제2 열교환 블록(800) 사이에는 제2 와류발생 블록(850)이 각각 설치된다, 그리고, 대응되는 상하 제1,2 열교환 블록(700,800)끼리 열매체를 주고받아 열교환을 하게 된다.</abstract><oa>free_for_read</oa></addata></record>
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subjects APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
BLASTING
CHEMICAL RIPENING OF FRUIT OR VEGETABLES
CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE ORHEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS
DRYING
DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
FOODS OR FOODSTUFFS
GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS
HEAT EXCHANGE IN GENERAL
HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
HEATING
HUMAN NECESSITIES
LIGHTING
MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLESOR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR
MECHANICAL ENGINEERING
PEELING VEGETABLES OR FRUIT IN BULK
PRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT,VEGETABLES, EDIBLE SEEDS
TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
THE PRESERVED, RIPENED, OR CANNED PRODUCTS
THEIR TREATMENT, NOT COVERED BY OTHER CLASSES
WEAPONS
title MULTI-STAGE SEPARATION HEAT-EXCHANGE TYPE DRYING SYSTEM
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