KR20020013950A - Bubbler apparatus for perlite - Google Patents
Bubbler apparatus for perlite Download PDFInfo
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- KR20020013950A KR20020013950A KR1020020003835A KR20020003835A KR20020013950A KR 20020013950 A KR20020013950 A KR 20020013950A KR 1020020003835 A KR1020020003835 A KR 1020020003835A KR 20020003835 A KR20020003835 A KR 20020003835A KR 20020013950 A KR20020013950 A KR 20020013950A
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- foaming
- pipe
- heat exchanger
- collector
- dust separator
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28B1/00—Producing shaped prefabricated articles from the material
- B28B1/50—Producing shaped prefabricated articles from the material specially adapted for producing articles of expanded material, e.g. cellular concrete
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B14/00—Use of inorganic materials as fillers, e.g. pigments, for mortars, concrete or artificial stone; Treatment of inorganic materials specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B14/02—Granular materials, e.g. microballoons
- C04B14/04—Silica-rich materials; Silicates
- C04B14/14—Minerals of vulcanic origin
- C04B14/18—Perlite
- C04B14/185—Perlite expanded
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Ceramic Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
본 발명은 퍼얼라이트(Perlite) 발포장치에 관한 것으로 퍼얼라이트 발포재는 건축자재인 단열재 콘크리이트경량골재 및 보온재로 많이 이용되고 있다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a Perlite foaming apparatus, which is widely used as a heat-insulating material for concrete aggregate and thermal insulation material, which is a building material.
이러한 용도로 많이 이용되고 있는 퍼얼라이트 발포재는 진주암(Perlite)을 필요에 따라 16메쉬 내지 40메쉬로 분쇄한 진주암석분을 고온에서 발포하여 얻어지게 되는바 본 발명은 장치구성인 퍼얼라이트 발포장치를 수개등분으로 분리시켜서 제작하고 사용시 운반조립하여 가스탱크 등 연료탱크의 외부보온을 현장에서 발포와 동시에 보온커버내에 충진하여 보온층을 간단히 작업실시 할수 있도록 구성시킨 것이다. 즉 수개등분으로 발포장치 분리하여 이송조립하므로 현장에서 직접 발포작업을 실시하여 가스탱크 외부거푸집 내에 퍼얼라이트 발포재를 공기압충진 작업으로 현장에서 능률적으로 작업실시 할수 있고 또 공장내에 설비하여서도 퍼얼라이트 발포재를 대량생산 할수 있도록 한 것이다.The pearlite foam material which is widely used for this purpose is obtained by foaming pearlite powder pulverized into 16 mesh to 40 mesh at a high temperature as needed. It is manufactured to be separated into several parts and transported and assembled during use, so that the external insulation of fuel tanks such as gas tanks is filled in the thermal cover at the same time as foaming at the site, so that the thermal insulation layer can be easily performed. In other words, since the foaming device is separated and transported into several parts, the foaming work can be carried out directly on site, and the work can be efficiently carried out on site by air pressure filling work in the external formwork of the gas tank. It was designed to mass produce ash.
특히 본 발명은 퍼얼라이트 발포장치에 의하여 일괄처리될 뿐아니라 집진기와 열교환기 및 미분진 분리기를 함께 구성시켜 보다 안전한 발포작업을 실시 할수 있고 또 발포작업을 손쉽게 할수 있도록 할 목적에 있다.In particular, the present invention is not only batch-processed by the pearlite foaming device but also comprises a dust collector, a heat exchanger and a fine dust separator together to provide a safer foaming operation and to facilitate the foaming operation.
기존의 퍼얼라이트 발포기는 수평으로 설치된 발포로내에 16∼40메쉬로 분쇄한 각각의 분말진주암을 투입하고 고열의 가열로서 발포하도록 하는 수평고정식의 공장발포기였다. 이러한 고정정착식 발포기는 그 시설구성이 복잡하게 되어 있을 뿐더러 발포작업 운전에 불편함과 발포가 비능률적이였다.The existing Perlite foaming machine was a horizontal fixed type factory foaming machine which puts each powder pearl rock crushed into 16-40 mesh in a horizontally installed foaming furnace and foams it by heating with high heat. This fixed-settling foamer was not only complicated in its construction, but also inconvenient in foaming operation and inefficient foaming.
또 발포재료를 용기에 포장하는 제품만을 산출하게 되므로 원거리의 거대한 가스탱크의 보온시설에 운반과 설치비용 등이 많이 소요되므로 고가의 보온설비를 해야하고 특히 공장주변에 많은 가스배출과 먼지 등이 유출되어 공기중에 혼합되므로 환경오염에도 큰 문제가 있어 왔다.In addition, since only the product that packs the foamed material into the container is calculated, it requires a lot of transportation and installation cost in the insulation facility of a huge gas tank in a long distance. Therefore, expensive insulation equipment must be installed. Since it is mixed in the air, there has been a big problem in environmental pollution.
본 발명은 종래 그와같은 문제점을 개선하고 현장에서도 손쉽게 발포작업과 보온시공을 간편하게 할수 있는 퍼얼라이트 발포장치를 제공하고져 하는 것이다.The present invention is to improve the conventional problems and to provide a pearlite foaming device that can easily foaming work and insulation construction in the field.
본 발명은 필요에 따라 16메쉬∼40메쉬로 분쇄시킨 분말진주암을 건조시켜주는 예열건조장치와 예열건조장치에서 건조시킨 건조분말진주암을 고열로 발포시키는 입치식 발포장치를 연결관에서 용이하게 조립과 분해가 되게하고 또 집진기와 열교환기 및 미분진 분리기를 연결관 긴도관 및 연결곡관에서 손쉽게 조립 분해될수 있도록 구성시켜 이송을 위한 분해와 현장에 운반하여 조립이 간단히 이루어지도록 하고 또 미분진을 분리시켜 열교관기에서 냉각과 함께 집진기에서 집진배열 처리를 실시하게 하므로 보다 안전한 발포작업을 실시 할수 있도록 한 것이다.The present invention can be easily assembled and assembled in a connecting pipe with a preheating drying device for drying the powdered pearl rock pulverized into 16 mesh to 40 mesh and a dry powdered pearl rock dried in the preheating dryer at high temperature. The dust collector, heat exchanger and fine dust separator can be easily assembled and disassembled in the connecting pipe long conduit and connecting curved pipe so that they can be disassembled for transportation and transported to the site for simple assembly and separate the fine dust. The cooling pipe in the heat piper and the dust collector in the dust collector are treated so that the safer foaming can be performed.
또한 본 발명은 위에서 열거된 예열건조장치, 발포장치, 집진기, 열교환기, 미분진 분리기는 각각 연결관 긴도관 및 연결곡관에서 쉽게 조립설치가 되므로 공장에 간단히 설비 이용될 수가 있고 또 손쉽게 운전할 수 있도록 할 목적에 있다. 또한 본 발명은 환경오염에 안전한 퍼얼라이트 발포장치를 제공할 목적에 있다.In addition, the present invention is the preheat drying device, foaming device, dust collector, heat exchanger, fine dust separator listed above can be easily installed and installed in the connecting pipe long conduit and connecting curved pipe, respectively, so that the plant can be simply used and easily operated The purpose is to. It is another object of the present invention to provide a pearlite foaming apparatus which is safe against environmental pollution.
본 발명을 첨부도면에 따라 상세히 설명하면 다음과 같다.The present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명의 평면구성을 보인 평면도1 is a plan view showing a planar configuration of the present invention
도 2는 본 발명의 개략측면도2 is a schematic side view of the present invention;
도 3은 본 발명에 있어 예열로에서 발포장치에 연결된 구성을 보인 발포장치의 측면도Figure 3 is a side view of the foaming apparatus showing a configuration connected to the foaming apparatus in the preheating furnace in the present invention
도 4는 본 발명에 있어서 예열로의 확대단면도Figure 4 is an enlarged cross-sectional view of the preheating furnace in the present invention
도 5는 도 4의 평단면도5 is a cross-sectional view of FIG.
도 6은 본 발명에 있어 발포재를 분리장치의 측면도Figure 6 is a side view of the foam separating device in the present invention
도 7은 도 6의 평면도7 is a plan view of FIG.
도 8은 본 발명에 있어 예열로의 측면도Figure 8 is a side view of the preheating furnace in the present invention
도 9는 본 발명에 있어 집진기의 측단면도Figure 9 is a side cross-sectional view of the dust collector in the present invention
도 10은 도 9의 종단면도10 is a longitudinal cross-sectional view of FIG.
도 11은 본 발명의 발포장치에 나오는 집진기의 분진발포재와 포집통에서 나오는 발포재를 혼합배출시키는 혼합배출기의 측면도11 is a side view of the mixing discharger for mixing and discharge the dust foaming material of the dust collector and the foaming material coming out of the collecting container in the foaming apparatus of the present invention
도면의 중요부분에 대한 부호의 설명Explanation of symbols for important parts of the drawings
1 : 예열건조장치 2 : 발포장치 3 : 집진기1: preheat drying device 2: foaming device 3: dust collector
4 : 열교환기 5 : 미분진 분리기 15 : 버켓이송장치4 heat exchanger 5 fine dust separator 15 bucket transfer device
20 : 연결관 21 : 연결곡관 21a, 21b : 연결관20: connector 21: connector 21a, 21b: connector
21c : 긴도관 22 : 사이클론 23 : 포집기21c: long conduit 22: cyclone 23: collector
24 : 에어공급부 25 : 배출관24: air supply unit 25: discharge pipe
본 발명은 도 1에 도시와 같이 용도에 따라 16메쉬∼40메쉬로 분쇄한 분말진주암을 예열건조시켜주는 예열건조장치(1)와 건조시킨 분말진주암을 발포시키는 발포장치(2)와 집진기 (3) 열교환기(4) 및 미분진 분리기(5)로 결합 구성된다.1 is a preheating drying apparatus 1 for preheating and drying a powdered pearl arm pulverized into 16 meshes to 40 meshes as shown in FIG. 1, and a foaming apparatus 2 and a dust collector 3 for foaming the dried powdered pearl arm. A) consisting of a heat exchanger (4) and a fine dust separator (5).
예열건조장치(1)는 도 4 및 도 5의 단면에서 보는 바와같이 중심부의 건조로 (6)가 배기통(7)과 지지통(8) 사이에 회전가능하게 장착되어 있고 건조로(6) 외면에는 재료유통공극(9)(9′)이 이중으로 형성되어 외면에 보온커버(10)가 씌워져 있다. 일측 버어너(11)의 열이 건조로(6)내에서 연소가열하고 또 배기통(7)으로 가스가 배열된다. 외부의 스크류식 정량투입기(12)로 부터 투입된 16∼40메쉬의 분말진주암은 투입통(13)으로 하부로 투입되어져서 건조로(6) 외면에 형성된 재료유통공극(9)(9′)으로 이송될 때 수열 건조되어지고 재료유통공극(9)과 재료유통공극 (9′) 끝부인 지지통(8) 하부내에서 화살표 방향으로 유도이송되어져서 건조되고배출통(40)을 통해 버켓이송장치(18)로 이송되게 구성된다. 건조된 분말진주암은 버켓이송장치(15)로서 발포장치(2)에 이송 공급시키도록 구성되었다.As shown in the cross-sectional view of FIGS. 4 and 5, the preheating drying apparatus 1 has a drying furnace 6 in the center thereof rotatably mounted between the exhaust cylinder 7 and the supporting cylinder 8 and the outer surface of the drying furnace 6. The material distribution gap 9 (9 ') is formed in a double, and the heat insulating cover 10 is covered on the outer surface. The heat of one side burner 11 is burned and heated in the drying furnace 6, and the gas is arranged in the exhaust cylinder 7. 16 to 40 mesh powder pearl arms introduced from the external screw-type dosing machine 12 are introduced into the input container 13 to the material distribution voids 9 and 9 'formed on the outer surface of the drying furnace 6. When transported, it is hydrothermally dried and guided in the direction of the arrow in the lower part of the support container 8, which is the end of the material distribution void 9 and the material distribution void 9 ', and is dried and the bucket conveying device through the discharge container 40. It is configured to be transferred to 18. The dried powder pearl arm was configured to be fed to the foaming apparatus 2 as a bucket transfer apparatus 15.
발포장치(2)는 도 3에서와 같이 세워서 설치한 수직발포로(16)가 입치되고 연결관(20)으로 버켓이송장치(15)와 연결된다. 세워 설치한 수직발포로(16) 하단부에 버어너(17)가 설치되어서 수직발포로(16) 내로 하부에서 상부로 가열연소 하도록 되어 있고 겸하여 일측에 대기공기의 강제송풍휀(18)이 설치되어 외부 대기공기를 취입하게 되어 있다. 여기에 연결관(20)을 통해 들어온 건조시킨 분말진주암은 내하부온도 950∼1000℃에서 7∼10배로 발포가 이루어진다. 또한 수직발포로(16) 상부의 온도는 850∼900℃의 온도가 유지되게 버어너 (17)의 가열온도를 조정 사용한다. 또한 수직발포로(16)의 외면은 냉각공기유통공극(19)을 형성시켜 냉공기유통이 되게하므로 발포재의 내면부착을 방지하게 하였다.The foaming apparatus 2 has a vertical foaming passage 16 installed upright as shown in FIG. 3, and is connected to the bucket transfer apparatus 15 by a connecting pipe 20. The burner 17 is installed at the lower end of the vertical foaming furnace 16 which is installed upright, and it is configured to heat and burn the upper to upper vertical foaming furnace 16, and a forced air blow 18 of atmospheric air is installed at one side. It is supposed to blow outside atmospheric air. Here, the dried powder pearl rock that came in through the connecting pipe 20 is foamed by 7 to 10 times at an internal lower temperature of 950 to 1000 ° C. In addition, the temperature of the upper part of the vertical foaming furnace 16 adjusts the heating temperature of the burner 17 so that the temperature of 850-900 degreeC may be maintained. In addition, the outer surface of the vertical foaming passage 16 forms a cooling air flow gap 19 to be a cold air flow, thereby preventing the adhesion of the inner surface of the foam material.
발포재는 상부 연결곡관(21)을 통해 분리되어 나간다. 또한 연결곡관(21)은 긴도관(21c)와 도 6의 미분진 분리기(5) 상부의 사이클론(22)에 연결되어서 발포재가 주입되고 미분진분리기(5)내 하부 포집통(23) 저면의 에어공급부(24)로 부터 공기의 강제공급으로 발포재가 배출관(25)을 통하여 나간다. 이때 현장의 가스탱크 등의 외부보온시공이 가능케 된다. 또한 미분진 분리기(5) 상부 사이클론(22) 내부로는 연교환기(4)의 연결관(21a)이 연결되므로 미분진 분리기(5) 내에서는 전체발포재 100 에 대하여 약 70%는 배출관(25)으로 나가게 되고 미분진 발포재 약 30%는 연결관(21a)을 통해 열교환기(4)를 통과하고 또 연결관(21b)으로 연결시킨 집진기 (3)로 나가게 되어 집진기(3)를 통과한 미분진의 발포재는 또한 현장보온재로 같이이용하게 된다. 열교환기(4)와 집진기(3)에는 공기흡입휀(26)(26a)을 부착하여 공기흡입으로 열교환기(4) 및 집진기(3) 내의 열공기를 흡입시키게 구성된다. 또한 집진기(3)내 하부에 포집기(41)가 있고 포집기(41) 하부측에 배출구(42)가 형성되어 미분진 발포재가 배출구(42)에서 나간다. 또 공기취입구(43)로 공기취임이 되도록 구성하였고 집진기(3)의 배열은 상부측의 배기통(45)으로 가스가 배출된다. 포집기(41) 저면에는 공기공급부(44)가 설치 되어있다.The foam material is separated through the upper connection pipe 21. In addition, the connecting curved tube 21 is connected to the long conduit 21c and the cyclone 22 of the upper part of the dust separator 5 of FIG. 6 so that the foam material is injected, and the bottom surface of the lower collecting container 23 in the dust separator 5 is connected. By the forced supply of air from the air supply unit 24, the foamed material exits through the discharge pipe 25. At this time, it is possible to construct external insulation such as gas tank on site. In addition, since the connecting pipe 21a of the lead exchanger 4 is connected inside the upper dust cyclone 22 of the fine dust separator 5, about 70% of the total foaming material 100 in the fine dust separator 5 is discharge pipe 25. ) And about 30% of the fine dust foam passes through the heat exchanger (4) through the connecting pipe (21a) and to the dust collector (3) connected to the connecting pipe (21b) to pass through the dust collector (3). Fine dust foam is also used as field insulation. An air suction fan 26 and 26a are attached to the heat exchanger 4 and the dust collector 3 so as to suck the hot air in the heat exchanger 4 and the dust collector 3 by air suction. In addition, there is a collector 41 in the lower part of the dust collector 3 and the outlet 42 is formed in the lower side of the collector 41, so that the fine dust foam material exits the outlet 42. In addition, the air intake 43 is configured to be air intake and the arrangement of the dust collector 3 is the gas discharged to the exhaust pipe 45 of the upper side. The air supply unit 44 is installed on the bottom of the collector 41.
열교환기(4)의 배열은 배열통(4′)을 통해 배기된다. 또 본 발명은 긴도관 (21c) 연결곡관 (21)과 사이클론(22) 사이에 착탈가능하게 연결사용하므로 분해조립이 된다. 여기의 열교환기(4)는 집진기(3) 내로 유입되기 전의 배기열을 열교환기(4)에서 냉각시키므로 집진기(3)의 보호가 되고 과열공기로 인한 집진기(3)의 고장을 방지하게 된다.The arrangement of the heat exchanger 4 is exhausted through the array cylinder 4 '. In addition, the present invention is disassembled and assembled because of the detachable connection between the long pipe 21c connecting curved pipe 21 and the cyclone 22. Since the heat exchanger 4 here cools the exhaust heat before entering the dust collector 3 in the heat exchanger 4, the heat exchanger 4 is protected by the dust collector 3 and prevents failure of the dust collector 3 due to overheated air.
또한 본 발명은 집진기(3)에서 나오는 분진발포재와 포집통(23)에서 나오는 발포재를 홉합사용하기 위하여 도 11의 혼합배출기(30)를 사용할 수도 있으며 주입기(31)과 주입기(31′)에 각각 자바라호오스(32)로 연결하여 하부 송풍휀(33)으로 송풍가압하여 혼합관(34)을 통해 혼합배출하여 가스탱크 보온용으로 현장에서 혼합 사용하도록 한다.In addition, the present invention may use the mixed discharger 30 of FIG. 11 in order to hop-use the dust foaming material coming out of the dust collector 3 and the foaming material coming out of the collecting container 23, and the injector 31 and the injector 31 '. Connected to each of the Java lahose 32 in the blower pressurized by the lower blower 33 to mix and discharge through the mixing pipe 34 to be used in the field for the gas tank insulation.
이러한 본 발명은 정량투입기(12)에서 주입된 16∼40메쉬의 분쇄진주암은 발포장치(2)에 주입되기전 예열건조장치(1)의 건조로(16) 외부 재료유통공극(9)(9′)을 통과 및 이송배출되면서 습기를 건조하고 또 버켓이송장치(15)로서 연결관(20)을 통해 발포장치(2)에 이송주입되면, 세워 설치한 수직발포로(16) 하부에 설치된 버어너(17)의 연소가열로서 로내하부온도 950∼1000℃의 고열에 의하여 발포가 이루어진다. 이때 발포는 7∼10배로 발포가 된다. 또한 수직발포로(16) 내의 상부온도는 850∼900℃의 온도가 유지되므로 발포재는 상부로 부상하여 연결곡관(21) 긴도관(21c) 및 사이클론(22)을 통해 미분진 분리기(5)의 포집통(23)에서 배출관 (25)을 통하여 현장의 가스탱크 외부보온충진시공에 직접 발포재가 공급케 되는데 본 발명은 이때 발포재 100 에 대하여 약 70%만 포집통(23)에서 배출되어 나가고 약 30%의 미분발포재는 상부로 분리 부상하여 연결관(21a)을 통해 열교환기(4) 및 집진기(3)에 운반되어져서 가스는 배기통(45)을 통해 배기케되는 집진작용에 의하여 집진케 되므로 집진기(3)를 통과한 잔여 미분발포재를 배출시켜 가스탱크 외부보온충진시공에 같이 혼입사용 할수 있으므로 발포재 이용에 큰 도움이 되고 경제적이다. 또한 열교환기(4)를 집진기(3)에 연결 설치하여 집진기(3) 내의 열교환을하게 하므로 집진기(3)가 원활히 작용을 하게 된다. 또한 발포장치(2)의 수직발포로(16) 외부에 설치된 냉각공기유통공극(19)으로 인하여 내벽면을 냉각시키므로 발포재가 벽면에 부착되지 않게 되므로 발포작업이 능률적이다.In the present invention, the 16-40 mesh pulverized pearl rock injected from the metering machine 12 is dried in the preheating and drying device 1 before the injection into the foaming device 2. ′) Is dried while passing and conveying discharged and transferred to the foaming device 2 through the connecting pipe 20 as a bucket transfer device (15), the burr installed in the lower vertical foaming (16) installed upright As the combustion heating of the honor 17, foaming is performed by high temperature of 950-1000 degreeC of lower part of furnace. At this time, the foaming is foamed 7 to 10 times. In addition, since the upper temperature in the vertical foaming furnace 16 is maintained at a temperature of 850 ~ 900 ℃, the foam material rises to the upper portion of the fine dust separator 5 through the connecting curved tube 21, the long conduit 21c and the cyclone 22 The foaming material is directly supplied to the on-site gas tank external insulation filling construction through the discharge pipe 25 in the collecting container 23. In the present invention, only about 70% of the foaming material 100 is discharged from the collecting container 23 and is about Since 30% of the fine powder is separated and floated to the upper part and is transported to the heat exchanger 4 and the dust collector 3 through the connecting pipe 21a, the gas is collected by the dust collecting action exhausted through the exhaust pipe 45. The remaining fine foamed material passed through the dust collector (3) can be mixed and used together with the gas tank external heat filling construction, so it is very helpful and economical to use the foamed material. In addition, the heat exchanger 4 is connected to the dust collector 3 so that the heat exchange in the dust collector 3 allows the dust collector 3 to function smoothly. In addition, since the inner wall surface is cooled due to the cooling air flow gap 19 installed outside the vertical foaming passage 16 of the foaming apparatus 2, the foaming material is not attached to the wall, so the foaming operation is efficient.
이와같은 본 발명은 연결관(20)의 착탈로서 예열건조장치(1) 및 버켓이송장치(15)와 발포장치(2)가 분리 또는 조립연결설치가 되고 또 긴도관(21c)과 연결관 (21a)(21b)에서 미분진 분리기(5) 열교환기(4)와 집진기(3)가 또한 분리와 조립이 손쉽게 되므로 현장에 이동운반이 용이 간편하여 현장에서 조립 설치할 수 있어 가스탱크의 외부보온시공을 현장에서 직접 손쉽게 할수 있는 효과가 있고 또 공장에서 고정식으로도 정착 설치하여 사용할 수가 있어 이용에 간편하고 또한 본 발명은 긴도관(21c)과 사이클론(22)를 통하여 발포재가 투입되어져서 미분진 분리기(5)의 포집통(23)내에 주입될 때에는 발포재 약 70%만 포집통(23)내에 연결된 배출관(25)을 통해 배출되어지고 나머지 미분상태의 발포재 30%는 포집통(23) 위로 흡상 분리되어져서 연결관(21a)을 통해 열교환기(4) 및 집진기(3)로 나가므로 미분 상태의 발포재가 집진기(3)에 의한 집진작용으로 유해한 가스분진의 외부배출이 적어 환경에 안전한 효과도 있다.The present invention as described above is detachable or assembled connection installation of the preheating drying device (1) and the bucket transfer device (15) and the foaming device (2) as the attachment and detachment of the connecting pipe (20) and the long conduit (21c) and the connecting pipe ( In 21a) and 21b, the dust separator 5, the heat exchanger 4, and the dust collector 3 are also easy to separate and assemble, so that they can be easily transported and installed on site. It is easy to use directly in the field and can also be fixed and installed in the factory can be used in the installation is easy to use and also the present invention is introduced into the foam material through the long pipe (21c) and cyclone (22) fine dust separator When injected into the collecting container 23 of (5), only about 70% of the foam material is discharged through the discharge pipe 25 connected in the collecting container 23, and the remaining 30% of the finely divided foam material is placed on the collecting container 23. It is separated by suction and heat-exchanges through connecting pipe 21a. 4 and so out into a dust collector (3) is safe to effect less external emission of the harmful gas to the dust collecting effect of the foam material precipitator (3) of the differential state environment.
또한 본 발명은 집진기(3)에서 나온 분진발포재와 포집통(23)에서 배출관 (25)을 통해 나오는 발포재를 도 11의 도시와 같이 혼합배출기(30)를 이용하므로 고루 혼합사용하여 현장시공에 도움이 되도록하는 이점도 있다.In addition, the present invention uses the mixed discharge machine 30 as shown in Figure 11 the dust foaming material from the dust collector (3) and the foaming material coming out through the discharge pipe (25) in the collecting container 23, so that the site construction by using evenly mixed There are also benefits to help.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020020003835A KR20020013950A (en) | 2002-01-23 | 2002-01-23 | Bubbler apparatus for perlite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020020003835A KR20020013950A (en) | 2002-01-23 | 2002-01-23 | Bubbler apparatus for perlite |
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| Publication Number | Publication Date |
|---|---|
| KR20020013950A true KR20020013950A (en) | 2002-02-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| KR1020020003835A KR20020013950A (en) | 2002-01-23 | 2002-01-23 | Bubbler apparatus for perlite |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104402281A (en) * | 2014-11-21 | 2015-03-11 | 信阳凯米特环保工程有限公司 | Opening expanded perlite complete production equipment |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0524891A (en) * | 1991-07-16 | 1993-02-02 | Kawasaki Heavy Ind Ltd | Powder granulating facilities |
| JPH06135753A (en) * | 1992-10-28 | 1994-05-17 | Onoda Cement Co Ltd | Production of artificial lightweight aggregate and method therefor |
| JP2000281401A (en) * | 1999-03-31 | 2000-10-10 | Taiheiyo Cement Corp | Lightweight fine aggregate for concrete and its production |
| JP2001278646A (en) * | 2000-03-30 | 2001-10-10 | Taiheiyo Cement Corp | Method of producing baked and foamed fine particles |
-
2002
- 2002-01-23 KR KR1020020003835A patent/KR20020013950A/en not_active Application Discontinuation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0524891A (en) * | 1991-07-16 | 1993-02-02 | Kawasaki Heavy Ind Ltd | Powder granulating facilities |
| JPH06135753A (en) * | 1992-10-28 | 1994-05-17 | Onoda Cement Co Ltd | Production of artificial lightweight aggregate and method therefor |
| JP2000281401A (en) * | 1999-03-31 | 2000-10-10 | Taiheiyo Cement Corp | Lightweight fine aggregate for concrete and its production |
| JP2001278646A (en) * | 2000-03-30 | 2001-10-10 | Taiheiyo Cement Corp | Method of producing baked and foamed fine particles |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104402281A (en) * | 2014-11-21 | 2015-03-11 | 信阳凯米特环保工程有限公司 | Opening expanded perlite complete production equipment |
| CN104402281B (en) * | 2014-11-21 | 2016-09-14 | 信阳凯米特环保工程有限公司 | Perforate expanded perlite complete production unit |
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