KR20010008744A - Apparatus for carbonizing food waste continuously - Google Patents
Apparatus for carbonizing food waste continuously Download PDFInfo
- Publication number
- KR20010008744A KR20010008744A KR1019990026713A KR19990026713A KR20010008744A KR 20010008744 A KR20010008744 A KR 20010008744A KR 1019990026713 A KR1019990026713 A KR 1019990026713A KR 19990026713 A KR19990026713 A KR 19990026713A KR 20010008744 A KR20010008744 A KR 20010008744A
- Authority
- KR
- South Korea
- Prior art keywords
- food waste
- carbonization
- pyrolysis
- continuous carbonization
- central axis
- Prior art date
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- 239000010794 food waste Substances 0.000 title claims abstract description 63
- 238000010000 carbonizing Methods 0.000 title abstract description 4
- 238000003763 carbonization Methods 0.000 claims abstract description 74
- 238000000197 pyrolysis Methods 0.000 claims abstract description 35
- 238000009826 distribution Methods 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 230000007423 decrease Effects 0.000 claims 1
- 230000000149 penetrating effect Effects 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 3
- 150000001247 metal acetylides Chemical class 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 2
- 241000209504 Poaceae Species 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 235000013324 preserved food Nutrition 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000010920 waste tyre Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
본 발명은 음식쓰레기의 연속 탄화장치에 관한 것으로, 특히, 음식물쓰레기를 연속적으로 탄화처리하고, 탄화물응착제거장치를 형성하여 음식쓰레기의 탄화가 진행됨에 따라 발생하는 음식쓰레기의 응착현상을 효과적으로 제거할 수 있도록 한 것이다.The present invention relates to a continuous carbonization apparatus of food waste, in particular, to continuously remove the carbonization of food waste, and to form a carbide adhesion removal device to effectively remove the adhesion of food waste generated as the carbonization of food waste proceeds. I would have to.
이를위하여, 본 발명에서는 열분해탄화부의 중심축에 탄화물제거장치를 설치하였다. 이 탄화물제거장치는 중심축에 형성된 관통부를 통과하면서 중심축과 수직으로 설치된 탄화물응착제거장치의 양끝단에 스크랩퍼가 부착되어 있다. 탄화물응착제거장치는 열분해탄화부의 입구와 중간 2군데에 설치되어 있으며 경우에 따라서 2군데 이상 설치할수도 있다. 탄화물응착제거장치의 회전방향은 드럼형상의 열분해탄화부가 회전하는 방향과 같거나 반대로 할 수도 있다. 탄화물응착제거장치의 회전속도는 드럼형상의 열분해탄화부의 회전속도와 속도차이를 둔다. 회전속도는 탄화물응착제거장치의 회전속도가 열분해탄화부의 회전속도보다 빠르게 하는 것이 일반적이나, 반대로 회전속도를 느리게할 수 도 있다.To this end, in the present invention, a carbide removal apparatus is installed on the central axis of the thermal decomposition carbonization unit. The carbide removal device has scrapers attached to both ends of the carbide adhesion removal device installed perpendicularly to the central axis while passing through the through-hole formed in the central axis. Carbide adhesion removal device is installed in the middle of the inlet and the middle of the pyrolysis carbonization unit, may be installed in more than two places in some cases. The direction of rotation of the carbide adhesion removing apparatus may be the same as or opposite to the direction in which the drum-shaped pyrolysis carbonization unit rotates. The rotation speed of the carbide debonding device is the speed difference between the rotation speed of the drum-shaped pyrolysis carbonization unit. The rotational speed is generally such that the rotational speed of the carbide adhesion removing device is faster than the rotational speed of the pyrolysis carbonization unit, but may also slow down the rotational speed.
탄화물응착제거장치의 하단부 스크랩퍼가 스스로의 무게인 자중에 의해 열분해탄화부의 하부 벽면에 보다 완벽하게 밀착하여 응착된 탄화물이 효율적으로 제거되도록 구성하였다.The scraper at the lower end of the carbide adhesion removal apparatus was more closely adhered to the lower wall of the pyrolysis carbonization unit by its own weight, so that the adhered carbide was efficiently removed.
또한, 열분해탄화부의 끝 부분에는 스크류잭으로 구성된 높낮이조절장치를 형성하여 음식쓰레기의 탄화상태에 따라, 높낮이를 적절하게 조절하면서 원활하고 연속적인 탄화가 이루어질 수 있도록 구성하였다.In addition, the end portion of the pyrolysis carbonization portion is formed by adjusting the height adjustment device consisting of a screw jack according to the carbonization state of the food waste, it is configured to enable smooth and continuous carbonization while adjusting the height appropriately.
종래의 음식쓰레기 탄화장치는 도3과 같이 일정량의 음식쓰레기가 투입되면 탄화를 완료한 후 다시 음식쓰레기를 투입하는 비연속 탄화장치가 일반적으로 이용되고 있으며, 음식쓰레기를 연속탄화 하는데 적합한 장치는 소개되지 않고 있다. 이 같은 비연속탄화장치는 도3과 같이 음식쓰레기 투입부(302)에 형성된 투입구(301)를 통해 투입된 음식쓰레기가 밀봉을 위하여 채워놓은 액체(303)속으로 투입된 후 흡입장치(304)와 이송스크류(307-1)를 통해 음식쓰레기가 건조기(305)로 운반되고, 건조기에 형성된 회전부(306)가 회전하면서 음식쓰레기를 탈수 및 건조하고, 탈수 및 건조된 음식쓰레기는 이송스크류(307-2)를 통해 탄화기(308)속으로 투입되었다.Conventional food waste carbonization apparatus is a non-continuous carbonization apparatus is generally used to put the food waste again after the completion of the carbonization if a certain amount of food waste is input as shown in Figure 3, a suitable device for continuous carbonization of food waste introduced It is not. Such discontinuous carbonization apparatus is fed to the intake device 304 and then fed into the liquid 303 filled for sealing the food waste introduced through the inlet 301 formed in the food waste inlet 302 as shown in FIG. Food waste is conveyed to the dryer 305 through the screw 307-1, and the rotating part 306 formed in the dryer rotates to dehydrate and dry the food waste, and the dehydrated and dried food waste is transferred to the screw 307-2. Through the carbonizer 308.
탄화기(308)에서는 가열기(310)를 통해 공급된 열풍이 탄화기(308)의 열풍공급부(311)를 통해 공급되면서 탄화기(308)속의 음식쓰레기의 탄화가 진행된다. 탄화기(308)에는 중심축(309)에 회전날개(315)가 부착되어 있는데, 이는 음식쓰레기가 탄화되면서 탄화기(308)의 벽면에 응착되는 것을 제거하기 위한 것이다. 탄화과정에서 발생된 폐가스는 폐가스배출구(312)를 통해 연돌(314)로 배출된다.In the carbonizer 308, the hot air supplied through the heater 310 is supplied through the hot air supply unit 311 of the carbonizer 308, and carbonization of the food waste in the carbonizer 308 proceeds. The rotary blade 315 is attached to the central axis 309 in the carbonizer 308, which removes the food waste from being stuck to the wall of the carbonizer 308 while carbonized. Waste gas generated in the carbonization process is discharged to the stack 314 through the waste gas outlet 312.
이 같은 종래의 음식쓰레기 탄화장치는 음식쓰레기를 연속으로 공급하고 탄화처리하는 구조에 적합한 구조를 구성하지 못하였고, 탄화기(308)의 중심축(309)에 형성된 응착된 탄화물을 제거하는 회전날개(315)가 탄화기(308)의 벽면으로부터 이격되어 설치됨으로서 응착된 탄화물을 효율적으로 제거할 수 없는 단점이 있었다.Such a conventional food waste carbonization device does not constitute a structure suitable for a structure for continuously supplying and carbonizing food waste, and rotating blades for removing the adhered carbide formed on the central axis 309 of the carbonizer 308. Since 315 is installed away from the wall surface of the carbonizer 308, there is a disadvantage in that the adhered carbide cannot be removed efficiently.
본 발명은 이 같은 종래 기술의 단점을 개선하기 의하여 음식쓰레기를 연속탄화할 수 있도록 적합한 구조로 형성하였고, 열분해탄화부의 벽면에 응착하는 음식쓰레기의 탄화물을 제거할 수 있도록 열분해탄화부의 중심축에 스크랩퍼가 부착된 탄화물응착제거장치를 형성하여 음식쓰레기의 탄화에서 가장 큰 문제가 되고 있는 탄화물의 응착을 효과적으로 제거할 수 있도록 함과 동시에, 열분해탄화부의 끝부분에 스크류잭으로 구성된 높낮이 조절장치를 구성하였다.The present invention has been formed in a structure suitable for continuous carbonization of the food waste by improving the disadvantages of the prior art, scrap on the central axis of the pyrolysis carbonization portion to remove the carbide of the food waste adhering to the wall surface of the pyrolysis carbonization portion By forming a carbide adhesion removal device with a fur, it is possible to effectively remove the adhesion of carbide, which is the biggest problem in carbonization of food waste, and at the same time, the height adjustment device composed of screw jack is formed at the end of the pyrolysis carbonization part. .
도1은 본 발명의 음식쓰레기의 연속탄화장치를 나타내는 사시도1 is a perspective view showing a continuous carbonization apparatus of food waste of the present invention
도2는 본 발명의 음식쓰레기의 연속탄화장치를 나타내는 정면도Figure 2 is a front view showing a continuous carbonization apparatus of food waste of the present invention
도3은 종래의 음식쓰레기의 탄화장치를 나타내는 개략구성도Figure 3 is a schematic configuration diagram showing a carbonization device of a conventional food waste
*** 도면의 주요 부분에 대한 부호설명 ****** Explanation of main parts of drawing ***
110 : 열분해탄화부110: pyrolysis carbonization unit
122, 126 : 탄화물응착제거장치122, 126: carbide adhesion removal device
120 : 중심축120: central axis
121, 125 : 관통부121, 125: penetrations
123, 127 : 스크랩퍼123, 127: scraper
128 : 스크류잭128: screw jack
본 발명의 보다 상세한 내용을 첨부한 도면에 의하여 상세히 설명하면 다음과 같다.If more detailed description of the present invention will be described in detail by the accompanying drawings as follows.
도1은 본 발명의 음식쓰레기의 연속탄화장치를 나타내는 사시도이고, 도2는 본 발명의 음식쓰레기의 연속탄화장치의 상세 구조를 나타내는 정면도이다.1 is a perspective view showing a continuous carbonization device of the food waste of the present invention, Figure 2 is a front view showing a detailed structure of the continuous carbonization device of the food waste of the present invention.
도1과 도2에 의하면, 먼저 음식쓰레기가 음식쓰레기 투입구(101)에 투입되면, 이송로(102)속에 설치된 이송컨베이어(103)가 작동하여 음식쓰레기를 유압투입기(104)에 이송하고, 유입투입기(104)는 유압으로 음식쓰레기를 공급관(105)에 이송한다.1 and 2, when the food waste is first introduced into the food waste inlet 101, the conveying conveyor 103 installed in the conveying path 102 is operated to transport the food waste to the hydraulic feeder 104, inflow The feeder 104 hydraulically transfers food waste to the supply pipe 105.
공급된 음식쓰레기는, 액체(107)가 주입된 만곡부가 형성된 제1예열부(106)를 통과하는데, 만곡부의 액체(107)를 통과하면서 음식쓰레기는 액체가 뭍은 상태로 공급관(105)을 통해 다음 단계로 이송된다.The supplied food waste passes through the first preheating unit 106 in which the curved portion into which the liquid 107 is injected is formed, and the food waste passes through the supply pipe 105 in a liquid-tight state while passing through the liquid 107 of the curved portion. Is conveyed to the next step.
한편 공급관(105)은 열분해장치(110)의 상부에 위치토록 하는데 이는 열분해장치(110)의 가열에 사용한 일을 예열에 다시 한번 사용할 수 있도록 한 것이다.On the other hand, the supply pipe 105 is positioned above the pyrolysis device 110, which allows the work used for heating the pyrolysis device 110 to be used once again for preheating.
이송된 음식쓰레기는 열분해장치(110)에서 발생한 수증기가 공급되면서 액체(107)를 통과할 때 뭍은 액체가 일정상태로 건조됨과 동시에 2차예열이 이루어지는 제2예열부(109)를 통과하여 열분해장치(110)로 공급된다. 여기서 제2예열부(109)는 수직 또는 급경사지게 형성하여 음식쓰레기가 낙하하는 동안 효과적으로 가열 건조되도록 하였다.The transported food waste is thermally decomposed through the second preheating unit 109 where secondary liquid is dried at the same time as the liquid is dried to a certain state while passing through the liquid 107 while water vapor generated from the pyrolysis device 110 is supplied. Supplied to the device 110. Here, the second preheating unit 109 is formed to be vertical or steep slope so that the food waste is effectively heated and dried while falling.
열분해탄화부(110)에 들어온 음식쓰레기는 가열장치(111)로부터 높은 열이 공급되면서 탄화가 진행되고 탄화된 음식쓰레기는 점차 배출관(112)으로 배출되어, 저장용기(113)에 떨어진다.The food waste entering the pyrolysis carbonization unit 110 is carbonized while high heat is supplied from the heating device 111, and the carbonized food waste is gradually discharged to the discharge pipe 112 and falls into the storage container 113.
저장용기(113)에는 액체(118)가 들어있으며 액체(118)는 주로 응축수로 채워져 있다.The reservoir 113 contains a liquid 118 and the liquid 118 is mainly filled with condensate.
응축수로 된 액체(118)는 배출된 탄화물을 냉각하며, 탄화물은 응축수로 된 액체(118)를 정화하는 상호작용을 한다. 액체(118)속에 떨어진 탄화물은 배출스크류(115)를 통해 밖으로 배출된다.The condensate liquid 118 cools the discharged carbides, and the carbides interact to purify the liquid 118 condensate. The carbide dropped into the liquid 118 is discharged out through the discharge screw 115.
열분해탄화부(110)의 내부는 중심축(120)이 중앙을 통과하면서 열분해탄화부(110)와 일체로 동작한다. 중심축(120)에는 관통부(121)(125)를 통과하는 탄화물응착제거장치(122)(126)가 관통부(121)(125)를 따라 슬라이딩 운동을 할 수 있도록 구성되어 있고, 탄화물응착제거장치(122)(126)의 양 끝단에는 스크랩퍼(123)(127)가 열분해탄화부(110)의 벽면(124)과 밀착되게 구성되어 있다. 특히, 중심축(120)에 형성된 관통부(121)(15)를 따라 스크랩퍼(123)(127)가 부착된 탄화물응착제거장치(122)(126)가 회전운동을 하면서 스크랩퍼의 무게인 자중을 받아 스크랩퍼(123)(127)가 열분해탄화부(110)의 하부 벽면에 충분하게 밀착되어 응착된 탄화물을 효율적으로 제거할 수 있도록 하였다.The inside of the pyrolysis carbonization unit 110 operates integrally with the pyrolysis carbonization unit 110 while the central shaft 120 passes through the center thereof. In the central shaft 120, the carbide adhesion removal apparatus 122 and 126 passing through the through portions 121 and 125 are configured to slide along the through portions 121 and 125, and the carbide adhesion Scrapers 123 and 127 are configured to be in close contact with the wall surface 124 of the pyrolytic carbonization unit 110 at both ends of the removal devices 122 and 126. In particular, the carbide adhesion removal apparatuses 122 and 126 having the scrapers 123 and 127 attached to the through parts 121 and 15 formed on the central shaft 120 rotate the rotational weight of the scraper. The scraper 123 and 127 were sufficiently adhered to the lower wall surface of the pyrolytic carbonization unit 110 in order to efficiently remove the adhered carbide.
탄화물응착제거장치(122)(126)는 열분해탄화부(110)의 입구와 중간 2부분에 설치하였으며, 경우에 따라서 2군데 이상 설치할 수도 있다. 탄화물응착제거장치(122)(126)는 중심축(120)과 수직으로 설치되어 있으며, 탄화물응착제거장치(122)(126)가 2군데 설치될 경우는 180。의 위상차를 갖도록 하여 중심축의 힘의 불균형적 분포로 인한 변형과 이로인한 모터의 과부하 발생을 방지하며, 3개 이상을 설치하는 경우에도 균등한 위상차를 주어 동일한 효과를 도모한다.Carbide adhesion removal device 122, 126 was installed at the inlet and the middle portion of the pyrolysis carbonization unit 110, may be installed in two or more places in some cases. Carbide adhesion removal apparatuses 122 and 126 are installed perpendicular to the central axis 120. When two places of carbide adhesion removal apparatuses 122 and 126 are installed, they have a phase difference of 180 °. This prevents deformation due to unbalanced distribution and overloading of the motor due to the unbalanced distribution, and gives the same effect evenly when three or more are installed.
열분해탄화부(110)의 벽면은 입구에서 중앙부까지는 중심축(120)을 중심으로 동일한 직경의 원통형을 이루다가, 중앙부 근처를 지나면서 원통형 벽면이 점차 직경이 짧아져 좁아지도록 구성하였는데, 이는 드럼형상의 열분해탄화부(110)에서 음식쓰레기의 탄화가 진행되면서 회전력과 스크류잭에 의한 높낮이 조절을 통해 탄화물이 배출관(112)쪽으로 용이하게 배출되도록 하기 위한 것이다.The wall surface of the pyrolysis carbonization unit 110 forms a cylindrical shape having the same diameter from the inlet to the central portion about the central axis 120, and the cylindrical wall surface is gradually shortened and narrowed while passing near the center portion. As the carbonization of the food waste proceeds in the pyrolysis carbonization unit 110, the carbides are easily discharged toward the discharge pipe 112 through the height adjustment by the rotational force and the screw jack.
또한, 열분해탄화부(110)의 내부온도는 입구에서 출구쪽으로 갈수록 점차 높아지도록 하였는데, 음식쓰레기의 건조가 진행되는 제1구역의 경우는 150에서 250℃의 범위로 가열하며, 음식쓰레기의 탄화가 본격적으로 진행되는 제2구역의 경우는 250에서 400℃의 범위로 가열하고, 탄화가 완성되는 제3구역은 온도가 다시 낮아지면서 400에서 300℃로 온도가 낮아지도록 하였다.In addition, the internal temperature of the pyrolysis carbonization unit 110 was gradually increased from the inlet to the outlet, in the case of the first zone where the drying of food waste proceeds, it is heated in the range of 150 to 250 ° C., and the carbonization of the food waste In the case of the second zone in earnest, the heating was performed in the range of 250 to 400 ° C., and the third zone in which carbonization was completed was lowered from 400 to 300 ° C. while the temperature was lowered again.
한편, 열분해탄화부(110)의 끝부분에는 연결부(129)를 통해 스크류잭지지대(30)에 결합된 스크류잭(128)이 상하로 움직이면서 열분해탄화부(110)의 높낮이를 조절하여 탄화물이 원활하게 가열되면서 배출도 용이하게 이루어지도록 구성되어 있다. 여기서 지지대(117)는 음식쓰레기 연속 탄화장치의 전체 장치를 고정하는 받침대 역할을 한다. 진공펌프(108)는 가열된 수증기를 뽑아서 응축기로 이송시키는 역할을 한다. 도1에서 미설명부호는 응축기(119)이다.On the other hand, at the end of the pyrolysis carbonization unit 110, the carbide jack is smoothly controlled by adjusting the height of the pyrolysis carbonization unit 110 while the screw jack 128 coupled to the screw jack support 30 is moved up and down through the connecting portion 129. It is configured to be easily discharged while being heated. Here, the support 117 serves as a pedestal for fixing the entire device of the food waste continuous carbonization device. The vacuum pump 108 serves to extract the heated steam and transfer it to the condenser. In FIG. 1, reference numeral denotes a condenser 119.
본 발명의 음식쓰레기의 연속탄화장치는 밀봉된 상태로 무산소 열분해를 이용하는 폐타이어의 열분해를 통한 오일 제조장치와. 폐플라스틱의 열분해와, 폐합성섬유의 열분해 및 목초를 무산소 열분해하여 유용한 약초수액을 제조하는데도 함께 이용할 수 있다The continuous carbonization apparatus of the food waste of the present invention is an oil production apparatus through pyrolysis of waste tires using anoxic pyrolysis in a sealed state. Pyrolysis of waste plastics, pyrolysis of waste synthetic fibers and anaerobic pyrolysis of grasses can also be used to produce useful herbal sap.
본 발명의 음식쓰레기의 연속탄화장치는 음식물쓰레기를 연속적으로 탄화처리하는데 최적의 구조를 형성하였고, 스크랩퍼가 부착된 탄화물응착제거장치를 형성하여 음식쓰레기의 탄화가 진행됨에 따라 발생하는 음식쓰레기의 응착현상을 효과적으로 제거할수 있도록 함과 동시에, 열분해탄화부의 온도분포를 차별화하여 음식쓰레기가 건조에서 탄화까지 연속처리되도록 구성하였다.The continuous carbonization apparatus of the food waste of the present invention forms an optimal structure for continuous carbonization of food waste, and forms a carbide adhesion removal device with a scraper, thereby adhering the food waste generated as carbonization of the food waste proceeds. In order to effectively remove the phenomenon, the temperature distribution of the pyrolytic carbonization unit was differentiated so that the food waste was continuously processed from drying to carbonization.
또한, 열분해탄화부의 끝 부분에는 스크류잭으로 구성된 높낮이조절장치를 형성하여 음식쓰레기의 탄화상태에 따라, 높낮이를 적절하게 조절하면서 원활하고 연속적인 탄화가 이루어질 수 있도록 구성하여 최적의 음식쓰레기 연속탄화장치를 실현하였다.In addition, at the end of the pyrolysis carbonization unit by forming a height adjustment device consisting of a screw jack, according to the carbonization state of the food waste, it is configured so that the smooth and continuous carbonization can be made while adjusting the height appropriately, the optimum food waste continuous carbonization device Realized.
Claims (6)
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KR100722333B1 (en) * | 2004-04-14 | 2007-06-04 | 주식회사 한국종합플랜트 | Thermal cracking equipment |
Citations (3)
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KR19980015732U (en) * | 1996-09-12 | 1998-06-25 | 정명구 | Drying Equipment of Solid Fuel Production System Using Garbage |
KR100233792B1 (en) * | 1990-06-06 | 1999-12-01 | 드폴 루이스 에이 | Burner axial seal scraper |
KR20000020076A (en) * | 1998-09-17 | 2000-04-15 | 안봉조 | Automatic incinerator of high temperature pyrolysis type |
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KR100233792B1 (en) * | 1990-06-06 | 1999-12-01 | 드폴 루이스 에이 | Burner axial seal scraper |
KR19980015732U (en) * | 1996-09-12 | 1998-06-25 | 정명구 | Drying Equipment of Solid Fuel Production System Using Garbage |
KR20000020076A (en) * | 1998-09-17 | 2000-04-15 | 안봉조 | Automatic incinerator of high temperature pyrolysis type |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR100722333B1 (en) * | 2004-04-14 | 2007-06-04 | 주식회사 한국종합플랜트 | Thermal cracking equipment |
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