KR950007048B1 - Waste treatment apparatus - Google Patents
Waste treatment apparatus Download PDFInfo
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- KR950007048B1 KR950007048B1 KR1019920003833A KR920003833A KR950007048B1 KR 950007048 B1 KR950007048 B1 KR 950007048B1 KR 1019920003833 A KR1019920003833 A KR 1019920003833A KR 920003833 A KR920003833 A KR 920003833A KR 950007048 B1 KR950007048 B1 KR 950007048B1
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- South Korea
- Prior art keywords
- gas
- furnace
- waste
- neutralization tank
- chamber
- Prior art date
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- 239000002699 waste material Substances 0.000 title claims abstract description 36
- 238000002485 combustion reaction Methods 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 16
- 239000000498 cooling water Substances 0.000 claims abstract description 11
- 230000003472 neutralizing effect Effects 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 41
- 238000000197 pyrolysis Methods 0.000 claims description 24
- 238000006386 neutralization reaction Methods 0.000 claims description 23
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 238000001914 filtration Methods 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 238000011084 recovery Methods 0.000 claims description 11
- 229910052799 carbon Inorganic materials 0.000 claims description 10
- 230000008929 regeneration Effects 0.000 claims description 10
- 238000011069 regeneration method Methods 0.000 claims description 10
- 238000004891 communication Methods 0.000 claims description 9
- 239000000567 combustion gas Substances 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 238000005336 cracking Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract 1
- 238000009835 boiling Methods 0.000 description 3
- 239000003610 charcoal Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 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 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000010920 waste tyre Substances 0.000 description 1
- 239000002916 wood waste Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
제1도는 본 발명에 의한 시스템의 계통도.1 is a schematic diagram of a system according to the present invention.
제2도는 본 발명의 시스템을 보인 개략 단면도.2 is a schematic cross-sectional view showing a system of the present invention.
제3도는 제2도의 A-A선 단면도.3 is a cross-sectional view taken along the line A-A of FIG.
* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
1 : 내부로 2 : 외부로1: inside 2: outside
3a,3b : 내외부중공축 4a,4b : 받침대3a, 3b: Internal and external hollow shafts 4a, 4b: Pedestal
5 : 외부중공축의 구멍 6 : 칸막이벽5: hole of external hollow shaft 6: partition wall
7 : 칸막이벽의 구멍 8 : 투입구7 hole in the partition wall 8 slot
9 : 폐기물 10 : 감속모우터9: waste 10: deceleration motor
11 : 연소실 12 : 버어너11: combustion chamber 12: burner
13 : 연통로 14 : 연도13: communication path 14: year
15 : 냉각물탱크 21 : 재생회수처리부15: cooling water tank 21: regeneration recovery unit
22 : 가스이송로 23 : 물재킷부22 gas passage 23 water jacket portion
24 : 제1여과실 25 : 제2여과실24: 1st filter room 25: 2nd filter room
26 : 여과부재 27 : 카본수집탱크26: filtration member 27: carbon collection tank
28,29 : 유분수집탱크 30 : 냉각수 탱크28,29: oil collection tank 30: cooling water tank
31 : 중화소 32 : 활성탄31: neutralization 32: activated carbon
33 : 가스중화조 34 : 중화제33: gas neutralization tank 34: neutralizing agent
35 : 이송관 36 : 배기관35 transfer pipe 36 exhaust pipe
41 : 중화조 42 : 여과용 필터41: neutralization tank 42: filter for filtration
43 : 펌프 44 : 분무부재43 pump 44 spray member
51 : 냉각실 52 : 송풍로51: cooling chamber 52: blower
53 : 냉풍기 54 : 가스공급관53: cold air fan 54: gas supply pipe
55,56 : 송풍기55,56: Blower
본 발명은 각종 폐기물을 처리하여 열원과 재생물을 얻도록 한 폐기물 처리장치에 관한 것이다.The present invention relates to a waste treatment apparatus for treating various wastes to obtain a heat source and a regenerated product.
더욱 상세히는 폐타이어, 폐합성수지, 폐기농수산물, 폐축산물, 목제폐기물등과 같은 각종 산업폐기물들을 환경공해에 지장없이 처리함에 그 특징이 있고, 또한 이와 같이 처리되는 폐기물에서 재생물을 얻어 다른용도로 재사용할 수 있도록 한 것이다.More specifically, it is characterized by treating various industrial wastes such as waste tires, waste synthetic resins, waste agricultural products, waste livestock products, wood wastes, etc. without disrupting the environmental pollution. It is intended for reuse.
일반적으로 지금까지 알려진 폐기물의 처리시스템은 운반, 분쇄, 건류, 열분해, 분리, 배연냉각, 재생물 회수, 무공해폐기, 배연의 공정을 거치도록 되어 있다.In general, waste treatment systems known to date are subject to transport, crushing, dry distillation, pyrolysis, separation, flue gas cooling, recovery of recycled products, pollution-free waste and flue gas.
본 발명에서는 이와 같은 각종 폐기물의 처리공정을 합리적이며, 경제적으로 처리할 수 있는 장치를 제공하고자 한 것으로, 각부의 구성을 첨부도면을 토대로하여 살펴보면 다음과 같다.In the present invention, to provide a device that can be reasonably, economical treatment of such various waste treatment process, looking at the configuration of each part based on the accompanying drawings as follows.
도면부호 “가”는 폐기물 분해로로서 내부로(1)와 외부로(2)로 구성되어 있으며, 내부로(1)의 중앙에는 이중관으로된 내외부 중공축(3a)(3b)이 좌우 양측에 설치된 받침대(4a)(4b)에 의해 회전이 가능하게 지지된 상태로 설치되고 외부중공축(3b)에는 구멍(5)이 무수히 뚫려져 있으며, 또한 그 외측으로 원통령의 내부로(1)가 고정설치되어 있다.Reference numeral “A” is a waste cracking furnace, which is composed of an inner furnace (1) and an outer furnace (2), and the inner and outer hollow shafts (3a) and (3b) formed of double pipes are disposed at the center of the inner furnace (1) on both sides. It is installed in such a state as to be rotatably supported by the installed pedestals 4a and 4b, and the outer hollow shaft 3b has a number of holes 5 formed therein. It is fixedly installed.
내부로(1)의 내부에는 3등분된 칸막이벽(6)이 내부로(1)와 외부중공축(3b) 사이에 연결설치되며, 상기한 칸막이벽(6)에는 다수개의 구멍(7)이 뚫려있어 내부로(1)에서 폐기물이 열분해될때 그 열분해가스(열)가 각 칸마다 서로 연통되도록 되며, 3등분으로 나뉘어진 내부로(1)의 각 칸마다 투입구(8)로부터 폐기물(9)이 투입되도록 되어 있다.In the interior of the interior 1, a partition wall 6 divided into thirds is installed between the interior 1 and the external hollow shaft 3b, and the partition wall 6 has a plurality of holes 7 formed therein. When the waste is pyrolyzed in the interior furnace (1), the pyrolysis gas (heat) is communicated with each compartment, and the waste (9) from the inlet (8) in each compartment of the interior furnace (1) divided into three sections. This is supposed to be input.
한편, 투입구(8)로 투입되는 폐기물(9)은 도시되지 아니한 별도의 이송용 컨베이어에 의해 분쇄된 상태로 이송되어 투입된다.On the other hand, the waste (9) introduced into the inlet (8) is conveyed in a pulverized state by a separate transport conveyor not shown is introduced.
도면부호 2는 외부로이다.Reference numeral 2 is outside.
이 외부로(2)는 연소실(11)로 되는 것으로 하부에는 버어너(12)가 설치되어 내부로(1)에 투입된 폐기물(9)을 가열 열분해시키며, 연소실(11)의 상부에는 지그재그형의 연통로(13)가 연도(14)와 연통되고 연통로(13)의 상부 외부로는 냉각용 물이 들어있는 냉각물탱크(15)가 설치되어 있다.The outer furnace 2 is a combustion chamber 11, and a burner 12 is installed at the lower part to heat pyrolyze waste 9 introduced into the inner furnace 1, and a zigzag-type upper part of the combustion chamber 11 is provided. The communication path 13 communicates with the flue 14, and a cooling water tank 15 containing cooling water is provided outside the upper part of the communication path 13.
한편, 회전하는 2중으로 된 내외부중공축(3a)(3b)의 일측단(도면의 좌측단)은 내부중공축(3a)이 바깥부분으로 연장된 후 그 단부가 막혀져 감속모우터(10)에 의하여 회전 가능하게 받침대(4a)에 의해 지지되어 있고, 타측단(도면의 우측단)은 내외부중공축(3a)(3b)으로 되어 받침대(4b) 위에 회전가능하게 받쳐져 있으며, 재생회수처리부(21)와 연통되어 있다.On the other hand, one side end (left end of the drawing) of the rotating double inner and outer hollow shafts 3a and 3b is closed after the inner hollow shaft 3a extends to the outer portion and thus the reduction motor 10 It is rotatably supported by the pedestal 4a, and the other end (right end of the drawing) is an internal and external hollow shaft 3a, 3b, which is rotatably supported on the pedestal 4b. In communication with (21).
재생회수처리부(21)는 내부로(1)로부터 열분해되어 이송되어온 열분해가스를 정류하는 정류실에 해당하는 것으로, 물재킷부(23)에 원형파이프 형상의 가스이송로(22)가 가로방향으로 무수히 설치되며, 물재킷부(23) 양측에는 제1여과실(24)과 제2여과실(25)이 다소 넓은 공간부로서 구비되고 있다.The regeneration recovery processing unit 21 corresponds to a rectifying chamber for rectifying pyrolysis gas that has been pyrolyzed and transported from the inner furnace 1, and a circular pipe-shaped gas transfer path 22 is formed in the water jacket portion 23 in the horizontal direction. It is provided innumerably, and the 1st filter room 24 and the 2nd filter room 25 are provided as a rather large space part in the water jacket part 23 both sides.
상기의 제1여과실에는 여과부재(26)가 설치되어 열분해가스에 섞인 카본블랙 및 비점이 높은 유분이 수집되어 그 하부에 설치된 카본수집탱크(27) 및 유분수집탱크(28)에 저장되도록 되고, 타측에는 제1여과실(24)을 거친 열분해가스가 가스이송로(22)를 거치면서 물재킷부(23)에 의해 냉각되어 제1여과실(24)에서 수집되지 않은 유분이 재차 수집되도록 하기 위하여 제2여과실이 구비되고 있으며, 제2여과실(25)의 하부에는 재차 수집된 유분이 저장될 수 있도록 또 다른 유분수집탱크(29)가 설치되어 있다.Filtration member 26 is installed in the first filtering chamber to collect carbon black and high boiling point oil mixed in pyrolysis gas, and to be stored in carbon collection tank 27 and oil collection tank 28 installed at the lower portion thereof. On the other side, the pyrolysis gas passing through the first filtering chamber 24 is cooled by the water jacket 23 while passing through the gas transfer path 22 so that the oil not collected in the first filtering chamber 24 is collected again. The second filter room is provided for the purpose, and another oil collection tank 29 is installed at the lower portion of the second filter room 25 so that the collected oil can be stored again.
상기한 물재킷부(23)는 냉각수의 순환이 이루어지도록 일측에 냉각수탱크(30)가 설치되어져 있으며, 이 냉각수탱크(30)로부터 냉각수가 순환되도록 되어 있다.The water jacket part 23 is provided with a cooling water tank 30 on one side to circulate the cooling water, and the cooling water is circulated from the cooling water tank 30.
한편, 상기한 재생회수처리부(21)의 제2여과실(25)의 상측 근접부에는 활성탄(32)을 내장시킨 중화소(31)와 내측에 액상의 중화제(34)가 담겨지고 연도(14)측으로부터 여과 및 중화처리되어 이송되어온 연소가스가 이송되는 이송관(35)이 설치된 가스중화조(33)가 차례로 접속설치되어 있는데, 재생 회수처리부(21)로부터 이송된 열분해가스는 1차로 중화조(31)에서 활성탄(32)에 의해 미세한 카본(분진)등이 여과되고 재차 가스중화조(33)를 거치면서 또 다시 여과가 된다.Meanwhile, the upper portion of the second filter chamber 25 of the regeneration recovery unit 21 includes a neutralizer 31 containing the activated carbon 32 and a liquid neutralizing agent 34 inside the flue 14. The gas neutralization tank 33 in which the transfer pipe 35 which transfers the combustion gas which has been filtered and neutralized from the side to which it is transported is installed in order. The pyrolysis gas transferred from the regeneration recovery processing unit 21 is first neutralized. In the tank 31, fine carbon (dust) or the like is filtered by the activated carbon 32 and again filtered through the gas neutralization tank 33.
이때 가스중화조(33)에는 내부에 액상의 중화제(34)가 저장되어 있어 그 이전에 여과되지 아니한 카본을 침지시키고 열분해된 가스중 수소를 중화시키게 된다.At this time, the gas neutralization tank 33 has a liquid neutralizing agent 34 stored therein to immerse the carbon which has not been filtered before, and neutralize hydrogen in the pyrolyzed gas.
한편, 외부로(2) 즉 연소실(11)로부터 연소된 연소열은 지그재그형으로 된 연통로(13) 및 연도(14)를 거쳐 그 상부에 설치된 중화조(41)에서 여과 및 중화가 되는데, 이 중화조(41)는 내부에 물이 저장되어 있고, 2개의 여과용 필터(42)가 하부가 물에 잠기도록 상부에 설치되어 있으며, 중화조(41) 상부에는 2개의 분무부재(44)가 설치되어 펌프(43)에 의하여 물이 분사되도록 되어 있다.On the other hand, the combustion heat burned from the outside (2), that is, the combustion chamber 11 is filtered and neutralized in the neutralization tank (41) installed at the upper part through the zigzag communication path (13) and the flue (14). The neutralization tank 41 has water stored therein, and two filtration filters 42 are installed at an upper part of the lower part soaking in water, and two spraying members 44 are provided at the upper part of the neutralization tank 41. It is installed so that water is sprayed by the pump 43.
따라서, 연도(14)를 통해 이송된 연소가스중 카본 및 기타 분진은 분사되는 물에 의해 물속으로 가라앉고 2개의 여과용 필터(42)를 거치면서 여과 및 중화가 이루어진 연소가스만 상기한 가스중화조(33)내부의 이송관(35)과 냉각실(51)내부에 접속설치된 배기관(36)을 통하면서 열전달이 이루어진 후 대기로 배출되는 것이다.Accordingly, carbon and other dusts in the combustion gas transported through the flue 14 are submerged into the water by the injected water, and only the combustion gas that has been filtered and neutralized while passing through the two filtration filters 42 is included in the gas. The heat transfer is made through the transfer pipe 35 inside the flower tank 33 and the exhaust pipe 36 connected to the cooling chamber 51 and then discharged to the atmosphere.
도면부호 51은 냉각실로서, 이 냉각실(51)내에는 내부로(1) → 재생회수처리부(21) → 중화소(31) 및 가스중화조(33)을 거쳐 이송된 열분해가스(폐기물의 열 분해에 의해 발생된 가스)가 유입되어 냉각되는 냉각실(51)로서 다수개의 송풍로(52)가 설치되어 있으며, 이 송풍로(52)를 통해 별도로 설치된 냉풍기(53)에 의해 냉풍이 공급되어 냉각이 행하여진다.Reference numeral 51 denotes a cooling chamber, and inside the cooling chamber 51, pyrolysis gas (waste matter) transferred through the interior 1 (1) → regeneration recovery unit 21 → neutralization tank 31 and gas neutralization tank (33). As the cooling chamber 51 into which the gas generated by thermal decomposition) flows and is cooled, a plurality of blowers 52 are provided, and cold air is supplied by a cooler 53 separately installed through the blowers 52. And cooling is performed.
한편, 상기와 같이 구성된 냉각실(51)과 연소실(11)의 하부 사이에는 송풍기(55)를 구비한 가스공급관(54)이 설치되어 있으며, 송풍기(55)의 강재송풍에 의하여 냉각실(51)내의 열분해가스가 연소실(11)측에 공급되며, 이와 같이 공급된 열분해가스는 보충 연료로서의 역할을 하게 된다.On the other hand, a gas supply pipe 54 having a blower 55 is installed between the cooling chamber 51 and the lower portion of the combustion chamber 11 configured as described above, and the cooling chamber 51 is formed by the steel blowing of the blower 55. The pyrolysis gas in the inside) is supplied to the combustion chamber 11 side, and the pyrolysis gas supplied in this way serves as a supplemental fuel.
따라서, 본 발명의 장치에 의해 처음 폐기물(9)을 연소시킬 때에는 연소실(11) 하부에 설치된 버어너(12)로서 가열하여 내부로(1)에 넣어진 폐기물(9)을 열분해시키지만 일단 일정한 시간동안 열분해가 이뤄진 후에는 자체발생된 열분해가스가 연료가 되어 소정의 시간 동안 연소가 이루어지는 것으로 폐기물(9)에 의해 얻어진 열분해가스를 연료로서 대체 사용하게 되므로 연료의 절감을 가져와 경제적이다.Therefore, when the waste 9 is first burned by the apparatus of the present invention, it is heated with a burner 12 installed under the combustion chamber 11 to thermally decompose the waste 9 put into the furnace 1, but for a predetermined time. After the pyrolysis is carried out for a while, the self-generated pyrolysis gas becomes a fuel and is burned for a predetermined time, so that the pyrolysis gas obtained by the waste 9 is replaced as a fuel, resulting in economical fuel savings.
물론, 열분해가스를 대체연료로 사용하지 못할 정도에 이르게 되면 도시하지 아니한 제어장치에 의해 자동으로 버어너(12)가 작동하여 내부로(1)내의 폐기물(9)을 연소시키는 것이다.Of course, when the pyrolysis gas can not be used as an alternative fuel, the burner 12 is automatically operated by a control device (not shown) to burn the waste 9 in the interior 1.
본원 발명에 의한 폐기물처리 과정을 살펴보면, 먼저, 이송용 컨베이어(도시생략)로부터 이송되어온 폐기물을 내부로(1)의 일측에 설치된 투입구(8)를 열어 그 내부에 넣고 투입구(8)를 닫는다.Looking at the waste treatment process according to the present invention, first, the waste conveyed from the conveying conveyor (not shown) open the inlet 8 installed on one side of the inner furnace 1 to put in the inside and close the inlet 8.
이어서 감속모우터(10)를 구동시키면 내부로(1)가 회전하게 된다.Subsequently, when the reduction motor 10 is driven, the inside 1 is rotated.
이와 동시어 버어너(12)를 점화시키면 버어너(12)의 연소실에 의해 내부로 (1)내에 넣어진 폐기물(9)이 열분해가 이루어진다.At the same time, when the burner 12 is ignited, the waste 9 enclosed in the inside 1 by the combustion chamber of the burner 12 is thermally decomposed.
이때 열분해에 의해 발생된 열분해가스는 외부중공축(3b)에 뚫린 구멍(5)을 통해 재생회수처리부(21)에 도달하여 1차여과실(24)내의 여과부재(26)에 의해 카본의 여과가 이루어지고 동시에 비점이 높은 유분(기름성분) 역시 응축되어 하부에 설치된 카본수집탱크(27) 및 유분수집탱크(28)에 모아지게 되며, 열분해가스는 재차 냉각수가 순환되고 있는 물재킷부(23)내에 연통되게 설치된 가스이송로(22)를 통과하면서 응축되어 2차 여과실(25)에서 비점이 낮은 유분이 모아져 그 하부에 설치된 유분수집탱크(29)에 수집된다.At this time, the pyrolysis gas generated by the pyrolysis reaches the regeneration recovery unit 21 through the hole 5 drilled in the external hollow shaft 3b, so that the filtration of carbon is carried out by the filtration member 26 in the primary filtration chamber 24. At the same time, a high boiling point oil (oil component) is also condensed and collected in the carbon collection tank 27 and the oil collection tank 28 installed at the lower portion, and the pyrolysis gas is again the water jacket portion 23 in which the cooling water is circulated. Condensed while passing through the gas transfer path 22 provided in communication therewith, the oil having a low boiling point is collected in the secondary filtration chamber 25 and collected in the oil collection tank 29 installed at the lower portion thereof.
그후 1차 및 2차에 걸쳐서 여과된 열분해 가스는 활성탄(32)이 저장된 중화조(1)를 걸치면서 미세한 카본등이 정제되고 가스중화조(33)에서 연소가스에 섞여있는 수소등이 중화된 후 냉각실(51)에서 냉각이 된다.After that, the pyrolysis gas filtered through the first and second stages is refined through the neutralization tank 1 in which the activated carbon 32 is stored, and fine carbon and the like are refined, and hydrogen mixed in the combustion gas in the gas neutralization tank 33 is neutralized. After that, cooling is performed in the cooling chamber 51.
이와 같이 냉각이 이루어진 열분해가스는 송풍기(55)의 강제 송풍력에 의해 가스공급관(54)을 통해 연소실(11) 내부로 공급되어 내부로(1)내의 폐기물(9)을 열분해시키는 것으로 상기와 같은 일련의 과정이 연속반복적으로 이루어지면서 열분해가 이루어지는 것이다.The pyrolysis gas thus cooled is supplied into the combustion chamber 11 through the gas supply pipe 54 by the forced blowing force of the blower 55 to thermally decompose the waste 9 in the interior 1 as described above. Pyrolysis occurs as a series of processes are repeated repeatedly.
한편, 버어너의 연소열에 의해 발생된 연소가스는 중화조(41)측부에 설치된 송풍기(56)의 흡인력에 의해 지그재그형으로된 연통로(13) 및 연도(14)를 거쳐 중화조(41)내에서 2개의 분무부재(44) 및 2개의 여과용필터(42)에 의해 카본등이 여과 및 냉각된 후 가스중화조(33)내측에 설치된 이송관(35) 및 냉각실(51) 내부에 설치된 배기관(36)을 통해 대기로 배출된다.On the other hand, the combustion gas generated by the combustion heat of the burner is passed through the communication path 13 and the flue 14 which are zigzag-shaped by the suction force of the blower 56 installed on the neutralization tank 41 side, and the neutralization tank 41. After the carbon and the like have been filtered and cooled by the two spray members 44 and the two filtration filters 42 therein, the transfer pipe 35 and the cooling chamber 51 installed inside the gas neutralization tank 33 are provided. It is discharged to the atmosphere through the installed exhaust pipe (36).
참고로 본원 발명의 장치에 의한 효과를 살펴보면,Looking at the effect of the device of the present invention for reference,
첫째 ; 각종 폐기물(9)을 열분해 처리시킴에 있어서 공해를 유발시키는 각종 물질이 본 장치내에서 여과 및 정화된 후 배출되므로 환경공해를 유발시킬 염려가 없으며,first ; In the pyrolysis treatment of various wastes 9, various substances causing pollution are discharged after being filtered and purified in the apparatus, so there is no fear of causing environmental pollution,
둘째 ; 본 장치내에서 열분해된 열분해가스를 연료로서 대체 사용하므로서 연료의 절약을 꾀할 수 있으며,second ; By using pyrolyzed pyrolysis gas as fuel in this device, it is possible to save fuel.
세째 ; 연소실(11) 외부로 냉각물탱크(15)가 설치되어 있으므로서 냉각물 탱크(15)내의 물을 별도로 인출하여 온수 혹은 기타 난방용 에너지로 활용할 수 있으며,Third; Since the coolant tank 15 is installed outside the combustion chamber 11, the water in the coolant tank 15 can be withdrawn separately and used as hot water or other heating energy.
네째 ; 내부로(1)에 열분해된 폐기물(9)은 숯이 되는 것으로 음식점등에서 사용하는 숯불용으로 사용될 경우 유해가스가 전혀없어 위생상 안전하고, 질이 좋은 숯으로 제공될 수 있는 것이며,Fourth; The waste (9) pyrolyzed in the furnace (1) is a charcoal, and when used for charcoal fires used in restaurants, there is no harmful gas, so that it can be provided as a safe, hygienic, high-quality charcoal.
다섯째 ; 제1,2여과실(재생회수처리부)에서 얻어진 유분은 별도로 수집하여 재사용될 수 있는 것이다.fifth ; The oil obtained in the first and second filtering chambers (regeneration recovery unit) can be collected separately and reused.
상기와 같이 본원 발명은 공해요인이 없고 특히 경제성을 갖는 장치를 제공하는 것으로 그 효과는 매우 큰 것이라 하겠다.As described above, the present invention provides a device having no pollution and particularly economic efficiency, and the effect thereof is very large.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1019920003833A KR950007048B1 (en) | 1992-03-09 | 1992-03-09 | Waste treatment apparatus |
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| Application Number | Priority Date | Filing Date | Title |
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| KR1019920003833A KR950007048B1 (en) | 1992-03-09 | 1992-03-09 | Waste treatment apparatus |
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| KR930019286A KR930019286A (en) | 1993-10-18 |
| KR950007048B1 true KR950007048B1 (en) | 1995-06-30 |
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