KR20150064370A - The kiln for Heating Circulation - Google Patents
The kiln for Heating Circulation Download PDFInfo
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- KR20150064370A KR20150064370A KR1020130149006A KR20130149006A KR20150064370A KR 20150064370 A KR20150064370 A KR 20150064370A KR 1020130149006 A KR1020130149006 A KR 1020130149006A KR 20130149006 A KR20130149006 A KR 20130149006A KR 20150064370 A KR20150064370 A KR 20150064370A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/02—Multi-step carbonising or coking processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Description
본 발명은 목탄 제조를 위한 탄화로 구조에 대한 것으로, 기존의 탄화로의 경우 탄화로의 구성이 개별적, 독립적인 구조로 설계되어 있어 탄화로 내에서 발생하는 탄화열이 낭비되는 구조로 되어 있으나, 본 발명의 탄화열 순환 방식 탄화로 시스템은 1차 탄화로(A)에서 탄화 과정에서 발생된 탄화열을 이용하여, 2차 탄화로(B) 내부에 적재된 목재의 수분을 17% 이하로 조절하여, 탄화 과정에서 필수적인 발생하는 목재 건조 건조 시간을 단축함으로써, 일반적으로 전체 탄화 공정에 소요되는 7일 정도의 시간을 4일 이내로 단축하여 목탄 제조에 소요되는 시간을 획기적으로 절감할 수 있는 시스템에 대한 것이다.The present invention relates to a charcoal furnace for producing charcoal. In the case of conventional charcoal furnaces, the charcoal furnace structure is designed individually and independently so that the heat of carbonization generated in the charcoal furnace is wasted. However, The carbonitriding system of the present invention can control the moisture content of the wood loaded in the secondary carbonization furnace (B) to 17% or less by using the heat of carbonization generated in the carbonization process in the primary carbonization furnace (A) By shortening the dry drying time of wood, which is indispensable to the carbonization process, it is possible to reduce the time required for charcoal production to a short time by shortening the time required for the entire carbonization process to within 4 days It is about.
본 발명은 1차 탄화로(A)의 폐열을 이용한 2차 탄화로(B)의 목재 건조 방법에 대한 것으로, 더욱 상세하게는 탄화로 내에서 나무를 태워 목탄을 제조 과정에서 발생하는 폐열, 즉 나무의 연소열을 이용하여 2차 탄화로(B) 내의 적층된 나무의 수분을 조절하는 탄화열 순환형 탄화로 시스템에 관한 것이다.The present invention relates to a method for drying wood of a secondary carbonization furnace (B) using waste heat of a primary carbonization furnace (A), more particularly, to a method of drying wood by burning wood in a carbonization furnace, The present invention relates to a carbonization heat-recycling type carbonization system for regulating moisture of a laminated wood in a secondary carbonization furnace (B) by using heat of combustion of wood.
일반적인 숯의 제조 과정을 보면, 먼저 가마의 입구를 통하여 내부에 나무를 적층하고, 입구를 밀폐한 다음, 아궁이에 불을 지펴 상부의 화구를 통하여 탄화로 내부로 열을 공급하여 나무가 상부로부터 하향 연소되면서 숯을 제조하는 방식으로 탄화로가 구성되어 있다. 이때 나무의 연소시 발생하는 연소열은 배출구 및 연통을 통하여 외부로 배출된다.In general, the process of manufacturing the charcoal is as follows: First, the wood is laminated through the entrance of the kiln, and the entrance is sealed. Then, the fire is lit in the oven and the heat is supplied to the inside of the carbonization furnace through the upper firebox, Carbonization furnaces are constructed by burning and producing charcoal. At this time, the heat of combustion generated when the wood is burned is discharged to the outside through the discharge port and the communication pipe.
이와 같을 목탄을 제조하는데 대락 5-6일 정도 걸리고, 제조된 목탄을 꺼낸 후 탄화로를 식히는데 걸리는 시간이 2-3일 정도이다. 전체 목탄 제조 공정에는 7-9일 정도 걸린다.It takes about 5-6 days to produce such charcoal, and it takes about 2-3 days to cool the charcoal after removing the charcoal. The entire charcoal manufacturing process takes about 7-9 days.
일반적으로 탄화로에서 탄화 과정에서 발생되는 폐열은 30,000kcal로서 매우 높다. 이러한 폐열이 아무런 활용이 없이 배출구를 통해 낭비되고 있는 문제점이 발생하고 있다.Generally, the waste heat generated in the carbonization process in the carbonization furnace is very high as 30,000 kcal. There is a problem that such waste heat is wasted through the discharge port without any utilization.
또한, 목탄 제조시 효율적인 목탄의 제조를 위해 목재의 수분량을 17% 이하로 조절하기 위해서 목재 건조실을 따로 운영되고 있다. 이때 소요되는 기간인 보통 2-3일 정도 소요된다.In addition, the wood drying chamber is operated independently to adjust the water content of the wood to 17% or less in order to produce charcoal efficiently in the production of charcoal. This takes about 2-3 days.
본 발명은 상기와 같은 종래의 문제점을 해소하기 위한 것으로, 그 목적은 탄화 과정에서 발생되는 폐열을 이용하여 2차 탄화로(B) 내의 목재의 수분 조절을 위한 건조 과정의 열원으로 이용함으로써, 1차 탄화로(A)에서 발생하는 탄화열의 낭비를 막음과 동시에 2차 탄화로(B) 자체를 건조실로 이용함으로써 건조실 구축 비용의 절감과 건조 후 탄화 과정에서 발생하는 목재의 건조실에서 탄화로의 이동 시간의 절감을 통해, 전체 탄화 과정의 비용과 시간을 줄일 수 있는 시스템을 제공하는데 있다.The object of the present invention is to solve the above-mentioned problems of the prior art by using waste heat generated in the carbonization process as a heat source for drying the wood in the secondary carbonization furnace B, It is possible to prevent the waste of the heat of carbonization occurring in the secondary carbonization furnace (A) and to reduce the cost of constructing the drying chamber by using the secondary carbonization furnace (B) itself as a drying chamber and to transfer the carbonization furnace from the drying chamber of the wood, Thereby reducing the time and cost of the entire carbonization process.
상기의 목적을 달성하기 위해 본 발명에서는 복수개의 탄화로와, 상기 복수개의 탄화로에서 발생하는 가스 및 탄화열의 배출을 위한 2개의 배출구(31,32,33,34), 그리고 각 배출구(31,32,33,34)에서는 발생하는 탄화열을 이동하기 위한 열전송관(21,22,23), 그리고 발생하는 탄화 가스를 외부로 배출하기 위한 연소구(11,12,13,14)와 탄화로에서 발생하는 가스와 탄화열을 연소구(11,12,13,14) 또는 열전송관(21,22,23)으로 방향 전환할 수 있는 밸브(41,42,43,44)와 탄화로에서 발생하는 가스와 탄화열의 상태를 파악하기 위한 온습도센서(61,62,63,64)와 온습도센서(61,62,63,64)의 정보를 취득하여 밸브(41,42,43,44)의 조절을 위한 제어반(51,52)으로 구성된다.In order to achieve the above object, according to the present invention, there are provided a plurality of carbonization furnaces, two outlets (31, 32, 33, 34) for exhausting gas and carbonization heat generated from the plurality of carbonization furnaces, 32, 33, 34), heat transfer tubes (21, 22, 23) for moving the generated heat of combustion, combustion holes (11, 12, 13, 14) for discharging generated carbonaceous gas to the outside, (41, 42, 43, 44) capable of redirecting gas and carbonized heat generated in the combustion chamber (11, 12, 13, 14) or heat transfer tubes Humidity and
이상에서 설명한 바와 같이 본 발명에서는 목탄의 제조 과정에서 필수 요소인 목재의 건조를 위한 건조실이 따로 필요하지 않으며, 건조실에서의 목재 건조 과정에 따른 열원을 목탄 제조 과정에서 낭비되고 있는 탄화열을 이용함으로써 에너지의 재활용이 가능하고, 건조실에서 탄화로로의 목재 이동 비용과 시간을 줄임으로써 목탄 제조를 단가를 낮출 수 있는 장점이 있다.As described above, in the present invention, a drying chamber for drying wood, which is an essential element in the process of manufacturing charcoal, is not required, and the heat source for drying the wood in the drying chamber is used by using the heat of carbonization, Energy can be recycled, and the cost of wood moving from the drying chamber to the carbonization furnace can be reduced, thereby reducing the manufacturing cost of the charcoal.
도 1은 본 발정에 따른 순환형 탄화로 시스템에 대한 구성도.1 is a schematic view of a circulation type carbonization furnace according to the present invention;
본 발명의 실시하기 위한 구체적인 실시예는 첨부도면에 의하여 상세하게 설명한다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS [0028] Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 따른 탄화로의 탄화열을 순환을 위한 시스템 이용한 구성도로서, 목탄을 제조하기 위한 탄화로를 2기 구비하고, 이 2기의 탄화로에는 목탄 제조시 발생하는 가스와 탄화열을 배출하기 위한 배출구(31,32,33,34)를 설치한다.FIG. 1 is a view showing a system using a system for circulating carbonization of a carbonization furnace according to the present invention, in which two carbonization furnaces for producing charcoal are provided. In the two carbonization furnaces, (31, 32, 33, 34) for discharging heat.
배출구(31,32,33,34)에는 탄화시 발생하는 가스를 배출하기 위한 연소구(11,12,13,14)와 탄화열의 전송을 위한 열전송관(21,22,23)과 연소구와 열전송관으로 가스와 탄화열을 분배하기 위한 밸브(41,42,43,44)로 구성한다.The
또한 탄화로 내에서 발생하는 가스 및 탄화열을 측정하기 위한 온습도센서(61,62,63,64)를 설치하고 측정된 온습도를 취합하여 밸브(41,42,43,44)를 조절하기 위한 제어반(51,52)를 설치한다.
1차 탄화로(A)에서 탄화 과정시 발생한 가스와 탄화열을 온습도센서(61,62)에서 측정하여 일정 온도(250도)에 이르렀을 경우 제어반(51)에서는 밸브(42)를 개폐하여 열전송관(22)를 통해 2차 탄화로(B)로 탄화열을 이송하고, 2차 탄화로에서는 밸브(43)를 개폐하여 탄화로 내부로 탄화열을 삽입하여 2차 탄화로(B)에 적층된 목재를 1차 탄화로(A)에서 발생된 탄화열로 건조시킨다.When the gas and carbonization heat generated during the carbonization process in the primary carbonization furnace A are measured by the temperature and
2차 탄화로(B)에 설치된 온습도센서(63,64)는 2차 탄화로 내의 목재의 온습도를 측정하여, 측정된 데이터를 제어반(52)로 전송하여 2차 탄화로내의 목재의 수분이 17% 이하로 되었을 경우 제어반(52)는 밸브(42,43)를 개폐하여 1차 탄화로에서 발생하는 배기 가스를 연소구(12)를 통해 외부로 배출한다.The temperature and
목탄 제조 과정에서 초기에 발생하는 가스 및 탄화열은 일정 정도의 수분을 포함함으로 제어반(51)에서는 배출되는 가스 및 탄화열이 일정 정도 습도 이하로 되었을 경우에 밸브(42)를 조절하여 2차 탄화로(B)로 탄화열을 전송하여 2차 탄화로에 적층된 목재의 건조에 1차 탄화로의 탄화열을 이용할 수 있도록 한다.Since the gas and carbonization heat generated at the beginning of the charcoal manufacturing process contain a certain amount of water, the
A,B : 탄화로
11,12,13,14 : 연소구
21,22,23 : 열전송관
31,32,33,34 : 배출구
41,42,43,44 : 밸브
51,52 : 제어반
61,62,63,64 : 온습도센서A, B:
11, 12, 13, 14:
21, 22, 23:
31, 32, 33, 34:
41, 42, 43,
51, 52: control panel
61, 62, 63, 64: Temperature and humidity sensor
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105202754A (en) * | 2015-10-23 | 2015-12-30 | 无锡溥汇机械科技有限公司 | Dual-channel gas heating device |
CN108908596A (en) * | 2018-07-28 | 2018-11-30 | 福建杜氏木业有限公司 | Bamboo chip carbonization drying process |
CN109397450A (en) * | 2018-11-08 | 2019-03-01 | 泉州台商投资区恒鑫隆网络科技有限公司 | A kind of carbonization of wood device |
CN110066673A (en) * | 2019-05-10 | 2019-07-30 | 浙江农林大学 | A kind of energy-saving and environment-friendly bamboo charcoal kiln structure |
KR102610844B1 (en) * | 2023-08-23 | 2023-12-06 | 주식회사 카본텍 | Processing system for manufacturing charcoal |
-
2013
- 2013-12-03 KR KR1020130149006A patent/KR20150064370A/en not_active Application Discontinuation
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105202754A (en) * | 2015-10-23 | 2015-12-30 | 无锡溥汇机械科技有限公司 | Dual-channel gas heating device |
CN108908596A (en) * | 2018-07-28 | 2018-11-30 | 福建杜氏木业有限公司 | Bamboo chip carbonization drying process |
CN109397450A (en) * | 2018-11-08 | 2019-03-01 | 泉州台商投资区恒鑫隆网络科技有限公司 | A kind of carbonization of wood device |
CN110066673A (en) * | 2019-05-10 | 2019-07-30 | 浙江农林大学 | A kind of energy-saving and environment-friendly bamboo charcoal kiln structure |
KR102610844B1 (en) * | 2023-08-23 | 2023-12-06 | 주식회사 카본텍 | Processing system for manufacturing charcoal |
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