CN2198275Y - High efficiency plant charring furnace - Google Patents

High efficiency plant charring furnace Download PDF

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Publication number
CN2198275Y
CN2198275Y CN 93221716 CN93221716U CN2198275Y CN 2198275 Y CN2198275 Y CN 2198275Y CN 93221716 CN93221716 CN 93221716 CN 93221716 U CN93221716 U CN 93221716U CN 2198275 Y CN2198275 Y CN 2198275Y
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China
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gas
valve
utility
model
liquid separator
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Expired - Fee Related
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CN 93221716
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Chinese (zh)
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邹本清
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Individual
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Individual
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Priority to CN 93221716 priority Critical patent/CN2198275Y/en
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Publication of CN2198275Y publication Critical patent/CN2198275Y/en
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Abstract

The utility model relates to a high efficiency plant charring furnace, which belongs to a plant type stick dry distillation device. The utility model is mainly composed of a furnace body (4), a cyclone dust collector (6), a cooling condenser (5), a gas-liquid separator (2), controlling valves A1, A2, A3, A4, A5, A6, a blower fan (3) and attached pieces thereof. The utility model adopts a method that furnace gas replaces water for direct cooling to enhance the quality of carbon production and the work efficiency of the production; the utility model can use non-condensable gas as fuel to decrease pollution and save energy; the utility model can also extract vegetable oil as chemical raw material or the fuel, which is suitable for the production of middle and small size manufacturers.

Description

High efficiency plant charring furnace
The utility model relates to a kind of charring furnace, particularly is suitable for vegetable fibre and is pressed into the device that clavate is carried out the charing processing.
The autocracy application of current relevant charring furnace is a lot of, is that 91229539.2 " energy-efficient charing stove " is exactly wherein a kind of as application number.It has adopted the oxygenation complex art of igniting, steam cooling cooling technology and condensation to reclaim the technical measures of wood tar oil.The weak point of this charing equipment is that structure is complicated, and the steam cooling effect is not good enough, and the time of coming out of the stove is longer, can't solve the utilization again and the atmospheric pollution of combustible gas.
The purpose of this utility model provides a kind of improved plant carbonated device, it can improve plant charcoal quality, shorten the time of coming out of the stove, save energy, minimizing pollute.
The purpose of this utility model realizes by following measure:
A, the flue that the charing material is housed 8 heating in body of heater 4, being provided with, and make it to produce hot gas, employing tornado dust collector 6 are removed the impurity in the hot gas, thereby improve the quality of charcoal.
B, the hot gas cooling of adopting cooler condenser 5 that the also process whirlwind removal of impurities of generation in the flue 8 is purified, cold air after the cooling is transmitted back in the flue 8 by gas blower again, the temperature of plant charcoal is wherein quickly fallen to below 50 ℃, shorten the time of coming out of the stove thereby quickened process of cooling, also omitted a cover spray equipment.
C, employing gas-liquid separator 2, gas and vegetables oil are separated, variable valve A1 enters the suitable for reading effusive inflammable gas of gas-liquid separator 2 in the combustion chamber 11 through the control valve A4 of piping combustion-supporting, improves the flue temperature and accelerates carbonization process, has saved fuel and has reduced atmospheric pollution.
The utility model has guaranteed carbonization quality owing to adopted the whirlwind impurity removing technology.Adopted to inflammable gas reclaim, combustion-supporting technical measures, can improve furnace temperature and reduce energy consumption and can reduce atmospheric pollution again.Use the cold air falling temperature technique, accelerated the process of cooling of flue, shortened the time of coming out of the stove.Thereby reached the purpose of design.
The concrete structure of utility model is provided by following embodiment and accompanying drawing.
Fig. 1 is the synoptic diagram of effective botanic charred furnace.
1 is storage tank among the figure, and 2 is gas-liquid separator, and 3 is gas blower, and 4 is body of heater, 5 is cooler condenser, and 6 is tornado dust collector, and 7 is chimney, and 8 is flue, 9 is fire door, and 10 is the upflow tube of gas-liquid separator, and 11 is the combustion chamber, A1, A2, A3, A4, A5, A6, is control valve." → " expression cooler condenser water (flow) direction, by under advance by last row.
The utility model is described in further detail below in conjunction with Fig. 1.
Effective botanic charred furnace is made up of many pipelines of body of heater 4, combustion chamber 11, flue 8, fire door 9, chimney 10, tornado dust collector 6, cooler condenser 5, gas-liquid separator 2, upflow tube 10, storage tank 1, gas blower 3 and control valve A1, A2, A3, A4, A5, A6 and different diameter.
Volume is set is 3.5 cubic metres the flue that can seal 8 in body of heater 4, is 270 millimeters pipeline by diameter, and flue 8 is connected with cooling cooler 5 with 3.5 square metres of heat interchanging areas and gas separator 2 with tornado dust collector 6.Upflow tube 10 on the gas-liquid separator 2 communicates with storage tank 1.Be that 150 millimeters pipeline is connected through valve A3, gas blower 3, valve A5, A6 the following outlet of cooler condenser 5 with flue 8 with diameter again.The upper outlet of gas-liquid separator 2 is that 60 millimeters pipelines are connected with A4 by diameter.The outlet of flue 8 with A1, A4, also be to be that 60 millimeters pipeline is connected by diameter, the outlet of gas-liquid separator 2 is that 60 millimeters pipelines are connected with diameter also with upflow tube 10, storage tank 1, valve A2.
Its process is: first shut-off valve A3, A5, A6, open valve A1, A2, A4 and give cooler condenser 5 logical cold water, again the coal in the combustion chamber 11 is lighted the heating flue 8 isolated with air, plant type rod in the flue of packing into is heated, makes moisture evaporation charing then (realization thermopositive reaction) and generate hot gas.After the normal operation, start tornado dust collector 6, cooler condenser 5, gas-liquid separator 2, upflow tube 10, storage tank 1, valve A2 and pipeline.Through tornado dust collector 6 impurity in the hot gas is removed, can be improved the quality of charing.Hot gas through purifying enters the cooling that is cooled in the cooler condenser 5, treats that vegetables oil splashes into gas-liquid separator 2 from cooler condenser 5 through valve A2, flows in the storage tank 1 when hydrops surpasses upflow tube 10, has so just reclaimed vegetables oil.Note regulating A1, the feed rate of control hot gas is utilized the effusive combustible gas of gas-liquid separator 2 upper outlets, combustible gas is entered in the combustion chamber 11 through valve A4, makes the combustion chamber keep the vigorous intensity of a fire, in time reduce or no longer fire coal saved the energy, stop gaseous emission, reduce atmospheric pollution.Made the flue temperature reach 490 ± 10 ℃ through 7~8 hours, shut-off valve A4, A1 stop heating.Treat that vegetables oil is after the amount that valve A2 splashes into gas separator 2 falls sharply, shut-off valve A2, open valve A3, A6 and gas blower 3, in the gas that cools is sent into flue 8, the temperature of flue 8 is descended rapidly, and suitable variable valve A5 is when making whole flue temperature all drop to below 50 ℃ equably, turn off the blast, open fire door 9 and go out charcoal.The charcoal of producing with this device has black glossy, button metal and stone sound arranged, water content is lower than 4%.The whole cycle is less than 12 hours, has improved work efficiency.

Claims (3)

1, a kind of effective botanic charred furnace, it is made up of body of heater (4), combustion chamber (11) and pipeline etc., it is characterized in that:
A, volume is set in body of heater (4) is 3.5 cubic metres the flue that can seal (8), and it and tornado dust collector (6) have the cooler condenser (5) of 3.5 square metres of heat interchanging areas, and gas-liquid separator (2) is connected with pipeline.
B, form the vegetables oil retrieving arrangement by upflow tube (10) and storage tank (1), the outlet of gas-liquid separator (2) communicates with upflow tube (10) and storage tank (1), valve (A2).
2, effective botanic charred furnace according to claim 1, it is characterized in that: refrigerating unit is made up of cooling condensation (5) and gas blower (3) and valve (A3, A6), and the following outlet of cooler condenser (5) communicates with flue (8) through valve (A3), gas blower (3), valve (A5, A6).
3, effective botanic charred furnace according to claim 1 is characterized in that: auxiliary combustion equipment is made up of gas-liquid separator (2) and control valve (A1, A4), and the upper outlet of gas-liquid separator communicates with valve (A4), combustion chamber (11).
CN 93221716 1993-08-16 1993-08-16 High efficiency plant charring furnace Expired - Fee Related CN2198275Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 93221716 CN2198275Y (en) 1993-08-16 1993-08-16 High efficiency plant charring furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 93221716 CN2198275Y (en) 1993-08-16 1993-08-16 High efficiency plant charring furnace

Publications (1)

Publication Number Publication Date
CN2198275Y true CN2198275Y (en) 1995-05-24

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ID=33800498

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 93221716 Expired - Fee Related CN2198275Y (en) 1993-08-16 1993-08-16 High efficiency plant charring furnace

Country Status (1)

Country Link
CN (1) CN2198275Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1098910C (en) * 2000-01-12 2003-01-15 中国科学技术大学 Thermal-cracking decoking biomass gasification furnace
CN100434361C (en) * 2007-03-12 2008-11-19 陈温福 Simply corncob granule carbonization furnace and preparation method thereof
CN106590699A (en) * 2015-10-20 2017-04-26 晏廷书 Coke quenching technology

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1098910C (en) * 2000-01-12 2003-01-15 中国科学技术大学 Thermal-cracking decoking biomass gasification furnace
CN100434361C (en) * 2007-03-12 2008-11-19 陈温福 Simply corncob granule carbonization furnace and preparation method thereof
CN106590699A (en) * 2015-10-20 2017-04-26 晏廷书 Coke quenching technology

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C19 Lapse of patent right due to non-payment of the annual fee
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