CN105950191A - Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating - Google Patents
Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating Download PDFInfo
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- CN105950191A CN105950191A CN201610243558.1A CN201610243558A CN105950191A CN 105950191 A CN105950191 A CN 105950191A CN 201610243558 A CN201610243558 A CN 201610243558A CN 105950191 A CN105950191 A CN 105950191A
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- gas
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- chamber
- waste gas
- heating
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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
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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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/02—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
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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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/18—Modifying the properties of the distillation gases in the oven
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Coke Industry (AREA)
Abstract
The invention discloses an integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating. The integrated apparatus comprises a charcoal burner, a gas storage cabinet and an exhaust gas purifying device, wherein the charcoal burner comprises a burner body and a burner pipe; a combustion nozzle is arranged in the burner body; a wood gas storage cavity and an exhaust gas storage cavity are arranged in the gas storage cabinet; the burner pipe is communicated with the wood gas storage cavity through a first wood gas conveyer pipe; the burner pipe and the burner body are both communicated with the exhaust gas storage cavity through a first exhaust gas conveyer pipe; the wood gas storage cavity is connected with a second wood gas conveyer pipe; and the exhaust gas storage cavity is connected with a second exhaust gas conveyer pipe which is used for conveying exhaust gas in the exhaust gas storage cavity to the exhaust gas purifying device. The integrated apparatus can improve destructive distillation efficiency and treat wood gas and exhaust gas produced in heating; the integrated apparatus can store wood gas, so a fuel is provided for heating; and the exhaust gas purifying device is used for purifying exhaust gas before evacuation of the exhaust gas, so environmental pollution is avoided.
Description
Technical field
The invention belongs to Linesless charcoal retorting technique field, the heating and the process heating that are specifically related to a kind of Linesless charcoal dry distilling are produced
The integrated apparatus of angry body.
Background technology
During charcoal burner charcoal processing, the high-temp waste gas of generation of forward and backward phase and wood gas, a lot of producers directly discharge, right
Environment causes the biggest pollution.Also have some producers, after high temperature wood gas is first carried out wood tar electric fishing collection, water receiving between entrance
Cooler, is down to wood gas about 180 DEG C, enters back into gas dust remover, from gas dust remover purified gas out, by gas drum
Blower fan press-in spray water cooler cooling and dehydration, after being down to the coal gas entrance gas storage holder voltage stabilizing of room temperature, delivered to by gas pressurizer
Each user (drying kiln cut by charcoal burner or wood) makees fuel, and process above flow process is complex, and cost is high, difficult operation, it is impossible to utilize
The heat of high temperature wood gas, and easily scaling loss cloth bag, the high temperature wood gas that the high-temp waste gas of early stage generation and later stage produce is not
Can efficiently separate.
Summary of the invention
It is an object of the invention to overcome above-mentioned deficiency of the prior art, it is provided that the heating of a kind of Linesless charcoal dry distilling and process
Heat the integrated apparatus of produced gas.This integrated apparatus can be effectively improved dry distillation efficiency, additionally it is possible to described heating
Wood gas and waste gas that link produces process, and make wood gas effectively to store, and then provide for described heating link
Fuel, can also empty after waste gas being carried out purified treatment by described waste gas purification apparatus, it is to avoid cause environment simultaneously again
Pollute.
For achieving the above object, the technical solution used in the present invention is: heating and the process heating of Linesless charcoal dry distilling are produced
The integrated apparatus of gas, it is characterised in that: include that charcoal burner, gas storage holder and waste gas purification apparatus, described charcoal burner include stove
Body and the flue being arranged in described body of heater, be provided with the burner noz(zle) for heating described flue, described storage in described body of heater
Being provided with wood gas storage chamber and waste gas storage chamber in gas holder, described flue and described wood gas storage chamber are by first
Xyloid coal letter shoot is connected, and described flue and described body of heater are all by the first waste gas pipeline and described waste gas storage chamber phase
Connection, described wood gas storage chamber connects to be had for the wood gas that it is interior is delivered to described burner noz(zle) for use as fuel
Second xyloid coal letter shoot, described waste gas storage chamber connects to be had for the waste gas that it is interior is delivered to described waste gas purification apparatus
The second waste gas pipeline.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
Multiple preheating groove utilizing wood gas heat and waste-gas heat that the flue of charcoal burner is preheated is offered on gas storage holder.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
Waste gas purification apparatus includes indirect water-cooling device and is positioned at the collecting pit below described indirect water-cooling device, and described indirect water-cooling device includes
Water cooler body, described water cooler this most internal be provided with cooling chamber, be positioned at the upper chamber above described cooling chamber and be positioned at
Lower chambers below described cooling chamber, is provided with multiple for connecting described upper chamber and lower chambers in described cooling chamber
Vertical tube, described water cooling body offers the water inlet for being passed through cooling water in described cooling chamber and for by described
The outlet that cooling water drainage in cooling chamber goes out, described water cooler body is provided with for connecting described upper chamber and second
The exhaust gas inlet of waste gas pipeline, for the waste gas outlet that the gas of bottom chamber is discharged and be used for the wood of bottom chamber
Vinegar liquid and wood tar mixed liquor are discharged to the discharging tube of collecting pit.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
Waste gas purification apparatus also includes the spray dehydration for the waste gas exported from described indirect water-cooling device carries out spray for dust suppression process
Tower, described spray dehydrating tower includes dehydrating tower body, and described dehydrating tower is the most internal to be provided with for the exhaust blast water interior for it
The injector head of mist, the upper end of described dehydrating tower body is provided with the evacuation port for being discharged by the waste gas through spray for dust suppression.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
This internal dehydration layer being provided with between described injector head and evacuation port for making waste gas be dehydrated of dehydrating tower.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
The first collecting chamber for storing wood tar it is provided with, for storing the second collecting chamber of wood vinegar and for depositing in collecting pit
Storage wood tar and the 3rd collecting chamber of wood vinegar mixed liquor, described 3rd collecting chamber and wood gas storage chamber and the described 3rd
Collecting chamber is all connected by mixed liquor conveying pipe with waste gas storage chamber, and described discharging tube extend into described 3rd collecting chamber
In, described 3rd collecting chamber is between described first collecting chamber and the second collecting chamber, and described first collecting chamber and the 3rd is collected
Chamber is separated by the first baffle plate, and described second collecting chamber and the 3rd collecting chamber are separated by second baffle, described first baffle plate
The wood tar overflow that is provided with in guiding described 3rd collecting chamber of middle part to the spout hole of described first collecting chamber, described the
The wood vinegar that the bottom of two baffle plates is provided with in guiding described 3rd collecting chamber enters the pod apertures of described second collecting chamber.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
It is provided with the first wood gas conveying fan on first xyloid coal letter shoot, described second xyloid coal letter shoot is provided with the second wood
Coal gas conveying fan.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
Waste gas conveying fan it is provided with on first waste gas pipeline.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
There is the first explosion venting valve of blast and for preventing in the wood gas being provided with on gas storage holder in preventing wood gas storage chamber
There is the second explosion venting valve of blast in the waste gas in waste gas storage chamber.
The integrated apparatus of produced gas is heated in the heating of above-mentioned Linesless charcoal dry distilling and process, it is characterised in that: described
The balanced valve for the pressure in described wood gas storage chamber is adjusted it is provided with on gas storage holder.
The present invention compared with prior art has the advantage that
1, the present invention can either complete the heating link of Linesless charcoal dry distilling by charcoal burner, and the body of heater of charcoal burner divides mutually with flue
From, by the way of lifting, flue is lifted in body of heater in use, and uses flue indirect heating manner, adding of flue
Hot link is carried out in body of heater, remaining shove charge, cool down, the link such as come out of the stove is carried out outside body of heater, the heating process of a flue is complete
Can directly lift another flue after one-tenth to heat, substantially increase dry distillation efficiency；This integrated apparatus can also be to institute
Wood gas and the waste gas of stating heating link generation process, and make wood gas effectively to store, and then are described heating ring
Joint provides fuel, it is to avoid cause waste and the pollution to air after being discharged by wood gas, simultaneously can also be clean by described waste gas
After gasifying device carries out purified treatment to waste gas, then will process after exhaust gas evacuation, it is to avoid to environment.
2, the present invention is by arranging preheating groove on gas storage holder, it is possible to preheats flue, takes full advantage of xyloid coal
Gas heat and the heat of waste-gas heat, the most effectively saved the fuel that flue is consumed in heating link simultaneously.Further, so
The cooling of wood gas in wood gas storage chamber can also be accelerated, and then by wood vinegar contained in wood gas and wood tar analysis
Go out, in like manner, it is also possible to the cooling of waste gas in acceleration waste gas storage chamber, make wood vinegar contained in waste gas and wood tar separate out.
3, waste gas can effectively be processed by the present invention by indirect water-cooling device, makes the wood vinegar in waste gas and wood burnt
Oil is effective to be separated out, and improves the yield of wood vinegar and wood tar, avoid the wood vinegar in waste gas and wood tar emptying simultaneously and
Cause environmental pollution.
4, the present invention is by arranging spray dehydrating tower, it is possible to carry out the waste gas discharged by indirect water-cooling device further
Reason, enables the dust in waste gas and other impurity thoroughly to be removed, it is ensured that the waste gas of emptying will not be to environment.
5, the present invention is by arranging the first explosion venting valve, it is possible to the wood gas generation explosion time in wood gas storage chamber,
Effectively released blast pressure by the first explosion venting valve, play the purpose of protection gas storage holder；In like manner, by arranging the second explosion venting valve,
Can effectively be released blast pressure by the second explosion venting valve at the waste gas generation explosion time in waste gas storage chamber, play protection
The purpose of gas storage holder.
6, the present invention is by arranging balanced valve, it can be ensured that the pressure in wood gas storage chamber is maintained at a safety
In the range of.
Below by drawings and Examples, technical scheme is described in further detail.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the A-A cutaway view Amplified image of Fig. 1.
Fig. 3 is the B-B cutaway view Amplified image of Fig. 1.
Fig. 4 is the enlarged drawing in Fig. 3 at E.
Fig. 5 is the C-C cutaway view Amplified image of Fig. 1.
Fig. 6 is the D-D cutaway view Amplified image of Fig. 1.
Description of reference numerals:
1 charcoal burner；1-1 body of heater；
1-2 flue；1-3 burner noz(zle)；
2 first xyloid coal letter shoots；3 first waste gas pipelines；
4 gas storage holders；4-1 wood gas storage chamber；
4-2 waste gas storage chamber；4-3 preheats groove；
4-4 mixed liquor delivery outlet；5 first wood gas conveying fans；
6 waste gas conveying fans；7 second wood gas conveying fans；
8 second xyloid coal letter shoots；9 indirect water-cooling devices；
9-1 water cooler body；9-2 upper chamber；
9-3 cooling chamber；9-4 vertical tube；
9-5 lower chambers；9-6 exhaust gas inlet；
9-7 waste gas outlet；9-8 discharging tube；
10 spray dehydrating towers；10-1 dehydrating tower body；
10-2 injector head；10-3 evacuation port；
10-4 is dehydrated layer；11 mixed liquor conveying pipes；
12 second waste gas pipelines；13 three way cock；
14 collecting pits；14-1 the first collecting chamber；
14-2 the second collecting chamber；14-3 the 3rd collecting chamber；
14-4 the first baffle plate；14-5 second baffle；
14-6 spout hole；14-7 pod apertures；
15 flue gas delivery pipe；16 first explosion venting valves；
17 balanced valves；18 second explosion venting valves.
19 first valves；20 second valves.
Detailed description of the invention
The integrated apparatus of produced gas, bag are heated in the heating of a kind of Linesless charcoal dry distilling as depicted in figs. 1 and 2 and process
Including charcoal burner 1, gas storage holder 4 and waste gas purification apparatus, described charcoal burner 1 includes body of heater 1-1 and is arranged in described body of heater 1-1
Flue 1-2, is provided with the burner noz(zle) 1-3 for heating described flue 1-2, arranges in described gas storage holder 4 in described body of heater 1-1
There are wood gas storage chamber 4-1 and waste gas storage chamber 4-2, described flue 1-2 and described wood gas storage chamber 4-1 by the
One xyloid coal letter shoot 2 is connected, and described flue 1-2 and described body of heater 1-1 is all by the first waste gas pipeline 3 and described waste gas
Storage chamber 4-2 is connected, and described wood gas storage chamber 4-1 connects to be had for the wood gas that it is interior is delivered to described burning
Nozzle 1-3 is for use as the second xyloid coal letter shoot 8 of fuel, and described waste gas storage chamber 4-2 connects to be had for interior giving up by it
Gas is delivered to the second waste gas pipeline 12 of described waste gas purification apparatus.
As depicted in figs. 1 and 2, in the present embodiment, this integrated apparatus in use, first will install wooden raw-material
Flue 1-2 is lifted in body of heater 1-1, and guarantees to be tightly connected between flue 1-2 and body of heater 1-1, and supplementing pipeline by combustion gas is
Burner noz(zle) 1-3 provides combustion gas, and then starts dry distilling for flue 1-2 heating, typically using temperature in flue be 350 DEG C as marking
Standard, when the temperature in flue 1-2 is less than 350 DEG C, in flue 1-2 expellant gas, wood gas content is the highest, now flue 1-2
Expellant gas the three way cock 13 through flue 1-2 upper end enter in the first waste gas pipeline 3, and now in body of heater 1-1
Flue gas through flue gas delivery pipe 15 also in the first waste gas pipeline 3, now in flue 1-2 in expellant gas and body of heater 1-1
Discharge flue gas and collectively form waste gas, and carry out in being delivered to the waste gas storage chamber 4-2 of gas storage holder 4 by the first waste gas pipeline 3
Storage, when the temperature in flue 1-2 constantly rises to more than 350 DEG C, now wood gas content in flue 1-2 expellant gas
Higher, the second valve 20 on the first waste gas pipeline 3 is turned off, in cutting off flue 1-2, wood gas is to the first waste gas pipeline 3
Conveying, and open the first valve 19 on the first xyloid coal letter shoot 2, make the wood gas in flue 1-2 to the first wood gas
Conveying pipe 2 carries, and is delivered to the wood gas storage chamber 4-1 of gas storage holder 4 by described first xyloid coal letter shoot 2 and deposits
Storage, the wood gas in described wood gas storage chamber 4-1 through the second xyloid coal letter shoot 8 be delivered to burner noz(zle) 1-3 for use as
The heating fuel of flue 1-2, waste gas now is only by the flue gas discharged in body of heater 1-1.
In the present embodiment, this integrated apparatus can either complete the heating link of Linesless charcoal dry distilling, described wood by charcoal burner 1
The body of heater 1-1 and flue 1-2 of charcoal stove 1 is separated, and is lifted in body of heater 1-1 by flue 1-2 in use by the way of lifting,
And using flue 1-2 indirect heating manner, the heating link of flue 1-2 is carried out in body of heater 1-1, remaining shove charge, cools down, goes out
The links such as stove are carried out outside body of heater 1-1, and the heating process of a flue 1-2 can directly lift another flue 1-2 after completing
Heat, substantially increase dry distillation efficiency；The wood gas that described heating link can also be produced by this integrated apparatus is with useless
Gas processes, and makes wood gas effectively to store, and then provides fuel for described heating link, it is to avoid discharged by wood gas
After cause waste and pollution to air, after waste gas can also being carried out purified treatment by described waste gas purification apparatus simultaneously,
Exhaust gas evacuation after processing again, it is to avoid to environment.
As depicted in figs. 1 and 2, described gas storage holder 4 offers multiple utilize wood gas heat and waste-gas heat to Linesless charcoal
The flue 1-2 of stove 1 carries out the preheating groove 4-3 preheated.
In the present embodiment, by arranging preheating groove 4-3 on described gas storage holder 4, it is possible to flue 1-2 is preheated,
Take full advantage of the heat of wood gas heat and waste-gas heat, the most effectively saved flue 1-2 simultaneously and disappeared in heating link
The fuel of consumption.Further, the cooling of wood gas in wood gas storage chamber 4-1 can also so be accelerated, and then by institute in wood gas
The wood vinegar contained and wood tar separate out, in like manner, it is also possible to the cooling of waste gas in acceleration waste gas storage chamber 4-2, make institute in waste gas
The wood vinegar contained and wood tar separate out.
As shown in Fig. 3, Fig. 4 and Fig. 5, described waste gas purification apparatus includes indirect water-cooling device 9 and is positioned at described indirect water-cooling
Collecting pit 14 below device 9, described indirect water-cooling device 9 includes water cooler body 9-1, is provided with in described water cooler body 9-1
Cooling chamber 9-3, it is positioned at the upper chamber 9-2 above described cooling chamber 9-3 and is positioned at the cavity of resorption below described cooling chamber 9-3
Room 9-5, is provided with multiple vertical tube 9-4 for connecting described upper chamber 9-2 and lower chambers 9-5, institute in described cooling chamber 9-3
State the water inlet offered on water cooling body 9-1 for being passed through cooling water in described cooling chamber 9-3 and for by described
The outlet that cooling water drainage in cooling chamber 9-3 goes out, described water cooler body 9-1 is provided with for connecting described upper chamber
9-2 and exhaust gas inlet 9-6 of the second waste gas pipeline 12, for waste gas outlet 9-7 that the gas in lower chambers 9-5 is discharged with
And for the wood vinegar in lower chambers 9-5 and wood tar mixed liquor being discharged to the discharging tube 9-8 of collecting pit 14.
In the present embodiment, in use, the waste gas in described second waste gas pipeline 12 is through waste gas for described indirect water-cooling device 9
Import 9-6 enters upper chamber 9-2, and the waste gas entered in upper chamber 9-2 enters into lower chambers 9-5, and vertical tube through vertical tube 9-4 again
Wood vinegar and wood tar, the wood vinegar of precipitation and wood is separated out after the cooling water temperature cooling of the waste gas cooled chamber 9-3 in 9-4
Tar mixed liquor is in discharging tube 9-8 is discharged to collecting pit 14, and remaining gas is discharged through waste gas outlet 9-7 again.In the present embodiment,
Waste gas can effectively be processed by described indirect water-cooling device 9, makes the wood vinegar in waste gas and wood tar effectively separate out, carries
The high yield of wood vinegar and wood tar, avoids the wood vinegar in waste gas and wood tar emptying to cause environmental pollution simultaneously.
As shown in Fig. 3, Fig. 4 and Fig. 5, described waste gas purification apparatus also includes for exporting from described indirect water-cooling device 9
Waste gas carry out the spray dehydrating tower 10 of spray for dust suppression process, described spray dehydrating tower 10 includes dehydrating tower body 10-1, described
The injector head 10-2 for the exhaust blast water smoke interior for it, described dehydrating tower body 10-1 it is provided with in dehydrating tower body 10-1
Upper end be provided with for by through spray for dust suppression waste gas discharge evacuation port 10-3.
In the present embodiment, by arranging spray dehydrating tower 10, it is possible to discharge by the waste gas outlet 9-7 of indirect water-cooling device 9
Waste gas be further processed, enable dust in waste gas and other impurity thoroughly to be removed, it is ensured that the waste gas of emptying
Will not be to environment.
In the present embodiment, arrange between described injector head 10-2 and evacuation port 10-3 in described dehydrating tower body 10-1
There is the dehydration layer 10-4 for making waste gas be dehydrated.Wherein, described dehydration layer 10-4 is made up of multiple plastics cascade ring stackings, described
Being provided with the pore passed through for waste gas on cascade ring, at waste gas during described pore rises, vapor adhesion is in pore hole
Between wall and adjacent pore, these steam constantly increase finally to fall, owing to described spray dehydrating tower 10 is adopted with the form of water droplet
With recirculated water, the water smoke that ejection is gone is pumped to injector head 10-2 again and proceeds spray for dust suppression, by arranging dehydration layer 10-4, energy
Substantial amounts of water is taken away by the enough effective waste gas that reduces.
As shown in Figure 6, the first collecting chamber 14-1 for storing wood tar it is provided with in described collecting pit 14, for storing
Second collecting chamber 14-2 of wood vinegar and for storing the 3rd collecting chamber 14-3 of wood tar and wood vinegar mixed liquor, described the
Three collecting chamber 14-3 and wood gas storage chamber 4-1 and described 3rd collecting chamber 14-3 all passes through with waste gas storage chamber 4-2
Mixed liquor conveying pipe 11 is connected, and described discharging tube 9-8 extend in described 3rd collecting chamber 14-3, described 3rd collecting chamber
14-3 between described first collecting chamber 14-1 and the second collecting chamber 14-2, described first collecting chamber 14-1 and the 3rd collecting chamber
14-3 is separated by the first baffle plate 14-4, described second collecting chamber 14-2 and the 3rd collecting chamber 14-3 by second baffle 14-5 every
Opening, the wood tar overflow that the middle part of described first baffle plate 14-4 is provided with in guiding described 3rd collecting chamber 14-3 is to described
The spout hole 14-6 of the first collecting chamber 14-1, the bottom of described second baffle 14-5 is provided with for guiding described 3rd collecting chamber
Wood vinegar in 14-3 enters pod apertures 14-7 of described second collecting chamber 14-2.
In the present embodiment, in use, the wood vinegar of waste gas storage chamber 4-2 bottom deposit and wood are burnt for described collecting pit 14
Oil mixed liquor is discharged by mixed liquor delivery outlet 4-4 and is delivered to described 3rd collection by corresponding mixed liquor conveying pipe 11
Chamber 14-3, wood vinegar and the wood tar mixed liquor of wood gas storage chamber 4-1 bottom deposit by mixed liquor delivery outlet 4-4 and pass through
Corresponding mixed liquor conveying pipe 11 is delivered to described 3rd collecting chamber 14-3, meanwhile, the lower chambers of described indirect water-cooling device 9
Wood vinegar and wood tar mixed liquor in 9-5 enter the 3rd collecting chamber 14-3 by discharging tube 9-8, now under discharging tube 9-8
End can extend in wood vinegar and the wood tar mixed liquor of the 3rd collecting chamber 14-3, so can be by the lower end seal of discharging tube 9-8
Live, it is to avoid waste gas escapes.Wood vinegar and wood tar mixed liquor are collected by described 3rd collecting chamber 14-3, due to wood vinegar and
The proportion of wood tar is different, the wood tar on upper strata in described spout hole 14-6 overflow to the first collecting chamber 14-1, the wood of lower floor
Vinegar liquid is flowed in the second collecting chamber 14-2 from described pod apertures 14-7, effectively achieves the separation of wood vinegar and wood tar.
As it is shown in figure 1, be provided with the first wood gas conveying fan 5 on described first xyloid coal letter shoot 2, described second wood
The second wood gas conveying fan 7 it is provided with on gas conveying tube 8.
In the present embodiment, by arranging the first wood gas conveying fan 5, it is possible to make the wood gas in flue 1-2 quick
It is delivered in the wood gas storage chamber 4-1 of gas storage holder 4, in like manner, by arranging the second wood gas conveying fan 7, it is possible to make wood
Wood gas in coal gas storage chamber 4-1 is quickly delivered to burner noz(zle) 1-3, provides sufficient xyloid coal for burner noz(zle) 1-3
Gas.
As it is shown in figure 1, be provided with waste gas conveying fan 6 on described first waste gas pipeline 3.By arranging waste gas conveying wind
Machine 6, it is possible to make the waste gas in entrance the first waste gas pipeline 3 quickly be delivered in the waste gas storage chamber 4-2 of gas storage holder 4.
As it is shown in figure 1, the wood gas being provided with on described gas storage holder 4 in preventing wood gas storage chamber 4-1 occurs
There is the second explosion venting valve 18 of blast in the first explosion venting valve 16 of blast and the waste gas in preventing waste gas storage chamber 4-2.
In the present embodiment, by arranging the first explosion venting valve 16, it is possible to the wood gas in wood gas storage chamber 4-1 occurs
Explosion time, is effectively released blast pressure by the first explosion venting valve 16, plays the purpose of protection gas storage holder 4；In like manner, by arranging
Two explosion venting valves 18, it is possible to the waste gas generation explosion time in waste gas storage chamber 4-2, are effectively released quick-fried by the second explosion venting valve 18
Fried pressure, plays the purpose of protection gas storage holder 4.
In the present embodiment, described first explosion venting valve 16 and the second explosion venting valve 18 are made circular valve body by steel plate, and valve body divides
It is two sections, is sandwiched between aluminium alloy diaphragm.At explosion time, first aluminium alloy diaphragm is tattered, effectively plays protection gas storage holder 4
Effect.
As it is shown in figure 5, be provided with on described gas storage holder 4 for the pressure in described wood gas storage chamber 4-1 is carried out
The balanced valve 17 of regulation.
In the present embodiment, described balanced valve 17 mainly has steel pipe and the counterweight being arranged on steel pipe to constitute, in use, when
When in wood gas storage chamber 4-1, wood gas pressure is higher than the described counterweight of balanced valve 17, wood gas push open described counterweight and then
A small amount of wood gas is discharged, and then makes the pressure in wood gas storage chamber 4-1 be maintained in the scope of a safety.
The above, be only presently preferred embodiments of the present invention, not impose any restrictions the present invention, every according to the present invention
Any simple modification, change and the equivalent structure transformation that above example is made by technical spirit, all still falls within skill of the present invention
In the protection domain of art scheme.
Claims (10)
1. Linesless charcoal dry distilling heating and process heat produced gas integrated apparatus, it is characterised in that: include charcoal burner
(1), gas storage holder (4) and waste gas purification apparatus, in described charcoal burner (1) includes body of heater (1-1) and is arranged on described body of heater (1-1)
Flue (1-2), be provided with the burner noz(zle) (1-3) for heating described flue (1-2), described storage in described body of heater (1-1)
Wood gas storage chamber (4-1) and waste gas storage chamber (4-2), described flue (1-2) and described xyloid coal it is provided with in gas holder (4)
Gas storage chamber (4-1) is connected by the first xyloid coal letter shoot (2), and described flue (1-2) and described body of heater (1-1) are the most logical
Crossing the first waste gas pipeline (3) to be connected with described waste gas storage chamber (4-2), described wood gas storage chamber (4-1) connects
Have for the wood gas that it is interior being delivered to the described burner noz(zle) (1-3) the second xyloid coal letter shoot (8) for use as fuel, institute
State waste gas storage chamber (4-2) and connect the second waste gas conveying having for the waste gas that it is interior being delivered to described waste gas purification apparatus
Pipe (12).
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: offer on described gas storage holder (4) and multiple utilize wood gas heat and waste-gas heat to carry out pre-to described flue (1-2)
The preheating groove (4-3) of heat.
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: described waste gas purification apparatus includes indirect water-cooling device (9) and is positioned at the collecting pit of described indirect water-cooling device (9) lower section
(14), described indirect water-cooling device (9) includes water cooler body (9-1), is provided with cooling chamber in described water cooler body (9-1)
(9-3), it is positioned at the upper chamber (9-2) of described cooling chamber (9-3) top and is positioned at the cavity of resorption of described cooling chamber (9-3) lower section
Room (9-5), is provided with multiple for connecting the perpendicular of described upper chamber (9-2) and lower chambers (9-5) in described cooling chamber (9-3)
Pipe (9-4), described water cooling body (9-1) offers the water inlet for being passed through cooling water in described cooling chamber (9-3)
Mouthful and for outlet that the cooling water drainage in described cooling chamber (9-3) is gone out, described water cooler body (9-1) is provided with
For connecting the exhaust gas inlet (9-6) of described upper chamber (9-2) and the second waste gas pipeline (12), for by lower chambers (9-5)
In the waste gas outlet (9-7) discharged of gas and for the wood vinegar in lower chambers (9-5) and wood tar mixed liquor are discharged to
The discharging tube (9-8) of collecting pit (14).
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 3 and process, and it is special
Levy and be: described waste gas purification apparatus also includes for the waste gas exported from described indirect water-cooling device (9) is carried out spray for dust suppression
The spray dehydrating tower (10) processed, described spray dehydrating tower (10) includes dehydrating tower body (10-1), described dehydrating tower body
(10-1) injector head (10-2) for the exhaust blast water smoke interior for it it is provided with in, described dehydrating tower body (10-1) upper
End is provided with the evacuation port (10-3) for being discharged by the waste gas through spray for dust suppression.
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 4 and process, and it is special
Levy and be: be positioned between described injector head (10-2) and evacuation port (10-3) in described dehydrating tower body (10-1) be provided with for
Make the dehydration layer (10-4) that waste gas is dehydrated.
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 3 and process, and it is special
Levy and be: be provided with the first collecting chamber (14-1) for storing wood tar in described collecting pit (14), be used for storing wood vinegar
The second collecting chamber (14-2) and for storing the 3rd collecting chamber (14-3) of wood tar and wood vinegar mixed liquor, the described 3rd
Collecting chamber (14-3) and wood gas storage chamber (4-1) and described 3rd collecting chamber (14-3) and waste gas storage chamber (4-2)
All being connected by mixed liquor conveying pipe (11), described discharging tube (9-8) extend in described 3rd collecting chamber (14-3), described
3rd collecting chamber (14-3) is positioned between described first collecting chamber (14-1) and the second collecting chamber (14-2), described first collecting chamber
(14-1) being separated by the first baffle plate (14-4) with the 3rd collecting chamber (14-3), described second collecting chamber (14-2) is collected with the 3rd
Chamber (14-3) is separated by second baffle (14-5), and the middle part of described first baffle plate (14-4) is provided with for guiding the described 3rd
The spout hole (14-6) of extremely described first collecting chamber (14-1) of the wood tar overflow in collecting chamber (14-3), described second baffle
(14-5) wood vinegar that bottom is provided with in guiding described 3rd collecting chamber (14-3) enters described second collecting chamber
(14-2) pod apertures (14-7).
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: being provided with the first wood gas conveying fan (5) on described first xyloid coal letter shoot (2), described second wood gas is defeated
Send and on pipe (8), be provided with the second wood gas conveying fan (7).
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: on described first waste gas pipeline (3), be provided with waste gas conveying fan (6).
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: the wood gas that is provided with on described gas storage holder (4) in preventing wood gas storage chamber (4-1) occurs the of blast
One explosion venting valve (16) and being used for prevents the waste gas in waste gas storage chamber (4-2) from second explosion venting valve (18) of blast occurring.
The integrated apparatus of produced gas is heated in the heating of Linesless charcoal dry distilling the most according to claim 1 and process, and it is special
Levy and be: be provided with flat for what the pressure in described wood gas storage chamber (4-1) was adjusted on described gas storage holder (4)
Weighing apparatus valve (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610243558.1A CN105950191A (en) | 2016-04-19 | 2016-04-19 | Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610243558.1A CN105950191A (en) | 2016-04-19 | 2016-04-19 | Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating |
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| Publication Number | Publication Date |
|---|---|
| CN105950191A true CN105950191A (en) | 2016-09-21 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610243558.1A Pending CN105950191A (en) | 2016-04-19 | 2016-04-19 | Integrated apparatus for carrying out heating in destructive distillation of charcoal and for treating gas produced by heating |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105950191A (en) |
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| CN203582809U (en) * | 2013-11-14 | 2014-05-07 | 永胜县益农新能源开发有限公司 | Condenser |
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| WO2007056982A2 (en) * | 2005-11-21 | 2007-05-24 | Winkelkoetter Peter | Method for converting organic secondary raw materials into atomised fuel oil as a base for especially fuels, device for carrying out the method, and corresponding fuels |
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Application publication date: 20160921 |