CN104910931B - A kind of farm's solid waste continuous pyrolysis carbonizing treatment method and device - Google Patents
A kind of farm's solid waste continuous pyrolysis carbonizing treatment method and device Download PDFInfo
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Abstract
The present invention relates to a kind of farm's solid waste continuous pyrolysis carbonizing treatment method and device, solid waste break process part：Solid waste is subjected to break process；Heat supply part：One burner is set, the bocca of burner is passed through in a combustion chamber and obtains high-temperature flue gas；Preposition process part：Solid waste after will be broken is inserted in preposition process chamber, and the high-temperature flue gas for introducing heat supply part is heated；Charing process part：Solid waste after preposition processing is sent into charing process room, the high-temperature flue gas for introducing heat supply part is heated；Air treatment section：The gas-phase product produced in preposition processing and charing process is collected respectively to be condensed, and obtains condensed fluid and on-condensible gas；Gas utilizes part：On-condensible gas is introduced in the combustion chamber of heat supply part and is burnt；Present invention also offers a kind of device for realizing this method.The present invention has the advantages that simple technique simplification, device structure, stable and reliable operation, carbonization time is short, capacity usage ratio is high.
Description
Technical field：
The invention belongs to organic waste treatment technical field, more particularly to a kind of farm's solid waste connects
Continuous pyrolysis charring processing method and processing device.
Background technology：
With development in agricultural science and technology and the increase of region cultivation density, feces of livestock and poultry, waste water etc. pair caused by farm
Rural area periphery ecological environment, water quality cause serious harm, particularly in recent years, the viral transmission such as bird flu, farm's waste
If harmless treatment not in time, especially dead livestock and poultry corpse, feces of livestock and poultry and useless feed etc. carry out improper processing, easily cause weight
The generation and propagation of big animal epidemic, or even environmental pollution is caused, the environmental pollution and healthy hidden danger system that farm's waste triggers
Row problem receives much concern.A few days ago, to the especially dead livestock and poultry harmless treatment of farm's waste as a kind of more effective money
Source treatment technology is used by industry gradually.
Chinese invention patent prospectus CN103484135B discloses a kind of efficiently meat corpse pyrolysis treatment device and side
Method, including meat corpse is packed into charging basket pusher into pyrolytic tank, heat source is provided by combustion chamber, makes meat corpse in 300-750 DEG C of condition
Lower pyrolysis charring, the flammable pyrolysis gas produced during pyrolysis charring are exported and burnt automatically, the high-temperature flue gas for generation of burning
Pyrolysis charring is supported in energy supply.During actual use, reflect according to applicant, which can preferably complete meat corpse
Pyrolysis charring, but its there are it is certain the problem of：The desiccation and charing of the device meat corpse integrally carry out in pyrolytic tank, due to
Meat corpse contains substantial amounts of moisture, it needs to consume more heat in drying process makes moisture evaporation in meat corpse, causes meat corpse
Carbonization temperature is low, and carbonization time length, the carbide rate of recovery is low, and the heating load of desiccation and the charing of meat corpse cannot be according to the actual requirements
It is adjusted, its equipment integrated artistic and counter structure are complicated, and of high cost, capacity usage ratio is low.
The content of the invention：
An object of the present invention is in view of the deficiencies of the prior art, there is provided a kind of farm's solid waste Continuous Heat
Solve carbonizing treatment method, this method is dry and charing is separated and independently performed by solid waste, using only a combustion chamber and supporting
Burner provides heat for the actual needs that solid waste is dry and carbonizes, and technique and counter structure simplify, and carbonization time is short, heat
The utilization rate of amount is high, and production cost is low.
The technology solution of the present invention is as follows：
A kind of farm's solid waste continuous pyrolysis carbonizing treatment method, including it is solid waste break process, heat supply, preposition
Processing, charing process, gas treatment and gas utilize part, it is characterised in that：
(a) solid waste break process part：Solid waste is subjected to break process；
(b) heat supply part：One burner is set, the bocca of burner is passed through in a combustion chamber and obtains high-temperature flue gas；
(c) preposition process part：Solid waste after will be broken is inserted in preposition process chamber, introduces the high temperature of heat supply part
Flue gas heats the indoor solid waste of preposition processing by the way of the heating of outer thermal jacket, temperature during work in chuck
For 500-700 DEG C, 100-250 DEG C is heated in preposition process chamber；
(d) charing process part：Solid waste after preposition processing is sent into charing process room, introduces the height of heat supply part
Warm flue gas, heats the indoor solid waste of charing process by the way of the heating of outer thermal jacket, during work in chuck
Temperature is 700-900 DEG C, and charing process heating indoor is to 450-650 DEG C；Charing process room is oxygen debt or anaerobic state；
(e) air treatment section：The gas-phase product produced during preposition process part and charing process is collected, using water
The mode of spray is condensed, and obtains condensed fluid and on-condensible gas；
(f) gas utilizes part：On-condensible gas is introduced in the combustion chamber of heat supply part and is burnt as fuel of heat supply,
The on-condensible gas occurs oxidation reaction and obtains high-temperature flue gas in the combustion chamber, and the temperature of high-temperature flue gas is 700-900 DEG C；
(g) will be discharged after the indoor solid residue cooling of charing process, sealing postcooling preserves.
Water spray is respectively adopted to the gas phase production produced in preposition process part and charing process partial routine in the present invention
Mode is condensed, and is on the one hand that the gas-phase product moisture content being collected into is higher, and shower water can fully blend rapidly with steam
Complete gas-liquid and be converted into liquid；On the other hand it is that can remove the dust contained in gas-phase product at the same time with water spray, plays net
Change the effect of on-condensible gas, on-condensible gas is passed through combustion chamber more abundant in burning.
As an improvement, the pressure of the outer thermal jacket of the preposition process part and charing process part outlet is by independent
Set an air-duct adjusting device being connected with corresponding outer thermal jacket outlet that control, preposition process part and charcoal is adjusted
The pressure changed in the outer thermal jacket of process part is negative pressure.
The pipe is controlled by varying the pipeline flow diameter for the exhaust duct being connected with the air-duct adjusting device
The sectional area in road, i.e., when the circulation diameter of pipeline is become small, the gas flow passed through in its unit interval can reduce；It is on the contrary then
On the contrary, flowing into the flow velocity and flow of gas so as to adjust in the outer thermal jacket of preposition process part and charing process part, and tie
The heating load of combined burner and then the normal working temperature for ensureing preposition process chamber and charing process room.
In the present invention on-condensible gas occur in the combustion chamber oxidation reaction acquisition high-temperature flue gas, be preposition process part and
Charing process part provides thermal energy, realizes energy recycling.
As an improvement, the flue gas of thermal jacket outlet discharge passes through activity outside the preposition process part and charing process part
Charcoal is adsorbed to be discharged with after bag-type dust processing.Particularly, for the nitrogen oxides that contains in flue gas, (NOx), bioxin etc. is poisonous
Qualified discharge after gas is purified by activated carbon adsorption and bag-type dust.
As an improvement, the solid waste includes the mixed of spoil, feces of livestock and poultry, internal organ, useless feed and filoplume composition
At least one of compound.
As an improvement, the burner is neat gas burner, the combustion of biomass particle burner, oil burner, coal dust
Burner.
Gas is utilized in part, and some components of on-condensible gas may not burn fully, using indoor combustion of burning
Burner provides auxiliary thermal source, promotes on-condensible gas fully to burn, while ensure the normal working temperature of combustion chamber.
As an improvement, the ignition temperature of the on-condensible gas is 1000~1100 DEG C.
It is another object of the present invention in view of the deficiencies of the prior art, there is provided a kind of farm's solid waste Continuous Heat
Carbonization processing device is solved, which is separately independently arranged drying machine and retort, only configures a combustion chamber and burner, according to
The actual needs of drying machine and retort carries out heat supply respectively, and equipment and counter structure simplify, and carbonization time is short and carbide returns
High income, operation cost are low, it can be achieved that extensive consecutive production.
The present invention solve the technical problem scheme be：
A kind of farm's solid waste continuous pyrolysis carbonization processing device, including solid waste break process unit, burning
Room, preprocessing unit, charing process unit, air processing unit and gas range site, it is characterised in that：
The solid waste break process unit, feeds solid waste into breaker and is crushed；
The combustion chamber sets a burner；
The preprocessing unit is external-heat drier, which is provided with drying machine chuck, and drying machine chuck leads to
Flue gas delivery pipe road is crossed to communicate with the high-temperature flue gas outlet of combustion chamber；
The charing process unit is external-heat retort, which is provided with retort chuck, and retort chuck leads to
Flue gas delivery pipe road is crossed with the high-temperature flue gas outlet of combustion chamber to be connected；
The air processing unit includes fume collection pipeline, treating column, and the gas vent of drying machine and retort passes through
Fume collection pipeline is connected with treating column, and the gas-phase product produced in drying machine and retort introduces treating column, through spray thrower
Condensed fluid is obtained after spray condensation；
The gas range site includes fixed gas conduit, and the gas outlet for the treatment of column passes through fixed gas conduit and combustion chamber phase
Connection, introduces combustion chamber, the high-temperature flue gas that combustion chamber produces passes through flue gas delivery pipe road by the on-condensible gas obtained in treating column
It is transmitted in drying machine chuck and retort chuck.
As an improvement, the export pipeline of the drying machine chuck and retort chuck be respectively provided with one be used for adjust it is corresponding
The air passage regulating valve of outlet pressure, controls drying machine to press from both sides by air passage regulating valve and the air-introduced machine being connected with the air passage regulating valve
Pressure in set and retort chuck.
The present invention carries out heat supply respectively using only a combustion chamber to drying machine chuck and retort chuck, should by adjusting
The heating load of burner and then adjusting, control and holding enter the temperature of drying machine chuck and the high-temperature flue gas in retort chuck
Degree, and the actual demand in technical process, by adjusting the air passage openings of sizes of air passage regulating valve and the air inducing of air-introduced machine
Amount realizes flow velocity of the high-temperature flue gas in drying machine chuck and retort chuck, and then adjusts, controls and keep drying machine and charcoal
Change stove and remain at suitable operating temperature, it is simple in structure, easily controllable.
As an improvement, being additionally provided with coupled the second logical air-introduced machine on the fixed gas conduit, on-condensible gas is introduced
Burn in combustion chamber as fuel of heat supply, and to the pressure in drying machine chuck and retort chuck individually, accurately
Control.
As an improvement, further include the work for being purified to the flue gas of drying machine chuck and the discharge of retort jacket outlet
Property charcoal adsorption tower and bag filter.
As an improvement, being respectively provided with a chilling tower on the drying machine chuck and retort jacket outlet pipeline, activated carbon is inhaled
Attached tower is located between the chilling tower and the air passage regulating valve, and bag filter outlet is equipped with coupled logical air-introduced machine, does
Dry machine chuck and the flue gas of retort jacket outlet discharge are first inhaled through chilling tower cooler to less than 200 DEG C, then through activated carbon respectively
Discharged after entering bag filter purification after attached tower and air passage regulating valve.
Compared with prior art, the beneficial effects of the present invention are：
(1) present invention is separated solid waste drying and charing independent by being separately separately provided drying machine and retort
Carry out, the normal mode for setting hot-blast stove is respectively adopted in drying machine and retort, and combustion chamber and hot-blast stove are classified as one, only made
With burner, mode of the combustion chamber to drying machine and retort difference heat supply is realized；It is adjusted merely by the heat supply of the burner
Measure and then adjust, control and keep the temperature into drying machine chuck and the high-temperature flue gas in retort chuck, the utilization of heat
Rate is high, and carbonization time is short, and production cost is low.
(2) by the structure and form of the treating column configured, the gas produced to solid waste in drying machine and retort
Phase product cleanup formula is recycled, it can be achieved that carrying out recycling recycling to the pyrolysis gas of a variety of organic solid wastes.
(3) by air passage regulating valve and the collective effect of air-introduced machine, drying machine and the pressure in retort chuck are realized
Precision control, can be according to the actual demand in technical process, by the air passage openings of sizes and air-introduced machine that adjust air passage regulating valve
Absorbing quantity realize flow velocity of the high-temperature flue gas in drying machine chuck and retort chuck, and then adjust, control and keep drying
Machine and retort remain negative pressure state and maintain suitable operating temperature, its simple in structure, easy to adjust and cost is low.
(4) pyrolysis gas purification and bag filter are added, is applicable to the pyrolytic carbon of wider organic solid waste
Change is handled, including common wooden, campanulaceae class biomass, and can particularly be directed to processed material can produce pollution in processing procedure
The solid waste of gas (e.g., Nox , bioxin etc.), such as house refuse, sewage plant sludge, hazardous solid waste, agricultural and stalk
Spoil, feces of livestock and poultry, house refuse, food debris, medical waste and harmful solid waste etc. of dying of illness.
In conclusion the present invention has, technique is simplified, device structure is simple, stable and reliable operation, carbonization time are short, energy
The advantages that utilization rate is high.
Brief description of the drawings：
The present invention is described further below in conjunction with the accompanying drawings：
Fig. 1 is the process flow chart of farm's solid waste continuous pyrolysis carbonizing treatment method of the embodiment of the present invention one；
Fig. 2 is the overall structure signal of farm's solid waste continuous pyrolysis carbonization processing device of the embodiment of the present invention two
Figure；
Fig. 3 is the part-structure schematic diagram of drying machine in the present invention；
Fig. 4 is the part-structure schematic diagram of retort in the present invention；
Fig. 5 is the overall structure diagram of air-duct adjusting device in the present invention.
In figure：1st, combustion chamber；1a, burner；2nd, drying machine；21st, drying machine chuck；The gas vent of 2a, drying machine；
The solids inlet of 2b, drying machine；The solid outlet of 2c, drying machine；3rd, rotary carbide furnace；31st, rotary carbide furnace chuck；3a, rotation
Turn the gas vent of retort；The solids inlet of 3b, rotary carbide furnace；1a, high-temperature flue gas outlet；4th, flue gas delivery pipe road；4a、
Dilute mouth；5th, fume collection pipeline；6th, treating column；61st, spray thrower；7th, the first air-introduced machine；8th, helical feed pipeline；9th, carbonize residual
Slag container；10th, fixed gas conduit；11st, export pipeline；12nd, air passage regulating valve；13rd, activated carbon adsorber；14th, bag filter；
15th, the second air-introduced machine；16th, chilling tower.
Embodiment：
As described below is only presently preferred embodiments of the present invention, and not the scope of the present invention is defined.
Embodiment one
Fig. 1 is the process flow chart of one farm's solid waste pyrolysis charring processing method of embodiment.As shown in Figure 1, one
Kind farm solid waste continuous pyrolysis carbonizing treatment method, including solid waste break process, heat supply, preposition processing, charing
Processing, gas treatment and gas utilize part；
(a) solid waste break process part：Solid waste is subjected to break process；
(b) heat supply part：One burner is set, the bocca of burner is passed through in a combustion chamber and obtains high-temperature flue gas；
(c) preposition process part：Solid waste after will be broken is inserted in preposition process chamber, introduces the high temperature of heat supply part
Flue gas heats the indoor solid waste of preposition processing by the way of the heating of outer thermal jacket, temperature during work in chuck
For 500-700 DEG C, 100-250 DEG C is heated in preposition process chamber；
(d) charing process part：Solid waste after preposition processing is sent into charing process room, introduces the height of heat supply part
Warm flue gas, heats the indoor solid waste of charing process by the way of the heating of outer thermal jacket, during work in chuck
Temperature is 700-900 DEG C, and charing process heating indoor is to 450-650 DEG C；Charing process room is oxygen debt or anaerobic state；
(e) air treatment section：The gas-phase product produced during preposition process part and charing process is collected, using water
The mode of spray is condensed, and obtains condensed fluid and on-condensible gas；
(f) gas utilizes part：On-condensible gas is introduced in the combustion chamber of heat supply part and is burnt as fuel of heat supply,
The on-condensible gas occurs oxidation reaction and obtains high-temperature flue gas in the combustion chamber, and the temperature of high-temperature flue gas is 700-900 DEG C；
(g) will be discharged after the indoor solid residue cooling of charing process, sealing postcooling preserves.
The outer thermal jacket of the preposition process part and charing process part outlet pressure by be separately provided one with
Control is adjusted in the air-duct adjusting device that corresponding outer thermal jacket outlet is connected so that at preposition process part and charing
The pressure managed in the outer thermal jacket of part is negative pressure.
The pipe is controlled by varying the pipeline flow diameter for the exhaust duct being connected with the air-duct adjusting device
The sectional area in road, i.e., when the circulation diameter of pipeline is become small, the gas flow passed through in its unit interval can reduce；It is on the contrary then
On the contrary, flowing into the flow velocity and flow of gas so as to adjust in the outer thermal jacket of preposition process part and charing process part, and tie
The heating load of combined burner and then the normal working temperature for ensureing preposition process chamber and charing process room.
The on-condensible gas occurs oxidation reaction and obtains high-temperature flue gas in the combustion chamber, is at preposition process part and charing
Reason part provides thermal energy.The ignition temperature of the on-condensible gas is 1000~1100 DEG C, realizes energy recycling.Before described
The flue gas of thermal jacket outlet discharge outside process part and charing process part is put, particularly, for the nitrogen oxidation contained in flue gas
Thing (the toxic gas such as NOx), bioxin row up to standard after air-duct adjusting device is purified by activated carbon adsorption and bag-type dust
Put.The burner is neat gas burner, biomass particle burner, oil burner, coal burner, and gas utilizes portion
In point, some components of on-condensible gas may not burn fully, and using burning, indoor burner provides auxiliary thermal source, promotees
On-condensible gas is fully burnt, while ensure the normal working temperature of combustion chamber.In in the present embodiment, the solid waste bag
Include at least one of mixture of spoil, feces of livestock and poultry, internal organ, useless feed and filoplume composition.
For the present invention in addition to farm's solid waste, other, which can carry out desiccation and the organic matter of charing, can be used as processing
Thing is handled by the set technique.
Embodiment two
Fig. 2 is the overall structure diagram of two farm's solid waste continuous pyrolysis carbonization processing device of embodiment.Such as Fig. 2
It is shown, a kind of farm's solid waste continuous pyrolysis carbonization processing device, including solid waste break process unit, combustion chamber 1,
Preprocessing unit, charing process unit, air processing unit and gas range site, the combustion chamber 1 set a burner
1a；As shown in figure 3, the preprocessing unit is external-heat drier 2, which is provided with drying machine chuck 21, dry
Machine chuck 21 is communicated by flue gas delivery pipe road 4 with the high-temperature flue gas outlet 1a of combustion chamber 1；As shown in figure 4, the charing process
Unit is external-heat retort 3, which is provided with retort chuck 31, and retort chuck 31 passes through flue gas delivery pipe road 4
It is connected with the high-temperature flue gas outlet 1a of combustion chamber 1；
The air processing unit includes fume collection pipeline 5, treating column 6, the gas vent 2a and retort of drying machine 2
3 gas vent 3a is connected by fume collection pipeline 5 with treating column 6 respectively, and treating column 6 is internally provided with spray thrower 61, its
Above the air inlet for the treatment of column 6, the gas-phase product produced in drying machine 2 is by its gas vent 2a through fume collection pipeline
5 are introduced in treating column 6 by the air inlet for the treatment of column 6, and the gas-phase product produced in retort 3 is by its gas vent 3a through flue gas
Collecting 5 introduce treating column 6 in, through spray thrower 61 spray condensation after obtain condensed fluid, after oil water separator realize oil,
Water separates；
Solid waste is sent into drying machine 2 by helical feed pipeline 8 by the solids inlet 2b of drying machine 2 in the present invention,
Discharge through its solid outlet 2c after desiccation in drying machine 2, and sent by helical feed pipeline 8 by 3 solids inlet 3b of retort
Enter in retort 3, the solid residue obtained after pyrolysis charring after the solid outlet 3c discharge coolings of retort 3 by sealing charing up for safekeeping
In residue container 9.
The gas range site includes fixed gas conduit 10, and fixed gas conduit 10 is equipped with coupled logical second and draws
Wind turbine 15, the gas outlet for the treatment of column 6 are connected by fixed gas conduit 10 with combustion chamber 1 respectively, and what is obtained in treating column 6 does not coagulate
Gas introduces combustion chamber 1 through fixed gas conduit 10 by its gas outlet by the second air-introduced machine 15 and burns, and on-condensible gas is firing
The high-temperature flue gas that oxidation reaction acquisition occurs in room 1 is burnt by flue gas delivery pipe road 4 through drying machine chuck 21 and retort chuck
31 imports are transmitted in drying machine chuck 21 and retort chuck 31, realize that combustion chamber 1 supplies drying machine 2 and retort 3 respectively
Heat.
The export pipeline 11 of the drying machine chuck 21 and retort chuck 31 be respectively provided with one be used for adjust it is corresponding go out
The air passage regulating valve 12 of mouth pressure, the export pipeline 11 of the air passage regulating valve 12 are respectively provided with an activated carbon adsorber 13, pass through work
Property charcoal adsorption tower 13 and drying machine chuck 21 and retort are pressed from both sides with the bag filter 14 that the activated carbon adsorber 13 is connected
The flue gas of the outlet of set 31 discharge carries out qualified discharge after purified treatment, meanwhile, the outlet of the bag filter 14 is provided with and it
The first air-introduced machine 7 being connected, as shown in figure 5, by adjust air passage regulating valve 12 air passage openings of sizes and with the air passage tune
The uninterrupted of the first air-introduced machine 7 that section valve 12 is connected, controls the pressure in drying machine chuck 21 and retort chuck 31 to be
Negative pressure, simple in structure, cost are low and easy to adjust.Wherein, air passage regulating valve 12 can be replaced by wind turbine, in drying machine chuck 21
Chilling tower 16 is respectively provided with the export pipeline 11 of retort chuck 31, which is located at before the wind turbine, passes through tune
The uninterrupted of the first air-introduced machine 7 and wind turbine is saved, it is negative pressure to control the pressure in drying machine chuck 21 and retort chuck 31.Institute
State and be additionally provided with the flue gas delivery pipe road 4 being connected with the import of drying machine chuck 21 for controlling 21 intake of drying machine chuck
Dilution mouth 4a, dilution mouth 4a be used for adjust enter drying machine chuck 21 in high-temperature flue gas temperature；At the same time, drying machine
2 and retort 3 in be both provided with temperature and pressure sensor so that pressure in drying machine chuck 21 and retort chuck 31 and
Temperature can individually, accurate control.
Claims (8)
1. a kind of farm's solid waste continuous pyrolysis carbonizing treatment method, including solid waste break process, heat supply, preposition place
Reason, charing process, gas treatment and gas utilize part, it is characterised in that：
(a) solid waste break process part：Farm's solid waste is subjected to break process；
(b) heat supply part：One burner is set, the bocca of burner is passed through in a combustion chamber and obtains high-temperature flue gas；
(c) preposition process part：Solid waste after will be broken is inserted in preposition process chamber, introduces the high-temperature flue gas of heat supply part
The preposition indoor solid waste of processing is heated by the way of the heating of outer thermal jacket, is heated to 100-200 DEG C；
(d) charing process part：Solid waste after preposition processing is sent into charing process room, introduces the high temperature cigarette of heat supply part
Gas, heats the indoor solid waste of charing process by the way of the heating of outer thermal jacket, is heated to 450-550 DEG C；Charcoal
Change process chamber is oxygen debt or anaerobic state；
(e) air treatment section：The gas-phase product produced during preposition process part and charing process is collected, using water spray
Mode condensed, obtain condensed fluid and on-condensible gas；
(f) gas utilizes part：On-condensible gas is introduced in the combustion chamber of heat supply part and is burnt as fuel of heat supply, this is not
Solidifying gas occurs oxidation reaction and obtains high-temperature flue gas in the combustion chamber；
(g) it will discharge, and recycled after the indoor solid residue cooling of charing process；
The pressure of the outer thermal jacket of the preposition process part and charing process part outlet by be separately provided one with it is opposite
Control is adjusted in the air-duct adjusting device that the outer thermal jacket outlet answered is connected, preposition process part and charing process part
Pressure in outer thermal jacket is negative pressure；
The intake of the outer thermal jacket of preposition process part passes through the dilution that is set on the flue gas delivery pipe road that is connected with its import
Mouth control.
A kind of 2. farm's solid waste continuous pyrolysis carbonizing treatment method as claimed in claim 1, it is characterised in that：It is described
The flue gas of thermal jacket outlet discharge is handled by activated carbon adsorption and bag-type dust outside preposition process part and charing process part
After discharge.
A kind of 3. farm's solid waste continuous pyrolysis carbonizing treatment method as claimed in claim 1, it is characterised in that：It is described
Solid waste includes at least one of mixture of spoil, feces of livestock and poultry, internal organ, useless feed and filoplume composition.
A kind of 4. farm's solid waste continuous pyrolysis carbonizing treatment method as claimed in claim 1, it is characterised in that：It is described
Burner is neat gas burner, biomass particle burner, oil burner, coal burner.
5. a kind of farm's solid waste continuous pyrolysis carbonization processing device, including solid waste break process unit, combustion chamber,
Preprocessing unit, charing process unit, air processing unit and gas range site, it is characterised in that：Further including right will
Seek a kind of farm's solid waste continuous pyrolysis carbonizing treatment method of 1-4 any one of them；
The solid waste break process unit, feeds solid waste into breaker and is crushed；
The combustion chamber sets a burner；
The preprocessing unit is external-heat drier, which is provided with drying machine chuck, and drying machine chuck passes through cigarette
Letter shoot road is communicated with the high-temperature flue gas outlet of combustion chamber；
The charing process unit is external-heat rotary carbide furnace, which is provided with rotary carbide furnace chuck, rotation
Retort chuck is connected by flue gas delivery pipe road with the high-temperature flue gas outlet of combustion chamber；
The air processing unit includes fume collection pipeline, treating column, and the gas vent of drying machine and rotary carbide furnace passes through
Fume collection pipeline is connected with treating column, and the gas-phase product produced in drying machine and rotary carbide furnace introduces treating column, through spray
Condensed fluid is obtained after leaching device spray condensation；
The gas range site includes fixed gas conduit, and the gas outlet for the treatment of column is connected by fixed gas conduit with combustion chamber
It is logical, the on-condensible gas obtained in treating column is introduced into combustion chamber, the high-temperature flue gas that combustion chamber produces is passed by flue gas delivery pipe road
Transport in drying machine chuck and rotary carbide furnace chuck；
The export pipeline of the drying machine chuck and rotary carbide furnace chuck is respectively provided with one and is used to adjust corresponding outlet pressure
Air passage regulating valve, pass through air passage regulating valve and the air-introduced machine being connected with the air passage regulating valve and control drying machine chuck and rotation
Pressure in retort chuck；
It is additionally provided with the flue gas delivery pipe road that import with drying machine chuck is connected for controlling drying machine chuck intake
Dilute mouth.
A kind of 6. farm's solid waste continuous pyrolysis carbonization processing device as claimed in claim 5, it is characterised in that：It is described
Coupled the second logical air-introduced machine is additionally provided with fixed gas conduit, using on-condensible gas introduce combustion chamber in as fuel of heat supply into
Row burning.
A kind of 7. farm's solid waste continuous pyrolysis carbonization processing device as claimed in claim 5, it is characterised in that：It is described
Coupled the second logical air-introduced machine is additionally provided with fixed gas conduit, using on-condensible gas introduce combustion chamber in as fuel of heat supply into
Row burning.
8. a kind of farm's solid waste continuous pyrolysis carbonization processing device as described in claim 5 to 7 is any, its feature exist
In：Further include the activated carbon adsorber for being purified to the flue gas of drying machine chuck and the discharge of rotary carbide furnace jacket outlet
And bag filter.
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| CN105219402A (en) * | 2015-10-19 | 2016-01-06 | 上海吉环科技有限公司 | A kind of full-automatic charring furnace for the treatment of ill domestic animal |
| CN107568107A (en) * | 2017-09-26 | 2018-01-12 | 邓玉平 | A kind of poultry manure processing transmission pyrolysis installation |
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