CN205603520U - Domestic waste dry distillation conversion processing system - Google Patents
Domestic waste dry distillation conversion processing system Download PDFInfo
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- CN205603520U CN205603520U CN201620356228.9U CN201620356228U CN205603520U CN 205603520 U CN205603520 U CN 205603520U CN 201620356228 U CN201620356228 U CN 201620356228U CN 205603520 U CN205603520 U CN 205603520U
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Abstract
The utility model relates to a domestic waste dry distillation conversion processing system, domestic waste dry distillation conversion processing system, including vacuum feed arrangement, reaction unit, recovery unit and gas collection circulating device, vacuum feed arrangement, reaction unit and recovery unit communicate in proper order, and vacuum feed arrangement includes pan feeding jar, first storage tank and second storage tank, the automatically controlled valve of second intercommunication, the export of second storage tank and reaction unit's import intercommunication are passed through through first automatically controlled valve intercommunication, the export of first storage tank and the import of second storage tank to the export of pan feeding jar and the import of first storage tank, still include vacuum apparatus and the actuating system that is used for driving vacuum apparatus, vacuum apparatus and first storage tank intercommunication. The beneficial effects of the utility model are that: vacuum feed arrangement has guaranteed that entire system reacts under the oxygen -free environment, do not produce poisonous, harmful gas, has avoided the secondary pollution to the environment.
Description
Technical field
This utility model relates to technical field of waste treatment, particularly relates to house refuse dry distilling conversion process system.
Background technology
Existing technology of garbage disposal mainly have compost, fill, burn, waste recovery etc..In garbage disposal routine techniques, composting technology is difficult to control the quality of composting material, and the workload of fly eradication deodorization is relatively big, and the fermentation period of compost is longer；Landfill waste can take substantial amounts of soil, and is easy to contaminated land and subsoil water；It is obvious that burning disposal has reduced training, and innoxious thoroughly occupation of land amount is little, and recycling residual heat is low, but produces substantial amounts of harmful gas, causes the secondary pollution of environment.Along with continuous attention to utilization of resources both at home and abroad, improving constantly of environmental requirement, how to strengthen effectively utilizing, avoid the secondary pollution of environment particularly important the resource.
Utility model content
This utility model provides one way of life rubbish dry distilling conversion process system, vacuum feeder ensure that whole system is reacted under oxygen-free environment, do not produces poisonous, harmful gas, it is to avoid the secondary pollution to environment.
The technical scheme that this utility model is used is:
House refuse dry distilling conversion process system, including vacuum feeder, reaction unit, retracting device and collection and confinement of gases circulating device；Described vacuum feeder, described reaction unit and described retracting device are sequentially communicated, and described vacuum feeder includes into batch can, the first storage tank and the second storage tank；Described enter batch can outlet connected by the first electrically-controlled valve with the import of described first storage tank, the outlet of described first storage tank is connected by the second electrically-controlled valve with the import of described second storage tank, the outlet of described second storage tank and the inlet communication of described reaction unit；
Also including vacuum equipment and for driving the drive system of described vacuum equipment, described vacuum equipment connects with described first storage tank.
Further, described collection and confinement of gases circulating device connects with the circulation of described reaction unit.
Further, the volume of described second storage tank is more than the volume of described first storage tank.
Further, described reaction unit includes drying unit and dry distillation reactor device；The import of the described drying unit import as described reaction unit and the outlet of described second storage tank, the outlet of described drying unit and the inlet communication of described dry distillation reactor device, the air inlet of described drying unit is connected by described collection and confinement of gases circulating device with the air vent of described dry distillation reactor device, the air vent of described drying unit connects with described retracting device, and the outlet of described dry distillation reactor device connects with described retracting device；
Also include that frequency heating device, described frequency heating device use with described dry distillation reactor matched with devices.
Further, described drying unit includes the first spiral propeller；Described first spiral propeller is arranged on the inside of described drying unit, and can be in the inner rotation of described drying unit, for being forced into the house refuse of described drying unit；
Described dry distillation reactor device includes the second spiral propeller；Described second spiral propeller is arranged on the inside of described dry distillation reactor device, and can be in the inner rotation of described dry distillation reactor device, for being forced into the house refuse of described dry distillation reactor device；
Described frequency heating device uses Segmented heating mode.
Further, described retracting device includes transporter, gas concentration unit and solid recovery unit；The import of described transporter and the outlet of described reaction unit, the import of described gas concentration unit and the first outlet of described transporter, the import of described solid recovery unit and the second outlet of described transporter, described gas concentration unit connects with the air vent of described drying unit.
Further, described transporter includes the 3rd spiral propeller；Described 3rd spiral propeller is arranged on the inside of described transporter, and can be in the inner rotation of described transporter, for being forced into the house refuse of described transporter；
Described gas concentration unit includes the coal gasification reaction device being sequentially communicated, multistage chiller, purifier and gas compressing apparatus；Being provided with pipeline dust remover between described coal gasification reaction device and described multistage chiller, described multistage chiller connects with the air vent of described drying unit.
Further, described multistage chiller includes one-level cooler and secondary coolers, the import of described one-level cooler is connected with described pipeline dust remover, described reaction unit respectively by valve, the outlet of described one-level cooler and the inlet communication of described secondary coolers；
Described purifier includes oil water separator, carbonization gas depurator and adsorber；Described oil water separator connects with the sewage draining exit of described one-level cooler and the sewage draining exit of described secondary coolers respectively, the import of described carbonization gas depurator and the outlet of described secondary coolers, the outlet of described carbonization gas depurator and the inlet communication of described adsorber, the bottom of described carbonization gas depurator is provided with automatic pollution discharge mouth；
Described gas compressing apparatus includes surge tank, air accumulator and compressor bank, the import of described surge tank and the outlet of described adsorber, and the outlet of described surge tank is connected by described compressor bank with the import of described air accumulator.
Further, described vacuum equipment is connected by check valve with described first storage tank.
Further, including multiple reaction unit groups, described vacuum feeder can be to reaction unit group conveying house refuse at least one described, any one of reaction unit group includes at least one or more described reaction unit, and described retracting device can reclaim gas and the solid product that any one of reaction unit generates.
The beneficial effects of the utility model:
1, the technical solution of the utility model is used, rubbish dry distilling in the case of anaerobic can be allowed to process, produce imflammable gas, oil, charcoal, imflammable gas is fully circulated, cool down, separate, compress, form stable pressure gas source for generating set generating, achieve recycling of material, turn waste into wealth, saved the energy.
2, vacuum equipment and the first storage tank are connected by check valve, it is ensured that the rubbish after the air of extraction does not refluxes and ensures evacuation just enters reaction unit.By the first electrically-controlled valve and the synergy of the second electrically-controlled valve, the first storage tank is carried out evacuation by vacuum equipment, it is ensured that whole system is reacted under oxygen-free environment.
3, the volume of the second storage tank is more than the volume of the first storage tank, it is ensured that can continuous feed and operation in reaction unit.
4, the water vapour produced during dry distillation reactor, imflammable gas, coke gas etc. are collected by collection and confinement of gases circulating device, and be delivered in reaction unit, rubbish in drying unit is dried preheating, preliminary fission reaction occurs, reduce the temperature of carbonization gas simultaneously, reduce the energy of dry distilling, reach the purpose of UTILIZATION OF VESIDUAL HEAT IN.
5, retort process uses frequency heating device heating, and frequency heating device uses Segmented heating mode, it is ensured that in dry distilling pipe, temperature can reach 1100 DEG C in 25min.
6, high-temperature gas can be landed vertically to 450 DEG C by one-level cooler from 1000 DEG C, and high-temperature gas can be landed vertically to about 40 DEG C by secondary coolers from 450 DEG C, it is achieved that the purpose cooling high-temperature gas.
7, the moisture in gas, tar, impurity etc. are separated by carbonization gas depurator, equipped with automatic draining device bottom carbonization gas depurator, Oil in circulating gas and water are separated；Adsorber is by the nitrogen oxides contained in gas and sulfur compounds adsorption.
8, through coal gasification reaction device, charcoal being converted into imflammable gas, the surge tank before the imflammable gas entrance compressor of supercooling, purification, by being stored in after compressor bank pressurized treatment in fuel gas air accumulator, stable output is for electrical power generators.Imflammable gas is processed by compressor boost, can greatly reduce the storage area of imflammable gas.Simultaneously can provide reliable and stable source of the gas for generating set, it is ensured that the normal operation of generating set.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model one embodiment.
nullWherein: 1. vacuum feeder、11. enter batch can、12. first storage tanks、13. second storage tanks、14. vacuum equipments、15. first electrically-controlled valve、16. second electrically-controlled valve、17. check valves、2. reaction unit、21. drying units、211. first spiral propellers、22. dry distillation reactor devices、221. second spiral propellers、3. retracting device、31. transporters、311. the 3rd spiral propellers、32. gas concentration units、321. coal gasification reaction devices、322. multistage chillers、3221. one-level cooler、3222. secondary coolers、323. purifier、3231. oil water separator、3232. carbonization gas depurator、3233. adsorber、324. gas compressing apparatus、3241. surge tank、3242. air accumulator、3243. compressor bank、325. pipeline dust remover、33. solid recovery units、4. collection and confinement of gases circulating device、5. frequency heating device.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing of the present utility model, provide the description of specific embodiment, but not as to any restriction of the present utility model.
Seeing Fig. 1, house refuse dry distilling conversion process system, including vacuum feeder 1, reaction unit 2, retracting device 3 and collection and confinement of gases circulating device 4；Vacuum feeder 1, reaction unit 2 and retracting device 3 are sequentially communicated, and collection and confinement of gases circulating device 4 connects with reaction unit 2 circulation.Vacuum feeder 1 for being delivered to reaction unit 2 by house refuse, and house refuse carries out dry distillation reactor in reaction unit 2, generates gas and solid product, and gas and solid product can enter recovering mechanism from rubbish reaction mechanism and recycle.House refuse first passes through sorting, the operation pretreatment such as broken, enters back in vacuum feeder 1, and entering reaction unit 2 via feed arrangement carries out dry distillation reactor, is then reclaimed the gas and solid product generated by recovering mechanism.
Also include positive-pressure explosion-proof ventilated control system, control system is connected with vacuum feeder 1, reaction unit 2, retracting device 3 and collection and confinement of gases circulating device 4, it is possible to control vacuum feeder 1, reaction unit 2, retracting device 3 and the running status of collection and confinement of gases circulating device 4.Control system includes photographic head, electrical control cabinet and terminal.Equipped with temperature detecting resistance on dry distillation reactor device 22, drying unit 21 parts, monitor the temperature in retort process at any time and control effectively.
Connection between vacuum feeder 1, reaction unit 2 and retracting device 3 three is all to seal, so that it is guaranteed that there is no oxygen in rubbish reaction mechanism, house refuse is made to carry out chemical reaction in the absence of oxygen, avoid generating harmful gas, so may further ensure that the gas of generation is nontoxic, will not contaminated air.
Wherein, vacuum feeder 1 includes into batch can the 11, first storage tank 12 and the second storage tank 13；The import of the outlet and the first storage tank 12 that enter batch can 11 is connected by the first electrically-controlled valve 15, and the outlet of the first storage tank 12 is connected by the second electrically-controlled valve 16 with the import of the second storage tank 13, the outlet of the second storage tank 13 and the inlet communication of reaction unit 2；Also including vacuum equipment 14 and for driving the drive system of vacuum equipment, vacuum equipment 14 is connected by check valve 17 with the first storage tank 12.First electrically-controlled valve the 15, second electrically-controlled valve 16, check valve 17 electrically connect with DCS operating system respectively.The volume of the second storage tank 13 is more than the volume of the first storage tank 12, it is ensured that can continuous feed and operation in reaction unit 2.Vacuum equipment 14 is vacuum pump.
When adding house refuse in vacuum feeder 1, first the second electrically-controlled valve 16 is closed, then house refuse is added in the first storage tank 12 by entering batch can 11, and close the first electrically-controlled valve 15, start check valve 17 and vacuum equipment 14 so that for vacuum state in the first storage tank 12；Closing check valve 17 and vacuum equipment 14, open the second electrically-controlled valve 16, house refuse is entered reaction unit 2 by the second storage tank 13.Ensure house refuse in the absence of oxygen, kinetics, dry distillation reactor occur in dry distillation reactor still, thus generates steam, combustible gas, oil gas and solid-state charcoal etc., the clean energy resource that can reuse.
Wherein, reaction unit 2 includes drying unit 21 and dry distillation reactor device 22；The import of drying unit 21 import as described reaction unit 2 and the outlet of the second storage tank 13, the outlet of drying unit 21 and the inlet communication of dry distillation reactor device 22, the air inlet of drying unit 21 is connected by collection and confinement of gases circulating device 4 with the air vent of dry distillation reactor device 22, the air vent of drying unit 21 connects with retracting device 3, and the outlet of dry distillation reactor device 22 connects with retracting device 3；Also include that frequency heating device 5, frequency heating device 5 support the use with dry distillation reactor device 22.
The water vapour produced during dry distillation reactor, imflammable gas, coke gas etc. are collected by collection and confinement of gases circulating device 4, and be delivered in reaction unit 2, rubbish in drying unit 21 is dried preheating, preliminary fission reaction occurs, reduce the temperature of carbonization gas simultaneously, reduce the energy of dry distilling, reach the purpose of UTILIZATION OF VESIDUAL HEAT IN.
The Main Function of frequency heating device 5 is to bring it about dry distillation reactor to house refuse heating, and frequency heating device 5 can be arranged on the inside of reaction unit 2, it is also possible to is arranged on the outside of reaction unit 2；As the preferred scheme of one, frequency heating device 5 is set in the outside of reaction unit 2, so can not only play the effect of heating, but also it can be avoided that frequency heating device 5 is arranged on inside, affect dry distillation reactor and the dry distillation reactor corrosion to frequency heating device 5 of house refuse.Reaction unit 2 is additionally provided with heat-insulation layer.
Drying unit 21 includes the first spiral propeller 211 and for the drive system driving the first spiral propeller to rotate；First spiral propeller 211 is arranged on the inside of drying unit 21, and can be in the inner rotation of drying unit 21, for being forced into the house refuse of drying unit 21；Dry distillation reactor device 22 includes the second spiral propeller 221 and for the drive system driving the second spiral propeller to rotate；Second spiral propeller 221 is arranged on the inside of dry distillation reactor device 22, and can be in the inner rotation of dry distillation reactor device 22, for being forced into the house refuse of dry distillation reactor device 22；Frequency heating device 5 uses Three-section type heating mode, is set the firing rate of each section of frequency heating device respectively by control system, and the firing rate of first paragraph heating is 50 DEG C/min, and heat time heating time is 12min；The firing rate of second segment heating is 40 DEG C/min, and heat time heating time is 8min；The firing rate of the 3rd section of heating is 36 DEG C/min, and heat time heating time is 5min；Thus guarantee, in 25min, material is heated to 1100 DEG C, the power of frequency heating device 5 is 250Kw, and the frequency of frequency heating device 5 is between 300KHz to 3000KHz.
The Main Function of the first spiral propeller 211 is the outlet that the house refuse entered in drying unit 21 is delivered to drying unit 21 from the import of drying unit 21；The Main Function of the second spiral propeller 221 is the outlet that the house refuse entered in dry distillation reactor device 22 device is delivered to dry distillation reactor device 22 from the import of dry distillation reactor device 22, in the process, the gas that dry distillation reactor produces enters collection and confinement of gases circulating device 4 from dry distillation reactor device 22 air vent, enter back into drying unit 21, and all gas and solid-state charcoal all enter recovering mechanism, recycle.
Wherein, retracting device 3 includes transporter 31, gas concentration unit 32 and solid recovery unit 33；The import of transporter 31 and the outlet of reaction unit 2, the import of gas concentration unit 32 and the first outlet of transporter 31, the import of solid recovery unit 33 and the second outlet of transporter 31, gas concentration unit 32 connects with the air vent of drying unit 21.
When needs solid carbon, solid carbon is entered solid recovery unit 33 by the second outlet, stores by being transported to storage reservoir by solid product conveyer；When needs gas products, solid carbon carries out reacting solid carbon is converted into imflammable gas in being entered gas concentration unit 32 by the first outlet, surge tank 3241 before the imflammable gas entrance compressor of supercooling, purification, by being stored in fuel gas air accumulator 3242 after compressor bank 3243 pressurized treatment, stable output is for electrical power generators.
Transporter 31 includes the 3rd spiral propeller 311 and for the drive system driving the 3rd spiral propeller to rotate；3rd spiral propeller 311 is arranged on the inside of transporter 31, and can be in the inner rotation of transporter 31, for being forced into the house refuse of transporter 31.
The Main Function of the 3rd spiral propeller 311 is the outlet that the house refuse entered in transporter 31 is delivered to transporter 31 from the import of transporter 31.
Gas concentration unit 32 includes coal gasification reaction device 321, multistage chiller 322, purifier 323 and the gas compressing apparatus 324 being sequentially communicated；Being provided with pipeline dust remover 325 between coal gasification reaction device 321 and multistage chiller 322, multistage chiller 322 connects with the air vent of drying unit 21；Solid recovery unit 33 also includes heat exchanger, and heat exchanger is set in the outside of shipping unit, is used for cooling down solid product.
Multistage chiller 322 includes one-level cooler 3221 and secondary coolers 3222, the import of one-level cooler 3221 is connected with pipeline dust remover 325, reaction unit 2 respectively by valve, the outlet of one-level cooler 3221 and the inlet communication of secondary coolers 3222；Purifier 323 includes oil water separator 3231, carbonization gas depurator 3232 and adsorber 3233；Oil water separator 3231 connects with the sewage draining exit of one-level cooler 3221 and the sewage draining exit of secondary coolers 3222 respectively, the import of carbonization gas depurator 3232 and the outlet of secondary coolers 3222, the outlet of carbonization gas depurator 3232 and the inlet communication of adsorber 3233, the bottom of carbonization gas depurator 3232 is provided with automatic pollution discharge mouth；Gas compressing apparatus 324 includes surge tank 3241, air accumulator 3242 and compressor bank 3243, the import of surge tank 3241 and the outlet of adsorber 3233, and the outlet of surge tank 3241 is connected by compressor bank 3243 with the import of air accumulator 3242.
Through the imflammable gas entrance surge tank 3241 of supercooling, purification, being stored in fuel gas air accumulator 3242 by compressor boost after being processed, stable output is for electrical power generators.Compressor bank 3243 uses intermittent operation mode, automatically turns on when cluster engine preposition air accumulator 3242 hypotony.It is automatically switched off when pressure reaches 0.4Mp.
Imflammable gas passes through compressor bank 3243 pressurized treatment, can greatly reduce the storage area of imflammable gas.Simultaneously can provide reliable and stable source of the gas for generating set, it is ensured that the normal operation of generating set.
High-temperature gas can be landed vertically to 450 DEG C by one-level cooler 3221 from 1000 DEG C, and high-temperature gas can be landed vertically to about 40 DEG C by secondary coolers 3222 from 450 DEG C, it is achieved that the purpose cooling high-temperature gas.
Wherein, any one drive system includes frequency conversion explosion proof motor, converter and chain wheel set, the output shaft of frequency conversion explosion proof motor is connected with the power shaft of converter, the output shaft of converter is connected with the power shaft of chain wheel set, the output shaft of chain wheel set is connected with the power shaft of spiral propeller, thus realizes the motion of band dynamic spiral propeller.
The Main Function of drive system is to provide power to spiral propeller, so that spiral propeller motion, house refuse, intermediate products and solid-state charcoal move automatically in the inside of dry distillation reactor device 22, it is not necessary to human assistance, improve the treatment effeciency of raw material rubbish.
Wherein, including multiple reaction unit groups, described vacuum feeder 1 can be to reaction unit group conveying house refuse at least one described, any one of reaction unit group includes at least one or more described reaction unit 2, and described retracting device 3 can reclaim gas and the solid product that any one of reaction unit generates.And in parallel between each reaction unit 2, the most each reaction unit 2 all can be with independent operating；Use multiple reaction unit 2 can accelerate the treatment effeciency of rubbish, save the time.And each reaction unit 2 all connects with vacuum feeder 1 and retracting device 3.
This utility model is not limited to above-mentioned preferred forms; those skilled in the art can draw other various forms of products under enlightenment of the present utility model; no matter but in its shape or structure, make any change; every have same as the present application or akin technical scheme, within all falling within protection domain of the present utility model.
Claims (10)
1. house refuse dry distilling conversion process system, including vacuum feeder (1), reaction unit
(2), retracting device (3) and collection and confinement of gases circulating device (4)；Described vacuum feeder (1),
Described reaction unit (2) and described retracting device (3) are sequentially communicated,
It is characterized in that: described vacuum feeder (1) includes into batch can (11), the first storage tank
(12) and the second storage tank (13)；Described enter the outlet of batch can (11) and described first storage tank
(12) import is connected by the first electrically-controlled valve (15), the outlet of described first storage tank (12)
Import with described second storage tank (13) is connected by the second electrically-controlled valve (16), described second storage
The outlet of batch can (13) and the inlet communication of described reaction unit (2)；
Also include vacuum equipment (14), described vacuum equipment (14) and described first storage tank (12)
Connection.
House refuse dry distilling conversion process system the most according to claim 1, it is characterised in that:
Described collection and confinement of gases circulating device (4) connects with described reaction unit (2) circulation.
House refuse dry distilling conversion process system the most according to claim 1, it is characterised in that:
The volume of described second storage tank (13) is more than the volume of described first storage tank (12).
House refuse dry distilling conversion process system the most according to claim 2, it is characterised in that:
Described reaction unit (2) includes drying unit (21) and dry distillation reactor device (22)；Described drying
The import of device (21) is as import and described second storage tank (13) of described reaction unit (2)
Outlet, the outlet of described drying unit (21) and entering of described dry distillation reactor device (22)
Mouth connection, the air inlet of described drying unit (21) and the aerofluxus of described dry distillation reactor device (22)
Mouthful by described collection and confinement of gases circulating device (4) connect, the air vent of described drying unit (21) with
Described retracting device (3) connects, the outlet of described dry distillation reactor device (22) and described retracting device
(3) connection；
Also include frequency heating device (5), described frequency heating device (5) and described dry distillation reactor
Device (22) supports the use.
House refuse dry distilling conversion process system the most according to claim 4, it is characterised in that:
Described drying unit (21) includes the first spiral propeller (211)；Described first spiral propeller (211)
It is arranged on the inside of described drying unit (21), and can be in the inside of described drying unit (21)
Rotate, be used for being forced into the house refuse of described drying unit (21)；
Described dry distillation reactor device (22) includes the second spiral propeller (221)；Described second spiral
Propeller (221) is arranged on the inside of described dry distillation reactor device (22), and can be in described dry distilling
The inner rotation of reaction unit (22), is used for being forced into the life of described dry distillation reactor device (22)
Rubbish alive；
Described frequency heating device (5) uses Segmented heating mode.
House refuse dry distilling conversion process system the most according to claim 4, it is characterised in that:
Described retracting device (3) includes that transporter (31), gas concentration unit (32) and solid reclaim
Device (33)；The import of described transporter (31) and the outlet of described reaction unit (2),
The import of described gas concentration unit (32) and the first outlet of described transporter (31),
The import of described solid recovery unit (33) and the second outlet of described transporter (31),
Described gas concentration unit (32) connects with the air vent of described drying unit (21).
House refuse dry distilling conversion process system the most according to claim 6, it is characterised in that:
Described transporter (31) includes the 3rd spiral propeller (311)；Described 3rd spiral propeller (311)
It is arranged on the inside of described transporter (31), and can be in the inside of described transporter (31)
Rotate, be used for being forced into the house refuse of described transporter (31)；
Coal gasification reaction device (321) that described gas concentration unit (32) includes being sequentially communicated, many
Level chiller (322), purifier (323) and gas compressing apparatus (324)；Described coal gas
Change and be provided with pipeline dust remover (325) between reaction unit (321) and described multistage chiller (322),
Described multistage chiller (322) connects with the air vent of described drying unit (21).
House refuse dry distilling conversion process system the most according to claim 7, it is characterised in that:
Described multistage chiller (322) includes one-level cooler (3221) and secondary coolers (3222),
The import of described one-level cooler (3221) by valve respectively with described pipeline dust remover (325),
Described reaction unit (2) connects, the outlet of described one-level cooler (3221) and described two grades of coolings
The inlet communication of device (3222)；
Described purifier (323) includes oil water separator (3231), carbonization gas depurator (3232)
With adsorber (3233)；Described oil water separator (3231) respectively with described one-level cooler (3221)
Sewage draining exit connect with the sewage draining exit of described secondary coolers (3222), described carbonization gas depurator
(3232) import and the outlet of described secondary coolers (3222), described carbonization gas purifies
The outlet of device (3232) and the inlet communication of described adsorber (3233), described carbonization gas depurator
(3232) bottom is provided with automatic pollution discharge mouth；
Described gas compressing apparatus (324) includes surge tank (3241), air accumulator (3242) and pressure
Contracting unit (3243), the import of described surge tank (3241) and going out of described adsorber (3233)
Mouth connection, institute is passed through in the outlet of described surge tank (3241) and the import of described air accumulator (3242)
State compressor bank (3243) connection.
House refuse dry distilling conversion process system the most according to claim 1, it is characterised in that:
Described vacuum equipment (14) is connected by check valve (17) with described first storage tank (12).
10. according to the house refuse dry distilling conversion process system described in claim 1～9 any one,
It is characterized in that: including multiple reaction unit group, described vacuum feeder (1) can be at least one
Individual described reaction unit group conveying house refuse, any one of reaction unit group includes at least one
Or multiple described reaction unit (2), described retracting device (3) can reclaim any one of instead
Answer gas and solid product that device generates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620356228.9U CN205603520U (en) | 2016-04-25 | 2016-04-25 | Domestic waste dry distillation conversion processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620356228.9U CN205603520U (en) | 2016-04-25 | 2016-04-25 | Domestic waste dry distillation conversion processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205603520U true CN205603520U (en) | 2016-09-28 |
Family
ID=56970977
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620356228.9U Active CN205603520U (en) | 2016-04-25 | 2016-04-25 | Domestic waste dry distillation conversion processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205603520U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105694926A (en) * | 2016-04-25 | 2016-06-22 | 何勇 | Destructive distillation conversion treatment system for household refuse |
| CN108707467A (en) * | 2018-04-11 | 2018-10-26 | 杭州电子科技大学 | Solid waste thermal splitting system |
-
2016
- 2016-04-25 CN CN201620356228.9U patent/CN205603520U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105694926A (en) * | 2016-04-25 | 2016-06-22 | 何勇 | Destructive distillation conversion treatment system for household refuse |
| CN108707467A (en) * | 2018-04-11 | 2018-10-26 | 杭州电子科技大学 | Solid waste thermal splitting system |
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