CN2465054Y - High-temp. cracking furnace and recovery device for refuse harmless treatment - Google Patents
High-temp. cracking furnace and recovery device for refuse harmless treatment Download PDFInfo
- Publication number
- CN2465054Y CN2465054Y CN 01214023 CN01214023U CN2465054Y CN 2465054 Y CN2465054 Y CN 2465054Y CN 01214023 CN01214023 CN 01214023 CN 01214023 U CN01214023 U CN 01214023U CN 2465054 Y CN2465054 Y CN 2465054Y
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- Prior art keywords
- recover
- cracking furnace
- dryer
- water
- temperature cracking
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a high-temperature cracking furnace and recovery device for refuse harmless treatment, which is composed of the high-temperature cracking furnace and the recovery device. The cracking furnace is provided with a drying cylinder body (52) and a carbonization cylinder body (51), screws (10) and (45) are arranged on the drying cylinder body (52) and the carbonization cylinder body (51) respectively; a hot air inlet duct (8) are connected with a pulse drying machine cylinder body (5) and a chimney (9) respectively; the pulse drying machine cylinder body (5) is connected with a feeding device (47) and a separator cylinder body (41); dust removers (15) and (18), the recovery devices (21) (22) (53) and (54), a gas washing tower (25), an oil-gas separator (28) and a security device (32) are interconnected on the cracking furnace via pipelines. The high-temperature cracking furnace and recovery device for refuse harmless treatment with the advantage of low cost is a new device which integrates the recovery of carbon, oil, gas and acid, and is suitable for the treatment of combustible refuse.
Description
The utility model relates to a kind of novel environment friendly equipment of combustible garbage harmless treatment, particularly a kind of high-temperature cracking furnace of harmless treatment rubbish and retracting device.
The main method of disposal of refuse is in the prior art: 1, compost treatment (anaerobism, aerobic compost method and mechanically composting method).2, burning disposal (simple and easy burning or burning electricity generation).3, landfill disposal (tradition is banked up, reclaimed fields from the sea, sanitary landfills).4, other method: comprise garbage derivatived burning, catalyzing hydrolysis, anaerobic methane production, making construction material, compression packing, breeding earthworm and pyrolysismethod etc.
In these processing methods, incineration treatment of garbage speed is fast, subtract appearance well, and factory building takes up an area of few, but investment is big, the operating cost height, and the discharging flue gas pollutes atmosphere.Its capital cost height of garbage compost, managerial skills are strict.The landfill disposal floor space is big, the addressing difficulty.
The disposal of refuse of the pyrolytic technique of application is also arranged at present both at home and abroad, external-heating revolving stove as developments such as Japanese kobe steel institute, Germany, the fusion gasification burner of developments such as Frankfort of the thatch this city, Luxembourg of Japan, Germany, France, Florida, US also has various fluid beds, moving bed, because of fixed bed etc.Domestic also have a similar application, and the biomass circulating fluid bed wood powder vapourizing unit as Chinese Academy of Sciences Guangzhou Energy Research Institute's development utilizes fast fluidization technology and biological thermal decomposition vaporization technology, produces combustible gas through high temperature thermalization reaction.The technology of the city waste or used plastics being made raw material production styrene monomer of Guangzhou environmental resource pyrolytic technique that developmental research utilizes development.But these technology mostly are single greatly or aerogenesis or charcoal processing or carry oil at present, and complex process, involve great expense the millions of easily units of a set of equipment, up to ten million unit.
The purpose of this utility model is: high-temperature cracking furnace and retracting device that a kind of harmless treatment rubbish is provided; it is cheap; the new equipment that collection charcoal, oil, gas, sour one reclaim; can eliminate refuse pollution effectively and can therefrom reclaim useful resources again, the purpose of reach conservation of nature, protecting the ecological balance, turn waste into wealth.
Formation of the present utility model: form by high-temperature cracking furnace and retracting device, high-temperature cracking furnace is by upper furnace body (6), middle body of heater (4) and lower furnace body (5) are formed, be installed on the pyrolysis furnace support (49), drying cylinder body (52) is installed in joint portion at upper furnace body (6) and middle body of heater (4), go up installation drying oven spiral (10) in drying cylinder body (52), charing cylindrical shell (51) is installed in joint portion at middle body of heater (4) and lower furnace body (50), go up installation charing body of heater spiral (45) at charing cylindrical shell (51), powdered carbon discharger (43) is connected with charing cylindrical shell (51), go up installation vapor discharge pipe (7) and chimney (9) at upper furnace body (6), hot blast inlet tube (8) connects pulse drier body (5) and chimney (9) respectively, dryer charging reductor (48) is connected with pulse drier body (5) by dryer feeder (47), feeder main frame (44) is connected with drying cylinder body (52), on feeder main frame (44), be installed into glassware motor (11), dryer separator cylindrical shell (41) is connected with pulse drier body (5), goes up at dryer separator cylindrical shell (41) ventilation blower (12) is installed.
Pyrolysis furnace is connected with left-handed cyclone dust collectors (15) by mixture pipe (13), left-handed cyclone dust collectors (15) are connected with dextrorotation deduster (18) by deduster tube connector (17), go up installation condenser (19) at dextrorotation deduster (18), condenser water seal (38) is installed in below at condenser (19), go up installation condenser escape pipe (20) in condenser water seal (38), condenser escape pipe (20) is connected every formula recover (21) with water by pipeline, water is connected with iris type recover (22) by pipeline every formula recover (21), iris type recover (22) is connected every formula recover (53) with water by pipeline, water is connected with iris type recover (54) by pipeline every formula recover (53), iris type recover (54) is connected with aeration tower (25) by tracheae (24), aeration tower (25) is connected with gs-oil separator (28) by pipeline, gs-oil separator (28) is connected with water ring vacuum pump (34) by pipeline, water ring vacuum pump (34) is connected with safety device (32) by pipeline, goes up at safety device (32) gas discharge pipe (30) and appendix (31) are installed.
Go up installation shaft bearing (3) at charing cylindrical shell (51) and drying cylinder body (52), connected by chain (2) between the diaxon bearing, bearing block (3) is connected with reductor (1) by power transmission shaft.
In the below of dryer separator cylindrical shell (41) dryer star is installed and removes glassware (42), dryer star is removed glassware (42) and is connected except that material reductor (40) by power transmission shaft and dryer, goes up at the ventilation blower (12) of dryer separator cylindrical shell (41) top dryer vapor discharge pipe (14) is installed.
Filter (23) is installed in top at iris type recover (22) (54), every the below of formula recover (21) (53) and iris type recover (22) (54) recover oil-collecting water seal (37) is arranged at water.
Deduster radiation shield (16) is arranged in left-handed cyclone dust collectors (15), and deduster dust-exhausting port (39) is equipped with in the lower end.
Go up installation gas washing water-main (36) at aeration tower (25), go up at gas washing water-main (36) gas washing water pipe (26) is installed, go up at gas washing water pipe (26) gas washing shower nozzle (27) is installed.
Separator oil pooling cylinder (35) is installed in below at gs-oil separator (28), goes up at safety device (32) the bright meter of liquid (33) is installed, and goes up at gas discharge pipe (30) spark arrester (29) is installed.
Compared with the prior art, the utility model not only can the nondegradable plastic products of cracking, as polybag, plastic film, polystyrene, mess-tin and scrap rubber raw material and discarded object, simultaneously to disposable direct combustible species, produce charcoal powder, wood tar, pyrolkigneous liquid, xylon gas as conversions such as the root bars of forest harvesting residue, the broken branches and fallen leaves, hill weeds, straw, wood chip, husk and crops and combustiblerefuses.
This equipment does not have waste gas, waste water, waste sludge discharge, non-secondary pollution.Do not need any additives, rate of recovery height, floor space is little, and is stable, easy operating, equipment manufacturing cost is cheap, and overall economic efficiency is good.
This equipment not only can be handled agricultural wastes innoxiously, and the combustible gas that produces when handling can be that farmers' family supplies gas through pipeline except that the required energy of supply equipment itself, the solution domestic gas.Handle the powdered carbon that straw reclaims, potassium content is very high, can make high-quality potash fertilizer and directly use.The acetic acid that reclaims is through being mixed with plant nutriment regulator, not only has very high fertilizer efficiency, and contaminated land not, product does not have residue, can not influence healthyly, and quality of vegetable is good, delicious, the weakness that does not have the chemical fertilizer planting vegetable, acetic acid itself has very strong insecticidal action simultaneously, so can play the effect that agricultural fertile agricultural chemicals is killed two birds with one stone simultaneously.The wood tar that reclaims can obtain products such as creosote, anti-poly-agent, floatation frother, wood pitch through reprocessing, these chemical products are essential raw material of industry such as medicine, synthetic rubber, metallurgy, can make the base starting material of boats and ships specialized paint, also can produce senior chemical industry base starting material such as interior ketone, cresols and therefrom decompose and extract light-weight fuel oil, have very high economic worth.
Accompanying drawing is the utility model structural representation.
Embodiment of the present utility model: as shown in drawings, pyrolysis furnace is made up of upper furnace body (6), middle body of heater (4) and lower furnace body (50), is installed on the pyrolysis furnace support (49).Drying cylinder body (52) is installed in joint portion at upper furnace body (6) and middle body of heater (4), go up installation drying oven spiral (10) and bearing block (3) in drying cylinder body (52), charing cylindrical shell (51) is installed in joint portion at middle body of heater (4) and lower furnace body (50), go up installation charing body of heater spiral (45) and bearing block (3) at charing cylindrical shell (51), on the sprocket wheel on the diaxon bearing chain (2) is arranged up and down, bearing block (3) is connected with reductor (1) by power transmission shaft.Powdered carbon discharger (43) is connected with charing cylindrical shell (51).
Go up installation vapor discharge pipe (7) and chimney (9) at upper furnace body (6), hot blast inlet tube (8) connects pulse drier body (5) and chimney (9) respectively.Dryer charging reductor (48) is connected with pulse drier body (5) by dryer feeder (47), and feeder main frame (44) is connected with drying cylinder body (52), is installed into glassware motor (11) on feeder main body (44).Dryer separator cylindrical shell (41) is connected with pulse drier body (5), in dryer separator cylindrical shell (41) top ventilation blower (12) is installed, dryer vapor discharge pipe (14) is installed on it, the below is installed dryer star and is removed glassware (42), and is connected except that material reductor (40) by power transmission shaft and dryer.
Pyrolysis furnace is connected with left-handed cyclone dust collectors (15) by mixture pipe (13), deduster radiation shield (16) is arranged in left-handed cyclone dust collectors (15), left-handed cyclone dust collectors (15) are connected with dextrorotation deduster (18) by deduster tube connector (17), go up installation condenser (19) at dextrorotation deduster (18), condenser water seal (38) is installed in below at condenser (19), there is deduster dust-exhausting port (39) below at left-handed cyclone dust collectors (15) and dextrorotation deduster (18), in the top of condenser water seal (38) condenser escape pipe (20) is installed.
Condenser escape pipe (20) is connected every formula recover (21) with water by pipeline, water is connected with iris type recover (22) by pipeline every formula recover (21), iris type recover (22) is connected every formula recover (53) with water by pipeline, water is connected with iris type recover (54) by pipeline every formula recover (53), filter (23) is installed in top at iris type recover (22) (54), every the below of formula recover (21) (53) and iris type recover (22) (54) recover oil-collecting water seal (37) is arranged at water.
Dividing plate recover (54) is connected with aeration tower (25) by tracheae (24), and aeration tower (25) is gone up gas washing water-main (36) is installed, and goes up at gas washing water-main (36) gas washing water pipe (26) is installed, and goes up at gas washing water pipe (26) gas washing shower nozzle (27) is installed.Aeration tower (25) is connected with gs-oil separator (28) by pipeline, the below of gs-oil separator (28) is separator oil pooling cylinder (35), the top is connected with water ring vacuum pump (34) by pipeline, water ring vacuum pump (34) is connected with safety device (32) by pipeline, go up installation gas discharge pipe (30), appendix (31) and the bright meter of liquid (33) at safety device (32), go up at gas discharge pipe (30) spark arrester (29) is installed.
Claims (7)
1, a kind of high-temperature cracking furnace of harmless treatment rubbish and retracting device, form by high-temperature cracking furnace and retracting device, it is characterized in that: high-temperature cracking furnace is by upper furnace body (6), middle body of heater (4) and lower furnace body (50) are formed, be installed on the pyrolysis furnace support (49), drying cylinder body (52) is installed in joint portion at upper furnace body (6) and middle body of heater (4), go up installation drying oven spiral (10) in drying cylinder body (52), charing cylindrical shell (51) is installed in joint portion at middle body of heater (4) and lower furnace body (50), go up installation charing body of heater spiral (45) at charing cylindrical shell (51), powdered carbon discharger (43) is connected with charing cylindrical shell (51), go up installation vapor discharge pipe (7) and chimney (9) at upper furnace body (6), hot blast inlet tube (8) connects pulse drier body (5) and chimney (9) respectively, dryer charging reductor (48) is connected with pulse drier body (5) by dryer feeder (47), feeder main frame (44) is connected with drying cylinder body (52), on feeder main frame (44), be installed into glassware motor (11), dryer separator cylindrical shell (41) is connected with pulse drier body (5), goes up at dryer separator cylindrical shell (41) ventilation blower (12) is installed;
Pyrolysis furnace is connected with left-handed cyclone dust collectors (15) by mixture pipe (13), left-handed cyclone dust collectors (15) are connected with dextrorotation deduster (18) by deduster tube connector (17), go up installation condenser (19) at dextrorotation deduster (18), condenser water seal (38) is installed in below at condenser (19), go up installation condenser escape pipe (20) in condenser water seal (38), condenser escape pipe (20) is connected every formula recover (21) with water by pipeline, water is connected with iris type recover (22) by pipeline every formula recover (21), iris type recover (22) is connected every formula recover (53) with water by pipeline, water is connected with iris type recover (54) by pipeline every formula recover (53), iris type recover (54) is connected with aeration tower (25) by tracheae (24), aeration tower (25) is connected with gs-oil separator (28) by pipeline, gs-oil separator (28) is connected with water ring vacuum pump (34) by pipeline, water ring vacuum pump (34) is connected with safety device (32) by pipeline, goes up at safety device (32) gas discharge pipe (30) and appendix (31) are installed.
2, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device, it is characterized in that: go up installation shaft bearing (3) at charing cylindrical shell (51) and drying cylinder body (52), connected by chain (2) between the diaxon bearing, bearing block (3) is connected with reductor (1) by power transmission shaft.
3, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device, it is characterized in that: in the below of dryer separator cylindrical shell (41) dryer star is installed and removes glassware (42), dryer star is removed glassware (42) and is connected except that material reductor (40) by power transmission shaft and dryer, goes up at the ventilation blower (12) of dryer separator cylindrical shell (41) top dryer vapor discharge pipe (14) is installed.
4, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device, it is characterized in that: filter (23) is installed in the top at iris type recover (22) (54), every the below of formula recover (21) (53) and iris type recover (22) (54) recover oil-collecting water seal (37) is arranged at water.
5, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device is characterized in that: deduster radiation shield (16) is arranged in left-handed cyclone dust collectors (15), and deduster dust-exhausting port (39) is equipped with in the lower end.
6, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device, it is characterized in that: go up at aeration tower (25) gas washing water-main (36) is installed, go up installation gas washing water pipe (26) at gas washing water-main (36), go up at gas washing water pipe (26) gas washing shower nozzle (27) is installed.
7, the high-temperature cracking furnace of harmless treatment rubbish according to claim 1 and retracting device, it is characterized in that: separator oil pooling cylinder (35) is installed in the below at gs-oil separator (28), go up the installation bright meter of liquid (33) at safety device (32), go up at gas discharge pipe (30) spark arrester (29) is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01214023 CN2465054Y (en) | 2001-01-27 | 2001-01-27 | High-temp. cracking furnace and recovery device for refuse harmless treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01214023 CN2465054Y (en) | 2001-01-27 | 2001-01-27 | High-temp. cracking furnace and recovery device for refuse harmless treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2465054Y true CN2465054Y (en) | 2001-12-12 |
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ID=33632867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01214023 Expired - Fee Related CN2465054Y (en) | 2001-01-27 | 2001-01-27 | High-temp. cracking furnace and recovery device for refuse harmless treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2465054Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100449207C (en) * | 2006-07-24 | 2009-01-07 | 王玉志 | Environmental protection, energy sources recovery type garbage treatment equipment |
| CN1864877B (en) * | 2006-05-22 | 2010-05-12 | 和云杉 | Garbage disposal unit and method thereof |
| CN102338556A (en) * | 2010-07-20 | 2012-02-01 | 来安县隆华摩擦材料有限公司 | Gasoline recovering and drying device used in process of machining clutch facing |
| CN102607034A (en) * | 2011-08-10 | 2012-07-25 | 唐荣太 | Device for garbage incineration and energy and fertilizer recovery |
| TWI454643B (en) * | 2009-12-25 | 2014-10-01 | ||
| CN105713670A (en) * | 2016-03-21 | 2016-06-29 | 安徽未名生物环保有限公司 | Refuse disposal system |
-
2001
- 2001-01-27 CN CN 01214023 patent/CN2465054Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1864877B (en) * | 2006-05-22 | 2010-05-12 | 和云杉 | Garbage disposal unit and method thereof |
| CN100449207C (en) * | 2006-07-24 | 2009-01-07 | 王玉志 | Environmental protection, energy sources recovery type garbage treatment equipment |
| TWI454643B (en) * | 2009-12-25 | 2014-10-01 | ||
| CN102338556A (en) * | 2010-07-20 | 2012-02-01 | 来安县隆华摩擦材料有限公司 | Gasoline recovering and drying device used in process of machining clutch facing |
| CN102607034A (en) * | 2011-08-10 | 2012-07-25 | 唐荣太 | Device for garbage incineration and energy and fertilizer recovery |
| CN102607034B (en) * | 2011-08-10 | 2014-09-10 | 唐荣太 | Device for garbage incineration and energy and fertilizer recovery |
| CN105713670A (en) * | 2016-03-21 | 2016-06-29 | 安徽未名生物环保有限公司 | Refuse disposal system |
| CN105713670B (en) * | 2016-03-21 | 2018-07-20 | 安徽未名生物环保有限公司 | A kind of refuse disposal system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |