CN202272741U - Apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel - Google Patents
Apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel Download PDFInfo
- Publication number
- CN202272741U CN202272741U CN2011203715243U CN201120371524U CN202272741U CN 202272741 U CN202272741 U CN 202272741U CN 2011203715243 U CN2011203715243 U CN 2011203715243U CN 201120371524 U CN201120371524 U CN 201120371524U CN 202272741 U CN202272741 U CN 202272741U
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- converter
- biofuel
- activated carbon
- cylindrical shell
- gac
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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Abstract
The utility model relates to an apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel, which comprises a raw material feeding motor a, a raw material feeding motor b, a raw material feed inlet a, a raw material feed inlet b, a feed screw a, a feed screw b, a waste heat boiler a and a waste heat boiler b and is characterized by also comprising a converter furnace head a, a converter furnace head b, a converter furnace tail a, a converter furnace tail b, a converter drive motor a, a converter drive motor b, a roller underframe a, a roller underframe b, a roller device a and a roller device b. The apparatus has the advantages that the apparatus produces continuously, has stable quality, is easy to control, has a novel structure, is simple and convenient to operate, and has low infrastructure instrument, small equipment volume and reasonable design; the automatic control of the operation process of the integral apparatus for making the carbonization materials, drying the activated carbon, regenerating the powdered activated carbon and recovering the biodiesel can be realized; and the pollution of gas generated in the carbonizing process to the environment is reduced.
Description
Technical field
The utility model relates to a kind of carbonization of gac carbonized stock, the oven dry of wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon.
Background technology
Carbonization: the pattern of making the gac carbonized stock is a lot, and the method that the ground a heatable brick bed of gac carbonized stock manufacturing works employing both at home and abroad smouldered: be made up of several a heatable brick bed simply chamber of smouldering, locular wall is built with refractory brick; Gac carbonized stock raw material is put into the chamber of smouldering, and a heatable brick bed side door igniting on ground, heat is imported in the ground a heatable brick bed; Afterwards ground a heatable brick bed side door is lived with mudding; After carbonized stock was smouldered 3 days in the ground a heatable brick bed, manual work clawed, and on carbonized stock, sprinkled water and cool off.Owing to there is not cooling to put in place, possibly revive during kiln discharge, produce fire; Must be more than 8 hours in outdoor placement; Usually output is 3-4 ton/3 day, produces a large amount of biofuel during carbonization, does not have recovery system; Environment is abominable, carbonization is inhomogeneous, labour intensity is big, yield poorly, of low quality, cooling is bad, fixed carbon is low after the carbonization, dust is big, original workshop-based, contaminate environment.
Oven dry: the oven dry of traditional gac, wet gac stand as on the ground, is dried, dried through sunshine, natural wind, labour intensity is big, yield poorly, original workshop-based.
Powdered Activated Carbon regeneration: this project is domestic still to be blank, all used saturated Powdered Activated Carbon is used as incineration treatment of garbage.
Biofuel reclaims: make the field at gac, reclaim biodiesel technology in the smoke gas treatment process, do not see pertinent literature.
The utility model content
The purpose of the utility model provides a kind of carbonization of gac carbonized stock, the oven dry of wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon.
The technical scheme that the utility model adopts is:
A kind of carbonization of gac carbonized stock; The oven dry of wet gac; The regeneration of Powdered Activated Carbon and biofuel recovery system device; Comprise raw material charging motor a; Raw material charging motor b; Material inlet a; Material inlet b; Feed auger a; Feed auger b; Waste heat boiler a and waste heat boiler b; Also comprise converter burner a; Converter burner b; Converter stove tail a; Converter stove tail b; Converter driving motor b; Converter driving motor a; Roller underframe a; Roller underframe b; Roller devices a and roller devices b
Said converter burner a, converter stove tail a, converter driving motor a, roller underframe a and roller devices a are located on the basic a through pre-embedded bolt successively; Be provided with feed auger a in the said converter burner a; Have material inlet a on the said feed auger a, said feed auger a is through raw material charging motor a control; Said converter stove tail a lower end is provided with discharge port a, and said discharge port a lower end is provided with discharging water cooler a, and said discharging water cooler a bottom is provided with feed box a; Link to each other through converter cylindrical shell a between said converter burner a and the converter stove tail a, said converter cylindrical shell a tilts to be located in the roller a; Said converter driving motor a links to each other with converter cylindrical shell a through converter transmission mechanism a; Be provided with thermocouple temperature measuring apparatus a in the said converter cylindrical shell a; Said converter burner a links to each other with biofuel retrieving arrangement a, and said biofuel retrieving arrangement a links to each other with waste heat boiler a, and said waste heat boiler a links to each other with converter stove tail b through the waste heat pipeline, and said converter stove tail a end is provided with waste heat source;
Said converter burner b, converter stove tail b, converter driving motor b, roller underframe b and roller devices b are located on the basic b through pre-embedded bolt successively; Be provided with feed auger b in the said converter burner b; Have material inlet b on the said feed auger b, said feed auger b is through raw material charging motor b control; Said converter stove tail b lower end is provided with discharge port b, and said discharge port b lower end is provided with discharging water cooler b, and said discharging water cooler b bottom is provided with feed box b; Link to each other through converter cylindrical shell b between said converter burner b and the converter stove tail b, said converter cylindrical shell b tilts to be located in the roller b; Said converter driving motor b links to each other with converter cylindrical shell b through converter transmission mechanism b; Be provided with thermocouple temperature measuring apparatus b in the said converter cylindrical shell b, be provided with converter stove inner central tube in the said thermocouple temperature measuring apparatus b; Said converter burner b links to each other with biofuel retrieving arrangement b, and said biofuel retrieving arrangement b links to each other with waste heat boiler b, and said waste heat boiler b links to each other with water wash column, and said water wash column links to each other with exhaust fan, and said exhaust fan is provided with blowdown stack;
Said converter burner a links to each other with biofuel retrieving arrangement a one end through pipeline, and the said biofuel retrieving arrangement a the other end links to each other with pipeline waste heat boiler a, and said biofuel retrieving arrangement a bottom links to each other with the biofuel storage tank through liquid sealing pipe.
Through stove head seal device a sealing, seal through stove tail sealing device a between said converter stove tail a and the converter cylindrical shell a between said converter burner a and the converter cylindrical shell a.
Said raw material charging motor a, converter driving motor a and thermocouple temperature measuring apparatus a are connected with housing a through lead respectively.
Through stove head seal device b sealing, seal through stove tail sealing device b between said converter stove tail b and the converter cylindrical shell b between said converter burner b and the converter cylindrical shell b.
Said raw material charging motor b, converter driving motor b and thermocouple temperature measuring apparatus b are connected with housing b through lead respectively.
Have access opening a on the said converter cylindrical shell a.
Have access opening b on the said converter cylindrical shell b.
Said converter cylindrical shell a from converter burner a to 1-45 ° of converter stove tail a inclination, said converter cylindrical shell b from converter burner b to 1-45 ° of converter stove tail b inclination.
Said biofuel retrieving arrangement a and biofuel retrieving arrangement b are shell and tube heat exchanger, finned heat exchanger or plate-type heat exchanger.
The utility model has the advantages that: continuous production, steady quality, good control, device construction is novel, and is easy and simple to handle, the Infrastructure less investment, equipment volume is little, and is reasonable in design; The regeneration and the operating process of biofuel recovery system of whole manufacturing carbonized stock, gac oven dry, Powdered Activated Carbon can realize automatic control; The gas that has produced when having reduced carbonization when the regeneration of whole manufacturing carbonized stock, gac oven dry, Powdered Activated Carbon and biofuel recovery system regenerated carbon is to the pollution of environment; Reclaimed biofuel such as acetic acid, methyl alcohol and wood tar oil and burnt, reduced energy consumption, reduce pollution, practiced thrift the production run cost environment to the influential spent organic solvent of environment.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail.
Fig. 1 is the structural representation of the utility model.
Fig. 2 collects synoptic diagram for biofuel reclaims.
Wherein: 1, raw material charging motor a, 2, material inlet a, 3, feed auger a, 4, converter burner a, 5, stove head seal device a, 6, converter transmission mechanism a; 7, biofuel retrieving arrangement a, 8, roller a, 9, waste heat boiler a, 10, converter cylindrical shell a, 11, access opening a, 12, roller devices a; 13, stove tail sealing device a, 14, converter stove tail a, 15, discharge port a, 16, roller underframe a, 17, basic a, 18, discharging water cooler a; 19, feed box a, 20, thermocouple temperature measuring equipment a, 21, housing a, 22, converter driving motor a, 23, waste heat boiler b, 24, raw material charging motor b; 25, material inlet b, 26, biofuel retrieving arrangement b, 27, feed auger b, 28, converter burner b, 29, stove head seal device b, 30, converter transmission mechanism b; 31, roller b, 32, converter cylindrical shell b, 33, access opening b, 34, roller devices b, 35, stove tail sealing device b, 36, converter stove tail b; 37, waste heat pipeline, 38, discharge port b, 39, roller underframe b, 40, basic b, 41, discharging water cooler b, 42, feed box b; 43, converter stove inner central tube b, 44, housing b, 45, thermocouple temperature measuring equipment b, 46, converter driving motor b, 47, water wash column, 48, blowdown stack; 49, exhaust fan, 50, waste heat source, 51, pipeline, 52, liquid sealing pipe, 53, the biofuel storage tank.
Embodiment
Shown in Fig. 1-2; The oven dry of the carbonization of a kind of gac carbonized stock of the utility model, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon; Comprise raw material charging motor a1, raw material charging motor b24, material inlet a2, material inlet b25, feed auger a3, feed auger b27, waste heat boiler a9 and waste heat boiler b23; Also comprise converter burner a4, converter burner b28, converter stove tail a14, converter stove tail b36, converter driving motor b46, converter driving motor a22, roller underframe a16, roller underframe b39, roller devices a12 and roller devices b34; Converter burner a4, converter stove tail a14, converter driving motor a46, roller underframe a16 and roller devices a12 are located on the basic a17 through pre-embedded bolt successively; Be provided with feed auger a3 in the converter burner a4; Have material inlet a2 on the feed auger a3, feed auger a3 is through raw material charging motor a1 control; Converter stove tail a14 lower end is provided with discharge port a15, and discharge port a15 lower end is provided with discharging water cooler a18, and discharging water cooler a18 bottom is provided with feed box a19; Link to each other through converter cylindrical shell a10 between converter burner a4 and the converter stove tail a14; Seal through stove head seal device a5 between converter burner a4 and the converter cylindrical shell a10; Seal through stove tail sealing device a12 between converter stove tail a14 and the converter cylindrical shell a10; Converter cylindrical shell a10 tilts and to be located in the roller a8, converter cylindrical shell a10 from converter burner a4 to 1-45 ° of converter stove tail a14 inclination; Converter driving motor a22 links to each other with converter cylindrical shell a10 through converter transmission mechanism a5, has access opening a11 on the converter cylindrical shell a10; Be provided with thermocouple temperature measuring apparatus a20 in the converter cylindrical shell a10, raw material charging motor a1, converter driving motor a22 and thermocouple temperature measuring apparatus a20 are connected with housing a21 through lead respectively; Converter burner a4 links to each other with biofuel retrieving arrangement a7, and biofuel retrieving arrangement a7 links to each other with waste heat boiler a9, and waste heat boiler a9 links to each other with converter stove tail b36 through waste heat pipeline 37, and converter stove tail a14 end is provided with waste heat source 50; Converter burner b28, converter stove tail b36, converter driving motor b46, roller underframe b39 and roller devices b34 are located on the basic b40 through pre-embedded bolt successively; Be provided with feed auger b27 in the converter burner b28; Have material inlet b25 on the feed auger b27, feed auger b27 is through raw material charging motor b24 control; Converter stove tail b36 lower end is provided with discharge port b38, and discharge port b38 lower end is provided with discharging water cooler b41, and discharging water cooler b41 bottom is provided with feed box b42; Link to each other through converter cylindrical shell b32 between converter burner b28 and the converter stove tail b36, converter cylindrical shell b32 tilts to be located in the roller b31, converter cylindrical shell b32 from converter burner b28 to 1-45 ° of converter stove tail b36 inclination; Converter driving motor b46 links to each other with converter cylindrical shell b32 through converter transmission mechanism b30; Seal through stove head seal device b29 between converter burner b28 and the converter cylindrical shell b32; Through stove tail sealing device b35 sealing, have access opening b33 on the converter cylindrical shell b32 between converter stove tail b36 and the converter cylindrical shell b32; Be provided with thermocouple temperature measuring apparatus b45 in the converter cylindrical shell b32, be provided with converter stove inner central tube 43 in the thermocouple temperature measuring apparatus b45, raw material charging motor b24, converter driving motor b46 and thermocouple temperature measuring apparatus b44 are connected with housing b44 through lead respectively; Converter burner b28 links to each other with biofuel retrieving arrangement b26, and biofuel retrieving arrangement b26 links to each other with waste heat boiler b23, and waste heat boiler b23 links to each other with water wash column 47, and water wash column 47 links to each other with exhaust fan 49, and exhaust fan 49 is provided with blowdown stack 48; Converter burner a4 links to each other with biofuel retrieving arrangement a7 one end through pipeline 51; The biofuel retrieving arrangement a7 the other end links to each other with pipeline waste heat boiler a9; Biofuel retrieving arrangement a7 bottom links to each other with biofuel storage tank 53 through liquid sealing pipe 52, and biofuel retrieving arrangement a7 and biofuel retrieving arrangement b26 are shell and tube heat exchanger, finned heat exchanger or plate-type heat exchanger.
The utility model has the advantages that: continuous production, steady quality, good control, device construction is novel, and is easy and simple to handle, the Infrastructure less investment, equipment volume is little, and is reasonable in design; The regeneration and the operating process of biofuel recovery system of whole manufacturing carbonized stock, gac oven dry, Powdered Activated Carbon can realize automatic control; The gas that has produced when having reduced carbonization when the regeneration of whole manufacturing carbonized stock, gac oven dry, Powdered Activated Carbon and biofuel recovery system regenerated carbon is to the pollution of environment; Reclaimed biofuel such as acetic acid, methyl alcohol and wood tar oil and burnt, reduced energy consumption, reduce pollution, practiced thrift the production run cost environment to the influential spent organic solvent of environment.
Claims (9)
1. the carbonization of a gac carbonized stock; The oven dry of wet gac; The regeneration of Powdered Activated Carbon and biofuel recovery system device; Comprise raw material charging motor a; Raw material charging motor b; Material inlet a; Material inlet b; Feed auger a; Feed auger b; Waste heat boiler a and waste heat boiler b; It is characterized in that: also comprise converter burner a; Converter burner b; Converter stove tail a; Converter stove tail b; Converter driving motor b; Converter driving motor a; Roller underframe a; Roller underframe b; Roller devices a and roller devices b
Said converter burner a, converter stove tail a, converter driving motor a, roller underframe a and roller devices a are located on the basic a through pre-embedded bolt successively; Be provided with feed auger a in the said converter burner a; Have material inlet a on the said feed auger a, said feed auger a is through raw material charging motor a control; Said converter stove tail a lower end is provided with discharge port a, and said discharge port a lower end is provided with discharging water cooler a, and said discharging water cooler a bottom is provided with feed box a; Link to each other through converter cylindrical shell a between said converter burner a and the converter stove tail a, said converter cylindrical shell a tilts to be located in the roller a; Said converter driving motor a links to each other with converter cylindrical shell a through converter transmission mechanism a; Be provided with thermocouple temperature measuring apparatus a in the said converter cylindrical shell a; Said converter burner a links to each other with biofuel retrieving arrangement a, and said biofuel retrieving arrangement a links to each other with waste heat boiler a, and said waste heat boiler a links to each other with converter stove tail b through the waste heat pipeline, and said converter stove tail a end is provided with waste heat source;
Said converter burner b, converter stove tail b, converter driving motor b, roller underframe b and roller devices b are located on the basic b through pre-embedded bolt successively; Be provided with feed auger b in the said converter burner b; Have material inlet b on the said feed auger b, said feed auger b is through raw material charging motor b control; Said converter stove tail b lower end is provided with discharge port b, and said discharge port b lower end is provided with discharging water cooler b, and said discharging water cooler b bottom is provided with feed box b; Link to each other through converter cylindrical shell b between said converter burner b and the converter stove tail b, said converter cylindrical shell b tilts to be located in the roller b; Said converter driving motor b links to each other with converter cylindrical shell b through converter transmission mechanism b; Be provided with thermocouple temperature measuring apparatus b in the said converter cylindrical shell b, be provided with converter stove inner central tube in the said thermocouple temperature measuring apparatus b; Said converter burner b links to each other with biofuel retrieving arrangement b, and said biofuel retrieving arrangement b links to each other with waste heat boiler b, and said waste heat boiler b links to each other with water wash column, and said water wash column links to each other with exhaust fan, and said exhaust fan is provided with blowdown stack;
Said converter burner a links to each other with biofuel retrieving arrangement a one end through pipeline, and the said biofuel retrieving arrangement a the other end links to each other with pipeline waste heat boiler a, and said biofuel retrieving arrangement a bottom links to each other with the biofuel storage tank through liquid sealing pipe.
2. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon; It is characterized in that: through stove head seal device a sealing, seal through stove tail sealing device a between said converter stove tail a and the converter cylindrical shell a between said converter burner a and the converter cylindrical shell a.
3. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon, it is characterized in that: said raw material charging motor a, converter driving motor a and thermocouple temperature measuring apparatus a are connected with housing a through lead respectively.
4. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon; It is characterized in that: through stove head seal device b sealing, seal through stove tail sealing device b between said converter stove tail b and the converter cylindrical shell b between said converter burner b and the converter cylindrical shell b.
5. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon, it is characterized in that: said raw material charging motor b, converter driving motor b and thermocouple temperature measuring apparatus b are connected with housing b through lead respectively.
6. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon is characterized in that: have access opening a on the said converter cylindrical shell a.
7. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon is characterized in that: have access opening b on the said converter cylindrical shell b.
8. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon; It is characterized in that: said converter cylindrical shell a from converter burner a to 1-45 ° of converter stove tail a inclination, said converter cylindrical shell b from converter burner b to 1-45 ° of converter stove tail b inclination.
9. the oven dry of the carbonization of a kind of gac carbonized stock according to claim 1, wet gac, the regeneration and the biofuel recovery system device of Powdered Activated Carbon, it is characterized in that: said biofuel retrieving arrangement a and biofuel retrieving arrangement b are shell and tube heat exchanger, finned heat exchanger or plate-type heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203715243U CN202272741U (en) | 2011-09-28 | 2011-09-28 | Apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203715243U CN202272741U (en) | 2011-09-28 | 2011-09-28 | Apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202272741U true CN202272741U (en) | 2012-06-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203715243U Withdrawn - After Issue CN202272741U (en) | 2011-09-28 | 2011-09-28 | Apparatus for carbonizing activated carbon carbonization materials, drying wet activated carbon, regenerating powdered activated carbon and recovering biodiesel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202272741U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502615A (en) * | 2011-09-28 | 2012-06-20 | 南通滨海活性炭有限公司 | Equipment for carbonization of activated carbon carbonized material, drying of wet activated carbon, regeneration of powdery activated carbon and recovery of biological diesel oil and manufacturing method thereof |
-
2011
- 2011-09-28 CN CN2011203715243U patent/CN202272741U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502615A (en) * | 2011-09-28 | 2012-06-20 | 南通滨海活性炭有限公司 | Equipment for carbonization of activated carbon carbonized material, drying of wet activated carbon, regeneration of powdery activated carbon and recovery of biological diesel oil and manufacturing method thereof |
| CN102502615B (en) * | 2011-09-28 | 2013-05-08 | 南通滨海活性炭有限公司 | Equipment for carbonization of activated carbon carbonized material, drying of wet activated carbon, regeneration of powdery activated carbon and recovery of biological diesel oil and manufacturing method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20120613 Effective date of abandoning: 20130508 |
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| RGAV | Abandon patent right to avoid regrant |