CN201002017Y - Combustion fuel oil type particulate active carbon regenerating turning kiln - Google Patents
Combustion fuel oil type particulate active carbon regenerating turning kiln Download PDFInfo
- Publication number
- CN201002017Y CN201002017Y CNU2007200931935U CN200720093193U CN201002017Y CN 201002017 Y CN201002017 Y CN 201002017Y CN U2007200931935 U CNU2007200931935 U CN U2007200931935U CN 200720093193 U CN200720093193 U CN 200720093193U CN 201002017 Y CN201002017 Y CN 201002017Y
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- furnace body
- inner furnace
- rotation inner
- active carbon
- heater
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Abstract
The utility model relates to a fuel-type particle active carbon reproduction rotary kiln which belongs to an active carbon reproduction device. The structure of the device is: the spiral feeder machine, the furnace head and the furnace end are separately positioned on the base plate, and a carbon collecting scoop is positioned at the bottom of the furnace end; the external fire-standing heat insulation furnace body is positioned on the base plate by the supporting roller and a plurality of fuel burner are separately positioned on the external fire-standing heat insulation furnace body which has a rotating internal furnace body; the rotating internal furnace body is connected with the electric motor through the big gear and the electric motor is positioned on the base plate through the stander; the activation device is connected with the tail of the rotating internal furnace body; the tail gas injection discharge device is arranged on the head of the furnace. The advantages of the utility model are: simple structure, convenient operation, high degree of automation, stable temperature of the active carbon reproduction, good activity of the reproduced active carbon, high heat efficiency, making good use of the heat energy, low cost and very practical.
Description
Technical field
The utility model relates to a kind of active carbon reclaim equiment, particularly a kind of fuel oil type granular activated carbon regeneration rotary kiln.
Background technology
At present, the granular active carbon reclaim equiment, particularly the rotary kiln type reclaim equiment adopts the silicon carbon rod more, and the thermal efficiency is low, the power consumption height, easy burn-out need be improved.
The utility model content
The purpose of this utility model is to provide a kind of fuel oil type granular activated carbon regeneration rotary kiln, has solved low, the problems such as power consumption is high, easy burn-out of the rotary kiln type reclaim equiment thermal efficiency commonly used.
The technical solution of the utility model is: comprise screw(-type) feeder, burner, rotation inner furnace body, oil burner, outside fire resistant heat preserving body of heater, stove tail, activating apparatus, tail gas jetting type discharger and base, wherein, screw(-type) feeder, burner and stove tail are separately fixed on the base, and this stove tail bottom is provided with carbon collecting bucket; Outside fire resistant heat preserving body of heater is fixed on the base by support roller and support thereof; Oil burner is arranged on the outside fire resistant heat preserving body of heater, this fire resistant heat preserving body of heater inside, outside is provided with the rotation inner furnace body, a plurality of oil burners are protected between body and the rotation inner furnace body to insulation provides the active carbon regenerative process required heat energy, burned flame sprays between thermal insulation furnace body and the rotating furnace body, make active carbon under blade that tilts and body of heater gyroscopic action, flow into the stove tail by inlet, finished charcoal; Activating apparatus is opened the activated water that magnet valve feeds certain flow by automatic control box control active carbon when the body of heater afterbody reaches uniform temperature, finished active carbon activation process; This rotation inner furnace body links to each other with motor by gear wheel; Activating apparatus links to each other with the afterbody of rotation inner furnace body, and tail gas jetting type discharger is arranged on the burner, and the steam that makes the beginning dry run produce is effectively discharged; Outside fire resistant heat preserving body of heater separates with the rotation inner furnace body of steel, be provided with blade in this rotation inner furnace body, in the rotation inner furnace body, rotation inner furnace body inclination certain angle effectively guarantees active carbon and hot blast contact area to blade along the equidistant installation of stove inwall circumferencial direction in the rotation.
Advantage of the present utility model is: simple in structure, easy to operate, and the automaticity height, the active carbon regeneration temperature is stable, and high temperature is long in the burner hearth time of staying, and regeneration back active carbon activity is good; With the fuel oil is thermal source, the combustion heat value height, and the rotation inner furnace body is established blade, has effectively increased active carbon and body of heater thermocontact area, thermal efficiency height; Heat energy utilization is good, and energy consumption is low, and is practical.
Description of drawings:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the A-A cross-sectional schematic of Fig. 1.
The specific embodiment:
As shown in Figure 1, the utility model comprises screw(-type) feeder 1, burner 2, rotation inner furnace body 3, three oil burners 4,5,6, outside fire resistant heat preserving body of heater 7, stove tail 8, activating apparatus 9, tail gas jetting type discharger 10 and bases 11, wherein, screw(-type) feeder 1, burner 2 and stove tail 8 are separately fixed on the base 11, and these stove tail 8 bottoms are provided with carbon collecting bucket 81; Outside fire resistant heat preserving body of heater 7 is fixed on the base 11 by support roller 71 and support 72 thereof; Three oil burners 4,5,6 are separately positioned on the outside fire resistant heat preserving body of heater 7, and these fire resistant heat preserving body of heater 7 inside, outside are provided with rotation inner furnace body 3, and this rotation inner furnace body 3 links to each other with motor 32 by gear wheel 31, and motor fixes by support 33 and base 11; Activating apparatus 9 links to each other with the afterbody of rotation inner furnace body 3, and tail gas jetting type discharger 10 is arranged on the burner, and the steam that makes the beginning dry run produce is effectively got rid of; Screw(-type) feeder 1 will treat that by burner regenerated carbon sends in the rotation in the stove 3, by a plurality of burners 4,5,6 provide heat energy between outside fire resistant heat preserving body of heater 7 and rotation inner furnace body 3, a plurality of burners complement each other and guarantee the stable of regenerative process fire box temperature, burned flame sprays between outside fire resistant heat preserving body of heater 7 and the interior stove interior 3 of rotation, it is temperature required to reach each section by automatic temperature-adjusting control, automatically the drying of active carbon regeneration is finished in control, high temperature carbonization and activate three processes, final charcoal is got rid of from stove tail 8, guaranteed the regenerability of active carbon, the process Automatic Control, the regeneration temperature precise control;
Outside fire resistant heat preserving body of heater 7 separates with the rotation inner furnace body 3 of steel, and the burning between is finished; Be provided with blade 34 in this rotation inner furnace body, blade 34 is along rotating the equidistant installation of inner furnace body inwall circumferencial direction in the rotation inner furnace body, rotation inner furnace body inclination certain angle, active carbon and hot blast contact area had both effectively been guaranteed, make active carbon again under the gyroscopic action of blade 34 that tilts and rotation inner furnace body 3, flow to stove tail 8 by inlet, finished charcoal; Burner is done thermal source with heavy oil or diesel oil, and thermal efficiency height is easy to control; Activating apparatus 9 makes active carbon open the activated water that magnetic valve feeds certain flow when the body of heater afterbody reaches uniform temperature by automatic control box control, thereby finishes the activation process of charcoal; Automatic control box control automatically advances charcoal, goes out charcoal, by temperature survey transmission control, and the unlatching of control burner, thereby the temperature of control burner hearth, it is temperature required in each stage to reach active carbon.
During use, after fire box temperature preheating uniform temperature, screw(-type) feeder 1 will be with certain speed by burner 2, will treat that regenerated carbon sends into rotation inner furnace body 3, rotation inner furnace body 3 is with speed rotation very slowly, and the calory burning of regulating multistage burner 4,5,6 makes it to mate with production capacity; Because rotation inner furnace body 3 inclination certain angles, active carbon can slowly flow to tail end from front end; Active carbon is a drying stage when just entering rotation inner furnace body 3, the water evaporates of absorption in the activated carbon granule, also volatilization thereupon of the lower boiling organic matter of part simultaneously, enter the roasting stage then, or title carbonation stage, the grain charcoal is heated and is warming up to 150~700 ℃, different organic matters raise with temperature, respectively with volatilization, decompose, carbonization, the form of oxidation, eliminate from the matrix of active carbon, this process is the stage of longer duration, enter activation stage subsequently, organic matter has the considerable part carbide to remain in the activated carbon capillary behind high temperature cabonization, this moment, carbide needed to carry out gasification reaction with oxidizing gas such as water vapours, made residual carbide be gasificated into CO at higher temperature
2, gases such as CO; Make micropore surface obtain cleaning, recover its absorption property, thereby finish the regeneration of charcoal; Activation process betides the end of rotation inner furnace body 3, flows into stove tail 8 then, discharges from carbon outlet port; Drying, roasting, activation three processes of regeneration provide heat energy by a plurality of burners 4,5,6, control each section temperature by automatic control box.
Claims (2)
1, a kind of fuel oil type granular activated carbon regeneration rotary kiln, it is characterized in that: comprise screw(-type) feeder, burner, rotation inner furnace body, oil burner, outside fire resistant heat preserving body of heater, stove tail, activating apparatus, tail gas jetting type discharger and base, wherein, screw(-type) feeder, burner and stove tail are separately fixed on the base, and this stove tail bottom is provided with carbon collecting bucket; Outside fire resistant heat preserving body of heater is fixed on the base by support roller and support thereof; A plurality of oil burners are separately positioned on the outside fire resistant heat preserving body of heater, and this fire resistant heat preserving body of heater inside, outside is provided with the rotation inner furnace body, and this rotation inner furnace body links to each other with motor by gear wheel, and motor fixes by support and base; Activating apparatus links to each other with the afterbody of rotation inner furnace body, and tail gas jetting type discharger is arranged on the burner.
2, fuel oil type granular activated carbon regeneration rotary kiln according to claim 1; it is characterized in that: said outside fire resistant heat preserving body of heater separates with the rotation inner furnace body of steel; be provided with blade in this rotation inner furnace body; blade in the rotation inner furnace body, rotates inner furnace body inclination certain angle along the equidistant installation of rotation inner furnace body inwall circumferencial direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200931935U CN201002017Y (en) | 2007-01-22 | 2007-01-22 | Combustion fuel oil type particulate active carbon regenerating turning kiln |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200931935U CN201002017Y (en) | 2007-01-22 | 2007-01-22 | Combustion fuel oil type particulate active carbon regenerating turning kiln |
Publications (1)
Publication Number | Publication Date |
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CN201002017Y true CN201002017Y (en) | 2008-01-09 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CNU2007200931935U Expired - Lifetime CN201002017Y (en) | 2007-01-22 | 2007-01-22 | Combustion fuel oil type particulate active carbon regenerating turning kiln |
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CN (1) | CN201002017Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104307500A (en) * | 2014-10-10 | 2015-01-28 | 程振国 | Granular activated carbon regenerating rotary kiln |
-
2007
- 2007-01-22 CN CNU2007200931935U patent/CN201002017Y/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104307500A (en) * | 2014-10-10 | 2015-01-28 | 程振国 | Granular activated carbon regenerating rotary kiln |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term |
Granted publication date: 20080109 |
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EXPY | Termination of patent right or utility model |