CN202193770U - Processing device for biomass sludge synthetic carbon - Google Patents

Processing device for biomass sludge synthetic carbon Download PDF

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Publication number
CN202193770U
CN202193770U CN 201120260199 CN201120260199U CN202193770U CN 202193770 U CN202193770 U CN 202193770U CN 201120260199 CN201120260199 CN 201120260199 CN 201120260199 U CN201120260199 U CN 201120260199U CN 202193770 U CN202193770 U CN 202193770U
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CN
China
Prior art keywords
dryer
inlet
belt conveyor
heater
roller
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Withdrawn - After Issue
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CN 201120260199
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Chinese (zh)
Inventor
赵顺华
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CHONGQING CHUANGNENG REGENERATION RESOURCE Co Ltd
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CHONGQING CHUANGNENG REGENERATION RESOURCE Co Ltd
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Priority to CN 201120260199 priority Critical patent/CN202193770U/en
Application granted granted Critical
Publication of CN202193770U publication Critical patent/CN202193770U/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Treatment Of Sludge (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The utility model discloses a processing device for biomass sludge synthetic carbon. The outlets of a first crushing machine (1) and a sludge tank (3) are connected to the inlet of the a mixer (2) through a belt conveyer; the mixer (2) is connected with the inlet of a first dryer (6) through the belt conveyer; the outlet of the first dryer (6) is connected with the inlet of a cooling machine (4) through the belt conveyer; the outlet of the cooling machine (4) is connected with the inlet of a second dryer (8) through the belt conveyer; two combustion furnaces (7) arranged respectively below the first dryer (6) and the second dryer (8) supply hot air flow for the first dryer (6) and the second dryer (8); the outlet of the second dryer (8) is connected with the inlet of a second crushing machine (10) through the belt conveyer; and the outlet of the second crushing machine (10) is connected with the inlet of a roller former (5). The processing device for biomass sludge synthetic carbon can produce biomass sludge synthetic carbon continuously, adopts mechanization operation completely, and greatly improves production efficiency, and meanwhile, as per production requirements, the efficiency of the combustion furnaces and the roller former is improved.

Description

The processing unit (plant) of the synthetic charcoal of biomass sludge
Technical field
The utility model belongs to the processing unit (plant) of biomass fuel, specifically, relates to the device of the synthetic carbon of a kind of process for processing biomass sludge.
Background technology
Get into 21 century, the mankind are faced with economic growth fast and energy shortage, environment protection triple burden.Particularly the energy and environment problem is the central topic that is related to the national economy Sustainable development that each state of the world today all faces.In order to alleviate and progressively to address this problem.The renewable new forms of energy project of active development of organizing is all strengthened in countries in the world.
Present most of sewage work in all parts of the country all can produce large batch of mud every day, and (mud is meant solid, semi-solid state and the liquid gurry of disposing of sewage and being produced here; Contain a large amount of organism, heavy metal and germ etc.); Sludge treatment is mainly taked the method for landfill, fertilising and burning, because the water cut of mud high (65%-80%) contains deleterious heavy metal again; Landfill disposal not only occupies a large amount of soils, and the severe contamination groundwater resource; As fertilizer sources uses, and also can cause secondary pollution, the agricultural product security that causes because of fertilising with influence the HUMAN HEALTH incident and happen occasionally, become the very important factor that influences agriculture prodn, health of the masses and social stability.
Bring burning electricity generation after also having part producer with the mud oven dry at present, the water cut of mud is big, density is big, viscosity is big, and generally all is powdery, semi-solid attitude; If take the secondary mechanical dehydration, dehydrating effect is poor, uses if directly get into the drying plant oven dry; Energy consumption is high, and cost is high, and the mud of approximately drying one ton need spend 200 yuan; And yield poorly, can't form batch process.
The biomass wide material sources, the various stalks of agriculture waste, the various crotch of forestry depleted, bark, tree root, wood working depleted wood chip, sawdust etc.The various wood chips of industrial gaseous waste, sawdust, packing material, Chinese medicine slag, the various templates of urban construction depleted, the annual branch of pruning of urban afforestation, various mashed furniture of depleted etc. in the life.Application at present is that raw material is processed as the synthetic charcoal of biomass sludge with it through series of process with biomass, mud; Become a kind of reasonable energy; But present process for processing all is artificial, workshop-based discontinuous production; Yield poorly, efficient is low, cost is high, be badly in need of the production line that a kind of continuity produces and carry out Fully-mechanized production.
The utility model content
For solving above technical problem, the purpose of the utility model be to provide a kind of continuously, the device of the synthetic charcoal of Mechanized Processing biomass sludge.
The utility model purpose is achieved in that the processing unit (plant) of the synthetic charcoal of a kind of biomass sludge; Comprise kibbler, mixer (2), sludge tank (3), dryer, cooler (4), roller head machine (5); Its key is: said first kibbler (1) all is connected mixer (2) inlet through belt conveyor with sludge tank (6) outlet; Said mixer (2) connects first dryer (6) inlet through belt conveyor; This first dryer (6) outlet connects cooler (4) inlet through belt conveyor; Said cooler (4) outlet connects the inlet of second dryer (8) through belt conveyor; Said first dryer (6) and second dryer (8) provide hot gas flow by the roasting kiln that issues setting (7), and said second dryer (8) outlet connects second kibbler (10) inlet through belt conveyor, and this second kibbler (10) outlet connects roller head machine (5) inlet through belt conveyor.
Biological material is introduced into first kibbler (1) and pulverizes; Get into mud in the sludge tank (3) again and be introduced into first dryer (6) oven dry after mixer (2) mixes, after getting into cooler (4), get into second dryer (8) oven dry once more then; Make on the one hand become loose, good permeability, density of mud diminish; And biological material can also absorb the moisture in the mud, and then mixture is dried, and can improve drying efficiency; Reduce the combustion efficacy that the biological on the other hand material of oven dry cost has promoted mud, improved the thermal value of the synthetic charcoal of mud.
Above-mentioned roasting kiln (7) comprises body of heater (7-1); Said body of heater (7-1) upper end is connected with flue (7-1a); Said body of heater (7-1) top is provided with the air duct (7-2) of coiling; This air duct (7-2) passes from body of heater (7-1) sidewall and is connected with blower fan (7-3), and said air duct (7-2) the other end stretches out floss hole along flue (7-1a).Simultaneously to the gas heating in air duct (7-2) and the air duct, the gas in the air duct was by the quick continual drying plant of sending into of blower fan when the coal of stove internal combustion etc. added warm air.Heat major part in the stove all is utilized fast to be seen off, from the furnace body wall dispersed heat seldom, has improved the HU of body of heater.
Above-mentioned air duct (2) is the serpentine coiling from down to up at body of heater (1).The area that this design absorbs heat is bigger.
Above-mentioned roller head machine (5); Comprise worktable (5-1), discharge bucket (5-2), roll extrusion storehouse (5-3); Said discharge bucket (5-2) is positioned under the roll extrusion storehouse (5-3); Rotation axis (5-3a) has been stretched at center, said roll extrusion storehouse (5-3), and this rotation axis (5-3a) zygomorphy is provided with roller (5-3b), and this bottom, roll extrusion storehouse (5-3) is that center ring is to having discharge hole (5-3c) with rotation axis (5-3a); It is characterized in that: said roller (5-3b) is taper, and this roller (5-3b) outer end diameter is little to be increased near rotation axis (5-3a) diameter gradually.Because this kind structure, the gap between roller (5-3b) outer end and the discharge port becomes greatly gradually, and roller (5-3b) is in the process of roll extrusion, and material can be endlessly from the outer end entering of roller, and evenly extruding is come out.
Above-mentioned discharge hole (5-3c) is that the center surrounds at least three circles with rotation axis (5-3a).Improve the speed of discharging greatly, improved the efficient of roll forming.
Beneficial effect: the synthetic charcoal of biomass sludge is produced in the utility model serialization fast, is Fully-mechanized operation, has improved production effect greatly, need carry out improved efficiency to roasting kiln and roller head machine owing to what produce simultaneously.The synthetic charcoal of the biomass sludge that processes has effectively solved the moisture height of mud, density is big, ventilation property is poor, viscosity is big, oven dry is difficult, the high difficult problem of oven dry cost; Biological material has promoted the combustion efficacy of mud with after mud cooperates, and has improved the thermal value that biomass sludge synthesizes charcoal, and combustionproperty is good.
Description of drawings
Fig. 1 connects synoptic diagram for the utility model;
Fig. 2 is a roasting kiln structural representation in the utility model;
Fig. 3 is a roller head machine structural representation in the utility model;
Fig. 4 is that the A of Fig. 3 is to view.
Embodiment
Embodiment
As shown in Figure 1; The processing unit (plant) of the synthetic charcoal of a kind of biomass sludge; Mainly form by kibbler, mixer 2, sludge tank 3, dryer, cooler 4, roller head machine 5; First kibbler 1 all is connected mixer 2 inlets through belt conveyor with sludge tank 6 outlets, and said mixer 2 connects first dryer, 6 inlets through belt conveyor, and these first dryer, 6 outlets connect cooler 4 inlets through belt conveyor; Said cooler 4 outlets connect the inlet of second dryer 8 through belt conveyor; Said first dryer 6 and second dryer 8 provide hot gas flow by the roasting kiln that issues setting 7, and 8 outlets of said second dryer connect second kibbler, 10 inlets through belt conveyor, and these second kibbler, 10 outlets connect roller head machine 5 inlets through belt conveyor.
Further find out by Fig. 2; Said roasting kiln 7 comprises body of heater 7-1; Said body of heater 7-1 upper end is connected with flue 7-1a; Said body of heater 7-1 top is provided with the air duct 7-2 of coiling, and this air duct 7-2 passes from body of heater 7-1 sidewall and is connected with blower fan 7-3, and the said air duct 7-2 the other end stretches out floss hole along flue 7-1a.Said air duct 2 is the serpentine coiling from down to up at body of heater 1.
Further by Fig. 3, the said roller head machine 5 of Fig. 4; Comprise worktable 5-1, discharge bucket 5-2, roll extrusion storehouse 5-3; Said discharge bucket 5-2 is positioned under the 5-3 of roll extrusion storehouse; Rotation axis 5-3a has been stretched at 5-3 center, said roll extrusion storehouse, and this rotation axis 5-3a zygomorphy is provided with roller 5-3b, and 5-3 bottom in this roll extrusion storehouse is that center ring is to having discharge hole 5-3c with rotation axis 5-3a; It is characterized in that: said roller 5-3b is taper, and this roller 5-3b outer end diameter is little to be increased near rotation axis 5-3a diameter gradually.Said discharge hole 5-3c is that the center surrounds three circles with rotation axis 5-3a.

Claims (5)

1. the processing unit (plant) of the synthetic charcoal of a biomass sludge; Comprise kibbler, mixer (2), sludge tank (3), dryer, cooler (4), roller head machine (5); It is characterized in that: said first kibbler (1) all is connected mixer (2) inlet through belt conveyor with sludge tank (6) outlet; Said mixer (2) connects first dryer (6) inlet through belt conveyor; This first dryer (6) outlet connects cooler (4) inlet through belt conveyor; Said cooler (4) outlet connects the inlet of second dryer (8) through belt conveyor; Said first dryer (6) and second dryer (8) provide hot gas flow by the roasting kiln that issues setting (7), and said second dryer (8) outlet connects second kibbler (10) inlet through belt conveyor, and this second kibbler (10) outlet connects roller head machine (5) inlet through belt conveyor.
2. the processing unit (plant) that synthesizes charcoal according to the said biomass sludge of claim 1; It is characterized in that: said roasting kiln (7) comprises body of heater (7-1); Said body of heater (7-1) upper end is connected with flue (7-1a); Said body of heater (7-1) top is provided with the air duct (7-2) of coiling, and this air duct (7-2) passes from body of heater (7-1) sidewall and is connected with blower fan (7-3), and said air duct (7-2) the other end stretches out floss hole along flue (7-1a).
3. according to the processing unit (plant) of the synthetic charcoal of the said biomass sludge of claim 2, it is characterized in that: said air duct (2) is the serpentine coiling from down to up at body of heater (1).
4. the processing unit (plant) that synthesizes charcoal according to the said biomass sludge of claim 1; It is characterized in that: said roller head machine (5); Comprise worktable (5-1), discharge bucket (5-2), roll extrusion storehouse (5-3), said discharge bucket (5-2) is positioned under the roll extrusion storehouse (5-3), and rotation axis (5-3a) has been stretched at center, said roll extrusion storehouse (5-3); This rotation axis (5-3a) zygomorphy is provided with roller (5-3b); Bottom, this roll extrusion storehouse (5-3) with rotation axis (5-3a) be center ring to having discharge hole (5-3c), said roller (5-3b) is taper, this roller (5-3b) outer end diameter is little to be increased near rotation axis (5-3a) diameter gradually.
5. according to the processing unit (plant) of the synthetic charcoal of the said biomass sludge of claim 4, it is characterized in that: said discharge hole (5-3c) is that the center surrounds at least three circles with rotation axis (5-3a).
CN 201120260199 2011-07-22 2011-07-22 Processing device for biomass sludge synthetic carbon Withdrawn - After Issue CN202193770U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201120260199 CN202193770U (en) 2011-07-22 2011-07-22 Processing device for biomass sludge synthetic carbon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201120260199 CN202193770U (en) 2011-07-22 2011-07-22 Processing device for biomass sludge synthetic carbon

Publications (1)

Publication Number Publication Date
CN202193770U true CN202193770U (en) 2012-04-18

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Application Number Title Priority Date Filing Date
CN 201120260199 Withdrawn - After Issue CN202193770U (en) 2011-07-22 2011-07-22 Processing device for biomass sludge synthetic carbon

Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102249217A (en) * 2011-07-22 2011-11-23 重庆创能再生资源有限公司 Processing system of biomass-sludge synthetic carbon

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102249217A (en) * 2011-07-22 2011-11-23 重庆创能再生资源有限公司 Processing system of biomass-sludge synthetic carbon

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20120418

Effective date of abandoning: 20130306

RGAV Abandon patent right to avoid regrant