CN102249217B - Processing system of biomass-sludge synthetic carbon - Google Patents
Processing system of biomass-sludge synthetic carbon Download PDFInfo
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- CN102249217B CN102249217B CN 201110205832 CN201110205832A CN102249217B CN 102249217 B CN102249217 B CN 102249217B CN 201110205832 CN201110205832 CN 201110205832 CN 201110205832 A CN201110205832 A CN 201110205832A CN 102249217 B CN102249217 B CN 102249217B
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- dryer
- biomass
- belt conveyor
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- heater
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- 239000010802 sludge Substances 0.000 title claims abstract description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 15
- 238000012545 processing Methods 0.000 title claims abstract description 13
- 238000001125 extrusion Methods 0.000 claims description 13
- 241000628997 Flos Species 0.000 claims description 3
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 238000002485 combustion reaction Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 3
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 239000002028 Biomass Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000010923 batch production Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 by pulverizer Chemical compound 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000010795 gaseous waste Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000013138 pruning Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Treatment Of Sludge (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The invention discloses a processing system of biomass-sludge synthetic carbon. In the invention, outlets of a first grinder (1) and a sludge tank (6) are connected with an inlet of a mixer (2) through a belt conveyer; the mixer (2) is connected with an inlet of a first dryer (6) through a belt conveyer; an outlet of the first dryer (6) is connected with an inlet of a cooler (4) through a belt conveyer; an outlet of the cooler (4) is connected with an inlet of a second drier (8) through a belt conveyer; a lower combustion furnace (7) supplies hot airflow to the first dryer (6) and the second drier (8); an outlet of the second drier (8) is connected with an inlet of a second grinder (10) through a belt conveyer; and an outlet of the second grinder (10) is connected with an inlet of a roll forming machine (5) through a belt conveyer. The processing system can rapidly and continuously produce the biomass-sludge synthetic carbon in a fully-mechanized operating mode, thus greatly enhancing production effect; and meanwhile, efficiency of the combustion furnace and the roll forming machine is improved based on the production demands.
Description
Technical field
The invention belongs to the system of processing of biomass fuel, specifically, relate to the system of the synthetic carbon of a kind of process for processing biomass sludge.
Background technology
Enter 21 century, the mankind are faced with fast economic growth 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 world 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.
At present most of sewage work in all parts of the country all can produce large batch of mud (the mud solid, semi-solid state and the liquid gurry that refer to dispose of sewage and produce herein every day; 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 content of mud high (65%-80%) contains again poisonous heavy metal, 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, and the agricultural product security that causes because of fertilising and affect the HUMAN HEALTH event and happen occasionally becomes the very important factor that affects agriculture production, health of the masses and social stability.
Bring burning electricity generation after also having at present part producer with the mud oven dry, the water content of mud is large, density is large, viscosity is large, and generally all be powdery, semi-solid attitude, if take the secondary mechanical dehydration, dehydrating effect is poor, if directly entering the drying plant oven dry uses, energy consumption is high, and cost is high, and the mud of approximately drying one ton need to spend 200 yuan, and yield poorly, can't form batch production.
The biomass wide material sources, the various stalks of agriculture waste, various crotch, bark, tree root that forestry is discarded, the wood chip that wood working is discarded, sawdust etc.The various wood chips of industrial gaseous waste, sawdust, packing material, Chinese medicine slag, the various templates that urban construction is discarded, the annual branch of pruning of urban afforestation, the various mashed furniture of discarding in the life etc.At present application is processed as biomass-sludge synthetic carbon take biomass, mud as raw material with it by series of process, 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, the production line of being badly in need of a kind of consecutive production carries out Fully-mechanized production.
Summary of the invention
For solving above technical problem, the object of the present invention is to provide a kind of continuously, the system of Mechanized Processing biomass-sludge synthetic carbon.
The present invention seeks to realize like this: a kind of system of processing of biomass-sludge synthetic carbon, comprise pulverizer, mixer (2), sludge tank (3), dryer, cooler (4), roller head machine (5), its key is: described first disintegrator (1) is connected 6 with sludge tank) export all by belt conveyor connection mixer (2) entrance, described mixer (2) connects the first dryer (6) entrance by belt conveyor, this the first dryer (6) outlet connects cooler (4) entrance by belt conveyor, described cooler (4) outlet connects the entrance of the second dryer (8) by belt conveyor, described the first dryer (6) and the second dryer (8) provide hot gas flow by the roasting kiln that issues setting (7), described the second dryer (8) outlet connects the second pulverizer (10) entrance by belt conveyor, and this second pulverizer (10) outlet is by belt conveyor connecting rolling forming machine (5) entrance.
Biomass material is introduced into first disintegrator (1) and pulverizes, enter with mud in the sludge tank (3) again and be introduced into the first dryer (6) oven dry after mixer (2) mixes, then after entering cooler (4), again enter the second dryer (8) oven dry, on the one hand so that mud becomes loose, good permeability, density diminishes, and biomass material can also absorb the moisture in the mud, and then mixture dried, can improve drying efficiency, reduce the oven dry cost on the other hand biomass material promoted the combustion efficacy of mud, improved the thermal value of the synthetic charcoal of mud.
Above-mentioned roasting kiln (7) comprises body of heater (7-1), described body of heater (7-1) upper end is connected with flue (7-1a), described 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 described 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 heat utilization ratio of body of heater.
Above-mentioned air duct (2) is the serpentine coiling from down to up at body of heater (1).The area of this design absorbing heat is larger.
Above-mentioned roller head machine (5), comprise worktable (5-1), discharge bucket (5-2), roll extrusion storehouse (5-3), described discharge bucket (5-2) is positioned under the roll extrusion storehouse (5-3), rotation axis (5-3a) has been stretched at center, described roll extrusion storehouse (5-3), this rotation axis (5-3a) zygomorphy is provided with roller (5-3b), this bottom, roll extrusion storehouse (5-3) hoop centered by rotation axis (5-3a) has discharge hole (5-3c), it is characterized in that: described roller (5-3b) is taper, and this roller (5-3b) outer end diameter is little to be increased gradually near rotation axis (5-3a) diameter.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 enters from the outer end of roller, evenly squeezes out.
Above-mentioned discharge hole (5-3c) surrounds at least three circles centered by rotation axis (5-3a).Greatly improve the speed of discharging, improved the efficient of roll forming.
Beneficial effect: biomass-sludge synthetic carbon is produced in fast serialization of the present invention, is Fully-mechanized operation, has greatly improved production effect, need to carry out improved efficiency to roasting kiln and roller head machine owing to what produce simultaneously.The biomass-sludge synthetic carbon that processes has effectively solved the moisture height of mud, density is large, ventilation property is poor, viscosity is large, oven dry is difficult, the high difficult problem of oven dry cost; Biomass material has promoted the combustion efficacy of mud with after mud cooperates, and has improved the thermal value of biomass-sludge synthetic carbon, and combustionproperty is good.
Description of drawings
Fig. 1 is connection diagram of the present invention;
Fig. 2 is combustion furnace structure synoptic diagram among the present invention;
Fig. 3 is roller head machine structural representation among the present invention;
Fig. 4 is that the A of Fig. 3 is to view.
Embodiment
Embodiment
As shown in Figure 1, a kind of system of processing of biomass-sludge synthetic carbon, mainly by pulverizer, mixer 2, sludge tank 3, dryer, cooler 4, roller head machine 5 forms, first disintegrator 1 is connected outlet all by belt conveyor connection mixer 2 entrances with sludge tank, described mixer 2 connects the first dryer 6 entrances by belt conveyor, these the first dryer 6 outlets connect cooler 4 entrances by belt conveyor, described cooler 4 outlets connect the entrance of the second dryer 8 by belt conveyor, described the first dryer 6 and the second dryer 8 provide hot gas flow by the roasting kiln 7 that issues setting, 8 outlets of described the second dryer connect the second pulverizer 10 entrances by belt conveyor, and these the second pulverizer 10 outlets are by belt conveyor connecting rolling forming machine 5 entrances.
Further found out by Fig. 2, described the first roasting kiln 7 comprises body of heater 7-1, described body of heater 7-1 upper end is connected with flue 7-1a, described 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 the described air duct 7-2 the other end stretches out floss hole along flue 7-1a.Described air duct 2 is the serpentine coiling from down to up at body of heater 1.
Further by the described roller head machine 5 of Fig. 3, Fig. 4, comprise worktable 5-1, discharge bucket 5-2, roll extrusion storehouse 5-3, described 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, described roll extrusion storehouse, this rotation axis 5-3a zygomorphy is provided with roller 5-3b, this roll extrusion storehouse 5-3 bottom hoop centered by rotation axis 5-3a has discharge hole 5-3c, it is characterized in that: described roller 5-3b is taper, and this roller 5-3b outer end diameter is little to be increased gradually near rotation axis 5-3a diameter.Described discharge hole 5-3c surrounds three circles centered by rotation axis 5-3a.
Claims (3)
1. the system of processing of a biomass-sludge synthetic carbon, comprise pulverizer, mixer (2), sludge tank (3), dryer, cooler (4), roller head machine (5), it is characterized in that: first disintegrator (1) is connected 3 with sludge tank) export all by belt conveyor connection mixer (2) entrance, described mixer (2) connects the first dryer (6) entrance by belt conveyor, this the first dryer (6) outlet connects cooler (4) entrance by belt conveyor, described cooler (4) outlet connects the entrance of the second dryer (8) by belt conveyor, described the first dryer (6) and the second dryer (8) provide hot gas flow by the roasting kiln that issues setting (7), described the second dryer (8) outlet connects the second pulverizer (10) entrance by belt conveyor, and this second pulverizer (10) outlet is by belt conveyor connecting rolling forming machine (5) entrance; Described roasting kiln (7) comprises body of heater (7-1), described body of heater (7-1) upper end is connected with flue (7-1a), described 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 described air duct (7-2) the other end stretches out floss hole along flue (7-1a); Described air duct (7-2) is the serpentine coiling from down to up at body of heater (7-1).
2. the system of processing of described a kind of biomass-sludge synthetic carbon according to claim 1, it is characterized in that: described roller head machine (5), comprise worktable (5-1), discharge bucket (5-2), roll extrusion storehouse (5-3), described discharge bucket (5-2) is positioned under the roll extrusion storehouse (5-3), rotation axis (5-3a) has been stretched at center, described roll extrusion storehouse (5-3), this rotation axis (5-3a) zygomorphy is provided with roller (5-3b), this bottom, roll extrusion storehouse (5-3) hoop centered by rotation axis (5-3a) has discharge hole (5-3c), it is characterized in that: described roller (5-3b) is taper, and this roller (5-3b) outer end diameter is little to be increased gradually near rotation axis (5-3a) diameter.
3. the system of processing of described a kind of biomass-sludge synthetic carbon according to claim 2, it is characterized in that: described discharge hole (5-3c) surrounds at least three circles centered by rotation axis (5-3a).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110205832 CN102249217B (en) | 2011-07-22 | 2011-07-22 | Processing system of biomass-sludge synthetic carbon |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110205832 CN102249217B (en) | 2011-07-22 | 2011-07-22 | Processing system of biomass-sludge synthetic carbon |
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| Publication Number | Publication Date |
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| CN102249217A CN102249217A (en) | 2011-11-23 |
| CN102249217B true CN102249217B (en) | 2013-01-23 |
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| CN 201110205832 Expired - Fee Related CN102249217B (en) | 2011-07-22 | 2011-07-22 | Processing system of biomass-sludge synthetic carbon |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103982900B (en) * | 2014-06-06 | 2017-04-12 | 湖州强马分子筛有限公司 | Environment-friendly and energy-saving combustion treatment method and device |
| CN108981405A (en) * | 2018-05-23 | 2018-12-11 | 合肥汇英科技有限公司 | A kind of energy utilization system comprehensively utilizing natural energy resources |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101260334A (en) * | 2008-04-29 | 2008-09-10 | 彭立军 | Technique for producing fuel stick from sludge and domestic refuse |
| CN102021057A (en) * | 2010-11-30 | 2011-04-20 | 宁波国海能源科技有限公司 | Method for preparing biomass solid molding fuel |
| CN202193770U (en) * | 2011-07-22 | 2012-04-18 | 重庆创能再生资源有限公司 | Processing device for biomass sludge synthetic carbon |
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Effective date of registration: 20160107 Address after: 401122, 11, 89 Jin Yu Avenue, North New District, Chongqing Patentee after: Chongqing crown environmental protection energy Co., Ltd. Address before: The 405422 Chongqing road Fuling District No. 132 town Patentee before: Chongqing Chuang Neng environmental protection equipment manufacturing Co., Ltd. |
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Address after: 401122 89 1-20-2, 3 and 11, 4 Jin Yu Avenue, North New District, Chongqing Patentee after: Chongqing crown environmental protection energy Limited by Share Ltd Address before: 401122, 11, 89 Jin Yu Avenue, North New District, Chongqing Patentee before: Chongqing crown environmental protection energy Co., Ltd. |
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Granted publication date: 20130123 Termination date: 20200722 |