CN207143196U - Biomass castoff, sludge treating system - Google Patents
Biomass castoff, sludge treating system Download PDFInfo
- Publication number
- CN207143196U CN207143196U CN201721102203.7U CN201721102203U CN207143196U CN 207143196 U CN207143196 U CN 207143196U CN 201721102203 U CN201721102203 U CN 201721102203U CN 207143196 U CN207143196 U CN 207143196U
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- CN
- China
- Prior art keywords
- mixer
- dryer
- biomass castoff
- sludge
- dewaterer
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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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a kind of biomass castoff, sludge treating system, including storage basin, pulverizer, mixer, dewaterer, dryer, ball press, first gravimetric feeder, second gravimetric feeder, air exhauster, spraying and dedusting deaeration tower, more conveying worms and Duo Tai belt conveyors, storage basin, dewaterer, first gravimetric feeder, mixer passes sequentially through conveying worm connection, pulverizer, second gravimetric feeder, mixer passes sequentially through belt conveyor connection, mixer, dryer, ball press passes sequentially through belt conveyor connection, dryer, air exhauster, spraying and dedusting deaeration tower is sequentially connected by pipeline.The system efficiently solves the aqueous problem high, density is big, poor air permeability, viscosity are big, drying is difficult, drying cost is high of sludge, greatly reduces cost.The system production cost is low and reduces the discharge of dust and foul smell.
Description
Technical field
It the utility model is related at recycling waste technical field, more particularly to a kind of biomass castoff, sludge
Reason system.
Background technology
Sludge is major small and medium-sized cities sewage treatment plants processing sewage and the discarded object of association (including at trade effluent
Manage factory).Sludge is also a kind of pollutant of substantial amounts.Its water content height (more than 80%), density is big, poor air permeability, virus
Bacterium is various, be it is a kind of still handle so far extremely difficult, processing cost is higher, the limited obsolete material of regeneration.Sludge
In containing 40% or so organic matter, and have certain energy reproducible utilization.The sludge resource of southern area is very abundant, and
And the speed increased every year is also very big.At present, although a sludge part realizes regeneration, remaining is largely still used
Landfill disposal.Sludge is because virus and bacteria is more, and content of beary metal is high, so sludge is made other regenerations and strictly limited
System.The best trans-utilization scheme of sludge is conversion regenerative resource, sludge is changed into fuel, all virus and bacterias can be whole
Burning is gone out cleared.
The source of biomass castoff is a lot：1st, urban industry, processing industry biomass castoff：Bamboo wood working industry gives up
Bark, sawdust, the leftover pieces abandoned, the discarded material head of Furniture manufacturing industry, corner, sawdust materials etc., food-processing industry is discarded
Certain herbaceous plants with big flowers melon shell, peanut shell, husk etc., the Chinese medicine slag discarded in pharmaceuticals industry production etc., the discarded vinasse of brewing industry, vinegar grain
Deng the discarded wooden, bamboo matter of, every profession and trade buying equipment, papery packaging etc.；2nd, the biomass castoff in urban construction：City is built
If the middle bamboo and wood matter template used, bamboo springboard, bamboo springboard, according to the rules, using must be changed after certain time limit, therefore produce
Substantial amounts of bamboo and wood discarded object；3rd, the discarded biomass castoff of reconstruction of the old city town：A large amount of timber wooden sticks that reconstruction of the old city town removes,
Timeworn furniture scrapped etc.；4th, urban afforestation, newly develop discarded biomass castoff：Cut after carrying out Pruning and rectifying to trees
The residual branch of plant, the trees not survived, the trees planted originally in reconstruction of the old city town are dug up discarded etc.；5th, life of urban resident gives up
The biomass castoff abandoned：The bamboo and wood discarded object that resident carries out the timeworn furniture of furniture displacement discarding, house decoration transformation is pulled down；6、
Domestic waste：Organic waste such as napkin paper, toilet paper, kitchen garbage, leaf, disposable bamboo-wood chopsticks etc.；7th, rural area is special
Biomass castoff caused by color industrial crops：Such as maize straw, straw waste of flax, crops stubble.
Utility model content
In order to solve the above technical problems, the utility model provides low a kind of saving energy, cost, reduction dust and foul smell
Biomass castoff, sludge treating system.
The technical solution of the utility model is as follows：A kind of biomass castoff, sludge treating system, including storage basin, powder
Broken machine, mixer, dewaterer, dryer, ball press, the first gravimetric feeder, the second gravimetric feeder, air exhauster, spray remove
Dirt deaeration tower, more conveying worms and Duo Tai belt conveyors, the storage basin, dewaterer, the first gravimetric feeder, stirring
Machine passes sequentially through conveying worm connection, and the pulverizer, the second gravimetric feeder, mixer pass sequentially through belt conveyor company
Connect, mixer, dryer, ball press pass sequentially through belt conveyor connection, and dryer, air exhauster, spraying and dedusting deaeration tower lead to
Piping is sequentially connected；Sludge in storage basin is transported in dewaterer by conveying worm to be dehydrated, and passes through first after dehydration
Gravimetric feeder enters mixer, and biomass castoff is put into pulverizer and crushed, and then passes through the second gravimetric feeder
Into in mixer, sludge stirs and evenly mixs resulting mixture with biomass castoff in mixer, and mixture delivers into drying
Dried in machine, subsequently into broken compressing in ball press.
Preferably, the pulverizer is half wet crushing mill, is more suitable for the crushing of biomass castoff, helps biology
The water content of matter discarded object is maintained at certain proportion.
Preferably, the spraying and dedusting deaeration tower is high-order spraying and dedusting deaeration tower, is particularly suitable for producing largely
The device of dust and foul smell, deodorization dust removing effects are more preferably.
Preferably, the mixer is pan mixer, more suitable for the mixing of sludge and biomass castoff.
Preferably, the dewaterer is belt type dewaterer, more suitable for the big soft material of the such moisture of sludge
Material.
Preferably, the dryer is rotating drum type drying machine, and drying effect is more preferable.
Preferably, the junction of the dryer and air exhauster is provided with separation net, prevents block sewage sludge biomass
Discarded object mixture enters.
The beneficial effects of the utility model are：2 pollution problems caused by solving the sludge of puzzlement people for many years, by dirt
Mud and biomass castoff effectively use, and are fabricated to as biomass-sludge synthetic carbon.The system first uses dewaterer by dirt
Mud is dehydrated to certain water content, then is dried after being stirred and evenly mixed by weight proportion with the biomass castoff after crushing, and this is effectively
Solve the aqueous problem high, density is big, poor air permeability, viscosity are big, drying is difficult, drying cost is high of sludge, greatly reduce into
This.The system production cost is low and reduces the discharge of dust and foul smell.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
The utility model is described in further detail with reference to the accompanying drawings and examples：
A kind of biomass castoff as shown in Figure 1, sludge treating system, mainly by storage basin 1, pulverizer 2, mixer
3rd, dewaterer 4, dryer 5, ball press 6, the first gravimetric feeder 7, the second gravimetric feeder 10, air exhauster 8, spraying and dedusting remove
Gas tower 9, more conveying worms and Duo Tai belt conveyors composition.Storage basin 1, dewaterer 4, the first gravimetric feeder 7, stirring
Machine 3 passes sequentially through conveying worm connection, and pulverizer 2, the second gravimetric feeder 10, mixer 3 pass sequentially through belt conveyor
Connection, mixer 3, dryer 5, ball press 6 pass sequentially through belt conveyor connection, and dryer 5, air exhauster 8, spraying and dedusting remove
Gas tower 9 is sequentially connected by pipeline；Sludge in storage basin 1 is transported in dewaterer 4 by conveying worm to be dehydrated, after dehydration
Mixer 3 is entered by the first gravimetric feeder 7, biomass castoff is put into pulverizer 2 and crushed, and then passes through the second meter
Weight batcher 10 also enters in mixer 3, and sludge stirs and evenly mixs resulting mixture with biomass castoff in mixer 3, mixes
Thing is delivered into dryer 5 and dried, subsequently into broken compressing in ball press 6.
Pulverizer 2 is half wet crushing mill, is more suitable for the crushing of biomass castoff, helps the aqueous of biomass castoff
Amount is maintained at certain proportion.Spraying and dedusting deaeration tower 9 is high-order spraying and dedusting deaeration tower, be particularly suitable for produce a large amount of dust and
The device of foul smell, deodorization dust removing effects are more preferably.Mixer 3 is pan mixer, more suitable for sludge and biomass castoff
Mixing.Dewaterer 4 is belt type dewaterer, more suitable for the big soft material of the such moisture of sludge.Dryer 5 is drum-type
Dryer, drying effect are more preferable.The junction of dryer 5 and air exhauster 8 is provided with separation net, prevents block sewage sludge biomass from giving up
Gurry mixture enters.
Sludge in storage basin 1 is introduced into dewaterer 4 dehydration so that sludge moisture content reaches setting ratio, then passes through
First gravimetric feeder 7 is by the sludge input mixer 3 of constant weight.Biomass castoff is put into pulverizer 2 and carried out
Crush, then delivered into the biomass castoff of constant weight in mixer 3 by the second gravimetric feeder 10.Sludge with
Biomass castoff is dried after being stirred and evenly mixed in mixer 3 into dryer 5, subsequently into smashing pressure in ball press 6
Shape is made and obtains biomass-sludge synthetic carbon product.The gas outlet of dryer 5 connects air exhauster 8 by pipeline, and air exhauster 8 connects
Spraying and dedusting deaeration tower 9 is connect, caused dust in drying course and foul smell suction spraying and dedusting deaeration tower 9 are subjected to dedusting and removed
It is smelly.
Claims (7)
1. a kind of biomass castoff, sludge treating system, it is characterised in that：Including storage basin (1), pulverizer (2), mixer
(3), dewaterer (4), dryer (5), ball press (6), the first gravimetric feeder (7), the second gravimetric feeder (10), air exhauster
(8), spraying and dedusting deaeration tower (9), more conveying worms and Duo Tai belt conveyors, the storage basin (1), dewaterer (4),
First gravimetric feeder (7), mixer (3) pass sequentially through conveying worm connection, the pulverizer (2), the second weight calculation feed
Machine (10), mixer (3) pass sequentially through belt conveyor connection, and mixer (3), dryer (5), ball press (6) pass sequentially through
Belt conveyor is connected, and dryer (5), air exhauster (8), spraying and dedusting deaeration tower (9) are sequentially connected by pipeline；Storage basin
(1) sludge in is transported in dewaterer (4) by conveying worm to be dehydrated, and is entered after dehydration by the first gravimetric feeder (7)
Enter mixer (3), biomass castoff is put into pulverizer (2) and crushed, then also enters by the second gravimetric feeder (10)
Enter in mixer (3), sludge stirs and evenly mixs resulting mixture with biomass castoff in mixer (3), and mixture delivers into
Dried in dryer (5), subsequently into broken compressing in ball press (6).
2. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The pulverizer (2) is half
Wet crushing mill.
3. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The spraying and dedusting degasification
Tower (9) is high-order spraying and dedusting deaeration tower.
4. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The mixer (3) is disk
Formula mixer.
5. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The dewaterer (4) is band
Formula dewaterer.
6. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The dryer (5) is to turn
Cylindrical dryer.
7. biomass castoff as claimed in claim 1, sludge treating system, it is characterised in that：The dryer (5) is with taking out
The junction of blower fan (8) is provided with separation net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721102203.7U CN207143196U (en) | 2017-08-31 | 2017-08-31 | Biomass castoff, sludge treating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721102203.7U CN207143196U (en) | 2017-08-31 | 2017-08-31 | Biomass castoff, sludge treating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207143196U true CN207143196U (en) | 2018-03-27 |
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ID=61670630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721102203.7U Active CN207143196U (en) | 2017-08-31 | 2017-08-31 | Biomass castoff, sludge treating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207143196U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109433787A (en) * | 2018-10-26 | 2019-03-08 | 武汉天源环保股份有限公司 | A kind of method of resource utilization after kitchen garbage deep dehydration |
-
2017
- 2017-08-31 CN CN201721102203.7U patent/CN207143196U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109433787A (en) * | 2018-10-26 | 2019-03-08 | 武汉天源环保股份有限公司 | A kind of method of resource utilization after kitchen garbage deep dehydration |
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