CN109251777A - A kind of production technology and its equipment of useless cloth sludge fuel particle - Google Patents
A kind of production technology and its equipment of useless cloth sludge fuel particle Download PDFInfo
- Publication number
- CN109251777A CN109251777A CN201811384469.4A CN201811384469A CN109251777A CN 109251777 A CN109251777 A CN 109251777A CN 201811384469 A CN201811384469 A CN 201811384469A CN 109251777 A CN109251777 A CN 109251777A
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- sludge
- cloth
- fuel particle
- useless
- centrifugation
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- 239000004744 fabric Substances 0.000 title claims abstract description 86
- 239000010802 sludge Substances 0.000 title claims abstract description 74
- 239000002245 particle Substances 0.000 title claims abstract description 68
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 37
- 239000000446 fuel Substances 0.000 title claims abstract description 36
- 238000005516 engineering process Methods 0.000 title claims abstract description 20
- 239000002699 waste material Substances 0.000 claims abstract description 33
- 238000005119 centrifugation Methods 0.000 claims abstract description 24
- 238000005469 granulation Methods 0.000 claims abstract description 22
- 230000003179 granulation Effects 0.000 claims abstract description 22
- 238000002156 mixing Methods 0.000 claims abstract description 14
- 239000000843 powder Substances 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 4
- 238000012856 packing Methods 0.000 claims description 18
- 238000005520 cutting process Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000007906 compression Methods 0.000 claims description 4
- 230000006835 compression Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 230000001681 protective effect Effects 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 5
- 239000003245 coal Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000004026 adhesive bonding Methods 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 230000007115 recruitment Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/22—Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/28—Cutting, disintegrating, shredding or grinding
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/32—Molding or moulds
-
- 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
Abstract
The invention discloses the production technologies and its equipment of a kind of useless cloth sludge fuel particle, comprising the following steps: 1), useless cloth powder cut, obtain cloth waste, cloth waste is transported to quantitative barrel；2), cloth waste is uniformly launched on blending transportation band by quantitative barrel；3) it, is launched on the blending transportation band for having spread cloth waste after sludge drying through auger；4), cloth waste and sludge are mixed in granulation device with the roller of planetary rotation, and mixture is squeezed by centrifugation is made fuel particle, fuel particle surface compact, and core has air gap.The present invention has high economic benefit, environmentally protective feature.
Description
Technical field
The present invention relates to a kind of production technology and equipments of solid particle, especially a kind of useless cloth sludge fuel particle
Production technology and its equipment.
Background technique
In recent years, environmentally protective idea becomes more and more popular, and environmentally protective policies and regulations also gradually increase, sewage
Treatment of Sludge becomes an emerging industry.After life and industrial sewage treatment, one of product is sludge.
The main post processing mode of sludge includes anaerobic fermentation, aerobic fermentation and anhydration and incineration etc., wherein anhydration and incineration be using compared with
Extensively, the relatively simple a kind of mode of means.But due to the property of material itself, the calorific value of sludge only has 700 kilocalories or so,
The efficiency of burning is lower.On the other hand, the useless cloth processing of textile industry has been increasingly becoming a great problem of manufacturer.Due to the cloth that gives up
Item itself is loose, and occupied space is big, and the low efficiency in terms of transporting with feeding, the benefit as fuel is not high, at present essentially as
Rubbish is toppled over or is accumulated.
Therefore, design it is a kind of there is high economic benefit, and the treatment process of environmentally protective useless cloth and sludge and its set
Standby is industry technical staff's urgent problem.
Summary of the invention
The object of the present invention is to provide the production technologies and its equipment of a kind of useless cloth sludge fuel particle.The present invention
With high economic benefit, environmentally protective feature.
Technical solution of the present invention: in a kind of production technology of useless cloth sludge fuel particle,
The following steps are included:
1) the cloth powder that, gives up is cut, and obtains cloth waste, cloth waste is transported to quantitative barrel；
2), cloth waste is uniformly launched on blending transportation band by quantitative barrel；
3) it, is launched on the blending transportation band for having spread cloth waste after sludge drying through auger；
4), cloth waste and sludge are mixed in granulation device with the roller of planetary rotation, and the revolution of roller is reciprocal circular-rotation, are mixed
It closes object and obtained fuel particle, fuel particle surface compact is squeezed by centrifugation, core has air gap.
In a kind of production technology of useless cloth sludge fuel particle above-mentioned, in step 3 and step 4, by weight
The accounting of meter, the cloth waste is 65-75%, remaining is sludge.
In a kind of production technology of useless cloth sludge fuel particle above-mentioned, in step 3 and step 4, by weight
Meter, the accounting of the cloth waste are 70%, remaining is sludge.
In a kind of production technology of useless cloth sludge fuel particle above-mentioned, in step 4, the water content of the sludge is
25%-35%.
In a kind of production technology of useless cloth sludge fuel particle above-mentioned, in step 4, the water content of the sludge is
30%.
Realize a kind of production equipment of the production technology of useless cloth sludge fuel particle above-mentioned, including successively through conveyer belt
Connect cloth powder cutting apparatus, quantitative barrel, sludge auger, granulation device and finished product bin；The granulation device includes cylinder
The mould of shape, the top of mould are equipped with feed inlet, and the circumferential wall of mould is equipped with die hole, the extruding of planetary rotation is equipped in mould
Roller, the outside of mould are equipped with the scraper cooperated with circumferential wall, and scraper is rotated around the axis of mould.
In a kind of production equipment of useless cloth sludge fuel particle above-mentioned, the scraper is arranged on fluted disc.
In a kind of production equipment of useless cloth sludge fuel particle above-mentioned, the finished product bin is connected with packing dress
It sets, packing apparatus includes centrifugation basal disc, and the top for being centrifuged basal disc is equipped with concentrator bowl, and it is cyclic annular to be centrifuged formation between basal disc and concentrator bowl
The rotation axis in gap, the bus and centrifugation basal disc of annular gap tilts；The lower section for being centrifuged basal disc, which is equipped with, accepts funnel, accepts
The lower end of funnel is equipped with a pair of of bond roll, and the side of bond roll is equipped with base band feed roller and applies packing element, and the other side of bond roll is set
There is coiled strip roller.
In a kind of production equipment of useless cloth sludge fuel particle above-mentioned, the outer circle wall of the concentrator bowl be equipped with
The tooth of driving device connection, concentrator bowl is identical as the centrifugation steering of basal disc, and revolving speed is different.
In a kind of production equipment of useless cloth sludge fuel particle above-mentioned, the charging of cloth powder cutting apparatus connection and
The conveyer belt of discharging is strong magnetic conveyer belt.
Compared with prior art, useless cloth is crushed to 1 centimetre or so first and is required with reaching granulation by the present invention, then and warp
Sludge after crossing desiccation disposition mix matching, and the material after blending is finally compressed into particle by particles compress all-in-one machine.?
On blending transportation band, cloth waste is under, and then sludge, which spreads the feeding on cloth waste, keeps contact of the cloth waste with sludge more stable, subsequent
In granulation device, is not in that cloth waste concentrates situation about floating on sludge, guarantees the effect of granulation.In granulation device, pass through
The reciprocal revolution of roller makes to cause the surface of particle further through the mode that centrifugation squeezes comprising a certain amount of air gap in mixture
Close, particle obtained will not be loose, and the particle with air gap is easy cracking in burning, improves efficiency of combustion.Moreover, originally
Invention makes particle obtained both will not be since cloth contained by cloth, the rational proportion of sludge in conjunction with the water content of control sludge
Amount height is easy to crack, and will not reduce whole calorific value because of sludge content height.The particle calorific value of output of the present invention is in 4000 kilocalories
Left and right, close to the raw coal of 5000 kilocalories, can replace to a certain extent, subsidize in conjunction with the processing of useless cloth and sludge, 1 year
Profit has high economic benefit at 2,000,000 yuan or more.And the present invention has effectively handled useless cloth and sludge, meets
Environmentally protective theory.
Further, packing apparatus of the invention first passes through the posture of centrifugation basal disc and concentrator bowl adjustment particle, then
Particle and base band are bonded, formation ammunition belt shape product, on the one hand this product neatly convenient for packing and loading and unloading goods, on the other hand exists
After base band is blown when burning, particle dispersion is burnt quickly abundant.
To sum up, the present invention has high economic benefit, environmentally protective feature.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is the arrangement schematic diagram of granulation device；
Fig. 3 is the structural schematic diagram of granulation device；
Fig. 4 is the structural schematic diagram of packing apparatus；
Fig. 5 is the schematic illustration of packing apparatus.
Appended drawing reference: 10- cloth powder cutting apparatus, 20- quantify barrel, 30- sludge auger, 40- granulation device, 41- mould
Disk, 42- feed inlet, 43- compression roller, 44- scraper, 45- fluted disc, 46- feeding packing auger, 47- feed feed bin, 48- cyclone dust removal
Device, 49- bag filter, 50- finished product bin, 61- centrifugation basal disc, 62- concentrator bowl, 63- annular gap, 64- accept funnel,
65- bond roll, 66- base band feed roller, 67- apply packing element, 68- tooth, 69- coiled strip roller.
Specific embodiment
Below with reference to embodiment, the invention will be further described, but is not intended as the foundation limited the present invention.
A kind of embodiment: production technology of useless cloth sludge fuel particle, comprising the following steps:
The following steps are included:
1) the cloth powder that, gives up is cut, and obtains cloth waste, cloth waste is transported to quantitative barrel；
2), cloth waste is uniformly launched on blending transportation band by quantitative barrel；
3), sludge is launched on the blending transportation band for having spread cloth waste through auger, and the accounting of cloth waste is 70%, remaining is dirt
Mud；
4), cloth waste and sludge are mixed in granulation device with the roller of planetary rotation, and the revolution of roller is reciprocal circular motion, are mixed
It closes object and obtained fuel particle, fuel particle surface compact is squeezed by centrifugation, core has air gap.
In step 4, the water content of the sludge is 30%.
A kind of production equipment of the production technology of useless cloth sludge fuel particle, including cloth powder is sequentially connected through conveyer belt
Cutting apparatus 10, quantitative barrel 20, sludge auger 30, granulation device 40 and finished product bin 50；The granulation device 40 includes circle
The mould 41 of tubular, the top of mould 41 are equipped with feed inlet 42, and the circumferential wall of mould 41 is equipped with die hole, is equipped in mould 41
The compression roller 43 of planetary rotation, the outside of mould 41 are equipped with the scraper 44 cooperated with circumferential wall, axis of the scraper 44 around mould 41
Line rotation.
The scraper 44 is arranged on fluted disc 45.
The finished product bin 50 is connected with packing apparatus, and packing apparatus includes centrifugation basal disc 61, is centrifuged the upper of basal disc 61
Side is equipped with concentrator bowl 62, is centrifuged between basal disc 61 and concentrator bowl 62 and forms annular gap 63, the bus of annular gap 63 and centrifugation
The rotation axis of basal disc 61 tilts；The lower section for being centrifuged basal disc 61, which is equipped with, accepts funnel 64, and the lower end for accepting funnel 64 is equipped with one
To bond roll 65, the side of bond roll 65 is equipped with base band feed roller 66 and applies packing element 67, and the other side of bond roll 65 is equipped with coiled strip
Roller 69.
The outer circle wall of the concentrator bowl 62 is equipped with the tooth 68 connecting with driving device, concentrator bowl 62 and centrifugation basal disc 61
Steering it is identical, revolving speed is different.
The conveyer belt of charging and discharging that the cloth powder cutting apparatus 10 connects is strong magnetic conveyer belt.
Working principle:
The main equipment of this production line is powder-cutting machine and particles compress all-in-one machine, in conjunction with the physical characteristic of raw material, to powder
Machine and particles compress all-in-one machine is cut to have carried out improving on the basis of former stalk crasher and particles compress all-in-one machine to adapt to give birth to
It produces.
The production line carries out being crushed to 1 centimetre or so to reach granulation requirement, then and by desiccation to useless cloth first
The sludge (moisture is 30% or so, and state is powdered) postponed mix matching, mixture proportion are as follows: cloth 70%, sludge 30%.
The material after blending is finally compressed into particle by particles compress all-in-one machine.
As shown in Figure 1, on the conveyor belt, first spread shred, then in shred upper berth sludge, cloth waste and sludge are connect
More stable, good mixing effect is touched, in subsequent granulation device 40, is not in that cloth waste concentrates situation about floating on sludge, guarantees
The effect of granulation.
As shown in figure 3, entering granulation device 40 after cloth waste and sludge mixing, the compression roller 43 of granulation device 40 will be mixed
Object is squeezed out from the die hole of mould 41, and then scraper 44 is hung up to form particle, and particle is sent into finished product bin 50 through conveyer belt.
The arrangement of granulation device 40 is as shown in Fig. 2, 46 be wherein feeding packing auger, 47 be charging feed bin, and 48 be cyclone dust removal
Device, 49 be bag filter.
The particle of finished product bin 50 is sent to packing apparatus through conveyer belt.Particle falls into concentrator bowl 62 and centrifugation basal disc from top
Between 61, as shown in figure 4, centrifugation basal disc 61 is driven moving axis driving, concentrator bowl 62 is driven by the tooth 68 on outer circle wall, the two
Turn to identical, revolving speed difference.Firstly, particle is thrown toward edge by centrifugal effect, falls into and accept funnel 64, in this process
In, particle always can radially be thrown away, i.e., the axis of particle completes the adjustment of posture along the radial direction of centrifugation basal disc 61；Its
It is secondary, if there is the particle of axis and centrifugation 61 radial skew of basal disc, then particle can be by card due to the presence of annular gap 63
Firmly, then due to the rotational speed difference of concentrator bowl 62 and centrifugation basal disc 61, particle is adjusted until falling into undertaking hopper in targeted attitude.
Particle in undertaking hopper, which is successively fallen, to be bonded in base band, by controlling the inlet amount of conveyer belt, prevents from accepting interior, hopper
Grain amount excessively causes to block.
Paper tape can also be used for environmental protection consideration in the preferred plastic tape of base band.Base band is driven by coiled strip roller 69, applies packing element 67
The cementing in base band is pressed in the base band of gluing (undertaking leakage by bond roll 65 from the particle fallen in funnel 64 is accepted
Baffle is equipped at the whereabouts of bucket is pressed in it in base band by bond roll to hold particle), it is thusly-formed ammunition belt shape product.
Apparatus of the present invention carry out trial operation in Huzhou Wuxing District, Nanxun District.To knitting inner children's clothing market scrap fabric, Wu Xing
The waste utilization in area, Nanxun District urban life industrial sludge not only effectively protects ecological environment, but also creates well for enterprise
Economic value.
Specific economic conditions are analyzed as follows:
Cloth mud granulizing production line (with a crusher, two compacting shape machine configuring conditions) according to 3 tons of yield/
Hour, calculated 8 hour/day of working time for the whole year production time 300 days, and production is 7200 tons, separately subtracts annual shut down and ties up
50 days 1200 tons of yield are repaired, annual yield is 6000 tons.
In granulating raw material proportion, useless cloth accounts for 70%, sludge and accounts for 30%.It is calculated by 6000 tons of annual total output, give up cloth
4200 tons/year, 1800 tons/year of sludge of material.
Useless 200 yuan/ton of cloth disposal consideration, sludge treatment take in 400 yuan/ton, and by the two ratio, (useless cloth is accounted for
70%, 30%) sludge, which accounts for, calculates, add up to 260 yuan/ton of disposal consideration.
According to particle calorific value, theoretically 1 ton of particle can substantially support 0.7 ton of coal, according to 650 yuan of existing coal price/
Ton, particle are worth 455 yuan/ton (455 yuan of coal costs can be saved by burning 1 ton of particle).
By the above two o'clock, income is total: 715 yuan/ton.
1 profit flow table of table
| Project | Detail | The amount of money |
| One, operating income | 715*6,000 | 4,290,000/ year |
| Two, production cost | ||
| Equipment depreciation | Equipment gross investment depreciation in 1,500,000,10 years | 150,000/ year |
| Recruitment cost | 5000 yuan/people of wage, 4 people | 240,000/ year |
| Power consumption | Power consumption 270KW/h, 0.8 yuan of the electricity charge/degree | 432,000/ year |
| Maintenance cost | 60,000/ year | |
| Factory's hire charge | 60,000/ year | |
| Traffic expense | 50 yuan/ton | 300,000/ year |
| Administration fee | 60,000/ year | |
| Sludge drying takes | 200 yuan/ton of desiccation cost | 360,000/ year |
| Total cost | 1,662,000/ year | |
| Three, profit | 2,628,000/ year |
As seen from the above table, the profit that the present invention is implemented is considerable.
Claims (10)
1. a kind of production technology of useless cloth sludge fuel particle, it is characterised in that: the following steps are included:
1) the cloth powder that, gives up is cut, and obtains cloth waste, cloth waste is transported to quantitative barrel；
2), cloth waste is uniformly launched on blending transportation band by quantitative barrel；
3) it, is launched on the blending transportation band for having spread cloth waste after sludge drying through auger；
4), cloth waste and sludge are mixed in granulation device with the roller of planetary rotation, and the revolution of roller is reciprocal circular motion, mixing
Object is squeezed by centrifugation is made fuel particle, fuel particle surface compact, and core has air gap.
2. a kind of production technology of useless cloth sludge fuel particle according to claim 1, it is characterised in that: in step 3
With in step 4, by weight, the accounting of the cloth waste is 65-75%, remaining is sludge.
3. a kind of production technology of useless cloth sludge fuel particle according to claim 2, it is characterised in that: in step 3
With in step 4, by weight, the accounting of the cloth waste is 70%, remaining is sludge.
4. a kind of production technology of useless cloth sludge fuel particle according to claim 1, it is characterised in that: in step 4
In, the water content of the sludge is 25%-35%.
5. a kind of production technology of useless cloth sludge fuel particle according to claim 4, it is characterised in that: in step 4
In, the water content of the sludge is 30%.
6. realize a kind of described in any item production equipments of the production technology of useless cloth sludge fuel particle of claim 1-5,
It is characterized by comprising be sequentially connected cloth powder cutting apparatus (10), quantitative barrel (20), sludge auger (30), system through conveyer belt
Grain device (40) and finished product bin (50)；The granulation device (40) includes cylindric mould (41), mould (41) it is upper
Side is equipped with feed inlet (42), and the circumferential wall of mould (41) is equipped with die hole, and the compression roller of planetary rotation is equipped in mould (41)
(43), the outside of mould (41) is equipped with the scraper (44) cooperated with circumferential wall, and scraper (44) is rotated around the axis of mould (41).
7. a kind of production equipment of useless cloth sludge fuel particle according to claim 6, it is characterised in that: described scrapes
Knife (44) is arranged on fluted disc (45).
8. a kind of production equipment of useless cloth sludge fuel particle according to claim 6, it is characterised in that: it is described at
Product feed bin (50) is connected with packing apparatus, and packing apparatus includes centrifugation basal disc (61), and the top of centrifugation basal disc (61) is equipped with centrifugation
Cylinder (62) is centrifuged between basal disc (61) and concentrator bowl (62) and forms annular gap (63), the bus of annular gap (63) and centrifugation
The rotation axis of basal disc (61) tilts；The lower section for being centrifuged basal disc (61), which is equipped with, accepts funnel (64), accepts under funnel (64)
End is equipped with a pair of of bond roll (65), and the side of bond roll (65) is equipped with base band feed roller (66) and applies packing element (67), bond roll
(65) the other side is equipped with coiled strip roller (69).
9. a kind of production equipment of useless cloth sludge fuel particle according to claim 8, it is characterised in that: the centrifugation
The outer circle wall of cylinder (62) is equipped with the tooth (68) connecting with driving device, the steering phase of concentrator bowl (62) and centrifugation basal disc (61)
Together, revolving speed is different.
10. a kind of production equipment of useless cloth sludge fuel particle according to claim 6, it is characterised in that: the cloth
The charging of powder cutting apparatus (10) connection and the conveyer belt of discharging are strong magnetic conveyer belt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811384469.4A CN109251777A (en) | 2018-11-20 | 2018-11-20 | A kind of production technology and its equipment of useless cloth sludge fuel particle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811384469.4A CN109251777A (en) | 2018-11-20 | 2018-11-20 | A kind of production technology and its equipment of useless cloth sludge fuel particle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109251777A true CN109251777A (en) | 2019-01-22 |
Family
ID=65043507
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811384469.4A Pending CN109251777A (en) | 2018-11-20 | 2018-11-20 | A kind of production technology and its equipment of useless cloth sludge fuel particle |
Country Status (1)
| Country | Link |
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| CN (1) | CN109251777A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101058758A (en) * | 2006-04-13 | 2007-10-24 | 徐日生 | Garbage environmental protection regenerative coal |
| CN101982532A (en) * | 2010-11-11 | 2011-03-02 | 沈阳航空航天大学 | System for preparing refuse derived fuel from high-calorific-value components of house refuse |
| CN105695032A (en) * | 2016-03-02 | 2016-06-22 | 普利资环境科技（苏州）有限公司 | System for making sludge into regenerated solid fuel |
| CN205368283U (en) * | 2016-03-02 | 2016-07-06 | 普利资环境科技（苏州）有限公司 | System for make regeneration solid fuel with mud |
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2018
- 2018-11-20 CN CN201811384469.4A patent/CN109251777A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101058758A (en) * | 2006-04-13 | 2007-10-24 | 徐日生 | Garbage environmental protection regenerative coal |
| CN101982532A (en) * | 2010-11-11 | 2011-03-02 | 沈阳航空航天大学 | System for preparing refuse derived fuel from high-calorific-value components of house refuse |
| CN105695032A (en) * | 2016-03-02 | 2016-06-22 | 普利资环境科技（苏州）有限公司 | System for making sludge into regenerated solid fuel |
| CN205368283U (en) * | 2016-03-02 | 2016-07-06 | 普利资环境科技（苏州）有限公司 | System for make regeneration solid fuel with mud |
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