CN204611781U - Garbage derivatived fuel preparation complexes integrated with burning electricity generation - Google Patents
Garbage derivatived fuel preparation complexes integrated with burning electricity generation Download PDFInfo
- Publication number
- CN204611781U CN204611781U CN201520223944.5U CN201520223944U CN204611781U CN 204611781 U CN204611781 U CN 204611781U CN 201520223944 U CN201520223944 U CN 201520223944U CN 204611781 U CN204611781 U CN 204611781U
- Authority
- CN
- China
- Prior art keywords
- garbage
- derivatived fuel
- treatment chamber
- biochemical treatment
- burning
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a kind of garbage derivatived fuel preparation complexes integrated with burning electricity generation, belongs to field of garbage disposal.Described integrated complexes comprise shell body, top pressure closure and garbage feeding door, and garbage feeding door is located at the side of shell body, and top pressure closure is positioned at the top of shell body; Wherein, sealing discharge bin, rubbish storage pond, refuse classification workshop, biochemical treatment chamber, derivatived fuel storehouse and burning boiler room are set in shell body.The utility model achieves the clean burning of house refuse and the comprehensive utilization of waste resource, decreases floor space and the construction investment of garbage incinerating power plant simultaneously, for consumer waste innocent, resource, minimizing process provide technical conditions.
Description
Technical field
The utility model relates to a kind of garbage derivatived fuel preparation complexes integrated with burning electricity generation, belongs to field of garbage disposal.
Background technology
Burning disposal is one of main method of domestic rubbish disposal, and the heat energy that waste incineration produces can be used for generating, heat supply, has the advantage of minimizing, resource.But because the house refuse of China is commonly mixed collection, the complicated component of composting, wherein containing a large amount of masonry dregs, metal object, the non-combustible material such as glass ceramics, with rubbishes from cooking such as a large amount of gourd, fruit and vegetable residues and leftovers, the moisture content of composting reaches more than 50%, Lower heat value is only about 4000kJ/kg, therefore composting directly burns and there is combustion conditions instability, be difficult to reach the requirement of incineration temperature >=850 in burner hearth that " consumer waste incineration Environmental capacity standard " specify DEG C, the pollutants such as hypertoxic carcinogenic substance bioxin can be produced, it is combustion-supporting that composting burning existence need add fossil fuel, containing masonry in slag, metal, glass and uncombusted thing, be difficult to recycling, flying dust output is many, the problems such as association percolate and stink.For solving composting burning disposal Problems existing, national " planning of " 12 " national application of city life garbage harmless treatment Facilities Construction " proposes: " emphasis promotes the control of the clean, of burning bioxin, flying dust harmlessness disposing and utilization, percolate process, smell and controls, encourages to adopt application technology as the second resource process house refuse ".
Utility model content
In order to overcome the deficiency that composting burning disposal exists, the utility model provides a kind of garbage derivatived fuel and prepares complexes integrated with burning electricity generation, and it is that junk-free burns the control of, bioxin, percolate process, smell controls and the recycling of house refuse provides technical conditions.
The utility model realizes by the following technical solutions:
A kind of garbage derivatived fuel preparation complexes integrated with burning electricity generation comprise shell body, top pressure closure and garbage feeding door, and garbage feeding door is located at the side of shell body, and top pressure closure is positioned at the top of shell body; Wherein,
Sealing discharge bin, rubbish storage pond, refuse classification workshop, biochemical treatment chamber, derivatived fuel storehouse and burning boiler room are set in shell body;
Garbage feeding door is arranged on sealing discharge bin side, sealing discharge bin connects rubbish storage pond, rubbish storage pond connects refuse classification workshop by uniform feeder of garbage, and refuse classification workshop is by dregs conveyer connected with outer casing external body, by rubbish from cooking conveyer connection biochemical treatment chamber, by broken thing conveyer connection derivatived fuel storehouse; Biochemical treatment chamber connects derivatived fuel storehouse by outfeed belt conveyor, and derivatived fuel storehouse connects burning boiler room by boiler feed bucket;
Garbage bag breaking machine for accepting the rubbish from uniform feeder of garbage is set in refuse classification workshop, garbage bag breaking machine connects garbage conveyor, garbage conveyor connects cylinder round sifter, cylinder round sifter connects 3 outfeed belt conveyors: dregs conveyer dregs being delivered to shell body outside, rubbish from cooking is delivered to the rubbish from cooking conveyer of biochemical treatment chamber, and oversize is delivered to the oversize conveyer in derivatived fuel storehouse;
Arrange in burning boiler room for burn from the rubbish in derivatived fuel storehouse burning boiler and use burning boiler to produce steam to carry out the turbine LP rotors that operates.
Further, in shell body, air blast machine room is also set; Wherein, sealing discharge bin is positioned at the front side in rubbish storage pond, biochemical treatment chamber is positioned at the left side in rubbish storage pond, air blast machine room is positioned on the left of sealing discharge bin and the front side of biochemical treatment chamber, refuse classification workshop is positioned at the rear side of rubbish storage pond and biochemical treatment chamber, burning boiler room is positioned at the rear side in refuse classification workshop, and derivatived fuel position in storehouse is in the left side of both the rear side of biochemical treatment chamber and refuse classification workshop and burning boiler room.
Further, in shell body, air blast machine room is also set; Wherein, sealing discharge bin is positioned at the front side in rubbish storage pond, biochemical treatment chamber is positioned at the left side in rubbish storage pond, air blast machine room is positioned on the left of sealing discharge bin and the front side of biochemical treatment chamber, refuse classification workshop is positioned at the rear side of rubbish storage pond and biochemical treatment chamber, derivatived fuel position in storehouse is on the left of the rear side and refuse classification workshop of biochemical treatment chamber, and burning boiler room is positioned at the left side in air blast machine room, biochemical treatment chamber and derivatived fuel storehouse.
Further, between garbage conveyor and cylinder round sifter, magnetic separator is set.
Further, in cylinder round sifter, be provided with 8 ~ 25mm, 25 ~ 120mm screening section, according to the different particle diameter of composting different material, its point elected as dregs class, rubbish from cooking class and oversize.
Further, in refuse classification workshop, the discharge end of oversize conveyer connects the charging aperture of shear crusher, oversize is cut into the broken thing of 30 ~ 80mm × 100 ~ 300mm by shear crusher, the discharging opening of shear crusher connects broken thing conveyer, and the discharge end of broken thing conveyer stretches in derivatived fuel storehouse.
Further, biochemical treatment chamber is divided into one or more by partition wall, arrange bridge grabbing crane in biochemical treatment chamber.
Further, the top of biochemical treatment chamber arranges circular arch shape diaphragm seal top cover, and circular arch shape diaphragm seal top cover is provided with several hot wells towards the one side of biochemical treatment chamber, and hot well is connected with recycle-water pipeline; Bottom biochemical treatment chamber, air duct is set.
Further, air duct is communicated with air supply line, and air supply line is connected with air blast, and air blast is positioned at air blast machine room.
Further, derivatived fuel storehouse arranges grab bucket crane, and the material sent into by outfeed belt conveyor and broken thing conveyer is mixed into garbage derivatived fuel and sends in the boiler feed bucket of burning boiler by grab bucket crane.
Further, the flue gas that burning boiler produces is discharged by chimney after smoke eliminator process.
Further, the top of sealing discharge bin is provided with biological purification plant, and biological purification plant arranges intake stack, and the odorous gas in device is introduced in biological purification plant by intake stack, is discharged after chitosan fluid dressing degraded purified treatment by aiutage.
The profile of described garbage derivatived fuel preparation complexes integrated with burning electricity generation is cuboid or square.
Compared with prior art, the beneficial effects of the utility model are:
(1) the composting burning disposal mode from conventional is different, this garbage derivatived fuel preparation complexes integrated with burning electricity generation, by to the sorting classification of composting and biochemical treatment, the masonry dregs in rubbish, glass, the noncombustibleses such as metal object sort out and carry out resource recycling, biochemical processing is adopted to reduce msw water content, combustible in composting is made derivatived fuel, moisture content≤20% of derivatived fuel, Lower heat value >=12540kJ/kg, there is good combustibility, reach into incineration furnace garbage Lower heat value >=5500kJ/kg, the requirement of incineration temperature >=850 DEG C in burner hearth, do not need to add fossil fuel combustion-supporting, effectively control the pollutants such as bioxin to produce, solve composting from source and burn the deficiency existed, the clean and effective achieving house refuse heat energy utilizes.
(2) conventional spam burning electricity generation factory is the moisture by the mode of waste deposit 5 ~ 7 days drainings being reduced in rubbish, period can produce 10% ~ 15% percolate, percolate is high concentrated organic wastewater, containing polluters such as heavy metals, generally adopt " anaerobism+aerobic+ultrafiltration nanofiltration counter-infiltration " PROCESS FOR TREATMENT at present, treatment facility investment is large, and operating cost is high, and the sewage after process does not reach Treated sewage reusing standard.The utility model adopts biochemical processing to make rubbish fermentation, sweat produces biological high temperature, biological high temperature makes moisture in rubbish evaporate with steam-like, steam adopts condensing mode to reclaim, the condensate quality reclaimed is good, greening and industrial production can be directly used in, solve the investment of routine techniques treatment facility large, the problem that processing cost is high, water quality treatment is poor.
(3) the utility model is provided with biological purification plant process stink, carries out biodegradation purified treatment to the odorous gas produced in garbage processing procedure, solves the ubiquitous stink pollution problem of destructor plant.
(4) the rational layout setting of the utility model, can make the building usable floor area in garbage disposal workshop significantly reduce, make whole layout compact and reasonable more; Biological purification plant is arranged on two layers of sealing discharge bin simultaneously, saves floor space.
(5) because composting per ton about produces 0.5 ton of derivatived fuel, decrease the burning amount of rubbish, the corresponding discharge capacity decreasing flue gas and pollutant, improves the utilization ratio of rubbish heat energy, achieves energy-saving and emission-reduction.
To sum up, the utility model burns by composting is prepared into derivatived fuel again, the deficiency that conventional spam burning electricity generation mode exists is solved from source, achieve the clean burning of house refuse and the comprehensive utilization of waste resource, decrease floor space and the construction investment of garbage incinerating power plant, for consumer waste innocent, resource, minimizing process provide technical conditions simultaneously.
Accompanying drawing illustrates:
Fig. 1 is front view of the present utility model,
Fig. 2 is the A-A direction view of Fig. 1 in embodiment 1,
Fig. 3 is the B-B direction view of Fig. 2,
Fig. 4 is the C-C direction view of Fig. 2,
Fig. 5 is the D-D direction view of Fig. 2,
Fig. 6 is the A-A view of Fig. 1 in embodiment 2;
Number in figure:
1, shell body; 2, top pressure closure; 3, garbage feeding door; 4, discharge bin is sealed; 5, rubbish storage pond; 6, biochemical treatment chamber; 7, outfeed belt conveyor; 8, air blast machine room; 9, refuse classification workshop; 10 burning boiler rooms; 11, derivatived fuel storehouse; 12, boiler feed bucket; 13, uniform feeder of garbage; 14, garbage bag breaking machine; 15, garbage conveyor; 16, cylinder round sifter; 17, magnetic separator; 18, dregs conveyer; 19, rubbish from cooking conveyer; 20, oversize conveyer; 21, shear crusher; 22, broken thing conveyer; 23, air duct; 24, bridge grabbing crane; 25, circular arch shape diaphragm seal top cover; 26, hot well; 27, grab bucket crane; 28, biological purification plant; 29, intake stack; 30, chitosan fluid dressing; 31, aiutage; 32, burning boiler; 33, turbine LP rotors; 34, smoke eliminator; 35, chimney.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
Embodiment 1
As shown in Figure 1, the profile of this garbage derivatived fuel preparation complexes integrated with burning electricity generation is cuboid or square, comprise shell body 1 and top pressure closure 2, arrange garbage feeding door 3 in a side of shell body 1, the side along garbage feeding door 3 is risen, be arranged in parallel air blast machine room 8 successively, biochemical treatment chamber 6, refuse classification workshop 9, burning boiler room 10, in the one end in refuse classification workshop 9 and burning boiler room 10, derivatived fuel storehouse 11 is set.
As shown in Figure 2, one side of sealing discharge bin 4 arranges garbage feeding door 3, cram packer enters sealing discharge bin 4 by garbage feeding door 3, rubbish is discharged into and the rubbish storage pond 5 sealing discharge bin 4 and be communicated with, biochemical treatment chamber 6 is divided into one or more by partition wall, one end contrary with rubbish storage pond 5 in biochemical treatment chamber 6 sets out material conveyer 7.Uniform feeder of garbage 13 is set in rubbish storage pond 5, by bridge grabbing crane 24, rubbish is fed uniform feeder of garbage 13; The discharge end of uniform feeder of garbage 13 connects the charging aperture of garbage bag breaking machine 14, and composting unloads to garbage conveyor 15 by the discharging opening of garbage bag breaking machine 14 after broken bag; The discharge end of garbage conveyor 15 connects the charging aperture of cylinder round sifter 16, and arrange magnetic separator 17 at the discharge end place of garbage conveyor 15, the metal object in rubbish sorts out by magnetic separator 17.Be provided with 8 ~ 25mm, 25 ~ 120mm screening section in cylinder round sifter 16, according to the different particle diameter of composting different material, its point elected as the oversizes such as dregs class, rubbish from cooking class and plastics, fabric, waste paper.Cylinder round sifter 16 is provided with 3 discharging openings, and wherein dregs discharging opening is connected with dregs conveyer 18, and the discharge end of dregs conveyer 18 is arranged on outside shell body 1; Rubbish from cooking discharging opening is connected with rubbish from cooking conveyer 19, and the discharge end of rubbish from cooking conveyer 19 stretches in biochemical treatment chamber 6; Oversize discharging opening is connected with oversize conveyer 20, the discharge end of oversize conveyer 20 is connected with the charging aperture of shear crusher 21, oversize is cut into the broken thing of 30 ~ 80mm × 100 ~ 300mm by shear crusher 21, the discharging opening of shear crusher 21 is connected with broken thing conveyer 22, the discharge end of broken thing conveyer 22 stretches in derivatived fuel storehouse 11, the boiler feed bucket 12 of burning boiler 32 is arranged in derivatived fuel storehouse 11, arranges burning boiler 32 and turbine LP rotors 33 in burning boiler room 10.
As shown in Figure 3, arrange air duct 23 bottom biochemical treatment chamber 6, air duct 23 is communicated with air supply line, and air supply line is connected with air blast, and air blast is positioned at air blast machine room.The top of biochemical treatment chamber 6 arranges bridge grabbing crane 24, rubbish from cooking is distributed in biochemical treatment chamber 6 by bridge grabbing crane 24, air duct 23 is to rubbish stockpile air feed, rubbish from cooking sweat produces 65 DEG C ~ 75 DEG C biological high temperature, moisture in rubbish is evaporated with steam-like, circular arch shape diaphragm seal top cover 25 is set at the top of biochemical treatment chamber 6, circular arch shape diaphragm seal top cover 25 is provided with several hot wells 26 towards the one side of biochemical treatment chamber 6, the steam that rubbish from cooking produces rises to circular arch shape diaphragm seal top cover 25 place, biochemical treatment chamber 6 top, water droplet is condensed under action of thermal difference, water droplet is collected by hot well 26, hot well 26 is connected with recycle-water pipeline, recycle.The biochemical cycle of rubbish from cooking is 6 ~ 15 days, the Material control that delivers from godown moisture content≤20%, be the combustible material such as humus, asphalitine at the microbial action remaining garbage conversion that cooks, rubbish from cooking after biochemical treatment feeds outfeed belt conveyor 7 by bridge grabbing crane 24, and outfeed belt conveyor 7 is sent in derivatived fuel storehouse 11.
As shown in Figure 4, derivatived fuel storehouse 11 arranges grab bucket crane 27, the material sent into by outfeed belt conveyor 7 and broken thing conveyer 22 is mixed into garbage derivatived fuel and sends in the boiler feed bucket 12 of burning boiler 32 by grab bucket crane 27, burning disposal is carried out by burning boiler 32, the steam that burning boiler 32 produces is sent into turbine LP rotors 33 and is generated electricity, and the flue gas that burning boiler 32 produces is discharged by chimney 35 after smoke eliminator 34 processes.
As shown in Figure 5, the top of sealing discharge bin 4 is provided with biological purification plant 28, biological purification plant 28 arranges intake stack 29, and the odorous gas in device is introduced in biological purification plant 28 by intake stack 29, is discharged after chitosan fluid dressing 30 degrades purified treatment by aiutage 31.
Concrete layout is: sealing discharge bin 4 is positioned at the front side in rubbish storage pond 5, biochemical treatment chamber 6 is positioned at the left side in rubbish storage pond 5, air blast machine room 8 is positioned on the left of sealing discharge bin 4 and the front side of biochemical treatment chamber 6, refuse classification workshop 9 is positioned at the rear side of rubbish storage pond 5 and biochemical treatment chamber 6, burning boiler room 10 is positioned at the rear side in refuse classification workshop 9, and derivatived fuel storehouse 11 is positioned at the rear side of biochemical treatment chamber 6 and refuse classification workshop 9 and the left side both burning boiler room 10.
Embodiment 2
Except following technical characteristic, all the other are with embodiment 1;
As shown in Figure 6, burning boiler room 10 is connected with the lateral vertical in air blast machine room 8, biochemical treatment chamber 6, derivatived fuel storehouse 11, and the boiler feed bucket 12 of burning boiler 32 is arranged in derivatived fuel storehouse 11.
Concrete layout is: also arrange air blast machine room 8 in shell body 1; Wherein, sealing discharge bin 4 is positioned at the front side in rubbish storage pond 5, biochemical treatment chamber 6 is positioned at the left side in rubbish storage pond 5, air blast machine room 8 is positioned on the left of sealing discharge bin 4 and the front side of biochemical treatment chamber 6, refuse classification workshop 9 is positioned at the rear side of rubbish storage pond 5 and biochemical treatment chamber 6, on the left of the rear side that derivatived fuel storehouse 11 is positioned at biochemical treatment chamber 6 and refuse classification workshop 9, burning boiler room 10 is positioned at the left side in air blast machine room 8, biochemical treatment chamber 6 and derivatived fuel storehouse 11.
Above-described embodiment is only be described preferred embodiment of the present utility model; not scope of the present utility model is limited; under the prerequisite not departing from the utility model design spirit; the various distortion that those of ordinary skill in the art make the technical solution of the utility model and improvement, all should fall in protection domain that the utility model claims determine.
Claims (12)
1. garbage derivatived fuel preparation complexes integrated with burning electricity generation comprise shell body (1), top pressure closure (2) and garbage feeding door (3), garbage feeding door (3) is located at the side of shell body (1), and top pressure closure (2) is positioned at the top of shell body (1); It is characterized in that:
Sealing discharge bin (4), rubbish storage pond (5), refuse classification workshop (9), biochemical treatment chamber (6), derivatived fuel storehouse (11) and burning boiler room (10) are set in shell body (1);
Garbage feeding door (3) is arranged on sealing discharge bin (4) side, sealing discharge bin (4) connects rubbish storage pond (5), rubbish storage pond (5) connects refuse classification workshop (9) by uniform feeder of garbage (13), and refuse classification workshop (9) are by dregs conveyer (18) connected with outer casing body (1) outside, by rubbish from cooking conveyer (19) connection biochemical treatment chamber (6), by broken thing conveyer (22) connection derivatived fuel storehouse (11); Biochemical treatment chamber (6) connects derivatived fuel storehouse (11) by outfeed belt conveyor (7), and derivatived fuel storehouse (11) connect burning boiler room (10) by boiler feed bucket (12);
Arrange in refuse classification workshop (9) and be used for accepting the garbage bag breaking machine (14) from the rubbish of uniform feeder of garbage (13), garbage bag breaking machine (14) connects garbage conveyor (15), garbage conveyor (15) connects cylinder round sifter (16), cylinder round sifter (16) connects 3 outfeed belt conveyors: dregs is delivered to the dregs conveyer (18) that shell body (1) is outside, rubbish from cooking is delivered to the rubbish from cooking conveyer (19) of biochemical treatment chamber (6), and oversize is delivered to the oversize conveyer (20) in derivatived fuel storehouse (11),
Burning boiler room (10) is interior arranges the turbine LP rotors (33) being used for burning and carrying out from the burning boiler (32) of the rubbish of derivatived fuel storehouse (11) and use burning boiler (32) production steam operating.
2. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, is characterized in that: also arrange air blast machine room (8) in shell body (1), wherein, sealing discharge bin (4) is positioned at the front side of rubbish storage pond (5), biochemical treatment chamber (6) is positioned at the left side of rubbish storage pond (5), air blast machine room (8) is positioned at the front side of sealing discharge bin (4) left side and biochemical treatment chamber (6), refuse classification workshop (9) is positioned at the rear side of rubbish storage pond (5) and biochemical treatment chamber (6), burning boiler room (10) is positioned at the rear side of refuse classification workshop (9), derivatived fuel storehouse (11) is positioned at the two left side of the rear side of biochemical treatment chamber (6) and refuse classification workshop (9) and burning boiler room (10).
3. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, is characterized in that: also arrange air blast machine room (8) in shell body (1), wherein, sealing discharge bin (4) is positioned at the front side of rubbish storage pond (5), biochemical treatment chamber (6) is positioned at the left side of rubbish storage pond (5), air blast machine room (8) is positioned at the front side of sealing discharge bin (4) left side and biochemical treatment chamber (6), refuse classification workshop (9) is positioned at the rear side of rubbish storage pond (5) and biochemical treatment chamber (6), derivatived fuel storehouse (11) is positioned at rear side and refuse classification workshop (9) left side of biochemical treatment chamber (6), burning boiler room (10) is positioned at air blast machine room (8), the left side of biochemical treatment chamber (6) and derivatived fuel storehouse (11).
4. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, is characterized in that: arrange magnetic separator (17) between garbage conveyor (15) and cylinder round sifter (16).
5. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, it is characterized in that: in cylinder round sifter (16), be provided with 8 ~ 25mm, 25 ~ 120mm screening section, according to the different particle diameter of composting different material, its point is elected as dregs class, rubbish from cooking class and oversize.
6. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, it is characterized in that: in refuse classification workshop (9), the discharge end of oversize conveyer (20) connects the charging aperture of shear crusher (21), oversize is cut into the broken thing of 30 ~ 80mm × 100 ~ 300mm by shear crusher (21), the discharging opening of shear crusher (21) connects broken thing conveyer (22), and the discharge end of broken thing conveyer (22) stretches in derivatived fuel storehouse (11).
7. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, it is characterized in that: biochemical treatment chamber (6) is divided into by partition wall one or more, bridge grabbing crane (24) is set in biochemical treatment chamber.
8. according to the arbitrary described garbage derivatived fuel preparation of claim 1-7 complexes integrated with burning electricity generation, it is characterized in that: the top of biochemical treatment chamber (6) arranges circular arch shape diaphragm seal top cover (25), circular arch shape diaphragm seal top cover (25) is provided with several hot wells (26) towards the one side of biochemical treatment chamber (6), and hot well (26) is connected with recycle-water pipeline; Biochemical treatment chamber (6) bottom arranges air duct (23).
9. garbage derivatived fuel preparation according to claim 8 complexes integrated with burning electricity generation, it is characterized in that: air duct (23) is communicated with air supply line, air supply line is connected with air blast, and air blast is positioned at air blast machine room (8).
10. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, it is characterized in that: derivatived fuel storehouse (11) arrange grab bucket crane (27), the material sent into by outfeed belt conveyor (7) and broken thing conveyer (22) is mixed into garbage derivatived fuel and sends in the boiler feed bucket (12) of burning boiler (32) by grab bucket crane (27).
11. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, is characterized in that: the flue gas that burning boiler (32) produces is discharged by chimney (35) after smoke eliminator (34) process.
12. garbage derivatived fuel preparation according to claim 1 complexes integrated with burning electricity generation, it is characterized in that: the top of sealing discharge bin (4) is provided with biological purification plant (28), biological purification plant (28) arranges intake stack (29), odorous gas in device is introduced in biological purification plant (28) by intake stack (29), is discharged after chitosan fluid dressing (30) degraded purified treatment by aiutage (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520223944.5U CN204611781U (en) | 2015-04-14 | 2015-04-14 | Garbage derivatived fuel preparation complexes integrated with burning electricity generation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520223944.5U CN204611781U (en) | 2015-04-14 | 2015-04-14 | Garbage derivatived fuel preparation complexes integrated with burning electricity generation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204611781U true CN204611781U (en) | 2015-09-02 |
Family
ID=53964339
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520223944.5U Expired - Fee Related CN204611781U (en) | 2015-04-14 | 2015-04-14 | Garbage derivatived fuel preparation complexes integrated with burning electricity generation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204611781U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791802A (en) * | 2015-04-14 | 2015-07-22 | 李轼 | Integrated set device for garbage derived fuel preparing and incinerating power generation |
-
2015
- 2015-04-14 CN CN201520223944.5U patent/CN204611781U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791802A (en) * | 2015-04-14 | 2015-07-22 | 李轼 | Integrated set device for garbage derived fuel preparing and incinerating power generation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102070308B (en) | Device technology configuration method for treating house refuses by using rotary cement kiln | |
| CN103322574B (en) | Utilize method and the treatment system thereof of tunnel kiln brick sintering production line cooperative disposal house refuse | |
| CN105032884B (en) | Cement rotary kiln collaboration processes house refuse and energy comprehensive utilization system and method | |
| CN102322642A (en) | Sludge drying and incinerating system on basis of incineration of waste grate furnace and treatment method thereof | |
| CN204544958U (en) | Cement rotary kiln associated treatment house refuse and energy comprehensive utilization system | |
| CN103834452B (en) | The equipment of fuel is produced by domestic refuse | |
| CN101216176A (en) | Garbage burning processing method and device capable of accomplishing dioxin and dust zero discharge | |
| CN101618954B (en) | Process for processing municipal domestic waste by cement rotary kiln | |
| CN103626409B (en) | Method and device for treatment in feeding household garbage into cement kiln in three routes | |
| CN106966618A (en) | A kind of method of cement kiln synergic processing house refuse | |
| CN102980193A (en) | Garbage incinerating exhaust gas using environment-friendly and energy-saving device | |
| CN101612629A (en) | A kind of city house refuse treatment method and device thereof | |
| CN102061181A (en) | Incineration-free low-temperature waste carbonization furnace and comprehensive utilization thereof | |
| CN107490008A (en) | A kind of domestic garbage pyrolysis gasification process of scale | |
| CN205402733U (en) | Domestic waste and/or industrial waste's processing production line | |
| CN102889597A (en) | Process and system for domestic garbage incineration waste heat drying pretreatment | |
| CN102950139A (en) | Novel system for high-energy conversion harmless recycling treatment on municipal domestic waste | |
| CN102049407A (en) | Municipal bulk solid waste treatment industrial symbiotic system | |
| CN1296150C (en) | Process for treating urban house refuse using dry method cement production system | |
| CN204276506U (en) | A kind of dry method cement rotary kiln associated treatment house refuse system | |
| CN102344259A (en) | Environmental-protection and energy-saving garbage incineration and waste gas utilization device | |
| CN207514918U (en) | A kind of rubbish cooperates with incinerating and treating device with semi-dry sludge | |
| CN204611781U (en) | Garbage derivatived fuel preparation complexes integrated with burning electricity generation | |
| CN203582743U (en) | Three-way kiln inlet treatment device for cement kiln household garbage | |
| CN104791802A (en) | Integrated set device for garbage derived fuel preparing and incinerating power generation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150902 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |