CN205536962U - Living beings pellet fuel drying device - Google Patents
Living beings pellet fuel drying device Download PDFInfo
- Publication number
- CN205536962U CN205536962U CN201620080529.3U CN201620080529U CN205536962U CN 205536962 U CN205536962 U CN 205536962U CN 201620080529 U CN201620080529 U CN 201620080529U CN 205536962 U CN205536962 U CN 205536962U
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- pipe
- shell
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- flowline
- heater
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Abstract
The utility model provides a living beings pellet fuel drying device, includes cylinder drying -machine, install wet material conveyor on the drying -machine feed inlet, install on the drying -machine discharge gate drier conveyor and cyclone and with the draught fan of cyclone intercommunication, still include hot -blast conveyor and fuel gas supply device, the utility model provides a living beings pellet fuel drying device is isolated the back at the dust by cyclone, need not remove dust, directly regards as fuel to burn in the dust, and then can not fly away the dust in the air, has also practiced thrift manual work and equipment cost.
Description
Technical field
The utility model relates to a kind of processing unit (plant), particularly to a kind of biomass granule fuel drying unit.
Background technology
Biomass granule fuel, also known as biomass molding fuel, it it is a kind of application waste wood, straw, sawdust and bark are as raw material, through selecting materials, pulverize, mixing, dry the techniques such as extruding, make a kind of incendivity, graininess cleaning fuel, it it is the national a kind of new cleaning fuel advocated energetically, in early stage baking operation, need to connect a cyclone separator at the discharge end for dry machine, after the dust that cyclone separator is separated carries out dedusting by bag-type dust or water mist dust-removing, isolated dust is concentrated and is poured into hearth combustion or makes bio-feritlizer, during transhipment dust, dust easily flies away in atmosphere, cause environmental pollution, and need extra one workman of arrangement to go to process dust, add cost of labor, therefore this problem must solve.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of biomass granule fuel drying unit, after dust is separated by cyclone separator, it is made without dedusting, directly dust is fallen as fuel combustion, and then will not dust be flown away in atmosphere, do not pollute the environment, also save artificial and equipment cost simultaneously.
In order to solve the problems referred to above, the technical solution of the utility model is: a kind of biomass granule fuel drying unit, the wet feed conveying device that including roller dryer, is arranged on dryer feeding mouth, the siccative conveying device being arranged on dryer discharging opening and cyclone separator and the air-introduced machine connected with cyclone separator, also include hot-blast conveying appliance and gas feeder
Described hot-blast conveying appliance includes shell, shell is connected with air-introduced machine by ash inlet tube, it is provided with heater in the enclosure, a blast pipe and discharge pipe have been respectively communicated with it at the two ends of heater, discharge pipe connects through shell with dryer, and blast pipe is in communication with the outside through shell, is provided with air inlet fan on blast pipe, connecting a cement output tank on the shell of one end relative with ash inlet tube, heater is positioned at the lower section of ash inlet tube；
Gas feeder includes oil tank, oil tank is communicated with air inlet pipe, flowline and oil filler, one end of flowline is positioned at ash inlet tube, the other end of flowline is positioned at the bottom of oil tank, connect at the mouth of pipe of one end that flowline is positioned at ash inlet tube and have an atomizer, the ash inlet tube outside atomizer is provided with cover of becalming；
Being provided with a pulse igniter on shell, the firing tip of pulse igniter is positioned at the mouth of pipe of flowline one end.
Further, heater includes two wind-collecting covers, described wind-collecting cover has the front end of circle and square rear end, the end face of rear end is provided with one piece of orifice plate, orifice plate is provided with multiple through hole, described heater also includes the many tubules identical with number of openings on orifice plate, two wind-collecting covers are connected at the two ends of each tubule by each through hole on respective orifice plate, the front end of one of them wind-collecting cover connects on the mouth of pipe of discharge pipe one end, and the front end of another one wind-collecting cover connects on the mouth of pipe of blast pipe one end.
Further, in ash inlet tube, multiple spoiler it is installed with.
Further, in the enclosure, the one end near cement output tank is provided with polylith deflector.
The beneficial effects of the utility model are: cyclone separator by dust separation out after, burn in dust can be transported to housing by ash inlet tube, the heat of the generation of burning is transported in dryer by heater, thermal source is provided for dryer, and then the dust without separating exposes in atmosphere, do not pollute the environment, and can external cleaner, reduce production cost and cost of labor.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings the utility model is described further:
Fig. 1 is structural representation of the present utility model,
Fig. 2 is the structural representation of the utility model hot-blast conveying appliance and gas feeder,
Fig. 3 is the perspective view of the utility model heater.
Fig. 4 is the close-up schematic view in Fig. 2 at A.
Detailed description of the invention
If Fig. 1 is to shown in 3, a kind of biomass granule fuel drying unit, the wet feed conveying device 2 that including roller dryer 1, is arranged on dryer 1 charging aperture, the siccative conveying device 3 being arranged on dryer 1 discharging opening and cyclone separator 4 and the air-introduced machine 5 connected with cyclone separator 4, wet feed conveying device 2 and siccative conveying device 3 can be conveying worms, the heavy phase port of cyclone separator 4 is provided with a Blowing stopper be connected with siccative conveyer
Also include hot-blast conveying appliance 6 and gas feeder 7, described hot-blast conveying appliance 6 includes shell 601, shell 601 is connected with air-introduced machine 5 by ash inlet tube 8, heater 13 it is provided with in shell 601, a blast pipe 10 and discharge pipe 11 it has been respectively communicated with at the two ends of heater 13, discharge pipe 11 connects through shell 601 with dryer 1, blast pipe 10 is in communication with the outside through shell 601, blast pipe 10 is provided with air inlet fan 12, connecting a cement output tank 9 on the shell 601 of one end relative with ash inlet tube 8, heater 13 is positioned at the lower section of ash inlet tube 8；
Gas feeder 7 includes oil tank 701, oil tank 701 is communicated with air inlet pipe 702, flowline 703 and oil filler 705, one end of flowline 703 is positioned at ash inlet tube 8, the other end of flowline 703 is positioned at the bottom of oil tank 701, connect at the mouth of pipe of one end that flowline 703 is positioned at ash inlet tube 8 and have an atomizer 704, on ash inlet tube 8 outside atomizer 704, cover 707 of becalming is installed, cover 707 of becalming is possible to prevent from ash inlet tube 8 air flowed out to be put out from root by the flame lighted, oil filler 705 is made up of oil filling pipe and the sealing lid of connection oil tank 701, flowline 703 can choose to install a valve 706.
Being provided with a pulse igniter 14 on shell 601, the firing tip of pulse igniter 14 is positioned at the mouth of pipe of flowline 703 one end.
Further, heater 13 includes two wind-collecting covers 132, described wind-collecting cover 132 has the front end of circle and square rear end, the end face of rear end is provided with one piece of orifice plate 133, orifice plate 133 is provided with multiple through hole, described heater 13 also includes the many tubules 131 identical with number of openings on orifice plate 133, two wind-collecting covers 132 are connected at the two ends of each tubule 131 by each through hole on respective orifice plate 133, the front end of one of them wind-collecting cover 132 connects on the mouth of pipe of discharge pipe 11 one end, the front end of another one wind-collecting cover 132 connects on the mouth of pipe of blast pipe 10 one end, tubule 131 expands heating surface, it is more favorable for absorbing heat.
Further, being installed with multiple spoiler 801 in ash inlet tube 8, the effect of spoiler 801 is the air-flow that quick washing comes to be slowed down or be changed to blow direction, prevents the too fast blowout of dust, and affects burning.
Further, being provided with polylith deflector 602 in shell 601, near one end of cement output tank 9, the dust ashes after deflector 602 is beneficial to burning are discharged, and will not be deposited in shell 601.
The course of work of the present utility model, is first turned on oil filler 705, oil filler 705 fill kerosene in oil tank 701, ensure that the height of kerosene covers the mouth of pipe of flowline 703, then oil filler 705 is sealed, in air inlet pipe 702, be passed through pressure-air, close the valve 706 on flowline 703；nullIt is then turned on air inlet fan 12、Roller dryer 1、Air-introduced machine 5、Wet feed conveying device 2 and siccative conveying device 3，Open valve 706 while opening the said equipment，Pressure-air compressing kerosene enters in flowline 703，Spray from atomizer 704 again，At unbalanced pulse igniter 14，The coal gas aerosol sprayed by atomizer 704 lights formation flame，Tubule 131 is toasted by flame，Hot gas is there is in tubule 131 after heating，Hot-air is blown in dryer 1 by discharge pipe 11，Material in dryer 1 is carried out preliminary drying，After drying materials，During after drying, material enters back into cyclone separator 4，Dust is pumped in ash inlet tube 8 by cyclone separator 4 by air-introduced machine 5，Air with dust is made wind speed slow down by the obstruct of spoiler 801 in ash inlet tube 8，The dust that speed slows down can receive the burning of gas-fired flame at the mouth of pipe of ash inlet tube 8，Form bigger flame tubule 131 is toasted，Improve the air themperature in tubule 131，And can persistently tubule 131 be toasted during persistently charging，And be blown in dryer 1 with the form of hot-air，Ashes and gas that dust combustion is formed are discharged by cement output tank 9.
The utility model will be after dust be separated by cyclone separator, it is not necessary to carries out dedusting, is directly fallen as fuel combustion by dust, and then will not fly away in atmosphere by dust, does not pollutes the environment, and also saves artificial and equipment cost simultaneously.
Claims (4)
1. a biomass granule fuel drying unit, the wet feed conveying device (2) that including roller dryer (1), is arranged on dryer (1) charging aperture, the siccative conveying device (3) being arranged on dryer (1) discharging opening and cyclone separator (4) and the air-introduced machine (5) connected with cyclone separator (4), it is characterized in that: also include hot-blast conveying appliance (6) and gas feeder (7)
Described hot-blast conveying appliance (6) includes shell (601), shell (601) is connected with air-introduced machine (5) by ash inlet tube (8), heater (13) it is provided with in shell (601), a blast pipe (10) and a discharge pipe (11) it has been respectively communicated with at the two ends of heater (13), discharge pipe (11) connects through shell (601) with dryer (1), blast pipe (10) is in communication with the outside through shell (601), blast pipe (10) is provided with air inlet fan (12), shell (601) piece cement output tank (9) of upper connection, heater (13) is positioned at the lower section of ash inlet tube (8)；
Gas feeder (7) includes oil tank (701), oil tank (701) is communicated with air inlet pipe (702), flowline (703) and oil filler (705), one end of flowline (703) is positioned at ash inlet tube (8), the other end of flowline (703) is positioned at the bottom of oil tank (701), connect at the mouth of pipe of one end that flowline (703) is positioned at ash inlet tube (8) and have an atomizer (704), atomizer (704) ash inlet tube (8) outward is provided with cover of becalming (707)；
Being provided with a pulse igniter (14) on shell (601), the firing tip of pulse igniter (14) is positioned at the mouth of pipe of flowline (703) one end.
A kind of biomass granule fuel drying unit the most according to claim 1, it is characterized in that: heater (13) includes two wind-collecting covers (132), described wind-collecting cover (132) has the front end of circle and square rear end, the end face of rear end is provided with one piece of orifice plate (133), orifice plate (133) is provided with multiple through hole, described heater (13) also includes the tubule (131) that many number of openings upper with orifice plate (133) are identical, two wind-collecting covers (132) are connected at the two ends of each tubule (131) by each through hole on respective orifice plate (133), the front end of one of them wind-collecting cover (132) connects on the mouth of pipe of discharge pipe (11) one end, the front end of another one wind-collecting cover (132) connects on the mouth of pipe of blast pipe (10) one end.
A kind of biomass granule fuel drying unit the most according to claim 1, it is characterised in that: in ash inlet tube (8), it is installed with multiple spoiler (801).
A kind of biomass granule fuel drying unit the most according to claim 1, it is characterised in that: in shell (601), it is provided with polylith deflector (602) near one end of cement output tank (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620080529.3U CN205536962U (en) | 2016-01-27 | 2016-01-27 | Living beings pellet fuel drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620080529.3U CN205536962U (en) | 2016-01-27 | 2016-01-27 | Living beings pellet fuel drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205536962U true CN205536962U (en) | 2016-08-31 |
Family
ID=56771132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620080529.3U Expired - Fee Related CN205536962U (en) | 2016-01-27 | 2016-01-27 | Living beings pellet fuel drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205536962U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108917329A (en) * | 2018-05-30 | 2018-11-30 | 江苏农牧科技职业学院 | A kind of chicken manure fast-drying device |
| CN112033110A (en) * | 2020-09-29 | 2020-12-04 | 江苏沃尔夫智能科技有限公司 | River sand drying device |
| CN114704848A (en) * | 2022-03-28 | 2022-07-05 | 西安热工研究院有限公司 | Coupling power generation system for drying biomass fuel by using low-temperature waste heat of thermal power generating unit |
-
2016
- 2016-01-27 CN CN201620080529.3U patent/CN205536962U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108917329A (en) * | 2018-05-30 | 2018-11-30 | 江苏农牧科技职业学院 | A kind of chicken manure fast-drying device |
| CN112033110A (en) * | 2020-09-29 | 2020-12-04 | 江苏沃尔夫智能科技有限公司 | River sand drying device |
| CN114704848A (en) * | 2022-03-28 | 2022-07-05 | 西安热工研究院有限公司 | Coupling power generation system for drying biomass fuel by using low-temperature waste heat of thermal power generating unit |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20190127 |