CN106123517A - A kind of biological particles drying process device - Google Patents
A kind of biological particles drying process device Download PDFInfo
- Publication number
- CN106123517A CN106123517A CN201610436062.6A CN201610436062A CN106123517A CN 106123517 A CN106123517 A CN 106123517A CN 201610436062 A CN201610436062 A CN 201610436062A CN 106123517 A CN106123517 A CN 106123517A
- Authority
- CN
- China
- Prior art keywords
- biological particles
- fixed
- drying
- breather
- gas tank
- 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.)
- Granted
Links
- 238000001035 drying Methods 0.000 title claims abstract description 75
- 239000002245 particle Substances 0.000 title claims abstract description 32
- 239000011148 porous material Substances 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims abstract description 5
- 230000001939 inductive effect Effects 0.000 claims description 10
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 230000001737 promoting effect Effects 0.000 abstract description 3
- 239000002028 Biomass Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000002360 explosive Substances 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000010902 straw Substances 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 239000002154 agricultural waste Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
- F26B9/08—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers including agitating devices, e.g. pneumatic recirculation arrangements
- F26B9/082—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers including agitating devices, e.g. pneumatic recirculation arrangements mechanically agitating or recirculating the material being dried
- F26B9/085—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers including agitating devices, e.g. pneumatic recirculation arrangements mechanically agitating or recirculating the material being dried moving the material in a substantially vertical sense using conveyors or agitators, e.g. screws or augers with vertical axis, which are positioned inside the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of biological particles drying process device, including drying baker and the drying device being sequentially arranged in drying baker, have outlet slot bottom drying baker, outlet slot is provided with material collecting box；Drying device includes mounting seat and the remittance gas tank being fixed in mounting seat, and the gas tank opposite side that converges is fixed with roundabout type breather, and breather upper surface has some main pores, is arranged above some conducting strips, and conducting strip is arranged above web plate；Remittance gas tank both sides are provided with gas cylinder, are connected with each other by flexible pipe between the gas cylinder of adjacent remittance gas tank；In drying baker, drying device lower surface position is provided with gag lever post.The present invention can carry out efficient drying to biological particles, the index of aridity is largely increased, avoid because being dried the pollution that thoroughly air is not caused by after-combustion, decrease the humidity of biological particles, storing and transportation is being difficult to mouldy, win considerable economic benefit for enterprise, be suitable for promoting and using.
Description
Technical field
The invention belongs to biomass field, particularly relate to a kind of biological particles drying process device.
Background technology
Biological particles has begun to more and more be applied to industry and the people as a kind of reproducible environment-friendly type energy
With field, but owing to utilizing crop straws for producing biomass fuel technology slower development, cause downstream with can industry (work
Industry, civilian etc.) Arrested Development of technology, the raw material such as major part straw is also used to agricultural or is incinerated, the most dirty
Contaminated environment waste again the agricultural wastes such as resource, only small part straw be used to make biomass fuel, and due to
The problem of technology, does not form large-area mass production.
At present, biological particles is because high humidity, the most mouldy, is not easy to transport and stores.Although the most also having not
Few biomass granulation machine drying device, but general drying device drying efficiency is low, and quality is unstable, and dried gas is arranged
There is solid waste pollution in putting, and large-scale drying equipment exists structure complexity, it is difficult to manufacture the deficiency high with cost.
Summary of the invention
It is an object of the invention to the problem above overcoming prior art to exist, it is provided that a kind of biological particles dried
Device, carries out efficient drying to biological particles, it is simple to transports and stores, and reduces Air-pollution From Combustion, low cost of manufacture.
For realizing above-mentioned technical purpose, reaching above-mentioned technique effect, the present invention is achieved through the following technical solutions:
A kind of biological particles drying process device, including drying baker and the drying device being sequentially arranged in drying baker,
Have outlet slot bottom drying baker, outlet slot is provided with material collecting box；
Described drying device includes mounting seat and the remittance gas tank being fixed in mounting seat, and the gas tank opposite side that converges is fixed with roundabout
Type breather, breather upper surface has some main pores, is arranged above some conducting strips, and conducting strip is arranged above net
Plate；
Described remittance gas tank both sides are provided with gas cylinder, are connected with each other by flexible pipe between the gas cylinder of adjacent remittance gas tank；
In described drying baker, drying device lower surface position is provided with gag lever post.
Further, described mounting seat two ends are fixed with rotating shaft, and shaft end is fixed with rotating disk, can carry out drying device
Arbitrarily rotate regulation, the biological particles in upper drying device above is delivered on the drying device of lower section, further
It is dried.
Further, described remittance gas tank is provided with notch near breather side, and breather two-port embeds and is arranged on groove
In Kou.
Further, described mounting seat side is fixed with card case, and embedding is arranged on remittance gas tank side.
Further, described breather two ends are fixed with side plate case so that biomass upper strata granule is the most effectively done
Dry, in hgher efficiency.
Further, being provided with fixed station in the middle of described side plate case medial surface, fixed station inner surface equidistant arrangement is distributed
Having some draw-in grooves, be fixed with conducting strip in draw-in groove successively, conducting strip has match with breather U-shaped near breather side
Groove, side plate case medial surface upper end has some auxiliary air vents, and lower end is fixed with inducing QI case, and breather has near inducing QI case side
Air guide port, described inducing QI case embeds and is arranged in air guide port.
Further, described drying baker inboard width, equal to the length at mounting seat two ends, prevents top in dry run
Biological particles is scattering on the drying device of lower floor.
Further, the mutual spacing of described main pore is 3～5cm, and aperture is 5～10mm, and drying efficiency is more preferably.
Further, described side plate case and side plate case mutual spacing are equal to the length at mounting seat two ends.
Further, described web plate is identical with conducting strip thickness and is 3～5mm so that web plate and the heat conduction of conducting strip
Efficiency is more preferable.
The invention has the beneficial effects as follows:
The present invention can carry out efficient drying to biological particles, and by arranging the drying device of multilamellar, the index of aridity obtains
It is greatly improved, it is to avoid because being dried the pollution that thoroughly air is caused by after-combustion, decrease the humidity of biological particles,
Storing and be difficult to mouldy in transportation, whole apparatus structure is simple, cheap for manufacturing cost, has won considerable economy for enterprise
Benefit, is suitable for promoting and using.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing a further understanding of the present invention, constitutes the part of the application, this
Bright schematic description and description is used for explaining the present invention, is not intended that inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the partial structurtes schematic diagram of the present invention；
Fig. 3 is the partial structurtes explosive view of the present invention；
Fig. 4 is the enlarged drawing in Fig. 3 at A；
Fig. 5 is the partial structurtes schematic diagram of the present invention；
Fig. 6 is the partial structurtes explosive view of the present invention；
Fig. 7 is the partial structurtes explosive view of the present invention；
Label declaration in figure: 1-drying baker, 2-material collecting box, 3-drying device, 11-outlet slot, 12-gag lever post, 31-install
Seat, 32-converge gas tank, 33-breather, 34-side plate case, 35-conducting strip, 36-web plate, 37-flexible pipe, 311-card case, 312-rotating shaft,
313-rotating disk, 321-notch, 322-gas cylinder, 331-air guide port, the main pore of 332-, 341-fixed station, 342-auxiliary air vent,
343-draw-in groove, 344-inducing QI case, 351-U type groove.
Detailed description of the invention
Below with reference to the accompanying drawings and in conjunction with the embodiments, the present invention is described in detail.
A kind of biological particles drying process device as shown in Figures 1 to 7, including drying baker 1 be sequentially arranged at dry
Drying device 3 in dry case 1, has outlet slot 11, is provided with material collecting box 2 in outlet slot 11 bottom drying baker 1；
Described drying device 3 includes mounting seat 31 and the remittance gas tank 32 being fixed in mounting seat 31, remittance gas tank 32 opposite side
Being fixed with roundabout type breather 33, breather 33 upper surface has some main pores 332, is arranged above some conducting strips 35,
Conducting strip 35 is arranged above web plate 36；
Described remittance gas tank 32 both sides are provided with gas cylinder 322, pass through flexible pipe between the gas cylinder 322 of adjacent remittance gas tank 32
37 are connected with each other；
In described drying baker 1, drying device 3 lower surface position is provided with gag lever post 12.
Wherein, mounting seat 31 two ends are fixed with rotating shaft 312, and rotating shaft 312 end is fixed with rotating disk 313, can be to drying device 3
Arbitrarily rotate regulation, the biological particles in upper drying device 3 above be delivered on the drying device 3 of lower section,
It is dried further.
Wherein, the gas tank 32 that converges is provided with notch 321 near breather 33 side, and breather 33 two-port embeds and is arranged on groove
In mouth 321.
Wherein, mounting seat 31 side is fixed with card case 311, and embedding is arranged on remittance gas tank 32 side.
Wherein, breather 33 two ends are fixed with side plate case 34 so that biomass upper strata granule obtains efficient drying simultaneously, effect
Rate is higher.
Wherein, being provided with fixed station 341 in the middle of side plate case 34 medial surface, fixed station 341 inner surface equidistant arrangement is distributed
Having some draw-in grooves 343, be fixed with conducting strip 35 in draw-in groove 343 successively, conducting strip 35 has near breather 33 side and ventilates
The U-type groove 351 that pipe 33 matches, side plate case 34 medial surface upper end has some auxiliary air vents 342, and lower end is fixed with inducing QI case
344, breather 33 has air guide port 331 near inducing QI case 344 side, and described inducing QI case 344 embeds and is arranged on air guide port 331
In.
Wherein, drying baker 1 inboard width, equal to the length at mounting seat 31 two ends, prevents the biomass of top in dry run
Granule is scattering on the drying device 3 of lower floor.
Wherein, the mutual spacing of main pore 332 is 3～5cm, and aperture is 5～10mm, and drying efficiency is more preferably.
Wherein, side plate case 34 and side plate case 34 mutual spacing are equal to the length at mounting seat 31 two ends.
Wherein, web plate 36 is identical with conducting strip 35 thickness and is 3～5mm so that web plate 36 and the heat conduction of conducting strip 35
Efficiency is more preferable.
During use, hot-air blower is installed bottom drying baker 1, and is connected with the drying device 3 of lowermost end by flexible pipe 37, depend on
Secondary hot blast is transmitted from bottom to top, owing to the temperature lower layer on upper strata is relatively low, the biological particles on the drying device 3 of lower floor
After reaching requirement, can rotate rotating disk 313 successively, the biological particles of upper end then can be by drying device 3 and drying baker 1
Crack is slipped to lower floor, then in the drying baker 1 of the superiors, continuously adds biological particles, circulate successively.
The present invention can carry out efficient drying to biological particles, and by arranging the drying device of multilamellar, the index of aridity obtains
It is greatly improved, it is to avoid because being dried the pollution that thoroughly air is caused by after-combustion, decrease the humidity of biological particles,
Storing and be difficult to mouldy in transportation, whole apparatus structure is simple, cheap for manufacturing cost, has won considerable economy for enterprise
Benefit, is suitable for promoting and using.
The ultimate principle of the present invention, principal character and advantages of the present invention have more than been shown and described.The technology of the industry
Personnel, it should be appreciated that the present invention is not restricted to the described embodiments, simply illustrating this described in above-described embodiment and description
The principle of invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, and these become
Change and improvement both falls within scope of the claimed invention.
Claims (10)
1. a biological particles drying process device, it is characterised in that: include drying baker (1) and be sequentially arranged at drying baker
(1) drying device (3) in, drying baker (1) bottom has outlet slot (11), is provided with material collecting box (2) in outlet slot (11)；
Described drying device (3) includes mounting seat (31) and the remittance gas tank (32) being fixed in mounting seat (31), remittance gas tank (32)
Opposite side is fixed with roundabout type breather (33), and breather (33) upper surface has some main pores (332), if being arranged above
Dry conducting strip (35), conducting strip (35) is arranged above web plate (36)；
Described remittance gas tank (32) both sides are provided with gas cylinder (322), pass through between the gas cylinder (322) of adjacent remittance gas tank (32)
Flexible pipe (37) is connected with each other；
In described drying baker (1), drying device (3) lower surface position is provided with gag lever post (12).
A kind of biological particles drying process device the most according to claim 1, it is characterised in that: described mounting seat (31)
Two ends are fixed with rotating shaft (312), and rotating shaft (312) end is fixed with rotating disk (313).
A kind of biological particles drying process device the most according to claim 1, it is characterised in that: described remittance gas tank (32)
Be provided with notch (321) near breather (33) side, breather (33) two-port embeds and is arranged in notch (321).
A kind of biological particles drying process device the most according to claim 1, it is characterised in that: described mounting seat (31)
Side is fixed with card case (311), and embedding is arranged on remittance gas tank (32) side.
A kind of biological particles drying process device the most according to claim 1, it is characterised in that: described breather (33)
Two ends are fixed with side plate case (34).
A kind of biological particles drying process device the most according to claim 5, it is characterised in that: described side plate case (34)
Being provided with fixed station (341) in the middle of medial surface, fixed station (341) inner surface equidistant arrangement is distributed some draw-in grooves (343), card
Being fixed with conducting strip (35) in groove (343) successively, conducting strip (35) has and breather (33) phase near breather (33) side
The U-type groove (351) coordinated, side plate case (34) medial surface upper end has some auxiliary air vents (342), and lower end is fixed with inducing QI case
(344), breather (33) has air guide port (331) near inducing QI case (344) side, and described inducing QI case (344) embeds and is arranged on
In air guide port (331).
7. according to a kind of biological particles drying process device described in any one of claim 1～6, it is characterised in that: described
Drying baker (1) inboard width is equal to the length at mounting seat (31) two ends.
A kind of biological particles drying process device the most according to claim 7, it is characterised in that: described main pore
(332) mutual spacing is 3～5cm, and aperture is 5～10mm.
A kind of biological particles drying process device the most according to claim 7, it is characterised in that: described side plate case (34)
With the length that side plate case (34) mutual spacing is equal to mounting seat (31) two ends.
A kind of biological particles drying process device the most according to claim 7, it is characterised in that: described web plate (36)
Identical with conducting strip (35) thickness and be 3～5mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610436062.6A CN106123517B (en) | 2016-06-16 | 2016-06-16 | A kind of biological particles drying process device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610436062.6A CN106123517B (en) | 2016-06-16 | 2016-06-16 | A kind of biological particles drying process device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106123517A true CN106123517A (en) | 2016-11-16 |
| CN106123517B CN106123517B (en) | 2018-10-26 |
Family
ID=57470778
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610436062.6A Active CN106123517B (en) | 2016-06-16 | 2016-06-16 | A kind of biological particles drying process device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106123517B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113712192A (en) * | 2021-08-27 | 2021-11-30 | 山东芝人堂药业有限公司 | Processing technology and preparation equipment of wall-broken ganoderma lucidum spore powder micro-capsule oil |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001095548A (en) * | 1999-09-30 | 2001-04-10 | Susumu Kiyokawa | Food dryer |
| CN202083192U (en) * | 2011-05-23 | 2011-12-21 | 山东弗斯特数控设备有限公司 | Mesh belt conveying impacting flow dryer |
| CN103234343A (en) * | 2013-04-26 | 2013-08-07 | 江苏安华电气自动化有限公司 | High-density conduction heating device of large-scale vacuum drying oven |
| CN203964590U (en) * | 2014-07-10 | 2014-11-26 | 邓大贵 | Energy saving type material drier |
| CN204594116U (en) * | 2015-04-07 | 2015-08-26 | 绍兴御茶村茶业有限公司 | A kind of tea drier |
-
2016
- 2016-06-16 CN CN201610436062.6A patent/CN106123517B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001095548A (en) * | 1999-09-30 | 2001-04-10 | Susumu Kiyokawa | Food dryer |
| CN202083192U (en) * | 2011-05-23 | 2011-12-21 | 山东弗斯特数控设备有限公司 | Mesh belt conveying impacting flow dryer |
| CN103234343A (en) * | 2013-04-26 | 2013-08-07 | 江苏安华电气自动化有限公司 | High-density conduction heating device of large-scale vacuum drying oven |
| CN203964590U (en) * | 2014-07-10 | 2014-11-26 | 邓大贵 | Energy saving type material drier |
| CN204594116U (en) * | 2015-04-07 | 2015-08-26 | 绍兴御茶村茶业有限公司 | A kind of tea drier |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113712192A (en) * | 2021-08-27 | 2021-11-30 | 山东芝人堂药业有限公司 | Processing technology and preparation equipment of wall-broken ganoderma lucidum spore powder micro-capsule oil |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106123517B (en) | 2018-10-26 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: Granite County of Hefei City, Anhui province 231243 Feixi Zhenyuan Sun Ji Xiang textile factory Applicant after: Anhui new agricultural Limited by Share Ltd Address before: Granite County of Hefei City, Anhui province 231243 Feixi Zhenyuan Sun Ji Xiang textile factory Applicant before: ANHUI XINSHENGLI BIOLOGY TECHNOLOGY CO., LTD. |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20180726 Address after: 230000 Anhui Hefei economic and Technological Development Zone, qinglongtan Road, West Light Road, East Binhe District North export processing zone, 124 public rental housing 1 Applicant after: Hefei Jun Machinery Technology Co., Ltd. Address before: 231243 Anhui Hefei Feixi County Huagang Town, sun Yuan Ji textile mill Applicant before: Anhui new agricultural Limited by Share Ltd |
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| TA01 | Transfer of patent application right | ||
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| TA01 | Transfer of patent application right |
Effective date of registration: 20180831 Address after: 516000 Guangdong Huizhou Zhongkai hi tech Zone, Chen Jiang Street, No. 4 Zhongjing Road (factory building), 8 floor. Applicant after: HUIZHOU YAOBANG ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Address before: 230000 Anhui Hefei economic and Technological Development Zone, qinglongtan Road, West Light Road, East Binhe District North export processing zone, 124 public rental housing 1 Applicant before: Hefei Jun Machinery Technology Co., Ltd. |
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| CP03 | Change of name, title or address |
Address after: 516006 8 / F, No. 4, Zhongjing Road, Chenjiang street, Zhongkai high tech Zone, Huizhou City, Guangdong Province Patentee after: Guangdong Yaobang Environmental Protection Technology Co., Ltd Address before: 516000 Guangdong Huizhou Zhongkai hi tech Zone, Chen Jiang Street, No. 4 Zhongjing Road (factory building), 8 floor. Patentee before: HUIZHOU YAOBANG ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. |