CN107149913A - A kind of thermal jet granulation drying system - Google Patents
A kind of thermal jet granulation drying system Download PDFInfo
- Publication number
- CN107149913A CN107149913A CN201610118996.5A CN201610118996A CN107149913A CN 107149913 A CN107149913 A CN 107149913A CN 201610118996 A CN201610118996 A CN 201610118996A CN 107149913 A CN107149913 A CN 107149913A
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- China
- Prior art keywords
- drying
- air filter
- drying tower
- electric heater
- thermal jet
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- 238000001035 drying Methods 0.000 title claims abstract description 61
- 238000005469 granulation Methods 0.000 title claims abstract description 14
- 230000003179 granulation Effects 0.000 title claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 25
- 230000002572 peristaltic effect Effects 0.000 claims abstract description 14
- 230000001105 regulatory effect Effects 0.000 claims abstract description 4
- 239000000843 powder Substances 0.000 claims description 27
- 238000000034 method Methods 0.000 abstract description 7
- 238000005453 pelletization Methods 0.000 abstract description 5
- 229920002521 macromolecule Polymers 0.000 abstract description 2
- 239000005416 organic matter Substances 0.000 abstract description 2
- 230000035611 feeding Effects 0.000 description 9
- 239000002245 particle Substances 0.000 description 5
- 235000013305 food Nutrition 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000021022 fresh fruits Nutrition 0.000 description 1
- 235000011868 grain product Nutrition 0.000 description 1
- 239000006193 liquid solution Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
- B01J2/04—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of thermal jet granulation drying system, including feeding device, main frame hot air apparatus, fluidized drying hot air apparatus, drying tower and material collecting device；The feeding device includes peristaltic pump and material placer, and peristaltic pump one end is connected by pipeline with material placer；The peristaltic pump other end is connected by flexible pipe with drying tower upper end, and regulating valve is provided with flexible pipe；The main frame hot air apparatus includes the first primary air filter, pressure fan, the first high efficiency particulate air filter and the first electric heater, and the first primary air filter is connected with pressure fan, high efficiency particulate air filter, the first electric heater and drying tower successively by airduct；The first adjusting valve is provided between first primary air filter and pressure fan；Thermal jet granulation drying system, its whole technological process is brief, and material residence time in granulating pelletizing process is short, and the cytoactive of macromolecule organic matter is not destroyed, practical, it is easy to promote the use of.
Description
Technical field
The present invention relates to food processing equipment technical field, specially a kind of thermal jet granulation drying system.
Background technology
In recent years, by liquid solution be made micropill in food processing it is increasingly common, do not changing material
Original nutrient is outer to be made micropill shape by solution, is convenient for carrying it, but in the processing work of micropill
During, the drying to micropill is a very crucial step, and the quality of its dry mass is directly influenced
The edible nourishing of micropill.
The drying of existing micropill mainly using by hand is toasted, its not only efficiency it is low, and baking
Temperature be also not easy hold, it is easy to cause micropill nutritional quality decline.
The content of the invention
Prior art is difficult to the need for meeting people, and in order to solve above-mentioned problem, the present invention is proposed
A kind of thermal jet granulation drying system, it using by the material after pelletization in 60~70 DEG C of hot blast spaces of low temperature
Mutual break-in, more perfect for particle round and smooth degree, the uniformity between interior boiling fluidized drying, particle.
To achieve the above object, the present invention provides following technical scheme：A kind of thermal jet granulation drying system,
Including feeding device, main frame hot air apparatus, fluidized drying hot air apparatus, drying tower and material collecting device；Institute
Stating feeding device includes peristaltic pump and material placer, and peristaltic pump one end passes through pipeline and material placer
Connection；The peristaltic pump other end is connected by flexible pipe with drying tower upper end, and regulation is provided with flexible pipe
Valve；The main frame hot air apparatus includes the first primary air filter, pressure fan, the first high efficiency particulate air filter
With the first electric heater, and the first primary air filter by airduct successively with pressure fan, high efficiency filter
Device, the first electric heater and drying tower connection；Set between first primary air filter and pressure fan
It is equipped with the first adjusting valve；The fluidized drying hot air apparatus includes the second primary air filter, second high
Filter and the second electric heater are imitated, and the second primary air filter is efficient with second successively by airduct
Filter, the second electric heater and drying tower connection；The material collecting device includes cyclone separator plus powder
Cylinder and air-introduced machine, and drying tower is connected with cyclone separator plus powder drum and air-introduced machine successively by airduct；
Sack cleaner is provided with described plus powder drum, and adds powder drum lower end to connect by airduct and powder feeding blower fan one end
Connect；The powder feeding blower fan other end is connected by airduct with drying tower upper end.
Further, it is provided with temperature controller between first electric heater and drying tower.
Further, pneumatic jar and pressure indicator are additionally provided with the drying tower.
Further, the pneumatic jar is provided with several, and is evenly distributed on drying tower.
Further, it is described plus the second adjusting valve is provided between powder drum and air-introduced machine.
Compared with prior art, the beneficial effects of the invention are as follows：Thermal jet granulation drying system, its is whole
Technological process is brief, and material residence time in granulating pelletizing process is short, and temperature of charge itself is low, does not break
The cytoactive of bad macromolecule organic matter, keeps pure natural characteristic；Material after pelletization is in 60~70 DEG C of low temperature
Seethe with excitement fluidized drying in hot blast space, mutually break-in between particle, for particle round and smooth degree, the uniformity more
Add U.S.；Whole set process is fabricated to Automatic Production Line, and the dried grain products of pelletization can be direct
Packaging enters lower road handling process；It is simple to operate, it is practical, it is easy to promote the use of.
Brief description of the drawings
Fig. 1 is overall structure diagram of the invention；
In figure：1- feeding devices, 2- main frames hot air apparatus, 3- fluidized dryings hot air apparatus, 4- drying towers,
5- material collecting devices, 6- peristaltic pumps, 7- materials placer, 8- pipelines, 9- flexible pipes, 10- regulating valves, 11-
First primary air filter, 12- pressure fan, the high efficiency particulate air filters of 13- first, the electric heaters of 14- first,
15- airducts, the adjusting valves of 16- first, the primary air filters of 17- second, the high efficiency particulate air filters of 18- second,
The electric heaters of 19- second, 20- cyclone separators, 21- add powder drum, 22- air-introduced machines, 23- sack cleaners,
24- powder feedings blower fan, 25- temperature controllers, the pneumatic jars of 26-, 27- pressure indicators, 28- second are adjusted
Air-valve.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the invention, and
The embodiment being not all of.Based on the embodiment in the present invention, those of ordinary skill in the art are not doing
Go out the every other embodiment obtained under the premise of creative work, belong to the scope of protection of the invention.
Referring to Fig. 1, a kind of embodiment that the present invention is provided：A kind of thermal jet granulation drying system, including supply
Expect device 1, main frame hot air apparatus 2, fluidized drying hot air apparatus 3, drying tower 4 and material collecting device 5；
The feeding device 1 include peristaltic pump 6 and material placer 7, and the one end of peristaltic pump 6 by pipeline 8 with
Material placer 7 is connected；The other end of peristaltic pump 6 is connected by flexible pipe 9 with the upper end of drying tower 4,
And regulating valve 10 is provided with flexible pipe 9；The main frame hot air apparatus 2 includes the first primary air filter
11st, pressure fan 12, the first high efficiency particulate air filter 13 and the first electric heater 14, and the first primary air mistake
Filter 11 by airduct 15 successively with pressure fan 12, high efficiency particulate air filter 13, the first electric heater 14 and
Drying tower 4 is connected；The first tune is provided between first primary air filter 11 and pressure fan 12
Air-valve 16；The fluidized drying hot air apparatus 3 includes the second primary air filter 17, the second efficient mistake
The electric heater 19 of filter 18 and second, and the second primary air filter 17 by airduct 15 successively with
Two high efficiency particulate air filters 18, the second electric heater 19 and drying tower 4 are connected；The material collecting device 5 includes rotation
Wind separator 20, plus powder drum 21 and air-introduced machine 22, and drying tower 4 by airduct 15 successively with whirlwind point
Connected from device 20 plus powder drum 21 and air-introduced machine 22；Sack cleaner is provided with described plus powder drum 21
23, and add the lower end of powder drum 21 to be connected by airduct 15 with the one end of powder feeding blower fan 24；The powder feeding blower fan 24
The other end is connected by airduct 15 with the upper end of drying tower 4；First electric heater 14 and drying tower 4
Between be provided with temperature controller 25；Pneumatic jar 26 is additionally provided with the drying tower 4 and pressure refers to
Show device 27；The pneumatic jar 26 is provided with several, and is evenly distributed on drying tower 4；It is described to add
The second adjusting valve 28 is provided between powder drum 21 and air-introduced machine 22.
Fresh fruit, fresh vegetables are beaten equal by thermal jet granulation drying system of the present invention when in use, first
It is added to after matter by peristaltic pump 6 in drying tower 4, in hot blast cocurrent effect lower surface moisture absorption heat
Amount volatilization, surface are because moisture evaporation forms close spheroid；Material avoids viscous wall, group in dropping process
The phenomenon such as poly-, powder is over dry carrier, and further sorbent surface and internal moisture are contacted simultaneously with close ball,
Under drop down onto the bottom of drying tower 4；It is furnished with fluidized drying hot air apparatus 3, close ball and powder carrier in equipment bottom
Fluidized state is in this space, the hot blast carrier with heat is further done to close ball with powder
Dry, two kinds of materials wash away mutually, and fine powder material comes off separation because of being further dried, and is floated with air carrier
Tail gas part is flowed to, cyclone separator 20 is carried out and is reclaimed with sack cleaner 23；Close ball is further done
It is dry to form uniform micropill little particle, fall from the lower discharge port of drying tower 4.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment,
And without departing from the spirit or essential characteristics of the present invention, can be real in other specific forms
The existing present invention.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and
It is nonrestrictive, the scope of the present invention is limited by appended claims rather than described above, therefore purport
Included by all changes fallen in the implication and scope of the equivalency of claim in the present invention.
Any reference in claim should not be considered as to the claim involved by limitation.
Claims (5)
- The drying system 1. a kind of thermal jet is pelletized, including feeding device (1), main frame hot air apparatus (2), Fluidized drying hot air apparatus (3), drying tower (4) and material collecting device (5)；It is characterized in that：It is described to supply Expect that device (1) includes peristaltic pump (6) and material placer (7), and peristaltic pump (6) one end passes through Pipeline (8) is connected with material placer (7)；Peristaltic pump (6) other end passes through flexible pipe (9) It is connected with drying tower (4) upper end, and regulating valve (10) is provided with flexible pipe (9)；The main frame heat Wind apparatus (2) includes the first primary air filter (11), pressure fan (12), the first high efficiency filter Device (13) and the first electric heater (14), and the first primary air filter (11) passes through airduct (15) Successively with pressure fan (12), high efficiency particulate air filter (13), the first electric heater (14) and drying tower (4) Connection；The first tune wind is provided between first primary air filter (11) and pressure fan (12) Valve (16)；The fluidized drying hot air apparatus (3) includes the second primary air filter (17), the Two high efficiency particulate air filters (18) and the second electric heater (19), and the second primary air filter (17) By airduct (15) successively with the second high efficiency particulate air filter (18), the second electric heater (19) and dry Tower (4) is connected；The material collecting device (5) include cyclone separator (20), plus powder drum (21) and Air-introduced machine (22), and drying tower (4) by airduct (15) successively with cyclone separator (20), plus Powder drum (21) and air-introduced machine (22) connection；Sack cleaner (23) is provided with described plus powder drum (21), And add powder drum (21) lower end to be connected by airduct (15) with powder feeding blower fan (24) one end；The powder feeding Blower fan (24) other end is connected by airduct (15) with drying tower (4) upper end.
- 2. a kind of thermal jet granulation drying system according to claim 1, it is characterized in that：Described first Temperature controller (25) is provided between electric heater (14) and drying tower (4).
- 3. a kind of thermal jet granulation drying system according to claim 1, it is characterized in that：The drying Pneumatic jar (26) and pressure indicator (27) are additionally provided with tower (4).
- 4. a kind of thermal jet granulation drying system according to claim 3, it is characterized in that：It is described pneumatic Jar (26) is provided with several, and is evenly distributed on drying tower (4).
- 5. a kind of thermal jet granulation drying system according to claim 1, it is characterized in that：Described plus powder The second adjusting valve (28) is provided between cylinder (21) and air-introduced machine (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610118996.5A CN107149913A (en) | 2016-03-03 | 2016-03-03 | A kind of thermal jet granulation drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610118996.5A CN107149913A (en) | 2016-03-03 | 2016-03-03 | A kind of thermal jet granulation drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107149913A true CN107149913A (en) | 2017-09-12 |
Family
ID=59791798
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610118996.5A Pending CN107149913A (en) | 2016-03-03 | 2016-03-03 | A kind of thermal jet granulation drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107149913A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187960A (en) * | 2017-12-28 | 2018-06-22 | 大连隆星新材料有限公司 | A kind of powder spraying system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002045675A (en) * | 2000-08-08 | 2002-02-12 | Ajinomoto Co Inc | Novel spray drying pelletizing device and manufacturing method of granular food product |
| CN2833468Y (en) * | 2005-09-06 | 2006-11-01 | 中国神马集团有限责任公司 | Material returning type fluidized bed drying apparatus |
| CN203494186U (en) * | 2013-09-30 | 2014-03-26 | 湖北三可建材科技有限公司 | Spray drying and powder preparing apparatus for polycarboxylic copolymer |
| CN104258783A (en) * | 2014-10-14 | 2015-01-07 | 南京高正农用化工有限公司 | Paraquat emetic adding device and application thereof |
| CN204100753U (en) * | 2014-09-16 | 2015-01-14 | 济南亿民动物药业有限公司 | A kind of Chinese medicinal granule high velocity fog drying system |
| CN204543593U (en) * | 2015-03-02 | 2015-08-12 | 宣威市浩阳农业生物科技开发有限公司 | Spray dryer |
-
2016
- 2016-03-03 CN CN201610118996.5A patent/CN107149913A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002045675A (en) * | 2000-08-08 | 2002-02-12 | Ajinomoto Co Inc | Novel spray drying pelletizing device and manufacturing method of granular food product |
| CN2833468Y (en) * | 2005-09-06 | 2006-11-01 | 中国神马集团有限责任公司 | Material returning type fluidized bed drying apparatus |
| CN203494186U (en) * | 2013-09-30 | 2014-03-26 | 湖北三可建材科技有限公司 | Spray drying and powder preparing apparatus for polycarboxylic copolymer |
| CN204100753U (en) * | 2014-09-16 | 2015-01-14 | 济南亿民动物药业有限公司 | A kind of Chinese medicinal granule high velocity fog drying system |
| CN104258783A (en) * | 2014-10-14 | 2015-01-07 | 南京高正农用化工有限公司 | Paraquat emetic adding device and application thereof |
| CN204543593U (en) * | 2015-03-02 | 2015-08-12 | 宣威市浩阳农业生物科技开发有限公司 | Spray dryer |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187960A (en) * | 2017-12-28 | 2018-06-22 | 大连隆星新材料有限公司 | A kind of powder spraying system |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170912 |