CN105651007B - A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device - Google Patents
A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device Download PDFInfo
- Publication number
- CN105651007B CN105651007B CN201610058802.7A CN201610058802A CN105651007B CN 105651007 B CN105651007 B CN 105651007B CN 201610058802 A CN201610058802 A CN 201610058802A CN 105651007 B CN105651007 B CN 105651007B
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- Prior art keywords
- heat
- vacuum
- recuperation
- barrel
- heater
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B7/00—Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/08—Drying solid materials or objects by processes not involving the application of heat by centrifugal treatment
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of medicinal material foodstuff seed low-temperature air energy vacuum drying devices, including wet stock bucket, recuperation of heat heater, thermal energy recoverer, air energy thermal power plant unit, vacuum heat-preserving drying cylinder, heat recovery cooler, promote barrel, anaerobic infuses nitrogen atmospheric chamber, horizontal feed barrel and machining center, the recuperation of heat heater, vacuum heat-preserving drying cylinder, heat recovery cooler, the one end for promoting barrel and horizontal feed barrel is respectively connected with vacuum pump, air drying of the present invention, do not hurt endosperm embryo, improve the germination percentage of seed, reduce precious seed resource waste, reduce occupation area of equipment, energy-saving and emission-reduction, it is the expense 30% that traditional coal is occurred, it may be implemented remotely to monitor by microprocessor and radio transmission apparatus.
Description
Technical field
The present invention relates to drying equipment, specifically a kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device.
Background technique
Drying unit is developed to the modern times with electric energy fossil fuels (coal) and plant from tradition hole through leaf bar etc., as heat
Source, by hot-air (60-120 DEG C), convection current promotes moisture to evaporate, and makes drying object dehydration, reaches drying purpose, and this device has
Following disadvantage:
1. heat utilization efficiency is low, heat is exhausted with moisture content.
2. apparatus is very big, complicated for operation, more people's cooperations are needed.
3. safety is poor, due to manually guarding temperature, often due to work carelessness, causes fire, leads to equipment burnout, entirely
State causes very big property loss per there is generation every year.
4. heat supply temperature can not the constant temperature difference fluctuated it is big, the kind in this way to the such high request of seed is unable to satisfy it
It is required that mainly influencing the germination percentage of seed.
Summary of the invention
It is above-mentioned to solve the purpose of the present invention is to provide a kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device
The problem of being proposed in background technique.
To achieve the above object, the invention provides the following technical scheme:
A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device, including wet stock bucket, recuperation of heat heater, thermal energy
Recover, vacuum heat-preserving drying cylinder, heat recovery cooler, promotes barrel, anaerobic note nitrogen atmospheric chamber, water at air energy thermal power plant unit
Flat conveying barrel and machining center, the recuperation of heat heater, vacuum heat-preserving drying cylinder, heat recovery cooler, promoted barrel and
It is equipped with spiral conveying mechanism in horizontal feed barrel, guarantees whole normal feeding using spiral conveying mechanism；The wet stock
There are centrifugal dehydrator, and the feeding inlet of the discharge port connection recuperation of heat heater of centrifugal dehydrator in bucket, recuperation of heat heater
The feeding inlet of the vacuum heat-preserving drying cylinder of discharge port connection lower section, the recuperation of heat of the discharge port connection lower section of vacuum heat-preserving drying cylinder
The feeding inlet of cooler, the discharge port connection of heat recovery cooler promote the feeding inlet of barrel, promote the discharge port connection of barrel
The top-feed mouth for the anaerobic note nitrogen atmospheric chamber being vertically arranged, anaerobic infuse the discharge port connection horizontal feed barrel of nitrogen atmospheric chamber
Feeding inlet, the feeding inlet of the discharge port connection machining center of horizontal feed barrel；The recuperation of heat heater, vacuum heat-preserving are dry
Cylinder, heat recovery cooler, the one end for promoting barrel and horizontal feed barrel are respectively connected with vacuum pump, are taken out inside using vacuum pump
Vacuum, in the environment of vacuum low-pressure, the boiling point of water is reduced, and the moisture in material can be quick when lower temperature at this time
Evaporation；The air energy thermal power plant unit send heat pipe, vacuum heat-preserving drying cylinder to send heat pipe and recuperation of heat cold by recuperation of heat heater
But device send heat pipe to be separately connected recuperation of heat heater, vacuum heat-preserving drying cylinder and heat recovery cooler, utilizes air energy heat supply machine
Group improves heat supply；The recuperation of heat heater send heat pipe, vacuum heat-preserving drying cylinder that heat pipe and heat recovery cooler is sent to send on heat pipe
It is equipped with temperature sensor, and the microprocessor in temperature sensor connection air energy thermal power plant unit, realizes volume using micro process
Determine temperature control；Wireless transport module is additionally provided in the air energy thermal power plant unit, and wireless transport module connects microprocessor,
Long-range control is easy to implement to whole；The thermal energy recoverer send heat pipe to connect recuperation of heat by product heat cal rod with thermal energy recoverer
Heater, the heat recovery cooler connect air energy thermal power plant unit by heat recovery cooler product heat cal rod；The thermal energy recycling
Device connects recuperation of heat heater by return fan；The air energy thermal power plant unit send heat pipe, vacuum to protect by recuperation of heat heater
Warm drying cylinder send heat pipe and heat recovery cooler that heat pipe is sent to be separately connected recuperation of heat heater, vacuum heat-preserving drying cylinder and recuperation of heat
Cooler.
As further scheme of the invention: the recuperation of heat heater, vacuum heat-preserving drying cylinder, recuperation of heat are cooling
Device, promotion barrel and horizontal feed barrel are sealing structure.
As further scheme of the invention: the bottom of the vacuum heat-preserving drying cylinder is additionally provided with bracket.
As further scheme of the invention: the promotion barrel is obliquely installed upwards.
Compared with prior art, the beneficial effects of the present invention are: air drying of the present invention, does not hurt endosperm embryo, seed is improved
Germination percentage reduces precious seed resource waste, reduces occupation area of equipment, energy-saving and emission-reduction, it is that traditional coal is occurred
Expense 30% may be implemented remotely to monitor by microprocessor and radio transmission apparatus.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of medicinal material foodstuff seed low-temperature air energy vacuum drying device of the present invention.
In figure: 1- wet stock bucket, 2- recuperation of heat heater, 3- thermal energy recoverer, 4- air energy thermal power plant unit, 5- vacuum are protected
During warm drying cylinder, 6- heat recovery cooler, 7- promote barrel, 8- anaerobic infuses nitrogen atmospheric chamber, 9- horizontal feed barrel, 10- are processed
The heart, 11- vacuum pump, 12- bracket, 13- product heat cal rod, 14- thermal energy recoverer send heat pipe, 15- return fan, 16- recuperation of heat heater
Send heat pipe, 17- vacuum heat-preserving drying cylinder that heat pipe, 18- heat recovery cooler is sent to send heat pipe, 19- heat recovery cooler product heat cal rod.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Referring to Fig. 1, in the embodiment of the present invention, a kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device, including
Wet stock bucket 1, recuperation of heat heater 2, thermal energy recoverer 3, air energy thermal power plant unit 4, vacuum heat-preserving drying cylinder 5, recuperation of heat are cold
But device 6, promotion barrel 7, anaerobic note nitrogen atmospheric chamber 8, horizontal feed barrel 9 and machining center 10, the recuperation of heat heater 2,
It is equipped with spiral conveying mechanism in vacuum heat-preserving drying cylinder 5, heat recovery cooler 6, promotion barrel 7 and horizontal feed barrel 9, benefit
Guarantee whole normal feeding with spiral conveying mechanism；There are centrifugal dehydrator, and the discharging of centrifugal dehydrator in the wet stock bucket 1
The feeding inlet of mouth connection recuperation of heat heater 2, the vacuum heat-preserving drying cylinder 5 of the discharge port connection lower section of recuperation of heat heater 2
Feeding inlet, the feeding inlet of the heat recovery cooler 6 of the discharge port connection lower section of vacuum heat-preserving drying cylinder 5, heat recovery cooler 6
Discharge port connection promotes the feeding inlet of barrel 7, and the discharge port for promoting barrel 7 connects the anaerobic note nitrogen atmospheric chamber 8 being vertically arranged
Top-feed mouth, anaerobic infuse the feeding inlet of the discharge port connection horizontal feed barrel 9 of nitrogen atmospheric chamber 8, and horizontal feed barrel 9 goes out
The feeding inlet of material mouth connection machining center 10；The recuperation of heat heater 2, heat recovery cooler 6, mentions vacuum heat-preserving drying cylinder 5
The one end for rising barrel 7 and horizontal feed barrel 9 is respectively connected with vacuum pump 11, is vacuumized inside using vacuum pump 11, in vacuum
In the environment of low pressure, the boiling point of water is reduced, at this time the moisture in material can when lower temperature rapid evaporation；The sky
Gas energy thermal power plant unit 4 send heat pipe 16, vacuum heat-preserving drying cylinder that heat pipe 17 and heat recovery cooler is sent to send by recuperation of heat heater
Heat pipe 18 is separately connected recuperation of heat heater 2, vacuum heat-preserving drying cylinder 5 and heat recovery cooler 6, utilizes air energy thermal power plant unit
4 improve heat supply；The thermal energy recoverer 3 send heat pipe 14 to connect recuperation of heat heater 2, institute by product heat cal rod 13 and thermal energy recoverer
It states thermal energy recoverer 3 and recuperation of heat heater 2 is connected by return fan 15；The heat recovery cooler 6 passes through heat recovery cooler
Product heat cal rod 19 connects air energy thermal power plant unit 4.
The recuperation of heat heater send heat pipe 16, vacuum heat-preserving drying cylinder that heat pipe 17 and heat recovery cooler is sent to send heat pipe 18
On be equipped with temperature sensor, and the microprocessor in temperature sensor connection air energy thermal power plant unit 4 is realized using micro process
Rated temperature control.
Wireless transport module is additionally provided in the air energy thermal power plant unit 4, and wireless transport module connects microprocessor, from
And entirety is easy to implement long-range control.
The recuperation of heat heater 2, heat recovery cooler 6, promotes barrel 7 and horizontal feed material at vacuum heat-preserving drying cylinder 5
Cylinder 9 is sealing structure.
The bottom of the vacuum heat-preserving drying cylinder 5 is additionally provided with bracket 12.
The promotion barrel 7 is obliquely installed upwards.
The working principle of the invention is: during actual motion, material, wet stock is added to wet stock bucket 1 first
Bucket 1 in have centrifugal dehydrator, using centrifugal dehydrator realize preliminary hydro-extraction, then material under the action of spiral conveying mechanism according to
It is secondary enter recuperation of heat heater 2, air energy thermal power plant unit 4, vacuum heat-preserving drying cylinder 5, heat recovery cooler 6, promoted barrel 7,
Anaerobic note nitrogen atmospheric chamber 8, horizontal feed barrel 9 and machining center 10, air energy thermal power plant unit 4 send heat by recuperation of heat heater
Pipe 16, vacuum heat-preserving drying cylinder send heat pipe 17 and heat recovery cooler to send, and heat pipe 18 is separately connected recuperation of heat heater 2, vacuum is protected
Warm drying cylinder 5 and heat recovery cooler 6 improve heat supply using air energy thermal power plant unit 4, while sending heat pipe 16, vacuum heat-preserving dry
Dry cylinder send heat pipe 17 and heat recovery cooler to send and is equipped with temperature sensor on heat pipe 18, and temperature sensor connection air can supply
Microprocessor in heat engine group 4 realizes that rated temperature controls using micro process, can be avoided the excessively high feelings of temperature occur in this way
Condition, recuperation of heat heater 2, vacuum heat-preserving drying cylinder 5, heat recovery cooler 6, the one end for promoting barrel 7 and horizontal feed barrel 9
It is respectively connected with vacuum pump 11, is vacuumized inside using vacuum pump 11, in the environment of vacuum low-pressure, the boiling point of water is reduced, this
When material in moisture can when lower temperature rapid evaporation, therefore the case where avoid temperature excessively high injury plumule；
It is more energy saving in this way by the design of thermal energy recoverer 3 so that whole can be realized preferable backheat effect.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie
In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power
Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims
Variation is included within the present invention.Any reference signs in the claims should not be construed as limiting the involved claims.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (4)
1. a kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device, including wet stock bucket, recuperation of heat heater, thermal energy return
It receives device, air energy thermal power plant unit, vacuum heat-preserving drying cylinder, heat recovery cooler, promote barrel, anaerobic note nitrogen atmospheric chamber, level
Convey barrel and machining center, which is characterized in that the recuperation of heat heater, heat recovery cooler, mentions vacuum heat-preserving drying cylinder
It rises in barrel and horizontal feed barrel and is equipped with spiral conveying mechanism；There is centrifugal dehydrator in the wet stock bucket, and is centrifuged de-
The vacuum heat-preserving of the feeding inlet of the discharge port connection recuperation of heat heater of water dispenser, the discharge port connection lower section of recuperation of heat heater is dry
The feeding inlet of dry cylinder, the feeding inlet of the heat recovery cooler of the discharge port connection lower section of vacuum heat-preserving drying cylinder, recuperation of heat are cooling
The discharge port connection of device promotes the feeding inlet of barrel, and the discharge port for promoting barrel connects the anaerobic note nitrogen atmospheric chamber being vertically arranged
Top-feed mouth, anaerobic infuse the feeding inlet of the discharge port connection horizontal feed barrel of nitrogen atmospheric chamber, the discharging of horizontal feed barrel
The feeding inlet of mouth connection machining center；The recuperation of heat heater, heat recovery cooler, promotes barrel at vacuum heat-preserving drying cylinder
Vacuum pump is respectively connected with one end of horizontal feed barrel；The air energy thermal power plant unit by recuperation of heat heater send heat pipe,
Vacuum heat-preserving drying cylinder send heat pipe and heat recovery cooler send heat pipe be separately connected recuperation of heat heater, vacuum heat-preserving drying cylinder and
Heat recovery cooler；The recuperation of heat heater send heat pipe, vacuum heat-preserving drying cylinder that heat pipe and heat recovery cooler is sent to send heat pipe
On be equipped with temperature sensor, and the microprocessor in temperature sensor connection air energy thermal power plant unit；The air energy heat supply
Wireless transport module is additionally provided in unit, and wireless transport module connects microprocessor；The thermal energy recoverer passes through product heat cal rod
Heat pipe is sent to connect recuperation of heat heater with thermal energy recoverer, the heat recovery cooler is connected by heat recovery cooler product heat cal rod
Air energy thermal power plant unit；The air energy thermal power plant unit send heat pipe, vacuum heat-preserving drying cylinder to send heat pipe by recuperation of heat heater
Heat pipe is sent to be separately connected recuperation of heat heater, vacuum heat-preserving drying cylinder and heat recovery cooler with heat recovery cooler.
2. medicinal material foodstuff seed low-temperature air energy vacuum drying device according to claim 1, which is characterized in that the heat
Recycling heater, vacuum heat-preserving drying cylinder, heat recovery cooler, promotion barrel and horizontal feed barrel is sealing structure.
3. medicinal material foodstuff seed low-temperature air energy vacuum drying device according to claim 1, which is characterized in that described true
The bottom of empty heat preservation and dryness cylinder is additionally provided with bracket.
4. medicinal material foodstuff seed low-temperature air energy vacuum drying device according to claim 1, which is characterized in that described to mention
Barrel is risen to be obliquely installed upwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610058802.7A CN105651007B (en) | 2016-01-28 | 2016-01-28 | A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610058802.7A CN105651007B (en) | 2016-01-28 | 2016-01-28 | A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105651007A CN105651007A (en) | 2016-06-08 |
| CN105651007B true CN105651007B (en) | 2019-04-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610058802.7A Expired - Fee Related CN105651007B (en) | 2016-01-28 | 2016-01-28 | A kind of medicinal material foodstuff seed low-temperature air energy vacuum drying device |
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| CN (1) | CN105651007B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106091592B (en) * | 2016-06-21 | 2019-04-02 | 金锢电气有限公司 | A kind of full-automatic dry cooling system and process |
| CN109114915A (en) * | 2018-10-17 | 2019-01-01 | 郑州鼎力新能源技术有限公司 | Dregs of a decoction steam multitube stoving process and equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4330946A (en) * | 1980-09-23 | 1982-05-25 | Ralph S. Tillitt | High efficiency material drying |
| CN201289278Y (en) * | 2008-11-04 | 2009-08-12 | 国家粮食储备局郑州科学研究设计院 | Tower type vacuum continuous drying apparatus for heat pump |
| CN102865723A (en) * | 2011-07-07 | 2013-01-09 | 江苏申久化纤有限公司 | Vacuum drying device and drying method |
| CN102914134A (en) * | 2012-10-15 | 2013-02-06 | 曾应祥 | Superheat steam drying device |
| CN204739878U (en) * | 2015-05-18 | 2015-11-04 | 程石 | Living beings dehydration device |
-
2016
- 2016-01-28 CN CN201610058802.7A patent/CN105651007B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4330946A (en) * | 1980-09-23 | 1982-05-25 | Ralph S. Tillitt | High efficiency material drying |
| CN201289278Y (en) * | 2008-11-04 | 2009-08-12 | 国家粮食储备局郑州科学研究设计院 | Tower type vacuum continuous drying apparatus for heat pump |
| CN102865723A (en) * | 2011-07-07 | 2013-01-09 | 江苏申久化纤有限公司 | Vacuum drying device and drying method |
| CN102914134A (en) * | 2012-10-15 | 2013-02-06 | 曾应祥 | Superheat steam drying device |
| CN204739878U (en) * | 2015-05-18 | 2015-11-04 | 程石 | Living beings dehydration device |
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| Publication number | Publication date |
|---|---|
| CN105651007A (en) | 2016-06-08 |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20190318 Address after: 610058 Collective Household No. 5 Furongxi Road, Youxian District, Mianyang City, Sichuan Province Applicant after: Huang Yuming Address before: 610058 Longmen Town, Peicheng District, Mianyang City, Sichuan Province Applicant before: MIANYANG YUSHENG TECHNOLOGY CO., LTD. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190412 Termination date: 20210128 |
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