CN204428856U - A kind of centrifugal spray drying system - Google Patents

A kind of centrifugal spray drying system Download PDF

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Publication number
CN204428856U
CN204428856U CN201420849338.XU CN201420849338U CN204428856U CN 204428856 U CN204428856 U CN 204428856U CN 201420849338 U CN201420849338 U CN 201420849338U CN 204428856 U CN204428856 U CN 204428856U
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CN
China
Prior art keywords
cyclone separator
small size
centrifugal spray
spray drying
drying system
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
Application number
CN201420849338.XU
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Chinese (zh)
Inventor
李斌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ganzhou Xinlong New Energy Materials Co ltd
Original Assignee
Ganzhou Xinlong New Energy Materials Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
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Priority to CN201420849338.XU priority Critical patent/CN204428856U/en
Application granted granted Critical
Publication of CN204428856U publication Critical patent/CN204428856U/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse 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

Abstract

The utility model relates to mechanical drying field, particularly a kind of centrifugal spray drying system.Comprise drying tower, cyclone separator, described drying tower is provided with high speed atomisation device, this high speed atomisation device connects charging aperture, it is characterized in that: described drying tower is provided with hot-air distributor, scavenging conduit, described hot-air distributor connects heater and air inlet, described scavenging conduit connects high pressure admission mouth, described cyclone separator comprises large size cyclone separator and small size cyclone separator, aforementioned drying tower conical lower portion connects large size cyclone separator, small size cyclone separator successively, and this small size cyclone separator is provided with recovery blower fan and is connected with aforementioned hot-air distributor.The utility model develops a kind of centrifugal spray drying system, have employed size two kinds of cyclone separators, realizes the abundant drying of material, and product quality is upgraded further, and supply is high-end requires client; In addition, the utility model is provided with recovery blower fan and is connected with hot-air distributor, by energy effective recycling, and energy-conserving and environment-protective.

Description

A kind of centrifugal spray drying system
Technical field
The utility model relates to mechanical drying field, particularly a kind of centrifugal spray drying system.
Background technology
After air is heated by heater, enter the hot-air distributor at drying tower top through pressure fan, after hot-air distributor, hot-air enters in drying tower uniformly, and moves in the shape of a spiral.Feed liquid is delivered to the centrifugal atomizer at drying tower top by material pump simultaneously, and feed liquid is sprayed into minimum misty liquid droplets.The surface area of feed liquid and hot air is increased greatly, and moisture content evaporates rapidly, is dry product at very short time inner drying.Dry product is separated with humid air by cyclone separator, and the vortex chamber of gathering materials bottom cyclone separator is delivered to whirly separator by the air of drying and is separated, and is collected in rewinding cylinder, and tail gas is discharged through air-introduced machine.
The operation principle of centrifugal spray drying system is similar, and how in detail raising work quality and efficiency are all the targets constantly pursued, and the recycling of the energy also seems extremely important in addition.
Summary of the invention
The purpose of this utility model is exactly solve above-mentioned technical problem, provides a kind of centrifugal spray drying system, practical, can be fully dry, and increases work efficiency and recycle the energy.
Technical problem of the present utility model is solved mainly through following technical proposals:
A kind of centrifugal spray drying system, comprise drying tower, cyclone separator, described drying tower is provided with high speed atomisation device, this high speed atomisation device connects charging aperture, it is characterized in that: described drying tower is provided with hot-air distributor, scavenging conduit, described hot-air distributor connects heater and air inlet, described scavenging conduit connects high pressure admission mouth, described cyclone separator comprises large size cyclone separator and small size cyclone separator, aforementioned drying tower conical lower portion connects large size cyclone separator successively, small size cyclone separator, this small size cyclone separator is provided with recovery blower fan and is connected with aforementioned hot-air distributor.
Further, also cloth envelop collector is provided with between described large size cyclone separator and small size cyclone separator.
Further, described cloth envelop collector is provided with the whirlpool chamber that gathers materials.
Further, described in the whirlpool chamber one end that gathers materials connect small size cyclone separator, the other end connects air inlet and air dehumidifier.
Concrete, described drying tower, large size cyclone separator are equipped with emptying blower fan.
Concrete, described air inlet is provided with roughing efficiency air filter.
Concrete, described its conical lower portion of small size cyclone separator is provided with rewinding cylinder.
The beneficial effects of the utility model are: the utility model develops a kind of centrifugal spray drying system, have employed size two kinds of cyclone separators, realize the abundant drying of material, and product quality is upgraded further, and supply is high-end requires client; In addition, between two cyclone separators, additionally use cloth envelop collector and vortex chamber of gathering materials, in technique, also improve the capability and performance of product; Finally, the utility model is provided with recovery blower fan and is connected with hot-air distributor, by energy effective recycling, and energy-conserving and environment-protective.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1. drying tower; 2. high speed atomisation device; 3. charging aperture; 4. heater; 5. air inlet; 6. hot-air distributor; 7. scavenging conduit; 8. high pressure admission mouth; 9. large size cyclone separator; 10. small size cyclone separator; 11. cloth envelop collectors; 12. gather materials vortex chamber; 13. air dehumidifiers; 14. rewinding cylinders; 15. reclaim blower fan; 16. emptying blower fans.
Detailed description of the invention
Below by embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is described in further detail.
A kind of centrifugal spray drying system, comprise drying tower 1, cyclone separator, described drying tower 1 is provided with high speed atomisation device 2, this high speed atomisation device 2 connects charging aperture 3, described drying tower 1 is provided with hot-air distributor 6, scavenging conduit 7, described hot-air distributor 6 connects heater 4 and air inlet 5, described scavenging conduit 7 connects high pressure admission mouth 8, described cyclone separator comprises large size cyclone separator 9 and small size cyclone separator 10, aforementioned drying tower 1 conical lower portion connects large size cyclone separator 9 successively, small size cyclone separator 10, this small size cyclone separator 10 is provided with recovery blower fan 15 and is connected with aforementioned hot-air distributor 6.
Further, cloth envelop collector 11 is also provided with between described large size cyclone separator 9 and small size cyclone separator 10.Described cloth envelop collector 11 is provided with the whirlpool chamber 12 that gathers materials.Described whirlpool chamber 12 one end that gathers materials connects small size cyclone separator 10, and the other end connects air inlet 5 and air dehumidifier 13.Described drying tower 1, large size cyclone separator 9 are equipped with emptying blower fan 16.Described air inlet 5 is provided with roughing efficiency air filter.Described its conical lower portion of small size cyclone separator 10 is provided with rewinding cylinder 14.
The present embodiment is the embodiment of the utility model example; for those skilled in the art; on the basis that the utility model discloses application process and principle; be easy to make various types of improvement or distortion; and the structure be not limited only to described by the above-mentioned detailed description of the invention of the utility model; therefore previously described mode is preferred version; and not there is restrictive meaning; every equivalence done according to the utility model changes and amendment, all in the scope protection domain of the utility model claims.

Claims (7)

1. a centrifugal spray drying system, comprise drying tower, cyclone separator, described drying tower is provided with high speed atomisation device, this high speed atomisation device connects charging aperture, it is characterized in that: described drying tower is provided with hot-air distributor, scavenging conduit, described hot-air distributor connects heater and air inlet, described scavenging conduit connects high pressure admission mouth, described cyclone separator comprises large size cyclone separator and small size cyclone separator, aforementioned drying tower conical lower portion connects large size cyclone separator successively, small size cyclone separator, this small size cyclone separator is provided with recovery blower fan and is connected with aforementioned hot-air distributor.
2. a kind of centrifugal spray drying system according to claim 1, is characterized in that: be also provided with cloth envelop collector between described large size cyclone separator and small size cyclone separator.
3. a kind of centrifugal spray drying system according to claim 2, is characterized in that: described cloth envelop collector is provided with the whirlpool chamber that gathers materials.
4. a kind of centrifugal spray drying system according to claim 3, is characterized in that: described in the whirlpool chamber one end that gathers materials connect small size cyclone separator, the other end connects air inlet and air dehumidifier.
5. a kind of centrifugal spray drying system according to claim 1, is characterized in that: described drying tower, large size cyclone separator are equipped with emptying blower fan.
6. a kind of centrifugal spray drying system according to claim 1 or 4, is characterized in that: described air inlet is provided with roughing efficiency air filter.
7. a kind of centrifugal spray drying system according to claim 1, is characterized in that: described its conical lower portion of small size cyclone separator is provided with rewinding cylinder.
CN201420849338.XU 2014-12-27 2014-12-27 A kind of centrifugal spray drying system Expired - Fee Related CN204428856U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420849338.XU CN204428856U (en) 2014-12-27 2014-12-27 A kind of centrifugal spray drying system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420849338.XU CN204428856U (en) 2014-12-27 2014-12-27 A kind of centrifugal spray drying system

Publications (1)

Publication Number Publication Date
CN204428856U true CN204428856U (en) 2015-07-01

Family

ID=53596778

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420849338.XU Expired - Fee Related CN204428856U (en) 2014-12-27 2014-12-27 A kind of centrifugal spray drying system

Country Status (1)

Country Link
CN (1) CN204428856U (en)

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Legal Events

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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: 20150701

Termination date: 20191227

CF01 Termination of patent right due to non-payment of annual fee