CN204154061U - A kind of high speed centrifugation atomization drying equipment producing Lauxite powder - Google Patents
A kind of high speed centrifugation atomization drying equipment producing Lauxite powder Download PDFInfo
- Publication number
- CN204154061U CN204154061U CN201420570532.4U CN201420570532U CN204154061U CN 204154061 U CN204154061 U CN 204154061U CN 201420570532 U CN201420570532 U CN 201420570532U CN 204154061 U CN204154061 U CN 204154061U
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- air
- separator
- high speed
- drying tower
- speed centrifugation
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Abstract
The utility model discloses a kind of high speed centrifugation atomization drying equipment producing Lauxite powder, comprise gasification burner, hot-air distributor, centrifugal atomizer, drying tower, cyclone separator and feed bin, it is characterized in that: described gasification burner is connected to hot-air distributor by warm-air pipe, hot-air distributor connects centrifugal atomizer, centrifugal atomizer is positioned at drying tower inner upper end, drying tower lower end is connected to discharge pipe, discharge pipe is connected to cyclone separator, cyclone separator comprises the willy-willy separator and whirly separator that are connected in series, willy-willy separator top is connected to air-introduced machine, whirly separator top is connected to circulating fan, whirly separator upper side send pipe to be connected to dehumidifier by wind, whirly separator lower end is connected to feed bin, feed bin lower end connects vibratory sieve.The utility model powder not easily glues wall and drying is complete.
Description
Technical field
The utility model relates to a kind of atomization drying equipment, particularly relates to a kind of high speed centrifugation atomization drying equipment producing Lauxite powder.
Background technology
In fields such as chemical industry, petrochemical industry, light industry, food, medicine, building materials, potteries, often need to be dried to dry powder to some solution, emulsion, suspension, pasty material, current general spray dryer realizes.Produce Lauxite generally adopt be dried powdered, easy preservation and can the pot-life be extended, but existing atomization drying equipment makes Lauxite powder not exclusively dry because the moisture in air enters in cyclone separator when entering cyclone separator discharging after by Lauxite liquid dried powdered, thus affects its pot-life.
Summary of the invention
For above-mentioned the deficiencies in the prior art, the utility model provides a kind of drying completely and be not easy to cause powder to glue the high speed centrifugation atomization drying equipment of the production Lauxite powder of wall.
A kind of high speed centrifugation atomization drying equipment producing Lauxite powder, comprise gasification burner, hot-air distributor, centrifugal atomizer, drying tower, cyclone separator and feed bin, it is characterized in that: described gasification burner is connected to hot-air distributor by warm-air pipe, hot-air distributor connects centrifugal atomizer, centrifugal atomizer is positioned at drying tower inner upper end, the outlet of drying tower lower end is connected to discharge pipe, discharge pipe is connected to cyclone separator, cyclone separator comprises the willy-willy separator and whirly separator that are connected in series, willy-willy separator top is connected to air-introduced machine, whirly separator top is connected to circulating fan, whirly separator upper side send pipe to be connected to dehumidifier by wind, whirly separator lower end is connected to feed bin, feed bin lower end connects vibratory sieve.
Described gasification burner is connected with pressure fan, air cleaner and burner, and described burner can be wooden chaff burner, diesel fuel burner.
In the shape of a spiral, drying tower top is provided with charging aperture in described drying tower inside.
Described drying tower lower end is connected to air sweepers, and air sweepers is provided with one, and to stretch into drying tower inner and against drying tower inwall and carry out revolving the stainless steel tube swept, and can stick to the powder cleaning of drying tower inwall.
Described willy-willy separator and whirly separator bottom are equipped with feed bin, and feed bin discharge hole place is provided with vacuum butterfly valve.
Described air-introduced machine is scroll casing type air-introduced machine, is connected to sack cleaner after air-introduced machine.
The beneficial effects of the utility model are:
1, connect air sweepers bottom the utility model drying tower, the stainless steel tube that air sweepers is provided with enters in drying tower to revolve along inwall and sweeps, and solves the problem that material glues wall;
2, the utility model connects dehumidifier in whirly separator upper end, can by cyclone separator with moisture drain, the Lauxite powder drying making acquisition is more complete, extends the pot-life of Lauxite powder.
Accompanying drawing explanation
Fig. 1 is main schematic diagram of the present utility model;
Fig. 2 is side schematic view of the present utility model.
In figure, 1-gasification burner, 2-warm-air pipe, 3-hot-air distributor, 4-drying tower, 5-discharge pipe, 6-willy-willy separator, 7-whirly separator, 8-circulating fan, 9-feed bin, 10-induced duct, 11-air-introduced machine, 12-sack cleaner, 13-air sweepers, 14-wind send pipe, 15-dehumidifier, 101-burner, 102-charging aperture, 103-stainless steel tube.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in further detail.
A kind of high speed centrifugation atomization drying equipment producing Lauxite powder, comprise gasification burner 1, hot-air distributor 3, centrifugal atomizer, drying tower 4, cyclone separator and feed bin 9, air cleaner is connected with before gasification burner 1, pressure fan and burner 101, air cleaner is for removing the impurity in air, make air purer, burner is wooden chaff burner, gasification burner 1 is connected to hot-air distributor 3 by warm-air pipe 2, hot-air distributor 3 connects centrifugal atomizer, centrifugal atomizer is positioned at drying tower 4 inner upper end, drying tower 4 top is provided with the charging aperture 102 be connected with centrifugal atomizer, drying tower 4 inside is in the shape of a spiral down to bottom, drying tower 4 outlet at bottom is connected to discharge pipe 5, discharge pipe 5 connects willy-willy separator 6 and whirly separator 7, drying tower 4 lower end is provided with air sweepers 13, air sweepers 13 is provided with one, and to stretch into drying tower 4 inner and against drying tower 4 inwall and carry out revolving the stainless steel tube 103 swept, by this stainless steel tube 103 pairs of drying tower inwalls revolve clear away clean can will stick to drying tower inwall powder cleaning.
Described willy-willy separator 6 and whirly separator 7 are for being connected in series, willy-willy separator 6 top is connected to air-introduced machine 11 through induced duct 10, air-introduced machine 11 is connected to sack cleaner 12, described air-introduced machine 11 is scroll casing type air-introduced machine, whirly separator 7 is fixed on separator platform, whirly separator 7 top is connected to circulating fan 8, whirly separator 7 upper side send pipe 14 to be connected to dehumidifier 15 by wind, whirly separator 7 lower end is connected to feed bin 9, and feed bin 9 lower end connects vibratory sieve.
Be equipped with feed bin bottom described willy-willy separator 6 and whirly separator 7, feed bin discharge hole place is provided with vacuum butterfly valve.
After air is sent into air cleaner and gasification burner 1 by pressure fan, the hot-air distributor 3 at drying tower 4 top is entered through warm-air pipe 2, enter in drying tower 4 equably by the hot-air of hot-air distributor 3, and rotate in the shape of a spiral and enter bottom drying tower 4 downwards, after temperature reaches preset value, Lauxite liquid is entered by charging aperture 102 by being pumped into drying tower 4 top, feed liquid is first through the centrifugal atomizer of device upper end in drying tower, by centrifugal atomizer, feed liquid is atomized in droplet, when just rapid vaporizing and drying powdered product after droplet with the hot air entering in drying tower, dry powder-product fall drying tower inwall and bottom rotary sliding to drying tower extract by the willy-willy separator 6 that is connected with discharge pipe 5 out, the air-flow extracted out through willy-willy separator 6 enters scroll casing type air-introduced machine 11, finally enter sack cleaner 12, air-flow is discharged, thinner powder then catch by whirly separator 7, the dehumidifier 15 be simultaneously connected with whirly separator 7 by powder with moisture take away, powder enters the feed bin 9 li being arranged on whirly separator 7 lower end, open the vacuum butterfly valve being arranged on feed bin 9 discharge outlet again, powder enters the vibratory sieve be connected with discharging opening, through screening, obtain 60 object Lauxite powders.
Connect air sweepers bottom the utility model drying tower, the stainless steel tube that air sweepers is provided with enters in drying tower to revolve along inwall and sweeps, and solves the problem that material glues wall; Connect dehumidifier in whirly separator upper end, can by cyclone separator with moisture drain, the Lauxite powder drying making acquisition is more complete, extends the pot-life of Lauxite powder.
Claims (9)
1. produce the high speed centrifugation atomization drying equipment of Lauxite powder for one kind, comprise gasification burner, hot-air distributor, centrifugal atomizer, drying tower, cyclone separator and feed bin, it is characterized in that: described gasification burner is connected to hot-air distributor by warm-air pipe, hot-air distributor connects centrifugal atomizer, centrifugal atomizer is positioned at drying tower inner upper end, the outlet of drying tower lower end is connected to discharge pipe, discharge pipe is connected to cyclone separator, cyclone separator comprises the willy-willy separator and whirly separator that are connected in series, willy-willy separator top is connected to air-introduced machine, whirly separator top is connected to circulating fan, whirly separator upper side send pipe to be connected to dehumidifier by wind, whirly separator lower end is connected to feed bin, feed bin lower end connects vibratory sieve.
2. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, is characterized in that: described gasification burner is connected with pressure fan, air cleaner and burner.
3. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 2, is characterized in that: described burner can be wooden chaff burner, diesel fuel burner.
4. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, is characterized in that: described drying tower inside in the shape of a spiral.
5. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, is characterized in that: drying tower top is provided with charging aperture.
6. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, is characterized in that: described drying tower lower end is connected to air sweepers.
7. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 6, is characterized in that: air sweepers is provided with one, and to stretch into drying tower inner and against drying tower inwall and carry out revolving the stainless steel tube swept.
8. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, it is characterized in that: be provided with feed bin bottom cyclone separator, feed bin discharge hole place is provided with vacuum butterfly valve.
9. the high speed centrifugation atomization drying equipment of production Lauxite powder according to claim 1, is characterized in that: described air-introduced machine is scroll casing type air-introduced machine, is connected to sack cleaner after air-introduced machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420570532.4U CN204154061U (en) | 2014-09-30 | 2014-09-30 | A kind of high speed centrifugation atomization drying equipment producing Lauxite powder |
Applications Claiming Priority (1)
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CN201420570532.4U CN204154061U (en) | 2014-09-30 | 2014-09-30 | A kind of high speed centrifugation atomization drying equipment producing Lauxite powder |
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CN204154061U true CN204154061U (en) | 2015-02-11 |
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CN201420570532.4U Expired - Fee Related CN204154061U (en) | 2014-09-30 | 2014-09-30 | A kind of high speed centrifugation atomization drying equipment producing Lauxite powder |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111707068A (en) * | 2020-07-02 | 2020-09-25 | 浙江汇翔化学工业有限公司 | Drying equipment for production of polycarboxylate water reducing agent |
CN113856226A (en) * | 2021-10-27 | 2021-12-31 | 山东省绿士农药有限公司 | Dry suspending agent type pesticide production line |
-
2014
- 2014-09-30 CN CN201420570532.4U patent/CN204154061U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111707068A (en) * | 2020-07-02 | 2020-09-25 | 浙江汇翔化学工业有限公司 | Drying equipment for production of polycarboxylate water reducing agent |
CN111707068B (en) * | 2020-07-02 | 2021-11-09 | 浙江汇翔新材料科技股份有限公司 | Drying equipment for production of polycarboxylate water reducing agent |
CN113856226A (en) * | 2021-10-27 | 2021-12-31 | 山东省绿士农药有限公司 | Dry suspending agent type pesticide production line |
CN113856226B (en) * | 2021-10-27 | 2022-09-13 | 山东省绿士农药有限公司 | Dry suspending agent type pesticide production line |
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Legal Events
Date | Code | Title | Description |
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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: 20150211 Termination date: 20170930 |
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CF01 | Termination of patent right due to non-payment of annual fee |