CN101354212A - Vibration fluidization drying system - Google Patents
Vibration fluidization drying system Download PDFInfo
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- CN101354212A CN101354212A CNA2008100209539A CN200810020953A CN101354212A CN 101354212 A CN101354212 A CN 101354212A CN A2008100209539 A CNA2008100209539 A CN A2008100209539A CN 200810020953 A CN200810020953 A CN 200810020953A CN 101354212 A CN101354212 A CN 101354212A
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- gas
- solid separator
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- fluidized bed
- air
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- 238000001035 drying Methods 0.000 title claims abstract description 41
- 238000005243 fluidization Methods 0.000 title claims description 20
- 239000007787 solid Substances 0.000 claims abstract description 55
- 239000000463 material Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims description 25
- 238000007664 blowing Methods 0.000 claims description 22
- 238000007599 discharging Methods 0.000 claims description 18
- 239000004744 fabric Substances 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 4
- 238000004806 packaging method and process Methods 0.000 claims description 2
- 238000005303 weighing Methods 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 2
- 230000000694 effects Effects 0.000 description 8
- 150000001298 alcohols Chemical class 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 239000002352 surface water Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 1
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 1
- TVXBFESIOXBWNM-UHFFFAOYSA-N Xylitol Natural products OCCC(O)C(O)C(O)CCO TVXBFESIOXBWNM-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-LECHCGJUSA-N alpha-D-xylose Chemical compound O[C@@H]1CO[C@H](O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-LECHCGJUSA-N 0.000 description 1
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000000845 maltitol Substances 0.000 description 1
- VQHSOMBJVWLPSR-WUJBLJFYSA-N maltitol Chemical compound OC[C@H](O)[C@@H](O)[C@@H]([C@H](O)CO)O[C@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O VQHSOMBJVWLPSR-WUJBLJFYSA-N 0.000 description 1
- 235000010449 maltitol Nutrition 0.000 description 1
- 229940035436 maltitol Drugs 0.000 description 1
- 229960002160 maltose Drugs 0.000 description 1
- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000000811 xylitol Substances 0.000 description 1
- HEBKCHPVOIAQTA-SCDXWVJYSA-N xylitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)CO HEBKCHPVOIAQTA-SCDXWVJYSA-N 0.000 description 1
- 235000010447 xylitol Nutrition 0.000 description 1
- 229960002675 xylitol Drugs 0.000 description 1
- 229960003487 xylose Drugs 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The invention relates to a vibrating-fluidized drying system, aiming at carrying out fluidized drying to wet alcohol raw materials. The vibrating-fluidized drying system comprises a vibrating-fluidized bed, a vibrating screen, a monolith crusher, a first gas-solid separator and a first gas valve; the vibrating screen connected with a discharge opening of the vibrating-fluidized bed comprises: a big grain-diameter outlet and a small grain-diameter outlet; the big grain-diameter outlet is connected with an intake opening of the first gas-solid separator by the monolith crusher, and a discharge opening of the first gas-solid separator is connected with an intake opening of the vibrating-fluidized bed. A big grain-diameter material dried and output by the vibrating-fluidized bed is effectively screened and crushed by the vibrating screen and the monolith crusher in sequence, then the big grain-diameter material is crushed to be small grain-diameter and delivered by the first gas-solid separator and the first gas valve to the vibrating-fluidized bed for being continuously dried and finally output from the small grain-diameter outlet of the vibrating screen, thereby realizing the purpose of carrying out vibrating-fluidized drying to the wet alcohol raw materials liable to form bigger blocks.
Description
Technical field
The present invention relates to a kind of vibration fluidization drying system that granular material is carried out fluidized drying.
Background technology
Existing vibrating fluid bed dryer, as the disclosed vibratory liquefaction bed apparatus of Japan Patent JP1245847, the disclosed Vibratingfluidbeddrier of Chinese patent literature CN2042584U, the disclosed fluid bed dryer of Chinese patent CN2077531U, the disclosed a kind of vibration composite fluidization bed dryer of Chinese patent CN2201633Y, though it is different on their structures, but something in common is to swash power shaking to introduce gas fluidized bed, the material particle is shaken swash the effect of power to be the jump fluidized state, dry institute calorific requirement is all provided by the hot-air that the outside feeds.
Chinese patent literature CN2833468 discloses a kind of revert type fluidized bed desiccation equipment, comprise feeder, fluid bed, air-heater and heater, air-cooler, discharger, particularly the other end of discharger links to each other with carrying distributor, carry two outlet valves of the distributor other end to link to each other with product pipeline with the returning charge pipeline respectively, the returning charge pipeline other end links to each other with upper end, returning charge storehouse, and the rotary unloading valve of the lower end in returning charge storehouse links to each other with feeder by pipeline.
Chinese patent literature CN1291920 discloses a kind of fluidized bed drying, grading plant, has the main body of the fluid bed of portion's formation within it, can be used for making powder shape raw material drying and it is classified as particulate and coarse grain.The downside that fluid bed in main body forms the zone is provided with porous template gas distribution grid, is provided with the infundibulate bellows at the downside of porous template gas distribution grid.Be connected with the dropping discharger so that discharge the dropping that falls in the bellows in the lower end of bellows.Be connected with gas supply system at the bellows place so that dryly infeed in the bellows with hot blast and classification fluidized gas with the gas effect having.
Above-mentioned the deficiencies in the prior art part is: can not carry out effective fluidized drying to wet alcohols feedstock (comprising: maltitol, xylitol, maltose and wood sugar etc.).These wet alcohols feedstock are crystalline solid, and often there is surface water in good fluidity on the crystal, and therefore moisture-sensitive in the normal temperature air easily forms bigger bulk, and existing fluidized bed drying equipment can not effectively be pulverized with dry it, and uncontrollable its humidity.
Summary of the invention
Technical problem to be solved by this invention provides a kind of vibration fluidization drying system that can carry out fluidized drying to wet alcohols feedstock.
For solving the problems of the technologies described above, the invention provides a kind of vibration fluidization drying system, comprising: vibrated fluidized bed is characterized in: also comprise: vibratory sieve, material all in one piece disintegrating machine, first gas-solid separator and first Blowing stopper; The vibratory sieve that links to each other with the discharging opening of vibrated fluidized bed comprises: big particle diameter outlet and small particle diameter outlet; Big particle diameter outlet links to each other through the feeding mouth of material all in one piece disintegrating machine with first gas-solid separator, and the discharging opening of first gas-solid separator links to each other with the charging aperture of vibrated fluidized bed through first Blowing stopper.
In the technique scheme, also comprise: second gas-solid separator and second Blowing stopper, the top of described vibrated fluidized bed is provided with a plurality of openings, and each opening links to each other with the feeding mouth of second gas-solid separator, and the discharging opening of second gas-solid separator links to each other with vibratory sieve through second Blowing stopper.
The present invention has positive effect: in (1) vibration fluidization drying system of the present invention, through the big particle diameter raw material of vibra fluidized bed drying output successively behind vibratory sieve and material all in one piece disintegrating machine, effective screening and pulverizing have been obtained, make big particle diameter raw material become small particle diameter, send into vibrated fluidized bed and continue drying through first gas-solid separator and first Blowing stopper then, and finally export from the small particle diameter outlet of vibratory sieve.Thereby realized that commute forms the purpose that the wet alcohols feedstock of relatively large shape is carried out fluidized drying.(2) in the vibration fluidization drying system of the present invention, particle from the wet alcohols feedstock that the feeding mouth of vibrated fluidized bed is sent into direct opening from the vibrated fluidized bed top under the effect of air-flow enters second gas-solid separator, behind second Blowing stopper, send into the whirlwind returning charge mouth of vibratory sieve, because only there is surface water in described particle, therefore it can obtain drying rapidly in vibrated fluidized bed, therefore can directly enter second gas-solid separator, behind second Blowing stopper, send into vibratory sieve, to improve drying efficiency.
Description of drawings
Fig. 1 is the structural representation of vibration fluidization drying system of the present invention;
Fig. 2 is the structural representation of vibratory sieve of the present invention;
Fig. 3 is that the A of Fig. 2 is to view;
Fig. 4 is the zoomed-in view of local B among Fig. 2.
The specific embodiment
(embodiment 1)
See Fig. 1, the vibration fluidization drying system of present embodiment comprises: vibrated fluidized bed 4, the vibratory sieve 18 that links to each other with the discharging opening 4-2 of vibrated fluidized bed 4, material all in one piece disintegrating machine 19, first gas-solid separator 1 and first Blowing stopper 2, second gas-solid separator 5 and second Blowing stopper 6, automatically package system, be used to export the combined type dehumidifier 17 of low temperature drying air-flow.
Vibrated fluidized bed 4 inside are provided with the bed board 4-7 of vibrating motor 4-5 and band passage, and bed board 4-7 is provided with baroceptor PI and temperature sensor TI.One end of vibrated fluidized bed 4 is feeding mouth 4-1, and the other end is discharging opening 4-2.Feeding mouth 4-1 links to each other with pan feeding pipeline a.RIC among Fig. 1 is a moment conditioning sterilizing unit, and TIC is the temperature indicator controller.
See Fig. 2-3, vibratory sieve 18 comprises: sieve nest 18-9, be located at a plurality of beam 18-7 of sieve nest 18-9 lower end, the plate 18-8 that gathers materials that is located at screen cloth 18-5 and the vibrating motor 18-6 in the sieve nest 18-9 and is located at screen cloth 18-5 below; Screen cloth 18-5 top is provided with charging aperture 18-3 and whirlwind returning charge mouth 18-4, and charging aperture 18-3 links to each other with the discharging opening 4-2 of vibrated fluidized bed 4, and the discharging opening of described second gas-solid separator 5 links to each other with whirlwind returning charge mouth 18-4 through second Blowing stopper 6.The particle diameter of the raw material by screen cloth 18-5 is 20 orders.
See Fig. 3, be connected with big particle diameter outlet 18-1 on the upper surface of screen cloth 18-5; See Fig. 1, big particle diameter outlet 18-1 links to each other through the feeding mouth of material all in one piece disintegrating machine 19 with first gas-solid separator 1, and the discharging opening of first gas-solid separator 1 links to each other with the returning charge mouth 4-6 of vibrated fluidized bed 4 through first Blowing stopper 2.
See Fig. 2, be connected with small particle diameter outlet 18-2 on the upper surface of the described plate 18-8 that gathers materials, small particle diameter outlet 18-2 links to each other with the inlet of automatic package system, and the dry material of handling is directly encapsulated, and prevents that it from being polluted by humid air, influences drying effect.
See Fig. 1, the top of vibrated fluidized bed 4 is provided with a plurality of openings (being generally 4 to 10), and each opening links to each other with the feeding mouth of second gas-solid separator 5, and the discharging opening of second gas-solid separator 5 links to each other with the whirlwind returning charge mouth 18-4 of vibratory sieve 18 through second Blowing stopper 6.Particle from the wet alcohols feedstock that feeding mouth 4-1 sends into directly enters second gas-solid separator 5 from described opening under the effect of air-flow, behind second Blowing stopper 6, send into the whirlwind returning charge mouth 18-4 of vibratory sieve 18, because described particle can obtain drying rapidly in vibrated fluidized bed 4, therefore improved drying efficiency.
The lower end 4-4 of the bringing-up section of described vibrated fluidized bed 4 is connected with hot air duct, and the lower end 4-3 of the cooling section of vibrated fluidized bed 4 is connected with cold air duct.
Hot air duct comprises: filter 12, air blast 13, high efficiency particulate air filter 14 and air heater 15 are imitated in the junior middle school of Xiang Lianing successively; The outlet side of air heater 15 links to each other with the lower end 4-4 of the bringing-up section of vibrated fluidized bed 4.Imitate filter 12 and high efficiency particulate air filter 14 and be used for the air of importing in the hot air duct is carried out dedusting and dehumidifying is filtered the junior middle school, and the air of guaranteeing to send into vibrated fluidized bed 4 is a heated drying air.
Cold air duct comprises: filter 22, second air blast 23, second high efficiency particulate air filter 24 and aerial cooler 16 are imitated in second junior middle school of Xiang Lianing successively; The outlet side of aerial cooler 16 links to each other with the lower end 4-3 of the cooling section of vibrated fluidized bed 4, guarantees that the air of sending into vibrated fluidized bed 4 is dry cold air.
Be connected with whirlpool air pump 3 on the air-vent at first gas-solid separator, 1 top, the feeding mouth of first gas-solid separator 1 is provided with feed pipe 1-1, the tubular inner wall of the feed pipe 1-1 and first gas-solid separator 1 is tangent, when guaranteeing that material enters first gas-solid separator, 1 inwall, directly act on mutually, to carry out gas solid separation rapidly and to guarantee gas-solid separating effect with the interior vortical flow of first gas-solid separator 1.
The feeding mouth of described second gas-solid separator 5 is provided with feeding pipe 5-1, and the tubular inner wall of the feeding pipe 5-1 and second gas-solid separator 5 is tangent, to guarantee gas-solid separating effect and separating rate; Be connected with sack cleaner 7 on the air-vent at second gas-solid separator, 5 tops, be connected with air-introduced machine 8 on the air-vent at sack cleaner 7 tops, to provide vortical flow to second gas-solid separator 5.
See Fig. 2 and 4, be provided with the many gussets that parallel in the sieve nest 18-9 of described vibratory sieve 18, the two ends of each gusset and sieve nest 18-9 inwall are fixedly linked; Each gusset comprises that correspondence is located at top board b1 and the lower platen b2 on the screen cloth 18-5 upper and lower end face, and top board b1 and lower platen b2 are fixedly linked by bolt b3, thereby make screen cloth 18-5 remain tensioning state, guarantee screening effect.
Described automatic package system comprises: the 3rd gas-solid separator 9 that links to each other with the small particle diameter outlet 18-2 of described vibratory sieve 18, the discharging opening of the 3rd gas-solid separator 9 links to each other with finished product basin 20 through the 3rd Blowing stopper 10, the discharging opening of finished product basin 20 links to each other with the packaging machine 30 of weighing automatically through the 4th Blowing stopper 21, thus the function that realization is weighed automatically and encapsulated.
Connect second air-introduced machine 11 on the air-vent of the 3rd gas-solid separator 9, the source of the gas end of the 3rd gas-solid separator 9 and the source of the gas end of material all in one piece disintegrating machine 19 all link to each other with combined type dehumidifier 17, to guarantee that the air that raw material was contacted after dry the processing is a low temperature drying gas, with the humidity of the raw material after the dry processing of effective control.
Among Fig. 1, h is the intake line of 160-170 ℃ vapours, and c is the air intake line, d Be the cold water watering pipeline, e is the air intake line, and f is the condensate output transistor road, and g is cold-water return Pipeline.
Claims (10)
1, a kind of vibration fluidization drying system comprises: vibrated fluidized bed (4) is characterized in that: also comprise: vibratory sieve (18), material all in one piece disintegrating machine (19), first gas-solid separator (1) and first Blowing stopper (2); The vibratory sieve (18) that links to each other with the discharging opening (4-2) of vibrated fluidized bed (4) comprising: big particle diameter outlet (18-1) and small particle diameter outlet (18-2); Big particle diameter outlet (18-1) links to each other through the feeding mouth of material all in one piece disintegrating machine (19) with first gas-solid separator (1), and the discharging opening of first gas-solid separator (1) links to each other with the returning charge mouth (4-6) of vibrated fluidized bed (4) through first Blowing stopper (2).
2, vibration fluidization drying system according to claim 1, it is characterized in that: also comprise: second gas-solid separator (5) and second Blowing stopper (6), the top of described vibrated fluidized bed (4) is provided with a plurality of openings, each opening links to each other with the feeding mouth of second gas-solid separator (5), and the discharging opening of second gas-solid separator (5) links to each other with vibratory sieve (18) through second Blowing stopper (6).
3, vibration fluidization drying system according to claim 1 and 2 is characterized in that: also comprise automatic package system, the small particle diameter outlet (18-2) of described vibratory sieve (18) links to each other with the inlet of automatic package system.
4, vibration fluidization drying system according to claim 1 and 2 is characterized in that: the lower end of the bringing-up section of described vibrated fluidized bed (4) is connected with hot air duct, and the lower end of the cooling section of vibrated fluidized bed (4) is connected with cold air duct;
Hot air duct comprises: filter (12), air blast (13), high efficiency particulate air filter (14) and air heater (15) are imitated in the junior middle school of Xiang Lianing successively; The outlet side of air heater (15) links to each other with the lower end of the bringing-up section of vibrated fluidized bed (4);
Cold air duct comprises: filter (22), second air blast (23), second high efficiency particulate air filter (24) and aerial cooler (16) are imitated in second junior middle school of Xiang Lianing successively; The outlet side of aerial cooler (16) links to each other with the lower end of the cooling section of vibrated fluidized bed (4).
5, vibration fluidization drying system according to claim 1 and 2 is characterized in that: the feeding mouth of described first gas-solid separator (1) is provided with feed pipe (1-1), and feed pipe (1-1) is tangent with the inwall of first gas-solid separator (1); Be connected with whirlpool air pump (3) on the air-vent at first gas-solid separator (1) top.
6, vibration fluidization drying system according to claim 1 and 2 is characterized in that: the feeding mouth of described second gas-solid separator (5) is provided with feeding pipe (5-1), and feeding pipe (5-1) is tangent with the inwall of second gas-solid separator (5); Be connected with sack cleaner (7) on the air-vent at second gas-solid separator (5) top, be connected with air-introduced machine (8) on the air-vent at sack cleaner (7) top.
7, vibration fluidization drying system according to claim 3 is characterized in that: described vibratory sieve (18) comprising: sieve nest (18-9), the plate that gathers materials (18-8) of being located at screen cloth (18-5) and the vibrating motor (18-6) in the sieve nest (18-9) and being located at screen cloth (18-5) below; Screen cloth (18-5) top is provided with charging aperture (18-3) and whirlwind returning charge mouth (18-4), charging aperture (18-3) links to each other with the discharging opening (4-2) of vibrated fluidized bed (4), and the discharging opening of described second gas-solid separator (5) links to each other with whirlwind returning charge mouth (18-4) through second Blowing stopper (6); Described big particle diameter outlet (18-1) links to each other with the upper surface of screen cloth (18-5), and small particle diameter outlet (18-2) links to each other with the upper surface of the plate that gathers materials (18-8).
8, vibration fluidization drying system according to claim 7 is characterized in that: be provided with the many gussets that parallel in the described sieve nest (18-9), the two ends of each gusset and sieve nest (18-9) inwall is fixedly linked; Each gusset comprises that correspondence is located at top board (b1) and the lower platen (b2) on screen cloth (18-5) upper and lower end face, and top board (b1) is fixedly linked by bolt (b3) with lower platen (b2).
9, vibration fluidization drying system according to claim 1 and 2 is characterized in that: also comprise the combined type dehumidifier (17) that is used to export the low temperature drying air-flow, combined type dehumidifier (17) links to each other with the source of the gas end of material all in one piece disintegrating machine (19).
10, vibration fluidization drying system according to claim 9, it is characterized in that: described automatic package system comprises: the 3rd gas-solid separator (9) that links to each other with the small particle diameter outlet (18-2) of described vibratory sieve (18), the discharging opening of the 3rd gas-solid separator (9) links to each other with finished product basin (20) through the 3rd Blowing stopper (10), and the discharging opening of finished product basin (20) links to each other with the packaging machine of weighing automatically (30) through the 4th Blowing stopper (21); Connect second air-introduced machine (11) on the air-vent of the 3rd gas-solid separator (9), the source of the gas end of the 3rd gas-solid separator (9) links to each other with combined type dehumidifier (17).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2008100209539A CN100554840C (en) | 2008-08-11 | 2008-08-11 | Vibration fluidization drying system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2008100209539A CN100554840C (en) | 2008-08-11 | 2008-08-11 | Vibration fluidization drying system |
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| Publication Number | Publication Date |
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| CN101354212A true CN101354212A (en) | 2009-01-28 |
| CN100554840C CN100554840C (en) | 2009-10-28 |
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| CNB2008100209539A Expired - Fee Related CN100554840C (en) | 2008-08-11 | 2008-08-11 | Vibration fluidization drying system |
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| CN103322773A (en) * | 2013-06-30 | 2013-09-25 | 金川集团股份有限公司 | System and method for drying sodium sulfite materials |
| CN103925784A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Multi-layer vibrating dryer |
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| CN103322773B (en) * | 2013-06-30 | 2015-06-17 | 金川集团股份有限公司 | System and method for drying sodium sulfite materials |
| CN103322773A (en) * | 2013-06-30 | 2013-09-25 | 金川集团股份有限公司 | System and method for drying sodium sulfite materials |
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| CN104274321A (en) * | 2013-07-11 | 2015-01-14 | 天士力制药集团股份有限公司 | Air-cooled dropping pill production line |
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| CN104274328A (en) * | 2013-07-11 | 2015-01-14 | 天士力制药集团股份有限公司 | Air-cooled dropping pill production line |
| CN103925784A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Multi-layer vibrating dryer |
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| CN100554840C (en) | 2009-10-28 |
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