CN205106274U - Soybean dietary fiber guarantees quality to dewater and uses drying -machine - Google Patents
Soybean dietary fiber guarantees quality to dewater and uses drying -machine Download PDFInfo
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- CN205106274U CN205106274U CN201520836334.2U CN201520836334U CN205106274U CN 205106274 U CN205106274 U CN 205106274U CN 201520836334 U CN201520836334 U CN 201520836334U CN 205106274 U CN205106274 U CN 205106274U
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- auger
- air
- drying tower
- bipacking
- dietary fiber
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Abstract
The utility model relates to a soybean dietary fiber guarantees quality to dewater and uses drying -machine, including two auger compounding conveyers, drying tower, cyclone I, air -blower and air heater, be provided with drier import and wet material import on two auger compounding conveyers, two auger compounding conveyers include two auger poles, the both ends of two auger poles are provided with oar form bits, and the centre is provided with helical blade, and the oar form bits staggered arrangement of each other on two auger poles, and the meshing cross arrangement of helical blade one -to -one carries the drying tower after dry material and wet stock mix in two auger compounding conveyers, the discharge end of drying tower and cyclone's I feeding end connection, the air outlet of air -blower passes through the air intake connection of air heater and drying tower. The utility model discloses a drying -machine improved drying efficiency greatly and the product quality that produces good, reduced manufacturing cost simultaneously.
Description
Technical field
The utility model relates to soybean dietary fiber production and processing field of mechanical technique, and particularly a kind of soybean dietary fiber is guaranteed the quality dehydration dryer.
Background technology
In soybean dietary fiber production technology, by Non-transgenic soybean dregs of rice pyrohydrolysis, centrifugation, and carry out sufficient purification, eliminated solubility sugar and partially protein, soybean dietary fiber is shown good water holding and emulsification function.The Semifinished fibre obtained, before crushing packing, must carry out drying.Because the cellulose after pyrohydrolysis presents wet glutinous state, cellulose moisture content still more than 85% and at the temperature of about 80 degrees Celsius viscosity be similar to rice cake, so dehydrate very difficult to it.Soybean dietary fiber dehydration dryer heat transfer property of the prior art is poor, material is with good adherence of in drying unit, mass transport difficulty, thus causing trouble rate is high, material not easily disperses after entering drying tower, cause piling up at the charging aperture of drying tower, reduce drying efficiency, and cause poor product quality, production cost high.
Utility model content
The purpose of this utility model is to provide a kind of soybean dietary fiber and guarantees the quality dehydration dryer, the bipacking-auger batch mixing conveyer of dryer ensure that certain pusher ability while ensure that the moisture infiltrating time between dry material and wet stock, material easily disperses after entering drying tower, substantially increase drying efficiency, and the failure rate is low of dryer, the good product quality produced, reduces production cost.
In order to solve the problems of the technologies described above, the technical scheme that the utility model adopts is: a kind of soybean dietary fiber is guaranteed the quality dehydration dryer, comprise bipacking-auger batch mixing conveyer, drying tower, cyclone separator I, air blast and air heater, described bipacking-auger batch mixing conveyer is provided with siccative import and wet feed import, described bipacking-auger batch mixing conveyer comprises two auger bars, the two ends of described two auger bars are provided with paddle gear piece, centre is provided with helical blade, and the paddle gear piece on two auger bars is mutually staggeredly arranged, helical blade engages arranged crosswise one to one, dry material and wet stock are transported in drying tower after mixing in bipacking-auger batch mixing conveyer, the discharge end of drying tower is connected with the feed end of cyclone separator I, the air outlet of described air blast is connected with the air inlet of drying tower by air heater.
Further, drying unit also comprises siccative pumpback device, described siccative pumpback device comprises whirlwind discharger, quantitatively return material packing auger conveyer and air-introduced machine, the discharge end of whirlwind discharger is connected with the siccative import of bipacking-auger batch mixing conveyer and sends into dry material in bipacking-auger batch mixing conveyer, the feed end of described quantitative return material packing auger conveyer is connected with the discharge end of cyclone separator I and the feed end of whirlwind discharger respectively with discharge end, and the air outlet of described air-introduced machine is connected with the air inlet of dry whirlwind discharger.
Further, the air inlet of described air-introduced machine is connected with drying tower.
Further, drying unit also comprises centrifugal batcher, and the discharge end of described centrifugal batcher is connected with the wet feed import of bipacking-auger batch mixing conveyer.
Further, drying unit also comprises cyclone separator II, and the air outlet of described cyclone separator I is connected with the air inlet of cyclone separator II.
Further, described drying tower is provided with decentralized institution in the cavity of its feed end, described decentralized institution comprises four cross mixing blade arranged in parallel, two mutual vertically disposed Eight characters blades and rotating shaft, described four cross mixing blade along rotating shaft axial direction successively winding on the rotary shaft and mutually arranged in a crossed manner, the winding of described Eight characters blade on the rotary shaft and be arranged on the below of cross mixing blade.
Compared with prior art, the utility model has following beneficial effect: the utility model makes siccative mix with wet feed by arranging siccative pumpback device, and reduce humidity and the viscosity of material, material, not with good adherence of in dryer, reduces the fault rate of dryer.By arranging paddle gear piece and helical blade in bipacking-auger batch mixing conveyer, certain pusher ability is ensure that while ensure that the moisture infiltrating time between dry material and wet stock, by arranging decentralized institution, form ring-type cloth air port, material is easily disperseed, the heating surface area and the hot blast wind that add material send ability simultaneously, substantially increase the drying efficiency of dryer and the good product quality produced, reduce production cost simultaneously.
Accompanying drawing explanation
Fig. 1 is that the utility model soybean dietary fiber is guaranteed the quality the structural representation of dehydration dryer;
Fig. 2 is that the utility model soybean dietary fiber is guaranteed the quality the bipacking-auger batch mixing conveyor construction schematic diagram of dehydration dryer;
Fig. 3 is B place broken section enlarged drawing in the utility model Fig. 1;
Fig. 4 is A-A place sectional view in the utility model Fig. 1;
Mark in figure: 1, centrifugal batcher, 2, whirlwind discharger, 3, bipacking-auger batch mixing conveyer, 301, auger bar, 302, paddle gear piece, 303, helical blade, 4, drying tower, 5, cyclone separator I, 6, quantitatively return material packing auger conveyer, 7, air blast, 8, air heater, 9, cyclone separator II, 10, air-introduced machine, 11, decentralized institution, 1101, cross mixing blade, 1102, Eight characters blade, 1103, rotating shaft.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is elaborated; the present embodiment is premised on technical solutions of the utility model; give detailed embodiment and concrete operating process, but protection domain of the present utility model is not limited to following embodiment.
As shown in the figure, a kind of soybean dietary fiber is guaranteed the quality dehydration dryer, comprise bipacking-auger batch mixing conveyer 3, drying tower 4, cyclone separator I 5, air blast 7 and air heater 8, described bipacking-auger batch mixing conveyer 3 is provided with siccative import and wet feed import, described bipacking-auger batch mixing conveyer 3 comprises two auger bars 301, the two ends of described two auger bars 301 are provided with paddle gear piece 302, centre is provided with helical blade 303, and the paddle gear piece 302 on two auger bars 301 is mutually staggeredly arranged, helical blade 303 engages arranged crosswise one to one, dry material and wet stock are transported in drying tower 4 after mixing in bipacking-auger batch mixing conveyer 3, the discharge end of drying tower 4 is connected with the feed end of cyclone separator I 5, the air outlet of described air blast 7 is connected with the air inlet of drying tower 4 by air heater 8.
Drying unit also comprises siccative pumpback device, described siccative pumpback device comprises whirlwind discharger 2, quantitative return material packing auger conveyer 6 and air-introduced machine 10, the discharge end of whirlwind discharger 2 is connected with the siccative import of bipacking-auger batch mixing conveyer 3 and sends into dry material in bipacking-auger batch mixing conveyer 3, the feed end of described quantitative return material packing auger conveyer 6 is connected with the discharge end of cyclone separator I 5 and the feed end of whirlwind discharger 2 respectively with discharge end, the air outlet of described air-introduced machine 10 is connected with the air inlet of dry whirlwind discharger 2, the air inlet of described air-introduced machine 10 is connected with drying tower 4.
Drying unit also comprises centrifugal batcher 1, and the discharge end of described centrifugal batcher 1 is connected with the wet feed import of bipacking-auger batch mixing conveyer 3.
Described drying tower 4 is provided with decentralized institution 11 in the cavity of its feed end, described decentralized institution 11 comprises four mutual vertically disposed Eight characters blades 1102 of cross mixing blade 1101, two arranged in parallel and rotating shaft 1103, winding is mutually arranged in a crossed manner on rotating shaft 1103 successively along the axial direction of rotating shaft 1103 for described four cross mixing blade 1101, and the winding of described Eight characters blade 1102 is on rotating shaft 1103 and be arranged on the below of cross mixing blade 1101.
Wet feed and siccative enter into bipacking-auger batch mixing conveyer 3 by the whirlwind discharger 2 in centrifugal batcher 1 and siccative pumpback device respectively and mix and be transported to drying tower 4, material is sent to the hot-air seasoning of drying tower 4 after decentralized institution 11 grinding dispersion, and hot blast is that the wind feeding air heater 8 produced by air blast 7 heats rear formation.By arranging paddle gear piece 302 and helical blade 303 in bipacking-auger batch mixing conveyer 3, while ensure that the moisture infiltrating time between dry material and wet stock, ensure that certain pusher ability.In drying tower 4, arrange decentralized institution 11, form ring-type cloth air port, material is easily disperseed, and the heating surface area and the hot blast wind that add material send ability simultaneously, substantially increase the drying efficiency of drying unit and the good product quality produced.Dried material carries through hot blast and enters into cyclone separator I 5 by the outlet of drying tower 4, and the separated rear portion of material becomes finished product and is discharged, and another part is given in bipacking-auger batch mixing conveyer 3 through siccative pumpback device and carries out next drying cycle.Siccative pumpback device comprises whirlwind discharger 2, quantitatively return material packing auger conveyer 6 and air-introduced machine 10, a part of siccative isolated in cyclone separator I 5 is evenly given in whirlwind discharger 2 by quantitative return material packing auger conveyer 6, the hot blast attracted from drying tower 4 is sent in whirlwind discharger 2 by air-introduced machine 10, then siccative is given to bipacking-auger batch mixing conveyer 3 from whirlwind discharger 2, completes siccative pumpback process.By arranging siccative pumpback device, siccative is mixed with wet feed, reduce humidity and the viscosity of material, material, not with good adherence of in drying unit, reduces the fault rate of drying unit, reduces production cost simultaneously.
Drying unit also comprises cyclone separator II 9, the air outlet of described cyclone separator I 5 is connected with the air inlet of cyclone separator II 9, cyclone separator I 5 is not separated material and hot blast completely and enters into cyclone separator II 9, after cyclone separator II 9 is separated, material recycle, hot blast is discharged, conservation and dedusting environment friendly.
Claims (6)
1. a soybean dietary fiber is guaranteed the quality dehydration dryer, it is characterized in that: comprise bipacking-auger batch mixing conveyer (3), drying tower (4), cyclone separator I (5), air blast (7) and air heater (8), described bipacking-auger batch mixing conveyer (3) is provided with siccative import and wet feed import, described bipacking-auger batch mixing conveyer (3) comprises two auger bars (301), the two ends of described two auger bars (301) are provided with paddle gear piece (302), centre is provided with helical blade (303), and the paddle gear piece (302) on two auger bars (301) is mutually staggeredly arranged, helical blade (303) engages arranged crosswise one to one, dry material and wet stock are transported in drying tower (4) after mixing in bipacking-auger batch mixing conveyer (3), the discharge end of drying tower (4) is connected with the feed end of cyclone separator I (5), the air outlet of described air blast (7) is connected with the air inlet of drying tower (4) by air heater (8).
2. a kind of soybean dietary fiber as claimed in claim 1 is guaranteed the quality dehydration dryer, it is characterized in that: drying unit also comprises siccative pumpback device, described siccative pumpback device comprises whirlwind discharger (2), quantitative return material packing auger conveyer (6) and air-introduced machine (10), the discharge end of whirlwind discharger (2) is connected with the siccative import of bipacking-auger batch mixing conveyer (3) and sends into dry material in bipacking-auger batch mixing conveyer (3), the feed end of described quantitative return material packing auger conveyer (6) is connected with the discharge end of cyclone separator I (5) and the feed end of whirlwind discharger (2) respectively with discharge end, the air outlet of described air-introduced machine (10) is connected with the air inlet of dry whirlwind discharger (2).
3. a kind of soybean dietary fiber as claimed in claim 2 is guaranteed the quality dehydration dryer, it is characterized in that: the air inlet of described air-introduced machine (10) is connected with drying tower (4).
4. a kind of soybean dietary fiber as described in claim as arbitrary in claims 1 to 3 is guaranteed the quality dehydration dryer, it is characterized in that: drying unit also comprises centrifugal batcher (1), the discharge end of described centrifugal batcher (1) is connected with the wet feed import of bipacking-auger batch mixing conveyer (3).
5. a kind of soybean dietary fiber as described in claim as arbitrary in claims 1 to 3 is guaranteed the quality dehydration dryer, it is characterized in that: drying unit also comprises cyclone separator II (9), the air outlet of described cyclone separator I (5) is connected with the air inlet of cyclone separator II (9).
6. a kind of soybean dietary fiber as described in claim as arbitrary in claims 1 to 3 is guaranteed the quality dehydration dryer, it is characterized in that: described drying tower (4) is provided with decentralized institution (11) in the cavity of its feed end, described decentralized institution (11) comprises four cross mixing blade (1101) arranged in parallel, two mutual vertically disposed Eight characters blades (1102) and rotating shaft (1103), winding is upper and mutually arranged in a crossed manner at rotating shaft (1103) successively along the axial direction of rotating shaft (1103) for described four cross mixing blade (1101), the winding of described Eight characters blade (1102) is gone up at rotating shaft (1103) and is arranged on the below of cross mixing blade (1101).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520836334.2U CN205106274U (en) | 2015-10-27 | 2015-10-27 | Soybean dietary fiber guarantees quality to dewater and uses drying -machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520836334.2U CN205106274U (en) | 2015-10-27 | 2015-10-27 | Soybean dietary fiber guarantees quality to dewater and uses drying -machine |
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| Publication Number | Publication Date |
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| CN205106274U true CN205106274U (en) | 2016-03-30 |
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| CN201520836334.2U Expired - Fee Related CN205106274U (en) | 2015-10-27 | 2015-10-27 | Soybean dietary fiber guarantees quality to dewater and uses drying -machine |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105265996A (en) * | 2015-10-27 | 2016-01-27 | 平顶山金晶生物科技有限公司 | Dryer for quality-guarantee dehydration of soybean dietary fiber |
| CN109028902A (en) * | 2018-08-28 | 2018-12-18 | 河南省德耀节能科技股份有限公司 | One kind is wet, glues class drying materials system and its drying equipment |
-
2015
- 2015-10-27 CN CN201520836334.2U patent/CN205106274U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105265996A (en) * | 2015-10-27 | 2016-01-27 | 平顶山金晶生物科技有限公司 | Dryer for quality-guarantee dehydration of soybean dietary fiber |
| CN105265996B (en) * | 2015-10-27 | 2019-03-22 | 平顶山金晶生物科技有限公司 | A kind of soybean dietary fiber is guaranteed the quality dehydration dryer |
| CN109028902A (en) * | 2018-08-28 | 2018-12-18 | 河南省德耀节能科技股份有限公司 | One kind is wet, glues class drying materials system and its drying equipment |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 467200, Yexian County industrial agglomeration area, Pingdingshan, Henan province (north side of culture Road) Patentee after: Pingdingshan Jinjing biological Polytron Technologies Inc Address before: 467200, Yexian County industrial agglomeration area, Pingdingshan, Henan province (north side of culture Road) Patentee before: Pingdingshan Jinchang Biological Technology Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160330 Termination date: 20171027 |