CN202532822U - Sodium glutamate drying fluidized bed - Google Patents
Sodium glutamate drying fluidized bed Download PDFInfo
- Publication number
- CN202532822U CN202532822U CN2011205647857U CN201120564785U CN202532822U CN 202532822 U CN202532822 U CN 202532822U CN 2011205647857 U CN2011205647857 U CN 2011205647857U CN 201120564785 U CN201120564785 U CN 201120564785U CN 202532822 U CN202532822 U CN 202532822U
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- CN
- China
- Prior art keywords
- vibrator unit
- hot blast
- sodium glutamate
- pneumatic vibrator
- sieve plate
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Abstract
The utility model provides a sodium glutamate drying fluidized bed which is provided with a shell. A partition plate is horizontally arranged at the lower part in the shell to divide the shell into an air flow drying chamber at the upper part and a hot air buffering chamber at the lower part; a material inlet and a material outlet are respectively arranged at the two ends of the air flow drying chamber, the upper part of the air flow drying chamber is connected with a tail wind collecting device, a pneumatic vibrator unit is installed on the partition plate, a screen plate is arranged above the pneumatic vibrator unit, the pneumatic vibrator unit drives the screen plate to vibrate; an air inlet of the pneumatic vibrator unit is connected with a hot air source, and an exhaust outlet is communicated with the hot air buffering chamber by the tail wind collecting tube. According to the sodium glutamate drying fluidized bed, hot air is utilized as a power source, and the pneumatic vibration mode is adopted, so electric energy is not used directly, the energy consumption is lowered, meanwhile, a wind shield is arranged at the upper end surface of the vibration screen plate to change the flowing direction of the hot air, so the drying efficiency is improved dramatically, and the frequency of occurrence of appearance flaws such as crystal combining, adhesion, big and small heads of a product is reduced.
Description
Technical field
The utility model belongs to sodium glutamate production equipment technical field, is specifically related to a kind of sodium glutamate oven dry fluid bed.
Background technology
Traditional sodium glutamate drying plant has belt drying equipment, drum dried equipment etc., but has disadvantage: on the one hand because of containing in the sodium glutamate crystal combines H
2The O molecule loses when temperature is too high easily; On the other hand, after wet sodium glutamate crystal contacted with each other, the time was long more, was easy to generate more and crystalline substance, thereby required bake out temperature to be controlled at 50~80 ℃ and flash bakings.The present vibrated fluidized bed that uses mostly carries out drying to product, and the use of vibrated fluidized bed meets the dry specific (special) requirements of crystal to a certain extent, but the bigger rooms for promotion of existence that remain unchanged such as drying rate and effect, crystal grain outward appearance.
The utility model content
The technical problem that the utility model solves: a kind of sodium glutamate oven dry fluid bed is provided, utilizes hot blast, adopt the pneumatic vibration mode as power source; Avoided direct use electric energy; Reduced energy resource consumption, in the oscillating screen plate upper surface deep bead has been set simultaneously, changed hot blast and flow to; Improve drying efficiency dramatically, reduced the frequency of occurrences of product and crystalline substance, adhesion, big or small first-class outward appearance flaw.
The technical scheme that the utility model adopts: a kind of sodium glutamate oven dry fluid bed, have housing, lower horizontal is provided with the hot blast surge chamber that dividing plate is divided into housing the pneumatic conveying drying chamber and the bottom on top in the said housing; The two ends of said pneumatic conveying drying chamber are respectively equipped with charging aperture and discharging opening, and top is connected with tail wind gathering-device; Above the said dividing plate pneumatic vibrator unit is installed, the top of said pneumatic vibrator unit is provided with sieve plate, drives the sieve plate vibration through pneumatic vibrator unit; Said pneumatic vibrator unit air inlet is connected with hot air source, and exhaust outlet is communicated with the hot blast surge chamber through tail wind collecting pipe.
Wherein, Said pneumatic vibrator unit is made up of air motor and cam mechanism; Said air motor is fixed on the dividing plate, and the air inlet of said air motor is connected through motor blast pipe and hot air source, and exhaust outlet is communicated with the hot blast surge chamber through motor tail wind collecting pipe; The below that said air motor driving cam means, said cam mechanism are positioned at sieve plate promotes the sieve plate vibration.
Further, be uniformly distributed with deep bead on the upper surface of said sieve plate, and the spacing between adjacent two deep beads is 0.5-2cm, the angle between deep bead and the sieve plate is 20-60 °.
Further, said hot blast surge chamber is provided with the hot blast compensating port, and the hot blast compensating port is connected with hot air source.
The utility model advantage compared with prior art:
1, use hot blast simultaneously as the power source and the oven dry thermal source of vibrating mechanism, wind energy and heat energy are combined and fully utilizes, comprehensive utilization of energy rate height, energy-saving effect is remarkable;
2, realized the coordination control of vibration frequency and hot blast air quantity, easy and simple to handle; Hot blast air quantity make-up system is set simultaneously, convenient compensation oven dry hot blast consumption;
3, the oscillating screen plate of particular design can change the hot blast flow direction, has increased the time of contact of hot blast and crystal grain, has improved drying efficiency;
4, hot blast blows crystal grain and makes the crystal grain turbulization, thereby it is more thorough that crystal grain is disperseed, and has shortened crystal grain time of contact to each other, has effectively contained and the generation of brilliant phenomenon.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the utility model structure side view;
Fig. 3 is the I portion enlarged drawing of Fig. 1.
The specific embodiment
A kind of embodiment of the utility model is described below in conjunction with accompanying drawing 1,2,3.
A kind of sodium glutamate oven dry fluid bed has housing 15, and lower horizontal is provided with the hot blast surge chamber 4 that dividing plate 13 is divided into housing 15 the pneumatic conveying drying chamber 12 and the bottom on top in the said housing 15; The two ends of said pneumatic conveying drying chamber 12 are respectively equipped with charging aperture 1 and discharging opening 10, and top is connected with tail wind gathering-device 11; Above the said dividing plate 16 pneumatic vibrator unit 7 is installed; Said pneumatic vibrator unit 7 is made up of air motor 6 and cam mechanism 5; Said air motor 6 is fixed on the dividing plate 16, and the air inlet of said air motor 6 is connected through motor blast pipe 8 and hot air source, and exhaust outlet is communicated with hot blast surge chamber 4 through motor tail wind collecting pipe 9; The below that said air motor 6 driving cam means 5, said cam mechanism 5 are positioned at sieve plate 2 promotes sieve plate 2 vibrations.Said hot blast surge chamber 4 is provided with hot blast compensating port 3, and hot blast compensating port 3 is connected with hot air source.
Be uniformly distributed with deep bead 14 on the upper surface of said sieve plate 2, and the spacing between adjacent two deep beads 14 is 0.5-2cm, the angle between deep bead 14 and the sieve plate 2 is 20-60 °.Its effect is to change hot blast to flow to, and increases material-gas time of contact and the contact for a long time each other of minimizing crystal in the dry run, reduces and brilliant generation.
In the course of work, hot blast at first gets into air motor 6, and blast is changed into 2 vibrations of power drive sieve plate, and the frequency of sieve plate 2 vibrations is by the unlatching platform number and the control of blast size of air motor 6; Hot blast through air motor 6 gets into 4 collections of hot blast surge chamber; Dividing plate 13 from hot blast surge chamber 4 tops evenly is blown into pneumatic conveying drying chamber 9; And under the effect of the deep bead 14 that is uniformly distributed with in the upper surface of sieve plate 2; Change wind direction and blow crystal grain rotation and oven dry crystal grain, drying efficiency significantly improves; So that during the crystal grain finish-drying, to hot blast surge chamber 4, make blast stable and reach dry demand through hot blast compensation inlet 3 compensation air quantity when the blast deficiency, the waste gas that produces in the pneumatic conveying drying chamber 12 in the drying course is collected the back discharge by tail wind gathering-device 11.
The utility model is on probation through the continuous several months in Baoji Fufeng Biotechnology Co., Ltd., and average daily dry sodium glutamate product improves more than 20%, and product appearance flaw and crystalline substance etc. significantly reduce, and the saves energy effect is obvious.
The foregoing description, just the preferred embodiment of the utility model is not to be used for limiting the utility model practical range, so all equivalences of being done with the said content of the utility model claim change, all should be included within the utility model claim scope.
Claims (4)
1. a sodium glutamate oven dry fluid bed has housing (15), and it is characterized in that: the interior lower horizontal of said housing (15) is provided with the hot blast surge chamber (4) that the dividing plate (16) that is uniformly distributed with through hole is divided into housing (15) the pneumatic conveying drying chamber (12) and the bottom on top; The two ends of said pneumatic conveying drying chamber (12) are respectively equipped with charging aperture (1) and discharging opening (10), and top is connected with tail wind gathering-device (11); Pneumatic vibrator unit (7) is installed above the said dividing plate (16), and the top of said pneumatic vibrator unit (7) is provided with sieve plate (2), drives sieve plate (2) vibration through pneumatic vibrator unit (7); Said pneumatic vibrator unit (7) air inlet is connected with hot air source, and exhaust outlet is communicated with hot blast surge chamber (4) through tail wind collecting pipe (9).
2. sodium glutamate oven dry fluid bed according to claim 1; It is characterized in that: said pneumatic vibrator unit (7) is made up of air motor (6) and cam mechanism (5); Said air motor (6) is fixed on the dividing plate (16); The air inlet of said air motor (6) is connected through motor blast pipe (8) and hot air source; Exhaust outlet is communicated with hot blast surge chamber (4) through motor tail wind collecting pipe (9), said air motor (6) driving cam means (5), and the below that said cam mechanism (5) is positioned at sieve plate (2) promotes sieve plate (2) vibration.
3. sodium glutamate oven dry fluid bed according to claim 1 and 2; It is characterized in that: be uniformly distributed with deep bead (14) on the upper surface of said sieve plate (2); And the spacing between adjacent two deep beads (14) is 0.5-2cm, and the angle between deep bead (14) and the sieve plate (2) is 20-60 °.
4. sodium glutamate oven dry fluid bed according to claim 3, it is characterized in that: said hot blast surge chamber (4) is provided with hot blast compensating port (3), and hot blast compensating port (3) is connected with hot air source.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205647857U CN202532822U (en) | 2011-12-29 | 2011-12-29 | Sodium glutamate drying fluidized bed |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205647857U CN202532822U (en) | 2011-12-29 | 2011-12-29 | Sodium glutamate drying fluidized bed |
Publications (1)
Publication Number | Publication Date |
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CN202532822U true CN202532822U (en) | 2012-11-14 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011205647857U Expired - Lifetime CN202532822U (en) | 2011-12-29 | 2011-12-29 | Sodium glutamate drying fluidized bed |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102538402A (en) * | 2011-12-29 | 2012-07-04 | 宝鸡阜丰生物科技有限公司 | Sodium glutamate drying fluidized bed |
CN108518967A (en) * | 2018-02-27 | 2018-09-11 | 青岛创高世纪信息科技有限公司 | A kind of drying screening integrated production line |
-
2011
- 2011-12-29 CN CN2011205647857U patent/CN202532822U/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102538402A (en) * | 2011-12-29 | 2012-07-04 | 宝鸡阜丰生物科技有限公司 | Sodium glutamate drying fluidized bed |
CN108518967A (en) * | 2018-02-27 | 2018-09-11 | 青岛创高世纪信息科技有限公司 | A kind of drying screening integrated production line |
CN108518967B (en) * | 2018-02-27 | 2024-06-04 | 大山合集团保康绿生现代农业有限公司 | Drying and screening integrated 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 | ||
CX01 | Expiry of patent term |
Granted publication date: 20121114 |
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CX01 | Expiry of patent term |