CN201819523U - Glucose drying and conveying device - Google Patents
Glucose drying and conveying device Download PDFInfo
- Publication number
- CN201819523U CN201819523U CN2010205153636U CN201020515363U CN201819523U CN 201819523 U CN201819523 U CN 201819523U CN 2010205153636 U CN2010205153636 U CN 2010205153636U CN 201020515363 U CN201020515363 U CN 201020515363U CN 201819523 U CN201819523 U CN 201819523U
- Authority
- CN
- China
- Prior art keywords
- drying
- glucose
- asta
- fan
- dust collector
- 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
Links
Images
Landscapes
- Freezing, Cooling And Drying Of Foods (AREA)
Abstract
The utility model relates to a glucose drying and conveying device which belongs to the production field of drying and conveying of materials, in particular to a device for drying and conveying dextrose monohydrate obtained by centrifugal separation after crystallization. The glucose drying and conveying device comprises a heat exchanger, a fan, a cyclone dust collector and a storage bin, and is characterized in that hot air at an outlet of the drying fan is used for driving glucose to ascend at a certain speed and reach the cyclone dust collector, and material enters into the storage bin after being separated in the cyclone dust collector; due to the operation of the material sucking fan, the cyclone dust collector and a wind pipe are under the negative pressure state, and then the material in the storage bin is driven to enter into the cyclone dust collector through the wind pipe. With the adoption of the glucose drying and conveying device, not only the dextrose monohydrate can be dried and cooled, but also the powder can be prevented from escaping.
Description
Technical field
The utility model belongs to the food chemical field, is specially the dry conveying device in the Dextrose Monohydrate production procedure.
Background technology
Crystal glucose can be divided into Dextrose Monohydrate and DEXTROSE ANHYDROUS according to the difference of manufacturing process, all is the cornstarch deep processed product.The technological process of production of Dextrose Monohydrate comprises: liquefaction, saccharification, concentrate, crystallization, drying etc., the crystallization Dextrose Monohydrate enters fluidized bed drying by conveying equipment after separating through centrifugal separator.Have air-introduced machine constantly internal gas to be discharged on fluid bed top, but when discharging gas, the sugar in the fluid bed also enter atmosphere with gas, causes very big waste.
The utility model content
The purpose of this utility model is exactly to provide a kind of Dextrose Monohydrate dry conveying device at the defective of above-mentioned existence.This device comprises heat exchanger, drying air fan, Asta-3746, suction blower fan, and described drying air fan air inlet connects heat exchanger, and this blower fan outlet connects four Asta-3746 imports, connects an auger on drying air fan air outlet pipeline, is the wet stock import; Four Asta-3746 bottom outlets connect feed bin, and the feed bin bottom is by the import of an Asta-3746 of pipeline connection, and the top outlet connects the suction air inlet, and the outlet of suction blower fan connects feed bin.
Operation principle is: when drying air fan turns round, blower fan inspiration hot-air drives the wet stock of coming in by auger with certain speed and rises, reach dry Dextrose Monohydrate in the process that hot-air rises, then enter four Asta-3746s, material separates the laggard feed bin of going in Asta-3746.And when drying air fan turned round, the also running simultaneously of suction blower fan and was in negative pressure state in the Asta-3746 that the suction blower fan is connected, and at this moment the pipeline that is connected with feed bin enters Asta-3746 with regard to the material in the suction storehouse, reaches the purpose of cooling material.And be connected with feed bin from the outlet of suction blower fan, avoid running powder.
Description of drawings
Fig. 1 is the main TV structure schematic diagram of the utility model embodiment, wherein: 1 heat exchanger, 2 drying air fans, 3 augers, 4 wet stock reservoirs, 5 dry airducts, 6 Asta-3746s, 7 dry feed bins, 8 suction airduct imports, 9 suction tubes, 10 Asta-3746s, 11 feed bins, the outlet of 12 suction blower fans, 13 suction blower fan imports, 14 suction blower fans.
The specific embodiment
The utility model is described in further detail in conjunction with Fig. 1:
As scheme shown in Figure 1: the dry conveying equipment of glucose is made up of heat exchanger 1, drying air fan 2, Asta-3746 6, feed bin 7, suction blower fan 14.When drying air fan turns round, the hot-air of blower fan inspiration drives the wet stock of coming in by auger 3 with certain speed and rises in dry airduct 5, reach dry Dextrose Monohydrate in the process that hot-air rises, then enter four Asta-3746s 6, material separates the laggard feed bin 7 of going in Asta-3746.When suction blower fan 14 running, and be in negative pressure state in the Asta-3746 10 that the suction blower fan is connected, at this moment the pipeline that is connected with feed bin 7 enters Asta-3746 10 with regard to the material in the suction storehouse, reaches the purpose of cooling material.
Claims (1)
1. the dry conveying equipment of glucose, comprise: heat exchanger, blower fan, Asta-3746, feed bin is characterized in that: the drying air fan air inlet connects heat exchanger, and this blower fan outlet connects four Asta-3746 imports, on drying air fan air outlet pipeline, connect an auger, be the wet stock import; Four Asta-3746 bottom outlets connect feed bin, and the feed bin bottom is by the import of an Asta-3746 of pipeline connection, and the top outlet connects the suction air inlet, and the outlet of suction blower fan connects feed bin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205153636U CN201819523U (en) | 2010-09-03 | 2010-09-03 | Glucose drying and conveying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205153636U CN201819523U (en) | 2010-09-03 | 2010-09-03 | Glucose drying and conveying device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201819523U true CN201819523U (en) | 2011-05-04 |
Family
ID=43917473
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010205153636U Expired - Fee Related CN201819523U (en) | 2010-09-03 | 2010-09-03 | Glucose drying and conveying device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201819523U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104605294A (en) * | 2015-02-16 | 2015-05-13 | 宁夏法福来清真食品股份有限公司 | Potato flour processing production line |
-
2010
- 2010-09-03 CN CN2010205153636U patent/CN201819523U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104605294A (en) * | 2015-02-16 | 2015-05-13 | 宁夏法福来清真食品股份有限公司 | Potato flour processing production line |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN204601643U (en) | A kind of spray-drying installation | |
CN203586721U (en) | Biomass wood chip drying system | |
CN203635345U (en) | Steam and fiber separating device for damp and hot fibers | |
CN103604285B (en) | A kind of biomass wood flour drying system and biomass wood flour drying means | |
CN203940714U (en) | A kind of full-automatic energy-saving material-saving drying machine | |
CN201819523U (en) | Glucose drying and conveying device | |
CN201645684U (en) | Aluminium and plastic separating system | |
CN100392336C (en) | Numerical control fluidized rotary floating dryer | |
CN103925784A (en) | Multi-layer vibrating dryer | |
CN2928453Y (en) | Plastic film recovery prilling machine | |
CN202885451U (en) | Highly-efficient and energy-saving drying device of pomace | |
CN206295901U (en) | Granular activated carbon quality homogenization installation | |
CN206637957U (en) | A kind of high-efficiency drying apparatus of chemical fertilizer | |
CN203810872U (en) | Multilayer vibrating dryer | |
CN110108092B (en) | High-speed rotational flow low-temperature drying system, method and application | |
CN202057152U (en) | Novel internally heated vibro-fluidized bed | |
CN203672084U (en) | Drying equipment for porous and fragile granular products | |
CN203281430U (en) | Solid phase drying and screening device of dewatering and drying integrated centrifugal machine | |
CN104990369A (en) | Tower type penetrating reverse flow fluidized drier | |
CN201801188U (en) | Down feather convey device | |
CN202245370U (en) | Grain impurity-removing conveying system | |
CN201914681U (en) | Wheel blade sealed type discharge device | |
CN206222885U (en) | A kind of spiral vacuum drier of solar energy | |
CN204787711U (en) | Pneumatic dryer | |
CN206535218U (en) | A kind of Highspeedcentrifugingandsprayingdrier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110504 Termination date: 20110903 |