CN2903853Y - Spraying drier for malt sugar powder - Google Patents
Spraying drier for malt sugar powder Download PDFInfo
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- CN2903853Y CN2903853Y CN 200520146817 CN200520146817U CN2903853Y CN 2903853 Y CN2903853 Y CN 2903853Y CN 200520146817 CN200520146817 CN 200520146817 CN 200520146817 U CN200520146817 U CN 200520146817U CN 2903853 Y CN2903853 Y CN 2903853Y
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Abstract
The utility model relates to a spraying drier for malt sugar powder, which is composed by a feed apparatus, an atomizer, a drying apparatus, a tower cleaning device, a separation & collection apparatus and a hot blast stove. The outlet of the feed apparatus connects with the feed port of the atomizer. The atomization disc of the atomizer is assembled downward inside the hot air distributor installed on the top of the drying device. The hot air inlet of the hot air distributor connects with the hot air outlet of the hot blast stove through a pipeline. The discharging port of the drying device and the tail gas discharging port connect respectively with the separation & collection apparatus through a cyclone feed pipe and appropriate pipelines. The device opens up a new path for production of malt sugar powder, provides a rapid drying and proper drying temperature, introduces no damage to nutrient content of the malt sugar, which eliminates the shortcomings of original crystallization process such as long process flow, complicated equipment, complex procedures and the problem of sugar powder bonding inside the tower in conventional atomization drying process, thus provides a spacious application prospect.
Description
Technical field
The utility model relates to a kind of drying equipment, relates in particular to a kind of maltitol powder spray-drying installation.
Background technology
The maltose of selling mostly is liquid on the market now, its dry is between 70%-80%, be widely used in the industries such as food, beverage and dairy products, but, brought inconvenience for storage and transportation, in storage and transportation because of malt syrup has characteristics such as perishable, that moisture is big, can be putrid and deteriorated, not only transportation, storage cost strengthen, and bring unnecessary economic loss to enterprise, also can cause environmental pollution.
At present, though the maltitol powder sale is arranged on the market, it produces the crystallisations that adopt more, need be from malt syrup through operations such as concentrated, decrease temperature crystalline, the filling demoulding, growing the grain, pulverizing, drying, screenings, and its production procedure is long, equipment is complicated, technology is loaded down with trivial details.And adopt the spray-drying mode to carry out maltitol powder production, be difficult to solve the sticking tower problem of Icing Sugar in the dry run again.
Summary of the invention
At above problem, the purpose of this utility model is to provide a kind of maltitol powder spray-drying installation, utilizes this device that malt syrup is dried to maltitol powder, so that storage and transportation.
For achieving the above object, the utility model is a kind of maltitol powder spray-drying installation of realizing like this, this device is by feeder apparatus, atomizer, drying equipment, sweep tower apparatus, separated and collected equipment and hot-blast stove constitute, the outlet of feeder apparatus links to each other with the inlet of atomizer, the atomizing disk of atomizer downwards be assemblied in the hot-air distributor at drying device top, the hot-air distributor hot air inlet links to each other with the hot-blast outlet of hot-blast stove with pipeline, and the discharge port of drying device is connected with separated and collected equipment with corresponding pipeline by the whirlwind feed pipe respectively with exhaust port.
Described feeder apparatus is made up of storage tank and charging pump, and the storage tank outlet links to each other with charging pump by pipeline, and the charging pump outlet links to each other with the atomizer charging aperture by pipeline.
Described atomizer is the centrifugal high speed atomizer of band atomizing disk.
Described drying equipment is made of drying tower, hot-air distributor, whirlwind distributor, and the following exit of drying equipment is equipped with the pneumatic discharge valve, and the drying tower cone sidepiece outlet of drying equipment is the exhaust port of drying equipment.
Described sweep tower apparatus by air compressor, air reservoir, air cleaner, air heater, slip-knot formula bellows chamber, sweep the tower tracheae and form, sweeping the tower tracheae directly is connected with slip-knot formula bellows chamber, bellows chamber is connected with the air heater outlet by pipeline, the air heater inlet is connected with the air cleaner outlet by pipeline, the air cleaner inlet is connected with the air reservoir outlet by pipeline, and the compressed air reservoir inlet is connected with the air compressor outlet by pipeline.
Described separated and collected equipment is made of two cyclone separators, the lower part outlet place of cyclone separator is equipped with the pneumatic discharge valve, the lower part outlet place of first cyclone separator is equipped with the pneumatic discharge valve, the hot-wind inlet of first cyclone separator is connected with the exhaust port of drying equipment by pipeline, the hot-blast outlet of first cyclone separator links to each other with an air-introduced machine by pipeline, the discharge port of first cyclone separator links to each other by ajutage with the air intake vent of second cyclone separator, the porch of this ajutage is communicated with the discharge port of drying equipment, the porch of this ajutage links to each other with the discharge port of drying equipment, the air outlet of second cyclone separator links to each other with another air-introduced machine by pipeline, and the pneumatic discharge valve place material mouth of second cyclone separator is the maltitol powder outlet; Can also at least one cyclone separator in parallel again on described first cyclone separator.
From technique scheme as can be seen, technological core of the present utility model is to utilize centrifugal spray drying equipment that malt syrup is carried out drying to handle, malt syrup is sent into high speed centrifugal type atomizer by screw pump, fully atomizing in drying tower, and feed liquid becomes highdensity little droplet.Directly being heated to hot blast about 200 ℃ in hot-blast stove is admitted in the drying tower with drop after mist is breathed out and fully contacts, moisture evaporates rapidly, feed liquid forms dry powder in drying tower, major part directly by automatic discharge valve continuous discharge to ajutage, the small part fine powder is recycled to ajutage with tail gas again through cyclone separator, carries by the cyclone separator centralized collection finished product maltitol powder that installs tail end through ajutage.This device has been opened up new way for the continuous production of maltitol powder.Utilize spray-drying installation production, drying time fast, baking temperature all the time, dry run can not destroyed the maltose nutritional labeling, changed original crystallisation long flow path, equipment complexity, technology is loaded down with trivial details and general spray drying device dry run in the shortcoming of Icing Sugar easy sticking to the tower, the gained maltitol powder is convenient to store transportation, be subjected to the welcome of industries such as vast food, beverage and dairy products deeply, have broad application prospects.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further explained explanation:
Among Fig. 1, this maltitol powder spray-drying installation is by feeding system, atomizer 4, drying device, separated and collected equipment, sweeping Tower System and hot-blast stove constitutes, the outlet of feeder apparatus links to each other with the inlet of atomizer, the atomizing disk 5 of atomizer is assemblied in downwards in the hot-air distributor 6 at drying equipment top, the hot blast import 3 of hot-air distributor 6 links to each other by the hot-blast outlet of pipeline with hot-blast stove 18, the air inlet of hot-blast stove 18 is connected with the air outlet of air intake machine 19, the discharge port of drying equipment is connected with separated and collected equipment with corresponding pipeline by ajutage respectively with exhaust port, sweep tower apparatus by air compressor 17, air reservoir 16, air cleaner 15, air heater 14, slip-knot formula bellows chamber, sweep tower tracheae 21, sweeping tower transmission mechanism 20 forms, sweeping tower tracheae 21 directly is connected with slip-knot formula bellows chamber, bellows chamber is connected with air heater 14 outlets by pipeline, air heater 14 inlets are connected with air cleaner 15 outlets by pipeline, air cleaner 15 inlets are connected with air reservoir 16 outlets by pipeline, and compressed air reservoir 16 inlets are connected with air compressor 17 outlets by pipeline.
Above-mentioned feeder apparatus is made of storage tank 1 and charging pump 2, and storage tank 1 must export with the inlet of charging pump 2 and link to each other by pipeline, and the outlet of charging pump 2 links to each other by the inlet of pipeline with atomizer 4.
Be connected with air intake machine 19 on the above-mentioned hot-blast stove 18.Atomizer 4 is centrifugal high speed atomizer.
Described drying equipment is made of drying tower 22, hot-air distributor 6, cyclone separator 9, and the following exit of drying equipment is equipped with pneumatic discharge valve 10, and the drying tower cone sidepiece outlet of drying equipment is the exhaust port 7 of drying equipment.
Above-mentioned separated and collected equipment is made of two cyclone separators 9, the exit, below of cyclone separator is separately installed with pneumatic discharge valve 10, the hot-wind inlet of first cyclone separator links to each other with the exhaust port 7 of drying equipment by pipeline, hot-blast outlet links to each other with air-introduced machine 8 by pipeline, the discharge port of first cyclone separator links to each other by ajutage with the air intake vent place of second cyclone separator, the porch of this ajutage is connected with the discharge port of drying equipment, and the inlet of this ajutage links to each other with air blower 13 by dehumidifier 12.Ajutage plays maltitol powder and carries and cooling effect.Pneumatic discharge valve 10 discharging openings of second cyclone separator link to each other with finished product storage tank 11.For enlarging disposal ability, can also at least one cyclone separator in parallel again on first cyclone separator.
Claims (6)
1, a kind of maltitol powder spray-drying installation, it is characterized in that this device by feeder apparatus, atomizer, drying equipment, sweep tower apparatus, separated and collected equipment and hot-blast stove and constitute, the outlet of feeder apparatus links to each other with the inlet of atomizer, the atomizing disk of atomizer downwards be assemblied in the hot-air distributor at drying device top, the hot-air distributor hot air inlet links to each other with the hot-blast outlet of hot-blast stove with pipeline, and the discharge port of drying device is connected with separated and collected equipment with corresponding pipeline by the whirlwind feed pipe respectively with exhaust port.
2, drying device according to claim 1 is characterized in that described feeder apparatus is made up of storage tank and charging pump, and the storage tank outlet links to each other with charging pump by pipeline, and charging pump exports and links to each other with the atomizer charging aperture by pipeline.
3, drying device according to claim 1 is characterized in that the centrifugal high speed atomizer of described atomizer for the band atomizing disk.
4, drying device according to claim 1, it is characterized in that described drying equipment is made of drying tower, hot-air distributor, whirlwind distributor, the following exit of drying equipment is equipped with the pneumatic discharge valve, and the drying tower cone sidepiece outlet of drying equipment is the exhaust port of drying equipment.
5, drying device according to claim 1, it is characterized in that described sweep tower apparatus by air compressor, air reservoir, air cleaner, air heater, slip-knot formula bellows chamber, sweep the tower tracheae and form, sweeping the tower tracheae directly is connected with slip-knot formula bellows chamber, bellows chamber is connected with the air heater outlet by pipeline, the air heater inlet is connected with the air cleaner outlet by pipeline, the air cleaner inlet is connected with the air reservoir outlet by pipeline, and the compressed air reservoir inlet is connected with the air compressor outlet by pipeline.
6, according to arbitrary described drying device of claim 1-5, it is characterized in that described separated and collected equipment is made of two cyclone separators, the lower part outlet place of cyclone separator is equipped with the pneumatic discharge valve, the lower part outlet place of first cyclone separator is equipped with the pneumatic discharge valve, the hot-wind inlet of first cyclone separator is connected with the exhaust port of drying equipment by pipeline, the hot-blast outlet of first cyclone separator links to each other with an air-introduced machine by pipeline, the discharge port of first cyclone separator links to each other by ajutage with the air intake vent of second cyclone separator, the porch of this ajutage is communicated with the discharge port of drying equipment, the porch of this ajutage links to each other with the discharge port of drying equipment, the air outlet of second cyclone separator links to each other with another air-introduced machine by pipeline, and the pneumatic discharge valve place material mouth of second cyclone separator is the maltitol powder outlet; Can also at least one cyclone separator in parallel again on described first cyclone separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520146817 CN2903853Y (en) | 2005-12-23 | 2005-12-23 | Spraying drier for malt sugar powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520146817 CN2903853Y (en) | 2005-12-23 | 2005-12-23 | Spraying drier for malt sugar powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2903853Y true CN2903853Y (en) | 2007-05-23 |
Family
ID=38079268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520146817 Expired - Fee Related CN2903853Y (en) | 2005-12-23 | 2005-12-23 | Spraying drier for malt sugar powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2903853Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251603A (en) * | 2014-09-03 | 2014-12-31 | 嘉善圣莱斯绒业有限公司 | Powder drying device |
-
2005
- 2005-12-23 CN CN 200520146817 patent/CN2903853Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251603A (en) * | 2014-09-03 | 2014-12-31 | 嘉善圣莱斯绒业有限公司 | Powder drying device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |