CN108106333A - A kind of Sucralose food-grade furnace drying method and drying unit - Google Patents
A kind of Sucralose food-grade furnace drying method and drying unit Download PDFInfo
- Publication number
- CN108106333A CN108106333A CN201711110044.XA CN201711110044A CN108106333A CN 108106333 A CN108106333 A CN 108106333A CN 201711110044 A CN201711110044 A CN 201711110044A CN 108106333 A CN108106333 A CN 108106333A
- Authority
- CN
- China
- Prior art keywords
- sucralose
- vacuum
- conical
- heating
- vacuum dryer
- 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.)
- Pending
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/12—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
- F26B11/14—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a horizontal or slightly-inclined plane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Drying Of Solid Materials (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
Abstract
The present invention relates to a kind of Sucralose food-grades to dry furnace drying method, comprises the following steps:Wet product Sucralose is added in interior heating conical vacuum dryer, wet product Sucralose material lifting is stirred by drying machine inner conical hurricane band, and to the inside and outside heating of material, steam is being pumped by vacuum pump, it exchanges heat to condense by plate and removes moisture, when moisture less than 0.3% to be qualified, and cool down to material, finished product Sucralose conveys next workshop section's processing after qualification after cooling.The advantage of the invention is that:Using heating conical vacuum dryer in novel spiral band, the sour Improving The Quality of Products in Sucralose product has effectively been handled, has not only improved image of the client to product, and has improved production efficiency and reduces energy consumption, improve working environment, economic benefit is brought to company.
Description
Technical field:
The present invention relates to a kind of production method of sweetener, more particularly to a kind of furnace drying method of Sucralose.
Background technology:
Sucralose is as a kind of new confectionery additive, it is than sucrose, saccharin, 3,4-Dihydro-6-methyl-1,2,3-oxathiazin-4-one 2,2-dioxide potassium salt, Aspartame, stevioside glycosides
Deng more advantageous, it is safe, performance is stablized, and is a kind of new high quality, non-nutritive high-potency sweetener, is fat
The optimal preferable sweet taste substitute of disease, angiocardiopathy and diabetic food;Fine chemical product field is fallen within, is food
The arm product of product additive.It not only expands rapidly in health food and the application range in medicine, but also is widely used in
More than 300 kinds of baked goods, beverage, mouth perfume (or spice) coffee, dairy products, frozen dessert, ice cream, pudding, jelly, jam, syrup etc. adds
In work product, accepted extensively by market at present and become one of most popular high sweetener
In sucrose trichloride production process, the Sucralose of drying workshop section production, most of is wet product Sucralose, at present for drying
Dry technique and the most selection fluid beds of equipment or vibrated fluidized bed, existing equipment and technique are difficult to promote yield, quality, going
Except the tart flavour in product and reduce energy consumption.
The content of the invention
The purpose of the present invention be exactly in order to solve the disadvantage that poor product quality existing for existing drying means, energy consumption original text,
A kind of Sucralose food-grade furnace drying method and its drying unit provided.
The technical solution adopted by the present invention is as follows:
1st, a kind of Sucralose food-grade drying drying unit, including interior heating conical vacuum dryer, interior heating conical vacuum
Drying machine connects vacuum buffer tank by pipe connecting formula heat exchanger, plate heat exchanger by pipeline, and vacuum buffer tank passes through
Pipeline connects pan feeding vacuum pump and dry vacuum;Plate heat exchanger connects condensation liquid bath by pipeline;
Interior heating conical vacuum dryer shell is equipped with tapered heating sleeve and vacuum sampler, interior to heat in conical vacuum dryer
Portion is equipped with head cover, and head cover is equipped with feed inlet, and interior heating conical vacuum dryer is internally provided with taper helical ribbon agitator, bottom
Equipped with emptying ball valve.
2nd, a kind of Sucralose food-grade drying furnace drying method, comprises the following steps:
Wet product Sucralose is added in interior heating conical vacuum dryer, by drying machine inner conical hurricane band to wet product three
Chlorine sucrose material lifting stirs, and to the inside and outside heating of material, is pumping steam by vacuum pump, exchanging heat by plate cold
It is solidifying to remove moisture, when moisture less than 0.3% to be qualified, and cool down to material, finished product Sucralose conveys after qualification after cooling
Next workshop section's processing.
The advantage of the invention is that:
Using conical vacuum dryer is heated in novel spiral band, the acid effectively handled in Sucralose product promotes product matter
Amount, not only improves image of the client to product, and improves production efficiency and reduce energy consumption, improves building ring
Economic benefit is brought in border to company.
Description of the drawings:
Fig. 1 is present invention process flow chart;
Fig. 2 is the structure chart that conical vacuum dryer is heated in the novel spiral band in Fig. 1.
Specific embodiment:
1st, a kind of Sucralose food-grade drying drying unit including heating conical vacuum dryer in ribbon, heats in ribbon
Conical vacuum dryer connects vacuum buffer tank by pipe connecting formula heat exchanger, plate heat exchanger by pipeline, and vacuum is delayed
It rushes tank and pan feeding vacuum pump and dry vacuum is connected by pipeline;Plate heat exchanger connects condensation liquid bath by pipeline.
2 shell of interior heating conical vacuum dryer is equipped with tapered heating sleeve 4 and vacuum sampler 7, interior heating conical vacuum
2 top of drying machine is equipped with head cover 5, and head cover 5 is equipped with feed inlet 6, and interior heating conical vacuum dryer 2 is internally provided with taper spiral shell
Belt stirrer 3, bottom are equipped with emptying ball valve.
Mainly by motor ribbon rotation in kettle is driven to drive material along kettle using heating conical vacuum dryer in ribbon
Wall rotation rotates and upgrades from bottom to top, and after material reaches top peak due to gravity, automatic stream vortex core returns to
Bottom.Vacuum pump and plate change, and the promotion of wet product Sucralose is stirred, and to the inside and outside heating of material, is passing through vacuum pump
Steam is pumped, exchanging heat to condense by plate removes moisture, and when moisture is less than 0.3% for qualification, finished product Sucralose conveys after qualification
Next workshop section's processing.
2nd, a kind of Sucralose food-grade drying furnace drying method, comprises the following steps:
A. wet product Sucralose is pumped by pan feeding vacuum, it is -0.08Mpa to take out material vacuum degree.One vacuum pumping material vacuum
Degree falls fast, and material just can not be taken out less than -0.06Mpa can cause wet product sugar plugging, is used so minimum two vacuum pumps just reach pan feeding.
Vacuum buffer tank is to prevent material moisture is brought into vacuum pump from causing unnecessary damage to equipment.Heating taper in novel spiral band
Among vacuum drier 6.Once it is pumped into about 900 ㎏ wet products sugar.Wet product sugar humidity parameter is 3% ~ 5%.
B. vacuum pump negative pressure is opened to -0.1Mpa(It is vacuum degree when extracting material evaporation moisture at this time), open hot water
(Hot water comes from recovery workshop)49-53 DEG C is heated to material into vacuum drier chuck, heating removing water is carried out to material
Part.
Plate changes the internal recirculated water for flowing, and moisture content temperature is down to room temperature temperature and can be cooled down.
C. material situation is observed by visor, when material is into powdered, the sampling of hot water vacuum breaker is closed, when moisture is less than 0.3%
For qualification, the chuck recirculated water in heating conical vacuum dryer in ribbon is opened, equipment kettle wall and internal ribbon have pipeline energy
Into hot water heating and circulating water cooling.Cool down to material, after being cooled to 32 DEG C, next workshop section's feed bin is removed into Sucralose conveying.
Claims (2)
1. a kind of Sucralose food-grade dries drying unit, it is characterised in that including interior heating conical vacuum dryer(2), it is interior
Conical vacuum dryer is heated by pipe connecting formula heat exchanger, plate heat exchanger connects vacuum buffer tank by pipeline, very
Empty buffer tank connects pan feeding vacuum pump and dry vacuum by pipeline;Plate heat exchanger connects condensation liquid bath by pipeline;
Interior heating conical vacuum dryer(2)Shell is equipped with tapered heating sleeve(4)And vacuum sampler(7), it is interior heating taper it is true
Empty drying machine(2)Top is equipped with head cover(5), head cover(5)It is equipped with feed inlet(6), interior heating conical vacuum dryer(2)It is interior
Portion is equipped with taper helical ribbon agitator(3), bottom be equipped with emptying ball valve(1).
2. a kind of Sucralose food-grade dries furnace drying method, comprise the following steps:
Wet product Sucralose is added in interior heating conical vacuum dryer, by drying machine inner conical hurricane band to wet product three
Chlorine sucrose material lifting stirs, and to the inside and outside heating of material, is pumping steam by vacuum pump, exchanging heat by plate cold
It is solidifying to remove moisture, when moisture less than 0.3% to be qualified, and cool down to material, finished product Sucralose conveys after qualification after cooling
Next workshop section's processing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711110044.XA CN108106333A (en) | 2017-11-12 | 2017-11-12 | A kind of Sucralose food-grade furnace drying method and drying unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711110044.XA CN108106333A (en) | 2017-11-12 | 2017-11-12 | A kind of Sucralose food-grade furnace drying method and drying unit |
Publications (1)
Publication Number | Publication Date |
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CN108106333A true CN108106333A (en) | 2018-06-01 |
Family
ID=62207211
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201711110044.XA Pending CN108106333A (en) | 2017-11-12 | 2017-11-12 | A kind of Sucralose food-grade furnace drying method and drying unit |
Country Status (1)
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CN (1) | CN108106333A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2189304Y (en) * | 1992-09-26 | 1995-02-08 | 罗光伦 | Vacuum drying machine with automatic temp. control using oil as heat carrier |
CN2898741Y (en) * | 2006-02-10 | 2007-05-09 | 万荣辉 | Vacuum drier with agitating crusher |
CN101571344A (en) * | 2009-06-11 | 2009-11-04 | 查晓峰 | Multifunctional vacuum conical mixing-drying unit |
CN105012978A (en) * | 2015-07-21 | 2015-11-04 | 遵义廖元和堂药业有限公司 | Multifunctional inverted-taper-type sterilizing equipment and sterilization process thereof |
CN204987732U (en) * | 2015-08-27 | 2016-01-20 | 浙江华洲药业有限公司 | Conical vacuum dryer |
-
2017
- 2017-11-12 CN CN201711110044.XA patent/CN108106333A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2189304Y (en) * | 1992-09-26 | 1995-02-08 | 罗光伦 | Vacuum drying machine with automatic temp. control using oil as heat carrier |
CN2898741Y (en) * | 2006-02-10 | 2007-05-09 | 万荣辉 | Vacuum drier with agitating crusher |
CN101571344A (en) * | 2009-06-11 | 2009-11-04 | 查晓峰 | Multifunctional vacuum conical mixing-drying unit |
CN105012978A (en) * | 2015-07-21 | 2015-11-04 | 遵义廖元和堂药业有限公司 | Multifunctional inverted-taper-type sterilizing equipment and sterilization process thereof |
CN204987732U (en) * | 2015-08-27 | 2016-01-20 | 浙江华洲药业有限公司 | Conical vacuum dryer |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180601 |