CN206843358U - The continuous treater of high-purity D fructose - Google Patents
The continuous treater of high-purity D fructose Download PDFInfo
- Publication number
- CN206843358U CN206843358U CN201720364567.6U CN201720364567U CN206843358U CN 206843358 U CN206843358 U CN 206843358U CN 201720364567 U CN201720364567 U CN 201720364567U CN 206843358 U CN206843358 U CN 206843358U
- Authority
- CN
- China
- Prior art keywords
- discharge nozzle
- feed pipe
- decolorizer
- carbon removal
- ground
- 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
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
It the utility model is related to a kind of continuous treater of high-purity D fructose, including decolorizer, carbon removal device, sterilization device, nutsch filter, crystallization growing the grain device, specific annexation are as follows：Decolorizer top installation feeder, condenser and agitating paddle, decolorizer are placed in the heating mantle of controllable temperature, and decolorizer bottom is formed with discharge nozzle, and discharge nozzle is connected with the feed pipe of carbon removal device by ground interface；The discharge nozzle of carbon removal device is formed with ground interface with the feed pipe of sterilization device and is connected, and the discharge nozzle of sterilization device has ground to be connected with the feed pipe of nutsch filter；Nutsch filter top is provided with vacuum pipe inlet and outlet, is vented section door, and nutsch filter bottom has discharge nozzle to have ground to be connected with the feed pipe for crystallizing growing the grain device, and crystallization growing the grain device is built-in to be stirred, and there is temperature controlled water bath outside.The device for the Totally-enclosed-type continuous production high purity crystalline fructose that the application provides can be carried out continuously decolouring, carbon removal, degerming, crystallization, growing the grain, and operation is quick, simple, can disposably produce high-purity crystallized fructose.
Description
Technical field
The utility model belongs to chemical reagent purification devices, especially a kind of continuous treater of high-purity D-Fructose.
Background technology
Fructose is a kind of natural sweetener of most sweet tea.Its sugariness is 1.5 times of sucrose, up to 1.8 times under low temperature.As sweet tea
Taste agent, though it is lower than the sugariness of synthetic sweetener, because it has trophism, have no toxic side effect, so being used widely.Fruit
Small to insulin degree of dependence in liver intracellular metabolite after sugar is absorbed by the body, especially crystal diabetin is diabetes, angiocarpy
The good nutritive sweetener with liver patient.Lactic acid is not produced after fructose metabolism, moreover it is possible to suppress the consumption of vivo protein, can be fast
Speed provides and supplement body energy, body endurance and metabolic effects, therefore is very suitable for preparing the function of supplement physical efficiency
Property drink.Nutritional supplement such as sportsman and physical labourer.Also can as parenteral solution, for cardiovascular disease, diabetes,
The treatment of brainpan disease and hepatopathy.So gradually the development and application in medicine, medical industry, its demand are increasing for fructose.
The production method of fructose mainly has from glucose extraction and with sucrose hydrolysis method.The fructose of two methods output
Content is 99%, and the fructose of pharma grade product is according to USP requirement content >=99.9%.
Utility model content
The purpose of this utility model is overcome the deficiencies in the prior art, there is provided one kind rapidly, continuously progress easy to operate,
The continuous treater of the high-purity D-Fructose to use manpower and material resources sparingly.
The utility model adopts the technical scheme that：
A kind of continuous treater of high-purity D-Fructose, including decolorizer, carbon removal device, sterilization device, nutsch filter, crystallization growing the grain
Device, specific annexation are as follows：
Decolorizer top installation feeder, condenser and agitating paddle, decolorizer are placed in the heating mantle of controllable temperature, are decolourized
Device bottom is formed with discharge nozzle, and discharge nozzle is connected with the feed pipe of carbon removal device by ground interface；The discharge nozzle and sterilization device of carbon removal device
Feed pipe be formed with ground interface and be connected, the discharge nozzle of sterilization device has ground to be connected with the feed pipe of nutsch filter；Nutsch filter top
Vacuum pipe inlet and outlet are installed, are vented section door, nutsch filter bottom has discharge nozzle to have ground phase with the feed pipe for crystallizing growing the grain device
Even, crystallization growing the grain device is built-in stirs, and there is temperature controlled water bath outside.
Moreover, the carbon removal device is by upper lid, bottom composition；There is feed pipe on upper lid；Have filter plate on bottom, under have discharging
Pipe, feed pipe have ground with discharge nozzle；Carbon removal device Shang Gai is sandwiched between filter paper the bottom of with；Two parts have flange to be fixed.
The advantages of the utility model and good effect are：
The device for the Totally-enclosed-type continuous production high purity crystalline fructose that the application provides can be decolouring, carbon removal, degerming, knot
Brilliant, growing the grain is carried out continuously, and operation is quick, simple, can disposably produce high-purity crystallized fructose.
The continuous closed progress of continuous treater operation of high-purity D-Fructose of the application, reduce the machine of bacterium intrusion
Meeting；Carbon removal, degerming use vacuum filter, fast and easy；Degerming use sterilization film (0.22 μm), it is degerming thorough；There is automatic warm
Degree control, ensure that 25~30 DEG C of crystallizations, 15~20 DEG C of growing the grains；The present apparatus can limited production, can also amplify, suitable for industrialization
Production.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the concrete structure of sterilization device.
Embodiment
With reference to embodiment, following embodiments, which are illustrative, are not limited is further illustrated to the utility model
, it is impossible to limit the scope of protection of the utility model with following embodiments.
A kind of continuous treater of high-purity D-Fructose, including decolorizer 1, carbon removal device 3, sterilization device 4, nutsch filter 5, crystallization
Growing the grain device 6, specific annexation are as follows：
The top of decolorizer 1 installation feeder 8, condenser 7 and agitating paddle 9, decolorizer are placed in the heating mantle 2 of controllable temperature
In, decolorizer bottom is formed with discharge nozzle 12, and discharge nozzle 12 is connected with the feed pipe 14 of carbon removal device 3 by ground interface；Carbon removal device 3
Discharge nozzle 15 is formed with ground interface with the feed pipe 16 of sterilization device 4 and is connected, the discharge nozzle 17 of sterilization device 4 and the charging of nutsch filter 5
Pipe 18 has ground to be connected；The top of nutsch filter 5 is provided with vacuum pipe inlet and outlet 10, is vented section door 11, discharging is arranged at the bottom of nutsch filter 5
Pipe 19 has ground to be connected with the feed pipe 20 for crystallizing growing the grain device 6, and the 6 built-in stirring 9 of crystallization growing the grain device, there is temperature controlled water bath 21 outside.
Carbon removal device 3 is made up of upper lid 22, bottom 24；There is feed pipe 14 on upper lid 22；Have filter plate 23 on bottom 24, under have discharge nozzle
15, feed pipe 14 has ground 25 with discharge nozzle 15；Carbon removal device Shang Gai is sandwiched between filter paper 26 bottom of with；Two parts have flange to be subject to
Fixed, sterilization device 4 is identical with carbon removal device structure, and simply the Shang Gai of sterilization device 4 is sandwiched between sterilization film (0.22 μm) bottom of with, instead of filter
Paper.
Case study on implementation
1st, the rough D-Fructoses of 2Kg, 3L95% ethanol, 5g activated carbons are added in the reactor.
2nd, heating is boiled, and stirs 20min.
3rd, the decompression of nutsch filter vacuum section door is opened.
4th, carbon removal device outlet section door, sterilization device outlet section door, decolorizer outlet section door are opened, completes carbon removal, degerming.
5th, nutsch filter vacuum section door is closed, sterilization device outlet section door is closed, opens nutsch filter and decontrol section door, material is put into
Crystallize in growing the grain device, start stirring.
6th, 25~30 DEG C are cooled to, adds crystal seed, is kept for 1 hour.
7th, in 15~20 DEG C of insulated and stirreds 10 hours, growing the grain.
8th, crystallization dries：80 DEG C are dried under reduced pressure, and obtain finished product 1.74Kg, yield 87%, content 99.9%.
Claims (2)
- A kind of 1. continuous treater of high-purity D-Fructose, it is characterised in that：Including decolorizer, carbon removal device, sterilization device, suction filtration Device, crystallization growing the grain device, specific annexation are as follows：Decolorizer top installation feeder, condenser and agitating paddle, decolorizer are placed in the heating mantle of controllable temperature, decolorizer bottom Portion is formed with discharge nozzle, and discharge nozzle is connected with the feed pipe of carbon removal device by ground interface；The discharge nozzle of carbon removal device and entering for sterilization device Expects pipe is formed with ground interface and is connected, and the discharge nozzle of sterilization device has ground to be connected with the feed pipe of nutsch filter；Install on nutsch filter top There are vacuum pipe inlet and outlet, be vented section door, nutsch filter bottom has discharge nozzle to have ground to be connected with the feed pipe for crystallizing growing the grain device, ties Brilliant growing the grain device is built-in to be stirred, and there is temperature controlled water bath outside.
- 2. the continuous treater of high-purity D-Fructose according to claim 1, it is characterised in that：The carbon removal device is by upper Lid, bottom composition；There is feed pipe on upper lid；Have filter plate on bottom, under have a discharge nozzle, feed pipe has ground with discharge nozzle；Remove Charcoal device Shang Gai is sandwiched between filter paper the bottom of with；Two parts have flange to be fixed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720364567.6U CN206843358U (en) | 2017-04-10 | 2017-04-10 | The continuous treater of high-purity D fructose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720364567.6U CN206843358U (en) | 2017-04-10 | 2017-04-10 | The continuous treater of high-purity D fructose |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206843358U true CN206843358U (en) | 2018-01-05 |
Family
ID=60792977
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720364567.6U Expired - Fee Related CN206843358U (en) | 2017-04-10 | 2017-04-10 | The continuous treater of high-purity D fructose |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206843358U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109170483A (en) * | 2018-07-03 | 2019-01-11 | 山东香驰健源生物科技有限公司 | A kind of syrup and preparation method thereof for cake |
-
2017
- 2017-04-10 CN CN201720364567.6U patent/CN206843358U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109170483A (en) * | 2018-07-03 | 2019-01-11 | 山东香驰健源生物科技有限公司 | A kind of syrup and preparation method thereof for cake |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102258163A (en) | Preparation process of dried honey | |
| CN107164274A (en) | A kind of lactic acid bacteria composite fungicide and its preparation method and application | |
| CN103908475A (en) | Traditional Chinese medicine preparation method | |
| CN108796026A (en) | Production, extraction and the purifying process of lysine | |
| CN109561711A (en) | The method for treating digestive pathologies | |
| CN206843358U (en) | The continuous treater of high-purity D fructose | |
| CN108294271A (en) | A kind of agitating device for honey production | |
| CN100333659C (en) | High-fructose honey preparing process | |
| CN102001957B (en) | Method for extracting L-threonine | |
| CN101109020A (en) | Vertical type continuous crystallization method adopting beforehand crystallization technique | |
| CN102523920B (en) | Preparation method of Grifola frondosa mycelial pellets and products thereof | |
| CN110396530A (en) | A method of improving production amount of threonine and yield | |
| CN104975051A (en) | Method for enriching GABA (gamma-aminobutyric acid) in mulberry leaves | |
| CN104844583A (en) | Method for producing puerarin | |
| CN105331643B (en) | A method of Pfansteihl is prepared using sophora bud dregs of a decoction fermentation | |
| CN105087712B (en) | A method of preparing high-purity D-MANNOSE | |
| CN106901289A (en) | A kind of production and processing technology of crystallized honey | |
| CN102070677B (en) | Method for refining raffinose | |
| CN104855677A (en) | Method for preparing composite high protein feed from rice residues | |
| CN209555221U (en) | Produce the production system of Rebaudiodside A D and Rebaudiodside A M | |
| CN101156663A (en) | Organism organic selenium honey health food and its preparation | |
| CN106072098A (en) | A kind of watermelon crystal eats the preparation method of gel | |
| CN106317262A (en) | Extraction method for producing alantin from chicories | |
| CN1966644A (en) | Preparation method of pear vinegar | |
| CN110115855A (en) | A kind of gibberellin plant growth regulator special-purpose crystallization pot |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180105 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |