CN206809892U - A kind of Jerusalem artichoke extract film concentration systems - Google Patents
A kind of Jerusalem artichoke extract film concentration systems Download PDFInfo
- Publication number
- CN206809892U CN206809892U CN201720545341.6U CN201720545341U CN206809892U CN 206809892 U CN206809892 U CN 206809892U CN 201720545341 U CN201720545341 U CN 201720545341U CN 206809892 U CN206809892 U CN 206809892U
- Authority
- CN
- China
- Prior art keywords
- jerusalem artichoke
- filter
- concentration systems
- artichoke extract
- film concentration
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Film concentration is the utility model is related to, discloses a kind of Jerusalem artichoke extract film concentration systems, including the stoste groove being sequentially connected in series by pipeline(1), delivery pump(2), bag type filtering device assembly, cartridge filter(3), high-pressure pump(4), membrane stack(5)And pan tank(6);Wherein, the both sides of filter membrane are respectively concentrate and production aqueous in the membrane stack, and concentrate leads to the pan tank, and production aqueous leads to discharging of waste liquid pipe(7);The stoste groove and pan tank are provided with CIP on-line cleaning devices(8).Jerusalem artichoke extract film concentration systems thickening efficiency of the present utility model is high, and less energy consumption, cost is low, suitable for large-scale production.And pol can be more than 26% in concentrate made from its concentration.
Description
Technical field
It the utility model is related to film concentration field, more particularly to a kind of Jerusalem artichoke extract film concentration systems.
Background technology
Jerusalem artichoke originates in North America, the incoming Europe of 17th century, rear incoming China.Its underground stem tuber is rich in starch, synanthrin etc.
Fructose polymers, it is edible, cook or cook gruel, salted white, shine Jerusalem artichoke processed and do, or produce starch and alcohol raw material.
Jerusalem artichoke after over cleaning, chopping, high temperature soak extraction, flocculation sediment, centrifugal filtration, it is necessary to further concentrate,
Common high temperature, it is concentrated under reduced pressure, energy consumption is preferable, and thickening efficiency is relatively low, and cost is larger, is not suitable for mass producing.
Application No. CN201410825851.X Chinese patent discloses a kind of fermented black Jerusalem artichoke extract, by with lower section
Method is made:(1) from Xuzhou Lvzhiye Biological Food Co., Ltd. according to made from the technology of patent of invention 201210582406.6
Fermented black Jerusalem artichoke, through drying and other treatment, moisture is less than 6%w/w, then crushed 40 mesh sieves, obtain fermented black Jerusalem artichoke coarse powder;
(2) pure water is added in the fermented black Jerusalem artichoke coarse powder obtained to step (1), after soaking 2h, is placed in grinding process in colloid mill, is made
Into fermented black Jerusalem artichoke slurry;(3) slurry made from step (2) is subjected to press filtration, obtains pressing filtering liquid and black Jerusalem artichoke slag respectively;Black Jerusalem artichoke
Slag is standby;(4) pressing filtering liquid that step (3) obtains is centrifuged, centrifugal rotational speed 10000-16000rpm, obtain supernatant and
Solid phase precipitation thing;Solid phase precipitation thing is standby;(5) supernatant for obtaining step (4) carries out refined filtration, obtains fermented black Jerusalem artichoke juice
Product.The patent enriches the kind of Jerusalem artichoke converted products, has expanded the scope of Jerusalem artichoke converted products, improves Jerusalem artichoke processing production
The added value of product, there is good exploiting economy value and benefit.But use or traditional method for concentration, cost compared with
It is high.
Utility model content
In order to solve the above-mentioned technical problem, the utility model provides a kind of Jerusalem artichoke extract film concentration systems.This practicality
New Jerusalem artichoke extract film concentration systems thickening efficiency is high, and less energy consumption, cost is low, suitable for large-scale production.And it is concentrated
Pol can be more than 26% in obtained concentrate.
Concrete technical scheme of the present utility model is:A kind of Jerusalem artichoke extract film concentration systems, including by pipeline successively
Stoste groove, delivery pump, bag type filtering device assembly, cartridge filter, high-pressure pump, membrane stack and the pan tank of series connection;Wherein, the film
The both sides of filter membrane are respectively concentrate and production aqueous in heap, and concentrate leads to the pan tank, and production aqueous leads to discharging of waste liquid
Pipe;The stoste groove and pan tank are provided with CIP on-line cleaning devices.
Preferably, the bag type filtering device assembly is made up of multiple bag filters in parallel.
Preferably, the filtering accuracy of the bag filter is 50 microns.
Preferably, the filtering accuracy of the cartridge filter is 5 microns.
Preferably, the filter membrane of the membrane stack is organosilicon/polyamide 6 amine film.
Preferably, the film production molasses sugar degree of the filter membrane is less than 0.1%.
Preferably, the operating pressure of the membrane stack is 34-36Bar, running temperature is 60-80 DEG C.
Jerusalem artichoke enters film of the present utility model after over cleaning, chopping, high temperature soak extraction, flocculation sediment, centrifugal filtration
The stoste groove of concentration systems, bag filter component being pumped into by conveying, bag filter filtering accuracy is 50 μm, and respectively
Group bag filter can mutually switch use, and bag filter enters cartridge filter, the filtering essence of cartridge filter after coming out
Spend for 5 μm, high-pressure pump, high pressure pump outlet connection membrane stack are entered after coming out, film production molasses sugar degree is less than 0.1%, and the water can be returned
With or directly discharge, concentrate enters pan tank, and pol is more than 26%, operating pressure 34-36Bar, running temperature 60-80
℃。
It is compared with the prior art, the beneficial effects of the utility model are:
1st, system is using bag type filtering device assembly in parallel, changeable use;
2nd, system is using high temperature sanitation-grade organosilicon/polyamide 6 amine film, and maximum allowable operating temperature (M.A.O.T.) can be with 35Bar pressure
Reach 80 degrees Celsius, the Jerusalem artichoke solution of high temperature extraction is without cooling;Thickening efficiency is high, energy consumption pin, and cost is low.
3rd, whole system is designed for sanitation-grade, and pipeline junction is welded using argon arc welding, and whole system exists equipped with CIP
Line cleans;
4th, Jerusalem artichoke solution can be concentrated to 26% pol by system, be directly entered the spray drying device of back segment.
Brief description of the drawings
Fig. 1 is a kind of structural representation of the present utility model.
Reference is:Stoste groove 1, delivery pump 2, cartridge filter 3, high-pressure pump 4, membrane stack 5, pan tank 6, discharging of waste liquid
Pipe 7, CIP on-line cleaning devices 8, bag filter 9.
Embodiment
With reference to embodiment, the utility model will be further described.In the utility model involved device,
Connection structure and method, it is device well known in the art, connection structure and method if without refering in particular to.
Embodiment 1
As shown in Figure 1:A kind of Jerusalem artichoke extract film concentration systems, including be sequentially connected in series by pipeline stoste groove 1, conveying
Pump 2, bag type filtering device assembly, cartridge filter 3, high-pressure pump 4, membrane stack 5 and pan tank 6.Wherein, filter membrane in the membrane stack
Both sides are respectively concentrate and production aqueous, and concentrate leads to the pan tank, and production aqueous leads to discharging of waste liquid pipe 7;The stoste
Groove and pan tank are provided with CIP on-line cleaning devices 8.
Wherein, the bag type filtering device assembly is made up of two bag filters 9 in parallel.The filtering essence of bag filter
Spend for 50 microns.The filtering accuracy of the cartridge filter is 5 microns.The filter membrane of the membrane stack is organosilicon/polyamide 6 amine film, film
Produce molasses sugar degree and be less than 0.1%.The operating pressure of membrane stack is 35Bar, and running temperature is 80 DEG C.
Embodiment 2
A kind of Jerusalem artichoke extract film concentration systems, including be sequentially connected in series by pipeline stoste groove 1, delivery pump 2, pocket type mistake
Filter module, cartridge filter 3, high-pressure pump 4, membrane stack 5 and pan tank 6.Wherein, the both sides of filter membrane are respectively in the membrane stack
Concentrate and production aqueous, concentrate lead to the pan tank, and production aqueous leads to discharging of waste liquid pipe 7;The stoste groove and pan tank
It is provided with CIP on-line cleaning devices 8.
Wherein, the bag type filtering device assembly is made up of three bag filters 9 in parallel.The filtering essence of bag filter
Spend for 50 microns.The filtering accuracy of the cartridge filter is 5 microns.The filter membrane of the membrane stack is organosilicon/polyamide 6 amine film, film
Produce molasses sugar degree and be less than 0.1%.The operating pressure of membrane stack is 34Bar, and running temperature is 60 DEG C.
Embodiment 3
A kind of Jerusalem artichoke extract film concentration systems, including be sequentially connected in series by pipeline stoste groove 1, delivery pump 2, pocket type mistake
Filter module, cartridge filter 3, high-pressure pump 4, membrane stack 5 and pan tank 6.Wherein, the both sides of filter membrane are respectively in the membrane stack
Concentrate and production aqueous, concentrate lead to the pan tank, and production aqueous leads to discharging of waste liquid pipe 7;The stoste groove and pan tank
It is provided with CIP on-line cleaning devices 8.
Wherein, the bag type filtering device assembly is made up of four bag filters 9 in parallel.The filtering essence of bag filter
Spend for 50 microns.The filtering accuracy of the cartridge filter is 5 microns.The filter membrane of the membrane stack is organosilicon/polyamide 6 amine film, film
Produce molasses sugar degree and be less than 0.1%.The operating pressure of membrane stack is 36Bar, and running temperature is 70 DEG C.
Jerusalem artichoke enters film of the present utility model after over cleaning, chopping, high temperature soak extraction, flocculation sediment, centrifugal filtration
The stoste groove of concentration systems, bag filter component being pumped into by conveying, bag filter filtering accuracy is 40-60 μm,
And each group bag filter can mutually switch use, bag filter enters cartridge filter, the mistake of cartridge filter after coming out
It is 5 μm to filter precision, and high-pressure pump, high pressure pump outlet connection membrane stack are entered after coming out, and film production molasses sugar degree is less than 0.1%, and the water can enter
Row reuse is directly discharged, and concentrate enters pan tank, and pol is more than 26%, operating pressure 34-36Bar, running temperature
60-80℃。
The utility model whole system mainly it is prominent following some:
1st, system is using bag type filtering device assembly in parallel, changeable use;
2nd, system is using high temperature sanitation-grade organosilicon/polyamide 6 amine film, and maximum allowable operating temperature (M.A.O.T.) can be with 35Bar pressure
Reach 80 degrees Celsius, the Jerusalem artichoke solution of high temperature extraction is without cooling;Thickening efficiency is high, energy consumption pin, and cost is low.
3rd, whole system is designed for sanitation-grade, and pipeline junction is welded using argon arc welding, and whole system exists equipped with CIP
Line cleans;
4th, Jerusalem artichoke solution can be concentrated to 26% pol by system, be directly entered the spray drying device of back segment.
It is described above, only it is preferred embodiment of the present utility model, not the utility model is imposed any restrictions, every
Any simple modification, change and the equivalent structure transformation made according to the utility model technical spirit to above example, still
Belong to the protection domain of technical solutions of the utility model.
Claims (6)
- A kind of 1. Jerusalem artichoke extract film concentration systems, it is characterised in that:Including the stoste groove being sequentially connected in series by pipeline(1), it is defeated Send pump(2), bag type filtering device assembly, cartridge filter(3), high-pressure pump(4), membrane stack(5)And pan tank(6);Wherein, the film The both sides of filter membrane are respectively concentrate and production aqueous in heap, and concentrate leads to the pan tank, and production aqueous leads to discharging of waste liquid Pipe(7);The stoste groove and pan tank are provided with CIP on-line cleaning devices(8).
- A kind of 2. Jerusalem artichoke extract film concentration systems as claimed in claim 1, it is characterised in that the bag type filtering device assembly By multiple bag filters in parallel(9)Form.
- A kind of 3. Jerusalem artichoke extract film concentration systems as claimed in claim 2, it is characterised in that the mistake of the bag filter It is 50 microns to filter precision.
- A kind of 4. Jerusalem artichoke extract film concentration systems as claimed in claim 1, it is characterised in that the mistake of the cartridge filter It is 5 microns to filter precision.
- 5. a kind of Jerusalem artichoke extract film concentration systems as claimed in claim 1, it is characterised in that the filter membrane of the membrane stack is Organosilicon/polyamide 6 amine film.
- A kind of 6. Jerusalem artichoke extract film concentration systems as claimed in claim 5, it is characterised in that the film production water of the filter membrane Pol is less than 0.1%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720545341.6U CN206809892U (en) | 2017-05-17 | 2017-05-17 | A kind of Jerusalem artichoke extract film concentration systems |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720545341.6U CN206809892U (en) | 2017-05-17 | 2017-05-17 | A kind of Jerusalem artichoke extract film concentration systems |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206809892U true CN206809892U (en) | 2017-12-29 |
Family
ID=60755772
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720545341.6U Active CN206809892U (en) | 2017-05-17 | 2017-05-17 | A kind of Jerusalem artichoke extract film concentration systems |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206809892U (en) |
-
2017
- 2017-05-17 CN CN201720545341.6U patent/CN206809892U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103468766B (en) | Preparation method of high-purity mannan oligosaccharide | |
CN103923219B (en) | The production and processing technology of the light phase of wheat flour and wheat flour substance-pentosan | |
CN101255453A (en) | Method for extracting purple sweet potato anthocyanin pigments by employing invoice process | |
CN102558327A (en) | Process for extracting sweet potato protein by thermal deposition method | |
CN107385001A (en) | Process for extracting sea cucumber oligopeptide and sea cucumber polysaccharide from sea cucumber deep-processing byproducts | |
CN100522982C (en) | Production process for extracting tea saponin from tea-oil tree cake by using water as dissoluent | |
CN102911278B (en) | Membrane concentration process used for carrageenan production | |
CN102382203B (en) | High-efficiency extraction process for polysaccharide of lotus seeds | |
CN103636917B (en) | Utilize Hydrodynamic Cavitation Technology from rice residue, extract the method for rice protein | |
CN1962686A (en) | Method for cleanly producing saponin by integrated utilization of yam | |
CN206809892U (en) | A kind of Jerusalem artichoke extract film concentration systems | |
CN103304677A (en) | Method for separating and purifying konjac glucomannan | |
CN102090619B (en) | Production method of precooked agaricus bisporus water concentrated solution | |
CN104830927B (en) | A kind of method that forulic acid oligosaccharide syrup is prepared using wheat bran | |
CN104211754A (en) | Method for preparing polysaccharides and glycoproteins from Medicago sativa L. stems | |
CN102775511A (en) | Method for extracting pepper polysaccharide from pepper residue | |
CN103520979A (en) | Special vacuum-type drum filter for treating ultrafiltration tank bottom substances and treatment method of ultrafiltration tank bottom substances | |
CN105294873A (en) | Extraction method for laminarin | |
CN216022129U (en) | Traditional chinese medicine separation and extraction system | |
CN107148431A (en) | Method for concentrating beta glucan | |
CN213570258U (en) | Production line preparation system for extracting polysaccharides and flavones from bamboo pulping liquid | |
CN212308463U (en) | System used in production process of eucommia ulmoides fine powder | |
CN101473979A (en) | Method for extracting trepang oil from boiled trepang juice | |
CN213431819U (en) | Preparation system for extracting polysaccharide flavone alkaloid from Moraceae plant liquid | |
CN207854963U (en) | Blueberry juice clarification system and the production line for including the blueberry juice clarification system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |