CN209302550U - A kind of enrichment facility of beta glucan - Google Patents
A kind of enrichment facility of beta glucan Download PDFInfo
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- CN209302550U CN209302550U CN201920700922.1U CN201920700922U CN209302550U CN 209302550 U CN209302550 U CN 209302550U CN 201920700922 U CN201920700922 U CN 201920700922U CN 209302550 U CN209302550 U CN 209302550U
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- filtered fluid
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Abstract
The utility model discloses a kind of enrichment facilities of beta glucan, it includes material box, filter, liquid reserve tank, hydraulic pump, hollow fiber ultrafiltration membrane module, magnetic control unit, concentrate branch and filtered fluid branch, the material box is connect by filter with liquid reserve tank, the liquid reserve tank is connected to hollow fiber ultrafiltration membrane module by hydraulic pump, the hollow fiber ultrafiltration membrane module is connected with magnetic control unit and filtered fluid branch respectively, the magnetic control unit is connected by concentrate branch with liquid reserve tank, the hollow fiber ultrafiltration membrane module includes inlet, hollow cylinder, fiber capillary outer tube, fiber capillary inner tube, stir bar magnet, filtered fluid liquid outlet, concentrate liquid outlet and Electromagnetically-operating platform, the fiber capillary outer tube is arranged in hollow cylinder.
Description
Technical field
The utility model relates to the technical field of glucan, especially a kind of enrichment facility of beta glucan.
Background technique
Beta glucan is the product new with one kind of unique process exploitation, derives from fresh food brewer's yeast.
It is a kind of polysaccharide, and general chemical structure is β -1,3 glucans and β -1, and 6 glucans, wherein the former has antitumor property,
And human body natural's immunity can be greatlyd improve, it is ideal drug and health food.
However existing beta glucan concentration technique needs to carry out under high temperature environment by the method for multiple-effect evaporation, this
Sample is not only easily destroyed the property of original glucan, while the energy consumption needed is higher, is unfavorable for the long-time service of equipment.
Utility model content
The shortcomings that the purpose of the utility model is to overcome the prior arts provides a kind of enrichment facility of beta glucan.
The purpose of this utility model is achieved through the following technical solutions: a kind of enrichment facility of beta glucan, a kind of β-
The enrichment facility of glucan, it includes material box, filter, liquid reserve tank, hydraulic pump, hollow fiber ultrafiltration membrane module, magnetic control list
Member, concentrate branch and filtered fluid branch, the material box are connect by filter with liquid reserve tank, and the liquid reserve tank passes through liquid
Press pump is connected to hollow fiber ultrafiltration membrane module, the hollow fiber ultrafiltration membrane module respectively with magnetic control unit and filtered fluid branch phase
Even, the magnetic control unit is connected by concentrate branch with liquid reserve tank, the hollow fiber ultrafiltration membrane module include inlet, in
Void column body, fiber capillary outer tube, fiber capillary inner tube, stirring bar magnet, filtered fluid liquid outlet, concentrate liquid outlet and Electromagnetically-operating
Platform, the fiber capillary outer tube are arranged in hollow cylinder, interior to be equipped with fiber capillary inner tube, and downside is equipped with concentrate liquid outlet,
The fiber capillary inner tube is connected with inlet, and outer surface is along multiple micropores are axially arranged with, for retaining macromolecular substances, fiber
Filtered fluid liquid outlet is equipped on the downside of capillary outer tube, the stirring bar magnet is arranged in fiber capillary inner tube, and the electromagnetic base is set
It sets under hollow cylinder, provides power for stirring bar magnet, the magnetic control unit is used to detect and the magnetism of filtering and concentrating liquid
Substance, including magnetic sensor, valve positioner, connection branch and Magnetic filtration device branch, the magnetic sensor are arranged in master
Road is connected with valve positioner, and the Magnetic filtration device branch includes shut-off valve B and magnetic filter, in filtering and concentrating liquid
Magnetisable material, and filtered fluid is recycled in liquid reserve tank, the connection branch includes shut-off valve A, filters branch with concentrate
It is connected.
Specifically, further including overflow valve, main road pressure gauge and branch pressure table, the overflow valve is arranged in overflow branch,
The main road pressure gauge is arranged between hydraulic pump and hollow fiber ultrafiltration membrane module, and the branch pressure table is arranged in concentrate branch
Road, for detecting the hydraulic of concentrate branch.
Specifically, the magnetic sensor is magnetic material content detector.
Specifically, the concentrate branch includes thermoregulator, concentrated solution discharge meter and concentrated solution discharge valve, the temperature
For adjusting concentrate temperature, the concentrated solution discharge meter is connected degree adjuster with liquid reserve tank, the concentrated solution discharge valve and section
Only valve A is connected, for adjusting concentrated solution discharge.
Specifically, the filtered fluid branch included filtered fluid flow valve, filtering flow meters and filtered fluid collecting box, institute
The setting of filtered fluid flow valve is stated between hollow fiber ultrafiltration membrane module and filtering flow meters, the filtering traffic meter and filtered fluid are received
Header is connected.
Specifically, the hollow fiber ultrafiltration membrane module has multiple fiber capillaries, it is poly- that each fiber capillary individually filters Portugal
Sugar juice.
The utility model has the advantage that enrichment facility of the utility model compared to traditional beta glucan, is not required to
High temperature is heated, energy consumption is lower, while the utility model uses the hollow fiber ultrafiltration membrane module with multiple fiber capillaries, often
As a micro dialysis bag on a fibre pipe, filtration and infiltration area is significantly increased, the efficiency of filtering is improved；This is practical new
Type is additionally provided with bar magnet for homogeneous solution concentration, prevents the appearance of concentration gradient, accelerates the rate of filtration.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the hollow fiber ultrafiltration membrane module schematic diagram of the utility model.
In figure: 1- material box 2- filter 3- liquid reserve tank 4- hydraulic pump 5- hollow fiber ultrafiltration membrane module 6- magnetic transducing
Device 7- valve positioner 8- shut-off valve A 9- shut-off valve B 10- magnetic filter 11- thermoregulator 12- concentrated solution discharge
Count 13- overflow valve 14- main road pressure gauge 15- concentrated solution discharge valve 16- branch pressure table 17- filtered fluid flow valve 18-
Filter flow meters 19- filtered fluid collecting box 51- inlet 52- hollow cylinder 53- fiber capillary outer tube 54- fiber hair
Thin inner tube 55- stirs bar magnet 56- filtered fluid liquid outlet 57- concentrate liquid outlet 58- electromagnetic base.
Specific embodiment
The utility model is further described with reference to the accompanying drawing, but the protection scope of the utility model is not limited to
It is as described below.
As shown in Fig. 1~2, a kind of enrichment facility of beta glucan, it includes material box 1, filter 2, liquid reserve tank 3, liquid
Press pump 4, hollow fiber ultrafiltration membrane module 5, magnetic control unit, concentrate branch and filtered fluid branch, the material box 1 pass through filtering
Device 2 is connect with liquid reserve tank 3, and the liquid reserve tank 3 is connected to hollow fiber ultrafiltration membrane module 5, the hollow fiber ultrafiltration film group by hydraulic pump 4
Part 5 is connected with magnetic control unit and filtered fluid branch respectively, and the magnetic control unit passes through concentrate branch and liquid reserve tank 3
It is connected, the hollow fiber ultrafiltration membrane module 5 includes inlet 51, hollow cylinder 52, fiber capillary outer tube 53, fiber capillary inner tube
54, bar magnet 55, filtered fluid liquid outlet 56, concentrate liquid outlet 57 and Electromagnetically-operating platform, the fiber capillary outer tube 53 is stirred to set
It sets in hollow cylinder 52, interior to be equipped with fiber capillary inner tube 54, downside is equipped with concentrate liquid outlet 57, the fiber capillary inner tube
54 are connected with inlet 51, and outer surface is along being axially arranged with multiple micropores, for retaining macromolecular substances, under fiber capillary outer tube 53
Side is equipped with filtered fluid liquid outlet 56, and the stirring bar magnet 55 is arranged in fiber capillary inner tube 54, and the electromagnetic base 58 is arranged
Under hollow cylinder 52, power is provided for stirring bar magnet 55, the magnetic control unit is used to detect and the magnetic of filtering and concentrating liquid
Property substance, including magnetic sensor 6, valve positioner 7, connection branch and Magnetic filtration device branch, the magnetic sensor 6 be arranged
In main road, it is connected with valve positioner 7, the Magnetic filtration device branch includes shut-off valve B and magnetic filter 10, dense for filtering
Magnetisable material in contracting liquid, and filtered fluid is recycled in liquid reserve tank 3, the connection branch includes shut-off valve A, with concentrate mistake
Branch is filtered to be connected.
It further, further include overflow valve 13, main road pressure gauge 14 and branch pressure table 16, the setting of overflow valve 13 exists
Overflow branch, the main road pressure gauge 14 are arranged between hydraulic pump 4 and hollow fiber ultrafiltration membrane module 5, the branch pressure table 16
It is arranged in concentrate branch, for detecting the hydraulic of concentrate branch.
Further, the magnetic sensor 6 is magnetic material content detector.
Further, the concentrate branch includes thermoregulator 11, concentrated solution discharge meter 12 and concentrated solution discharge valve
15, for adjusting concentrate temperature, the concentrated solution discharge meter 12 is connected the thermoregulator 11 with liquid reserve tank 3, described dense
Contracting flow quantity valve 15 is connected with shut-off valve A8, for adjusting concentrated solution discharge.
Further, the filtered fluid branch included that filtered fluid flow valve 17, filtering flow meters 18 and filtered fluid are received
Header 19, the setting of filtered fluid flow valve 17 is between hollow fiber ultrafiltration membrane module 5 and filtering flow meters 18, the filtering stream
Meter is connected with filtered fluid collecting box 19.
Further, the hollow fiber ultrafiltration membrane module 5 has multiple fiber capillaries, and each fiber capillary individually filters Portugal
Glycan solution.
The course of work of the utility model is as follows: glucan mixed liquor imported in material box 1, it is preliminary by filter 2
Glucan mixed liquor is inputted in liquid reserve tank 3 after filtering, is entered after providing pressure by hydraulic pump 4 for mixing liquid through inlet
In fiber capillary inner tube 54, the macromolecular substances in mixed liquor are formed in the tube by the surface micropore retention of fiber capillary inner tube 54
Filtered fluid, glucan small molecule flow to fiber capillary outer tube 53 from micropore and form concentrate, and filtered fluid is through filtered fluid liquid outlet
56, filtered fluid flow valve 17 and filtering flow meters 18 are to filtered fluid collecting box 19, due to also setting inside fiber capillary inner tube 53
There is bar magnet, therefore there are magnetisable material in concentrate, when magnetisable material is accumulated after repeatedly recycling, causes concentrate that can not accord with
Standardization, therefore concentrate needs to carry out magnetisable material detection by magnetic sensor 6, and signal is passed to valve positioner 7,
When the amount of magnetisable material in concentrate is higher than the threshold value of setting, valve positioner controls shut-off valve 8(shut-off valve A) it closes, it cuts
Only valve 9(shut-off valve B) it opens, concentrate will be by 10 filtering magnetic substance of magnetic filter at this time, and is directly back to liquid storage
Circulating filtration concentration is carried out in case, if magnetisable material is lower than given threshold, shut-off valve A is opened, and concentrate passes through concentrate at this time
After flow valve 15 adjusts flow, fluid temperature and fluid flow successively are adjusted by temperature controller 11 and concentrated solution discharge meter 12
And it returns in liquid reserve tank；After circulation is filtered for multiple times, with the continuous discharge of small molecule in filter membrane pipe, macromolecular is trapped
It is deposited in film surface, concentration is higher and higher, and then forms concentration gradient, therefore be additionally provided with stirring in fiber capillary inner tube 54
Bar magnet 55 controls stirring bar magnet periodically agitation glucan mixed liquor by electromagnetic base 58, guarantees that substance distribution is equal in solution
It is even, accelerate the rate of filtration.
The above, the only preferred embodiment of the utility model, not do limit in any form to the utility model
System.Anyone skilled in the art, in the case where not departing from technical solutions of the utility model ambit, all using above-mentioned
The technology contents make many possible changes and modifications to technical solutions of the utility model, or be revised as equivalent variations etc.
Imitate embodiment.Therefore, all contents without departing from technical solutions of the utility model, the technology according to the utility model is to the above reality
Any change modification, equivalent variations and modification that example is made are applied, the protection scope of the technical program is belonged to.
Claims (6)
1. a kind of enrichment facility of beta glucan, it is characterised in that: it include material box (1), filter (2), liquid reserve tank (3),
Hydraulic pump (4), hollow fiber ultrafiltration membrane module (5), magnetic control unit, concentrate branch and filtered fluid branch, the material box (1)
It is connect by filter (2) with liquid reserve tank (3), the liquid reserve tank (3) is connected to hollow fiber ultrafiltration membrane module by hydraulic pump (4)
(5), the hollow fiber ultrafiltration membrane module (5) is connected with magnetic control unit and filtered fluid branch respectively, the magnetic control unit
It is connected by concentrate branch with liquid reserve tank (3), the hollow fiber ultrafiltration membrane module (5) includes inlet (51), hollow cylinder
(52), fiber capillary outer tube (53), fiber capillary inner tube (54), stirring bar magnet (55), filtered fluid liquid outlet (56), concentrate go out
Liquid mouth (57) and Electromagnetically-operating platform, fiber capillary outer tube (53) setting are interior to be equipped with fiber capillary in hollow cylinder (52)
Inner tube (54), downside are equipped with concentrate liquid outlet (57), and the fiber capillary inner tube (54) is connected with inlet (51), outer surface
Along multiple micropores are axially arranged with, for retaining macromolecular substances, filtered fluid liquid outlet is equipped on the downside of fiber capillary outer tube (53)
(56), in fiber capillary inner tube (54), the electromagnetic base (58) is arranged in hollow cylinder for stirring bar magnet (55) setting
(52) under, power is provided for stirring bar magnet (55), the magnetic control unit is used to detect and the magnetisable material of filtering and concentrating liquid,
Including magnetic sensor (6), valve positioner (7), connection branch and Magnetic filtration device branch, magnetic sensor (6) setting
In main road, it is connected with valve positioner (7), the Magnetic filtration device branch includes shut-off valve B(9) and magnetic filter (10), it uses
Magnetisable material in filtering and concentrating liquid, and filtered fluid is recycled in liquid reserve tank (3), the connection branch includes shut-off valve A
(8), it is connected with concentrate filtering branch.
2. a kind of enrichment facility of beta glucan according to claim 1, it is characterised in that: further include overflow valve (13),
Main road pressure gauge (14) and branch pressure table (16), the overflow valve (13) are arranged in overflow branch, the main road pressure gauge
(14) it is arranged between hydraulic pump (4) and hollow fiber ultrafiltration membrane module (5), the branch pressure table (16) is arranged in concentrate branch
Road, for detecting the hydraulic of concentrate branch.
3. a kind of enrichment facility of beta glucan according to claim 1, it is characterised in that: the magnetic sensor (6)
For magnetic material content detector.
4. a kind of enrichment facility of beta glucan according to claim 1, it is characterised in that: the concentrate branch includes
Thermoregulator (11), concentrated solution discharge meter (12) and concentrated solution discharge valve (15), the thermoregulator (11) is for adjusting
Concentrate temperature, the concentrated solution discharge meter (12) are connected with liquid reserve tank (3), the concentrated solution discharge valve (15) and shut-off valve A
(8) it is connected, for adjusting concentrated solution discharge.
5. a kind of enrichment facility of beta glucan according to claim 1, it is characterised in that: the filtered fluid branch includes
Filtered fluid flow valve (17), filtering flow meters (18) and filtered fluid collecting box (19), the filtered fluid flow valve (17) is crossed to set
It sets between hollow fiber ultrafiltration membrane module (5) and filtering flow meters (18), the filtering traffic meter and filtered fluid collecting box (19)
It is connected.
6. a kind of enrichment facility of beta glucan according to claim 1, it is characterised in that: the hollow fiber ultrafiltration membrane module
(5) there are multiple fiber capillaries, each fiber capillary individually filters dextran solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920700922.1U CN209302550U (en) | 2019-05-15 | 2019-05-15 | A kind of enrichment facility of beta glucan |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920700922.1U CN209302550U (en) | 2019-05-15 | 2019-05-15 | A kind of enrichment facility of beta glucan |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209302550U true CN209302550U (en) | 2019-08-27 |
Family
ID=67682437
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920700922.1U Active CN209302550U (en) | 2019-05-15 | 2019-05-15 | A kind of enrichment facility of beta glucan |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209302550U (en) |
-
2019
- 2019-05-15 CN CN201920700922.1U patent/CN209302550U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: SICHUAN KELUN XINGUANG HEALTH PHARMACEUTICAL Co.,Ltd. Assignor: SICHUAN HETAI SYNLIGHT BIOTECHNOLOGY Co.,Ltd. Contract record no.: X2020510000011 Denomination of utility model: Concentration device of beta-glucan Granted publication date: 20190827 License type: Common License Record date: 20200529 |