CN207667449U - A kind of plasma extraction system - Google Patents
A kind of plasma extraction system Download PDFInfo
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- CN207667449U CN207667449U CN201721626950.0U CN201721626950U CN207667449U CN 207667449 U CN207667449 U CN 207667449U CN 201721626950 U CN201721626950 U CN 201721626950U CN 207667449 U CN207667449 U CN 207667449U
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- outlet tube
- return duct
- liquid
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- membrane filter
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Abstract
The utility model discloses a kind of plasma extraction systems,Including membrane filter,It is pressurized pump group,Liquid concentration detection device,Valve group,Liquid-in pipe,Return duct group,Delivery pipe,First outlet tube,Second outlet tube,First concentrate efferent duct and liquid material temporary storage tank,The input port of membrane filter is connected to delivery pipe,The filtrate (liquid of membrane filter is connected to the first outlet tube,The concentrated solution outlet of membrane filter is connected to the second outlet tube,Second outlet tube respectively with return duct group,First concentrate efferent duct is connected to,Liquid concentration detection device and liquid material temporary storage tank are installed on the second outlet tube,It includes the different booster pump of multiple power to be pressurized pump group,Valve group includes multiple valves,Return duct group includes the return duct of multiple parallel connections successively,One booster pump of installation and a valve on each return duct,Each return duct connection delivery pipe and the second outlet tube,The utility model is conducive to improve the utilization rate of blood plasma.
Description
Technical field
The utility model belongs to blood processing technique field, is specifically related to a kind of plasma extraction system.
Background technology
As people deepen continuously to the understanding of animal blood and the promotion of comprehensive utilization technique, China's animal blood it is comprehensive
Conjunction is also being continuously increased using processing capacity；Since the water content of animal blood plasma is up to 93% or so, before preparing albumen powder
It needs to be concentrated and dried animal blood plasma, to achieve the purpose that reduce reagent consumption and energy consumption；Currently, enterprise is into promoting circulation of blood
There are mainly two types of the methods for starching concentration：One, single batch single cycle condensing mode, it would be desirable to the blood plasma of concentration in filter device into
Row repeatedly cycle concentration；Two, two sections of condensing modes are unidirectionally concentrated progressively in two filter devices；Both blood
Starching the defect of condensing mode is：The concentration of plasma extraction can not accurately control；Concentration can only be 78% hereinafter, leading to plasma protein
The purity of product is not high.
Invention content
In view of this, the purpose of this utility model is to provide a kind of plasma extraction system, stored by liquid material temporary storage tank
Concentrate after the concentration of blood plasma single detects the concentration and evidence of concentrate after the concentration of blood plasma single by liquid concentration detection device
This control blood plasma continues cycling through filtering or progressive filtering；Meanwhile the return duct of multiple parallel connections successively shares a membrane filter
So that optimized integral structure is conducive to cost-effective.
In order to achieve the above object, a kind of plasma extraction system of the utility model, including membrane filter, supercharging pump group, liquid
Bulk concentration detection device, valve group, liquid-in pipe, return duct group, delivery pipe, the first outlet tube, the second outlet tube, the first concentrate
Efferent duct and liquid material temporary storage tank, the input port of the membrane filter are connected to delivery pipe, the filtrate (liquid of membrane filter and first
Outlet tube is connected to, and the concentrated solution outlet of membrane filter is connected to the second outlet tube, the second outlet tube respectively with return duct group, first
Concentrate efferent duct is connected to, and liquid concentration detection device and liquid material temporary storage tank are equipped on the second outlet tube, and supercharging pump group includes
The different booster pump of multiple power, valve group include multiple valves, and return duct group includes the return duct of multiple parallel connections successively,
One booster pump of installation and a valve on each return duct, each return duct connection delivery pipe and the second outlet tube, liquid-in pipe
It is connected to one of return duct and the power of booster pump is less than it on the rear of booster pump on the return duct, the return duct
The power of his booster pump.
Further, the membrane filter is nano-filtration membrane filter.
Further, further include reverse osmosis membrane filt, water pipe, the second concentrate efferent duct, water pot and the modulation of low albumen powder
Container, the input port of reverse osmosis membrane filt are connected to the first outlet tube, and the filtrate (liquid of reverse osmosis membrane filt passes through water pipe
It is connected to water pot, the concentrated solution outlet of reverse osmosis membrane filt is modulated container by the second concentrate efferent duct and low albumen powder and connected
It is logical.
Further, further include the first cartridge filter, the first cartridge filter is mounted on membrane filter and reverse osmosis membrane mistake
On the first outlet tube between filter.
Further, further include the second cartridge filter being mounted on liquid-in pipe.
Further, further include controller, liquid concentration detection device is liquid concentration testing sensor, and controller connection increases
Press pump group, valve group, liquid concentration testing sensor.
The beneficial effects of the utility model are：
1. a kind of plasma extraction system of the utility model is conducive to obtain the plasma protein products of high-purity, blood is accurately controlled
The concentration of concentrate after slurry concentration；The concentrate after the concentration of blood plasma single is stored by liquid material temporary storage tank, is examined by strength of fluid
The concentration for surveying device detection concentrate continues through former return duct and is recycled if the concentration of concentrate is not up to setting value
Filtering；If the concentration of concentrate reaches setting value, progressive filtering is carried out by other return ducts；Due to the gradually mistake of blood plasma
Filter, the concentration of concentrate gradually increase, and therefore, in progressive filter process, the power of the booster pump used is sequentially increased, and ensure
Plasma flow is smooth.
2. a kind of plasma extraction overall system architecture optimization of the utility model, is conducive to cost-effective；It is multiple in parallel successively
Return duct share a membrane filter, a liquid concentration detection device so that the circulating filtration of blood plasma or progressive filtering
It can be realized by a membrane filter and a liquid concentration detection device.
3. a kind of plasma extraction system of the utility model is conducive to improve the utilization rate of blood plasma；Blood plasma passes through nanofiltration membrane
Device obtains the concentrate of filtrate and high concentration, and the concentrate of high concentration is exported by the first concentrate efferent duct, can pass through spray
Mist seasoning prepares high protein powder；Filtrate is input in reverse osmosis membrane filt by the first outlet tube and carries out concentration and recovery simultaneously
Clear water and plasma protein are obtained, plasma protein is transported in low albumen powder modulation container by the second concentrate efferent duct and is allocated
And obtain low albumen powder；Clear water is transported in water pot by water pipe.
4. a kind of plasma extraction system of the utility model controls the coordination work between each booster pump, each valve by controller
Make.
Description of the drawings
In order to keep the purpose of this utility model, technical solution and advantageous effect clearer, the utility model provides as follows
Attached drawing illustrates：
Fig. 1 is a kind of structural schematic diagram of plasma extraction system of the utility model.
Reference numeral：1- membrane filters；2- is pressurized pump group；3- liquid concentration detection devices；4- valve groups；5- liquid-in pipes；
6- return duct groups；7- delivery pipes；The first outlet tubes of 8-；The second outlet tubes of 9-；10- the first concentrate efferent ducts；11- liquid materials are temporary
Tank；12- reverse osmosis membrane filts；13- water pipes；14- the second concentrate efferent ducts；15- water pots；The low albumen powders of 16- modulate container；
The first cartridge filters of 17-；The second cartridge filters of 18-.
Specific implementation mode
Below in conjunction with attached drawing, the preferred embodiment of the utility model is described in detail.
As shown in Figure 1；A kind of plasma extraction system of the utility model, including membrane filter 1, supercharging pump group 2, strength of fluid
Detection device 3, valve group 4, liquid-in pipe 5, return duct group 6, delivery pipe 7, the first outlet tube 8, the concentration of the second outlet tube 9, first
It is liquid efferent duct 10, liquid material temporary storage tank 11, reverse osmosis membrane filt 12, water pipe 13, the second concentrate efferent duct 14, water pot 15, low
Albumen powder modulates container 16, the first cartridge filter 17, the second cartridge filter 18 and controller；Membrane filter 1 uses nanofiltration
The input port of membrane filter, membrane filter 1 is connected to delivery pipe 7, and the filtrate (liquid of membrane filter 1 is connected to the first outlet tube 8,
The concentrated solution outlet of membrane filter 1 is connected to the second outlet tube 9；Second outlet tube 9 respectively with return duct group 6, the first concentrate
Efferent duct 10 is connected to, and liquid concentration detection device 3 and liquid material temporary storage tank 11, strength of fluid detection are equipped on the second outlet tube 9
Device 3 is liquid concentration testing sensor；It includes the different booster pump of multiple power to be pressurized pump group 2, used here as three
Booster pump；Valve group 4 includes multiple valves；Return duct group 6 includes the return duct of multiple parallel connections successively, is installed on each return duct
One booster pump and a valve, each return duct connection delivery pipe 7 and the second outlet tube 9；Used here as three return ducts, divide
Not Wei the first return duct, the second return duct, third return duct, the power of the increasing pump on the first return duct is minimum, third reflux
The power of increasing pump on pipe is maximum；Liquid-in pipe 5 is connected to the first return duct and positioned at the rear of booster pump on the return duct；Instead
The input port of osmosis membrane filter 12 is connected to the first outlet tube 8, and the filtrate (liquid of reverse osmosis membrane filt 12 passes through water pipe 13
It is connected to water pot 15, the concentrated solution outlet of reverse osmosis membrane filt 12 is modulated by the second concentrate efferent duct 14 with low albumen powder
Container 16 is connected to；First cartridge filter 17 is mounted on the first outlet tube 8 between membrane filter 1 and reverse osmosis membrane filt 12
On；Second cartridge filter 18 is mounted on liquid-in pipe 5；Controller connection supercharging pump group 2, valve group 4, strength of fluid detection pass
Sensor.
The course of work of present embodiment：Blood plasma is inputted by liquid-in pipe 5, blood plasma is input to film mistake by the first return duct
Filtrate and concentrate are obtained in filter 1；The concentrate after the concentration of blood plasma single is stored by liquid material temporary storage tank 11；It is dense by liquid
The concentration that degree detection device 3 detects concentrate is simultaneously reflected to controller, and controller is provided with the first setting value being sequentially increased, the
Two setting values, third setting value control the co-ordination between each booster pump, each valve by controller；If the concentration of concentrate
Not up to the first setting value then continues through the first return duct and carries out circulating filtration；If the concentration of concentrate reaches the first setting
Value then carries out progressive filtering by the second return duct and similarly if the concentration of concentrate reaches the second setting value, passes through third
Return duct carries out progressive filtering, if the concentration of concentrate reaches third setting value, is exported from the first concentrate efferent duct, concentration
Liquid at concentrations up to 80%；Filtrate is input in reverse osmosis membrane filt 12 by the first outlet tube 8 and carries out concentration and recovery simultaneously
Clear water and plasma protein are obtained, plasma protein, which is transported to low albumen powder, by the second concentrate efferent duct 14 modulates in container 16
It allocates and obtains low albumen powder；Clear water is transported in water pot by water pipe.
Finally illustrate, preferred embodiment above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, to the greatest extent
Pipe has been described in detail the utility model by above preferred embodiment, but those skilled in the art should manage
Solution, can in the form and details make it various changes, without departing from the utility model claims book institute
The range of restriction.
Claims (6)
1. a kind of plasma extraction system, it is characterised in that：Including membrane filter, supercharging pump group, liquid concentration detection device, valve
Group, liquid-in pipe, return duct group, delivery pipe, the first outlet tube, the second outlet tube, the first concentrate efferent duct and liquid material temporary storage tank,
The input port of the membrane filter is connected to delivery pipe, and the filtrate (liquid of membrane filter is connected to the first outlet tube, membrane filter
Concentrated solution outlet be connected to the second outlet tube, the second outlet tube is connected to return duct group, the first concentrate efferent duct respectively,
Liquid concentration detection device and liquid material temporary storage tank are installed, supercharging pump group includes the different increasing of multiple power on two outlet tubes
Press pump, valve group include multiple valves, and return duct group includes the return duct of multiple parallel connections successively, and one is installed on each return duct
Booster pump and a valve, each return duct connection delivery pipe and the second outlet tube, liquid-in pipe are connected to one of return duct
And the power of booster pump is less than the power of other booster pumps on the rear of booster pump on the return duct, the return duct.
2. a kind of plasma extraction system as described in claim 1, it is characterised in that：The membrane filter is nanofiltration membrane
Device.
3. a kind of plasma extraction system as claimed in claim 2, it is characterised in that：Further include reverse osmosis membrane filt, water pipe,
Second concentrate efferent duct, water pot and low albumen powder modulate container, and the input port of reverse osmosis membrane filt connects with the first outlet tube
Logical, the filtrate (liquid of reverse osmosis membrane filt is connected to by water pipe with water pot, and the concentrated solution outlet of reverse osmosis membrane filt passes through
Second concentrate efferent duct modulates reservoir with low albumen powder.
4. a kind of plasma extraction system as claimed in claim 3, it is characterised in that：Further include the first cartridge filter, first
Cartridge filter is mounted on the first outlet tube between membrane filter and reverse osmosis membrane filt.
5. such as a kind of plasma extraction system of Claims 1 to 4 any one of them, it is characterised in that：Further include being mounted on into liquid
The second cartridge filter on pipe.
6. such as a kind of plasma extraction system of Claims 1 to 4 any one of them, it is characterised in that：Further include controller, liquid
Concentration detection apparatus is liquid concentration testing sensor, controller connection supercharging pump group, valve group, strength of fluid detection sensing
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721626950.0U CN207667449U (en) | 2017-11-29 | 2017-11-29 | A kind of plasma extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721626950.0U CN207667449U (en) | 2017-11-29 | 2017-11-29 | A kind of plasma extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207667449U true CN207667449U (en) | 2018-07-31 |
Family
ID=62966518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721626950.0U Expired - Fee Related CN207667449U (en) | 2017-11-29 | 2017-11-29 | A kind of plasma extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207667449U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115487582A (en) * | 2022-10-17 | 2022-12-20 | 广东百维生物科技有限公司 | Method for recovering precisely filtered collagen liquid |
-
2017
- 2017-11-29 CN CN201721626950.0U patent/CN207667449U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115487582A (en) * | 2022-10-17 | 2022-12-20 | 广东百维生物科技有限公司 | Method for recovering precisely filtered collagen liquid |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180731 Termination date: 20201129 |