CN106000103A - Fluid feed liquid concentration device - Google Patents
Fluid feed liquid concentration device Download PDFInfo
- Publication number
- CN106000103A CN106000103A CN201610583964.2A CN201610583964A CN106000103A CN 106000103 A CN106000103 A CN 106000103A CN 201610583964 A CN201610583964 A CN 201610583964A CN 106000103 A CN106000103 A CN 106000103A
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- Prior art keywords
- concentrator
- concentration
- membrane separation
- fluid
- pipeline
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/027—Nanofiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/08—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/145—Ultrafiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/18—Apparatus therefor
Abstract
The invention discloses a fluid feed liquid concentration device. The fluid feed liquid concentration device comprises a storage device and a conveying device which are communicated with each other through a pipe. The fluid feed liquid concentration device further comprises a membrane separation concentrator. The membrane separation concentrator is communicated in the pipe through a valve device. The concentration process is achieved through the membrane separation concentrator, a membrane separation technology is used to remove water molecules in fluid feed liquid, a certain pressure and a flowing motion of fluid are provided in the membrane separation concentrator to discharge a certain amount of moisture in the mixed fluid out of the membrane separation concentrator within a certain time, and feed liquid raw stock high in concentration remains. The device can prepare products relatively accurate in concentration through working time and pressure flow control. Moisture can be concentrated continuously through the production mode of the device, heating of the products for the reason of concentration is not needed, vacuum operation is not needed, and the problems that during conventional fluid feed liquid concentration, inherent smell is lost, the production is not continuous and the difficulty in control occurs are effectively solved.
Description
Technical field
The present invention relates to food and medicine technical field of processing equipment, more particularly, it relates to a kind of fluid material
Liquid concentrator.
Background technology
In food and medicine processing industry, concentrate the behaviour being exactly to remove partial solvent (typically water) from solution
Make process, be also solute and the uniform mixed liquor of solvent be partially separated process.Feed liquid can be removed by concentrating
In substantial amounts of moisture, reduce quality and volume, reduce packaging, storage and freight；Concentration can carry
High goods concentration, increases osmotic pressure, reduces water activity, suppresses growth of microorganism, extends the shelf life；
Concentration can be as the preprocessing process being dried, crystallize or be dehydrated completely；Can reduce dehydrated by concentration
Energy consumption in journey, reduces production cost；Concentration can also effectively remove undesirable volatile material and not
Good local flavor, improves product quality.But material can lose some local flavor or nutrient substance in concentration process,
Therefore, it is very important for selecting rational method for concentration and suitable condition.
Most fluid feedstream of the prior art realizes concentrating by the way of transpiring moisture, as utilized heating
Vacuumizing makes the moisture in product feed liquid evaporate, and the taste intrinsic due to high concentration feed liquid and fragrance meeting exist
Have during vacuum dispelling the stagnated QI and discharge phenomenon with vacuum pump, cause the loss of flavor that food is intrinsic, serious even system
Produce substandard products.
As in the processing of bean products, such as processing high concentration bean curd manufacturing engineering, original condensing mode is:
Heating in vacuum fermented bean drink about 20 minutes under vacuum state, use monoblock type to concentrate the mode removing moisture removal, taste
Road and fragrance cause a large amount of loss；And the traditional method multi-pass operation to be passed through of heating in vacuum, and with
Time confirm that fermented bean drink concentration, complicated operating environment and qualitative control all affect production efficiency, heating in vacuum is dense
Contracting is not continuous way, and after repeatedly concentrating, the loss of the taste that product is intrinsic drastically increases, and becomes making height
The obstacle of quality product.
In sum, how to efficiently solve fluid feedstream such as fermented bean drink and lose the skills such as intrinsic abnormal smells from the patient when concentrating
Art problem, is current those skilled in the art's urgent problem.
Summary of the invention
In view of this, it is an object of the invention to provide a kind of fluid feedstream concentrator, this fluid feedstream
The design of concentrator can efficiently solve fluid feedstream such as fermented bean drink and lose the skills such as intrinsic abnormal smells from the patient when concentrating
Art problem.
In order to achieve the above object, the present invention provides following technical scheme:
A kind of fluid feedstream concentrator, including by the storage device of pipeline connection and conveyer device, also
Including membrane separation concentration device, described membrane separation concentration device be communicated in pipeline by valving.
Preferably, in above-mentioned fluid feedstream concentrator, described storage device includes the liquid storage providing raw material
Tank, is provided with level sensor in described liquid storage tank, the liquid level in induction system.
Preferably, in above-mentioned fluid feedstream concentrator, also include master control set, described master control set with
Described level sensor is electrically connected, and described liquid storage tank is connected with pipeline by going out liquid automatic valve, described
Go out liquid automatic valve to be electrically connected with described master control set.
Preferably, in above-mentioned fluid feedstream concentrator, described in go out liquid automatic valve and described liquid storage tank
Bottom connection.
Preferably, in above-mentioned fluid feedstream concentrator, described conveyer device includes leading to described liquid storage tank
Cross the transfer pump that pipeline is connected.
Preferably, in above-mentioned fluid feedstream concentrator, described transfer pump and described membrane separation concentration device it
Between pipeline connect have the defecator for removing foreign body.
Preferably, in above-mentioned fluid feedstream concentrator, described membrane separation concentration device includes two or two
The membrance concentration unit of more parallel, described membrance concentration unit all accesses pipeline by part flow arrangement.
Preferably, in above-mentioned fluid feedstream concentrator, described membrance concentration unit is all connected with collecting tank,
Being provided with concentrated solution delivery pump between described membrance concentration unit and described collecting tank, described membrance concentration unit is equal
It is communicated with and the blowoff line of other liquid isolated for discharging.
Preferably, in above-mentioned fluid feedstream concentrator, also include for cleaning described membrance concentration unit
Detergent line, described detergent line is all connected with described membrance concentration unit by cleaning control valve, described
Cleaning pump and cleaned filter it is provided with in detergent line.
Preferably, in above-mentioned fluid feedstream concentrator, also include for detection membrane segregation apparatus and conveying
The pressure inductor of pipeline inner pressure between device, described pressure inductor is electrically connected with described master control set,
The pressure data that described master control set is recorded by pressure inductor controls opening of described cleaning control valve
Close.
The fluid feedstream concentrator that the present invention provides, including by the storage device of pipeline connection and conveying
Device, also includes membrane separation concentration device, described membrane separation concentration device be communicated in pipeline by valving
In.Use the technical scheme that the present invention provides, realized the process concentrated by membrane separation concentration device, use
Hydrone in fluid feedstream is removed by the principle of membrance separation, supplies certain pressure in membrane separation concentration device
With the flow motion of fluid, within a certain period of time a certain amount of moisture in fluid-mixing is discharged membrance separation
Concentrator, leaves the feed liquid oleo stock that concentration is higher, and this device can pass through working time and pressure flow hybrid control
Prepare the product that concentration is relatively accurate, use this equipment the mode of production can with continuous concentration moisture,
And without because product is heated by the reason concentrated, being not required to carry out vacuumizing, efficiently solve
During conventional fluid feed liquid concentrates, intrinsic abnormal smells from the patient can be lost, produce the discontinuous problem controlling to be difficult to etc..
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to reality
Execute the required accompanying drawing used in example or description of the prior art to be briefly described, it should be apparent that below,
Accompanying drawing in description is only some embodiments of the present invention, for those of ordinary skill in the art,
On the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The system schematic of the fluid feedstream concentrator that Fig. 1 provides for the embodiment of the present invention.
In accompanying drawing, labelling is as follows:
Liquid storage tank 1, level sensor 2, go out liquid automatic valve 3, transfer pump 4, defecator 5, membrance concentration
Unit 6, blowoff line 7, concentrated solution delivery pump 8, detergent line 9, cleaning pump 10, cleaned filter 11.
Detailed description of the invention
The embodiment of the invention discloses a kind of fluid feedstream concentrator, exist solving fluid feedstream such as fermented bean drink
The technical problems such as intrinsic abnormal smells from the patient are lost during concentration.
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the present invention, and
It is not all, of embodiment.Based on the embodiment in the present invention, those of ordinary skill in the art are not doing
Go out the every other embodiment obtained under creative work premise, broadly fall into the scope of protection of the invention.
Refer to the system schematic of the fluid feedstream concentrator that Fig. 1, Fig. 1 provide for the embodiment of the present invention.
The fluid feedstream concentrator that the present invention provides, including by the storage device of pipeline connection and conveying
Device, also includes membrane separation concentration device, described membrane separation concentration device be communicated in pipeline by valving
In.
Wherein, control whether membrane separation concentration device accesses pipeline work by valving, optionally arrange
Master control, realizes controlling, to improve the automaticity of equipment to valving by master control；Optionally exist
Equipment arranges attemperating unit, in order to make membrane separation concentration device work within the temperature range of suitable services,
It is unlikely to too high causes quality variation with the work efficiency and holding product temperature improving membrance concentration.Membrance separation
Use filter membrane to realize the concentration of feed liquid in concentrator, can determine according to different feed liquid kinds and use film
Kind, conventional filter membrane includes following several: reverse osmosis membrane, is used for removing chemical ion composition；Nanofiltration
Film, for removing the material of the molecular weight certain class between 200-500, according under polymer particles state,
Removal degree is different, is i.e. line style or spherical relevant with the apperance of particle；Ultrafilter membrane, removes molecular weight
2000-200000 secondary filter.Additionally, this type of filter membrane also has variety classes not enumerate at this.
Optionally, when using this equipment to carry out the production such as bean product, the follow-up of membrane separation concentration device is gone back
Arranging other machine-shaping devices, the fermented bean drink after concentration is directly entered and solidifies for the space of molding,
After solidification, after Preset Time, product finalizes the design almost, and carries out rupturing operation by intracavity shearing device, to cut-out
Product pack, preserve bean curd original flavor, produce the bean curd of safe high-quality.
Use the technical scheme that the present invention provides, realized the process concentrated by membrane separation concentration device, use
Hydrone in fluid feedstream is removed by the principle of membrance separation, supplies certain pressure in membrane separation concentration device
With the flow motion of fluid, within a certain period of time a certain amount of moisture in fluid-mixing is discharged membrance separation
Concentrator, leaves the feed liquid oleo stock that concentration is higher, and this device can pass through working time and pressure flow hybrid control
Prepare the product that concentration is relatively accurate, use this equipment the mode of production can with continuous concentration moisture,
And without because product is heated by the reason concentrated, being not required to carry out vacuumizing, efficiently solve
During conventional fluid feed liquid concentrates, intrinsic abnormal smells from the patient can be lost, produce the discontinuous problem controlling to be difficult to etc..
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, described storage device includes the liquid storage tank 1 providing raw material, sets in described liquid storage tank 1
It is equipped with level sensor 2, the liquid level in induction system.
Owing to liquid storage tank directly connects with the working line of equipment, examined in time by arranging of level sensor
Liquid level in examining system is to determine, whether membrance concentration separator position exists the raw material of q.s adds
Work, when material quantity deficiency, instantly prompting operator add raw material by liquid storage tank in system；In addition
Level sensor is preferred, equally the retaining amount in sensing liquid storage tank, when the raw material in liquid storage tank not
Point out operator to supplement raw material in time during foot, or carry out the time-out produced.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, also including master control set, described master control set is electric with described level sensor 2
Connecting, described liquid storage tank 1 is connected with pipeline by going out liquid automatic valve 3, described in go out liquid automatic valve 3
It is electrically connected with described master control set.
The technical scheme that the present embodiment provides is provided with master control set, and master control set can receive level sensor
The real-time level signal sent, and by judge whether that liquid opened out by needs automatic with the contrast of presupposed information
Valve supplements raw material to membrance concentration separator；When requiring supplementation with raw material, it is automatic that master control set controls liquid
Valve opening supplements in equipment specifies the raw material of component so that equipment carries out continuous continual production, carries
The high automaticity of equipment, improves the efficiency of production.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, described in go out liquid automatic valve 3 and connect with the bottom of described liquid storage tank 1.
The technical scheme that the present embodiment provides arranges liquid outlet in the bottom of liquid storage tank, and goes out liquid automatic valve
Connection.Material liquid, when liquid storage tank exports, goes out liquid steady to use this design to ensure, true in valve opening
Under stable condition, changes in flow rate is little will not carry substantial amounts of air, decreases air unnecessary in system and deposits
Amount, decreases the foam of output in production.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, described conveyer device includes the transfer pump 4 connected with described liquid storage tank 1 by pipeline.
The technical scheme that the present embodiment provides arranges transfer pump in pipeline, and transfer pump is positioned at liquid storage tank and film
In pipeline between concentrating and separating device.There is provided necessity and suitable by the membrance separation moisture that is set to of transfer pump
The operating pressure closed, and suitable flow is provided, in order to the liquid near immediate updating film, it is ensured that infiltration
Pressure reduction, makes the operation of membrance separation efficiently carry out.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, pipeline between described transfer pump 4 and described membrane separation concentration device connect have for
Remove the defecator 5 of foreign body.
The present embodiment provide technical scheme arrange between transfer pump and membrance concentration separator defecator with
Just remove the granule in oleo stock or the impurity of other states, the film in effective protecting film concentrating and separating device, prevent
Only on film, impurity accumulation causes separation efficiency to reduce；In like manner, also can set between transfer pump and liquid storage tank
Put filter, prevent the impurity in oleo stock from entering transfer pump and cause impurity at transfer pump to pile up flux depression
Hurry up.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, described membrane separation concentration device includes the membrance concentration unit of two or more parallel connections
6, described membrance concentration unit 6 all accesses pipeline by part flow arrangement.
The technical scheme that the present embodiment provides, membrane separation concentration device includes multiple membrance concentration unit, whole films
Upgrading unit all accesses pipeline by part flow arrangement, and the liquid outlet of membrance concentration unit arranges equally and flows device,
Product is collected so that unified.The present embodiment is provided with multiple membrance concentration unit, can carry out membrance concentration simultaneously
Work, improves thickening efficiency, and can effectively prevent the operating pressure of single membrance concentration unit excessive
Cause membrane structure loss too fast.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, described membrance concentration unit 6 is all connected with collecting tank, described membrance concentration unit 6 with
Be provided with concentrated solution delivery pump 8 between described collecting tank, described membrance concentration unit 6 be all communicated with for arranging
Go out the blowoff line 7 of other liquid isolated.
In the technical scheme that the present embodiment provides, include collecting tank, by concentrated solution collecting pump, film is dense
The isolated concentrated solution of contracting unit is unified to be recycled in collecting tank, and unified receipts are the most effectively easy in this design
Collection allotment；Blowoff line is set simultaneously, owing to using the mode of this membrance concentration of membrance concentration unit, so
When output product, also can directly discharge eliminate at the opposite side output clear water of film simultaneously
The cost that waste water processes.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, also include the detergent line 9 for cleaning described membrance concentration unit 6, described cleaning
Pipeline 9 is all connected with described membrance concentration unit 6 by cleaning control valve, sets in described detergent line 9
It is equipped with cleaning pump 10 and cleaned filter 11.
The principle using permeable membrane carries out liquid concentration, the work initial stage due to membrane structure better performances, so
System is not required to the highest pressure in position can realize osmosis filtration, institute along with running time lengthening, film
Through performance declines, it is difficult to carry out the concentration of product the most efficiently.Arrange in system clearly for this situation
Wash pipeline, when stopping producing, provide cleaning power that film is rinsed by cleaning pump, in order to remove
Impurity on film, recovers the concentrating capacity of membrane structure；Also set up filter will to be used for cleaning simultaneously
Water the most once filter, remove the impurity that may carry, it is ensured that cleaning performance.
For optimizing technique scheme further, on the basis of above-described embodiment preferably, above-mentioned fluid
In feed liquid concentrator, also include for the pressure of pipeline inner pressure between detection membrane segregation apparatus and conveyer device
Power induction apparatus, described pressure inductor is electrically connected with described master control set, and described master control set is by pressure
The pressure data that power induction apparatus records controls the opening and closing of described cleaning control valve.
When reverse osmosis membrane accumulated impurity, its through performance is deteriorated, thus it is slack-off to cause system to run, pipe
Intrinsic pressure in road thus raises, so the technical scheme that the present embodiment proposes arranges pressure sensitive in pipeline
Device can accurately judge the situation of equipment operating condition and film, judges that film is the need of clearly by master control set
Wash, if desired for then opening.
Cleaning process, specifically, initial stage discharge pressure runs under very light pressure, changes over time
The rubbish of membrance separation becomes many, and the water yield discharged by blowoff line is tailed off, and inside is uprised by pressure, this
Time by master control set, production is switched to automatic washing mode, be carried out removing rubbish within membrance separation
After rubbish, then produce.
Of course for ensureing that equipment is in good operating mode, it is possible to producing gap routine cleaning membrane structure, i.e.
Complete automatically to be cleaned up by the rubbish within device and membrane separator after flow process produces, flow can be implemented about
During for producing, the 20% of flow circulates to reach to clean purpose in a large number.
In this specification, each embodiment uses the mode gone forward one by one to describe, and each embodiment stresses
Being the difference with other embodiments, between each embodiment, identical similar portion sees mutually.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses
The present invention.Multiple amendment to these embodiments will be aobvious and easy for those skilled in the art
See, generic principles defined herein can without departing from the spirit or scope of the present invention,
Realize in other embodiments.Therefore, the present invention is not intended to be limited to the embodiments shown herein,
And it is to fit to the widest scope consistent with principles disclosed herein and features of novelty.
Claims (10)
1. a fluid feedstream concentrator, including by the storage device of pipeline connection and conveyer device,
It is characterized in that, also include that membrane separation concentration device, described membrane separation concentration device connect with by valving
In pipeline.
Fluid feedstream concentrator the most according to claim 1, it is characterised in that described storage fills
Put the liquid storage tank including providing raw material, in described liquid storage tank, be provided with level sensor, for induction system
Interior liquid level.
Fluid feedstream concentrator the most according to claim 2, it is characterised in that also include master control
Device, described master control set is electrically connected with described level sensor, and described liquid storage tank is automatic by going out liquid
Valve and pipeline are connected, described in go out liquid automatic valve and be electrically connected with described master control set.
Fluid feedstream concentrator the most according to claim 3, it is characterised in that described in go out liquid from
Movable valve connects with the bottom of described liquid storage tank.
Fluid feedstream concentrator the most according to claim 2, it is characterised in that described conveying fills
Put the transfer pump including being connected by pipeline with described liquid storage tank.
Fluid feedstream concentrator the most according to claim 5, it is characterised in that described transfer pump
And the pipeline between described membrane separation concentration device is connected the defecator for removing foreign body.
7. according to the fluid feedstream concentrator described in any one of claim 3 to 6, it is characterised in that
Described membrane separation concentration device includes the membrance concentration unit of two or more parallel connections, described membrance concentration unit
All access pipeline by part flow arrangement.
Fluid feedstream concentrator the most according to claim 7, it is characterised in that described membrance concentration
Unit is all connected with collecting tank, is provided with concentrated solution conveying between described membrance concentration unit and described collecting tank
Pump, described membrance concentration unit is all communicated with and the blowoff line of other liquid isolated for discharging.
Fluid feedstream concentrator the most according to claim 8, it is characterised in that also include for
Cleaning the detergent line of described membrance concentration unit, described detergent line is by cleaning control valve and described film
Upgrading unit all connects, and is provided with cleaning pump and cleaned filter in described detergent line.
Fluid feedstream concentrator the most according to claim 9, it is characterised in that also include using
The pressure inductor of pipeline inner pressure between detection membrane segregation apparatus and conveyer device, described pressure inductor
It is electrically connected with described master control set, the pressure data control that described master control set is recorded by pressure inductor
Make the opening and closing of described cleaning control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610583964.2A CN106000103A (en) | 2016-07-22 | 2016-07-22 | Fluid feed liquid concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610583964.2A CN106000103A (en) | 2016-07-22 | 2016-07-22 | Fluid feed liquid concentration device |
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| Publication Number | Publication Date |
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| CN106000103A true CN106000103A (en) | 2016-10-12 |
Family
ID=57117409
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610583964.2A Pending CN106000103A (en) | 2016-07-22 | 2016-07-22 | Fluid feed liquid concentration device |
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| CN (1) | CN106000103A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108261924A (en) * | 2016-12-30 | 2018-07-10 | 上海杰隆生物制品股份有限公司 | A kind of preparation of the dehydration removing sodium device and hyponatremia slurry protein powder of animal blood plasma |
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| CN103495343A (en) * | 2013-10-21 | 2014-01-08 | 哈尔滨工业大学 | Device for concentrating glucose by multi-membrane method and method for preparing concentrated glucose by device |
| CN203710923U (en) * | 2013-12-20 | 2014-07-16 | 黄山华绿园生物科技有限公司 | Concentrating system |
| CN104084047A (en) * | 2014-07-17 | 2014-10-08 | 新疆鹏弘生物科技有限公司 | Glycyrrhiza extracting solution clarification and concentration membrane system |
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Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6899812B2 (en) * | 1998-11-23 | 2005-05-31 | Zenon Environmental Inc. | Water filtration using immersed membranes |
| CN101080263A (en) * | 2004-10-15 | 2007-11-28 | 特诺有限公司 | Improved method and device for concentrating a slurry |
| CN101641016A (en) * | 2007-01-18 | 2010-02-03 | 太平洋进程有限公司 | Mobile concentration system that is used to suckle and method |
| CN101934196A (en) * | 2009-07-14 | 2011-01-05 | 中国制浆造纸研究院 | Plate type ultra-filtration membrane separation device for chemical-mechanical pulp making waste liquid concentration |
| CN103084066A (en) * | 2013-01-23 | 2013-05-08 | 余苟 | Membrane filtration gelatin dehydration preconcentration system |
| CN103495343A (en) * | 2013-10-21 | 2014-01-08 | 哈尔滨工业大学 | Device for concentrating glucose by multi-membrane method and method for preparing concentrated glucose by device |
| CN203710923U (en) * | 2013-12-20 | 2014-07-16 | 黄山华绿园生物科技有限公司 | Concentrating system |
| CN104084047A (en) * | 2014-07-17 | 2014-10-08 | 新疆鹏弘生物科技有限公司 | Glycyrrhiza extracting solution clarification and concentration membrane system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108261924A (en) * | 2016-12-30 | 2018-07-10 | 上海杰隆生物制品股份有限公司 | A kind of preparation of the dehydration removing sodium device and hyponatremia slurry protein powder of animal blood plasma |
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