CN205575983U - Novel automatic concentrated desalination degerming system of albumen liquid - Google Patents
Novel automatic concentrated desalination degerming system of albumen liquid Download PDFInfo
- Publication number
- CN205575983U CN205575983U CN201620347884.2U CN201620347884U CN205575983U CN 205575983 U CN205575983 U CN 205575983U CN 201620347884 U CN201620347884 U CN 201620347884U CN 205575983 U CN205575983 U CN 205575983U
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- China
- Prior art keywords
- inlet
- enrichment facility
- ultrafiltration apparatus
- defecator
- liquid
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- 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
- 239000007788 liquid Substances 0.000 title claims abstract description 50
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 15
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 44
- 238000001802 infusion Methods 0.000 claims abstract description 21
- 238000001914 filtration Methods 0.000 claims abstract description 10
- 239000011550 stock solution Substances 0.000 claims description 24
- 239000012530 fluid Substances 0.000 claims description 19
- 230000001954 sterilising effect Effects 0.000 claims description 12
- 238000004659 sterilization and disinfection Methods 0.000 claims description 12
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 claims description 10
- 102000002322 Egg Proteins Human genes 0.000 claims description 10
- 108010000912 Egg Proteins Proteins 0.000 claims description 10
- 235000014103 egg white Nutrition 0.000 claims description 10
- 210000000969 egg white Anatomy 0.000 claims description 10
- 229910000831 Steel Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 239000010959 steel Substances 0.000 claims description 9
- 238000007789 sealing Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 238000011118 depth filtration Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 108091003079 Bovine Serum Albumin Proteins 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 229940098773 bovine serum albumin Drugs 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 108010088751 Albumins Proteins 0.000 description 1
- 102000009027 Albumins Human genes 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- -1 salt small-molecule Chemical class 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a novel automatic concentrated desalination degerming system of albumen liquid, includes liquid tank, filter equipment, enrichment facility and ultrafiltration device, enrichment facility upper end be provided with ultrafiltration device inlet and filter equipment inlet, the enrichment facility bottom is provided with ultrafiltration device infusion mouthful and the liquid mouth is returned to stoste, liquid tank is linked together with the filter equipment inlet through stoste infusion pipeline, and the filter equipment liquid outlet is linked together through clear solution pipeline and enrichment facility, the enrichment facility is linked together in ultrafiltration device inlet, ultrafiltration device liquid outlet respectively through ultrafiltration device infusion mouth and ultrafiltration device inlet to it is linked together with liquid tank to communicate back the liquid pipeline through stoste time liquid mouth. The utility model discloses an adopt liquid tank, filter equipment, enrichment facility to communicate the filtration degerming circulation on the throne of formation and the concentrated desalination circulation that cooperates filter equipment, ultrafiltration device to constitute each other, can realize concentration, desalination, degerming on the throne, improve production efficiency greatly, reduce workman intensity of labour.
Description
Technical field
This utility model relates to purifying plant technical field, particularly relates to a kind of Novel egg white liquor automatic concentration desalination sterilization system.
Background technology
During the purification thickening filtration of bovine serum albumin solution, owing to the thickening filtration time is longer, frequently result in growing of antibacterial in concentration tank, be therefore badly in need of a kind of there is the most degerming concentration systems.
Summary of the invention
In place of the purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of simple in construction, easy to use, a kind of Novel egg white liquor automatic concentration desalination sterilization system that whole automatizatioies concentrating and desalinating is the most degerming can be realized.
The purpose of this utility model is achieved through the following technical solutions:
A kind of Novel egg white liquor automatic concentration desalination sterilization system, including original fluid container, defecator, enrichment facility and ultrafiltration apparatus, described enrichment facility upper end be provided with ultrafiltration apparatus inlet and defecator inlet, be provided with ultrafiltration apparatus infusion port and stock solution liquid return hole bottom enrichment facility;Described original fluid container is connected with defecator inlet by stock solution infusion pipeline, and defecator liquid outlet is connected with enrichment facility by clear liquid pipeline;Described enrichment facility is connected respectively at ultrafiltration apparatus inlet, ultrafiltration apparatus liquid outlet by ultrafiltration apparatus infusion port and ultrafiltration apparatus inlet, and is connected with original fluid container by stock solution liquid return hole connection liquid back pipe road;Described defecator uses many group plate filter compositions, this filter strainer plate uses high accuracy aseptic filtration plate to carry out in-depth filtration, this plate filter is made up of inlet, liquid outlet, multi-stage booster pump, rustless steel sheet frame, Pressure gauge, described plate filter inlet is provided above Pressure gauge, stock solution infusion pipeline is connected with inlet by the multi-stage booster pump arranged bottom plate filter, and inlet filters by being shaped with the groove feed liquor suitable with inlet in rustless steel sheet frame;Being shaped with semicircle sealing outside described rustless steel sheet frame groove inlet side to cover, liquid outlet side is inwardly shaped with and seals, with semicircle, the semicircle seal groove that lid is suitable;It is set with metal inner tube in described enrichment facility, between enrichment facility outer wall and metal inner tube, is provided with vacuum layer, outside described device, be set with the multistage annular heating coil suitable with metal inner tube position.
And, described semicircle seal that lid periphery is uniform is shaped with a plurality of sealing fin.
And, at described defecator, the ultrafiltration apparatus inlet of setting, defecator inlet, ultrafiltration apparatus infusion port, stock solution liquid return hole are mounted on controlling ultrafiltration apparatus inlet dress valve, defecator inlet fast-assembling valve, ultrafiltration apparatus infusion port fast-assembling valve and the stock solution liquid return hole fast-assembling valve of its opening and closing.
And, it is additionally provided with Concentration Testing mouth bottom described enrichment facility.
And, it is additionally provided with the fluid level control device controlling defecator opening and closing inside described enrichment facility.
Advantage of the present utility model and economic effect be:
This utility model overcomes tradition concentration systems cannot circulate degerming technical barrier in place, the concentrating and desalinating of the filtration sterilization circulation in place formed by using original fluid container, defecator, enrichment facility to be interconnected and complement filter device, ultrafiltration apparatus composition circulates, concentration, desalination, the most degerming can be realized, it is greatly improved production efficiency, reduces labor strength.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of this utility model plate filter;
Fig. 3 is the partial enlarged drawing in this utility model A portion;
Fig. 4 is the structural representation of this utility model enrichment facility.
Detailed description of the invention
For content of the present utility model, feature and effect can be further appreciated that, hereby enumerate following example, and it is as follows to coordinate accompanying drawing to describe in detail.It should be noted that the present embodiment is illustrative, it not determinate, it is impossible to thus limit protection domain of the present utility model.
A kind of Novel egg white liquor automatic concentration desalination sterilization system, including original fluid container 11, defecator 13, enrichment facility 8 and ultrafiltration apparatus 1, described enrichment facility upper end be provided with ultrafiltration apparatus inlet 4 and defecator inlet 7, be provided with ultrafiltration apparatus infusion port 17 and stock solution liquid return hole 15 bottom enrichment facility;Described original fluid container is connected with defecator inlet by stock solution infusion pipeline 12, and defecator liquid outlet is connected with enrichment facility by clear liquid pipeline 9;Described enrichment facility is connected respectively at ultrafiltration apparatus inlet 19, ultrafiltration apparatus liquid outlet 2 by ultrafiltration apparatus infusion port and ultrafiltration apparatus inlet, and is connected with original fluid container by stock solution liquid return hole connection liquid back pipe road 10;Described defecator uses many group plate filter compositions, this filter strainer plate uses high accuracy aseptic filtration plate to carry out in-depth filtration, this plate filter is formed 21 by inlet 22, liquid outlet 23, multi-stage booster pump 24, rustless steel sheet frame 20, Pressure gauge, described plate filter inlet is provided above Pressure gauge, stock solution infusion pipeline is connected with inlet by the multi-stage booster pump arranged bottom plate filter, and inlet filters by being shaped with groove 25 feed liquor suitable with inlet in rustless steel sheet frame;Being shaped with semicircle sealing lid 26 outside described rustless steel sheet frame groove inlet side, liquid outlet side is inwardly shaped with and seals, with semicircle, the semicircle seal groove 27 that lid is suitable;It is set with metal inner tube 31 in described enrichment facility, between enrichment facility outer wall and metal inner tube, is provided with vacuum layer 30, outside described device, be set with the multistage annular heating coil 29 suitable with metal inner tube position.
And, described semicircle seal that lid periphery is uniform is shaped with a plurality of sealing fin 28.Described defecator uses many group plate filter compositions, and this filter strainer plate described uses high accuracy aseptic filtration plate to carry out in-depth filtration.At described defecator, the ultrafiltration apparatus inlet of setting, defecator inlet, ultrafiltration apparatus infusion port, stock solution liquid return hole are mounted on controlling ultrafiltration apparatus inlet dress valve 3, defecator inlet fast-assembling valve 6, ultrafiltration apparatus infusion port fast-assembling valve 18 and the stock solution liquid return hole fast-assembling valve 16 of its opening and closing.Concentration Testing mouth 14 it is additionally provided with bottom described enrichment facility.The fluid level control device 5 controlling defecator opening and closing it is additionally provided with inside described enrichment facility.
This integrating device all uses sanitation-grade anticorrosive material manufacture, inside and outside smooth easy to clean, and cleaning solution can discharge thoroughly, stops cleaning solution and pollutes protein liquid.Ultrafiltration apparatus and enrichment facility are in closed state at work, are prevented effectively from outside antibacterial and enter feed liquid and produce external contamination.Plate filter is interconnected with enrichment facility, original fluid container, forms filtration cycle, thus realizes the most degerming.And can be by regulating the unlatching size adjustment circulating fluid flow rate of the every valve of enrichment facility, with the working time of controlling filter.Set up fluid level control device and achieve the automation mechanized operation of filter.Complete equipment is manufactured and designed by production scale, and each several part equipment is mutually matched, it is easy to control product quality.
In use, the low concentration bovine serum albumin solution (abbreviation stock solution) that will extract in retort, add in the original fluid container of this integrated system, connect main power, by liquid level meter control, filter is opened naturally.First closing stock solution liquid return hole fast-assembling valve when filtrate has just enter into concentration tank, in device to be concentrated, liquid opens stock solution liquid return hole fast-assembling valve when being more than half.Now, in original fluid container, feed liquid starts the cycle over flowing, and is able to filtration sterilization.Opening ultrafiltration apparatus, regulation ultrafilter inlet and outlet pressure table makes the moisture in stock solution, the salt small-molecule substance that grades constantly discharge on request, and albumin is trapped, being back in concentration tank, As time goes on, protein liquid is concentrated, salt reduces, and protein concentration is improved.Finally, close enrichment facility and be connected to the stock solution liquid return hole fast-assembling valve of original fluid container, stock solution is all filtered and completes in pumping into concentration tank to concentrate.Concentrated solution is the most freeze-dried makes powdered finished product.
Claims (5)
1. a Novel egg white liquor automatic concentration desalination sterilization system, including original fluid container, defecator, enrichment facility and ultrafiltration apparatus, described enrichment facility upper end be provided with ultrafiltration apparatus inlet and defecator inlet, be provided with ultrafiltration apparatus infusion port and stock solution liquid return hole bottom enrichment facility;Described original fluid container is connected with defecator inlet by stock solution infusion pipeline, and defecator liquid outlet is connected with enrichment facility by clear liquid pipeline;Described enrichment facility is connected respectively at ultrafiltration apparatus inlet, ultrafiltration apparatus liquid outlet by ultrafiltration apparatus infusion port and ultrafiltration apparatus inlet, and is connected with original fluid container by stock solution liquid return hole connection liquid back pipe road;Described defecator uses many group plate filter compositions, this filter strainer plate uses high accuracy aseptic filtration plate to carry out in-depth filtration, this plate filter is made up of inlet, liquid outlet, multi-stage booster pump, rustless steel sheet frame, Pressure gauge, described plate filter inlet is provided above Pressure gauge, stock solution infusion pipeline is connected with inlet by the multi-stage booster pump arranged bottom plate filter, and inlet filters by being shaped with the groove feed liquor suitable with inlet in rustless steel sheet frame;Being shaped with semicircle sealing outside described rustless steel sheet frame groove inlet side to cover, liquid outlet side is inwardly shaped with and seals, with semicircle, the semicircle seal groove that lid is suitable;It is set with metal inner tube in described enrichment facility, between enrichment facility outer wall and metal inner tube, is provided with vacuum layer, outside described device, be set with the multistage annular heating coil suitable with metal inner tube position.
A kind of Novel egg white liquor automatic concentration desalination sterilization system the most according to claim 1, it is characterised in that: described semicircle seal that lid periphery is uniform is shaped with a plurality of sealing fin.
A kind of Novel egg white liquor automatic concentration desalination sterilization system the most according to claim 1, it is characterised in that: at described defecator, the ultrafiltration apparatus inlet of setting, defecator inlet, ultrafiltration apparatus infusion port, stock solution liquid return hole are mounted on controlling ultrafiltration apparatus inlet dress valve, defecator inlet fast-assembling valve, ultrafiltration apparatus infusion port fast-assembling valve and the stock solution liquid return hole fast-assembling valve of its opening and closing.
A kind of Novel egg white liquor automatic concentration desalination sterilization system the most according to claim 1, it is characterised in that: it is additionally provided with Concentration Testing mouth bottom described enrichment facility.
A kind of Novel egg white liquor automatic concentration desalination sterilization system the most according to claim 1, it is characterised in that: it is additionally provided with the fluid level control device controlling defecator opening and closing inside described enrichment facility.
Priority Applications (1)
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CN201620347884.2U CN205575983U (en) | 2016-04-21 | 2016-04-21 | Novel automatic concentrated desalination degerming system of albumen liquid |
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CN201620347884.2U CN205575983U (en) | 2016-04-21 | 2016-04-21 | Novel automatic concentrated desalination degerming system of albumen liquid |
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CN201620347884.2U Expired - Fee Related CN205575983U (en) | 2016-04-21 | 2016-04-21 | Novel automatic concentrated desalination degerming system of albumen liquid |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108380054A (en) * | 2018-05-09 | 2018-08-10 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
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2016
- 2016-04-21 CN CN201620347884.2U patent/CN205575983U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108380054A (en) * | 2018-05-09 | 2018-08-10 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20201125 Address after: 239400 north of balinghu road and west of Guanshan Avenue, Changcheng New District, Mingguang City, Chuzhou City, Anhui Province Patentee after: Anhui Kangyuan Biotechnology Co.,Ltd. Address before: 301800 Tianjin city Xin'an District Baodi Town New Road North (positive Street Road No. 6) Patentee before: TIANJIN KANGYUAN BIOTECHNOLOGY Co.,Ltd. |
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TR01 | Transfer of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160914 |
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CF01 | Termination of patent right due to non-payment of annual fee |