CN202222379U - Salted egg white desalination and concentration equipment - Google Patents

Salted egg white desalination and concentration equipment Download PDF

Info

Publication number
CN202222379U
CN202222379U CN2011203232619U CN201120323261U CN202222379U CN 202222379 U CN202222379 U CN 202222379U CN 2011203232619 U CN2011203232619 U CN 2011203232619U CN 201120323261 U CN201120323261 U CN 201120323261U CN 202222379 U CN202222379 U CN 202222379U
Authority
CN
China
Prior art keywords
salted egg
concentration equipment
desalination
egg albumen
storage device
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011203232619U
Other languages
Chinese (zh)
Inventor
谭先铸
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN2011203232619U priority Critical patent/CN202222379U/en
Application granted granted Critical
Publication of CN202222379U publication Critical patent/CN202222379U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Meat, Egg Or Seafood Products (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model provides salted egg white desalination and concentration equipment which comprises a material storage device as well as a film component, a filter and a material supply pump which are connected in sequence through a pipeline; the circulating reflux port of the material storage device is connected with the material outlet of the film component; and the inlet of the material supply pump is connected with the material outlet of the material storage device. The salted egg white desalination and concentration equipment has the benefits of being operated at ordinary temperature, being energy-saving and environment-friendly, adopting a physical technology, being pollution-free and safe, and having a simple structure and a simple operating process.

Description

Salted egg albumen desalination and concentration equipment
Technical field
The utility model relates to a kind of desalination and concentration equipment of liquid material, relates in particular to a kind of salted egg albumen desalination and concentration equipment that is applied to food industry.
Background technology
In food industry, usually can only use preserved egg yellow, because salted egg albumen is because of containing a large amount of moisture and salinity; Can't normally eat; If abandon, not only make a large amount of protein losses in the egg white, also can cause severe contamination to environment; Therefore need carry out desalination and concentration to salted egg albumen, with effective extraction protein wherein.
Summary of the invention
The purpose of the utility model is to provide a kind of salted egg albumen desalination and concentration equipment, to satisfy salted egg albumen is carried out desalination and is extracted the wherein needs of protein.
To achieve these goals; The salted egg albumen desalination and concentration equipment that the utility model provides comprises material storage device and the membrane module that is connected successively through pipeline, filter, charging pump; The material outlet that loops back head piece and said membrane module of said material storage device is connected, and the import of said charging pump is connected with the material outlet of said material storage device.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, also comprise the supercharging circulating pump, said supercharging circulating pump is connected between said filter and the membrane module.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, also connect a bypass pipeline between said supercharging inlet of circulating pump and the outlet.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, also comprise heat exchanger, said heat exchanger is connected between the material outlet of material inlet and material storage device of said charging pump.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, be provided with rinse liquid outlet between said heat exchanger and the charging pump.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, the protein of said material storage device concentrates the liquid outlet and is provided with a valve.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, said material storage device is a material pot.
According to a kind of preferred implementation of above-mentioned salted egg albumen desalination and concentration equipment, wherein, said membrane module is a rolled membrane module.
The salted egg albumen desalination and concentration equipment that the utility model provides comprises filter, power set, raw material storage and feedway etc.; Its simply high efficiency extraction separate macromolecular protein and micromolecular salt grades, many beneficial effects such as the utlity model has normal temperature operation, energy-conserving and environment-protective, physical technology, green safety, device structure is simple, operating procedure is simple.
Description of drawings
Fig. 1 is the principle assumption diagram of the utility model preferred embodiment.
The specific embodiment
Below in conjunction with the accompanying drawing and the specific embodiment the utility model is explained further details.
Fig. 1 schematically shows the theory structure of the utility model preferred embodiment; Shown in it, this preferred embodiment includes but not limited to: as material pot 10, membrane module 3, supercharging circulating pump 6, filter 7, charging pump 8, heat exchanger 9, the valve 11 of the usefulness of material storage device.Wherein, the material outlet that loops back head piece 2, membrane module 3, supercharging circulating pump 6, filter 7, charging pump 8, heat exchanger 9, material pot 10 13 of material pot 10 connects through pipeline 4 successively, is connected with bypass duct 5 between the import of supercharging circulating pump 6 and the outlet.The protein that valve 11 is connected in material pot 10 concentrates the liquid outlet so that the protein that control outflow from material pot 10 is extracted from salted egg albumen concentrates liquid.In other embodiments, the material storage device is not limited to pot type equipment.
In this preferred embodiment, membrane module 3 is a rolled membrane module, is provided with rinse liquid outlet 14 between heat exchanger 9 and the charging pump 8, the liquid afterwards such as cleaning material pot 10 parts such as grade of being convenient to release.
When using this preferred embodiment; Raw material salted egg albumen solution from 1 input of the material inlet of material pot 10, is flowed out from material outlet 13, then via the driving of power output part charging pump 8, supercharging circulating pump 6; Between mass treatment parts membrane module 3, filter 7, heat exchanger 9, circulate; When the extraction concentration to salted egg albumen reaches technological requirement, can open valve 11, the protein that output can be applied to food concentrates liquid.Wherein, the salt solution that comprises small molecular weight material that filters out sees through liquid and flows out from the filtered fluid outlet 15 of membrane module 3.
In sum; The alleged salted egg albumen desalination and concentration of the utility model is meant the mixture of different-grain diameter molecule in the salted egg albumen through membrane module the time; According to different molecular weight, realize Selective Separation, whereby; Can macromolecule materials such as protein in the salted egg albumen effectively be separated with small molecular weight material such as salt, water, reach salted egg albumen solution desalination, concentrate.Through foregoing description, can know that the utility model runs on normal temperature environment when salted egg albumen solution is carried out desalination and concentration, loss of effective components is few; Energy consumption is low, has not only kept the natural flavor of egg, and energy-conserving and environment-protective; Technical process is pure physical process, does not have any chemical substance of interpolation, and food security is secure; Product structure is simple, operating procedure is simple, and production drops into little, and cost is low.
Can know that by technological general knowledge the utility model can be realized through other the embodiment that does not break away from its spirit or essential feature.Therefore, above-mentioned disclosed embodiment with regard to each side, all just illustrates, and is not only.All in the utility model scope or the change that is being equal in the scope of the utility model all comprised by the utility model.

Claims (8)

1. salted egg albumen desalination and concentration equipment; It is characterized in that; Comprise material storage device and the membrane module that is connected successively through pipeline, filter, charging pump; The material outlet that loops back head piece and said membrane module of said material storage device is connected, and the import of said charging pump is connected with the material outlet of said material storage device.
2. salted egg albumen desalination and concentration equipment according to claim 1 is characterized in that, also comprises the supercharging circulating pump, and said supercharging circulating pump is connected between said filter and the membrane module.
3. salted egg albumen desalination and concentration equipment according to claim 2 is characterized in that, also connects a bypass pipeline between said supercharging inlet of circulating pump and the outlet.
4. salted egg albumen desalination and concentration equipment according to claim 1 is characterized in that, also comprises heat exchanger, and said heat exchanger is connected between the material outlet of import and material storage device of said charging pump.
5. salted egg albumen desalination and concentration equipment according to claim 4 is characterized in that, is provided with rinse liquid outlet between said heat exchanger and the charging pump.
6. salted egg albumen desalination and concentration equipment according to claim 1 is characterized in that, the protein of said material storage device concentrates the liquid outlet and is provided with a valve.
7. salted egg albumen desalination and concentration equipment according to claim 1 is characterized in that said material storage device is a material pot.
8. salted egg albumen desalination and concentration equipment according to claim 1 is characterized in that said membrane module is a rolled membrane module.
CN2011203232619U 2011-08-31 2011-08-31 Salted egg white desalination and concentration equipment Expired - Fee Related CN202222379U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203232619U CN202222379U (en) 2011-08-31 2011-08-31 Salted egg white desalination and concentration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203232619U CN202222379U (en) 2011-08-31 2011-08-31 Salted egg white desalination and concentration equipment

Publications (1)

Publication Number Publication Date
CN202222379U true CN202222379U (en) 2012-05-23

Family

ID=46072994

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203232619U Expired - Fee Related CN202222379U (en) 2011-08-31 2011-08-31 Salted egg white desalination and concentration equipment

Country Status (1)

Country Link
CN (1) CN202222379U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102669724A (en) * 2012-05-24 2012-09-19 广州宝旺农副产品有限公司 Production process of dry eggs
CN102697090A (en) * 2012-05-31 2012-10-03 集美大学 Salted duck egg white desalination device
CN102972800A (en) * 2012-12-12 2013-03-20 江南大学 Device and method for micro-wave and vacuum ultra-filtrating integrated desalination of marinated egg white

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102669724A (en) * 2012-05-24 2012-09-19 广州宝旺农副产品有限公司 Production process of dry eggs
CN102669724B (en) * 2012-05-24 2014-09-10 广州宝旺农副产品有限公司 Production process of dry eggs
CN102697090A (en) * 2012-05-31 2012-10-03 集美大学 Salted duck egg white desalination device
CN102697090B (en) * 2012-05-31 2013-09-04 集美大学 Salted duck egg white desalination device
CN102972800A (en) * 2012-12-12 2013-03-20 江南大学 Device and method for micro-wave and vacuum ultra-filtrating integrated desalination of marinated egg white

Similar Documents

Publication Publication Date Title
CN201505465U (en) Continuous extraction separation concentrator
CN202222379U (en) Salted egg white desalination and concentration equipment
CN203043849U (en) Self-control ultrafiltration system
CN101982222A (en) Device for continuously concentrating gelatin by membrane technology
CN102972800B (en) Device and method for micro-wave and vacuum ultra-filtrating integrated desalination of marinated egg white
MX2016015260A (en) Silica products from geothermal fluids by reverse osmosis.
CN104397364B (en) A kind of pig blood extraction and application method
CN202569788U (en) Energy-saving refrigeration filtering unit
CN206391877U (en) A kind of milk concentrating and treating system
CN204841021U (en) Concentrated unit of poor cold extraction of high pressure
CN106349123A (en) Method for separating taurine in taurine crude product mother solution
CN103461642A (en) Preparation device for pig blood albumen powder with high performance
CN106914137A (en) A kind of film concentration systems and method
CN107376651A (en) A kind of Ultra filtration membrane method and device
CN104431413A (en) Method of comprehensively utilizing pig blood
Zhang et al. A rotating disk ultrafiltration process for recycling alfalfa wastewater
CN201823337U (en) Concentrating and crystallizing equipment for 5-hydroxyl tryptophan
EP3134200A1 (en) System for reducing product losses, product dilution, chemical dilution and water consumption in a crossflow membrane separation system
CN205874272U (en) Soybean peptide desalination purification enrichment facility
CN206127175U (en) Device of separation taurine in taurine crude mother liquor
CN201832564U (en) Continuous gelatin concentrating device by membrane method
CN205095449U (en) Pigment extraction device
CN207581439U (en) A kind of device to cold bile-duct dead angle ozone sterilization
CN102603439B (en) Method for adsorbing, coarse-filtering and fine-filtering impurities in oxidant saline solution
CN202881282U (en) Continuous and automatic reaction and separation device for soybean peptide

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120523

Termination date: 20130831