CN107439806A - A kind of method of wet method adjustment albumen powder protein content - Google Patents
A kind of method of wet method adjustment albumen powder protein content Download PDFInfo
- Publication number
- CN107439806A CN107439806A CN201710618960.8A CN201710618960A CN107439806A CN 107439806 A CN107439806 A CN 107439806A CN 201710618960 A CN201710618960 A CN 201710618960A CN 107439806 A CN107439806 A CN 107439806A
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- protein content
- albumen
- underflow
- butt
- mixing tank
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K20/00—Accessory food factors for animal feeding-stuffs
- A23K20/10—Organic substances
- A23K20/142—Amino acids; Derivatives thereof
- A23K20/147—Polymeric derivatives, e.g. peptides or proteins
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D11/00—Control of flow ratio
- G05D11/02—Controlling ratio of two or more flows of fluid or fluent material
- G05D11/035—Controlling ratio of two or more flows of fluid or fluent material with auxiliary non-electric power
- G05D11/08—Controlling ratio of two or more flows of fluid or fluent material with auxiliary non-electric power by sensing concentration of mixture, e.g. measuring pH value
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Polymers & Plastics (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Zoology (AREA)
- Animal Husbandry (AREA)
- Food Science & Technology (AREA)
- Power Engineering (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Peptides Or Proteins (AREA)
- Meat, Egg Or Seafood Products (AREA)
Abstract
The present invention relates to corn deep processing field, more particularly to a kind of method of wet method adjustment albumen powder protein content.The method that the wet method adjusts albumen powder protein content, including（1）Detect the butt protein content of protein concentrate slurries；（2）Regulatory protein content；（3）Protein content meets the requirements；（4）Steady production；（5）Production is fluctuated；The method of the wet method adjustment albumen powder protein content of the present invention, it is simple to operate, conveniently meet the requirement for the albumen powder that market difference egg contains, utilize on-line monitoring and the Automation Design programme-control protein slurry butt protein content, coarse starch milk is added to adjust the butt protein content of protein slurry to required value by finely tuning, this method can be widely popularized use in wet method starch production process, be a kind of method of truly feasible replacement albumen powder dry method batch mixing.
Description
Technical field
The present invention relates to corn deep processing field, more particularly to a kind of method of wet method adjustment albumen powder protein content,
In corn wet producing starch production process, it is ensured that the protein content of its byproduct albumen powder is in less deviation range
It is interior, effectively meet customer need, to avoid albumen powder from causing albumen mixture because protein content is uneven.
Background technology
For a long time, in Corn Starch Wet production process, important requirement is whole production held stationary, it is desirable to is formed sediment
The indices of powder and various byproducts all have stability.But for the businessman of albumen powder, for matching different animals
Feed or same biological different phase feed, the protein content of required albumen powder is different, in this case, starch life
Producer is produced to ensure that the stability of production it is necessary to keep albumen powder high protein content within a period of time, is protected within a period of time
Albumen powder low protein content is held, effective mixture processing is carried out according to customer demand to meet the requirement in albumen powder market；Or
It is the albumen powder for the ankyrin content that Starch Production manufacturer production goes out, it is how many albumen powders just commercially to sell egg to contain,
Easily cause can not meet the needs of market, often albumen powder does not sell good price, or albumen powder does not have market.To meet market
Demand, generally require and mixture is carried out to albumen powder, one kind is to carry out albumen powder mixture by equipment, and input is larger, but mixture is imitated
Fruit is undesirable；One kind is by manually carrying out mixture, although mixture can reach market demands, workload, working strength are larger,
Mixture is costly, most importantly, artificial to carry out unsafe factor of the albumen powder mixture with the presence of pollution.
The content of the invention
The present invention is in order to make up the defects of being not easy regulatory protein amyloid proteins content during existing production of corn starch, there is provided
A kind of simple and easy, the method for adjust automatically albumen powder protein content in the production process of starch.
The present invention is achieved through the following technical solutions：
A kind of method of wet method adjustment albumen powder protein content, it is characterised in that：Comprise the following steps：
（1）Detect the butt protein content of protein concentrate slurries：Treat heregulin underflow through passing through albumen in dense seitan mixing tank
Underflow contactor pump exports, and treats that heregulin underflow butt albumen contains in albumen on-line quick detection device detection albumen underflow contactor pump
Amount, and pass the data to control terminal；
（2）Regulatory protein content：When heregulin underflow butt protein content is undesirable, control terminal sends instruction,
Return valve I is opened, while opens the pneumatic control valve III on seperator, the inlet amount of heregulin underflow is treated by adjustment to adjust
The butt protein content of dense seitan mixing tank；
（3）Protein content meets the requirements：Work as step（2）When adjusting the butt protein content of dense seitan mixing tank and meeting the requirements, egg
White on-line quick detection device gives the data transfer of monitoring to control terminal, and control terminal sends instruction, opens pneumatic operated valve II, together
When closing volume valve I, satisfactory albumen underflow in dense seitan mixing tank is entered qualified tank, subsequently into subsequent processing；
（4）Steady production：When workshop steady production, the inlet amount of seperator is relatively stable, and now pneumatic control valve III is opened
Degree is in state is relatively fixed, and pneumatic operated valve II is in open mode, and return valve I is closed；
（5）Production is fluctuated：When fluctuation occurs in workshop, heregulin underflow butt albumen is treated in dense seitan mixing tank
Fluctuation also occurs in content, now repeats（1）、（2）（3）Step, until the protein slurry butt egg in dense seitan mixing tank contains
It is satisfactory stationary value.
Further, the albumen on-line quick detection device is near infrared online monitor, monitors albumen underflow in real time
The butt protein content of albumen underflow in contactor pump, to ensure that the protein content of final albumen powder product meets the requirements.
Step（2）It is coarse starch milk in the seperator, general seitan thickener underflow, which is used as, treats that heregulin underflow enters
Dense seitan mixing tank, because its protein content is higher, coarse starch milk is added into dense seitan mixing tank by seperator, makes albumen
Protein content is reduced to suitable protein content in underflow, meets the requirement of production.
The return valve I controls albumen underflow contactor pump to dense seitan mixing tank reflux entry, by undesirable egg
White underflow returns the allotment that dense seitan mixing tank carries out protein content again, that is, do not meet will for the protein content of albumen underflow
When asking, return valve I is in opening, is closed when qualified.
The pneumatic operated valve II controls albumen underflow contactor pump to be fed to qualified tank, when the protein content of albumen underflow conforms to
When asking, pneumatic operated valve II is in opening, and qualified protein slurry enters qualified tank, when protein content is undesirable, pneumatically
Valve II is closed.
The pneumatic control valve III controls seperator to squeeze into roughly starch milk to dense seitan mixing tank, and adjusts pneumatic regulation
The aperture of valve III, adjusting the amount for the coarse starch milk for flowing into dense seitan mixing tank, finally adjust albumen in dense seitan mixing tank
The protein content of underflow.
The beneficial effects of the invention are as follows：The method of the wet method adjustment albumen powder protein content of the present invention, it is simple to operate, it is convenient
Meet the requirement for the albumen powder that market difference egg contains, utilize on-line monitoring and the Automation Design programme-control protein slurry butt egg
Bai Hanliang, coarse starch milk is added to adjust the butt protein content of protein slurry to required value by finely tuning, this method can be
Use is widely popularized in wet method starch production process, is a kind of method of truly feasible replacement albumen powder dry method batch mixing.
Brief description of the drawings
Accompanying drawing 1 is process flow diagram of the invention；
In figure, 1. dense seitan mixing tanks, 2. seperators, 3. seitan thickener underflows, 4. qualified tanks, 5. albumen underflow batch mixings
Pump, 6. albumen on-line quick detection devices, 7. pneumatic operated valves II, 8. return valves I, 9. fast feed pumps, 10. slow feed pumps, 11.
Pneumatic control valve III.
Embodiment
The present invention is described in further detail below by specific embodiment, but these embodiments are only that citing
Illustrate, the scope of the present invention is not defined.
During existing starch wet production, after protein slurry is separated with farinaceous size by main seperator, it is referred to as
Albumen thin pulp, albumen thin pulp turn into albumen underflow by thickener concentration, and traditional method is that albumen underflow enters albumen underflow tank
Afterwards, directly squeezed into after albumen sheet frame is dehydrated, dried, crushing packing by albumen underflow pump, the protein content of albumen powder without
Method adjusts, it is impossible to meets the market demand, influences Business Economic Benefit.
The method of the wet method adjustment albumen powder protein content of the present invention, comprises the following steps：
（1）Detect the butt protein content of protein concentrate slurries：Treat heregulin underflow through passing through albumen in dense seitan mixing tank 1
Underflow contactor pump 5 exports, and albumen on-line quick detection device 6 is near infrared online monitor detection albumen underflow contactor pump 5
Heregulin underflow butt protein content is treated, and passes the data to control terminal；
（2）Regulatory protein content：When heregulin underflow butt protein content is undesirable, control terminal sends instruction,
Open return valve I 8, while open the pneumatic control valve III 11 on seperator 2, return valve I 8 control albumen underflow contactor pump 5 to
The dense reflux entry of seitan mixing tank 1, undesirable albumen underflow is returned into dense seitan mixing tank 1 again and carries out protein content
Allotment, be coarse starch milk in seperator 2, the general conduct of seitan thickener underflow 3 treats that heregulin underflow enters dense seitan batch mixing
Tank 1, because its protein content is higher, controls seperator 2 to be squeezed into dense seitan mixing tank 1 by pneumatic control valve III 11 and roughly form sediment
Powder breast, and the aperture of pneumatic control valve III 11 is adjusted, it is final next to adjust the amount for the coarse starch milk for flowing into dense seitan mixing tank 1
Adjust the protein content of albumen underflow in dense seitan mixing tank 1 and protein content is reduced to suitable albumen and contain
Amount, meets the requirement of production；
（3）Protein content meets the requirements：Work as step（2）When adjusting the butt protein content of dense seitan mixing tank 1 and meeting the requirements, egg
White on-line quick detection device 6 gives the data transfer of monitoring to control terminal, and control terminal sends instruction, opens pneumatic operated valve II 7,
Return valve I 8 is simultaneously closed off, pneumatic operated valve II 8 controls albumen underflow contactor pump 5 to be fed to qualified tank 4, when the albumen of albumen underflow contains
When amount meets the requirements, pneumatic operated valve II 7 is in opening, and qualified protein slurry enters qualified tank 4, subsequently into next work
When sequence protein content is undesirable, pneumatic operated valve II 7 is closed；
（4）Steady production：When workshop steady production, the inlet amount of seperator 2 is relatively stable, now pneumatic control valve III 11
Aperture is in and is relatively fixed state, and pneumatic operated valve II 7 is in open mode, and return valve I 8 is closed；
（5）Production is fluctuated：When fluctuation occurs in workshop, heregulin underflow butt egg is treated in dense seitan mixing tank 1
Fluctuation also occurs in Bai Hanliang, now repeats（1）、（2）（3）Step, until the protein slurry butt egg in dense seitan mixing tank 1
Containing being satisfactory stationary value.
Step（1）—（3）When generally workshop is just started shooting or there is fluctuation-type progress in Workshop Production, and Workshop Production occurs
Big failure or he due to external cause frequently opens together, stop or process index is not all considered as production ripple in desired load range
It is dynamic.Albumen underflow in qualified tank 4 first passes through fast feed pump 9（Flow is big, and pressure is small）Squeeze into sheet frame, make the filter cloth in sheet frame
Quickly form effective filtering layer and carry out fast filtering, until filtering is to a certain degree, then with slow feed pump 10（Slow feed pump pressure
It is high）Charging, while increase feed pressure and stop charging untill sheet frame requirement pressure.Then after suppressing a period of time using air
Release, carry out sheet frame discharging.
The method of the wet method adjustment albumen powder protein content of the present invention, it is simple to operate, conveniently meet what market difference egg contained
The requirement of albumen powder, using on-line monitoring and the Automation Design programme-control protein slurry butt protein content, added by fine setting
Enter coarse starch milk adjust the butt protein content of protein slurry can be in wet method starch production process to required value, this method
Use is widely popularized, is a kind of method of truly feasible replacement albumen powder dry method batch mixing.
Claims (6)
- A kind of 1. method of wet method adjustment albumen powder protein content, it is characterised in that：Comprise the following steps：（1）Detect the butt protein content of protein concentrate slurries：Treat heregulin underflow through passing through albumen in dense seitan mixing tank Underflow contactor pump exports, and treats that heregulin underflow butt albumen contains in albumen on-line quick detection device detection albumen underflow contactor pump Amount, and pass the data to control terminal；（2）Regulatory protein content：When heregulin underflow butt protein content is undesirable, control terminal sends instruction, Return valve I is opened, while opens the pneumatic control valve III on seperator, the inlet amount of heregulin underflow is treated by adjustment to adjust The butt protein content of dense seitan mixing tank；（3）Protein content meets the requirements：Work as step（2）When adjusting the butt protein content of dense seitan mixing tank and meeting the requirements, egg White on-line quick detection device gives the data transfer of monitoring to control terminal, and control terminal sends instruction, opens pneumatic operated valve II, together When closing volume valve I, satisfactory albumen underflow in dense seitan mixing tank is entered qualified tank, subsequently into subsequent processing；（4）Steady production：When workshop steady production, the inlet amount of seperator is relatively stable, now the aperture of pneumatic control valve In the state that is relatively fixed, pneumatic operated valve II is in open mode, and return valve I is closed；（5）Production is fluctuated：When fluctuation occurs in workshop, heregulin underflow butt albumen is treated in dense seitan mixing tank Fluctuation also occurs in content, now repeats（1）、（2）（3）Step, until the protein slurry butt egg in dense seitan mixing tank contains It is satisfactory stationary value.
- 2. the method for wet method adjustment albumen powder protein content according to claim 1, it is characterised in that：The albumen is online Device for fast detecting is near infrared online monitor, and the butt albumen for monitoring albumen underflow in albumen underflow contactor pump in real time contains Amount.
- 3. the method for wet method adjustment albumen powder protein content according to claim 1, it is characterised in that：Step（2）It is described It is coarse starch milk in seperator.
- 4. the method for wet method adjustment albumen powder protein content according to claim 1, it is characterised in that：The return valve I Control albumen underflow contactor pump that undesirable albumen underflow is returned into dense seitan again to dense seitan mixing tank reflux entry Mixing tank carries out the allotment of protein content.
- 5. the method for wet method adjustment albumen powder protein content according to claim 1, it is characterised in that：The pneumatic operated valve II Control albumen underflow contactor pump is fed to qualified tank.
- 6. the method for wet method adjustment albumen powder protein content according to claim 1, it is characterised in that：The pneumatic regulation Valve III controls seperator to squeeze into roughly starch milk to dense seitan mixing tank, and adjusts the aperture of pneumatic control valve III, to adjust stream Enter the amount of the coarse starch milk of dense seitan mixing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710618960.8A CN107439806A (en) | 2017-07-26 | 2017-07-26 | A kind of method of wet method adjustment albumen powder protein content |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710618960.8A CN107439806A (en) | 2017-07-26 | 2017-07-26 | A kind of method of wet method adjustment albumen powder protein content |
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| CN107439806A true CN107439806A (en) | 2017-12-08 |
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| CN201710618960.8A Pending CN107439806A (en) | 2017-07-26 | 2017-07-26 | A kind of method of wet method adjustment albumen powder protein content |
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Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101863988A (en) * | 2010-06-02 | 2010-10-20 | 中粮生化能源(榆树)有限公司 | Method and equipment for improving starch quality and protein yield |
| CN102511658A (en) * | 2011-11-04 | 2012-06-27 | 中粮生物化学（安徽）股份有限公司 | Processing method of sugar slag generated in wet-method sugar preparation, endosperm protein product and wet-method sugar preparation method |
| CN102816249A (en) * | 2012-09-05 | 2012-12-12 | 施韧 | Method and system for washing corn starch by reduced swirler separation |
| CN203448049U (en) * | 2013-08-22 | 2014-02-26 | 山东星光生物科技有限公司 | Corn gluten meal blending system |
| CN105630017A (en) * | 2016-03-10 | 2016-06-01 | 波通瑞华科学仪器(北京)有限公司 | Method and device for automatically controlling content of strong gluten liquid dry-base albumen |
| CN205581668U (en) * | 2016-03-10 | 2016-09-14 | 波通瑞华科学仪器(北京)有限公司 | Automatic control dense seitan liquid and do equipment of basic protein content |
| CN205635435U (en) * | 2016-05-30 | 2016-10-12 | 泊头市华瑞机械制造有限公司 | Energy -saving starch whirl washing device |
| CN106422951A (en) * | 2016-09-23 | 2017-02-22 | 江苏中德电子材料科技有限公司 | Intelligent blending system |
| CN106832009A (en) * | 2017-03-01 | 2017-06-13 | 中粮生化能源（龙江）有限公司 | A kind of method for producing cornstarch in corn wet milling production technology using cellulase preparation |
| CN106905439A (en) * | 2017-04-13 | 2017-06-30 | 潍坊盛泰药业有限公司 | A kind of protein treatment process in Starch Production |
-
2017
- 2017-07-26 CN CN201710618960.8A patent/CN107439806A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101863988A (en) * | 2010-06-02 | 2010-10-20 | 中粮生化能源(榆树)有限公司 | Method and equipment for improving starch quality and protein yield |
| CN102511658A (en) * | 2011-11-04 | 2012-06-27 | 中粮生物化学（安徽）股份有限公司 | Processing method of sugar slag generated in wet-method sugar preparation, endosperm protein product and wet-method sugar preparation method |
| CN102816249A (en) * | 2012-09-05 | 2012-12-12 | 施韧 | Method and system for washing corn starch by reduced swirler separation |
| CN203448049U (en) * | 2013-08-22 | 2014-02-26 | 山东星光生物科技有限公司 | Corn gluten meal blending system |
| CN105630017A (en) * | 2016-03-10 | 2016-06-01 | 波通瑞华科学仪器(北京)有限公司 | Method and device for automatically controlling content of strong gluten liquid dry-base albumen |
| CN205581668U (en) * | 2016-03-10 | 2016-09-14 | 波通瑞华科学仪器(北京)有限公司 | Automatic control dense seitan liquid and do equipment of basic protein content |
| CN205635435U (en) * | 2016-05-30 | 2016-10-12 | 泊头市华瑞机械制造有限公司 | Energy -saving starch whirl washing device |
| CN106422951A (en) * | 2016-09-23 | 2017-02-22 | 江苏中德电子材料科技有限公司 | Intelligent blending system |
| CN106832009A (en) * | 2017-03-01 | 2017-06-13 | 中粮生化能源（龙江）有限公司 | A kind of method for producing cornstarch in corn wet milling production technology using cellulase preparation |
| CN106905439A (en) * | 2017-04-13 | 2017-06-30 | 潍坊盛泰药业有限公司 | A kind of protein treatment process in Starch Production |
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Application publication date: 20171208 |