CN102994569A - Method for adjusting concentration of slurry in vital gluten production - Google Patents
Method for adjusting concentration of slurry in vital gluten production Download PDFInfo
- Publication number
- CN102994569A CN102994569A CN2012105511061A CN201210551106A CN102994569A CN 102994569 A CN102994569 A CN 102994569A CN 2012105511061 A CN2012105511061 A CN 2012105511061A CN 201210551106 A CN201210551106 A CN 201210551106A CN 102994569 A CN102994569 A CN 102994569A
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- Prior art keywords
- tank
- valve
- starch
- underflow
- slurry
- Prior art date
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- 239000002002 slurry Substances 0.000 title claims abstract description 37
- 108010068370 Glutens Proteins 0.000 title claims abstract description 22
- 235000021312 gluten Nutrition 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title abstract description 13
- 229920002472 Starch Polymers 0.000 claims abstract description 60
- 235000019698 starch Nutrition 0.000 claims abstract description 60
- 239000008107 starch Substances 0.000 claims abstract description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000012530 fluid Substances 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 8
- 239000000843 powder Substances 0.000 claims description 19
- 238000000465 moulding Methods 0.000 claims description 13
- 238000004513 sizing Methods 0.000 claims description 7
- 238000011010 flushing procedure Methods 0.000 claims description 3
- 239000008399 tap water Substances 0.000 abstract description 3
- 235000020679 tap water Nutrition 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract 6
- 241000209140 Triticum Species 0.000 abstract 1
- 235000021307 Triticum Nutrition 0.000 abstract 1
- 235000013312 flour Nutrition 0.000 abstract 1
- 101100298225 Caenorhabditis elegans pot-2 gene Proteins 0.000 description 7
- 238000005406 washing Methods 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000005070 ripening Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The invention belongs to the field of wheat flour processing, and specifically relates to a method for adjusting the concentration of slurry in vital gluten production. The method comprises the following steps: materials containing wet glutens and starches and the like are rinsed at a forming sieve by using tap water; after the rinsing is completed, starch liquid flows out through a water outlet pipe at the forming sieve and is divided into two paths, one path flows to a reclaimed water tank, the other path flows to a thickened slurry tank, and the paths of the starch liquid is controlled by valves; when the concentration of starch slurry in the thickened slurry tank is low, a valve II is closed, and a valve I is opened, so that the starch liquid enters the reclaimed water tank, and when the concentration of starch slurry in the thickened slurry tank is too high, the valve I is closed, and the valve II is opened, so that the starch liquid enters the thickened slurry tank; the starch liquid entering the reclaimed water tank enters a slurry mixing tank again and then conveyed for reusing; and the starch liquid entering the thickened slurry tank is pumped to a fluid saccharification workshop by using a thickened slurry pump. The concentration of slurry in vital gluten production is adjusted by using the method disclosed by the invention, so that the concentration of materials in the thickened slurry tank is kept in a certain concentration range, thereby facilitating the later production.
Description
?
Technical field
The invention belongs to the wheat-flour manufacture field, be specifically related to adjust in a kind of gluten powder production the method for powder slurry concentration.
Background technology
The original technical process of glutelin washing system: because contain some starch in wet gluten, in order to improve the gluten powder quality, must be wherein starch washing out, by spray high-pressure wash water in the moulding sieve, enter the underflow tank with the washing water of starch.
Shortcoming: owing to need to strengthen or reduce leaching requirement according to the situation of gluten washing, cause mixing starch slurry change in concentration larger, again because moulding sieve spray high-pressure wash water whereabouts only enters the underflow tank, and then cause starch slurry change in concentration in the underflow tank, after the alcohol-fueled car indirect fermentation, ripe mash wine part height is inhomogeneous, impact is normal produces, and wine part is sometimes too low, causes a large amount of steam of alcohol distillation waste, and production cost increases.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of adjust powder slurry concentration in gluten powder production method.
The present invention also provides special-purpose equipment in above-mentioned method.
The method of adjusting powder slurry concentration in gluten powder production of the present invention is to solve above technical problem by following technical scheme:
Adjust the method for powder slurry concentration during a kind of gluten powder is produced, comprise following step:
The material that contains wet gluten, starch etc. rinses through tap water at moulding sieve place, and the starch fluid after flushing flows out through the outlet conduit at overmolding sieve place, minute two branch roads, and one leads to middle water pot, and other one leads to the underflow tank, and starch fluid is controlled its outlet by valve; When starch slurry concentration in the underflow tank was low, the valve-off II was opened the valve I, allows starch fluid advance middle water pot, and when in the underflow tank during starch slurry excessive concentration, the valve-off I is opened the valve II, allows starch fluid advance the underflow tank; Entering starch fluid in water pot enters the tank of sizing mixing again and is transmitted back to use; Enter starch fluid in the underflow tank by the underflow pump pump to the thinning workshop.
In above-mentioned method, special-purpose equipment comprises the tank of sizing mixing, middle water pot, the underflow tank of series connection successively; The outlet of underflow tank is connected with the underflow pump of product pump to the thinning workshop; This equipment also comprises the moulding sieve, and the moulding sieve is connected with outlet conduit, and described outlet conduit divides two branch roads, and one is connected with middle water pot, and another is connected with the underflow tank, and the water in outlet conduit both can lead to middle water pot, also can lead to the underflow tank; When starch slurry concentration in the underflow tank was low, the valve-off II was opened the valve I, allows starch fluid advance middle water pot, and when in the underflow tank during starch slurry excessive concentration, the valve-off I is opened the valve II, allows starch fluid advance the underflow tank.
In the production of gluten powder, contain some starch in wet gluten, in order to improve the gluten powder quality, must be wherein starch washing out, by spray high-pressure wash water in the moulding sieve, with the washing water of the starch outlet conduit through overmolding sieve place, lead to respectively middle water pot and underflow tank, starch fluid is controlled its outlet by different valves, thereby reaches the purpose that the material concentration in the underflow tank is adjusted, make the material in the underflow tank remain on certain concentration, make it but in carrying out follow-up production.
Beneficial effect of the present invention is, has adopted above method to adjust adjusting powder slurry concentration in gluten powder production, and the material in the underflow tank is remained in certain concentration range, is convenient to carry out follow-up production.Equipment of the present invention is simple, and large-scale industrial production also is convenient in convenient operation and control.
Description of drawings
Fig. 1 is the structural representation of traditional equipment;
Fig. 2 is the structural representation after equipment improvement of the present invention;
In figure, the 1-tank of sizing mixing, water pot in 2-, 3-underflow tank, 4-underflow pump, 5-moulding sieve, 6-valve I, 7-valve II.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is further described, so that those skilled in the art more understands the present invention, but does not limit the present invention with this.
Embodiment 1
The material that contains wet gluten, starch etc. rinses through tap water at moulding sieve place, and the starch fluid after flushing flows out through the outlet conduit at overmolding sieve 5 places, minute two branch roads, and one leads to middle water pot 2, and other one leads to underflow tank 3, and starch fluid is controlled its outlet by valve; When the interior starch slurry concentration of underflow tank 3 was low, valve-off II 7 was opened valve I 6, allows starch fluid advance middle water pot 2, and when the interior starch slurry excessive concentration of underflow tank 3, valve-off I 6 is opened valve II 7, allows starch fluid advance underflow tank 3; Entering starch fluid in water pot 2 enters the tank 1 of sizing mixing again and is transmitted back to use; Enter starch fluid in underflow tank 3 by underflow pump 4 pumps to the thinning workshop.
Embodiment 2
In the method for embodiment 1, special-purpose equipment comprises the tank 1 of sizing mixing, middle water pot 2, the underflow tank 3 of series connection successively; The outlet of described underflow tank 3 is connected with the underflow pump of product pump to the thinning workshop; This equipment also comprises moulding sieve 5, and moulding sieve 5 is connected with outlet conduit, and outlet conduit divides two branch roads, and one is connected with middle water pot 2, and another is connected with underflow tank 3, and the water in outlet conduit both can lead to middle water pot 2, also can lead to underflow tank 3; When the interior starch slurry concentration of underflow tank 3 was low, valve-off II 7 was opened valve I 6, allows starch fluid advance middle water pot 2, and when the interior starch slurry excessive concentration of underflow tank 3, valve-off I 6 is opened valve II 7, allows starch fluid advance underflow tank 3.
Be its structural representation of equipment before not improving in Fig. 1, can not control the concentration of starch fluid in this figure, in the underflow tank, starch slurry concentration is at the 8-10 degree Beaume, and fermentation after ripening raw spirit part only has 5-6%(vol) left and right, ton alcohol is with approximately 5.3 tons of steam;
After improvement: starch slurry concentration only has the 16-17 degree Beaume in the underflow tank, and fermentation after ripening raw spirit part is at 10.5-11.5%(vol) left and right, ton alcohol is with approximately 4.0 tons of steam;
Approximately 1.3 tons of ton alcohol steam savings are worth approximately 210 yuan, and therefore from cost, equipment of the present invention and method have reduced cost greatly.
Claims (2)
1. adjust the method for powder slurry concentration during a gluten powder is produced, comprise following step:
The material that contains wet gluten is washed flushing at moulding sieve place through from the beginning, wherein starch is washed out, and after rinsing, amyloid starch fluid flows out through the outlet conduit at overmolding sieve place, divide two branch roads, article one, lead to middle water pot, other one leads to the underflow tank, and starch fluid is controlled its outlet by valve; When starch slurry concentration in the underflow tank was low, the valve-off II was opened the valve I, allows starch fluid advance middle water pot, and when in the underflow tank during starch slurry excessive concentration, the valve-off I is opened the valve II, allows starch fluid advance the underflow tank; Entering starch fluid in water pot enters the tank of sizing mixing again and is transmitted back to use; Enter starch fluid in the underflow tank by the underflow pump pump to the thinning workshop.
2. special-purpose equipment in the method for adjustment powder slurry concentration during a kind of gluten powder as claimed in claim 1 is produced, described equipment comprises the tank of sizing mixing, middle water pot, the underflow tank of series connection successively; The outlet of described underflow tank is connected with the underflow pump of product pump to the thinning workshop; Described equipment also comprises the moulding sieve, it is characterized in that, described moulding sieve is connected with outlet conduit, described outlet conduit divides two branch roads, and one is connected with middle water pot, and another is connected with the underflow tank, water in outlet conduit both can lead to middle water pot, also can lead to the underflow tank; When starch slurry concentration in the underflow tank was low, the valve-off II was opened the valve I, allows starch fluid advance middle water pot, and when in the underflow tank during starch slurry excessive concentration, the valve-off I is opened the valve II, allows starch fluid advance the underflow tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210551106.1A CN102994569B (en) | 2013-01-17 | 2013-01-17 | Method for adjusting concentration of slurry in vital gluten production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210551106.1A CN102994569B (en) | 2013-01-17 | 2013-01-17 | Method for adjusting concentration of slurry in vital gluten production |
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| Publication Number | Publication Date |
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| CN102994569A true CN102994569A (en) | 2013-03-27 |
| CN102994569B CN102994569B (en) | 2014-12-10 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105981914A (en) * | 2015-02-09 | 2016-10-05 | 许兆明 | Production method and production device for vital wheat gluten and starch slurry of wheat |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101003781A (en) * | 2007-01-05 | 2007-07-25 | 天津商学院 | Light bioreactor |
| CN101850219A (en) * | 2010-04-29 | 2010-10-06 | 哈尔滨工程大学 | Continuous flow self-adjusting dosing device |
| CN202087091U (en) * | 2011-06-02 | 2011-12-28 | 黑龙江北大荒斯达奇生物科技有限公司 | Modified starch recycling equipment |
| CN202543117U (en) * | 2012-05-13 | 2012-11-21 | 黑龙江北大荒斯达奇生物科技有限公司 | Residual starch recovery plant in process of skimming liquid by using scraper |
-
2013
- 2013-01-17 CN CN201210551106.1A patent/CN102994569B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101003781A (en) * | 2007-01-05 | 2007-07-25 | 天津商学院 | Light bioreactor |
| CN101850219A (en) * | 2010-04-29 | 2010-10-06 | 哈尔滨工程大学 | Continuous flow self-adjusting dosing device |
| CN202087091U (en) * | 2011-06-02 | 2011-12-28 | 黑龙江北大荒斯达奇生物科技有限公司 | Modified starch recycling equipment |
| CN202543117U (en) * | 2012-05-13 | 2012-11-21 | 黑龙江北大荒斯达奇生物科技有限公司 | Residual starch recovery plant in process of skimming liquid by using scraper |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105981914A (en) * | 2015-02-09 | 2016-10-05 | 许兆明 | Production method and production device for vital wheat gluten and starch slurry of wheat |
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| CN102994569B (en) | 2014-12-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: BINZHOU ZHONGYU FOOD CO., LTD. Free format text: FORMER OWNER: BINZHOU TAIYU WHEAT INDUSTRY CO., LTD. Effective date: 20140923 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20140923 Address after: 256651, No. five, No. 91, Indus Road, Binzhou Industrial Park, Shandong, Binzhou, China Applicant after: BINZHOU ZHONGYU FOOD Co.,Ltd. Address before: 256651, No. two, No. 68, Phoenix Road, foreshore, Binzhou, Shandong, Beizhen Applicant before: BINZHOU TAIYU WHEAT CO.,LTD. |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Method of adjusting slurry concentration in Wheat Gluten Production Effective date of registration: 20211118 Granted publication date: 20141210 Pledgee: Binzhou Bincheng Branch of China Construction Bank Co.,Ltd. Pledgor: BINZHOU ZHONGYU FOOD Co.,Ltd. Registration number: Y2021370000141 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230117 Granted publication date: 20141210 Pledgee: Binzhou Bincheng Branch of China Construction Bank Co.,Ltd. Pledgor: BINZHOU ZHONGYU FOOD Co.,Ltd. Registration number: Y2021370000141 |