CN102994569B - 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
- CN102994569B CN102994569B CN201210551106.1A CN201210551106A CN102994569B CN 102994569 B CN102994569 B CN 102994569B CN 201210551106 A CN201210551106 A CN 201210551106A CN 102994569 B CN102994569 B CN 102994569B
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- Prior art keywords
- tank
- starch
- valve
- underflow
- slurry
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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 12
- 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
- 239000008399 tap water Substances 0.000 claims abstract description 4
- 235000020679 tap water Nutrition 0.000 claims abstract description 4
- 239000000843 powder Substances 0.000 claims description 19
- 238000000465 moulding Methods 0.000 claims description 13
- 238000004513 sizing Methods 0.000 claims description 7
- 239000006227 byproduct Substances 0.000 claims 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
- 238000011010 flushing procedure Methods 0.000 description 2
- 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
- 238000005728 strengthening Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (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 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 in wet gluten containing some starch, in order to improve gluten powder quality, must starch washing wherein out, by spray high-pressure wash water in moulding sieve, enter underflow tank with the washing water of starch.
Shortcoming: owing to strengthening or minimizing 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 underflow tank, and then cause starch slurry change in concentration in underflow tank, after alcohol-fueled car indirect fermentation, ripe mash wine part height is inhomogeneous, impact is normal produces, and wine part is sometimes too low, causes alcohol distillation to waste a large amount of steam, 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 equipment in above-mentioned method.
Gluten powder of the present invention is adjusted powder slurry concentration method in producing is to solve above technical problem by following technical scheme:
Gluten powder is adjusted a method for powder slurry concentration in producing, comprise following step:
Material containing 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, point two branch roads, and one leads to middle water pot, and other one leads to underflow tank, and starch fluid is by its outlet of valve control; In the time that in underflow tank, starch slurry concentration is low, valve-off II, opens valve I, allows starch fluid enter middle water pot, and when in underflow tank when starch slurry excessive concentration, valve-off I, opens valve II, allows starch fluid enter 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 underflow tank by underflow pump pump to thinning workshop.
In above-mentioned method, special 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 to thinning workshop by product pump; This equipment also comprises moulding sieve, and 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 underflow tank, and the water in outlet conduit both can lead to middle water pot, also can lead to underflow tank; In the time that in underflow tank, starch slurry concentration is low, valve-off II, opens valve I, allows starch fluid enter middle water pot, and when in underflow tank when starch slurry excessive concentration, valve-off I, opens valve II, allows starch fluid enter underflow tank.
In the production of gluten powder, in wet gluten, contain some starch, in order to improve gluten powder quality, must be starch washing wherein out, by spray high-pressure wash water in moulding sieve, outlet conduit with the washing water of starch through overmolding sieve place, lead to respectively middle water pot and underflow tank, starch fluid is by different its outlets of valve control, thereby reaches the object that the material concentration in underflow tank is adjusted, make the material in 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 adjusting powder slurry concentration adjustment in gluten powder production, and the material in 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 is also convenient in convenient operation and control.
Brief description of the 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
Material containing wet gluten, starch etc. rinses through tap water at moulding sieve place, and the outlet conduit that the starch fluid after flushing sieves 5 places through overmolding flows out, point two branch roads, and one leads to middle water pot 2, and other one leads to underflow tank 3, and starch fluid is by its outlet of valve control; In the time that the interior starch slurry concentration of underflow tank 3 is low, valve-off II 7, opens valve I 6, allows starch fluid enter middle water pot 2, and in the time of the interior starch slurry excessive concentration of underflow tank 3, valve-off I 6, opens valve II 7, allows starch fluid enter 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 thinning workshop.
Embodiment 2
In the method for embodiment 1, special 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 to thinning workshop by product pump; 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; In the time that the interior starch slurry concentration of underflow tank 3 is low, valve-off II 7, opens valve I 6, allows starch fluid enter middle water pot 2, and in the time of the interior starch slurry excessive concentration of underflow tank 3, valve-off I 6, opens valve II 7, allows starch fluid enter underflow tank 3.
In Fig. 1, be not improve previous its structural representation of equipment, in this figure, can not control the concentration of starch fluid, in underflow tank, starch slurry concentration is at 8-10 degree Beaume, and fermentation after ripening raw spirit part only has 5-6%(vol) left and right, ton approximately 5.3 tons of steam for alcohol;
After improvement: in underflow tank, starch slurry concentration only has 16-17 degree Beaume, fermentation after ripening raw spirit part is at 10.5-11.5%(vol) left and right, ton approximately 4.0 tons of steam for alcohol;
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. gluten powder is adjusted a method for powder slurry concentration in producing, and comprises following step:
Material containing wet gluten rinses through tap water at moulding sieve place, and starch is wherein 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 underflow tank, and starch fluid is by its outlet of valve control; In the time that in underflow tank, starch slurry concentration is low, valve-off II, opens valve I, allows starch fluid enter middle water pot, and when in underflow tank when starch slurry excessive concentration, valve-off I, opens valve II, allows starch fluid enter 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 underflow tank by underflow pump pump to thinning workshop.
2. a kind of gluten powder as claimed in claim 1 is adjusted equipment special in the method for powder slurry concentration in producing, and 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 to thinning workshop by product pump; Described equipment also comprises 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 underflow tank, water in outlet conduit both can lead to middle water pot, also can lead to underflow tank; In the time that in underflow tank, starch slurry concentration is low, valve-off II, opens valve I, allows starch fluid enter middle water pot, and when in underflow tank when starch slurry excessive concentration, valve-off I, opens valve II, allows starch fluid enter 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 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102994569A CN102994569A (en) | 2013-03-27 |
| CN102994569B true CN102994569B (en) | 2014-12-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201210551106.1A Active CN102994569B (en) | 2013-01-17 | 2013-01-17 | Method for adjusting concentration of slurry in vital gluten production |
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Families Citing this family (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 |
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| Publication number | Publication date |
|---|---|
| CN102994569A (en) | 2013-03-27 |
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| 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 |