CN105237646B - The Processes and apparatus of process is soaked during corn deep processing - Google Patents
The Processes and apparatus of process is soaked during corn deep processing Download PDFInfo
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- CN105237646B CN105237646B CN201510779334.8A CN201510779334A CN105237646B CN 105237646 B CN105237646 B CN 105237646B CN 201510779334 A CN201510779334 A CN 201510779334A CN 105237646 B CN105237646 B CN 105237646B
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Abstract
The present invention proposes a kind of Processes and apparatus of immersion process during corn deep processing, wherein main workshop section is steeping tank unit, other auxiliary units include sour tank, heat exchanger, bucket elevator, screw conveyer, conveying water pot, open impeller pump, wet corn buffer-stored tank, flushing water pot, gravity curved screen and degerming mill.Soak tank and 4 collar-shaped liquid distribution pipes are set, be followed successively by from top to bottom：First outlet tube, the second outlet tube, the first inlet tube and the second inlet tube.The larger soak of concentration, adds from below, soaks with the corn contact that will be discharged, is discharged from top, is recycled；The relatively low soak of concentration, therefrom lower section add, and the corn contact moved down, carries out the circulation immersion of long period.Soak is discharged from top, removes corn pulp preparation section.The present invention is only soaked by single tank, and continuous feed discharging, to soak recycled for multiple times, reduces environmental pollution, equipment investment and energy consumption, saves land used space；Whole system automated control, reduces personnel depaly and cost of labor.
Description
Technical field
The invention belongs to corn deep processing field, the immersion process during corn deep processing is related generally to, especially one
The technique of immersion process during kind corn deep processing and its equipment used.
Background technology
Corn is not only grain ration and " king of feed " of people, and essential industry raw material, the industrial products that can be processed into
Up to kind more than 3000.Carry out China's maize industry processing to develop rapidly, the corn of consumption increases considerably, to the jade in China or even the world
Rice balance between supply and demand and circulation layout all generate great influence.Full appreciation and the weight of further investigation maize industry processing development
Act on and its caused influence, formulate the reach of science countermeasure, for actively doing macro adjustments and controls of the grain well, keep corn to supply
Balance is sought, promotes economic heath development in China's to suffer from particularly important meaning.
Corn is the big kind in commodity market all the time, " corn " and with the addition of as main cereal crops
" new identity ", in addition to most basic agricultural planting and the food of primary, feed processing, have also appeared using physics, changes
The technology such as method and Fermentation Engineering carries out corn the processing of depth.Corn deep processing product mainly have cornstarch,
Corn protein powder, converted starch, corn starch sugar, corn oil, edible alcohol, alcohol fuel, glutamic acid, lysine, polylactic acid,
The thousands of kinds such as xylitol, chemical industry alcohol, protein feed, fiber feedstuff, corn deep processing product are widely used in weaving, vapour
The industries such as car, food, medicine, material.Continuous with processing level is deepened, and forms maize economy system.China is the whole world the
Two big maize production states, while be also world's second largest country of consumption, once it was confined to the corn of food and feed for major consumers
Nowadays there is great variety, in addition to the feed consumption of steady-state growth, corn deep processing industry develops rapidly these years.Corn is three
Most suitable as the kind of the raw material of industry, and the highest cereal crops of processing stage in generalized grain crop.Corn producing industry
Feature is that processing space is big, industry chain length, product are extremely abundant, including starch, starch sugar, converted starch, alcohol, enzyme preparation,
The big series of flavouring, medicinal, chemical industry etc. eight, but mainly starch and alcohol, other products are the two product deepers time mostly
Processed goods or production byproduct, these profound processed goods or byproduct its be worth it is at a relatively high i.e. with higher additional
Value, can bring high profit therewith.In conclusion industrial corn consumption belongs to the southern exposure industry in Maize Industry, it is that corn is total
Fastest-rising part in consumption, corn processing have obtained many applications in fields such as food, medicine, chemical industry, are at a high speed
Growth stage, tomorrow requirement promise well.As Chinese maize processing industry degree deepens constantly, product chain constantly expands and extend,
Corn deep processing industry market scale and have a high potential.
Corn deep processing is to optimize the structure of production, lengthening manufacturing chain, increases the specific manifestation of added value of product, and solve
One important measures of rural economy, rural development and rural demography.For example Ethanol can be refined.Alcohol, which is made, with corn solves energy problem.For another example：It is beautiful
The rice plumule dregs of rice, alcohol plumule dregs of rice feed, maize peel whitewashing, maize peel, corn protein powder, wheat bran etc..
The main purpose of corn deep processing production technology is to improve the higher product yield of added value as far as possible, such as albumen,
Starch, plumule etc., reduce the low product yield of added value, such as corn pulp, fiber etc. as far as possible.In order to realize each component in corn
Purifying, it is necessary to by different technique and equipment means, progressively isolate each component.
The purpose of immersion, exactly softens corn kernel, as far as possible leaches soluble matter therein, into corn pulp, together
When cannot make the loss of effective components such as albumen and starch again in corn pulp.After corn kernel softening, it is easy to the wet of subsequent technique
The de- embryo of mill, takes off the high-speed separation of fiber and albumen, and ensure the quality of final starch product.
Earliest soaking technology is direct quiescent processes, i.e., directly mixes soak with corn, when remaining certain
Between and temperature after, bleed off soak, wet corn enters next procedure.The time that this method needs is most long, and immersion effect is worst,
Efficiency is minimum, can not also ensure the yield and quality of product.
Soaking technology commonly used at present is adverse current soaking technology, according to immersion amount and soaking time, design 6-12
Steeping tank, in integrated artistic, realizes quantity-produced purpose.But for single steeping tank, technique is interval.This work
In skill, corn is also static in itself, but soak is counter-current flow.I.e. new soak only add will discharging immersion
Tank, after a certain period of time, soak are pumped to previous steeping tank and reuse.Before previous steeping tank discharging, soak and quilt
It is sent to again previous steeping tank, and so on.This technique significantly reduces the consumption of soak, can ensure product substantially
Yield and quality.Shortcoming is as it was previously stated, power consumption and floor space are larger.
The content of the invention
It is an object of the invention to propose to soak during a kind of corn deep processing the Processes and apparatus of process, the technique category
The continuous technique for soaking corn of single tank in production of corn starch, can be effectively reduced investment and floor space, reduce power consumption and
The steam consumption, saves production cost, problems existing in the prior art can be solved by using the technique and equipment.
In order to reach foregoing invention purpose, the equipment scheme in technical solution of the present invention is：Soaked during corn deep processing
The main workshop section of equipment of bubble process be steeping tank unit, other auxiliary units include acid tank, heat exchanger, bucket elevator, spiral
Formula conveyer, wet corn buffer-stored tank, rinse water pot, gravity curved screen and degerming mill.Wherein soak tank and 4 collar-shapeds are set
Liquid distribution pipe, is followed successively by from top to bottom：First outlet tube, the second outlet tube, the first inlet tube and the second inlet tube, wherein the
Two inlet tubes are positioned at the lower section of immersion tank body, and the first inlet tube is positioned at the middle lower section of immersion tank body.The larger soak of concentration, from
Added below single tank, soak with the corn contact that will be discharged, discharged from top, recycled；The relatively low soak of concentration, from
Lower section adds in single tank, and the corn contact moved down, carries out the circulation immersion of long period.Soak is discharged from top,
Remove corn pulp preparation section.It is specific as follows：
Bucket elevator is connected with screw conveyor, and screw conveyor is connected to the top of steeping tank；
Immersion tank body is from top to bottom disposed with overflow pipe, the first outlet tube, the second outlet tube, the first inlet tube, the
Two inlet tubes；This 4 pipelines of wherein the first outlet tube, the second outlet tube, the first inlet tube, the second inlet tube pass through annular cloth
Acid tube and steeping tank unicom；
Dense sulfurous acid tank is connected with First Heat Exchanger, and dense sulfurous acid is delivered in steeping tank by the second inlet tube；
Dilute sulfurous acid tank is connected with the second heat exchanger, and by the first inlet tube by dilute sulfurous acid be delivered in steeping tank with
Dense sulfurous acid mixing；
Second inlet tube and overflow pipe are connected after converging with dilute sulfurous acid tank；The soak that finishes is acted on from the first inlet tube
Flow out to corn evaporator；
Pot bottom connection wet corn surge tank is soaked, wet corn surge tank is connected with gravity curved screen, and gravity curved screen will separate
The Solid Conveying and Melting gone out to next workshop section degerming mill；Liquid is delivered to bath tank by gravity curved screen, bath tank respectively with wet corn
Surge tank is connected with dense sulfurous acid tank.
Process program in technical solution of the present invention is：
The first step, charging：
A-1. method one：Corn distiller's dried grain is transported to corn from silo, by bucket elevator and screw conveyor and soaks
Tank is steeped, and enters tank body from tank top；
A-2. method two：Corn distiller's dried grain enters conveying water pot, is entered after being mixed with water by open impeller pump from tank deck and soaked
Steep tank；
B. for dense sulfurous acid after First Heat Exchanger, it is from bottom to up, with corn to input to the second inlet tube, liquid flow direction
Grain flow direction forms convection current；
C. dilute sulfurous acid tank is inputted to the first inlet tube, mixed with dense sulfurous acid equally after the second heat exchanger；
Second step, discharging：
A. the wet corn after immersion includes two kinds of forms of solid, liquid from steeping tank bottom discharge, at this time material, and material first passes through
Wet corn surge tank, is then transferred to gravity curved screen and is separated；Solid after separation is sent to the degerming mill of next workshop section,
Liquid after separation after tank of washing by water, go to wet corn surge tank and be used to help conveying wet corn by a part, and another part returns
Dense sulfurous acid tank is returned to be reused；
B. it is located at the steeping tank first half, the sulfurous acid of efficacy wanes is transmitted back to dilute sulfurous acid tank through the second outlet tube, at the same time
Converge from the soak that tank deck overflow goes out by overflow pipe and the second outlet tube, together return to dilute sulfurous acid tank, this partially liq
With dilute sulfurous acid in dilute sulfurous acid tank it is formulated after enter steeping tank from the first inlet tube again；The soak that finishes is acted on from the
One outlet tube is gone out, and is sent into corn slurry evaporator and is carried out other process.In the immersion process of corn, the corn soaking time
For 45 it is small when, temperature control is at 50 DEG C, and for the first tank corn after production target is reached, which can continuous production.
The beneficial effects of the invention are as follows：
Single tank immersion, corn are continuously added to above steeping tank, and lower section is continuously discharged, i.e. continuous feed, continuous discharge；Leaching
Liquid recycled for multiple times is steeped, reduces environmental pollution；Land used space is saved, reduces equipment investment, reduces energy consumption；In immersion
Easily controllable soak concentration, temperature and time, realizes whole system automated control, reduces personnel depaly and cost of labor.
Other features and advantages of the present invention will be illustrated in the following description, also, partly becomes from specification
Obtain it is clear that or being understood by implementing the present invention.The purpose of the present invention and other advantages can be by the explanations write
Specifically noted structure is realized and obtained in book, claims and attached drawing.
Brief description of the drawings
The present invention is described in more detail with reference to the accompanying drawings and examples.In order to illustrate more clearly of of the invention real
The technical solution in a technology is applied, attached drawing needed in the description of embodiment technology will be briefly described, and shown below
And easy insight, drawings in the following description are only some embodiments of the present invention (except prior art diagram), for this area
For those of ordinary skill, in the following detailed description, the above objects, features and advantages of the present invention will be evident；And
And without creative efforts, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is the equipment schematic diagram of immersion process during corn deep processing of the invention
Corresponding component title of the numeral represented by with letter in figure：
1 bucket elevator, 11 second heat exchanger
2 screw conveyor, 12 first inlet tube
3 steeping tank, 13 second inlet tube
4 wet corn surge tank, 14 first outlet tube
5 gravity curved screen, 15 15 second outlet tube
6 degerming mill, 16 overflow pipe
7 bath tank, 17 annular cloth acid tube
8 dilute sulfurous acid tanks 18 convey water pot
9 dense 19 open impeller pumps of sulfurous acid tank
10 First Heat Exchangers
Embodiment
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.Before this it should be noted that this specification
And term used in claims or word are unable to limited interpretation as the implication in common implication or dictionary, and should
It is construed to based on the principle that can be suitably defined to the concept of term to illustrate its invention inventor in the best way
Meet the implication and concept of the technology of the present invention thought.Therewith, the structure represented in the embodiment described in this specification and attached drawing
Simply one of preferred embodiment, can not represent the technological thought of the present invention completely, it will therefore be appreciated that for this
May there are the various equivalents that can be replaced and variation for invention.
For example, some vocabulary has been used to censure specific components among specification and claim.People in the art
Member is, it is to be appreciated that hardware manufacturer may call same component with different nouns.This specification and claims are not
In a manner of the difference of title is used as and distinguishes component, but it is used as the criterion of differentiation with the difference of component functionally.
The "comprising" of specification and claim mentioned in is an open language in the whole text, therefore should be construed to " include but do not limit
In "." substantially " refer in receivable error range, those skilled in the art can be described within a certain error range solution
Technical problem, basically reaches the technique effect.In addition, " coupling " word directly and is indirectly electrically connected comprising any herein
Means.Therefore, if one first device of described in the text is coupled to a second device, representing the first device directly can electrically connect
The second device is connected to, or the second device is electrically connected to indirectly by other devices or connection means.Specification
Subsequent descriptions for implement the present invention better embodiment, so it is described description be by illustrate the present invention rule for the purpose of,
It is not limited to the scope of the present invention.Protection scope of the present invention is when subject to appended claims institute defender.
Below by taking attached drawing as an example, how the equipment and technique that illustrate the present invention operate, as shown in Figure 1, the corn is deep
The equipment of process, including bucket elevator 1, screw conveyor 2, steeping tank 3, wet corn surge tank 4, again are soaked in process
The bent sieve 5 of power, degerming mill 6, bath tank 7, dilute sulfurous acid tank 8, dense sulfurous acid tank 9, First Heat Exchanger 10, the second heat exchanger 11, the
One inlet tube 12, the second inlet tube 13, the first outlet tube 14, the second outlet tube 15, overflow pipe 16, annular cloth acid tube 17, conveying
Water pot 18, open impeller pump 19；
Bucket elevator 1 is connected with screw conveyor 2, and screw conveyor 2 is connected to the top of steeping tank 3；Or conveying
Water pot 18 is connected by open impeller pump 19 with the top of steeping tank 3；
3 body of steeping tank be from top to bottom disposed with overflow pipe 16, the first outlet tube 14, the second outlet tube 15, first into
Liquid pipe 12, the second inlet tube 13, wherein the second inlet tube 13 is located at the lower section of 3 body of steeping tank, the first inlet tube 12 is positioned at immersion
The middle lower section of 3 body of tank；This 4 wherein the first outlet tube 14, the second outlet tube 15, the first inlet tube 12, the second inlet tube 13 pipes
Road passes through annular cloth acid tube 17 and 3 unicom of steeping tank；
Dense sulfurous acid tank 9 is connected with First Heat Exchanger 10, and dense sulfurous acid is delivered to immersion by the second inlet tube 13
In tank 3；
Dilute sulfurous acid tank 8 is connected with the second heat exchanger 11, and dilute sulfurous acid is delivered to immersion by the first inlet tube 12
Mixed in tank 3 with dense sulfurous acid；
Second outlet tube 15 and overflow pipe 16 are connected after converging with dilute sulfurous acid tank 8；The soak that finishes is acted on from first
Outlet tube 14 flows out to corn evaporator；
3 bottom of steeping tank connection wet corn surge tank 4, wet corn surge tank 4 is connected with gravity curved screen 5, and gravity curved screen 5 will
The Solid Conveying and Melting isolated to next workshop section degerming mill 6；Liquid is delivered to bath tank 7 by gravity curved screen 5, and bath tank 7 is distinguished
It is connected with wet corn surge tank 4 and dense sulfurous acid tank 9.
Comprised the following steps that using the technique that process is soaked during the corn deep processing of the said equipment：
The first step, charging：
A-1. method one：Corn distiller's dried grain is transported to corn from silo, by bucket elevator 1 and screw conveyor 2
Steeping tank 3, and enter tank body from tank top；
A-2. method two：Corn distiller's dried grain enter conveying water pot 18, after being mixed with water by open impeller pump 19 from tank deck into
Enter 3 tank body of steeping tank；
B. dense sulfurous acid is after First Heat Exchanger 10, inputs to the second inlet tube 13, liquid flow direction for from bottom to up, with
Niblet flows to form convection current；
C. dilute sulfurous acid tank is inputted to the first inlet tube 12, mixed with dense sulfurous acid equally after the second heat exchanger 11；
Second step, discharging：
A. the wet corn after immersion includes two kinds of forms of solid, liquid from 3 bottom discharge of steeping tank, at this time material, and material first passes through
Wet corn surge tank 4 is crossed, gravity curved screen 5 is then transferred to and is separated；Solid after separation is sent to the de- of next workshop section
Embryo mill 6, the liquid after separation is after tank 7 of washing by water, and a part goes to wet corn surge tank 4 and is used to help conveying wet corn, separately
A part returns to dense sulfurous acid tank 9 and is reused；
B. it is located at 3 first half of steeping tank, the sulfurous acid of efficacy wanes is transmitted back to dilute sulfurous acid tank 8 through the second outlet tube 15,
Converge at the same time from the soak that tank deck overflow goes out by overflow pipe 16 and the second outlet tube 15, together return to dilute sulfurous acid tank 8, this
Enter steeping tank 3 from the first inlet tube 12 again after dilute sulfurous acid is formulated in partially liq and dilute sulfurous acid tank 8；Effect finishes
Soak go out from the first outlet tube 14, be sent into corn slurry evaporator carry out other process.In the immersion process of corn
In, when the corn soaking time is 45 small, temperature control is at 50 DEG C, and the first tank corn is after production target is reached, the system
Continuous production.
Above-described embodiment is soaked only by single tank, continuous feed, continuous discharge, and the multiple circulation profit of soak
With reducing environmental pollution, save land used space, reduce equipment investment and energy consumption；Whole system automated control,
Reduce personnel depaly and cost of labor.
It should be noted that although some preferred embodiments of the present invention have shown and described in described above, but such as preceding institute
State, it should be understood that the present invention is not limited to form disclosed herein, is not to be taken as the exclusion to other embodiment, and can
For various other combinations, modification and environment, and above-mentioned teaching or correlation can be passed through in the scope of the invention is set forth herein
The technology or knowledge in field are modified.And changes and modifications made by those skilled in the art do not depart from the spirit and model of the present invention
Enclose, then all should be in the protection domain of appended claims of the present invention.
Claims (3)
1. the equipment of process is soaked during a kind of corn deep processing, including bucket elevator (1), screw conveyor (2), immersion
Tank (3), wet corn surge tank (4), gravity curved screen (5), degerming mill (6), bath tank (7), dilute sulfurous acid tank (8), dense sulfurous acid
Tank (9), First Heat Exchanger (10), the second heat exchanger (11), the first inlet tube (12), the second inlet tube (13), the first outlet tube
(14), the second outlet tube (15), overflow pipe (16), annular cloth acid tube (17), conveying water pot (18), open impeller pump (19), its
It is characterized in that：
Bucket elevator (1) is connected with screw conveyor (2), and screw conveyor (2) is connected to the top of steeping tank (3)；Or
Conveying water pot (18) is connected via open impeller pump (19) with the top of steeping tank (3)；
Steeping tank (3) body is from top to bottom disposed with overflow pipe (16), the first outlet tube (14), the second outlet tube (15),
One inlet tube (12), the second inlet tube (13), wherein the second inlet tube (13) is located at the lower section of steeping tank (3) body, the first feed liquor
Pipe (12) is located at the middle lower section of steeping tank (3) body；Wherein the first outlet tube (14), the second outlet tube (15), the first inlet tube
(12), this 4 pipelines of the second inlet tube (13) pass through annular cloth acid tube (17) and steeping tank (3) unicom；
Dense sulfurous acid tank (9) is connected with First Heat Exchanger (10), and dense sulfurous acid is delivered to leaching by the second inlet tube (13)
Steep in tank (3)；
Dilute sulfurous acid tank (8) is connected with the second heat exchanger (11), and dilute sulfurous acid is delivered to leaching by the first inlet tube (12)
Mixed in bubble tank (3) with dense sulfurous acid；
Second outlet tube (15) and overflow pipe (16) are connected after converging with dilute sulfurous acid tank (8)；The soak that finishes is acted on from the
One, which goes out inlet tube (14), flows out to corn evaporator；
Steeping tank (3) bottom connection wet corn surge tank (4), wet corn surge tank (4) are connected with gravity curved screen (5), and gravity is bent
(5) are sieved by the degerming mill (6) of the Solid Conveying and Melting isolated to next workshop section；Liquid is delivered to bath tank by gravity curved screen (5)
(7), tank (7) of washing by water is connected with wet corn surge tank (4) and dense sulfurous acid tank (9) respectively.
2. the technique of process is soaked during a kind of corn deep processing, it is characterised in that：The technique is used such as institute in claim 1
The equipment stated, it is comprised the following steps that：
The first step, charging：
A-1. method one：Corn distiller's dried grain is transported to corn from silo, by bucket elevator (1) and screw conveyor (2)
Steeping tank (3), and enter tank body from tank top；
A-2. method two：Corn distiller's dried grain enter conveying water pot (18), after being mixed with water by open impeller pump (19) from tank deck into
Enter steeping tank (3) tank body；
B. dense sulfurous acid is after First Heat Exchanger (10), inputs to the second inlet tube (13), liquid flow direction for from bottom to up, with
Niblet flows to form convection current；
C. dilute sulfurous acid tank is inputted to the first inlet tube (12), mixed with dense sulfurous acid equally after the second heat exchanger (11)；
Second step, discharging：
A. the wet corn after immersion includes two kinds of forms of solid, liquid from steeping tank (3) bottom discharge, at this time material, and material first passes through
Wet corn surge tank (4), is then transferred to gravity curved screen (5) and is separated；Solid after separation is sent to next workshop section
Degerming mill (6), liquid after separation after bath tank (7), a part go to wet corn surge tank (4) be used to help convey it is wet
Corn, another part return to dense sulfurous acid tank (9) and are reused；
B. it is located at steeping tank (3) first half, the sulfurous acid of efficacy wanes is transmitted back to dilute sulfurous acid tank through the second outlet tube (15)
(8), while from the soak that tank deck overflow goes out by overflow pipe (16) and the second outlet tube (15) converge, together return to dilute sulfurous
Enter again from the first inlet tube (12) after dilute sulfurous acid is formulated in sour tank (8), this partially liq and dilute sulfurous acid tank (8) and soak
Steep tank (3)；Act on the soak finished to go out from the first outlet tube (14), be sent into corn slurry evaporator and carry out at other techniques
Reason.
3. the technique of process is soaked during corn deep processing according to claim 2, it is characterised in that：In the leaching of corn
During bubble, when the corn soaking time is 45 small, temperature control is at 50 DEG C, and after production target is reached, this is the first tank corn
System can continuous production.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510779334.8A CN105237646B (en) | 2015-11-16 | 2015-11-16 | The Processes and apparatus of process is soaked during corn deep processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510779334.8A CN105237646B (en) | 2015-11-16 | 2015-11-16 | The Processes and apparatus of process is soaked during corn deep processing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105237646A CN105237646A (en) | 2016-01-13 |
| CN105237646B true CN105237646B (en) | 2018-04-13 |
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ID=55035508
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510779334.8A Expired - Fee Related CN105237646B (en) | 2015-11-16 | 2015-11-16 | The Processes and apparatus of process is soaked during corn deep processing |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1238725A (en) * | 1969-03-10 | 1971-07-07 | ||
| SU1659423A1 (en) * | 1988-09-19 | 1991-06-30 | Институт Автоматики Ан Киргсср | Apparatus for steeping grain in starch manufacture |
| CN202450015U (en) * | 2011-10-31 | 2012-09-26 | 山东西王生化科技有限公司 | Soaking tank used in production process of corn starch |
| CN203187611U (en) * | 2013-01-28 | 2013-09-11 | 山东省鲁洲食品集团有限公司 | Corn countercurrent continuous soaking device |
| CN103992410A (en) * | 2014-05-15 | 2014-08-20 | 菱花集团有限公司 | Method and device for soaking corn by utilizing desulfurization water from power plant in starch production process |
| CN204138576U (en) * | 2014-09-07 | 2015-02-04 | 山东祥瑞药业有限公司 | A kind of adverse current corn successive soaking tank |
| CN104672336A (en) * | 2015-02-06 | 2015-06-03 | 山东祥瑞药业有限公司 | Corn starch production process |
-
2015
- 2015-11-16 CN CN201510779334.8A patent/CN105237646B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1238725A (en) * | 1969-03-10 | 1971-07-07 | ||
| SU1659423A1 (en) * | 1988-09-19 | 1991-06-30 | Институт Автоматики Ан Киргсср | Apparatus for steeping grain in starch manufacture |
| CN202450015U (en) * | 2011-10-31 | 2012-09-26 | 山东西王生化科技有限公司 | Soaking tank used in production process of corn starch |
| CN203187611U (en) * | 2013-01-28 | 2013-09-11 | 山东省鲁洲食品集团有限公司 | Corn countercurrent continuous soaking device |
| CN103992410A (en) * | 2014-05-15 | 2014-08-20 | 菱花集团有限公司 | Method and device for soaking corn by utilizing desulfurization water from power plant in starch production process |
| CN204138576U (en) * | 2014-09-07 | 2015-02-04 | 山东祥瑞药业有限公司 | A kind of adverse current corn successive soaking tank |
| CN104672336A (en) * | 2015-02-06 | 2015-06-03 | 山东祥瑞药业有限公司 | Corn starch production process |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105237646A (en) | 2016-01-13 |
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