CN105192243A - Flour deep processing method and gluten washing machine used in method - Google Patents
Flour deep processing method and gluten washing machine used in method Download PDFInfo
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- CN105192243A CN105192243A CN201510701969.6A CN201510701969A CN105192243A CN 105192243 A CN105192243 A CN 105192243A CN 201510701969 A CN201510701969 A CN 201510701969A CN 105192243 A CN105192243 A CN 105192243A
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Abstract
The invention provides a flour deep processing method. According to the method, flour and water are firstly mixed and kneaded to obtain dough; then, the dough is washed to obtain gluten dough and a paste liquid. The gluten dough is dehydrated and dried to obtain wheat gluten. The paste liquid undergoes centrifugal separation to obtain a paste liquid A and a paste liquid B. The paste liquid A is dehydrated and dried to obtain starch A. The paste liquid B is further processed to obtain alcohol. In comparison with the prior art, the flour processing method provided by the invention can be adopted to simultaneously produce wheat gluten, the starch A and alcohol. The three products have high market price and are in great demand. Under the condition of equal quantity of raw materials, yield and economic benefit are maximized.
Description
Technical field
The present invention relates to food field of deep, specifically a kind of flour deep working method.
Background technology
Wheat is the one of China staple crops, and its output is large, be of high nutritive value, the crowd in suitable all ages and classes stage.
Along with industrial expansion, wheat is not only ground into powder and makes steamed bun steamed stuffed bun.More wheat has the food of Different Nutrition value and purposes by producing, the most common is exactly starch, Gluten.Then, in wheat processing process, by loaded down with trivial details workshop section, the higher starch of quality and Gluten just can be obtained.Loaded down with trivial details workshop section comprises with face, washes one's face, dewaters, dry etc., water consumption is large, also can take away partial starch, and these water has certain temperature mostly, directly discharges, both wasted, cause environmental pollution while dehydration.
Summary of the invention
The object of the invention is, in order to solve in prior art flour processing not thoroughly, waste serious, with serious pollution defect, to provide a kind of flour deep working method to solve the problems referred to above.
The present invention is achieved through the following technical solutions above-mentioned technical purpose:
A kind of flour deep working method, comprises the following steps:
A. and face: after flour mixes with water, be kneaded into dough, wherein face water is than being 1:0.7, and water is heated to 25 DEG C ~ 30 DEG C;
B. slaking: by dough leave standstill 15 ~ 25 minutes, allow dough nature slaking;
C. wash one's face: add water dough upset stirring, repeatedly clean and obtain clear dough and powder slurries for 4 ~ 6 times;
D. dehydrate: first extracted in step c by the moisture content in clear dough with dewaterer, then clear dough is utilized in drying machine 130 ~ 150 DEG C of vapour removal moisture content, drying machine tail gas temperature DEG C controls at 48 DEG C ~ 63 DEG C, Gluten moisture content≤9% obtained after drying;
E. the powder slurries in step c are first crossed 250 mesh sieves and remove impurity, then go out A starch slurry and B starch slurry with horizontal screw centrifuge centrifugation;
F. the A starch slurry in step e is sent into drying tower after horizontal screw centrifuge dehydration to dry; Dry flash temperature controls at about 120 DEG C, and baking temperature controls at about 160 DEG C, forms A starch, A starch moisture content≤10% after drying;
G. will add cassava in the B starch slurry in step e and mix thoroughly and form thick slurries; In thick slurries, add α-amylase and heat and make boiling wine with dregs; In boiling wine with dregs, add carbohydrase make converted mash; Converted mash to be sent in fermentation tank and add yeast and carry out fermentation and make ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, obtains alcohol.
Further, in step g, the input amount of cassava is 50% of B starch slurry weight; α-amylase is AMS, and reacts by the proportioning that thick slurries per ton drop into 0.23kg AMS; The course of reaction of thick slurries and AMS heats through three grades: one-level is heated to 50 DEG C, secondary is heated to 80-85 DEG C, three grades and is heated to 105 DEG C; Finally the compound of thick slurries and AMS is dropped in heat insulation tank and be incubated two hours and keep temperature DEG C to be 100 DEG C, finally formation boiling wine with dregs; Saccharifying tank is entered after boiling wine with dregs is cooled to 60 DEG C, and be carbohydrase and its reaction that boiling wine with dregs per ton drops into 1.4kg according to weight ratio, under the temperature remains within the normal range normal pressure, reaction is made converted mash after 60 hours and is entered in fermentation tank, and is yeast and the brew fermentation that converted mash per ton drops into 0.4kg according to mass ratio; When temperature is 30 DEG C, yeast and converted mash ferment 8 hours in fermentation tank, obtain ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, finally obtains the alcohol that concentration is 10v/v.
Preferably, in steps d, clear dough is back to through the dilute slurry that dewaterer is deviate from and washes one's face in workshop section.
Preferably, in step f, A starch slurry produces dilute slurry after horizontal screw centrifuge dehydration; Dilute slurry is back to face and washes one's face in workshop section.
Further, a kind of for washing muscle machine in flour deep working method, comprise casing; Described bottom half is longitudinally provided with a bridge of the nose; Screw feeder is equipped with respectively in described bridge of the nose both sides; The rotation screw feeder face of described screw feeder and the bridge of the nose and cabinet wall are tangent line matched in clearance; Described casing is provided with hole, is provided with bearing in described hole; The axle of described screw feeder drives rotation through described bearing by the power assembly be positioned at outside casing and transmission assembly; Described bearing outer wall is provided with the convex rafter of some circles; Described hole wall is provided with the groove coincide with described convex rafter; The rotation screw feeder face of described screw feeder is provided with several and stirs pawl.
Preferably, described nose depth of beam is lower than the height of described screw feeder; The top of the described bridge of the nose is linear structure.
Preferably, described two screw feeders drive locking phase to rotation by a set of power assembly and transmission assembly.
Preferably, described bearing outer wall is provided with the convex rafter of 2 circle; Seal is provided with between described convex rafter and groove.
Compared with prior art, there is following advantage in the present invention:
By flour processing method provided by the invention, can make Gluten, A starch and alcohol, these three kinds of product market prices are high simultaneously, and demand is large, in the raw-material situation of equivalent, makes output and maximization of economic benefit.And the dilute slurry of discharging in each workshop section is back to part workshop section, the energy-saving and emission-reduction really done.
Provided by the inventionly wash muscle machine, by the convex rafter structure arranged between bearing and box body wall, even if vibrate for a long time, between bearing and box body wall, relative displacement can not be there is, therebetween gap can not increase, and lenticular occlusion structure can be good at stoping slurries to leak outside; Tangent line matched in clearance between two screw feeders and the bridge of the nose and box body wall, well cuts off dough, to avoid dough and glues the situation that axle turns and occur; In screw feeder rotation process, screw feeder rotates stirring pawl that imperial face is arranged can fast broken face group, dough is contacted very well with water, washs more thorough; The bridge of the nose top of linear structure, is convenient to the same dough that cutting two screw feeders are pullled; The bridge of the nose lower than screw feeder height is arranged, and the slurries being convenient to both sides screw feeder stirring flow mutually, even texture.
Accompanying drawing explanation
Fig. 1 is the flow chart of flour deep working method of the present invention;
Fig. 2 is a kind of overall structure schematic diagram washing muscle machine of the present invention;
Fig. 3 is the syndeton schematic diagram in Fig. 2 shaft and hole;
Fig. 4 is the axial section of Fig. 2.
Detailed description of the invention
For making to have a better understanding and awareness architectural feature of the present invention and effect of reaching, coordinating detailed description in order to preferred embodiment and accompanying drawing, being described as follows:
As described in Figure 1, a kind of flour deep working method, comprises the following steps:
A. and face: after flour mixes with water, be kneaded into dough, wherein face water is than being 1:0.7, and water is heated to 25 DEG C ~ 30 DEG C;
B. slaking: by dough leave standstill 15 ~ 25 minutes, allow dough nature slaking;
C. wash one's face: add water dough upset stirring, repeatedly clean and obtain clear dough and powder slurries for 4 ~ 6 times;
D. dehydrate: first extracted in step c by the moisture content in clear dough with dewaterer, then clear dough is utilized in drying machine 130 ~ 150 DEG C of vapour removal moisture content, drying machine tail gas temperature DEG C controls at 48 DEG C ~ 63 DEG C, Gluten moisture content≤9% obtained after drying;
E. the powder slurries in step c are first crossed 250 mesh sieves and remove impurity, then go out A starch slurry and B starch slurry with horizontal screw centrifuge centrifugation;
F. the A starch slurry in step e is sent into drying tower after horizontal screw centrifuge dehydration to dry; Dry flash temperature controls at about 120 DEG C, and baking temperature controls at about 160 DEG C, forms A starch, A starch moisture content≤10% after drying;
G. will add cassava in the B starch slurry in step e and mix thoroughly and form thick slurries; In thick slurries, add α-amylase and heat and make boiling wine with dregs; In boiling wine with dregs, add carbohydrase make converted mash; Converted mash to be sent in fermentation tank and add yeast and carry out fermentation and make ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, obtains alcohol.
Wherein, in step g, the input amount of cassava is 50% of B starch slurry weight; α-amylase is AMS, and reacts by the proportioning that thick slurries per ton drop into 0.23kg AMS; The course of reaction of thick slurries and AMS heats through three grades: one-level is heated to 50 DEG C, secondary is heated to 80-85 DEG C, three grades and is heated to 105 DEG C; Finally the compound of thick slurries and AMS is dropped in heat insulation tank and be incubated two hours and keep temperature DEG C to be 100 DEG C, finally formation boiling wine with dregs; Saccharifying tank is entered after boiling wine with dregs is cooled to 60 DEG C, and be carbohydrase and its reaction that boiling wine with dregs per ton drops into 1.4kg according to weight ratio, under the temperature remains within the normal range normal pressure, reaction is made converted mash after 60 hours and is entered in fermentation tank, and is yeast and the brew fermentation that converted mash per ton drops into 0.4kg according to mass ratio; When temperature is 30 DEG C, yeast and converted mash ferment 8 hours in fermentation tank, obtain ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, finally obtains the alcohol that concentration is 10v/v.
In steps d, clear dough is back in gluten washing room through the dilute slurry that dewaterer is deviate from.
In step f, A starch slurry produces dilute slurry after horizontal screw centrifuge dehydration; Dilute slurry is back to in face and gluten washing room.
In specific works, pneumatic convey equipment is utilized to carry out reception process from the flour between flour lorry.Flour after metering through elevator deliver to dough mixing machine mix with water rub after form dough, wherein face water compares is 1:0.7, and water is heated to 25 DEG C ~ 30 DEG C.The dough of becoming reconciled enters homogeneous slaking in homogenizer subsequently, about 15 ~ 25 minutes curing times, and the wheat gluten water suction after slaking in powder cure into wheat gluten.
Dough after homogeneous slaking is delivered to and to be washed in muscle machine water filling stirring and washing 4 ~ 6 times repeatedly, obtains clear dough and powder slurries.Clear dough is through being processed into Gluten, and powder serum portion is used for processing the A starch made, the obtained alcohol of another part processing.
Clear dough is moisture higher, and inserted dewaterer dehydration, then insert in drying machine and utilize 130 ~ 150 DEG C of vapour removal moisture content, drying machine tail gas temperature DEG C controls at 48 DEG C ~ 63 DEG C, Gluten moisture content≤9% obtained after drying.The water that clear dough is deviate from still also has part gluten, can be back in gluten washing room, to improve the economic worth of flour, important is using water wisely, energy-saving and emission-reducing, is applicable to the demand of social overall situation, the requisite measure of Ye Shi factory sustainable development.
Also have more impurity in powder slurries, later product quality is affected to some extent.So, first remove the impurity in powder slurries with 250 mesh sieves.Containing A starch and B starch in powder slurries now.Method provided by the invention utilizes horizontal screw centrifuge centrifugation to go out A starch slurry and B starch slurry; Certainly can also be that other the machine with same function is to complete this operation.
After A starch slurry is separated, after horizontal screw centrifuge dehydration, sends into drying tower dry; Dry flash temperature controls at about 120 DEG C, and baking temperature controls at about 160 DEG C, forms A starch, A starch moisture content≤10% after drying.Dewater the same with gluten, A powder slurries can produce equally when dewatering generous amount containing the water of certain starch, if the change be not used, could discharge after also needing to process it, cause a large amount of waste.So, method provided by the invention be by generous amount containing certain starch Water circulation in face, wash one's face workshop section, even can with its as low-temperature receiver to other products carry out cooling process.
If B starch slurry dewatered drying is made B starch, its economic worth is not high.In order to make product economy maximizing the benefits, method provided by the invention forms thick slurries by adding cassava and mix thoroughly in B starch slurry; In thick slurries, add α-amylase and heat and make boiling wine with dregs; In boiling wine with dregs, add carbohydrase make converted mash; Converted mash to be sent in fermentation tank and add yeast and carry out fermentation and make ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, obtains alcohol.
Wherein, the input amount of cassava is 50% of B starch slurry weight; α-amylase is AMS, and reacts by the proportioning that thick slurries per ton drop into 0.23kg AMS; The course of reaction of thick slurries and AMS heats through three grades: one-level is heated to 50 DEG C, secondary is heated to 80-85 DEG C, three grades and is heated to 105 DEG C; Finally the compound of thick slurries and AMS is dropped in heat insulation tank and be incubated two hours and keep temperature DEG C to be 100 DEG C, finally formation boiling wine with dregs; Saccharifying tank is entered after boiling wine with dregs is cooled to 60 DEG C, and be carbohydrase and its reaction that boiling wine with dregs per ton drops into 1.4kg according to weight ratio, under the temperature remains within the normal range normal pressure, reaction is made converted mash after 60 hours and is entered in fermentation tank, and is yeast and the brew fermentation that converted mash per ton drops into 0.4kg according to mass ratio; When temperature is 30 DEG C, yeast and converted mash ferment 8 hours in fermentation tank, obtain ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, finally obtains the alcohol that concentration is 10v/v.
As shown in Figure 2, Figure 3, Figure 4, one washes muscle machine, comprises casing 1; Bottom half is longitudinally provided with a bridge of the nose 2; The bridge of the nose 2 both sides are equipped with screw feeder 3 respectively; The rotation screw feeder face 33 of screw feeder 3 is tangent line matched in clearance with the bridge of the nose 2 and cabinet wall; Casing is provided with hole, is provided with bearing 4 in hole; The axle 31 of screw feeder 3 drives through bearing 4 and by the actuating unit be positioned at outside casing 1 and rotates; Bearing 4 outer wall is provided with the convex rafter 41 of some circles; Hole wall is provided with the groove coincide with convex rafter 41; The rotation screw feeder face 33 of screw feeder 3 is provided with several and stirs pawl 32.
The height of height lower than screw feeder 3 washing the bridge of the nose 2 in muscle machine provided by the invention, facilitates the flowing of both sides slurries.The top of the bridge of the nose 2 is linear structure, conveniently cuts the dough pullled by two screw feeders 3.
Two screw feeders 3 can adopt a set of power assembly and transmission assembly to drive locking phase to rotation.
Bearing outer wall provided by the invention is provided with the convex rafter 41 of 2 circle.Seal 5 is provided with between convex rafter 41 and groove.Can be sealing compound, sealing strip with seal 5, or other nontoxic encapsulants with same function all can be used in the present invention.
In specific works, muscle machine of washing provided by the invention can also replace dough mixing machine to use.First put in casing 1 by a certain proportion of water and flour, start screw feeder 3, under the stirring in the rotation screw feeder face 33 of screw feeder 3 is mixed, water and flour repeat to contact and finally form dough.
Appropriate water is dropped into again in casing 1, start screw feeder 3, two screw feeders 3 do move toward one another, stirring the tangent line matched in clearance effect between pawl 32 and screw feeder face 33 and the bridge of the nose 2, casing 1, dough is cut off fast, and under the mixing power effect of screw feeder 3, doughball is rinsed fast by flowing water and rubs, after repeatedly washing several times, obtain gluten and powder slurries.
The axle 31 of screw feeder 3 is connected with casing 1 by bearing 4, and screw feeder 3 can corresponding body pivot.In screw feeder 3 whipping process, due to vibration, bearing 4 is unavoidable produces dislocation or distortion between meeting and hole, cause spillage.The present invention is according to the wall thickness of casing 1, and can arrange the convex rafter 41 of varying number at the outer wall of bearing 4, convex rafter 41 is embedded in the groove in hole, and fills out with sealing strip 5, and screw feeder 3 displacement in whipping process is reduced, and not spillage.
More than show and describe general principle of the present invention, principal character and advantage of the present invention.The technical staff of the industry should understand; the present invention is not restricted to the described embodiments; the just principle of the present invention described in above-described embodiment and description; the present invention also has various changes and modifications without departing from the spirit and scope of the present invention, and these changes and improvements all fall in claimed scope of the present invention.The protection domain of application claims is defined by appending claims and equivalent thereof.
Claims (8)
1. a flour deep working method, is characterized in that: deep working method comprises the following steps:
A. and face: after flour mixes with water, be kneaded into dough, wherein face water is than being 1:0.7, and water is heated to 25 DEG C ~ 30 DEG C;
B. slaking: by dough leave standstill 15 ~ 25 minutes, allow dough nature slaking;
C. gluten washing: add water dough upset stirring, repeatedly clean and obtain clear dough and powder slurries for 4 ~ 6 times;
D. dehydrate: first extracted in step c by the moisture content in clear dough with dewaterer, then clear dough is utilized in drying machine 130 ~ 150 DEG C of vapour removal moisture content, drying machine tail gas temperature DEG C controls at 48 DEG C ~ 63 DEG C, Gluten moisture content≤9% obtained after drying;
E. the powder slurries in step c are first crossed 250 mesh sieves and remove impurity, then isolate A starch slurry and B starch slurry with horizontal screw centrifuge;
F. the A starch slurry in step e is sent into drying tower after horizontal screw centrifuge dehydration to dry; Dry flash temperature controls at about 120 DEG C, and baking temperature controls at about 160 DEG C, forms A starch, A starch moisture content≤10% after drying;
G. will add cassava in the B starch slurry in step e and mix thoroughly and form thick slurries; In thick slurries, add α-amylase and heat and make boiling wine with dregs; In boiling wine with dregs, add carbohydrase make converted mash; Converted mash to be sent in fermentation tank and add yeast and carry out fermentation and make ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, obtains alcohol.
2. a kind of flour deep working method according to claim 1, is characterized in that: in step g, the input amount of cassava is 50% of B starch slurry weight; α-amylase is AMS, and carries out proportioning in the ratio that thick slurries per ton drop into 0.23kg AMS; The course of reaction of thick slurries and AMS heats through three grades: one-level is heated to 50 DEG C, secondary is heated to 80-85 DEG C, three grades and is heated to 105 DEG C; Finally the compound of thick slurries and AMS is dropped in heat insulation tank and be incubated two hours and keep temperature to be 100 DEG C, finally form boiling wine with dregs; Saccharifying tank is entered after boiling wine with dregs is cooled to 60 DEG C, and be that boiling wine with dregs per ton drops into the carbohydrase of 1.4kg and boiling wine with dregs reacts according to weight ratio, under the temperature remains within the normal range normal pressure, reaction is made converted mash after 60 hours and is entered in fermentation tank, and is yeast and the brew fermentation that converted mash per ton drops into 0.4kg according to mass ratio; When temperature is 30 DEG C, yeast and converted mash ferment 8 hours in fermentation tank, obtain ripe wine with dregs; Ripe wine with dregs, through centrifugation and distillation, finally obtains the alcohol that concentration is 10v/v.
3. a kind of flour deep working method according to claim 1, is characterized in that: in steps d, clear dough is back to through the dilute slurry that dewaterer is deviate from and washes one's face in workshop section.
4. a kind of flour deep working method according to claim 1, is characterized in that: in step f, A starch slurry produces dilute slurry after horizontal screw centrifuge dehydration; Dilute slurry is back to face and washes one's face in workshop section.
5., for washing a muscle machine in a kind of flour deep working method of described claim 1, it is characterized in that: described in wash muscle machine and comprise casing; Described bottom half is longitudinally provided with a bridge of the nose; Screw feeder is equipped with respectively in described bridge of the nose both sides; The rotation screw feeder face of described screw feeder and the bridge of the nose and cabinet wall are tangent line matched in clearance; Described casing is provided with hole, is provided with bearing in described hole; The axle of described screw feeder drives rotation through described bearing by the power assembly be positioned at outside casing and transmission assembly; Described bearing outer wall is provided with the convex rafter of some circles; Described hole wall is provided with the groove coincide with described convex rafter; The rotation screw feeder face of described screw feeder is provided with several and stirs pawl.
6. one according to claim 5 washes muscle machine, it is characterized in that: described nose depth of beam is lower than the height of described screw feeder; The top of the described bridge of the nose is linear structure.
7. one according to claim 5 washes muscle machine, it is characterized in that: described two screw feeders drive locking phase to rotation by a set of power assembly and transmission assembly.
8. one according to claim 7 washes muscle machine, it is characterized in that: described bearing outer wall is provided with the convex rafter of 2 circle; Seal is provided with between described convex rafter and groove.
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| CN201510701969.6A CN105192243A (en) | 2015-10-23 | 2015-10-23 | Flour deep processing method and gluten washing machine used in method |
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| CN201510701969.6A CN105192243A (en) | 2015-10-23 | 2015-10-23 | Flour deep processing method and gluten washing machine used in method |
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| CN105146048A (en) * | 2015-10-23 | 2015-12-16 | 宿州市皖神面制品有限公司 | Gluten washing machine |
| CN106578334A (en) * | 2016-11-08 | 2017-04-26 | 程彪 | Processing method of gluten |
| CN113115855A (en) * | 2021-04-25 | 2021-07-16 | 宿州市皖神面制品有限公司 | Production method of wet gluten and all-in-one machine for beating and winding wet gluten |
| CN114246245A (en) * | 2021-12-30 | 2022-03-29 | 河南飞天农业开发股份有限公司 | Production process of vital gluten special for wiredrawing protein |
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| CN114246245A (en) * | 2021-12-30 | 2022-03-29 | 河南飞天农业开发股份有限公司 | Production process of vital gluten special for wiredrawing protein |
| CN114246245B (en) * | 2021-12-30 | 2023-08-01 | 河南飞天生物科技股份有限公司 | Production process of wheat gluten special for wiredrawing protein |
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Application publication date: 20151230 |