CN109675678A - Paddy pulp density On-line Control refining system and cereal grinding method - Google Patents
Paddy pulp density On-line Control refining system and cereal grinding method Download PDFInfo
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- CN109675678A CN109675678A CN201910160957.5A CN201910160957A CN109675678A CN 109675678 A CN109675678 A CN 109675678A CN 201910160957 A CN201910160957 A CN 201910160957A CN 109675678 A CN109675678 A CN 109675678A
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- paddy
- fiberizer
- pulp density
- cereal
- glutinous rice
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- 235000013339 cereals Nutrition 0.000 title claims abstract description 42
- 238000000227 grinding Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000007670 refining Methods 0.000 title claims abstract description 21
- 241000209094 Oryza Species 0.000 claims abstract description 120
- 235000007164 Oryza sativa Nutrition 0.000 claims abstract description 120
- 235000009566 rice Nutrition 0.000 claims abstract description 120
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 229920002472 Starch Polymers 0.000 claims abstract description 23
- 235000019698 starch Nutrition 0.000 claims abstract description 23
- 239000006188 syrup Substances 0.000 claims abstract description 22
- 235000020357 syrup Nutrition 0.000 claims abstract description 22
- 238000005259 measurement Methods 0.000 claims abstract description 9
- 239000002002 slurry Substances 0.000 claims description 63
- 238000001739 density measurement Methods 0.000 claims description 15
- 230000003139 buffering effect Effects 0.000 claims description 14
- 239000008107 starch Substances 0.000 claims description 8
- 240000008042 Zea mays Species 0.000 claims description 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 3
- 235000005822 corn Nutrition 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 244000000231 Sesamum indicum Species 0.000 claims description 2
- 235000003434 Sesamum indicum Nutrition 0.000 claims description 2
- 244000062793 Sorghum vulgare Species 0.000 claims description 2
- 235000021307 Triticum Nutrition 0.000 claims description 2
- 244000098338 Triticum aestivum Species 0.000 claims description 2
- 235000019713 millet Nutrition 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims 1
- 235000013312 flour Nutrition 0.000 abstract description 23
- 235000013305 food Nutrition 0.000 abstract description 16
- 238000012545 processing Methods 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000010865 sewage Substances 0.000 abstract description 5
- 239000003205 fragrance Substances 0.000 abstract description 4
- 235000020265 peanut milk Nutrition 0.000 abstract description 4
- 108090000623 proteins and genes Proteins 0.000 description 6
- 102000004169 proteins and genes Human genes 0.000 description 6
- 239000000428 dust Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000003801 milling Methods 0.000 description 3
- 235000016709 nutrition Nutrition 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000004537 pulping Methods 0.000 description 3
- 235000017060 Arachis glabrata Nutrition 0.000 description 2
- 244000105624 Arachis hypogaea Species 0.000 description 2
- 235000010777 Arachis hypogaea Nutrition 0.000 description 2
- 235000018262 Arachis monticola Nutrition 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 235000020232 peanut Nutrition 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 101100406317 Arabidopsis thaliana BCE2 gene Proteins 0.000 description 1
- 101100493897 Arabidopsis thaliana BGLU30 gene Proteins 0.000 description 1
- 101100518161 Arabidopsis thaliana DIN4 gene Proteins 0.000 description 1
- 101100422614 Arabidopsis thaliana STR15 gene Proteins 0.000 description 1
- 101100063437 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) DIN7 gene Proteins 0.000 description 1
- 101100141327 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) RNR3 gene Proteins 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 101150112501 din1 gene Proteins 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
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- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C11/00—Other auxiliary devices or accessories specially adapted for grain mills
- B02C11/04—Feeding devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C11/00—Other auxiliary devices or accessories specially adapted for grain mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C9/00—Other milling methods or mills specially adapted for grain
- B02C9/04—Systems or sequences of operations; Plant
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Cereal-Derived Products (AREA)
Abstract
The invention discloses a kind of paddy pulp density On-line Control refining system and cereal grinding methods, the paddy pulp density On-line Control refining system includes fiberizer, it is respectively used to the feeder from water to fiberizer and waterworks of grain transportation and, and the densitometer and/or densimeter that paddy starches dense degree are ground for measuring fiberizer, so that according to the rate of feeding of the state modulator feeder of measurement and/or the water feed rate of waterworks.The present invention adjusts the speed for adding cereal or adding water in time, prevents paddy pulp density is excessive from causing paddy paste by the way that the density that paddy is starched is monitored online；Glutinous rice flour and face are added by sticky rice syrup, the fragrance of rice is remained in sticky rice syrup, so that sticky rice food is in good taste；By reducing the usage amount of glutinous rice flour, so that the quality of sticky rice food is guaranteed, and reduces the sewage quantity of production glutinous rice flour discharge, and since the processing cost of Rice & peanut milk is significantly less than the processing cost of glutinous rice flour, to reduce the processing cost of sticky rice food.
Description
Technical field
The present invention relates to cereal processing technique fields, and in particular to a kind of paddy pulp density On-line Control refining system and cereal
Grinding method.
Background technique
The well received Chinese tradition snack such as the rice dumpling, rice cake be made of using glutinous rice as main material, by taking the rice dumpling as an example,
Traditional production method is then by glutinous rice flour and at dough, then by glutinous rice dough the rice dumpling to be made first by glutinous rice grinds.
With the raising of food processing machinery degree, it is able to that glutinous rice is processed into the quick-frozen foods such as the rice dumpling on a large scale, but
It is in today of the sticky rice foods such as the scale processing rice dumpling, the current processing method of bakery and confectionery is still by making or purchasing
Glutinous rice flour is bought, then by glutinous rice flour and at dough, then by machining rice dumpling etc. are made in dough, although under mechanical-assisted,
The techniques such as milling and face are easily many, but there are still following deficiencies for the mode of this extensive production dough:
First, the nutritional ingredients such as protein are lost or are destroyed serious in glutinous rice.The processing process of glutinous rice flour are as follows: glutinous rice → leaching
Bubble → sand milling crushing → sieving → filters pressing → broken → drying → packaging → finished product, process is more, and energy consumption is high, in pressure-filtering process,
So that a large amount of protein loss in glutinous rice.
Second, since filters pressing will lead to a large amount of protein loss in glutinous rice and enter in the water of discharge after glutinous rice pulverizing, so that
Discharge is largely containing the sewage of protein, and the sewage treatment difficulty containing protein is big and energy consumption is high.
Glutinous rice flour is being carried out drying link by third, and the fragrance in glutinous rice is lost, and fragrance is also not present in manufactured food,
Food taste bad to process.
4th, at high cost and buying glutinous rice flour quality is difficult to ensure.Since glutinous rice flour is processed by glutinous rice, so that glutinous rice
The price of powder is higher than glutinous rice, and a large amount of buying glutinous rice flours are difficult to verify its quality.
There is also similar situations for the processing of other cereal foods.
Summary of the invention
The present invention is intended to provide a kind of paddy pulp density On-line Control refining system and cereal grinding method, solve the prior art
The technical problem that middle sticky rice food poor taste, processing cost are high, pollution energy consumption is high.
In order to solve the above technical problems, the first aspect of the present invention is:
It designs a kind of paddy pulp density On-line Control refining system, including fiberizer, is respectively used to convey paddy into the fiberizer
The feeder and waterworks of object and water, and for measure the fiberizer grind paddy starch dense degree densitometer or/and
Densimeter so that the rate of feeding of the feeder according to the state modulator that the densitometer or/and densimeter measure and/or
The water feed rate of the waterworks.
Preferably, the paddy for adjusting flow is equipped in the discharge outlet of the fiberizer starch buffering hopper, the paddy slurry
The bottom of buffering hopper is communicated with paddy slurry delivery pipe, has paddy pulp density measurement pipe, institute in parallel or series in the paddy slurry delivery pipe
Densitometer is stated to be mounted in the paddy pulp density measurement pipe.
Preferably, the top of the paddy slurry buffering hopper is communicated with overflow pipe, the end of paddy the slurry delivery pipe and overflow pipe
End is communicated in paddy slurry container.
Preferably, it is equipped on the pipeline section before paddy slurry delivery pipe is with the paddy pulp density measurement pipe in parallel or series
Paddy starches delivery pump and the first valve, sets on the pipeline section of paddy slurry delivery pipe and the paddy pulp density measurement pipe in parallel or series
There is the second valve.
It preferably, further include that paddy for grinding to the fiberizer starches the secondary grinding pulp grinder reprocessed.
It preferably, further include feed back control system, the feeder includes conveying auger, and the feed back control system includes
Master controller, electric machine controller, the master controller receives the density signal of the densimeter measurement, and is believed according to the density
Number feedback arrive the electric machine controller, the electric machine controller control the motor speed of the conveying auger with control feeding speed
Degree；The master controller is PLC or single-chip microcontroller, the electric machine controller are frequency converter or servo-driver.
Preferably, which is characterized in that the fiberizer is that millstone pulping machine, hammer crusher or roller are broken
Machine.
The second aspect of the present invention is:
Design a kind of cereal grinding method, comprising the following steps:
(1) according to the defibrination speed of fiberizer, continue to add cereal and water into fiberizer respectively with speed according to a certain percentage；
(2) concentration or density that the fiberizer grinds paddy slurry are measured by densitometer or/and densimeter；
(3) the dense degree starched according to the paddy controls the speed for adding cereal into the fiberizer and/or controls to described
The speed of water is added in fiberizer.
Preferably, the cereal is at least one of glutinous rice, wheat kernel, corn, peanut, rice, millet, sesame.
Preferably, the cereal is glutinous rice, is milled into sticky rice syrup after the glutinous rice is sufficiently impregnated, the sticky rice syrup it is close
Degree is 1~1.5g/cm3.
The beneficial technical effect of the present invention lies in:
1. carrying out room temperature defibrination using cereal of the fiberizer to immersion, by the way that the density that paddy is starched is monitored online, adjust in time
Section plus cereal or add water speed, prevent paddy pulp density is excessive from causing paddy paste, be reduced or avoided nutriment destruction or
It is lost.
2. by directly with addition paddy slurry substitution moisture and partial grains powder carries out and face, paddy starch in retain to greatest extent
Original flavor substance in cereal, substantially improves the mouthfeel of sticky rice food, and paddy pulp density On-line Control defibrination of the present invention
System can large-scale processing produce the grain meal slurry that can retain former Flavor substance and nutritional ingredient so that this mouthfeel
Good sticky rice food can realize that industrialized production is processed.
3. the buying of cereal powder can be reduced using paddy slurry and face, and purchasing grain dust on a large scale can make grain dust obtain not
To sufficiently careful examination, therefore, the quality for the grain dust purchased on a large scale be cannot be guaranteed, and reduce the grain dust of buying
Usage amount, so that the quality of cereal foods is guaranteed.
4. by taking glutinous rice as an example, since the processing cost of sticky rice syrup is significantly less than the processing cost of glutinous rice flour, the dough of equivalent
Cost of manufacture, the mode for directlying adopt glutinous rice flour and face is significantly less than by the way of sticky rice syrup plus glutinous rice flour and face, thus
Reduce the processing cost of sticky rice food.
5., due to reducing the usage amount of glutinous rice flour, reducing production glutinous rice flour discharge for making the rice dumpling or rice cake
Sewage quantity, it is energy-saving, it is environmental-friendly.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of 1 paddy pulp density On-line Control refining system of the embodiment of the present invention；
Fig. 2 is the circuit block diagram of 1 paddy pulp density On-line Control refining system of the embodiment of the present invention；
Fig. 3 is the circuit diagram of 1 paddy pulp density On-line Control refining system of the embodiment of the present invention；
Fig. 4 is the flow chart of 2 cereal grinding method of the embodiment of the present invention.
In figure, each label signal are as follows: fiberizer 11, defibrination hopper 111, the outlet of paddy slurry 112, feeder 12, cereal hopper
121, conveying auger 122, motor 1221, retarder 1222, waterworks 13, clear water tanks 131, water pump 132, feed pipe 133, section
It flows valve 134, overflow pipe 135, overflow valve 136, paddy slurry buffering hopper 141, paddy and starches delivery pipe 142, paddy pulp density measurement pipe
143, densitometer 144, paddy slurry delivery pump 145, the first valve 146, the second valve 147, overflow pipe 148, paddy slurry container 15, secondary
Broken pipe 161, secondary grinding pulp grinder 162, paddy slurry bucket 163, master controller 171, electric machine controller 172,24V DC power supply 173,
220V AC power source 174, bracket 18.
Specific embodiment
Illustrate a specific embodiment of the invention with reference to the accompanying drawings and examples, but following embodiment is used only in detail
It describes the bright present invention in detail, does not limit the scope of the invention in any way.
Embodiment 1:
A kind of paddy pulp density On-line Control refining system, please refers to Fig.1 to Fig.3.
As shown in Figure 1, paddy pulp density On-line Control refining system provided in an embodiment of the present invention includes fiberizer 11, defibrination
Machine 11 is the internal millstone pulping machine with grinding wheel, which is additionally provided with for the defibrination hopper to fiberizer 11
The feeder 12 and waterworks 13 of glutinous rice and water are conveyed in 111 respectively, fiberizer 11 and feeder 12 are placed on mount 18,
Wherein, feeder 12 is located at 11 top of fiberizer.
Feeder 12 includes the cereal hopper 121 on top and the conveying auger 122 of lower part, and 121 bottom of cereal hopper goes out
Mouth is communicated to the feed inlet of conveying auger 122, and the rear of conveying auger 122 is equipped with motor 1221 and retarder 1222, motor
1221 output shaft and the input axis connection of retarder 1222, the output shaft of retarder 1222 and the shaft of conveying auger 122 connect
It connects, the rotation of motor 1221 can drive the shaft of conveying auger 122 to rotate, so that the helical blade of conveying auger 122 rotates
Glutinous rice in cereal hopper 121 is transported in defibrination hopper 111, during feeding glutinous rice, the revolving speed of motor 1221 and conveying
The rate of feeding of auger 122 is directly proportional.
Waterworks 13 include clear water tanks 131, water pump 132 and feed pipe 133, and the front end of feed pipe 133 is located at clear water tanks
131 bottoms, water pump 132 are arranged on feed pipe 133, and the end of feed pipe 133 is switched to defibrination hopper 111, passes through water pump 132
The water in clear water tanks 131 is retracted in defibrination hopper 111 with feed pipe 133.
Throttle valve 134 is installed on feed pipe 133, and is communicated on the pipeline section between water pump 132 and throttle valve 134
Overflow pipe 135 is equipped with overflow valve 136 on overflow pipe 135, be adjusted by throttle valve 134 into defibrination hopper 111 plus
The speed of water, and if 132 water supply of water pump is excessive, can be backflowed by overflow pipe 135 into clear water tanks 131.
The mode to feed into defibrination hopper 111 is as follows: will first impregnate the glutinous rice loading cereal hopper 121 well and after draining
In, and have the clean water of sufficient amount in clear water tanks 131, start the water pump 132 of waterworks 13, opens throttle valve 134, make water supply
Pipe 133 adds water into defibrination hopper 111 according to water velocity appropriate；Start motor 1221, by conveying auger 122 to defibrination
Add glutinous rice in hopper 111, so adds glutinous rice while adding water, starched glutinous rice and water mill at paddy by fiberizer 11.
During 11 grain milling of fiberizer slurry, in the defibrination speed allowed band of fiberizer 11, if to defibrination material
In bucket 111 plus the speed of glutinous rice is relative to the excessive velocities for adding water, then paddy slurry can be made excessively dense, causes paddy paste to be melted into and is
Ripe paddy slurry, if into defibrination hopper 111 plus the speed of glutinous rice is relative to adding the speed of water excessively slow, defibrination inefficiency, because
This need control plus glutinous rice and plus water speed, make plus glutinous rice and add water speed mutually coordinate, to avoid paddy paste, and improve
Defibrination efficiency.
For this purpose, the dense degree that the embodiment of the present invention grinds paddy slurry by measuring fiberizer 11 adjusts and adds into fiberizer 11
Glutinous rice or the speed of water supply make the glutinous rice being added in fiberizer 11, water be in suitable ratio.Specifically, in fiberizer 11
Paddy slurry outlet 112 is equipped with paddy slurry buffering hopper 141, and paddy slurry buffering hopper 141 is fixed on mount 18, paddy slurry buffering hopper 141
Top be opening, bottom be communicated with paddy slurry delivery pipe 142, paddy slurry delivery pipe 142 on be parallel with paddy pulp density measurement pipe
143, densitometer 144 is installed in paddy pulp density measurement pipe 143, the densitometer 144 is raw for Beijing Science and Technology Ltd., WorldCom
The on-line densimeter of the model TQ889U of production, can real-time measurement paddy slurry density, and can export relevant to paddy pulp density
Signal.
Paddy slurry delivery pipe 142 it is in parallel with paddy pulp density measurement pipe 143 before pipeline section on be equipped with paddy starch delivery pump 145 and
First valve 146, the conveying capacity that the pumpability of paddy slurry delivery pump 145 will starch delivery pipe 142 with paddy are adapted, paddy slurry conveying
Pump 145, to meet the measurement demand of densitometer 144, is starched in paddy to guarantee that paddy slurry has certain flow velocity in subsequent pipeline
The pipeline section that delivery pipe 142 and paddy pulp density measurement pipe 143 are in parallel is equipped with the second valve 147.
When the paddy ground to fiberizer 11 starches dense degree and measures, paddy slurry delivery pump 145 does not start first, and first
Valve 146 is in close state, and is opened the first valve 146 after paddy starches and accumulates a certain amount of paddy slurry in buffering hopper 141 and is opened
Dynamic paddy starches delivery pump 145, if the defibrination speed of fiberizer 11 is not caught up with, leads to the flow velocity that paddy is starched in paddy pulp density measurement pipe 143
It crosses slowly without the measurement demand for being able to satisfy densitometer 144, then paddy can be made to starch in delivery pipe 142 more by adjusting the second valve 147
More paddy slurries are diverted in paddy pulp density measurement pipe 143.
It is communicated with overflow pipe 148 on the top that paddy starches buffering hopper 141, paddy starches the end of delivery pipe 142 and overflow pipe 148
It is communicated in paddy slurry container 15.When the defibrination excessive velocities of fiberizer 11 make paddy slurry buffering hopper 141 in paddy slurry cannot and
It when Shi Yougu starches the outflow of delivery pipe 142, can be flowed in paddy slurry container 15, be prevented in paddy slurry buffering hopper 141 by overflow pipe 148
Paddy starch overflow.
Under normal circumstances, the paddy slurry granularity for carrying out grinding acquisition for the first time to glutinous rice and water using fiberizer 11 is thicker, slightly
Granularity paddy slurry is not able to satisfy to be required with face, therefore, the bottom of paddy slurry container 15 is communicated to by second-time breakage pipe 161 and is used for pair
The paddy that fiberizer 11 is ground starches the secondary grinding pulp grinder 162 reprocessed, and secondary grinding pulp grinder 162 is communicated to finally by pipeline again
Paddy slurry bucket 163, secondary grinding pulp grinder 162 is fine-grained high-speed breakage pump, to accumulate a certain amount of paddy slurry in paddy slurry container 15
Afterwards, paddy slurry is crushed by starting secondary grinding pulp grinder 162 again, to obtain fine granularity paddy slurry.
Further, paddy of embodiment of the present invention pulp density On-line Control refining system further includes feed back control system, such as Fig. 2
With shown in Fig. 3, feed back control system includes master controller 171, electric machine controller 172, wherein master controller 171 is
S7200PLC, electric machine controller 172 are MM420 frequency converter, signal output line road and the master controller 171 of densitometer 144
The electrical connection of I0.0 input pin, tetra- output pins of Q0.0, Q0.1, Q0.2, Q0.3 and electric machine controller of master controller 171
This four digital signal input ends of 172 DIN1, DIN2, DIN3, DIN4 are for electrical connection.
The signal that densitometer 144 is fed back represents the dense degree for the paddy slurry that measurement obtains, the letter fed back according to densitometer 144
Number, master controller 171 and electric machine controller 172 control motor 1221 and convert adjusting in 15 kinds of different rotating speeds.In feed pipe 133
Into defibrination hopper 111 plus in the case that the speed of water is certain, if the paddy that densitometer 144 measures starches excessively dense, master controller
171 and electric machine controller 172 to control 1221 revolving speed of motor slack-off so that conveying auger 122 is reduced into defibrination hopper 111 plus glutinous
The speed of rice, if the paddy that densitometer 144 measures is starched, dense degree is too low, and master controller 171 and electric machine controller 172 control motor
1221 revolving speeds become faster, so that conveying auger 122 accelerates into defibrination hopper 111 plus the speed of glutinous rice.
Feed back control system further includes 24V DC power supply 173, and 24V DC power supply 173 is for connecting 220V AC power source
174,220V AC power sources 174 are alternating current, and 220V alternating current is converted to 24V direct current, 24V direct current by 24V DC power supply 173
Source 173 is as densitometer 144, the power supply of master controller 171, and the control circuit power supply as electric machine controller 172, motor control
The main circuit of device 172 processed inputs 220V alternating current, and exports three-phase alternating current to power on rotation for motor 1221.
By real-time feedback control conveying auger 122 into defibrination hopper 111 plus glutinous rice speed so that plus water speed
With add the speed of glutinous rice mutually to coordinate, under the premise of guaranteeing 11 defibrination efficiency of fiberizer, paddy slurry can be prevented excessively dense and paste
Change.
The present embodiment paddy pulp density On-line Control refining system is not limited to carry out defibrination to glutinous rice, can also be with to other cereal
Carry out defibrination, such as corn, peanut.
Embodiment 2
A kind of cereal grinding method, the grinding method can be used for grinding Rice & peanut milk, referring to Fig. 4, this method specifically includes following step
It is rapid:
Step S110: it according to the defibrination speed of fiberizer, is persistently added according to a certain percentage into fiberizer with speed respectively glutinous
Rice and water.Millstone pulping machine, hammer crusher or roller crusher can be used in fiberizer, by fiberizer by glutinous rice and
Water mill is starched at paddy.
Step S120: the density of paddy slurry is ground by densimeter measurement fiberizer.It is added in order to prevent glutinous in fiberizer
The ratio of rice and water is uncoordinated, causes paddy slurry excessively dense and be gelatinized, thus is starched come real-time monitoring paddy by densitometer dense
Degree.
Step S130: according to the paddy pulp density of densimeter measurement, the speed that glutinous rice is added into fiberizer is controlled.According to close
Degree meter feedback result adjusts the ratio of glutinous rice and water in fiberizer, so that the paddy slurry ground by adjusting the speed of addition glutinous rice
For the life sticky rice syrup not being gelatinized.
Further, can also secondary grinding be carried out to the paddy slurry that fiberizer is ground, keep final paddy slurry granularity thinner, with symbol
Close requirement.
It is 1~1.5g/cm3 by the concentration control of the sticky rice syrup ground, through a large number of experiments, the density in the grinding method
In range, sticky rice syrup will not be gelatinized, and meter Xiang Qi is denseer in sticky rice syrup, and if excessive concentration, sticky rice syrup are easy gelatinization, discomfort
In industrialization large-scale production, if concentration is lower, meter Xiang Qi is weaker in Rice & peanut milk, and the meter Xiang Yue that sticky rice syrup retains is dense, using this
The glutinous rice product mouthfeel such as rice dumpling made of sticky rice syrup and face is better.
Glutinous rice flour is added in the above-mentioned sticky rice syrup processed and when at dough, the sticky rice syrup processed must be it is fresh, do not have
There is the life sticky rice syrup of gelatinization, the fragrance of glutinous rice is remained compared with glutinous rice flour, in sticky rice syrup, and reduce the nutritional ingredients such as protein
Loss, also without sewage discharge when making sticky rice syrup, energy consumption is reduced, and is conducive to environmental protection.Using sticky rice syrup and glutinous rice flour
With at the dough production sticky rice foods such as the rice dumpling it is in good taste, and reduce the amount of purchase of glutinous rice flour, it is glutinous for glutinous rice flour
Rice & peanut milk processing cost is lower, in the case where large-scale processing sticky rice food, substitutes glutinous rice flour, Neng Goujie using part sticky rice syrup
Save great amount of cost.
The present invention is described in detail above in conjunction with drawings and examples, still, those of skill in the art
Member is it is understood that without departing from the purpose of the present invention, can also carry out each design parameter in above-described embodiment
Change, forms multiple specific embodiments, is common variation range of the invention, is no longer described in detail one by one herein.
Claims (10)
1. a kind of paddy pulp density On-line Control refining system, which is characterized in that including fiberizer, be respectively used to the fiberizer
The feeder and waterworks of middle grain transportation and water, and the density that paddy starches dense degree is ground for measuring the fiberizer
Meter or/and densimeter, so that the feeding speed of the feeder according to the state modulator that the densitometer or/and densimeter measure
The water feed rate of degree and/or the waterworks.
2. paddy pulp density On-line Control refining system according to claim 1, which is characterized in that in going out for the fiberizer
It is equipped with the paddy for adjusting flow at material mouth and starches buffering hopper, the bottom of the paddy slurry buffering hopper is communicated with paddy slurry delivery pipe,
There is paddy pulp density measurement pipe in parallel or series in the paddy slurry delivery pipe, the densitometer is mounted on the paddy pulp density measurement pipe
On.
3. paddy pulp density On-line Control refining system according to claim 2, which is characterized in that the paddy slurry buffering hopper
Top be communicated with overflow pipe, the end of the paddy slurry delivery pipe and overflow pipe is communicated in paddy slurry container.
4. paddy pulp density On-line Control refining system according to claim 2, which is characterized in that starch delivery pipe in the paddy
With the paddy pulp density measurement pipe in parallel or series before pipeline section be equipped with paddy slurry delivery pump and the first valve, starched in the paddy
Delivery pipe and the pipeline section of the paddy pulp density measurement pipe in parallel or series are equipped with the second valve.
5. paddy pulp density On-line Control refining system according to claim 1, which is characterized in that further include for described
The paddy that fiberizer is ground starches the secondary grinding pulp grinder reprocessed.
6. paddy pulp density On-line Control refining system according to claim 1, which is characterized in that further include feedback control dress
It sets, the feeder includes conveying auger, and the feed back control system includes master controller, electric machine controller, the main control
Device receives the density signal of the densimeter measurement, and according to density signal feedback to the electric machine controller, the electricity
Machine controller controls the motor speed of the conveying auger to control rate of feeding；The master controller is PLC or single-chip microcontroller, institute
Stating electric machine controller is frequency converter or servo-driver.
7. paddy pulp density On-line Control refining system according to claim 1, which is characterized in that the fiberizer is mill
Formula fiberizer, hammer crusher or roller crusher.
8. a kind of cereal grinding method, which comprises the following steps:
(1) according to the defibrination speed of fiberizer, continue to add cereal and water into fiberizer respectively with speed according to a certain percentage；
(2) concentration or density that the fiberizer grinds paddy slurry are measured by densitometer or/and densimeter；
(3) the dense degree starched according to the paddy controls the speed for adding cereal into the fiberizer and/or controls to described
The speed of water is added in fiberizer.
9. cereal grinding method according to claim 8, which is characterized in that the cereal is glutinous rice, wheat kernel, corn, flower
At least one of life, rice, millet, sesame.
10. cereal grinding method according to claim 9, which is characterized in that the cereal is glutinous rice, and the glutinous rice is filled
Sticky rice syrup is milled into after sub-dip bubble, the density of the sticky rice syrup is 1~1.5g/cm3.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113499827A (en) * | 2021-06-11 | 2021-10-15 | 郑州思念食品有限公司 | Grain pulp preparation system, preparation method and application thereof |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102150784A (en) * | 2010-09-02 | 2011-08-17 | 北京康得利机械设备制造有限公司 | Refining concentration automatic control system |
| US20110214577A1 (en) * | 2010-03-08 | 2011-09-08 | Delice Co., Ltd. | Apparatus for producing confectionery |
| CN103790059A (en) * | 2014-01-24 | 2014-05-14 | 华南理工大学 | Device and method for medium-concentration beating fed through medium-concentration pulp pump |
| CN203965273U (en) * | 2014-05-14 | 2014-11-26 | 武汉龙净环保工程有限公司 | Slurry density of desulfurizing absorption column measurement mechanism |
| CN205409413U (en) * | 2015-08-11 | 2016-08-03 | 重庆胜钢机械设备有限公司 | Thick liquid concentration automatic control system is ground to bean or pea |
| CN206399759U (en) * | 2016-12-30 | 2017-08-11 | 大唐贵州发耳发电有限公司 | A kind of device for serosity density measurement |
| CN206772755U (en) * | 2017-06-16 | 2017-12-19 | 聊城信源集团有限公司 | A kind of measuring system of desulfurization carbide slag slurry parameter |
| CN206951309U (en) * | 2017-06-12 | 2018-02-02 | 河南张老有生物科技有限公司 | One three separate type refining systems of mill |
| CN209576874U (en) * | 2019-03-04 | 2019-11-05 | 郑州思念食品有限公司 | Paddy pulp density On-line Control refining system |
-
2019
- 2019-03-04 CN CN201910160957.5A patent/CN109675678B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110214577A1 (en) * | 2010-03-08 | 2011-09-08 | Delice Co., Ltd. | Apparatus for producing confectionery |
| CN102150784A (en) * | 2010-09-02 | 2011-08-17 | 北京康得利机械设备制造有限公司 | Refining concentration automatic control system |
| CN103790059A (en) * | 2014-01-24 | 2014-05-14 | 华南理工大学 | Device and method for medium-concentration beating fed through medium-concentration pulp pump |
| CN203965273U (en) * | 2014-05-14 | 2014-11-26 | 武汉龙净环保工程有限公司 | Slurry density of desulfurizing absorption column measurement mechanism |
| CN205409413U (en) * | 2015-08-11 | 2016-08-03 | 重庆胜钢机械设备有限公司 | Thick liquid concentration automatic control system is ground to bean or pea |
| CN206399759U (en) * | 2016-12-30 | 2017-08-11 | 大唐贵州发耳发电有限公司 | A kind of device for serosity density measurement |
| CN206951309U (en) * | 2017-06-12 | 2018-02-02 | 河南张老有生物科技有限公司 | One three separate type refining systems of mill |
| CN206772755U (en) * | 2017-06-16 | 2017-12-19 | 聊城信源集团有限公司 | A kind of measuring system of desulfurization carbide slag slurry parameter |
| CN209576874U (en) * | 2019-03-04 | 2019-11-05 | 郑州思念食品有限公司 | Paddy pulp density On-line Control refining system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113499827A (en) * | 2021-06-11 | 2021-10-15 | 郑州思念食品有限公司 | Grain pulp preparation system, preparation method and application thereof |
| CN113499827B (en) * | 2021-06-11 | 2024-02-20 | 思念食品(河南)有限公司 | Cereal pulp preparation system, preparation method and application thereof |
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