CN209576874U - Paddy pulp density On-line Control refining system - Google Patents
Paddy pulp density On-line Control refining system Download PDFInfo
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- CN209576874U CN209576874U CN201920271060.5U CN201920271060U CN209576874U CN 209576874 U CN209576874 U CN 209576874U CN 201920271060 U CN201920271060 U CN 201920271060U CN 209576874 U CN209576874 U CN 209576874U
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- paddy
- pulp density
- fiberizer
- line control
- glutinous rice
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Abstract
The utility model discloses a kind of paddy pulp density On-line Control refining systems, 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 utility model 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 utility model relates to cereal processing technique fields, and in particular to a kind of paddy pulp density On-line Control refining system.
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
→ immersion → sand milling crushing → sieving → filters pressing → broken → drying → packaging → finished product, process is more, and energy consumption is high, in pressure-filtering process
In, 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.
Utility model content
The utility model is intended to provide a kind of paddy pulp density On-line Control refining system, solves sticky rice food in the prior art
The technical problem that poor taste, processing cost are high, pollution energy consumption is high.
In order to solve the above technical problems, the first aspect of the utility model is:
Design a kind of paddy pulp density On-line Control refining system, including fiberizer, be respectively used to it is defeated into the fiberizer
The feeder and waterworks of cereal and water are sent, and grinds the densitometer that paddy starches dense degree for measuring the fiberizer
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 advantageous effects of the utility model are:
1. carry out room temperature defibrination to the cereal of immersion using fiberizer, by the way that the density that paddy is starched is monitored online, and
When adjust plus cereal or the speed for adding water, prevent paddy pulp density is excessive from causing paddy paste, the broken of nutriment be reduced or avoided
Bad or loss.
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 the utility model paddy pulp density On-line Control
Refining system can large-scale processing produce the grain meal slurry that can retain former Flavor substance and nutritional ingredient so that this
Sticky rice food in good taste 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 utility model embodiment；
Fig. 2 is the circuit block diagram of 1 paddy pulp density On-line Control refining system of the utility model embodiment；
Fig. 3 is the circuit diagram of 1 paddy pulp density On-line Control refining system of the utility model embodiment.
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 specific embodiment of the present utility model with reference to the accompanying drawings and examples, but following embodiment only uses
It is described in detail the utility model, does not limit the scope of the utility model 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 by the embodiment of the utility model includes fiberizer 11,
Fiberizer 11 is the internal millstone pulping machine with grinding wheel, which is additionally provided with for the defibrination material to fiberizer 11
The feeder 12 and waterworks 13 of glutinous rice and water are conveyed in bucket 111 respectively, fiberizer 11 and feeder 12 are placed on bracket 18
On, 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 utility model embodiment grinds paddy slurry by measuring fiberizer 11 is adjusted to fiberizer 11
In plus glutinous rice or water supply speed, so that the glutinous rice being added in fiberizer 11, water is 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 is opening, and bottom is communicated with paddy slurry delivery pipe 142, is parallel with the measurement of paddy pulp density in paddy slurry delivery pipe 142
Pipe 143 is equipped with densitometer 144 in paddy pulp density measurement pipe 143, which is 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 related 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, the utility model embodiment paddy pulp density On-line Control refining system further includes feed back control system,
As shown in Figures 2 and 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.
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 utility model is described in detail above in conjunction with drawings and examples, still, the skill of technical field
Art personnel, can also be to each specific in above-described embodiment it is understood that without departing from the purpose of the present invention
Parameter changes, and forms multiple specific embodiments, is the common variation range of the utility model, no longer detailed one by one herein
It states.
Claims (7)
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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920271060.5U CN209576874U (en) | 2019-03-04 | 2019-03-04 | Paddy pulp density On-line Control refining system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920271060.5U CN209576874U (en) | 2019-03-04 | 2019-03-04 | Paddy pulp density On-line Control refining system |
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| Publication Number | Publication Date |
|---|---|
| CN209576874U true CN209576874U (en) | 2019-11-05 |
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ID=68371466
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675678A (en) * | 2019-03-04 | 2019-04-26 | 郑州思念食品有限公司 | Paddy pulp density On-line Control refining system and cereal grinding method |
| CN116355685A (en) * | 2022-08-05 | 2023-06-30 | 云南省林业和草原科学院 | Intelligent oil extraction machine and oil extraction process thereof |
-
2019
- 2019-03-04 CN CN201920271060.5U patent/CN209576874U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675678A (en) * | 2019-03-04 | 2019-04-26 | 郑州思念食品有限公司 | Paddy pulp density On-line Control refining system and cereal grinding method |
| CN109675678B (en) * | 2019-03-04 | 2024-03-22 | 思念食品(河南)有限公司 | Cereal pulp density on-line control pulping system and cereal pulping method |
| CN116355685A (en) * | 2022-08-05 | 2023-06-30 | 云南省林业和草原科学院 | Intelligent oil extraction machine and oil extraction process thereof |
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| GR01 | Patent grant | ||
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| TR01 | Transfer of patent right |
Effective date of registration: 20211228 Address after: 450000 room A22, No. 9-2, Liudong Road, Zhengzhou area (Jinshui), pilot Free Trade Zone, Zhengzhou City, Henan Province Patentee after: Miss Food Co.,Ltd. Address before: 450000 No.15 Yingcai street, Huiji District, Zhengzhou City, Henan Province Patentee before: ZHENGZHOU SYNEAR FOOD Co.,Ltd. |
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| TR01 | Transfer of patent right |
Effective date of registration: 20230825 Address after: No. 13 Yingcai Street, Yingbin Road Street, Huiji District, Zhengzhou City, Henan Province, 450000 Patentee after: Miss Food (Henan) Co.,Ltd. Address before: 450000 room A22, No. 9-2, Liudong Road, Zhengzhou area (Jinshui), pilot Free Trade Zone, Zhengzhou City, Henan Province Patentee before: Miss Food Co.,Ltd. |