CN206119057U - Interval circulation continuous production soaks jar - Google Patents
Interval circulation continuous production soaks jar Download PDFInfo
- Publication number
- CN206119057U CN206119057U CN201620661860.4U CN201620661860U CN206119057U CN 206119057 U CN206119057 U CN 206119057U CN 201620661860 U CN201620661860 U CN 201620661860U CN 206119057 U CN206119057 U CN 206119057U
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- CN
- China
- Prior art keywords
- tank body
- liquid outlet
- circulation
- electrode
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000010924 continuous production Methods 0.000 title abstract description 4
- 239000007788 liquid Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000007789 sealing Methods 0.000 claims abstract description 7
- 125000004122 cyclic group Chemical group 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 8
- 239000011229 interlayer Substances 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 abstract description 20
- 235000009566 rice Nutrition 0.000 abstract description 20
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 240000007594 Oryza sativa Species 0.000 abstract 1
- 230000001737 promoting effect Effects 0.000 abstract 1
- 241000209094 Oryza Species 0.000 description 19
- 230000003544 deproteinization Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 230000007071 enzymatic hydrolysis Effects 0.000 description 2
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 235000001014 amino acid Nutrition 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
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- Cereal-Derived Products (AREA)
Abstract
The utility model discloses an interval circulation continuous production soaks jar, including a jar body, promote the water pump, a jar body upper end is equipped with the feed inlet, jar internal upper portion is equipped with the nozzle, a jar body lower extreme is equipped with discharge gate, circulation liquid outlet in proper order, discharge gate and circulation liquid outlet intercommunication are equipped with the filter screen between discharge gate and the circulation liquid outlet, the open end of circulation liquid outlet is equipped with sealing mechanism, the circulation liquid outlet links to each other through promoting the water pump with the nozzle, has realized the circulation of soak through the elevator pump. The utility model discloses a soak a jar simple structure, easy operation to degree of automation is high, reduces the input of manpower, and is intelligent relatively, production take off the former tangible attitude that albumen keeps the rice, and high resilience, taste are better.
Description
Technical field
This utility model is related to steeping tank, and in particular to a kind of interval circulation is continuous to produce steeping tank.
Background technology
At present, the artificial reconstructed method that domestic deproteinization rice is adopted mostly, this method is by starch material powder
It is broken and then plastotype obtains this deproteinization rice into the shape of rice again.Method prepared by this rice is complicated, to equipment
Requirement is higher, and, the necessary aminoacid for also needing containing many human bodies, trace element etc., China. in rice besides the starch
Patent of invention (Authorization Notice No. CN103211163B, authorized announcement date 2014.09.17) discloses a kind of adding for deproteinization rice
Work method, the method process rice using enzyme solution and obtain deproteinization rice, using the deproteinization rice of the technology processing, produce
Product outward appearance, color and luster, local flavor and mouthfeel are consistent with general rice, and removal of protein rate highest can be more than 95%.Compared to artificial
Reproduce rice, nutritive value is more rich, but in the production process of deproteinization rice, need by Raw Materials Rice be immersed in containing
Enzymolysis processing is carried out in the steeping tank of protease, general steeping tank is static immersing tank, and not only soak time is long, and due to
The effect of gravity, makes upper strata, and middle level, the pH of the soak of lower floor are inconsistent, directly results in the rice Degree of Enzymatic Hydrolysis in steeping tank
It is uneven, affect Deproteinated quality.
Utility model content
The purpose of this utility model is aiming at the deficiency of above-mentioned technology, there is provided a kind of simple structure, soak are uniformly divided
A kind of continuous production steeping tank of interval circulation for producing deproteinization rice of cloth.
For achieving the above object, the technical solution used in the present invention is:
The continuous production steeping tank of one kind interval circulation, including tank body, lifting water pump, tank body upper end is provided with charging aperture, tank body
Internal upper part is provided with nozzle, and tank body lower end is sequentially provided with discharging opening, circulation liquid outlet, and discharging opening is connected with circulation liquid outlet, discharged
Drainage screen is provided between mouth and circulation liquid outlet, the opening for circulating liquid outlet is provided with sealing mechanism, circulation liquid outlet and nozzle
It is connected by lifting water pump.
Further, the both sides of the tank body are provided with constant temperature interlayer.
Further, sight glass is provided with the top of the tank body;The both sides of the tank body are provided with bracing frame.
Further, the top of the tank body is provided with the first pH electrode, and middle part is provided with the second pH electrode, and bottom is provided with the 3rd
PH electrode;The tank body is externally provided with pH numerical control tables, cyclic control system, the first pH electrode of the pH numerical controls table Real-time Collection, and
Two pH electrode, the signal of the 3rd pH electrode, and the signal for collecting is compared, result is simultaneously sent to loop control by computing
System, is controlled to lift the start and stop of water pump by cyclic control system.
The beneficial effects of the utility model:
(1) high degree of automation of the present utility model, reduces the input of manpower, relatively intelligentization.
(2) steeping tank completes self-loopa according to the situation of soak, so that soak is each in the upper, middle and lower layer of tank body
The pH value of distributed points keeps relatively uniform, so that the rice Degree of Enzymatic Hydrolysis in steeping tank is relatively uniform, and then makes rice de-
Albumen rate reaches pre- fixing one's aim.
(3) original form of rice is kept using the deproteinization that this utility model is produced, and high resilience, mouthfeel is more
It is good.
(4) steeping tank simple structure of the present utility model, easy to operate.
Description of the drawings
Fig. 1 is structural representation of the present utility model;
Block diagrams of the Fig. 2 for cyclic control system;
Wherein, dog-house 1, nozzle 2, tank body 3, the first pH electrode 4, constant temperature interlayer 5, the second pH electrode 6, the 3rd pH electrode
7th, discharging opening 8, sealing mechanism 9, drainage screen 10, circulation liquid outlet 11, lifting water pump 12, bracing frame 13, sight glass 14.
Specific embodiment
As shown in figure 1, a kind of interval circulation is continuous to produce steeping tank, including tank body 3,3 top of tank body are drum, under
Portion is cone shape.3 upper end of tank body is provided with charging aperture 1, and the top in tank body 3 is provided with nozzle 2, and 3 lower end of tank body is sequentially provided with out
Material mouth 8, circulation liquid outlet 11, discharging opening 8 are connected with circulation liquid outlet 11, and are set between discharging opening 8 and circulation liquid outlet 11
There is drainage screen 10, the opening for circulating liquid outlet 11 is provided with sealing mechanism 9, and sealing mechanism 9 carries out sealing circulation liquid outlet 11, prevents
Only germ contamination.Lifting water pump 12 is additionally provided with outside tank body 3, circulation liquid outlet 11 is connected by lifting water pump 12 with nozzle 2.Lifted
Water pump 12 bottom can be filtered after soak, pump into the top of steeping tank 3 and sprayed by nozzle 2, realize following for soak
Ring.
Wherein, the both sides of tank body 3 are additionally provided with constant temperature interlayer 5, and constant temperature interlayer 5 can prevent the temperature drop in steeping tank
It is too fast, affect the enzyme activity in soak.The top of tank body 3 is provided with sight glass 14, facilitates the leaching of the rice in people's observation tank body
Blister state;The both sides of tank body 3 are provided with bracing frame 13, and the placement for making steeping tank firm is on the ground.
Wherein, the top of tank body 3 is provided with the first pH electrode 4, and middle part is provided with the second pH electrode 6, and it is electric that bottom is provided with the 3rd pH
Pole 7;With reference to shown in Fig. 2, tank body 3 is externally provided with pH numerical control tables, cyclic control system, the first pH electrode of pH numerical control table Real-time Collections 4,
Second pH electrode 6, the signal of the 3rd pH electrode 7, and the signal for collecting being compared, computing, wherein pH numerical controls table are by
One pH electrode 4, the second pH electrode 6, the 3rd pH electrode 7 collect signal and are converted into pH numerical value a, b, c;If the numerical value of a, b, c
Difference is more than 0.1, and result is sent to cyclic control system, lifts water pump 12 by cyclic control system control and starts, lifts water
After pump 12 starts, the soak of bottom is pumped into into the top of steeping tank 3 after drainage screen 10 is filtered and is sprayed by nozzle 2,
The circulation of soak is realized, until a, the absolute difference of the numerical value of b, c is not more than 0.1, result is sent to cyclic control system,
Water pump is lifted by cyclic control system control to stop, steeping tank is in static condition.This cyclic control system can be controlled automatically
System lifts the start and stop of water pump, reaches the effect of intermittent cyclic soak, the dress of this Automated condtrol circulation immersion liquid
Put more intelligent, it is efficient.
Claims (4)
1. a kind of interval circulation is continuous produces steeping tank, it is characterised in that:Including tank body (3), lift water pump (12), the tank body
(3) upper end is provided with charging aperture (1), and tank body (3) internal upper part is provided with nozzle (2);Tank body (3) lower end is sequentially provided with discharging
Mouthful (8), circulation liquid outlet (11), the discharging opening (8) are connected with liquid outlet (11) is circulated, the discharging opening (8) with recycle
Drainage screen (10) is provided between liquid mouth (11), the opening of circulation liquid outlet (11) is provided with sealing mechanism (9);The circulation
Liquid outlet (11) is connected by lifting water pump (12) with nozzle (2).
2. interval circulation according to claim 1 is continuous produces steeping tank, it is characterised in that:The both sides of the tank body (3)
It is provided with constant temperature interlayer (5).
3. interval circulation according to claim 1 is continuous produces steeping tank, it is characterised in that:Set at the top of the tank body (3)
There is sight glass (14);The both sides of the tank body (3) are provided with bracing frame (13).
4. interval circulation according to claim 1 is continuous produces steeping tank, it is characterised in that:The top of the tank body (3)
The first pH electrode (4) is provided with, middle part is provided with the second pH electrode (6), and bottom is provided with the 3rd pH electrode (7);Tank body (3) peripheral hardware
There are pH numerical control tables, cyclic control system, the first pH electrode of the pH numerical controls table Real-time Collection, the second pH electrode, the 3rd pH electrode
Signal, the signal for collecting is compared, result is simultaneously sent to cyclic control system by computing, by cyclic control system control
System lifts the start and stop of water pump (12).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620661860.4U CN206119057U (en) | 2016-06-28 | 2016-06-28 | Interval circulation continuous production soaks jar |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620661860.4U CN206119057U (en) | 2016-06-28 | 2016-06-28 | Interval circulation continuous production soaks jar |
Publications (1)
Publication Number | Publication Date |
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CN206119057U true CN206119057U (en) | 2017-04-26 |
Family
ID=58561019
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620661860.4U Expired - Fee Related CN206119057U (en) | 2016-06-28 | 2016-06-28 | Interval circulation continuous production soaks jar |
Country Status (1)
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CN (1) | CN206119057U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107684065A (en) * | 2017-10-18 | 2018-02-13 | 青岛大洋天德食品有限公司 | Peanut infusion system |
-
2016
- 2016-06-28 CN CN201620661860.4U patent/CN206119057U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107684065A (en) * | 2017-10-18 | 2018-02-13 | 青岛大洋天德食品有限公司 | Peanut infusion system |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170426 |