CN106390829A - Syrup mixing method for maltose syrup preparation - Google Patents
Syrup mixing method for maltose syrup preparation Download PDFInfo
- Publication number
- CN106390829A CN106390829A CN201611081922.5A CN201611081922A CN106390829A CN 106390829 A CN106390829 A CN 106390829A CN 201611081922 A CN201611081922 A CN 201611081922A CN 106390829 A CN106390829 A CN 106390829A
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- Prior art keywords
- tank body
- temperature
- cooling water
- reducing motor
- unit
- Prior art date
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Links
- 238000002156 mixing Methods 0.000 title claims abstract description 35
- 239000006188 syrup Substances 0.000 title claims abstract description 17
- 235000020357 syrup Nutrition 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims abstract description 16
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 title claims abstract description 15
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 title claims abstract description 15
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 58
- 239000000498 cooling water Substances 0.000 claims abstract description 34
- 238000001514 detection method Methods 0.000 claims abstract description 27
- 239000002002 slurry Substances 0.000 claims description 26
- 230000006698 induction Effects 0.000 claims description 14
- 238000004513 sizing Methods 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 6
- 238000013019 agitation Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 238000011897 real-time detection Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000000007 visual effect Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 235000021433 fructose syrup Nutrition 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 230000036413 temperature sense Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/072—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
- B01F27/0723—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis oblique with respect to the rotating axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/071—Fixing of the stirrer to the shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/074—Stirrers characterised by their mounting on the shaft having two or more mixing elements being concentrically mounted on the same shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
- B01F27/906—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms with fixed axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/211—Measuring of the operational parameters
- B01F35/2115—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2214—Speed during the operation
- B01F35/22142—Speed of the mixing device during the operation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2215—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/95—Heating or cooling systems using heated or cooled stirrers
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
- C13K7/00—Maltose
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F2035/98—Cooling
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention relates to a syrup mixing method for maltose syrup preparation. The method is performed by use of the following components: a tank body and a stirring component mounted in the tank body; the stirring component comprises a stirring shaft rotatably mounted in the center of the tank body, a gear motor used for driving the stirring shaft and arranged on the outer side of the top of the tank body; middle stirring blades in the middle part of an inner chamber of the tank body and bottom stirring blades at the bottom of the inner chamber of the tank body are arranged on the stirring shaft; the middle stirring blades sleeve the stirring shaft by virtue of a shaft sleeve, and the middle stirring blade is empty shell shaped, a cavity of the middle stirring blade is communicated with a sleeve cavity of the shaft sleeve; the bottom of the shaft sleeve is connected with a cooling water inlet pipe, and the top of the shaft sleeve is connected with a cooling water outlet pipe; the cooling water inlet pipe and the cooling water outlet pipe are connected with a cooling water circulating unit; the cooling water circulating unit is connected with a control unit; a temperature detection rod is mounted in the tank body, and is connected with a temperature sensing unit; and the control unit is connected with the gear motor and the cooling water circulating unit.
Description
Technical field
The present invention relates to maltose syrup production equipment field, particularly to maltose syrup production size mixing equipment.
Background technology
Tank of sizing mixing is the equipment prepared high fructose syrup, must use in maltose syrup, and the structure of tank of sizing mixing directly affects produces
The quality of product.Need fermentation liquid is stirred in addition it is also necessary to real-time control be carried out to temperature, liquid level height etc. in tank when sizing mixing,
Existing tank stirring efficiency of sizing mixing is low, heat exchange is insufficient, and temperature control stability is poor it is impossible to adaptation produces needs, and due to forming sediment
The materials such as the protein that contains in powder, fat, lead to, during sizing mixing, size mixing insufficient in tank of sizing mixing, or even liquid level upper strata
One layer of oil film of floating, had both been unfavorable for the process of sizing mixing of material, the filtration after impact is sized mixing again, the speed of decolouring etc..
Content of the invention
The applicant is directed to the disadvantages mentioned above of prior art, is studied and improves, and provides a kind of maltose syrup preparation to use
Mixing method, using following scheme:
A kind of maltose syrup preparation mixing method, comprises the following steps:
The first step:Set the temperature threshold of the temperature induction unit being connected with temperature detection bar in tank body, including minimum threshold
Value and highest threshold value;
Second step:The rotating speed of reducing motor, time parameter are set by control unit, described rotating speed include rated speed and
The slow-speed of revolution, and set the working time parameter of cooling water circulation unit;
3rd step:Slurry is inserted tank body from the upper end import of tank body;
4th step:Start reducing motor, reducing motor drives shaft to rotate, using middle part stirring vane and bottom stirring
Blade is to the slurry agitation in tank body;The temperature of slurry in temperature detection bar real-time detection tank body, when temperature induction unit sensing
Temperature signal when being more than the highest threshold value setting, send the signal to control unit, described control unit adjusts reducing motor
Rotating speed so that reducing motor is in low speed state, and start cooling water circulation unit to the middle part slurry cooling in tank body,
Until after the temperature of temperature induction unit sensing is less than the lowest threshold setting, control unit controls reducing motor to recover normal and turns
Speed, and stop cooling water circulation unit;When reach set size mixing the time after, control cooling water circulation unit be automatically stopped deceleration
Motor works;
5th step:After the completion of sizing mixing, open the outlet at bottom release slurry of tank body.
Improvement further as technique scheme:
Temperature detection bar is provided with multiple temperature detecting point.
Described temperature detecting point can on temperature detection bar height up and down position.
Described temperature detecting point can rotate around temperature detection bar.
It is provided with valve, described valve is provided with pressure inductor at outlet at bottom.
The method have technical effect that:
The present invention is combined using middle part stirring vane and bottom stirring vane, realizes quick, high-efficiency stirring to slurry;
Setting real time temperature Detection & Controling device, realizes temperature adjusting and mixing speed, the linkage of water cooling, its regulating effect is good,
Speed is fast, reliability is high;The bottom stirring vane of present invention setting can avoid paste deposition in the bottom of tank body, makes bottom slurry
Kick up, middle part stirring vane is arranged for multilamellar, successively stirs from bottom to up, realization is efficient, high-quality is sized mixing.
Brief description
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the control principle block diagram of the present invention
In figure:1st, tank body;2nd, mixing component;21st, shaft;22nd, reducing motor;23rd, middle part stirring vane;24th, bottom
Stirring vane;241st, tilting section;242nd, vertical section;243rd, breach;25th, axle sleeve;3rd, upper end import;4th, outlet at bottom;5th, temperature
Detection bar;6th, height detection bar;7th, visual window;8th, cooling water inlet pipe;9th, cooling water outlet pipe;10th, cooling water circulation unit;
11st, control unit;12nd, temperature induction unit.
Specific embodiment
Below in conjunction with the accompanying drawings the specific embodiment of the present invention is described further.
Embodiment 1:As shown in Figure 1 and Figure 2, the maltose syrup preparation mixing method of the present embodiment, including tank body 1 and peace
It is loaded on the mixing component 2 in tank body 1, tank body 1 is provided with upper end import 3 and outlet at bottom 4, mixing component 2 includes rotating to be installed
In tank body 1 center and center overlapping of axles setting with tank body 1 shaft 21, drive shaft 21 and be placed in tank body 1 top
The reducing motor 22 in outside, shaft 21 is provided with the middle part stirring vane 23 in the middle part of tank body 1 inner chamber and is located in tank body 1
The bottom stirring vane 24 in bottom of chamber portion, middle part stirring vane 23 is sheathed on shaft 21 by axle sleeve 25, axle sleeve 25 and tank body 1
Between be fixedly connected, middle part stirring vane 23 is ghost shape, and its cavity connects with the mantle cavity of axle sleeve 25, the bottom connection of axle sleeve 25
Cooling water inlet pipe 8, top connects cooling water outlet pipe 9, cooling water inlet pipe 8 and cooling water outlet pipe 9 with cooling water circulation
Unit 10 connects, and cooling water circulation unit 10 is connected with control unit 11;It is provided with the inner chamber of tank body 1 near the setting of its inwall
Temperature detection bar 5, temperature detection bar 5 is connected with temperature induction unit 12, and the outfan of temperature induction unit 12 connects and controls
The input of unit 11, the outfan of control unit 11 connects reducing motor 22 and cooling water circulation unit 10.
During work, the temperature threshold of design temperature sensing unit 12, including lowest threshold and highest threshold value;Control unit 11
The middle rotating speed setting reducing motor 22, time parameter, rotating speed includes rated speed and the slow-speed of revolution, sets cooling water circulation unit 10
Working time;After all parameter settings finish, slurry is inserted tank body 1 from the upper end import 3 of tank body 1;Start the electricity that slows down
Machine 22, reducing motor 22 drives shaft 21 to rotate, using middle part stirring vane 23 and bottom stirring vane 24 in tank body 1
Slurry agitation;The temperature of slurry in temperature detection bar 5 real-time detection tank body 1, when the temperature signal of temperature induction unit 12 sensing
During more than the highest threshold value setting, send the signal to control unit 11, control unit 11 adjusts the rotating speed of reducing motor 22, makes
Obtain reducing motor 22 and be in low speed state, and start cooling water circulation unit 10, cooling water is from the cooling of axle sleeve 25 bottom
Water water inlet pipe 8 enters in axle sleeve 25 and middle part stirring vane 23, and flows out from the cooling water outlet pipe 9 at top, works as temperature sense
After the temperature of unit 12 sensing is less than the lowest threshold setting, control unit 11 controls reducing motor 22 to recover rated speed, and
Stop cooling water circulation unit 10 to work;When reach set size mixing the time after, control unit 11 is automatically stopped reducing motor 22
Work.
Combined using middle part stirring vane 23 and bottom stirring vane 24, realize quick, the high-efficiency stirring to slurry;Bottom
Portion's stirring vane 24 can avoid paste deposition in the bottom of tank body 1, so that bottom slurry is kicked up, and improves stirring efficiency and effect.
Embodiment 2:As the improvement further of above-described embodiment 1, as shown in figure 1, middle part stirring vane 23 includes up and down
The multilamellar being spaced apart, and it is symmetrically positioned in the radially opposite sides of shaft 21;Bottom stirring vane 24 is single layer structure, is arranged symmetrically
Radially opposite sides in shaft 21;Angle α between middle part stirring vane 23 and shaft 21 be less than bottom stirring vane 24 with
Angle β between shaft 21.
Middle part stirring vane 23 is arranged for multilamellar, successively stirs from bottom to up, and realization is efficient, high-quality is sized mixing.Wherein, in
Angle α between portion's stirring vane 23 and shaft 21 is less than the angle β between bottom stirring vane 24 and shaft 21, so
The purpose of setting is, because the resistance of bottom slurry is larger, while ensureing stirring efficiency, can suitably reduce bottom stirring
The torsion of blade 24 root, extends its service life.
Embodiment 3:As the improvement further of embodiment 1, as shown in figure 1, temperature detection bar 5 is provided with multiple upper and lower cloth
The temperature detecting point put, temperature detecting point is connected with temperature induction unit 12.Because the height of tank body 1 is higher, using multiple temperature
Degree test point, it is to avoid lead to due to upper and lower temperature difference examine indeterminable situation appearance, its temperature detection reliability is higher.Further
Ground, temperature detecting point can adjust height and position on temperature detection bar 5, be accurately defined by realizing detecting, and also can be around
Temperature detection bar 5 rotates, and adjusts detection direction.
Embodiment 4:As the improvement further of above-described embodiment 1, as shown in figure 1, being provided with close in the inner chamber of tank body 1
The height detection bar 6 of its inwall setting, the outside of tank body 1 is provided with the visual window 7 of observed temperature detection bar 5 and height detection bar 6.
The height of whipping temp in tank body 1 and slurry can directly be observed from visual window 7.
Embodiment 5:As the improvement further of above-described embodiment 1, as shown in figure 1, middle part stirring vane 23 is in tank body 1
Radial span A be more than radial span B in tank body 1 for the bottom stirring vane 24.The span of bottom stirring vane 24 can not be too
Greatly, its deformation under big slurry agitation resistance can be avoided.
Embodiment 6:As the improvement further of above-described embodiment 1, as shown in figure 1, bottom stirring vane 24 includes and stirs
Mix axle 21 be connected tilting section 241 and the vertical section 242 in tilting section 241 outer end downward bending, tilting section 241 is cut be provided with scarce
Mouth 243.The bottom stirring vane 24 of both sides forms domes, and during stirring, resistance is little;At breach 243, form sharp blade,
Beneficial to stirring.
Embodiment 7:As shown in figure 1, the maltose syrup preparation mixing method of the present embodiment, comprise the following steps:
The first step:Set the temperature threshold of the temperature induction unit 12 being connected with temperature detection bar 5 in tank body 1, including
Low threshold and highest threshold value;
Second step:The rotating speed of reducing motor 22, time parameter are set by control unit 11, rotating speed include rated speed and
The slow-speed of revolution, and set the working time parameter of cooling water circulation unit 10;
3rd step:Slurry is inserted tank body 1 from the upper end import 3 of tank body 1;
4th step:Start reducing motor 22, reducing motor 22 drives shaft 21 to rotate, using middle part stirring vane 23 and
Bottom stirring vane 24 is to the slurry agitation in tank body 1;In temperature detection bar 5 real-time detection tank body 1, the temperature of slurry, works as temperature
When the temperature signal of sensing unit 12 sensing is more than the highest threshold value setting, send the signal to control unit 11, control unit
The rotating speed of 11 regulation reducing motors 22 is so that reducing motor 22 is in low speed state, and it is right to start cooling water circulation unit 10
Middle part slurry cooling in tank body 1, until after the temperature of temperature induction unit 12 sensing is less than the lowest threshold setting, control single
Unit 11 controls reducing motor 22 to recover rated speed, and stops cooling water circulation unit 10;When reach set size mixing the time after,
Control cooling water circulation unit 10 to be automatically stopped reducing motor 22 to work;
5th step:After the completion of sizing mixing, open tank body 1 outlet at bottom 4 release slurry.
Further, in the present invention, at outlet at bottom 4, it is provided with valve, described valve is provided with pressure inductor, this pressure
Power induction apparatuss are used for detecting slurry pressure, and pressure signal are sent to control unit, when the pressure detecting is more than setting
During value, stop the charging toward in tank body 1, thus ensureing that the slurry once stirring in tank body 1 is in rational scope, optimal to ensure
Stirring efficiency and effect.
Claims (5)
1. a kind of maltose syrup preparation mixing method is it is characterised in that comprise the following steps:
The first step:Set the temperature threshold of the temperature induction unit (12) being connected with temperature detection bar (5) in tank body (1), including
Lowest threshold and highest threshold value;
Second step:Set rotating speed, the time parameter of reducing motor (22) by control unit (11), described rotating speed includes normal turning
Speed and the slow-speed of revolution, and set the working time parameter of cooling water circulation unit (10);
3rd step:Slurry is inserted tank body (1) from the upper end import (3) of tank body (1);
4th step:Start reducing motor (22), reducing motor (22) drives shaft (21) to rotate, using middle part stirring vane
And bottom stirring vane (24) is to the slurry agitation in tank body (1) (23);Temperature detection bar (5) real-time detection tank body (1) entoplasm
The temperature of material, when the temperature signal that temperature induction unit (12) senses is more than the highest threshold value setting, sends the signal to control
Unit (11) processed, described control unit (11) adjusts the rotating speed of reducing motor (22) so that reducing motor (22) is in the slow-speed of revolution
State, and start cooling water circulation unit (10) to the middle part slurry cooling in tank body (1), until temperature induction unit (12) sense
After the temperature answered is less than the lowest threshold setting, control unit (11) controls reducing motor (22) to recover rated speed, and stops
Cooling water circulation unit (10);When reach set size mixing the time after, control cooling water circulation unit (10) be automatically stopped deceleration
Motor (22) works;
5th step:After the completion of sizing mixing, open outlet at bottom (4) the release slurry of tank body (1).
2. maltose syrup preparation mixing method according to claim 1 is it is characterised in that set on temperature detection bar (5)
There are multiple temperature detecting point.
3. maltose syrup preparation mixing method according to claim 2 is it is characterised in that described temperature detecting point can be in
The upper height up and down position of temperature detection bar (5).
4. maltose syrup preparation mixing method according to claim 2 is it is characterised in that described temperature detecting point can be around
Temperature detection bar (5) rotates.
5. maltose syrup preparation mixing method according to claim 1 is it is characterised in that outlet at bottom (4) place is provided with
Valve, described valve is provided with pressure inductor.
Priority Applications (1)
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CN201611081922.5A CN106390829B (en) | 2016-11-30 | 2016-11-30 | Mixing method is used in malt syrup preparation |
Applications Claiming Priority (1)
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CN201611081922.5A CN106390829B (en) | 2016-11-30 | 2016-11-30 | Mixing method is used in malt syrup preparation |
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CN106390829A true CN106390829A (en) | 2017-02-15 |
CN106390829B CN106390829B (en) | 2019-10-15 |
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Cited By (6)
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CN111298682A (en) * | 2020-04-08 | 2020-06-19 | 杭州筋钢人健康科技有限公司 | Processing device for mixture in colloidal form |
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