CN205954016U - Yeast self -dissolving equipment - Google Patents
Yeast self -dissolving equipment Download PDFInfo
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- CN205954016U CN205954016U CN201620726694.1U CN201620726694U CN205954016U CN 205954016 U CN205954016 U CN 205954016U CN 201620726694 U CN201620726694 U CN 201620726694U CN 205954016 U CN205954016 U CN 205954016U
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- central siphon
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Abstract
The utility model discloses a yeast self -dissolving equipment, it includes that one has the main casing body of apron and the hollow transmission shaft that an at least root zone has hollow thick liquid leaf, and the apron encloses synthetic inclosed main cavity room with the main casing body, and main outer wall of cavity is equipped with cavity steam air inlet and cavity vapor vent mouth, and hollow transmission shaft vertically runs through the main cavity room, hollow central siphon of low temperature section and the hollow central siphon coaxial coupling of high temperature section that hollow transmission shaft is not fed through by each other form, and it has low temperature section steam pipe and high temperature section steam pipe to hold separately in the lumen of hollow central siphon of low temperature section and the hollow central siphon of high temperature section, and hollow central siphon of low temperature section and the hollow central siphon of high temperature section be synchronous the rotation by electromotor drive, and the top of the hollow central siphon of low temperature section is provided with the feed inlet, and the below of the hollow central siphon of high temperature section is provided with the bin outlet the utility model discloses can provide the continuous production mode, equipment itself requires lowly to moisture, showing to be less than enzymolysis tank, and it is quick to heat up.
Description
Technical field
The utility model is related to microorganism production equipment, more particularly, to a kind of yeast autolysis equipment.
Background technology
Yeast is widely used in the fields such as bread fermentation, beer fermentation, animal feed, and its species is various, including bread ferment
Mother, brewer's yeast, molasses yeast etc..Much existing food materials, such as molasses, cornstarch, corn syrup and beet etc.,
All substantial amounts of yeast can be turned out by way of fermentation.
Yeast nutritious, containing protein, carbohydrate, needed by human 8 kinds of amino acid and 14 kinds of mineral matters,
The nutriments such as the vitamin containing almost all kinds, nucleic acid and glutathione.Yeast is through broken wall, enzymolysis, self-dissolving etc.
Internal nutriment can be discharged after technique, thus having strong fragrance, substantial amounts of nutriment such as small peptide and flavor amino
Acid, free nucleotide, vitamin etc. also can be from internal releases, such that it is able to directly be absorbed by people and animal, therefore from last century
The nineties start, and constantly study in food and field of fodder and carry out broken wall and degraded yeast egg using modes such as enzymolysis, self-dissolvings
White matter, thus produce various yeast autolyzates, extract and extract etc..
Applied well using yeast autolysis technology production yeast autolyzate, yeast extract, food dressing, self-dissolving
Purpose is exactly to obtain to be worth higher product, obtains the higher Dissolve things inside of nutritive value, can produce free nucleosides after yeast autolysis
Acid, small peptide and free amino acid etc., nucleotides has significant delicate flavour and immunologic function, and such as yeast hydrolyate is it is simply that refer to ferment
Female is bacterial classification, and the thalline obtaining through liquid fermentation concentrates after self-dissolving or external source enzymatic hydrolysis or the product that obtain is dried.Ferment
Female hydrolysate has more preferable nutritive value than original yeast in Animal nutrition field.
Existing yeast autolysis is mainly produced using industrial enzymatic vessel, and enzymatic vessel is a kind of dedicated for enzyme digestion reaction
Device, often for enclosed construction, have heating, insulation and agitating function.Enzymatic vessel self-dissolving produce have control accurately, reacted
Entirely, the advantages of technology maturation.
Existing enzymatic vessel produces yeast autolyzate and also has a disadvantage that：
1, the moisture of material is had high demands, enzyme digestion reaction is to carry out in liquid conditions, in order to be sufficiently mixed enzymolysis,
Material needs there is good mobility, and therefore, material moisture generally requires higher than 95%, and otherwise material is too sticky can lead to
Mixing efficiency reduces, or even cannot stir and flow, occluding device.
2, enzymatic vessel produces and is batch type and discontinuous produce, and material needs discharge after react in enzymatic vessel, entering
The production of row next batch.So enzymolysis process is accomplished by multiple enzymatic vessels and is produced side by side.This results in Productive statistics and carries
Height, also improves difficulty to producing control.
3, heat up slowly it is difficult to meet the requirement of ultra-short Time self-dissolving.Because enzymatic vessel is mainly entered by the sleeve of tank body
Row heats up, and the contact area of therefore intensification is only limitted to the circumference of sleeve, which results in material and heats up time-consuming longer, material reaches
The good time from solubility temperature increases, thus reducing production efficiency.
Utility model content
The purpose of this utility model is that the deficiency making up above-mentioned yeast autolysis equipment is defect, provides one kind to be used for yeast
The equipment of self-dissolving.
To achieve these goals, the utility model employs technical scheme below：A kind of yeast autolysis equipment, it includes
One main casing carrying cover plate and at least one Hollow Transmission Shafts carrying hollow blade, cover plate and main casing enclose airtight
Main chamber, main chamber chamber outer wall is provided with cavity steam inlet and cavity steam exhaust-gas mouth, and Hollow Transmission Shafts are longitudinally through described master
Chamber, by the hollow central siphon of mutually disconnected low-temperature zone and the hollow central siphon of high temperature section is coaxially connected forms for Hollow Transmission Shafts, low-temperature zone
Low-temperature zone steam pipe and high temperature section steam pipe is each accommodated, low-temperature zone is empty in the tube chamber of hollow central siphon and the hollow central siphon of high temperature section
Central spindle tube and the hollow central siphon of the high temperature section synchronous axial system by motor-driven, the top of the hollow central siphon of low-temperature zone is provided with charging
Mouthful, the lower section of the hollow central siphon of high temperature section is provided with discharge gate.
Low-temperature zone steam inlet and low-temperature zone steam exhaust-gas mouth are arranged at same one end of the hollow central siphon of low-temperature zone, low-temperature zone
Steam pipe is bendingly arranged at low-temperature zone hollow central siphon tube chamber；High temperature section steam inlet and high temperature section steam exhaust-gas mouth are arranged at
Same one end of the hollow central siphon of high temperature section, high temperature section steam pipe is bendingly arranged at low-temperature zone hollow central siphon tube chamber.
Cover plate lower surface is provided with spray equipment.
The described Hollow Transmission Shafts with hollow blade have two, are arranged side by side in main chamber's inner chamber.
Described blade is helical blade.
Main casing bottom is provided with height and adjusts bearing, and the height of the regulation bearing below the hollow central siphon of high temperature section is low
In the height of the regulation bearing below the hollow central siphon of low-temperature zone, main chamber bottom is 3～10 ° with the angle of horizontal plane.
Main chamber bottom is 3～5 ° with the angle of horizontal plane.
The length of the hollow central siphon of low-temperature zone accounts for the 1/3 to 1/2 of Hollow Transmission Shafts total length.
The cavity wall of main chamber be provided with 4～10 for monitoring from the temperature sensor of solubility temperature.
Compared with the existing technology, advantage is the utility model：
1. the utility model is the continuous mode of production, by continuously stirred and certain inclination angle of blade, material continue from
Toward discharge gate persistent movement, during blade stirring conveying material, material reaches from solubility temperature, according to volume of equipment charging aperture
And the speed of blade rotating speed or material movement, with material throw in speed, blade rotating speed jointly determine material the self-dissolving time it is ensured that
Material movement completes self-dissolving when reaching discharge gate.Therefore, material conveying and self-dissolving are to occur simultaneously.With step enzymatic vessel phase
The production technology of continous way is conducive to preamble, the design of post-order process and steady production to ratio.Can be differently configured from and be mounted in parallel multiple stage
Enzymatic vessel, technique only needs 1 blade self-dissolving equipment, thus decreasing equipment investment and producing control difficulty.
2. the utility model adopts horizontal main body, the mode of built-in double helix blade stirring being stirred, equipment itself
Low to moisture requirement, substantially less than enzymatic vessel.
3. heat up quick, it is heater so that the thermal interface of material that the blade of blade self-dissolving equipment is stirring again
Long-pending to be significantly higher than the mode using cavity heat supply so that material can heat up quickly, compare with enzymatic vessel, during same production
Between, the time that material heats up can substantially reduce.
Brief description
Fig. 1 is front view of the present utility model.
Fig. 2 is the top view of Fig. 1 equipment.
Fig. 3 is the A direction view of Fig. 1.
Wherein, belt wheel 1. reductor 2. travelling gear 3. cover plate, 4. charging aperture 5. low-temperature zone heating hollow blade 6.
Cavity steam inlet 7. high temperature section heats hollow blade 8. temperature sensor, 9. spray equipment 10. cavity steam exhaust-gas mouth
11. overflow plate, 12. discharge gate 13. equipment is entered with horizontal plane angle 14. high temperature section steam exhaust-gas mouth 15. high temperature section steam
Gas port 16. motor, 17. main casing, 18. transmission main shaft, 19. low-temperature zone steam inlet 20. low-temperature zone steam exhaust-gas mouth
21. bearing 22..
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings.It should be appreciated that specific embodiment described herein
Only in order to explain the utility model, do not limit the utility model.
Referring to Fig. 1～Fig. 3, this device includes belt wheel 1, reductor 2, travelling gear 3, cover plate 4, charging aperture 5, low-temperature heat
Hollow blade 6, cavity steam inlet 7, high-temperature heating hollow blade 8, temperature sensor 9, spray equipment 10, cavity steam row
Gas port 11., overflow plate 12, discharge gate 13, high temperature section steam exhaust-gas mouth 15, high temperature section steam inlet 16, motor 17, main casing
Body 18, transmission main shaft 19, low-temperature zone steam inlet 20, low-temperature zone steam exhaust-gas mouth and 21. and. bearing 22 etc..
Cover plate 4 and main casing 18 enclose and are shaped as airtight equipment main chamber, are provided with cavity in the lateral wall of main casing and steam
Vapour air inlet 7, the bottom of main casing are provided with cavity steam exhaust-gas mouth 11.Hollow transmission main shaft 19 has two, abreast longitudinally
It is arranged at main chamber indoor,.By the hollow central siphon of low-temperature zone and the hollow central siphon of high temperature section is coaxially connected forms for each transmission main shaft, and two
Mutually do not connect between the hollow central siphon of section.It is hollow that low-temperature zone steam inlet 20 and low-temperature zone steam exhaust-gas mouth 21 are arranged at low-temperature zone
Same one end of central siphon, it is hollow that low-temperature zone steam pipe enters low-temperature zone hollow central siphon arrival low-temperature zone from low-temperature zone steam inlet 20
Then the most end of central siphon turns back, and stretches out from low-temperature zone steam exhaust-gas mouth 21.Similarly, high temperature section steam inlet 16 and high temperature section
Steam exhaust-gas mouth 15 is arranged at same one end of the hollow central siphon of high temperature section, and high temperature section steam pipe enters from high temperature section steam inlet 16
The hollow central siphon of high temperature section reaches the most end of the hollow central siphon of high temperature section and then turns back, and stretches out from high temperature section steam exhaust-gas mouth 21.Preferably
Ground, the length of the hollow central siphon of low-temperature zone accounts for the 1/3 to 1/2 of Hollow Transmission Shafts total length, and remaining is the hollow central siphon of high temperature section.Low-temperature zone
The top of hollow central siphon is provided with charging aperture 5, and the lower section of the hollow central siphon of high temperature section is provided with discharge gate 13.Power transmission shaft periphery is arranged
There is helical blade.Transmission main shaft one end connects travelling gear 3, and travelling gear 3 is engaged with reductor 2 gear of output end, slows down
Machine 2 input connects motor output end by belt wheel, and the transmission main shaft other end connects steam and imports and exports.Wherein one end and motor
17 and reductor 2 connected by travelling gear, drive transmission main shaft to rotate by motor and reductor.
The lower surface of cover plate 4 is provided with multiple spray equipments 10.During production, the shower nozzle of low-temperature zone can spray exogenous enzymes with
Improve enzymolysis efficiency.
Main casing bottom is provided with height and adjusts bearing 22, the height of the regulation bearing below the hollow central siphon of high temperature section
Less than the height of the regulation bearing below the hollow central siphon of low-temperature zone, the angle that makes main chamber bottom and horizontal plane is 3～
10 °, preferably 3～5 °.Certainly, main chamber bottom can also be by the ground line gradient residing for equipment Lai real with the angle of horizontal plane
Existing.
The cavity wall of main chamber is provided with 4～10 temperature sensors, for monitoring from solubility temperature.Low-temperature zone uses 0.2-
The steam of 0.4Mpa pressure is heated, and the temperature being shown using the temperature sensor of low-temperature zone is adjusting steam pressure.High temperature
Section is heated using the steam of 0.5-0.6Mpa pressure, and the temperature being shown using the temperature sensor of high temperature section is adjusting steam
Pressure.
Material starts to warm up after charging aperture access arrangement, and the temperature controlling range of low-temperature zone is 45 DEG C～60 DEG C, thing
The temperature controlling range that material enters high temperature section is 75 DEG C～95 DEG C.
The material self-dissolving time is controlled with feed rate by the volume of hollow blade chamber, by equipment and horizontal plane
3 °～5 ° inclination angles are accelerating and to improve the mobile performance of material.
Material low-temperature zone time control at 20～60 minutes, material should be maintained at 30 in high temperature section residence time～
120 minutes.Device Host is provided with overflow plate near discharge gate.Main casing bottom is provided with discharge gate.Overflow is overflowed after material self-dissolving
Plate, is delivered to subsequent processing by discharge gate.
After production terminates, equipment all of spray equipment spray disinfectant and clear water, carry out disinfection cleaning to equipment.Use
The comparison of enzymatic vessel and blade self-dissolving equipment comparison production of the present utility model and result see table 1：
Table 1：Two kinds of self-dissolving equipment produce contrast
As seen from the table, its effect is significant is better than enzymatic vessel.
Claims (9)
1. a kind of yeast autolysis equipment it is characterised in that：It include one carry the main casing of cover plate and at least one carry hollow
The Hollow Transmission Shafts of paddle, cover plate and main casing enclose airtight main chamber, and main chamber chamber outer wall is provided with cavity steam inlet
And cavity steam exhaust-gas mouth, longitudinally through main chamber room, Hollow Transmission Shafts are empty by mutually disconnected low-temperature zone for Hollow Transmission Shafts
The central spindle tube and hollow central siphon of high temperature section is coaxially connected forms, in the tube chamber of the hollow central siphon of low-temperature zone and the hollow central siphon of high temperature section each
Accommodate low-temperature zone steam pipe and high temperature section steam pipe, the hollow central siphon of low-temperature zone and the hollow central siphon of high temperature section are by motor-driven
Synchronous axial system, the top of the hollow central siphon of low-temperature zone is provided with charging aperture, and the lower section of the hollow central siphon of high temperature section is provided with discharge gate.
2. yeast autolysis equipment according to claim 1 it is characterised in that：Low-temperature zone steam inlet and low-temperature zone steam
Exhaust outlet is arranged at same one end of the hollow central siphon of low-temperature zone, and low-temperature zone steam pipe is bendingly arranged at low-temperature zone hollow central siphon pipe
Chamber；High temperature section steam inlet and high temperature section steam exhaust-gas mouth are arranged at same one end of the hollow central siphon of high temperature section, high temperature section steam
Pipe is bendingly arranged at low-temperature zone hollow central siphon tube chamber.
3. yeast autolysis equipment according to claim 1 it is characterised in that：Cover plate lower surface is provided with spray equipment.
4. yeast autolysis equipment according to claim 1 it is characterised in that：The described Hollow Transmission Shafts with hollow blade
There are two, be arranged side by side in main chamber's inner chamber.
5. yeast autolysis equipment according to claim 4 it is characterised in that：Described blade is helical blade.
6. yeast autolysis equipment according to claim 1 it is characterised in that：Main casing bottom is provided with height regulation
Seat, the height positioned at the regulation bearing below the hollow central siphon of high temperature section is less than the regulation bearing below the hollow central siphon of low-temperature zone
Height, the angle of main chamber bottom and horizontal plane is 3～10 °.
7. yeast autolysis equipment according to claim 6 it is characterised in that：Main chamber bottom is 3 with the angle of horizontal plane
～5 °.
8. yeast autolysis equipment according to claim 1 it is characterised in that：The length duty heart of the hollow central siphon of low-temperature zone passes
The 1/3 to 1/2 of moving axis total length.
9. yeast autolysis equipment according to claim 1 it is characterised in that：The cavity wall of main chamber is provided with 4～10 use
In monitoring from the temperature sensor of solubility temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620726694.1U CN205954016U (en) | 2016-07-08 | 2016-07-08 | Yeast self -dissolving equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620726694.1U CN205954016U (en) | 2016-07-08 | 2016-07-08 | Yeast self -dissolving equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205954016U true CN205954016U (en) | 2017-02-15 |
Family
ID=57971453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620726694.1U Active CN205954016U (en) | 2016-07-08 | 2016-07-08 | Yeast self -dissolving equipment |
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| Country | Link |
|---|---|
| CN (1) | CN205954016U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107083295A (en) * | 2017-06-12 | 2017-08-22 | 沈晨 | One primary yeast uniform spraying device |
-
2016
- 2016-07-08 CN CN201620726694.1U patent/CN205954016U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107083295A (en) * | 2017-06-12 | 2017-08-22 | 沈晨 | One primary yeast uniform spraying device |
| CN107083295B (en) * | 2017-06-12 | 2020-06-09 | 山西涌泉香醋业股份有限公司 | Even sprinkler of yeast |
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