CN203613175U - Rotary solid bioreactor - Google Patents
Rotary solid bioreactor Download PDFInfo
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- CN203613175U CN203613175U CN201320716126.XU CN201320716126U CN203613175U CN 203613175 U CN203613175 U CN 203613175U CN 201320716126 U CN201320716126 U CN 201320716126U CN 203613175 U CN203613175 U CN 203613175U
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- cylindrical shell
- pipe
- valve
- convolution
- cylinder body
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
- A61L2/04—Heat
- A61L2/06—Hot gas
- A61L2/07—Steam
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Abstract
The utility model relates to a rotary solid bioreactor, which comprises a cylinder body, a gas inlet/outlet system and a temperature control system, wherein the cylinder body is sequentially composed of an inner cylinder body and a heat insulation layer from inside to outside; a cavity between the inner cylinder body and the heat insulation layer forms a jacket; a feeding opening is formed in the upper end of the cylinder body; an inoculating pipe is arranged on an end cover of the feeding opening, and a spraying device is arranged at the top of the inoculating pipe; a discharging opening is formed in the lower end of the cylinder body; the opening/closing of the discharging opening is controlled by a butterfly valve; the two ends of the cylinder body are respectively fixed on a machine frame; a motor drives the cylinder body to rotate around the machine frame through a conveyor belt or a chain. Via arranging the feeding opening, the discharging opening and the inoculating pipe on the cylinder body and arranging the independent gas inlet/outlet system and the temperature control system, the rotary solid bioreactor integrates functions of mixing, steam sterilization, cooling, inoculating, automatic fermenting, vacuum drying and the like, and promotes the solid biologic brewing technique to develop towards a trend of large scale, high efficiency and high product quality.
Description
Technical field
The utility model relates to fermentation industry field, particularly a kind of bipyramid convolution solid bio-reactor.
Background technology
Solid bio-reactor is the key equipment in solid-state fermentation technology, and at present solid bio-reactor exists fermenting process easily by series of problems such as mixing of materials inequality in living contaminants, fermenting process, heat radiation difficulty, ventilation are not smooth.Domestic main or with traditional open in the majority in this respect, can not avoid living contaminants.Compared with modern solid bio-reactor, as common drum type bioreactor, rotary shaft bio-reactor face, discharging difficulty, power consumption are large, ventilation is smooth, mix inhomogeneous shortcoming; and reactor volume is little, amplify difficulty, be not suitable for modern brewing technique to mass-producing, efficient and realize the high-quality future development of product.
Utility model content
The purpose of this utility model is that a kind of bipyramid that integrates the several functions such as batch mixing, steam sterilizing, cooling, inoculation, fermentation automatically, vacuum-drying solid bio-reactor that circles round is provided in order to address the above problem.
In order to achieve the above object, the technical scheme that the utility model is taked is: a kind of convolution solid bio-reactor, comprise cylindrical shell, air inlet system and exhaust system and temperature control system, it is characterized in that, described cylindrical shell is made up of inner barrel and thermal insulation layer from inside to outside successively, and the cavity between described inner barrel and thermal insulation layer forms chuck, and described cylindrical shell upper end is provided with opening for feed, the end cap of described opening for feed is provided with inoculated tube, and the top of described inoculated tube is provided with spray equipment; Described cylindrical shell lower end is provided with discharge port, and by the switch of discharge port described in butterfly valve control, the two ends of described cylindrical shell are separately fixed in frame, and motor rotates around frame by cylindrical shell described in travelling belt or chain-driving.
In such scheme, in described cylindrical shell, be provided with central shaft, described central shaft is fixed on the two ends of described cylindrical shell by bearing; On described central shaft, be fixed with rake teeth, central shaft does not rotate with the rotation of cylindrical shell like this, in the time of barrel body rotation, can realize the secondary stirring to material, solves material caking and mixes inhomogeneous problem.
Further, described rake teeth is welded on described central shaft.
Further, described cylindrical shell is the tapered cylindrical shells in two ends.
In such scheme, described air inlet system and exhaust system comprise sterile air inlet pipe, vapor pipe and right rotation joint, described right rotation jiont treatment is on the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe and described vapor pipe are inserted into described cylinder lumen by described right rotation joint from the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe is inlet mouth at the port of described cylinder lumen, in the inlet ductwork of described sterile air inlet pipe, be parallel with vacuum pump, described vapor pipe is air outlet at the port of described cylinder lumen.
Further, described sterile air inlet pipe is provided with intake valve, and the pipeline between described sterile air inlet pipe and described vacuum pump is provided with vacuum pumping valve, is provided with successively tensimeter and vent valve on described vapor pipe.
In such scheme, described temperature control system comprises steam inlet pipe, blow-off pipe and anticlockwise joint, described anticlockwise jiont treatment is on the turning axle of described cylindrical shell left end, and described steam inlet pipe and described blow-off pipe are inserted into the cavity of described chuck from the turning axle of described cylindrical shell left end by described anticlockwise joint.
Further, described steam inlet pipe is provided with steam valve, and described blow-off pipe is provided with wash water valve.
In such scheme, the break-make of described intake valve, described vent valve, described steam valve, described wash water valve, described vacuum pumping valve and described motor is controlled by automatic control system.
Technique effect of the present utility model: by opening for feed, discharge port and inoculated tube are set on cylindrical shell; and independent air inlet system and exhaust system and temperature control system be set; realized several functions such as integrating batch mixing, steam sterilizing, cooling, inoculation, fermentation automatically, vacuum-drying, promoted solid-state biological brewed technology to mass-producing, efficiently and realize the high-quality future development of product.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is that A in Fig. 1 is to structural representation.
In figure, 1, automatic control system 2, steam inlet pipe 3, steam valve 4, blow-off pipe 5, wash water valve 6, frame 7, anticlockwise joint 8, sterile air inlet pipe 9, intake valve 10, inoculated tube 11, opening for feed 12, bearing 13, inner barrel 14, chuck 15, thermal insulation layer 16, spray equipment 17, rake teeth 18, central shaft 19, air outlet 20, inlet mouth 21, temperature sensor 22, discharge port 23, butterfly valve 24, chain 25, motor 26, right rotation joint 27, tensimeter 28, vent valve 29, vapor pipe 30, vacuum pumping valve 31, vacuum pump.
Embodiment
Further describe the utility model below in conjunction with accompanying drawing.
A kind of bipyramid convolution solid bio-reactor, comprise cylindrical shell, air inlet system and exhaust system and temperature control system, described cylindrical shell two ends are tapered, described cylindrical shell is made up of inner barrel 13 and thermal insulation layer 15 from inside to outside successively, cavity between described inner barrel 13 and thermal insulation layer 15 forms chuck 14, described cylindrical shell upper end is provided with opening for feed 11, and the end cap of described opening for feed 11 is provided with inoculated tube 10, and the top of described inoculated tube 10 is provided with spray equipment; Described cylindrical shell lower end is provided with discharge port 22, is controlled the switch of described discharge port 22 by butterfly valve 23, and the two ends of described cylindrical shell are separately fixed in frame 6, and motor 25 rotates around frame 6 by cylindrical shell described in travelling belt or chain-driving.In described cylindrical shell, be provided with central shaft 18, described central shaft 18 is fixed on the two ends of described cylindrical shell by bearing 12; On described central shaft, be welded with strip rake teeth 17, central shaft 18 does not rotate with the rotation of cylindrical shell like this, in the time of barrel body rotation, can realize the secondary stirring to material, solves material caking and mixes inhomogeneous problem.Described air inlet system and exhaust system comprise sterile air inlet pipe 8, vapor pipe 29 and right rotation joint 26, described right rotation joint 26 is arranged on the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe 8 and described vapor pipe 29 are inserted into described cylinder lumen by described right rotation joint 26 from the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe 8 is inlet mouth 20 at the port of described cylinder lumen, in the inlet ductwork of described sterile air inlet pipe 8, be parallel with vacuum pump 31, described vapor pipe 29 is air outlet 19 at the port of described cylinder lumen.Described sterile air inlet pipe 8 is provided with intake valve 9, and the pipeline between described sterile air inlet pipe 8 and described vacuum pump 31 is provided with vacuum pumping valve 30, is provided with successively tensimeter 27 and vent valve 28 on described vapor pipe 29.Described temperature control system comprises steam inlet pipe 2, blow-off pipe 4 and anticlockwise joint 7, described anticlockwise joint 7 is arranged on the turning axle of described cylindrical shell left end, and described steam inlet pipe 2 and described blow-off pipe 4 are inserted into the cavity of described chuck 14 from the turning axle of described cylindrical shell left end by described anticlockwise joint 7.Described steam inlet pipe 2 is provided with steam valve 3, and described blow-off pipe 4 is provided with wash water valve 5.The break-make of described intake valve 9, described vent valve 28, described steam valve 3, described wash water valve 5, described vacuum pumping valve 30 and described motor 25 is controlled by automatic control system 1.
The concrete operations principle of air inlet system and exhaust system is: sterile air enters into tank body from sterile air inlet pipe 8 by intake valve 9 and inlet mouth 20.Inlet mouth 20 is the cylinder of sealing, and it is 1-5mm aperture that surface is equipped with intensive diameter, at inlet mouth 20 cylinder outer cover last layer 100-500 object filter clothes, prevents that material from entering inlet mouth 20.The air that enters tank body is discharged tank body by venting port, vent valve, vapor pipe, and venting port is the cylinder of sealing, and it is 1-5mm aperture that surface is equipped with intensive diameter, at inlet mouth cylinder outer cover last layer 100-500 object filter cloth, prevents that material from entering air outlet 19.Air intake-exhaust system realizes aperture, adjusting air inflow quantity and the tank pressure to intake valve 9 and vent valve 28 by Controlling System 1 manually or automatically.
The concrete operations principle of temperature control system is: before fermentation, steam valve 3 is opened, and steam enters chuck 14 material is carried out to sterilizing, and the water of condensation producing when sterilizing is discharged by wash water valve 5, blow-off pipe 4.In the time of sterilizing, open and close the material in cylindrical shell is carried out to sterilizing by controlling steam valve 3 and wash water valve 5, steam can not enter in cylindrical shell, on the humidity of material almost without affecting.
After sterilizing finishes, steam valve 3 is opened, and passes into water coolant at steam inlet pipe 2, and the material of the bacterium of having gone out is lowered the temperature, and water coolant is discharged by wash water valve 5, blow-off pipe 4.Meanwhile, sterile air enters by sterile air inlet pipe 8, inlet mouth 20, and tank body is carried out to pressurize and cooling, and air is discharged by air outlet 19, vent valve 28, vapor pipe 29.Detect temperature in cylindrical shell by the temperature sensor 21 in tank body.
After material sterilizing cooling, open inoculated tube 10, inoculate by spray equipment 16.During the fermentation, steam valve 3 is opened, and automatically passes into thermostat(t)ed water at steam inlet pipe 2, and the material of the bacterium of having gone out is carried out to constant temperature, and thermostat(t)ed water backwater is discharged by wash water valve 5, blow-off pipe 4, realizes the temperature of fermentation materials is controlled automatically.After fermentation ends, steam constant temperature water valve 3 is opened, and steam enters chuck 14, and the water of condensation of generation is discharged by wash water valve 5, blow-off pipe 4, and to heating material, the material vacuumizing having fermented by vacuum pumping valve 30 and vacuum pump 31 carries out vacuum-drying.More than control and can automatically control or manually control by automatic control system 1.
Claims (10)
1. a convolution solid bio-reactor, comprise cylindrical shell, air inlet system and exhaust system and temperature control system, it is characterized in that, described cylindrical shell is made up of inner barrel (13) and thermal insulation layer (15) from inside to outside successively, cavity between described inner barrel (13) and thermal insulation layer (15) forms chuck (14), described cylindrical shell upper end is provided with opening for feed (11), and the end cap of described opening for feed (11) is provided with inoculated tube (10), and the top of described inoculated tube (10) is provided with spray equipment; Described cylindrical shell lower end is provided with discharge port (22), is controlled the switch of described discharge port (22) by butterfly valve (23), and it is upper that the two ends of described cylindrical shell are separately fixed at frame (6), and motor (25) rotates around frame (6) by cylindrical shell described in travelling belt or chain-driving.
2. a kind of convolution solid bio-reactor according to claim 1, is characterized in that, in described cylindrical shell, be provided with central shaft (18), described central shaft (18) is fixed on the two ends of described cylindrical shell by bearing (12); On described central shaft, be fixed with rake teeth (17).
3. a kind of convolution solid bio-reactor according to claim 2, is characterized in that, described rake teeth (17) is welded on described central shaft (18).
4. according to the one convolution solid bio-reactor described in any one claim in claim 1-3, it is characterized in that, described cylindrical shell is the tapered cylindrical shells in two ends.
5. a kind of convolution solid bio-reactor according to claim 1, it is characterized in that, described air inlet system and exhaust system comprise sterile air inlet pipe (8), vapor pipe (29) and right rotation joint (26), described right rotation joint (26) is arranged on the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe (8) and described vapor pipe (29) are inserted into described cylinder lumen by described right rotation joint (26) from the turning axle of described cylindrical shell right-hand member, described sterile air inlet pipe (8) is inlet mouth (20) at the port of described cylinder lumen, in the inlet ductwork of described sterile air inlet pipe (8), be parallel with vacuum pump (31), described vapor pipe (29) is air outlet (19) at the port of described cylinder lumen.
6. a kind of convolution solid bio-reactor according to claim 5, it is characterized in that, described sterile air inlet pipe (8) is provided with intake valve (9), pipeline between described sterile air inlet pipe (8) and described vacuum pump (31) is provided with vacuum pumping valve (30), is provided with successively tensimeter (27) and vent valve (28) on described vapor pipe (29).
7. a kind of convolution solid bio-reactor according to claim 1, it is characterized in that, described temperature control system comprises steam inlet pipe (2), blow-off pipe (4) and anticlockwise joint (7), described anticlockwise joint (7) is arranged on the turning axle of described cylindrical shell left end, and described steam inlet pipe (2) and described blow-off pipe (4) are inserted into the cavity of described chuck (14) from the turning axle of described cylindrical shell left end by described anticlockwise joint (7).
8. a kind of convolution solid bio-reactor according to claim 7, is characterized in that, described steam inlet pipe (2) is provided with steam valve (3), and described blow-off pipe (4) is provided with wash water valve (5).
9. a kind of convolution solid bio-reactor according to claim 6, is characterized in that, the break-make of described intake valve (9), described vent valve (28), described vacuum pumping valve (30) and described motor (25) is controlled by automatic control system (1).
10. a kind of convolution solid bio-reactor according to claim 8, is characterized in that, the break-make of described steam valve (3), described wash water valve (5) and described motor (25) is controlled by automatic control system (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320716126.XU CN203613175U (en) | 2013-11-14 | 2013-11-14 | Rotary solid bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320716126.XU CN203613175U (en) | 2013-11-14 | 2013-11-14 | Rotary solid bioreactor |
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| Publication Number | Publication Date |
|---|---|
| CN203613175U true CN203613175U (en) | 2014-05-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201320716126.XU Expired - Fee Related CN203613175U (en) | 2013-11-14 | 2013-11-14 | Rotary solid bioreactor |
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| CN (1) | CN203613175U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107164225A (en) * | 2017-06-12 | 2017-09-15 | 福州法莫优科机械科技有限公司 | Solid bacterium Slag treatment device and its application method |
| CN113587583A (en) * | 2021-09-27 | 2021-11-02 | 苏州锦艺新材料科技有限公司 | Double-cylinder processing mechanism for producing silicon micropowder |
| CN114134035A (en) * | 2021-12-10 | 2022-03-04 | 普瑞特机械制造股份有限公司 | Rotary heating equipment for screening yeast powder |
| CN114164069A (en) * | 2021-12-10 | 2022-03-11 | 普瑞特机械制造股份有限公司 | Yeast powder screening system |
-
2013
- 2013-11-14 CN CN201320716126.XU patent/CN203613175U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107164225A (en) * | 2017-06-12 | 2017-09-15 | 福州法莫优科机械科技有限公司 | Solid bacterium Slag treatment device and its application method |
| CN113587583A (en) * | 2021-09-27 | 2021-11-02 | 苏州锦艺新材料科技有限公司 | Double-cylinder processing mechanism for producing silicon micropowder |
| CN113587583B (en) * | 2021-09-27 | 2022-01-25 | 苏州锦艺新材料科技有限公司 | Double-cylinder processing mechanism for producing silicon micropowder |
| CN114134035A (en) * | 2021-12-10 | 2022-03-04 | 普瑞特机械制造股份有限公司 | Rotary heating equipment for screening yeast powder |
| CN114164069A (en) * | 2021-12-10 | 2022-03-11 | 普瑞特机械制造股份有限公司 | Yeast powder screening system |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140528 Termination date: 20171114 |
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| CF01 | Termination of patent right due to non-payment of annual fee |