CN210215388U - Alcohol production saccharification adds enzyme mixing arrangement - Google Patents
Alcohol production saccharification adds enzyme mixing arrangement Download PDFInfo
- Publication number
- CN210215388U CN210215388U CN201920597596.6U CN201920597596U CN210215388U CN 210215388 U CN210215388 U CN 210215388U CN 201920597596 U CN201920597596 U CN 201920597596U CN 210215388 U CN210215388 U CN 210215388U
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- cylinder
- nozzle pipe
- alcohol production
- nozzle
- saccharification
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Abstract
The utility model provides an alcohol production saccharification adds enzyme mixing arrangement, include: the device comprises a cylinder, a motor and a speed reducer which are sequentially connected with the upper end of the cylinder, a discharge hole at the upper end of the side wall of the cylinder, and a feed hole at the lower end of the cylinder; an output shaft of the speed reducer penetrates into the cylinder body, and a push type stirrer and a mixed flow type stirrer are sequentially arranged on the output shaft from top to bottom; the lower end of the cylinder body is provided with a nozzle pipe sleeved outside the feed inlet, the side wall of the nozzle pipe is provided with an enzyme metering inlet, and the rear end of the nozzle pipe is provided with a mash nozzle led into the nozzle pipe; the utility model discloses the combination formula agitator that multiple stirring leaf is constituteed plays transport and mixing action on the one hand, and the preceding low pressure material continuous flow of pulling prevents to appear gluing thick mash and blocks up the pipeline on the one hand, and mixing efficiency is high, mixing time is short, shortens diastase mixing time for whole saccharification efficiency shortens the equipment flow, guarantees alcohol fermentation effect when being suitable for no saccharification technology.
Description
Technical Field
The utility model relates to an alcohol production facility technical field particularly, relates to an alcohol production saccharification adds enzyme mixing arrangement.
Background
In the alcohol production process, the mash material after liquefaction needs a saccharification technology, a large mixing tank is needed for the traditional saccharification technology, a mixing agent such as saccharifying enzyme is added into the mixing tank, starch in the material is converted into glucose, half hour of saccharification time is needed after mixing, the time is long, but the existing saccharification device causes poor mixing effect of the enzyme and the material, and the effect of rapid saccharification is difficult to meet.
SUMMERY OF THE UTILITY MODEL
The utility model discloses just based on at least one of above-mentioned technical problem, provided a new alcohol production saccharification and added enzyme mixing arrangement for whole saccharification efficiency shortens equipment flow.
In view of this, the utility model provides an alcohol production saccharification adds enzyme mixing arrangement, include: the device comprises a cylinder, a motor and a speed reducer which are sequentially connected with the upper end of the cylinder, a discharge hole at the upper end of the side wall of the cylinder, and a feed hole at the lower end of the cylinder; an output shaft of the speed reducer penetrates into the cylinder body, and a push type stirrer and a mixed flow type stirrer are sequentially arranged on the output shaft from top to bottom; the lower end of the cylinder body is provided with a nozzle pipe sleeved outside the feed inlet, the side wall of the nozzle pipe is provided with an enzyme metering inlet, and the rear end of the nozzle pipe is provided with a mash nozzle introduced into the nozzle pipe.
Preferably, the propeller-type stirrer is a variable cross-section propeller-type stirrer, and the number of the variable cross-section propeller-type stirrers is at least two.
Preferably, the mixed-flow stirrer is a six-blade disc turbine stirrer.
Preferably, the mash nozzle tip is higher than the enzyme metering inlet.
Preferably, the lower end of the feed inlet is a flared opening with a large opening facing outwards.
The utility model has the advantages that: through above technical scheme, with enzyme liquid suction system, practice thrift conveying equipment power energy consumption, the combination formula agitator that multiple stirring leaf is constituteed plays transport and mixing action on the one hand, and the preceding low pressure material continuous flow of pulling prevents to appear glues thick mash and blocks up the pipeline on the one hand, and mixing efficiency is high, mixing time is short, shortens diastase mix time for whole saccharification efficiency, shortens the equipment flow, guarantees the alcohol fermentation effect when being suitable for no saccharification technology.
Drawings
FIG. 1 shows a schematic diagram of an alcohol production saccharification plus enzyme mixing device according to an embodiment of the present invention;
in the figure: 1 is a cylinder, 2 is a motor, 3 is a reducer, 4 is a discharge port, 5 is a feed port, 6 is an output shaft, 7 is a propulsion stirrer, 8 is a mixed flow stirrer, 9 is a nozzle pipe, 10 is an enzyme metering inlet, and 11 is a mash nozzle.
Detailed Description
In order to make the aforementioned objects, features and advantages of the present invention more clearly understood, the present invention will be described in further detail with reference to the accompanying drawings and detailed description. It should be noted that the embodiments and features of the embodiments of the present application may be combined with each other without conflict.
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention, however, the present invention may be practiced in other ways than those specifically described herein, and therefore the scope of the present invention is not limited by the specific embodiments disclosed below.
As shown in figure 1, the utility model provides an alcohol production saccharification adds enzyme mixing arrangement, include: the device comprises a cylinder body 1, a motor 2 and a speed reducer 3 which are sequentially connected with the upper end of the cylinder body 1, a discharge port 4 at the upper end of the side wall of the cylinder body 1, and a feed port 5 at the lower end of the cylinder body 1; an output shaft 6 of the speed reducer 3 penetrates into the barrel 1, and a push type stirrer 7 and a mixed flow type stirrer 8 are sequentially arranged on the output shaft 6 from top to bottom; the lower end of the cylinder body 1 is provided with a nozzle pipe 9 which is sleeved outside the feed inlet 5, the diameter of the nozzle pipe 9 is larger than that of the feed inlet 5, the side wall of the nozzle pipe 9 is provided with an enzyme metering inlet 10, the rear end of the nozzle pipe 9 is provided with a mash nozzle 11 which is introduced into the nozzle pipe, the rear end of the mash nozzle 11 is provided with a baffle plate to seal the nozzle pipe 9, so that a Venturi nozzle is formed, saccharifying enzymes can conveniently enter the cylinder body 1 from the enzyme metering inlet 10, the propelling type stirrer 7 is a variable cross-section spiral arc blade type stirrer (CBY blade), the number of the variable cross-section spiral arc blade type stirrers is at least two, the mixed flow type stirrer 8 is a six-folded blade disc turbine type stirrer, the materials and the enzymes are fully mixed due to residues in the materials, the propelling type stirrer 7 pushes the mixtures out from the discharge port 4, the top end of the mash nozzle 11 is higher than the enzyme metering inlet 10, and.
Above combine the figure detail to describe the technical scheme of the utility model, the utility model discloses a technical scheme provides a new alcohol production saccharification adds enzyme mixing arrangement, with enzyme liquid suction system, practice thrift conveying equipment power energy consumption, the combination formula agitator that multiple stirring leaf is constituteed plays transport and mixing action on the one hand, the preceding low pressure material continuous flow of pulling prevents to appear gluing thick mash and blocks up the pipeline on the one hand, mixing efficiency is high, mixing time is short, shorten the diastatic enzyme mixing time, accelerate whole saccharification efficiency, shorten equipment flow, guarantee alcohol fermentation effect when being suitable for no saccharification technology.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (5)
1. An alcohol production saccharification adds enzyme mixing arrangement which characterized in that includes: the device comprises a cylinder, a motor and a speed reducer which are sequentially connected with the upper end of the cylinder, a discharge hole at the upper end of the side wall of the cylinder, and a feed hole at the lower end of the cylinder; an output shaft of the speed reducer penetrates into the cylinder body, and a push type stirrer and a mixed flow type stirrer are sequentially arranged on the output shaft from top to bottom; the lower end of the cylinder body is provided with a nozzle pipe sleeved outside the feed inlet, the side wall of the nozzle pipe is provided with an enzyme metering inlet, and the rear end of the nozzle pipe is provided with a mash nozzle introduced into the nozzle pipe.
2. The alcohol production saccharification plus enzyme mixing device of claim 1, characterized in that: the propelling type stirrer is a variable cross-section propeller type stirrer, and the number of the variable cross-section propeller type stirrers is at least two.
3. The alcohol production saccharification plus enzyme mixing device of claim 1, characterized in that: the mixed-flow stirrer is a six-blade disc turbine stirrer.
4. The alcohol production saccharification plus enzyme mixing device of claim 1, characterized in that: the top end of the mash nozzle is higher than the enzyme metering inlet.
5. The alcohol production saccharification plus enzyme mixing device of claim 1, characterized in that: the lower end of the feed inlet is a horn mouth with a large opening facing outwards.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201920597596.6U CN210215388U (en) | 2019-04-28 | 2019-04-28 | Alcohol production saccharification adds enzyme mixing arrangement |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201920597596.6U CN210215388U (en) | 2019-04-28 | 2019-04-28 | Alcohol production saccharification adds enzyme mixing arrangement |
Publications (1)
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CN210215388U true CN210215388U (en) | 2020-03-31 |
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CN201920597596.6U Expired - Fee Related CN210215388U (en) | 2019-04-28 | 2019-04-28 | Alcohol production saccharification adds enzyme mixing arrangement |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115232708A (en) * | 2022-07-18 | 2022-10-25 | 鲍兴权 | Sewage discharge system for edible alcohol saccharified mash and fermented mash |
-
2019
- 2019-04-28 CN CN201920597596.6U patent/CN210215388U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115232708A (en) * | 2022-07-18 | 2022-10-25 | 鲍兴权 | Sewage discharge system for edible alcohol saccharified mash and fermented mash |
CN115232708B (en) * | 2022-07-18 | 2023-03-28 | 鲍兴权 | Sewage discharge system for edible alcohol saccharified mash and fermented mash |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200331 Termination date: 20210428 |
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CF01 | Termination of patent right due to non-payment of annual fee |