CN217202774U - Continuous enzymolysis device of concentrated oat pulp - Google Patents
Continuous enzymolysis device of concentrated oat pulp Download PDFInfo
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- CN217202774U CN217202774U CN202123208507.0U CN202123208507U CN217202774U CN 217202774 U CN217202774 U CN 217202774U CN 202123208507 U CN202123208507 U CN 202123208507U CN 217202774 U CN217202774 U CN 217202774U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
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Abstract
The utility model provides a continuous enzymolysis device of thick liquid of oat, it includes former thick liquid jar, first thermoregulation mechanism, first enzyme jar, first coil pipe, second thermoregulation mechanism, second add enzyme jar, second coil pipe and finished product jar, wherein: the raw slurry tank is used for storing oat slurry; the feed inlet and the magma jar of first thermoregulation mechanism are connected, and first thermoregulation mechanism's discharge gate and first coiled pipe are connected, and first thermoregulation mechanism makes oat thick liquid reach the liquefaction temperature, and first enzyme jar that adds is used for implementing the enzyme that adds to oat thick liquid, and oat thick liquid is in first coiled pipe accomplishes the liquefaction. The feed inlet of a second temperature adjusting mechanism is connected with the first coil pipe, the discharge outlet of the second temperature adjusting mechanism is connected with the second coil pipe, the second temperature adjusting mechanism is used for heating the oat pulp to enable the oat pulp to reach the saccharification temperature, the second enzyme adding tank is used for adding enzyme to the oat pulp, and the oat pulp is saccharified in the second coil pipe. The utility model discloses carry out liquefaction and saccharification to the oat slurry stage by stage, in succession, promoted the enzymolysis effect of oat slurry.
Description
Technical Field
The utility model belongs to the technical field of food processing and specifically relates to a thick liquid continuous enzymolysis device of oat.
Background
The traditional grain enzymolysis mode is usually batch centralized treatment, namely multiple enzymolysis links such as liquefaction, saccharification and the like are completed in the same enzymolysis tank. However, different enzymolysis links have different requirements on temperature, and the problem of lagging temperature regulation is inevitably caused by adopting the same enzymolysis tank to implement a plurality of enzymolysis links, so that the accurate control of the whole enzymolysis process is difficult to implement, and the enzymolysis effect is finally influenced.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model provides a continuous enzymolysis device of oat dense slurry, its concrete technical scheme as follows:
the utility model provides a thick continuous enzymolysis device of thick liquid of oat, its includes former thick liquid jar, first temperature regulating mechanism, first enzyme jar, first coil pipe, second temperature regulating mechanism, second add enzyme jar, second coil pipe and finished product jar, wherein:
the primary pulp tank is used for storing oat pulp to be subjected to enzymolysis;
the feed inlet of the first temperature regulating mechanism is connected with the discharge outlet of the raw slurry tank through a first pipeline, the discharge outlet of the first temperature regulating mechanism is connected with the feed inlet of the first coil pipe through a second pipeline, the first enzyme adding tank is connected to the second pipeline, the first temperature regulating mechanism is used for heating the oat slurry to enable the oat slurry to reach the liquefaction temperature, the first enzyme adding tank is used for adding enzyme to the oat slurry for the first time, and the liquefaction of the oat slurry added with enzyme for the first time in the first coil pipe is completed;
the feeding hole of the second temperature adjusting mechanism is connected with the discharging hole of the first coil pipe through a third pipeline, the discharging hole of the second temperature adjusting mechanism is connected with the feeding hole of the second coil pipe through a fourth pipeline, the second enzyme adding tank is connected to the fourth pipeline, the second temperature adjusting mechanism is used for heating the oat slurry to enable the oat slurry to reach the saccharification temperature, the second enzyme adding tank is used for adding enzyme to the oat slurry for the second time, and the saccharification of the oat slurry added with enzyme for the second time is completed in the second coil pipe;
the feed inlet of finished product jar through the fifth pipeline with the discharge gate of second coil pipe is connected, the finished product jar is used for storing the concentrated thick liquid of oat.
In some embodiments, it further comprises a drive pump connected to the first conduit.
In some embodiments, the drive pump is a variable frequency rotary pump.
In some embodiments, the first temperature regulating mechanism and the second temperature regulating mechanism are both plate heat exchangers.
In some embodiments, the feed port of the first enzyme adding tank is provided with a first flow meter.
In some embodiments, the feed port of the second enzyme addition tank is provided with a second flow meter.
The utility model provides a continuous enzymolysis device of thick liquid of oat, first mechanism that adjusts the temperature, first enzyme jar and the first coil pipe of adding mutually support to implement the liquefaction to the thick liquid of oat, second mechanism, the second that adjusts the temperature adds enzyme jar, the second coil pipe mutually supports, in order to implement the saccharification to the thick liquid of oat. Compare with traditional batch centralized processing mode, the utility model discloses stage by stage, implement liquefaction and saccharification to the oat pulp in succession to realized the accurate temperature control of liquefaction, saccharification, thereby promoted the enzymolysis effect of oat pulp.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings which are needed in the embodiments and are practical will be briefly described below and will be obvious, the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts. Wherein, the first and the second end of the pipe are connected with each other,
FIG. 1 is a schematic structural view of the oat thick pulp continuous enzymolysis device of the utility model;
fig. 1 includes: the device comprises a raw pulp tank 1, a first temperature regulating mechanism 2, a first enzyme adding tank 3, a first coil pipe 4, a second temperature regulating mechanism 5, a second enzyme adding tank 6, a second coil pipe 7, a finished product tank 8 and a driving pump 9.
Detailed Description
In order to make the above objects, features and advantages of the present invention more comprehensible, the present invention is described in detail with reference to the accompanying drawings and the detailed description.
Different enzymolysis links are different in requirements on temperature, and the problem of lagging temperature regulation is caused by the fact that the same enzymolysis tank is adopted to implement a plurality of enzymolysis links, so that the whole enzymolysis process is difficult to accurately control, and the enzymolysis effect is finally influenced.
In view of this, the utility model provides a continuous enzymolysis device of thick liquid of oat, as shown in fig. 1, this continuous enzymolysis device of thick liquid of oat includes former thick liquid jar 1, first temperature regulating mechanism 2, first enzyme jar 3, first coil pipe 4, second temperature regulating mechanism 5, second and add enzyme jar 6, second coil pipe 7 and finished product jar 8, wherein:
the raw slurry tank 1 is used for storing oat slurry to be subjected to enzymolysis.
The feed inlet of first temperature adjusting mechanism 2 is connected with the discharge gate of magma jar 1 through first pipeline, and the discharge gate of first temperature adjusting mechanism 2 is connected with the feed inlet of first coil pipe 4 through the second pipeline, and first enzyme jar 3 that adds is connected on the second pipeline. Optionally, a driving pump 9 is arranged on the first pipeline, and the oat slurry in the raw slurry tank 1 flows into the first temperature adjusting mechanism 2 through the first pipeline under the driving of the driving pump 9.
In order to realize accurate control of the flow rate of the oat slurry in the first pipeline, the drive pump 9 is a variable-frequency rotor pump.
The first tempering means 2 is arranged to effect heating of the oat slurry so that the oat slurry reaches a predetermined liquefaction temperature. Optionally, the first temperature adjusting mechanism 2 is a plate-type heat exchanger, and the oat slurry is heated to the liquefaction temperature by heat exchange with a heating plate of the plate-type heat exchanger in the plate-type heat exchanger. The first enzyme adding tank 3 is used for carrying out the first enzyme adding to the oat pulp, namely, the first enzyme adding tank 3 adds the liquefied enzyme into the second pipeline, and the liquefied enzyme is mixed with the oat pulp flowing through the second pipeline.
The oat pulp carrying the liquefying enzyme enters the first coil 4 and flows along the first coil 4, and in the process, the oat pulp is liquefied under the action of the liquefying enzyme.
It is thus clear that through the cooperation of first mechanism 2, the first enzyme jar 3 and the first coil 4 that adds of adjusting the temperature, the utility model discloses a liquefaction to the thick liquid of oat. In the actual production process, can carry out the adaptability to the length of first coil pipe 4 according to factors such as the velocity of flow of liquefaction time requirement, thick liquids to guarantee that the oat thick liquid is abundant liquefied.
The feed inlet of the second temperature adjusting mechanism 5 is connected with the discharge outlet of the first coil pipe 4 through a third pipeline, the discharge outlet of the second temperature adjusting mechanism 5 is connected with the feed inlet of the second coil pipe 7 through a fourth pipeline, and the second enzyme adding tank 6 is connected on the fourth pipeline.
The second temperature adjusting mechanism 5 is used for heating the oat slurry to enable the oat slurry to reach the saccharification temperature, optionally, the second temperature adjusting mechanism 5 adopts a plate type heat exchanger, and the liquefied oat slurry generates heat exchange with a heating plate of the plate type heat exchanger in the plate type heat exchanger so as to be heated to the saccharification temperature. The second enzyme adding tank 6 is used for performing a second enzyme adding to the oat slurry, that is, the second enzyme adding tank 6 adds saccharifying enzyme into the fourth pipeline, and the saccharifying enzyme is mixed with the oat slurry flowing through the fourth pipeline.
The oat pulp carrying the saccharifying enzyme enters the second coil pipe 7 and flows along the second coil pipe 7, and in the process, the oat pulp is saccharified under the action of the saccharifying enzyme.
It is thus clear that, through the cooperation of second temperature adjusting mechanism 5, second enzyme jar 6, second coil pipe 7, the utility model discloses a saccharification to the thick liquid of oat. Similarly, in the actual production process, the length of the second coil pipe 7 can be adaptively set according to the saccharification time requirement, the flow rate of the slurry and other factors, so that the oat slurry is fully saccharified.
A feed inlet of the finished product tank 8 is connected with a discharge outlet of the second coil pipe 7 through a fifth pipeline, and the finished product tank 8 is used for storing the oat thick pulp after saccharification.
Compare with traditional batch centralized processing mode, the utility model discloses carry out liquefaction, the saccharification to the oat pulp stage by stage, continuously to realized the accurate temperature regulation of liquefaction, saccharification, thereby promoted the enzymolysis effect of oat pulp.
With continued reference to FIG. 1, optionally, the feed port of the first enzyme adding tank 3 is provided with a first flow meter, by which precise control of the amount of enzyme added to the first enzyme adding tank 3 can be carried out. In the same way, optionally, a second flowmeter is arranged at the feeding port of the second enzyme adding tank 6, and the second flowmeter can accurately control the enzyme adding amount of the second enzyme adding tank 6.
The invention has been described above with a certain degree of particularity and detail. It will be understood by those of ordinary skill in the art that the description of the embodiments is merely exemplary and that all changes that may be made without departing from the true spirit and scope of the present invention are intended to be within the scope of the present invention. The scope of the invention is defined by the appended claims rather than by the foregoing description of the embodiments.
Claims (6)
1. The utility model provides a thick continuous enzymolysis device of thick liquid of oat, its characterized in that, it includes former thick liquid jar, first temperature regulating mechanism, first enzyme jar, first coil pipe, second temperature regulating mechanism, second add enzyme jar, second coil pipe and finished product jar, wherein:
the primary pulp tank is used for storing oat pulp to be subjected to enzymolysis;
the feed inlet of the first temperature regulating mechanism is connected with the discharge outlet of the raw slurry tank through a first pipeline, the discharge outlet of the first temperature regulating mechanism is connected with the feed inlet of the first coil pipe through a second pipeline, the first enzyme adding tank is connected to the second pipeline, the first temperature regulating mechanism is used for heating the oat slurry to enable the oat slurry to reach the liquefaction temperature, the first enzyme adding tank is used for adding enzyme to the oat slurry for the first time, and the liquefaction of the oat slurry added with enzyme for the first time in the first coil pipe is completed;
the feed inlet of the second temperature adjusting mechanism is connected with the discharge outlet of the first coil pipe through a third pipeline, the discharge outlet of the second temperature adjusting mechanism is connected with the feed inlet of the second coil pipe through a fourth pipeline, the second enzyme adding tank is connected to the fourth pipeline, the second temperature adjusting mechanism is used for heating the oat pulp to enable the oat pulp to reach the saccharification temperature, the second enzyme adding tank is used for adding enzyme to the oat pulp for the second time, and the saccharification of the oat pulp added for the second time in the second coil pipe is completed;
the feed inlet of finished product jar through the fifth pipeline with the discharge gate of second coil pipe is connected, the finished product jar is used for storing the concentrated thick liquid of oat.
2. The continuous enzymatic hydrolysis apparatus for oat thick stock of claim 1, further comprising a drive pump connected to the first pipe.
3. The continuous enzymatic hydrolysis apparatus for oat thick slurry according to claim 2, wherein the driving pump is a variable frequency rotor pump.
4. The apparatus for continuous enzymatic hydrolysis of oat thick slurry according to claim 1, wherein the first temperature adjusting mechanism and the second temperature adjusting mechanism are plate type heat exchangers.
5. The continuous enzymatic hydrolysis device of oat thick pulp according to claim 1, characterized in that a first flow meter is arranged at the feeding port of the first enzyme adding tank.
6. The continuous enzymatic hydrolysis device for oat thick slurry according to claim 1, wherein a second flow meter is arranged at the feeding port of the second enzyme adding tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123208507.0U CN217202774U (en) | 2021-12-20 | 2021-12-20 | Continuous enzymolysis device of concentrated oat pulp |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123208507.0U CN217202774U (en) | 2021-12-20 | 2021-12-20 | Continuous enzymolysis device of concentrated oat pulp |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217202774U true CN217202774U (en) | 2022-08-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123208507.0U Active CN217202774U (en) | 2021-12-20 | 2021-12-20 | Continuous enzymolysis device of concentrated oat pulp |
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| Country | Link |
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| CN (1) | CN217202774U (en) |
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2021
- 2021-12-20 CN CN202123208507.0U patent/CN217202774U/en active Active
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