CN210103968U - Starch milk jet liquefaction system - Google Patents
Starch milk jet liquefaction system Download PDFInfo
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- CN210103968U CN210103968U CN201920443920.9U CN201920443920U CN210103968U CN 210103968 U CN210103968 U CN 210103968U CN 201920443920 U CN201920443920 U CN 201920443920U CN 210103968 U CN210103968 U CN 210103968U
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- steam
- jet
- liquefaction system
- valve
- starch milk
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Abstract
The utility model discloses a starch milk jet liquefaction system, including spraying the liquefier body, the side intercommunication of spraying the liquefier body has first steam line, and first steam line is equipped with valve I and steam flowmeter I along the direction of admitting air in proper order, and the top surface intercommunication of spraying the liquefier body has second steam line, and second steam line is equipped with valve II and steam flowmeter II along the direction of admitting air in proper order, and the opposite side intercommunication of second steam line has the feed line on spraying the liquefier body, and the feed line is equipped with valve III and mass flowmeter along the direction of admitting air in proper order; a discharging cavity is communicated with one side of the jet liquefier body, which is opposite to the first steam pipeline; the injection liquefaction system of this scheme liquefaction is effectual, the energy consumption is low and easily control air input and feed rate.
Description
Technical Field
The utility model relates to a high fructose syrup production field, specificly relate to a starch milk sprays liquefaction system.
Background
In the prior art, in the production process of the high fructose syrup, the starch milk is subjected to injection liquefaction, and the processes of saccharifying liquid in the subsequent working section, DX evaporation and the like are limited due to the density limitation and the liquefaction effect limitation of the starch milk during the injection liquefaction, so that the final purpose of energy saving and potential digging cannot be achieved; in addition, the injection liquefaction system in the prior art can not realize effective control to air inflow and feeding volume, and the discharge quality is unstable.
Disclosure of Invention
The technical problem to be solved by the utility model is to provide a starch milk jet liquefaction system that liquefaction effect is good, the energy consumption is low and easily control air input and feed volume.
In order to solve the above problem, the utility model provides a following technical scheme: the starch milk injection liquefaction system comprises an injection liquefier body, wherein a first steam pipeline is communicated with the side surface of the injection liquefier body, a valve I and a steam flow meter I are sequentially arranged on the first steam pipeline along the air inlet direction, a second steam pipeline is communicated with the top surface of the injection liquefier body, a valve II and a steam flow meter II are sequentially arranged on the second steam pipeline along the air inlet direction, a feeding pipeline is communicated with one side, opposite to the second steam pipeline, of the injection liquefier body, and a valve III and a mass flow meter are sequentially arranged on the feeding pipeline along the feeding direction; and a discharging cavity is communicated with one side of the jet liquefier body opposite to the first steam pipeline.
In order to realize that the materials in the jet liquefier body smoothly enter the discharging cavity and improve the discharging efficiency, the technical scheme of the invention also comprises the following steps: and a conical guide plate is arranged at the joint of the jet liquefier body and the discharge cavity.
Further, in order to facilitate the ejection of the material, the technical scheme of the invention further comprises: the discharge cavity is conical, and the size of a small opening of the conical discharge cavity is the same as that of the discharge end of the guide plate.
In order to further improve the liquefaction effect, the technical scheme of the invention also comprises the following steps: and a collision device is arranged in the discharge cavity.
The technical scheme of the invention also comprises: and a feeding thermometer is arranged on the feeding pipeline.
The technical scheme of the invention also comprises: and the valve I, the valve II and the valve III are all electromagnetic valves.
The utility model has the advantages that: compared with the prior art, the utility model aims at providing a starch milk jet liquefaction system that liquefaction is effectual, the energy consumption is low and easily control air input and feed volume, in order to realize above-mentioned technological effect, firstly, this scheme is equipped with two steam air inlet pipelines, two steam pipelines are 90 degrees settings each other, the area of contact of steam and material in the jet liquefier has been increased, can show improvement jet liquefaction efficiency and jet density, the energy consumption is reduced, make the concentration of saccharification liquid improve simultaneously, improve the raw material concentration for follow-up DX evaporation workshop section, reach the purpose of practicing thrift steam; secondly, the steam pipeline and the feed pipeline of this scheme all are equipped with control flap and flowmeter, can realize the effective control to air input and feeding volume, have ensured the stability of jet liquefaction process.
Drawings
In order to more clearly illustrate the embodiments or technical solutions in the prior art of the present invention, the drawings used in the description of the embodiments or prior art will be briefly described below, and it is obvious for those skilled in the art that other drawings can be obtained based on these drawings without creative efforts.
FIG. 1 is a schematic structural diagram of a starch injection liquefaction system according to an embodiment of the present invention.
Wherein, 1 is the injection liquefier body, 2 is first steam line, 3 is solenoid valve I, 4 is steam flowmeter I, 5 is second steam line, 6 is solenoid valve II, 7 is steam flowmeter II, 8 is the feeding pipeline, 9 is the feeding thermometer, 10 is solenoid valve III, 11 is mass flow meter, 12 is ejection of compact chamber, 13 is collision device, 14 is the guide plate.
Detailed Description
In order to make those skilled in the art better understand the technical solution of the present invention, the technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the drawings in the embodiment of the present invention, and it is obvious that the described embodiment is only a part of the embodiment of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The starch milk injection liquefaction system comprises an injection liquefier body 1, wherein the side surface of the injection liquefier body 1 is communicated with a first steam pipeline 2, the first steam pipeline 2 is sequentially provided with an electromagnetic valve I3 and a steam flow meter I4 along the air inlet direction, the top surface of the injection liquefier body 1 is communicated with a second steam pipeline 5, the second steam pipeline 5 is sequentially provided with an electromagnetic valve II 6 and a steam flow meter II 7 along the air inlet direction, one side of the injection liquefier body 1, opposite to the second steam pipeline 5, is communicated with a feeding pipeline 8, and the feeding pipeline 8 is sequentially provided with a feeding thermometer 9, an electromagnetic valve III 10 and a mass flow meter 11 along the feeding direction; the opposite side intercommunication of the first steam pipeline 2 on the jet liquefier body 1 has a discharge chamber 12, is equipped with collision device 13 in the discharge chamber 12, is equipped with conical guide plate 14 with discharge chamber 12 junction in the jet liquefier body 1, and discharge chamber 12 is the toper, and the osculum size of conical discharge chamber 12 is the same with the discharge end size of guide plate 14.
Although the present invention has been described in detail by referring to the drawings in connection with the preferred embodiments, the present invention is not limited thereto. Various equivalent modifications or substitutions can be made on the embodiments of the present invention by those skilled in the art without departing from the spirit and scope of the present invention, and these modifications or substitutions are within the scope of the present invention/any person skilled in the art can easily conceive of the changes or substitutions within the technical scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (6)
1. Starch milk sprays liquefaction system, including spraying the liquefier body, its characterized in that: the side surface of the jet liquefier body is communicated with a first steam pipeline, the first steam pipeline is sequentially provided with a valve I and a steam flow meter I along the air inlet direction, the top surface of the jet liquefier body is communicated with a second steam pipeline, the second steam pipeline is sequentially provided with a valve II and a steam flow meter II along the air inlet direction, one side of the jet liquefier body, opposite to the second steam pipeline, is communicated with a feeding pipeline, and the feeding pipeline is sequentially provided with a valve III and a mass flow meter along the air inlet direction; and a discharging cavity is communicated with one side of the jet liquefier body opposite to the first steam pipeline.
2. The starch milk jet liquefaction system of claim 1, characterized in that: and a conical guide plate is arranged at the joint of the jet liquefier body and the discharge cavity.
3. The starch milk jet liquefaction system of claim 2, characterized in that: the discharge cavity is conical, and the size of a small opening of the conical discharge cavity is the same as that of the discharge end of the guide plate.
4. The starch milk jet liquefaction system of claim 1, characterized in that: and a collision device is arranged in the discharge cavity.
5. The starch milk jet liquefaction system of claim 1, characterized in that: and a feeding thermometer is arranged on the feeding pipeline.
6. The starch milk jet liquefaction system of claim 1, characterized in that: and the valve I, the valve II and the valve III are all electromagnetic valves.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920443920.9U CN210103968U (en) | 2019-04-02 | 2019-04-02 | Starch milk jet liquefaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920443920.9U CN210103968U (en) | 2019-04-02 | 2019-04-02 | Starch milk jet liquefaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210103968U true CN210103968U (en) | 2020-02-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920443920.9U Active CN210103968U (en) | 2019-04-02 | 2019-04-02 | Starch milk jet liquefaction system |
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| Country | Link |
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| CN (1) | CN210103968U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112444142A (en) * | 2020-11-02 | 2021-03-05 | 国投生物科技投资有限公司 | Starch slurry heating equipment |
-
2019
- 2019-04-02 CN CN201920443920.9U patent/CN210103968U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112444142A (en) * | 2020-11-02 | 2021-03-05 | 国投生物科技投资有限公司 | Starch slurry heating equipment |
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