CN212451360U - Distillation device - Google Patents
Distillation device Download PDFInfo
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- CN212451360U CN212451360U CN202020904259.XU CN202020904259U CN212451360U CN 212451360 U CN212451360 U CN 212451360U CN 202020904259 U CN202020904259 U CN 202020904259U CN 212451360 U CN212451360 U CN 212451360U
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- distillation
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- air outlet
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Abstract
The utility model provides a distillation device, its structure is: the distillation disc with a cavity structure is supported at the bottom end in the steamer by a plurality of supports, a plurality of air outlet channels are uniformly distributed on the upper end surface, the air outlet channels are of a round table structure with a large upper part and a small lower part, the large opening end faces upwards and is flush with the upper end surface of the distillation disc to serve as an air outlet end, and the small opening end extends downwards to be communicated in the cavity of the distillation disc; the center of the bottom of the distillation disc is communicated with a steam buffer cavity through an air inlet pipe, a check valve is arranged on the air inlet pipe, and the other end of the steam buffer cavity is connected to an external steam pipeline. The utility model discloses be applied to during the white spirit distillation operation, steam distributes inhomogeneous current situation when can improving the distillation.
Description
Technical Field
The utility model relates to a making wine technical field, the more specifically distillation plant that says so.
Background
Traditional distillation plant is in distillation process, and inside steam entered distillation plant through steam conduit, because traditional distillation plant used the coiled tube structure, when heating, steam often had the inhomogeneous condition of distribution, influenced whole distillation effect on the one hand, and on the other hand can produce adverse effect to the quality of product.
SUMMERY OF THE UTILITY MODEL
The utility model discloses aim at solving above-mentioned technical problem to a certain extent at least. Therefore, the utility model provides a distillation plant is applied to in the white spirit distillation operation to steam distributes inhomogeneous current situation when can improve the distillation in hope.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the distillation device is structurally characterized in that:
the distillation disc with a cavity structure is supported at the bottom end in the steamer by a plurality of supports, a plurality of air outlet channels are uniformly distributed on the upper end surface, the air outlet channels are of a round table structure with a large upper part and a small lower part, the large opening end faces upwards and is flush with the upper end surface of the distillation disc to serve as an air outlet end, and the small opening end extends downwards to be communicated in the cavity of the distillation disc;
the center of the bottom of the distillation disc is communicated with a steam buffer cavity through an air inlet pipe, a check valve is arranged on the air inlet pipe, and the other end of the steam buffer cavity is connected to an external steam pipeline.
Furthermore, the diameter of the large opening end of the air outlet pore passage is twice as large as that of the small opening end.
Compared with the prior art, the utility model discloses beneficial effect embodies:
the utility model discloses the succinct novelty of structural design, easy to carry out, with low costs, technological effect is good, application scope is wide, is through outside steam conduit air feed, gets into distillation disc through steam cushion chamber and intake pipe in proper order, and the back evenly flows out through a plurality of pore of giving vent to anger of distillation disc upper end equipartition, has realized steam evenly distributed's good effect, causes harmful effects to the product quality because of steam temperature is inconsistent, pressure distribution is inhomogeneous when having avoided the distillation. Because the inner hole of the air outlet pore passage is small, and the outer hole of the air outlet pore passage is large, when steam flows out through the air outlet pore passage, the problem of steam injection can be effectively avoided. In addition, the check valve is arranged on the air inlet pipe, so that other liquid substances can be prevented from flowing back to enter the steam pipeline after distillation.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
fig. 2 is a schematic structural view of the intake duct in fig. 1.
In the figure, 1 distillation disc; 2, a bracket; 3, air inlet pipe; 4, a check valve; 5, a steam buffer cavity; 6, a steam pipeline; 7 air outlet channels.
Detailed Description
To make the purpose, technical solution and advantages of the embodiments of the present invention clearer, the embodiments of the present invention are combined to clearly and completely describe the technical solution in the embodiments of the present invention, and obviously, the described embodiments are some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
Referring to fig. 1 to 2, the distillation apparatus of the present embodiment is structurally configured as follows:
the distillation disc 1 with a cavity structure is supported at the bottom end in the steamer by a plurality of supports 2, a plurality of air outlet channels 7 are uniformly distributed on the upper end surface, the air outlet channels are in a round platform type structure with a big top and a small bottom, the big end is upward and is flush with the upper end surface of the distillation disc to be used as an air outlet end, and the small end is downward extended to be communicated in the cavity of the distillation disc;
the center of the bottom of the distillation disc is communicated with a steam buffer cavity 5 through an air inlet pipe 3, a check valve 4 is arranged on the air inlet pipe, the other end of the steam buffer cavity is connected to an external steam pipeline, and the check valve enables air flow to the distillation disc only from the steam buffer cavity, so that foreign matters are prevented from flowing back to enter the steam pipeline 6.
Wherein, the diameter size of the large opening end of the air outlet pore passage is twice of the diameter size of the small opening end.
In this embodiment, the boiler is not shown, the size of the distillation disc is set as required according to the size of the external container (such as the boiler), and the installation height from the bottom end of the boiler can be set as required.
While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the claims and their equivalents.
Claims (2)
1. A distillation apparatus, characterized by:
the distillation disc with a cavity structure is supported at the bottom end in the steamer by a plurality of supports, a plurality of air outlet channels are uniformly distributed on the upper end surface, the air outlet channels are of a round table structure with a large upper part and a small lower part, the large opening end faces upwards and is flush with the upper end surface of the distillation disc to serve as an air outlet end, and the small opening end extends downwards to be communicated in the cavity of the distillation disc;
the center of the bottom of the distillation disc is communicated with a steam buffer cavity through an air inlet pipe, a check valve is arranged on the air inlet pipe, and the other end of the steam buffer cavity is connected to an external steam pipeline.
2. The distillation apparatus of claim 1, wherein: the diameter of the large opening end of the air outlet pore passage is twice that of the small opening end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202020904259.XU CN212451360U (en) | 2020-05-26 | 2020-05-26 | Distillation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202020904259.XU CN212451360U (en) | 2020-05-26 | 2020-05-26 | Distillation device |
Publications (1)
Publication Number | Publication Date |
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CN212451360U true CN212451360U (en) | 2021-02-02 |
Family
ID=74501111
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN202020904259.XU Active CN212451360U (en) | 2020-05-26 | 2020-05-26 | Distillation device |
Country Status (1)
Country | Link |
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CN (1) | CN212451360U (en) |
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2020
- 2020-05-26 CN CN202020904259.XU patent/CN212451360U/en active Active
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