CN210251295U

CN210251295U - Crystallization gas-liquid separation device suitable for biological raw materials

Info

Publication number: CN210251295U
Application number: CN201920784171.6U
Authority: CN
Inventors: 张楚扬; 袁爱国; 陈德苞; 苏木平; 陈秀英
Original assignee: Shantou Jiahe Biological Technology Co ltd
Current assignee: Shantou Jiahe Biological Technology Co ltd
Priority date: 2019-05-28
Filing date: 2019-05-28
Publication date: 2020-04-07
Anticipated expiration: 2029-05-28

Abstract

The utility model belongs to the technical field of biological raw materials research and development, a crystallization gas-liquid separation equipment suitable for biological raw materials is related to, the utility model discloses a following technical scheme: the utility model provides a crystallization gas-liquid separation device suitable for biological raw materials, mainly by heating the cavity and for heating the cavity and carry out the main heating device that heats, heating the cavity including the middle holding chamber that is used for the holding solution and be located the feed valve of its bottom, holding chamber's top set up for holding chamber carry out steam separation's steam extraction equipment, the utility model has the advantages of: in the crystallization production process of the biological raw material, the continuous separation of crystals or solution in steam flow in the steam extraction process is further realized, and the reflux utilization is further realized.

Description

Crystallization gas-liquid separation device suitable for biological raw materials

Technical Field

The utility model relates to a biological raw materials research and development technical field especially relates to a crystallization gas-liquid separation equipment suitable for biological raw materials.

Background

In the conventional crystallization process of biological raw materials, a crystallization kettle is required to further crystallize a solution of the biological raw materials to separate moisture of the further solution, generally, a heating device is adopted to heat the crystallization kettle, and further steam is pumped away, so that the whole crystallization process is realized.

Disclosure of Invention

One of the purposes of the utility model is to provide a crystallization gas-liquid separation device suitable for biological raw materials.

In order to achieve the above purpose, the utility model adopts the following technical scheme: a crystallization gas-liquid separation device suitable for biological raw materials mainly comprises a heating chamber and a main heating device for heating relative to the heating chamber, wherein the heating chamber comprises a middle accommodating chamber for accommodating solution and a feed valve positioned at the bottom of the middle accommodating chamber, steam pumping equipment for performing steam separation relative to the accommodating chamber is arranged at the top of the accommodating chamber, a pumping hole of the steam pumping equipment is communicated with an exhaust hole of the accommodating chamber, and a separation mechanism for separating crystals or solution in steam flow discharged from the exhaust hole is arranged between the exhaust hole and the accommodating chamber.

Furthermore, the separation mechanism for separating the crystal or the solution discharged from the steam flow of the exhaust port is provided with a separation chamber with a hollow chamber, the exhaust pipe orifice is arranged on one side of the separation chamber, the air inlet pipe orifice is arranged at the bottom of the separation chamber, and the air inlet pipe orifice extends upwards from the inner side of the heating chamber to the inner side of the separation chamber and is higher than the exhaust pipe orifice.

Furthermore, the bottom of the separation chamber forms a downward inclined plane, and a material outlet is arranged at the tail end of the inclined plane.

Furthermore, an intermediate chamber is arranged at the bottom of the material discharge port, and an auxiliary heating device for heating output relative to the intermediate chamber is arranged.

Furthermore, the bottom of the middle chamber is communicated with the bottom of the heating chamber through a first communication pipe.

Furthermore, first communicating pipe wear to establish and extend under the partial arc in the heating chamber, first communicating pipe be located the exposure mouth of heating chamber and be located arc extension bottom department down.

Further, a material conveying pump is arranged on the first communication pipe between the middle chamber and the heating chamber.

Furthermore, a filter screen is arranged on one side of the air inlet pipe orifice, which is positioned in the heating chamber.

Furthermore, the filter screen comprises a first filter screen layer and a second filter screen layer which are vertically stacked, meshes of the first filter screen layer and meshes of the second filter screen layer are staggered, the meshes are hollow meshes which are distributed at intervals, and the central axes of the meshes are parallel to the central axis of the air inlet pipe orifice.

Furthermore, a spraying pump for spraying and outputting relative to the material outlet is arranged at the top of the material outlet of the separation chamber, and a liquid inlet of the spraying pump is communicated with the bottom of the inner cavity of the heating chamber through a second communicating pipe.

The utility model has the advantages that: in the crystallization production process of the biological raw material, the continuous separation of crystals or solution in steam flow in the steam extraction process is further realized, and the reflux utilization is further realized.

Description of the drawings:

FIG. 1 is a schematic illustration of an example product;

FIG. 2 is a schematic illustration of an example product;

FIG. 3 is a schematic illustration of an example product;

FIG. 4 is a schematic illustration of an example product;

FIG. 5 is a schematic illustration of a portion of an example product;

FIG. 6 is a schematic illustration of a portion of an example product.

The specific implementation mode is as follows:

the following detailed description of the embodiments of the present invention will be made with reference to the accompanying drawings. It is to be understood that the description of the embodiments herein is for purposes of illustration and explanation only and is not intended to limit the invention.

Example 1: referring to fig. 1-6, a crystallization gas-liquid separation device suitable for biological raw materials is mainly composed of a heating chamber 1 and a main heating device for heating relative to the heating chamber 1, wherein the main heating device can be a known device for heating the heating chamber or a main heating device as described in example 2, the heating chamber 1 includes an intermediate accommodating chamber 10 for accommodating a solution and a feeding valve 11 at the bottom thereof, a steam pumping device 2 for performing steam separation relative to the accommodating chamber 19 is arranged at the top of the accommodating chamber 10, a pumping port 21 of the steam pumping device 2 is communicated with a gas outlet of the accommodating chamber 10, and a separation mechanism 3 for separating crystals or the solution in steam flow discharged from the gas outlet is arranged between the gas outlet and the accommodating chamber 10.

Further, the separation mechanism 3 for separating the crystals or the solution discharged from the steam flow of the exhaust port has a separation chamber 31 with a hollow cavity, the exhaust pipe orifice is arranged on one side of the separation chamber 31 and communicated with the exhaust port 21 of the steam exhaust device 2, an air inlet pipe orifice 35 is arranged at the bottom of the separation chamber 31, and the air inlet pipe orifice 35 extends upwards from the inner side of the heating chamber 1 to the inner side of the separation chamber 31 and is higher than the exhaust pipe orifice 32.

In the crystallization production process of the biological raw material, the continuous separation of crystals or solution in steam flow in the steam extraction process is further realized, and the reflux utilization is further realized.

Further, the bottom of the separation chamber 31 forms a downward inclined surface 37, and a material discharge port 32 is provided at the end of the inclined surface, so that the material or the solution is guided to the material discharge port 32 to be discharged.

Further, an intermediate chamber 33 is provided at the bottom of the material discharge port 32, and an auxiliary heating device 34 for heating output with respect to the intermediate chamber 33 is provided, and the intermediate chamber 33 is maintained or raised at a temperature at which it is not further crystallized in the intermediate chamber 33 when appropriate.

Further, the bottom of the intermediate chamber 33 is connected to the bottom of the heating chamber 1 via a first communication pipe 4, which in use, further conducts the solution or crystallized material separated in the separation chamber 31.

Further, the first communicating pipe 4 penetrates through a part of the arc-shaped lower extension 41 in the heating chamber 1, the first communicating pipe 4 is located at the bottom of the arc-shaped lower extension 41 at the leakage opening 42 of the heating chamber 1, when in use, the discharged material or solution at the leakage opening 42 is further reduced to be discharged along with the steam flow, and the arc-shaped lower extension 41 can play a certain role in stopping.

Further, a material feed pump 43 is provided in the first communication pipe 4 between the intermediate chamber 33 and the heating chamber 1 to maintain dynamic propulsion of the crystal material or solution.

Furthermore, a filter screen 36 is arranged on one side of the air inlet pipe orifice 35, which is located in the heating chamber 1, preferably, the filter screen 36 comprises a first filter screen layer and a second filter screen layer which are stacked up and down, the meshes of the first filter screen layer and the second filter screen layer are staggered, the meshes are hollow meshes which are distributed at intervals, the central axes of the meshes are parallel to the central axis of the air inlet pipe orifice, in the steam extraction process, when steam flows into the air inlet pipe orifice, the steam flows into the meshes of the first filter screen layer first, then flows into the meshes of the staggered second filter screen layer, and then is discharged to an exhaust port, and in the process, the air flow is turned to reduce the discharge of the solution or the crystallization material along with the steam flow.

Further, the separation chamber is provided with a spray pump 8 for spraying and outputting relative to the material outlet at the top of the material outlet 32, and a liquid inlet of the spray pump 8 is communicated with the bottom of the inner cavity of the heating chamber 1 through a second communicating pipe 81, and is particularly suitable for spraying and outputting relative to the material outlet to impact the material outlet when the material outlet of the separation chamber 31 is blocked, so as to prevent the material outlet from being blocked.

Further, be provided with for heating chamber 1 bottom department carry out stirring output's stirring vane 91, stirring vane 91 is connected by driving motor 9 transmission, and is concrete, and the use of cooperation this stirring part makes holistic crystallization effect more even.

Of course, the above is only the preferred embodiment of the present invention, and the application range of the present invention is not limited thereto, so all the equivalent changes made in the principle of the present invention should be included in the protection scope of the present invention.

Claims

1. A crystallization gas-liquid separation device suitable for biological raw materials mainly comprises a heating chamber and a main heating device which is used for heating relative to the heating chamber, and is characterized in that: the heating chamber comprises a middle accommodating chamber for accommodating the solution and a feed valve positioned at the bottom of the middle accommodating chamber, the top of the accommodating chamber is provided with a steam pumping device for performing steam separation relative to the accommodating chamber, a pumping hole of the steam pumping device is communicated with an exhaust port of the accommodating chamber, and a separation mechanism for separating crystals or the solution discharged in steam flow of the exhaust port is arranged between the exhaust port and the accommodating chamber.

2. The crystallization gas-liquid separation device according to claim 1, wherein: the separation mechanism for separating the crystal or the solution discharged from the steam flow of the air outlet is provided with a separation chamber of a hollow chamber, one side of the separation chamber is provided with an air outlet pipe orifice, the bottom of the separation chamber is provided with an air inlet pipe orifice, and the air inlet pipe orifice upwards extends to the inner side of the separation chamber from the inner side of the heating chamber and is higher than the air outlet pipe orifice.

3. The crystallization gas-liquid separation device according to claim 2, wherein: the bottom of the separation chamber forms a downward inclined plane, and a material outlet is arranged at the tail end of the inclined plane.

4. The crystallization gas-liquid separation device according to claim 3, wherein: and the middle chamber is arranged at the bottom of the material outlet, and an auxiliary heating device for heating and outputting relative to the middle chamber is arranged.

5. The crystallization gas-liquid separation device according to claim 4, wherein: the bottom of the middle chamber is communicated with the bottom of the heating chamber through a first communication pipe.

6. A separation apparatus of crystallization gas-liquid suitable for use in biological raw material as claimed in claim 5, wherein: first communicating pipe wear to establish and extend under the partial arc in the heating chamber, first communicating pipe be located heating chamber's the mouth that leaks and be located arc extension bottom department down.

7. A separation apparatus of crystallization gas-liquid suitable for use in biological raw material as claimed in claim 6, wherein: a material conveying pump is arranged on the first communication pipe between the middle chamber and the heating chamber.

8. A separation apparatus of crystal gas and liquid suitable for use in biological raw material as claimed in any one of claims 2 to 7, wherein: a filter screen is arranged on one side of the air inlet pipe orifice positioned in the heating chamber.

9. A crystallization gas-liquid separation apparatus suitable for use with a biological raw material as set forth in claim 8, wherein: the filter screen comprises a first filter screen layer and a second filter screen layer which are vertically stacked, meshes of the first filter screen layer and meshes of the second filter screen layer are staggered, the meshes are hollow meshes which are distributed at intervals, and the central axes of the meshes are parallel to the central axis of the air inlet pipe orifice.

10. A crystallization gas-liquid separation apparatus suitable for use in biological raw materials according to claim 7, wherein: the separation chamber is positioned at the top of the material outlet and is provided with a spray pump for spraying and outputting relative to the material outlet, and a liquid inlet of the spray pump is communicated with the bottom of the inner cavity of the heating chamber through a second communicating pipe.