CN218106752U - Circulating enrichment device of corn silk separation liquid - Google Patents
Circulating enrichment device of corn silk separation liquid Download PDFInfo
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- CN218106752U CN218106752U CN202222089626.7U CN202222089626U CN218106752U CN 218106752 U CN218106752 U CN 218106752U CN 202222089626 U CN202222089626 U CN 202222089626U CN 218106752 U CN218106752 U CN 218106752U
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Abstract
The application relates to the field of preparation of corn silk concentrate, in particular to a circulating enrichment device for corn silk separating medium. The device comprises: a first pipe, a circulation pump, a heating member, a separating member, and a second pipe; the circulating pump is used for receiving the corn stigma separation liquid and conveying the separation liquid to the heating element through the first pipeline; the heating element is used for receiving hot steam and heating the separation liquid through the hot steam; the circulating pump is also used for conveying the water evaporated by heating in the separation liquid in the heating element, the hot steam and the residual separation liquid to the separation element through the second pipeline; the separating piece is used for separating the water and the hot steam which are evaporated due to heating in the separating liquid from the rest separating liquid; the circulating pump is also used for conveying the residual separation liquid in the separation member to the heating member through the first pipeline. This application has formed circulating enrichment device through the setting of first pipeline etc. and the moisture in the separating medium is constantly taken away through hot steam to the in-process, can accomplish the preparation of corn silk concentrate.
Description
Technical Field
The application relates to the field of preparation of corn silk concentrate, in particular to a circulating enrichment device for corn silk separating medium.
Background
The preparation of existing corn silk concentrates is generally industrialized because they typically require dual effect falling film evaporators for concentration, and such industrialized equipment cannot be easily placed in a laboratory or other relatively small scale demanding setting. Therefore, when the corn stigma concentrated solution is needed, corresponding preparation work needs to be carried out in advance, and inconvenience is brought to actual working life.
Furthermore, the above-described harvesting method may become even more inconvenient as, in some use scenarios, the corn silk concentrate of different corn varieties may be required.
SUMMERY OF THE UTILITY MODEL
The application provides a circulating enrichment device of corn silk parting liquid can solve the problem of awkward in laboratory or other relatively miniature demand sight of the preparation equipment of current corn silk concentrate.
The technical scheme of this application is a circulating enrichment device of corn silk parting liquid, the device includes: the device comprises a first pipeline, a circulating pump arranged between two ends of the first pipeline, a heating element communicated with one end of the first pipeline through the bottom, a separating element communicated with the other end of the first pipeline through the bottom, and a second pipeline communicated with the top of the heating element and the top of the separating element;
the circulating pump is used for receiving the corn stigma separation liquid and conveying the separation liquid to the heating element through a first pipeline;
the heating element is used for receiving hot steam and heating the separation liquid through the hot steam;
the circulating pump is also used for conveying the moisture, the hot steam and the residual separation liquid evaporated by heating in the separation liquid in the heating element to the separation element through a second pipeline;
the separating piece is used for separating the water and the hot steam which are evaporated due to heating in the separating liquid from the rest separating liquid;
the circulating pump is also used for conveying the residual separation liquid in the separation part to the heating part through a first pipeline;
and the separating part is also used for conveying the concentrated solution obtained after the circulating enrichment to the outside of the device.
Optionally, the apparatus further comprises: a heat source element;
the heat source element is used for receiving external water and heating the water to obtain hot steam, and delivering the hot steam to the heating element.
Optionally, the apparatus further comprises: a stock solution piece;
the stock solution piece is communicated with the circulating pump and is used for conveying the separation solution to the circulating pump.
Optionally, the dope element comprises:
the device comprises a stock solution shell, an openable cover body arranged at the top of the stock solution shell, a soft water inlet pipe communicated with the cover body, a stirring and crushing piece arranged in the stock solution shell, a driver for driving the stirring and crushing piece to be in transmission connection, and a filtering piece arranged at the lower end of the stirring and crushing piece.
Optionally, the crutcher includes:
the cutting device comprises a vertically arranged rotating rod, cutting blades vertically and uniformly arranged on the rod body of the rotating rod, and a fixing sheet connected with the inner wall of the stock solution shell and connected with the two ends of the rotating rod in a rotating mode.
Optionally, the fixing sheet is configured to be arranged on the inner wall of the stock solution shell in a manner of edge fitting, and a fixing ring rotationally connected with the rotating rod and a plurality of connecting rods fixedly connecting the edges and the fixing ring are arranged in the fixing sheet;
and the setting number of the connecting rods in the fixed sheet close to the top of the rotating rod is smaller than that of the connecting rods in the fixed sheet close to the bottom of the rotating rod.
Optionally, the number of the connecting rods in the fixed sheet close to the top of the rotating rod is three;
and the number of the connecting rods in the fixed sheet close to the bottom of the rotating rod is twenty.
Optionally, the apparatus further comprises: an outer housing; a bearing frame is arranged in the outer shell;
first pipeline, circulating pump, heating member, separation piece, second pipeline and stoste spare all set up in the shell, and heating member, separation piece and stoste spare all with accept the frame and can dismantle the connection.
Has the advantages that:
1) The movable type garage is simple in structure and convenient to use, can be moved into the storehouse when not needed, and can be taken out for use immediately when needed.
2) This application has constituted a circulating enrichment device through the setting of first pipeline, circulating pump, heating member, separator and second pipeline completely, and the moisture in the separating medium is constantly taken away through hot steam to the in-process, and whole process can be repeated according to the actual demand, has what kind of requirement to the corn silk concentrate promptly, and the circulation that carries out corresponding number of times to the corn silk concentrate promptly can.
In conclusion, the preparation equipment can solve the problem that the existing preparation equipment for the corn stigma concentrated solution is inconvenient to use in a laboratory or other small-sized demand scenes
Drawings
In order to more clearly explain the technical solution of the present application, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious to those skilled in the art that other drawings can be obtained according to the drawings without any creative effort.
FIG. 1 is a top view of a circulating type corn stigma separating liquid enriching apparatus according to an embodiment of the present application;
FIG. 2 is a schematic structural view of a heating element and a separating element in an embodiment of the present application;
FIG. 3 is a schematic view of the heat source unit and the raw liquid unit in the embodiment of the present application;
FIG. 4 is a schematic structural diagram of a raw liquid piece in an embodiment of the present application;
wherein, 1-a first pipeline; 2-a circulating pump; 3-a heating element; 4-a separator; 5-a second conduit; 6-heat source element; 7-stock solution piece; 71-dope shell; 72-a cover; 73-water inlet pipe; 74-a milling element; 741-rotating rods; 742-cutting blades; 743-a fixing piece; 75-a driver; 76-filter member; 8-a bearing frame.
Detailed Description
Reference will now be made in detail to embodiments, examples of which are illustrated in the accompanying drawings. When the following description refers to the accompanying drawings, like numbers in different drawings represent the same or similar elements unless otherwise indicated. The embodiments described in the following examples do not represent all embodiments consistent with the present application. But merely as exemplifications of systems and methods consistent with certain aspects of the application, as recited in the claims.
The application provides a circulating enrichment facility of corn silk parting liquid, as shown in fig. 1, fig. 1 is a top view of the circulating enrichment facility of corn silk parting liquid in the embodiment of the application, and the apparatus includes: the device comprises a first pipeline 1, a circulating pump 2, a heating element 3, a separating element 4, a second pipeline 5, a heat source element 6, a stock solution element 7 and an outer shell.
The first pipe 1 and the second pipe 5 are both heat-resistant pipes.
The first conduit 1 is located near the ground at the lower end of the device.
The circulation pump 2 is arranged somewhere between the two ends of the first conduit 1.
Wherein, the circulating pump 2 is used for receiving the corn stigma separation liquid and conveying the separation liquid to the heating element 3 through the first pipeline 1; the circulating pump 2 is also used for leading the water, the hot steam and the residual separation liquid evaporated by being heated in the separation liquid in the heating element 3 to pass through a second pipeline 5 to the separation element 4; the circulation pump 2 is also used to convey the remaining separation liquid in the separation member 4 through the first conduit 1 to the heating member 3.
The circulation pump 2 is provided for strongly circulating the separated liquid.
As shown in fig. 2, fig. 2 is a schematic structural view of a heating member and a separating member in the embodiment of the present application, and the bottom of the heating member 3 is communicated with one end of the first pipe 1.
Wherein the heating element 3 is adapted to receive hot steam and to heat the separation liquid by means of the hot steam. The high-temperature hot steam has stronger heating capacity, so that the separation liquid in the pipeline can be efficiently heated.
The bottom of the separating member 4 communicates with the other end of the first pipe 1. Wherein, the separating member 4 is used for separating the water and the hot steam evaporated by being heated in the separating liquid from the rest separating liquid; the separator 4 is also used to convey the concentrated liquid obtained after the cyclic enrichment to the outside of the device.
The purpose of the separating element 4 is to remove the hot steam and the evaporated moisture from the separated liquid, and to obtain a more concentrated extract than before.
A second conduit 5 is arranged higher up in the device and communicates the top of the heating element 3 and the top of the separating element 4.
As shown in fig. 3, fig. 3 is a schematic structural view of a heat source member and a raw liquid member in the embodiment of the present application, the first pipe 1, the heating member 3, and the separating member 4 are not shown in fig. 3, and the heat source member 6 is communicated with the heating member 3.
Wherein the heat source element 6 is used for receiving external water and heating the water to obtain hot steam, and delivering the hot steam to the heating element 3.
The starting and the closing of the heat source element 6 can be manually set, and a remote control valve can also be set to control the starting and the closing of the heat source element 6, because the heat source element 6 is used in cooperation with the circulation direction of the separation liquid, the energy input of the device is recovered to the maximum extent, and therefore in practical use, the starting time of the heat source element 6 needs to be paid attention.
The stock solution piece 7 is communicated with the circulating pump 2 and is used for conveying the separation solution to the circulating pump 2.
The stock solution 7 is obtained from the most original separated liquid extracted from the corn stigma.
As shown in fig. 4, fig. 4 is a schematic structural diagram of a raw liquid piece in an embodiment of the present application, and the raw liquid piece 7 includes: a stock solution shell 71, an openable cover body 72 arranged at the top of the stock solution shell 71, a soft water inlet pipe 73 communicated with the cover body 72, a stirring and crushing piece 74 arranged in the stock solution shell 71, a driver 75 driving the stirring and crushing piece 74 to be in transmission connection, and a filter 76 arranged at the lower end of the stirring and crushing piece 74.
Specifically, dope housing 71 may be provided in two removably attached portions adjacent to where filter element 76 is located, facilitating replacement and cleaning of filter element 76 after use of the device.
Wherein the masher 74 includes:
a vertically disposed rotating rod 741 and cutting blades 742 disposed uniformly in a vertical direction on a shaft of the rotating rod 741, and a fixing piece 743 connected to an inner wall of the dope housing 71 and rotatably connected to both ends of the rotating rod 741.
The fixing plate 743 is configured to be attached to the inner wall of the raw liquid housing 71 at the edge, and a fixing ring rotatably connected with the rotating rod 741 and a plurality of connecting rods fixedly connecting the edge and the fixing ring are arranged inside the fixing plate.
And the number of the connection rods provided in the fixing plate 743 near the top of the rotation rod 741 is smaller than the number of the connection rods provided in the fixing plate 743 near the bottom of the rotation rod 741.
In some embodiments, the number of tie bars provided in the securing tab 743 near the top of the swivel rod 741 is three; the number of the connecting rods provided in the fixing piece 743 near the bottom of the rotating rod 741 is twenty.
The outer housing is the housing of the entire device. A receiving frame 8 is arranged in the outer shell. The carrier 8 is used for placing some components in the device.
First pipeline 1, circulating pump 2, heating member 3, separator 4, second pipeline 5, heat source spare 6 and stoste spare 7 all set up in the shell, and heating member 3, separator 4, heat source spare 6 and stoste spare 7 all can dismantle with accepting frame 8 and be connected.
Specifically, the receiving frame 8 is provided with a transverse railing, and the outer sides of the heating element 3, the separating element 4, the heat source element 6 and the stock solution element 7 close to the receiving frame 8 are all provided with right-angle bending bends which can be erected on the top side of the railing, so that the heating element 3, the separating element 4, the heat source element 6 and the stock solution element 7 can be detachably connected with the receiving frame 8.
The support frame 8 is arranged to facilitate the assembly, disassembly and cleaning of the various components in the device.
The working principle is as follows:
(1) When the raw material is corn silk and the target product is corn silk concentrated extract, the corn silk is firstly placed into the stock solution shell 71 through the cover body 72, then the stirring and crushing piece 74 is started to stir the corn silk, and the separation solution flowing down after the corn silk is crushed can reach the circulating pump 2 after being filtered by the filter piece 76.
(2) Water is supplied into the heat source element 6 and the heat source element 6 is activated, and the heat source element 6 heats the water to generate heat steam.
(3) The circulation pump 2 is started and the circulation pump 2 delivers the separated liquid to the heating element 3 through the first conduit 1. In the heating member 3, the separation liquid is heated by the hot vapor and a part of the solvent water in the separation liquid is heated and evaporated to become the hot vapor.
(4) The circulation pump 2 delivers hot steam and separation liquid to the separation member 4 via a second conduit 5. Within the separating member 4, the hot vapour and the separating liquid are separated by density or other separation principles.
(5) The circulation pump 2 is started again and the circulation pump 2 delivers the separation liquid in the separation member 4 to the heating member 3 via the first conduit 1. And (5) repeating the step (4) and the step (5) in a circulating way until the corn stigma concentrated solution meeting the expected standard is obtained after proper circulation times and then is discharged through the separating piece 4.
The embodiments of the present application have been described in detail, but the present application is only a preferred embodiment of the present application and should not be construed as limiting the scope of the present application. All equivalent changes and modifications made within the scope of the present application shall fall within the scope of the present application.
Claims (8)
1. The circulating type enriching device for the corn stigma separation liquid is characterized by comprising: the device comprises a first pipeline, a circulating pump arranged between two ends of the first pipeline, a heating element communicated with one end of the first pipeline through the bottom, a separating element communicated with the other end of the first pipeline through the bottom, and a second pipeline communicated with the top of the heating element and the top of the separating element;
the circulating pump is used for receiving the corn stigma separation liquid and conveying the separation liquid to the heating element through a first pipeline;
the heating element is used for receiving hot steam and heating the separation liquid through the hot steam;
the circulating pump is also used for conveying the moisture, the hot steam and the residual separation liquid evaporated by heating in the separation liquid in the heating element to the separation element through a second pipeline;
the separating piece is used for separating the water and the hot steam which are evaporated due to heating in the separating liquid from the rest separating liquid;
the circulating pump is also used for conveying the residual separation liquid in the separation part to the heating part through a first pipeline;
and the separating part is also used for conveying the concentrated solution obtained after the circulating enrichment to the outside of the device.
2. The recycling-type corn silk separating medium enriching device as claimed in claim 1, further comprising: a heat source element;
the heat source element is used for receiving external water and heating the water to obtain hot steam, and delivering the hot steam to the heating element.
3. The recycling-type corn silk separating medium enriching device as claimed in claim 1, further comprising: a stock solution piece;
the stock solution piece is communicated with the circulating pump and is used for conveying the separation solution to the circulating pump.
4. The circulating type corn silk separating liquid enriching device as claimed in claim 3, wherein the stock solution member comprises:
the device comprises a stock solution shell, an openable cover body arranged at the top of the stock solution shell, a soft water inlet pipe communicated with the cover body, a stirring and crushing piece arranged in the stock solution shell, a driver for driving the stirring and crushing piece to be in transmission connection with a filtering piece arranged at the lower end of the stirring and crushing piece.
5. The circulating type corn silk separating medium enriching device as claimed in claim 4, wherein the stirring and crushing member comprises:
the cutting device comprises a vertically arranged rotating rod, cutting blades vertically and uniformly arranged on the rod body of the rotating rod, and a fixing sheet connected with the inner wall of the stock solution shell and connected with the two ends of the rotating rod in a rotating mode.
6. The circulating type corn silk separating liquid enriching device as claimed in claim 5, wherein the fixing plate is configured to be attached at the edge to the inner wall of the raw liquid shell, and is internally provided with a fixing ring which is rotatably connected with the rotating rod and a plurality of connecting rods which are fixedly connected with the edge and the fixing ring;
and the setting number of the connecting rods in the fixed sheet close to the top of the rotating rod is smaller than that of the connecting rods in the fixed sheet close to the bottom of the rotating rod.
7. The circulating type corn silk separating liquid enriching device as claimed in claim 6, wherein the number of the connecting rods in the fixed sheet near the top of the rotating rod is three;
and the number of the connecting rods in the fixing sheet close to the bottom of the rotating rod is twenty.
8. The recycling-type corn silk separating medium enriching device as claimed in claim 6, further comprising: an outer housing; a bearing frame is arranged in the outer shell;
first pipeline, circulating pump, heating member, separation piece, second pipeline and stoste spare all set up in the shell, and heating member, separation piece and stoste spare all with accept the frame and can dismantle the connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222089626.7U CN218106752U (en) | 2022-08-10 | 2022-08-10 | Circulating enrichment device of corn silk separation liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222089626.7U CN218106752U (en) | 2022-08-10 | 2022-08-10 | Circulating enrichment device of corn silk separation liquid |
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| Publication Number | Publication Date |
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| CN218106752U true CN218106752U (en) | 2022-12-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202222089626.7U Active CN218106752U (en) | 2022-08-10 | 2022-08-10 | Circulating enrichment device of corn silk separation liquid |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116786191A (en) * | 2023-08-18 | 2023-09-22 | 黑龙江省农业科学院玉米研究所 | Corn fine processing assembly, device and use method |
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2022
- 2022-08-10 CN CN202222089626.7U patent/CN218106752U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116786191A (en) * | 2023-08-18 | 2023-09-22 | 黑龙江省农业科学院玉米研究所 | Corn fine processing assembly, device and use method |
| CN116786191B (en) * | 2023-08-18 | 2023-11-03 | 黑龙江省农业科学院玉米研究所 | Corn fine processing assembly, device and use method |
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