CN212308463U - System used in production process of eucommia ulmoides fine powder - Google Patents
System used in production process of eucommia ulmoides fine powder Download PDFInfo
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- CN212308463U CN212308463U CN202021913996.2U CN202021913996U CN212308463U CN 212308463 U CN212308463 U CN 212308463U CN 202021913996 U CN202021913996 U CN 202021913996U CN 212308463 U CN212308463 U CN 212308463U
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Abstract
The utility model belongs to the technical field of the eucommia ulmoides processing equipment, concretely relates to used system in eucommia ulmoides extract powder production process. The utility model provides a system, include: one end of the extraction kettle is connected with a water inlet pipeline; the extraction kettle is connected in series with a horizontal screw centrifuge, a tubular centrifuge, a membrane filtration device, a membrane concentration device and a spray dryer in turn. The beneficial effects of the utility model reside in that: in the system provided by the utility model, three-stage filtration, namely three-stage filtration of a horizontal screw centrifuge, a tubular centrifuge and a membrane filtration device, is adopted, so that impurities in the feed liquid are filtered to the maximum extent, and the quality of the product is ensured; the system provided by the utility model realizes the continuous production of the eucommia ulmoides fine powder, and all links are carried out simultaneously in the whole production process, thereby improving the production efficiency; through the eucommia ulmoides fine powder produced by the system of the utility model, the content of active ingredients is higher.
Description
Technical Field
The utility model belongs to the technical field of the eucommia ulmoides processing equipment, concretely relates to used system in eucommia ulmoides extract powder production process.
Background
Regarding the processing equipment of the eucommia ulmoides fine powder, the applicant has studied and improved, and the applicant discloses in CN208300895U a processing equipment of the eucommia ulmoides fine powder, which is characterized by comprising a water washing device, an air drying device, a microwave drying device and a crushing device; the washing device comprises a first-stage washing tank and a second-stage washing tank, wherein the first-stage washing tank comprises an air pipe arranged in the tank, the air pipe is connected with an air compressor outside the tank, and a screen conveying track is arranged above the air pipe; the secondary water washing tank comprises a spray pipeline arranged above the secondary water washing tank, a high-pressure spray head is arranged on the spray pipeline, and the spray pipeline is connected with the water tank through a high-pressure water pump; transferring eucommia ulmoides between the first-stage water washing tank and the second-stage water washing tank through a screen; the air drying device is a continuous flow-through drying device; the microwave drying device comprises a conveyor belt, more than one microwave heating unit is arranged above the conveyor belt, an exhaust and moisture removal pipeline communicated with the interior of the microwave heating unit is arranged above the microwave heating unit, and an exhaust fan is arranged on the exhaust and moisture removal pipeline; the crushing device comprises a crusher, and the tail end of a conveyor belt of the microwave drying device is positioned above a feed inlet of the crusher.
The processing equipment mainly focuses on the links of cleaning and crushing the eucommia ulmoides raw material, and the subsequent extraction treatment and refining after extraction are not disclosed correspondingly, but the inventor finds that the obtained eucommia ulmoides fine powder has the defects of more impurities and relatively low content of active ingredients in the extraction process of the eucommia ulmoides fine powder, and also needs corresponding equipment for improving the matched process in the process of further improving the eucommia ulmoides fine powder product.
Therefore, in view of the above situation, the inventor invents a corresponding production system for the production process of extracting and refining the eucommia ulmoides fine powder, and provides equipment support for improving the production efficiency of the eucommia ulmoides fine powder, the purity of the product and the content of active ingredients.
Disclosure of Invention
In order to solve the technical problem, the utility model provides a system used in the production process of eucommia ulmoides fine powder.
The utility model provides an used system in eucommia ulmoides fine powder production process mainly includes: an extraction kettle, a horizontal screw centrifuge, a tubular centrifuge, membrane filtration equipment, membrane concentration equipment and a spray dryer; the extraction kettle, the horizontal screw centrifuge, the tubular centrifuge, the membrane filtration equipment, the membrane concentration equipment and the spray dryer are sequentially connected in series through pipelines.
All pipelines are provided with delivery pumps.
The two ends of the membrane filtration equipment are respectively connected with a first storage tank and a clear liquid tank; the first storage tank is connected with an outlet pipeline of the tubular centrifuge.
One end of the membrane concentration equipment is connected with a second storage tank and a third storage tank in parallel, and the other end of the membrane concentration equipment is connected with a pure water tank; the second storage tank and the third storage tank are respectively connected with the spray dryer; the second storage tank and the third storage tank are respectively provided with a pipeline which converges to the pure water tank.
One end of the membrane concentration equipment is connected with a second storage tank and a third storage tank in parallel, and the other end of the membrane concentration equipment is connected with a pure water tank; the second storage tank is sequentially connected with the fourth storage tank and the spray dryer; the third storage tank is connected with the fourth storage tank and the spray dryer in sequence; and the second storage tank and the third storage tank are respectively provided with a pipeline which converges to the pure water tank.
As a preferred, the utility model provides an used system in the eucommia ulmoides fine powder production process, its structure is as follows:
the outlet of the extraction kettle is connected with a horizontal screw centrifuge; the horizontal screw centrifuge is connected with the inlet of the tubular centrifuge; a discharge pipeline of the tubular centrifuge is divided into two paths, one path is connected with the first storage tank, and the other path is connected with the membrane filtration equipment; the first storage tank is connected with the membrane filtration equipment through a pipeline; the other end of the membrane filtration equipment is connected with a clear liquid tank, and a discharge pipeline of the clear liquid tank is divided into two paths which are respectively communicated with the second storage tank and the third storage tank; the second storage tank and the third storage tank are respectively connected with the membrane concentration equipment in parallel; the second storage tank is sequentially connected with the fourth storage tank and the spray dryer; the third storage tank is connected with the fourth storage tank and the spray dryer in sequence; and the second storage tank and the third storage tank are respectively provided with a pipeline which converges to the pure water tank.
The extraction kettle is connected with the water purifier 1 through a water inlet pipeline.
The lower part in the extraction kettle is provided with a filter screen.
The distance between the filter screen and the extraction kettle is 1/20-1/10 of the height of the extraction kettle.
In the system, the delivery pumps are arranged between the water purifier and the extraction kettle, between the extraction kettle and the horizontal screw centrifuge, between the horizontal screw centrifuge and the pipe centrifuge, between the pipe centrifuge and the first storage tank, between the clear liquid tank and the second storage tank/the third storage tank, between the second storage tank and the fourth storage tank, between the third storage tank and the fourth storage tank, and between the fourth storage tank and the spray dryer.
The beneficial effects of the utility model reside in that:
(1) in the system provided by the utility model, three-stage filtration, namely three-stage filtration of a horizontal screw centrifuge, a tubular centrifuge and a membrane filtration device, is adopted, so that impurities in the feed liquid are filtered to the maximum extent, and the quality of the product is ensured;
(2) the system provided by the utility model realizes the continuous production of the eucommia ulmoides fine powder, and all links are carried out simultaneously in the whole production process, thereby improving the production efficiency;
(3) through the utility model discloses an eucommia ulmoides fine powder that system produced, active ingredient content wherein is higher, for example, chlorogenic acid content is about 6.1%, geniposide about 0.17%, geniposide about 5.5%, rutin is about 0.7%, aucubin is about 7.6%, total active ingredient content is about 20%, is 6 ~ 7 times of the fine powder active substance content of production under traditional equipment and the process condition.
Drawings
FIG. 1 is a schematic structural view of example 1;
FIG. 2 is a schematic structural view of example 2;
FIG. 3 is a schematic structural view of embodiment 3;
FIG. 4 is a schematic structural view of example 4;
FIG. 5 is a schematic structural view of example 5;
in the figure, 1-a water purifier, 2 an extraction kettle, 3-a horizontal screw centrifuge, 4-a tubular centrifuge, 5-a membrane filtration device, 6-a membrane concentration device, 7-a spray dryer, 501-a first storage tank, 502-a clear liquid tank, 601-a second storage tank, 602-a third storage tank, 603-a pure water tank and 701-a fourth storage tank.
Detailed Description
The invention will be further described with reference to the accompanying drawings and specific embodiments so that those skilled in the art may better understand the invention, but the invention is not limited thereto.
Example 1
The system used in the production process of the eucommia ulmoides fine powder mainly comprises the following steps: the device comprises an extraction kettle 2, a horizontal screw centrifuge 3, a tubular centrifuge 4, a membrane filtration device 5, a membrane concentration device 6 and a spray dryer 7; the extraction kettle 2, the horizontal screw centrifuge 3, the tubular centrifuge 4, the membrane filtering equipment 5, the membrane concentration equipment 6 and the spray dryer 7 are sequentially connected in series through pipelines.
All pipelines are provided with conveying pumps for conveying materials.
Example 2
The system used in the production process of the eucommia ulmoides fine powder mainly comprises the following steps: the device comprises an extraction kettle 2, a horizontal screw centrifuge 3, a tubular centrifuge 4, a membrane filtration device 5, a membrane concentration device 6 and a spray dryer 7; the extraction kettle 2, the horizontal screw centrifuge 3, the tubular centrifuge 4, the membrane filtering equipment 5, the membrane concentration equipment 6 and the spray dryer 7 are sequentially connected in series through pipelines.
The two ends of the membrane filtering device 5 are respectively connected with a first storage tank 501 and a clear liquid tank 502; the first tank 501 is connected to the outlet line of the tube centrifuge 4.
All pipelines are provided with conveying pumps for conveying materials.
Example 3
The system used in the production process of the eucommia ulmoides fine powder mainly comprises the following steps: the device comprises an extraction kettle 2, a horizontal screw centrifuge 3, a tubular centrifuge 4, a membrane filtration device 5, a membrane concentration device 6 and a spray dryer 7; the extraction kettle 2, the horizontal screw centrifuge 3, the tubular centrifuge 4, the membrane filtering equipment 5, the membrane concentration equipment 6 and the spray dryer 7 are sequentially connected in series through pipelines.
The two ends of the membrane filtering device 5 are respectively connected with a first storage tank 501 and a clear liquid tank 502; the first tank 501 is connected to the outlet line of the tube centrifuge 4.
One end of the membrane concentration device 6 is connected in parallel with a second storage tank 601 and a third storage tank 602, and the other end is connected with a pure water tank 603; the second storage tank 601 and the third storage tank 602 are respectively connected with the spray dryer 7; the second tank 601 and the third tank 602 also have a pipe respectively converging to a pure water tank 603.
All pipelines are provided with conveying pumps for conveying materials.
Example 4
The system used in the production process of the eucommia ulmoides fine powder mainly comprises the following steps: the device comprises an extraction kettle 2, a horizontal screw centrifuge 3, a tubular centrifuge 4, a membrane filtration device 5, a membrane concentration device 6 and a spray dryer 7; the extraction kettle 2, the horizontal screw centrifuge 3, the tubular centrifuge 4, the membrane filtering equipment 5, the membrane concentration equipment 6 and the spray dryer 7 are sequentially connected in series through pipelines.
The two ends of the membrane filtering device 5 are respectively connected with a first storage tank 501 and a clear liquid tank 502; the first tank 501 is connected to the outlet line of the tube centrifuge 4.
One end of the membrane concentration device 6 is connected in parallel with a second storage tank 601 and a third storage tank 602, and the other end is connected with a pure water tank 603; the second storage tank 601 is connected with the fourth storage tank 701 and the spray dryer 7 in sequence; the third storage tank 602 is connected with the fourth storage tank 701 and the spray dryer 7 in sequence; and the second storage tank 601 and the third storage tank 602 are respectively provided with a pipeline which converges to the pure water tank 603.
All pipelines are provided with conveying pumps for conveying materials.
Example 5
The system used in the production process of the eucommia ulmoides fine powder mainly comprises the following steps: the device comprises an extraction kettle 2, a horizontal screw centrifuge 3, a tubular centrifuge 4, a membrane filtration device 5, a membrane concentration device 6 and a spray dryer 7;
the extraction kettle 2 is connected with the water purifier 1 through a water inlet pipeline; a filter screen is arranged at the lower part in the extraction kettle 2;
the distance between the filter screen and the extraction kettle 2 is about 1/12 of the height of the extraction kettle 2;
the outlet of the extraction kettle 2 is connected with a horizontal screw centrifuge 3; the horizontal screw centrifuge 3 is connected with the inlet of the tubular centrifuge 4; the discharge pipeline of the tubular centrifuge 4 is divided into two paths, one path is connected with the first storage tank 501, and the other path is connected with the membrane filtration equipment 5; the first storage tank 501 is connected with the membrane filtration device 5 through a pipeline; the other end of the membrane filtration device 5 is connected with a clear liquid tank 502, and a discharge pipeline of the clear liquid tank 502 is divided into two paths which are respectively communicated with a second storage tank 601 and a third storage tank 602;
one end of the membrane concentration device 6 is connected in parallel with a second storage tank 601 and a third storage tank 602, and the other end is connected with a pure water tank 603; the second storage tank 601 is connected with the fourth storage tank 701 and the spray dryer 7 in sequence; the third storage tank 602 is connected with the fourth storage tank 701 and the spray dryer 7 in sequence; and the second storage tank 601 and the third storage tank 602 are respectively provided with a pipeline which converges to the pure water tank 603.
When the system operates, pure water in the water purifier 1 enters the extraction kettle 2, the cleaned folium cortex eucommiae materials are put into the extraction kettle 2 for extraction, the extracted materials are filtered by a filter screen at the lower part of the extraction kettle 2, filtrate sequentially enters the horizontal spiral centrifugal machine 3, the tubular centrifugal machine 4 and the membrane filtering device 5 for three-stage filtration, the filtered filtrate enters the membrane concentration device 6 for concentration, and the concentrated materials enter the spray dryer 7 for spray drying, so that the cortex eucommiae fine powder product with high active ingredient content can be obtained.
Through the utility model discloses a system draws the back to the eucommia ulmoides fine powder, and the content of the active ingredient in the eucommia ulmoides fine powder of gained specifically is: the content of chlorogenic acid is about 6.1%, geniposide is about 0.17%, geniposide is about 5.5%, rutin is about 0.7%, aucubin is about 7.6%, and the content of total active ingredients is about 20%, which is 6-7 times of the content of active substances of refined powder produced under the traditional equipment and process conditions.
Claims (10)
1. Used system in the refined powder production process of eucommia ulmoides, its characterized in that, the system include: an extraction kettle (2), a horizontal screw centrifuge (3), a tubular centrifuge (4), membrane filtration equipment (5), membrane concentration equipment (6) and a spray dryer (7); the extraction kettle (2), the horizontal screw centrifuge (3), the tubular centrifuge (4), the membrane filtration equipment (5), the membrane concentration equipment (6) and the spray dryer (7) are sequentially connected in series through pipelines.
2. The system for producing refined eucommia ulmoides powder according to claim 1, wherein all pipes are provided with a transfer pump.
3. The system for producing the eucommia ulmoides fine powder according to claim 1, wherein a first storage tank (501) and a clear liquid tank (502) are respectively connected to two ends of the membrane filtration device (5); the first storage tank (501) is connected with an outlet pipeline of the tube centrifuge (4).
4. The system for producing refined eucommia ulmoides powder according to claim 1, wherein one end of the membrane concentration device (6) is connected in parallel with a second storage tank (601) and a third storage tank (602), and the other end is connected with a pure water tank (603); the second storage tank (601) and the third storage tank (602) are respectively connected with the spray dryer (7); the second storage tank (601) and the third storage tank (602) are respectively provided with a pipeline which converges to the pure water tank (603).
5. The system for use in the production of fine eucommia ulmoides powder according to claim 1, wherein,
one end of the membrane concentration equipment (6) is connected with a second storage tank (601) and a third storage tank (602) in parallel, and the other end is connected with a pure water tank (603); the second storage tank (601) is sequentially connected with the fourth storage tank (701) and the spray dryer (7); the third storage tank (602) is sequentially connected with the fourth storage tank (701) and the spray dryer (7); and the second storage tank (601) and the third storage tank (602) are respectively provided with a pipeline which converges to the pure water tank (603).
6. The system for use in the production of fine eucommia ulmoides powder according to claim 1, wherein,
the outlet of the extraction kettle (2) is connected with a horizontal screw centrifuge (3); the horizontal screw centrifuge (3) is connected with the inlet of the tubular centrifuge (4); a discharge pipeline of the tubular centrifuge (4) is divided into two paths, one path is connected with the first storage tank (501), and the other path is connected with the membrane filtration equipment (5); the first storage tank (501) is connected with the membrane filtration equipment (5) through a pipeline; the other end of the membrane filtering device (5) is connected with a clear liquid tank (502), and a discharge pipeline of the clear liquid tank (502) is divided into two paths which are respectively communicated with a second storage tank (601) and a third storage tank (602); the second storage tank (601) and the third storage tank (602) are respectively connected with the membrane concentration equipment (6) in parallel; the second storage tank (601) is sequentially connected with the fourth storage tank (701) and the spray dryer (7); the third storage tank (602) is sequentially connected with the fourth storage tank (701) and the spray dryer (7); and the second storage tank (601) and the third storage tank (602) are respectively provided with a pipeline which converges to the pure water tank (603).
7. The system for producing refined eucommia ulmoides powder according to claim 6, wherein the extraction tank (2) is connected to the water purifier (1) through a water inlet pipe.
8. The system for producing eucommia ulmoides oliver powder according to claim 6, wherein a filter screen is installed at the lower part of the extraction pot (2).
9. The system for producing eucommia ulmoides oliver extract powder according to claim 8, wherein the distance between the filter screen and the extraction kettle (2) is 1/20-1/10 of the height of the extraction kettle (2).
10. The system for producing refined eucommia ulmoides powder according to claim 8 or 9, wherein a transfer pump is disposed between the water purifier (1) and the extraction kettle (2), between the extraction kettle (2) and the horizontal decanter centrifuge (3), between the horizontal decanter centrifuge (3) and the tubular centrifuge (4), between the tubular centrifuge (4) and the first storage tank (501), between the clear water tank and the second storage tank (601)/the third storage tank (602), between the second storage tank (601) and the fourth storage tank (701), between the third storage tank (602) and the fourth storage tank (701), and between the fourth storage tank (701) and the spray dryer (7).
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111973649A (en) * | 2020-09-04 | 2020-11-24 | 山东贝隆杜仲生物工程有限公司 | Production process and system of eucommia ulmoides fine powder |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111973649A (en) * | 2020-09-04 | 2020-11-24 | 山东贝隆杜仲生物工程有限公司 | Production process and system of eucommia ulmoides fine powder |
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