CN210845514U - Xylo-oligosaccharide extract integral type secondary separation device - Google Patents

Xylo-oligosaccharide extract integral type secondary separation device Download PDF

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Publication number
CN210845514U
CN210845514U CN201921470508.2U CN201921470508U CN210845514U CN 210845514 U CN210845514 U CN 210845514U CN 201921470508 U CN201921470508 U CN 201921470508U CN 210845514 U CN210845514 U CN 210845514U
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China
Prior art keywords
separation
tank
xylo
cavity
secondary separation
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Expired - Fee Related
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CN201921470508.2U
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Chinese (zh)
Inventor
成成
刘亚军
刘亚川
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Henan Yuanlong Biological Technology Co ltd
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Henan Yuanlong Biological Technology Co ltd
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Abstract

The utility model relates to an xylo-oligosaccharide extract integral type secondary separation device, including bearing fossil fragments, the knockout drum, atomizer, ultrasonic atomization device, the molecular sieve filter, the negative pressure pump, spray pump, wash medicament jar and control circuit, the knockout drum is airtight cavity structures with wasing the medicament jar, wherein the knockout drum inlay in bearing fossil fragments and with bear fossil fragments coaxial distribution, it is at least one to wash the medicament jar, and bear fossil fragments lateral surface interconnect, wherein the molecular sieve filter inlays in the knockout drum, and with a knockout drum top-down equal separation one-level separation chamber, a second grade separation chamber, atomizer inlays in the one-level separation intracavity, establish two at least ultrasonic atomization device in the second grade separation intracavity. This novel effectual improvement separation operating efficiency of more traditional secondary splitter on the one hand, the very big improvement separation operating efficiency of on the other hand still effectually reduces the operation energy consumption cost and the equipment running loss of separation operation simultaneously.

Description

Xylo-oligosaccharide extract integral type secondary separation device
Technical Field
The utility model relates to a xylo-oligosaccharide extract integral type secondary separation device belongs to concentrator technical field.
Background
The secondary separation equipment for liquid materials is the main equipment during the production of xylo-oligosaccharide, but in the practical production and use, the currently used secondary separation equipment usually performs operations such as percolation, filter pressing and the like through a traditional ionic membrane filtering mechanism, or performs separation operations through equipment such as distillation, fractionation and the like, although the use requirements can be met, on one hand, the equipment structure is large in size, the operation and maintenance operation labor intensity is large, the cost is high, on the other hand, when separation is performed, the loss of the separation equipment is relatively large, parts such as a filter element and the like need to be frequently replaced, and meanwhile, the separation operation usually needs to be assisted by auxiliary systems such as heating equipment and the like, so that the separation operation efficiency and the separation operation continuity are low, the equipment operation and maintenance cost is high, and the efficiency and the cost of the separation operation of the liquid materials in the.
Therefore, in order to solve the above problems, it is urgently needed to develop a brand new secondary separation device for producing xylo-oligosaccharide so as to meet the requirements of practical use.
SUMMERY OF THE UTILITY MODEL
To exist not enough on the prior art, the utility model provides a xylo-oligosaccharide extract integral type secondary separator, this novel simple structure, the overall arrangement is compact reasonable, the degree of integration is high, on the one hand more traditional secondary splitter is effectual to be improved and to separate the operating efficiency, the structure volume of having simplified splitter and the degree of difficulty and the cost of maintaining the operation, on the other hand very big improvement separation operating efficiency, the operation energy consumption cost and the equipment running loss of separation operation still effectually having reduced simultaneously, thereby very big improvement the work efficiency and the separation operation continuity and the stability of separation operation, and reduced equipment running loss, equipment operation and maintenance cost have been reduced.
In order to achieve the above purpose, the utility model discloses a realize through following technical scheme:
an integrated secondary separation device for xylo-oligosaccharide extracting solution comprises a bearing keel, a separation tank, an atomizing nozzle, an ultrasonic atomizing device, a molecular sieve filter, a negative pressure pump, a spray pump, a cleaning agent tank and a control circuit, wherein the separation tank and the cleaning agent tank are of a closed cavity structure, the separation tank is embedded in the bearing keel and is coaxially distributed with the bearing keel, at least one cleaning agent tank is connected with the outer side surface of the bearing keel, the molecular sieve filter is embedded in the separation tank, the separation tank is divided into a primary separation cavity and a secondary separation cavity from top to bottom, the primary separation cavity is communicated with the secondary separation cavity through the molecular sieve filter, the upper end surface of the separation tank corresponding to the primary separation cavity is provided with a discharge port and a cleaning port and is communicated with the negative pressure pump through the discharge port and is communicated with the spray pump through the cleaning port, the side surface of the separation tank corresponding to the primary separation cavity is provided with a drain outlet, atomizer is a plurality of, inlay in the one-level separation intracavity and with wash mouthful intercommunication, establish two at least ultrasonic atomization device in the second grade separation intracavity, and each ultrasonic atomization device encircles second grade separation chamber axis equipartition in second grade separation chamber bottom, a charge door and a bin outlet are established to the separator tank lateral wall that second grade separation chamber corresponds, the negative pressure pump, the spray pump all is connected with bearing fossil fragments up end, and the spray pump passes through the honeycomb duct respectively with the washing mouth and the washing medicament jar intercommunication of separator tank, control circuit respectively with ultrasonic atomization device, the negative pressure pump, spray pump electrical connection.
Furthermore, a temperature sensor and an air pressure sensor are arranged in the primary separation cavity and the secondary separation cavity of the separation tank, and the temperature sensor and the air pressure sensor are electrically connected with the control circuit.
Furthermore, the axis of the atomizing nozzle is intersected with the axis of the molecular sieve filter.
Furthermore, at least one heat exchanger is arranged in the secondary separation cavity, and the heat exchanger corresponds to the inner surface of the side wall of the separation tank of the secondary separation cavity.
Furthermore, the control circuit is a circuit structure based on a programmable controller, and the control circuit is additionally provided with at least one data communication port.
This novel simple structure, the overall arrangement is compact reasonable, the degree of integration is high, on the one hand than the effectual improvement separation operating efficiency of traditional secondary splitter, the structure volume of having simplified splitter and the degree of difficulty and the cost of maintaining the operation, on the other hand very big improvement separation operating efficiency, the effectual operation energy consumption cost and the equipment running loss that has reduced the separation operation simultaneously, thereby very big improvement the work efficiency and the separation operation continuity and the stability of separation operation, and reduced equipment running loss, equipment operation and maintenance cost have been reduced.
Drawings
The present invention will be described in detail with reference to the accompanying drawings and specific embodiments.
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
In order to make the utility model realize, the technical end, the creation characteristics, the achievement purpose and the efficacy are easy to understand and understand, and the utility model is further explained by combining the specific implementation mode.
FIG. 1 shows an integrated secondary separation device for xylo-oligosaccharide extract, which comprises a bearing keel 1, a separation tank 2, an atomizer 3, an ultrasonic atomizer 4, a molecular sieve filter 5, a negative pressure pump 6, a spray pump 7, a cleaning agent tank 8 and a control circuit 9, wherein the separation tank 2 and the cleaning agent tank 8 are both of a closed cavity structure, the separation tank 2 is embedded in the bearing keel 1 and coaxially distributed with the bearing keel 1, at least one cleaning agent tank 8 is connected with the outer side surface of the bearing keel 1, the molecular sieve filter 5 is embedded in the separation tank 2, the separation tank 2 is divided into a primary separation chamber 21 and a secondary separation chamber 22 from top to bottom, the primary separation chamber 21 and the secondary separation chamber 22 are mutually communicated through the molecular sieve filter 5, a discharge port 23 and a cleaning port 24 are arranged on the upper end surface of the separation tank corresponding to the primary separation chamber 21, and communicate with negative pressure pump 6 through bin outlet 23, communicate with spray pump 7 through wash port 24, a drain 25 is established to the knockout drum 2 side surface that the one-level separation chamber 21 corresponds, atomizer 3 is a plurality of, inlay in the one-level separation chamber 21 and communicate with wash port 24, establish two at least ultrasonic atomization device 4 in the second grade separation chamber 22, and each ultrasonic atomization device 4 encircles the equipartition of second grade separation chamber 22 axis in second grade separation chamber 22 bottom, a charge door 26 and a bin outlet 23 are established to the knockout drum 2 lateral wall that the second grade separation chamber 22 corresponds, negative pressure pump 6, spray pump 7 all is connected with bearing keel 1 up end, and spray pump 7 communicates with wash port 24 and washing medicament jar 8 of knockout drum 2 respectively through the honeycomb duct, control circuit 9 respectively with ultrasonic atomization device 4, negative pressure pump 6, spray pump 7 electrical connection.
In this embodiment, the first-stage separation cavity 21 and the second-stage separation cavity 22 of the separation tank 2 are both provided with a temperature sensor 10 and an air pressure sensor 11, and the temperature sensor 10 and the air pressure sensor 11 are both electrically connected with the control circuit 9.
In this embodiment, the axis of the atomizer 3 intersects with the axis of the molecular sieve filter 5.
In this embodiment, at least one heat exchanger 12 is disposed in the secondary separation cavity 22, and the heat exchanger 12 and the inner surface of the sidewall of the separation tank 2 correspond to the secondary separation cavity 22.
In this embodiment, the control circuit 9 is a circuit structure based on a programmable controller, and the control circuit is further provided with at least one data communication port.
This is novel in concrete implementation, at first to constituting this neotype fossil fragments that bear, knockout drum, atomizer, ultrasonic atomization device, molecular sieve filter, negative pressure pump, spray pump, washing medicament jar and control circuit assemble, then with the knockout drum through charge door and outside material supply pipeline intercommunication, collect the pipeline intercommunication with the separation material with second grade separation chamber is direct, the pipeline intercommunication is collected with the separation material to the one-level separation chamber through negative pressure pump, communicate control circuit and external power system afterwards, thereby accomplish this novel assembly.
When the heat exchanger is assembled, the heat exchanger can be connected with an external temperature regulating system according to the use requirement. L is
When the materials are separated, firstly, the external materials to be separated are filled into the secondary separation cavity through the feed inlet, then the ultrasonic atomization device is driven to operate, the moisture and part of the organic liquid materials in the secondary separation cavity are ultrasonically atomized, and the inorganic salt and part of the liquid organic liquid materials are retained in the secondary separation cavity; and then driving a negative pressure pump to operate, forming a low-pressure environment in the primary separation cavity, filtering and separating liquid mist in the secondary separation cavity through a molecular sieve filter, conveying separated mist-state materials with small particle sizes into the primary separation cavity, conveying the separated mist-state materials into a separated material collecting pipeline through a discharge hole of the primary separation cavity, and simultaneously returning residual materials with large particle sizes filtered by the molecular sieve filter into the secondary separation cavity and conveying the residual materials into the separated material collecting pipeline from a discharge hole corresponding to the secondary separation cavity, thereby completing separation operation.
In addition, when the operation, accessible heat exchanger is connected with outside temperature regulating system in addition, realizes improving material atomizing operating efficiency to material temperature regulation in the secondary separation chamber.
After the separation operation is completed, the medicament in the cleaning medicament tank is pressurized and conveyed to the atomizing nozzle through the spraying pump, and is sprayed to the molecular sieve filter through the atomizing nozzle to reversely clean the molecular sieve filter, so that the aims of improving the maintenance efficiency and the operation continuity of equipment and reducing the maintenance cost and the replacement cost of the equipment are fulfilled.
This novel simple structure, the overall arrangement is compact reasonable, the degree of integration is high, on the one hand than the effectual improvement separation operating efficiency of traditional secondary splitter, the structure volume of having simplified splitter and the degree of difficulty and the cost of maintaining the operation, on the other hand very big improvement separation operating efficiency, the effectual operation energy consumption cost and the equipment running loss that has reduced the separation operation simultaneously, thereby very big improvement the work efficiency and the separation operation continuity and the stability of separation operation, and reduced equipment running loss, equipment operation and maintenance cost have been reduced.
It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.

Claims (5)

1. The utility model provides a xylo-oligosaccharide extract integral type secondary separation device which characterized in that: the integrated secondary separation device for the xylo-oligosaccharide extracting solution comprises a bearing keel, a separation tank, an atomizing nozzle, an ultrasonic atomizing device, a molecular sieve filter, a negative pressure pump, a spray pump, a cleaning agent tank and a control circuit, wherein the separation tank and the cleaning agent tank are of an airtight cavity structure, the separation tank is embedded in the bearing keel and is coaxially distributed with the bearing keel, at least one cleaning agent tank is connected with the outer side surface of the bearing keel, the molecular sieve filter is embedded in the separation tank, the separation tank is divided into a primary separation cavity and a secondary separation cavity from top to bottom, the primary separation cavity and the secondary separation cavity are communicated with each other through the molecular sieve filter, the upper end surface of the separation tank corresponding to the primary separation cavity is provided with a discharge hole and a cleaning hole and is communicated with the negative pressure pump through the discharge hole and is communicated with the spray pump through the cleaning hole, a drain is established to the separator tank side surface that the one-level separation chamber corresponds, atomizer is a plurality of, inlay in the one-level separation intracavity and with wash the mouth intercommunication, two at least ultrasonic atomization devices are established to the second grade separation intracavity, and each ultrasonic atomization device encircles second grade separation chamber axis equipartition in second grade separation chamber bottom, a charge door and a bin outlet are established to the separator tank lateral wall that second grade separation chamber corresponds, negative pressure pump, spray pump all with bear fossil fragments up end and be connected, just spray pump pass through the honeycomb duct respectively with the washing mouth of separator tank and wash the medicament jar intercommunication, control circuit respectively with ultrasonic atomization device, negative pressure pump, spray pump electrical connection.
2. The integrated secondary separation device for xylo-oligosaccharide extracting solution as claimed in claim 1, wherein a temperature sensor and an air pressure sensor are respectively arranged in the primary separation cavity and the secondary separation cavity of the separation tank, and the temperature sensor and the air pressure sensor are electrically connected with the control circuit.
3. The integrated secondary separation device for xylo-oligosaccharide extracting solution as claimed in claim 1, wherein the axis of the atomizing nozzle intersects with the axis of the molecular sieve filter.
4. The integrated secondary separation device for the xylo-oligosaccharide extracting solution as claimed in claim 1, wherein at least one heat exchanger is arranged in the secondary separation chamber, and the heat exchanger is arranged on the inner surface of the side wall of the separation tank corresponding to the secondary separation chamber.
5. The integrated secondary separation device for xylo-oligosaccharide extracting solution as claimed in claim 1, wherein said control circuit is a circuit structure based on a programmable controller, and said control circuit is further provided with at least one data communication port.
CN201921470508.2U 2019-09-05 2019-09-05 Xylo-oligosaccharide extract integral type secondary separation device Expired - Fee Related CN210845514U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921470508.2U CN210845514U (en) 2019-09-05 2019-09-05 Xylo-oligosaccharide extract integral type secondary separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921470508.2U CN210845514U (en) 2019-09-05 2019-09-05 Xylo-oligosaccharide extract integral type secondary separation device

Publications (1)

Publication Number Publication Date
CN210845514U true CN210845514U (en) 2020-06-26

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ID=71294672

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921470508.2U Expired - Fee Related CN210845514U (en) 2019-09-05 2019-09-05 Xylo-oligosaccharide extract integral type secondary separation device

Country Status (1)

Country Link
CN (1) CN210845514U (en)

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200626

Termination date: 20210905

CF01 Termination of patent right due to non-payment of annual fee