CN210845306U - Secondary separation tower for xylo-oligosaccharide extracting solution - Google Patents
Secondary separation tower for xylo-oligosaccharide extracting solution Download PDFInfo
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- CN210845306U CN210845306U CN201921470509.7U CN201921470509U CN210845306U CN 210845306 U CN210845306 U CN 210845306U CN 201921470509 U CN201921470509 U CN 201921470509U CN 210845306 U CN210845306 U CN 210845306U
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- tower body
- tower
- bearing
- air
- xylo
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Abstract
The utility model relates to an xylo-oligosaccharide extract secondary separation tower, including bearing post, the tower body, the spray pump, atomizer, air vortex tube, a heat exchanger, bear fossil fragments, the drainage pump, drive fan and control circuit, terminal surface and four at least bearing post connections under the tower body, a discharge gate is all established to tower body up end and lower terminal surface, a feed inlet is established to the tower body side surface, two at least air intakes and two at least air outlets, bear fossil fragments and inlay in the tower body, atomizer a plurality of inlay in bearing fossil fragments internal surface to communicate each other through feed inlet and spray pump, the heat exchanger inlays in the tower body and symmetric distribution is in bearing fossil fragments top and below tower body. This novel effectual improvement separation operating efficiency has reduced the height of knockout tower and has reduced the volume of knockout tower, and on the other hand is when effectively improving separation operating efficiency, the effectual operation energy consumption, the cost that has reduced the separation operation in addition to resource comprehensive recovery rate in the separation operation has been improved.
Description
Technical Field
The utility model relates to a xylo-oligosaccharide extract secondary separation tower belongs to concentrator technical field.
Background
The secondary separation tower is the main equipment during xylo-oligosaccharide production, but in the in-service use of actual production, the secondary separation tower that uses at present often is traditional structure, though can satisfy the use needs, but the secondary separation tower often the structure is complicated, volume and height all are great relatively, and the high-grade resource recovery utilization ratio of operation energy consumption is also low relatively, therefore traditional secondary separation tower has seriously influenced the improvement of xylo-oligosaccharide production efficiency and the reduction of manufacturing cost to caused comparatively serious waste of resources in process of production.
Therefore, in order to solve the above problems, it is urgently needed to develop a brand new secondary separation tower device for producing xylo-oligosaccharide so as to meet the requirements of practical use.
SUMMERY OF THE UTILITY MODEL
To the not enough that exists on the prior art, the utility model provides a xylo-oligosaccharide extract secondary knockout tower, this novel simple structure, the overall arrangement is compact reasonable, integrates the degree height, on the one hand than the effectual improvement separation operating efficiency of traditional secondary knockout tower, reduced the height of knockout tower and reduced the volume of knockout tower, on the other hand is when effectively improving separation operating efficiency, in addition effectual operation energy consumption, the cost that has reduced the separation operation to resource comprehensive recovery utilization rate in the separation operation has been improved.
In order to achieve the above purpose, the utility model discloses a realize through following technical scheme:
a secondary separation tower for xylo-oligosaccharide extracting solution comprises bearing columns, a tower body, a spray pump, an atomizing nozzle, air vortex tubes, a heat exchanger, bearing keels, drainage pumps, a driving fan and a control circuit, wherein the tower body is of a columnar closed cavity structure with the axis vertical to the horizontal plane, the lower end face of the tower body is connected with at least four bearing columns, the bearing columns are uniformly distributed around the axis of the tower body and form an included angle of 0-45 degrees with the axis of the tower body, the upper end face and the lower end face of the tower body are respectively provided with a discharge port, the side surface of the tower body is provided with a feed port, at least two air inlets and at least two air outlets, the discharge ports are respectively communicated with one drainage pump, the bearing keels are of frame structures which are coaxially distributed with the tower body, are embedded in the tower body and are connected with the inner surface of the tower body, the atomizing nozzle, and the atomizing nozzles are mutually connected in parallel and are mutually communicated with the spray pump through the feed inlet, the number of the heat exchangers is two, the heat exchangers are embedded in the tower body and are symmetrically distributed in the tower body above and below the bearing keel, and are coaxially distributed with the tower body, and each heat exchanger is mutually communicated with an air inlet and an air outlet to form a working group, wherein the air inlet of the heat exchanger above the bearing keel is communicated with the high-temperature exhaust port of the air vortex tube, the air inlet of the heat exchanger below the bearing keel is communicated with the low-temperature exhaust port of the air vortex tube, each air outlet is communicated with the air inlet of the air vortex tube through a driving fan, at least one air vortex tube is arranged, the drainage pump, the driving fan and the control circuit are all connected with the outer surface of the tower body, and the control circuit is electrically connected with the spray pump, the drainage pump and the driving fan respectively.
Furthermore, the height of the bearing keel is 1/10-1/5 of the height of the tower body, and the distance between the lower end face of the bearing keel and the lower end face of the tower body is not less than 30% of the height of the tower body.
Furthermore, the bearing columns are connected with each other through at least one tray which is coaxially distributed with the tower body, the distance between the tray and the lower end face of the tower body is not less than 10 cm, and the air vortex tube is connected with the upper end face of the tray.
Furthermore, when the distance between the heat exchanger and the bearing keel is not less than 10 cm, and two or more heat exchangers are arranged above and below the bearing keel, two adjacent heat exchangers are connected in series.
Furthermore, the feed inlet, the air inlet and the air outlet are respectively provided with at least one control valve, and the control valves are electrically connected with the control circuit.
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, it is compact reasonable to arrange, integrates the degree height, on the one hand than the effectual improvement separation operating efficiency of traditional secondary knockout tower, has reduced the height of knockout tower and has reduced the volume of knockout tower, and on the other hand is when effectively improving separation operating efficiency, the effectual operation energy consumption, the cost that have reduced the separation operation in addition to resource comprehensive recovery rate in the separation operation has been improved.
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.
The secondary separation tower of xylo-oligosaccharide extract as shown in figure 1 comprises a bearing column 1, a tower body 2, a spray pump 3, an atomizing spray head 4, an air vortex tube 5, a heat exchanger 6, a bearing keel 7, a drainage pump 8, a driving fan 9 and a control circuit 10, wherein the tower body 2 is a columnar closed cavity structure with the axis vertical to the horizontal plane, the lower end surface of the tower body is connected with at least four bearing columns 1, each bearing column 1 is uniformly distributed around the axis of the tower body 2 and forms an included angle of 0-45 degrees with the axis of the tower body 2, the upper end surface and the lower end surface of the tower body 2 are respectively provided with a discharge port 21, the side surface of the tower body 2 is provided with a feed port 22, at least two air inlets 23 and at least two air outlets 24, wherein the discharge ports 21 are respectively communicated with one drainage pump 8, the bearing keel 7 is a frame structure coaxially distributed with the tower body, a plurality of atomizing nozzles 4 are embedded on the inner surface of the bearing keel 7 and form an included angle of 0-45 degrees with the axis of the tower body 2, the atomizing nozzles 4 are mutually connected in parallel and are mutually communicated with the spray pump 3 through a feed inlet 22, two heat exchangers 6 are embedded in the tower body 3 and are symmetrically distributed in the tower body 3 above and below the bearing keel 7 and are coaxially distributed with the tower body 3, each heat exchanger 6 is mutually communicated with an air inlet 23 and an air outlet 24 to form a working group, wherein the air inlet 23 of the heat exchanger 6 above the bearing keel 7 is communicated with a high-temperature exhaust port of the air vortex tube 5, the air inlet 23 of the heat exchanger 6 below the bearing keel 7 is communicated with a low-temperature exhaust port of the air vortex tube 5, each air outlet 24 is communicated with an air inlet of the air vortex tube 5 through a driving fan 9, at least one air vortex tube 5 is connected with the side surface of, the drainage pump 8, the driving fan 9 and the control circuit 10 are all connected with the outer surface of the tower body 2, and the control circuit 10 is respectively and electrically connected with the spraying pump 3, the drainage pump 8 and the driving fan 9.
In this embodiment, the height of the bearing keel 7 is 1/10-1/5 of the height of the tower body 3, and the distance between the lower end face of the bearing keel 7 and the lower end face of the tower body 3 is not less than 30% of the height of the tower body 3.
In this embodiment, the support columns 1 are connected to each other through at least one tray 11 coaxially distributed with the tower body 2, a distance between the tray 11 and the lower end face of the tower body 2 is not less than 10 cm, and the air vortex tube 5 is connected to the upper end face of the tray 11.
In this embodiment, when the distance between the heat exchanger 6 and the bearing keel 7 is not less than 10 cm, and two or more heat exchangers 6 are arranged above and below the bearing keel 7, two adjacent heat exchangers 6 are connected in series.
In this embodiment, the feed port 22, the air inlet 23 and the air outlet 24 are all provided with at least one control valve 12, and the control valve 12 is electrically connected with the control circuit 10.
In this embodiment, the control circuit 10 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 the concrete implementation, at first fixes a position the tower body through bearing the post, then to the tower body with spray pump, atomizer, air vortex tube, heat exchanger, bear fossil fragments, drainage pump, drive fan and control circuit and connect the location, treat to separate raw materials conveying pipeline intercommunication with tower body feed inlet and outside at last, collect the pipeline intercommunication with tower body up end and lower terminal surface discharge gate and outside material, communicate control circuit and external power system, can accomplish the novel assembly of cost.
When carrying out the separation operation, at first wait to separate raw materials conveying line through the outside that the pump that sprays is right and supply with the material and carry out the pressure boost injection, and form raw materials fog in the tower body through atomizer, all form negative pressure environment through drainage pump in tower body first and lower half simultaneously, through negative pressure environment and with the help of the different materials of raw materials fog under the action of gravity, partly tiny particle, discharge gate discharge from the tower body upper end is followed to low density and little quality material side, otherwise, the discharge gate is discharged bottom the tower body to big quality material side, thereby realize the material and collect.
When the vaporific material is discharged from the discharge ports of the upper end surface and the lower end surface of the tower body, partial external air and the gas in the heat exchanger in the tower body are pressurized by the driving fan and are conveyed into the air vortex tube, the high-temperature gas flow and the low-temperature gas flow are formed after the treatment of the air vortex tube, then the high-temperature gas flow is conveyed into the heat exchanger above the bearing keel, the material discharged from the upper end surface of the tower body is heated, the discharging speed of the material from the upper end of the tower body is improved, the low-temperature gas flow is conveyed into the heat exchanger below the bearing keel, the material discharged from the lower end surface of the tower body is cooled, the cooling and condensation of the material discharged from the lower end surface of the tower body are realized, the material quality is further improved, the discharging efficiency of the material flow from the lower end surface of the tower body is improved, finally the gas flow after the heat exchange, and the energy consumption of equipment operation is reduced.
This novel simple structure, it is compact reasonable to arrange, integrates the degree height, on the one hand than the effectual improvement separation operating efficiency of traditional secondary knockout tower, has reduced the height of knockout tower and has reduced the volume of knockout tower, and on the other hand is when effectively improving separation operating efficiency, the effectual operation energy consumption, the cost that have reduced the separation operation in addition to resource comprehensive recovery rate in the separation operation has been improved.
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 (6)
1. A xylo-oligosaccharide extract secondary knockout tower which characterized in that: the xylo-oligosaccharide extract secondary separation tower comprises bearing columns, a tower body, a spray pump, atomizing nozzles, air vortex tubes, a heat exchanger, bearing keels, drainage pumps, a driving fan and a control circuit, wherein the tower body is of a columnar closed cavity structure with the axis vertical to the horizontal plane, the lower end face of the tower body is connected with at least four bearing columns, the bearing columns are uniformly distributed around the axis of the tower body and form an included angle of 0-45 degrees with the axis of the tower body, the upper end face and the lower end face of the tower body are respectively provided with a discharge port, the side surface of the tower body is provided with a feed port, at least two air inlets and at least two air outlets, the discharge ports are respectively communicated with one drainage pump, the bearing keels are of a frame structure which is coaxially distributed with the tower body, are embedded in the tower body and are connected with the inner surface of the tower body, the atomizing nozzles are, and the atomizing nozzles are mutually connected in parallel and are mutually communicated with the spray pump through the feed inlet, the number of the heat exchangers is two, the heat exchangers are embedded in the tower body and are symmetrically distributed in the tower body above and below the bearing keel, and are coaxially distributed with the tower body, and each heat exchanger is mutually communicated with an air inlet and an air outlet to form a working group, wherein the air inlet of the heat exchanger above the bearing keel is communicated with the high-temperature exhaust port of the air vortex tube, the air inlet of the heat exchanger below the bearing keel is communicated with the low-temperature exhaust port of the air vortex tube, each air outlet is communicated with the air inlet of the air vortex tube through a driving fan, at least one air vortex tube is arranged, the drainage pump, the driving fan and the control circuit are all connected with the outer surface of the tower body, and the control circuit is electrically connected with the spray pump, the drainage pump and the driving fan respectively.
2. The secondary separation tower for xylo-oligosaccharide extracting solution as claimed in claim 1, wherein the height of the bearing keel is 1/10-1/5% of the height of the tower body, and the distance between the lower end face of the bearing keel and the lower end face of the tower body is not less than 30% of the height of the tower body.
3. The xylo-oligosaccharide extract secondary separation tower of claim 1, wherein the support columns are connected with each other through at least one tray coaxially distributed with the tower body, the distance between the tray and the lower end face of the tower body is not less than 10 cm, and the air vortex tube is connected with the upper end face of the tray.
4. The secondary separation tower for the xylo-oligosaccharide extracting solution as claimed in claim 1, wherein the distance between the heat exchanger and the bearing keel is not less than 10 cm, and when two or more heat exchangers are arranged above and below the bearing keel, two adjacent heat exchangers are connected in series.
5. The secondary separation tower for the xylo-oligosaccharide extracting solution as claimed in claim 1, wherein at least one control valve is arranged at each of the feeding port, the air inlet and the air outlet, and the control valves are electrically connected with a control circuit.
6. The secondary separation tower for xylo-oligosaccharide extracting solution as claimed in claim 1, wherein the control circuit is a circuit structure based on a programmable controller, and the control circuit is further provided with at least one data communication port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921470509.7U CN210845306U (en) | 2019-09-05 | 2019-09-05 | Secondary separation tower for xylo-oligosaccharide extracting solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921470509.7U CN210845306U (en) | 2019-09-05 | 2019-09-05 | Secondary separation tower for xylo-oligosaccharide extracting solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210845306U true CN210845306U (en) | 2020-06-26 |
Family
ID=71282754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921470509.7U Expired - Fee Related CN210845306U (en) | 2019-09-05 | 2019-09-05 | Secondary separation tower for xylo-oligosaccharide extracting solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210845306U (en) |
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2019
- 2019-09-05 CN CN201921470509.7U patent/CN210845306U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200626 Termination date: 20210905 |