CN210845304U - Self-circulation xylo-oligosaccharide concentration mechanism - Google Patents
Self-circulation xylo-oligosaccharide concentration mechanism Download PDFInfo
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- CN210845304U CN210845304U CN201921469975.3U CN201921469975U CN210845304U CN 210845304 U CN210845304 U CN 210845304U CN 201921469975 U CN201921469975 U CN 201921469975U CN 210845304 U CN210845304 U CN 210845304U
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Abstract
The utility model relates to a self-loopa xylo-oligosaccharide concentrated mechanism, including bearing fossil fragments, concentrated operation jar, negative-pressure air fan, shunt tubes, collector pipe, main booster pump, pressure sensor, consistency transmitter, temperature sensor and control circuit, concentrated operation jar equipartition is in bearing fossil fragments, and each concentrated operation jar passes through shunt tubes and main booster pump intercommunication, through collector pipe and negative-pressure air fan intercommunication, and concentrated operation jar is including a jar body, molecular sieve filter, honeycomb duct, drainage tube, electric heater unit, supplementary booster pump and circulating pump, control circuit and the outer surface connection of bearing fossil fragments. Compared with the traditional xylo-oligosaccharide concentration equipment, the utility model greatly simplifies the equipment structure and volume; on the other hand, the working efficiency of concentration operation and the automation degree of the concentration operation are greatly improved, and the comprehensive recycling rate of materials in the concentration operation is effectively improved.
Description
Technical Field
The utility model relates to a self-loopa xylo-oligosaccharide concentrated mechanism belongs to concentrator technical field.
Background
Xylo-oligosaccharide is in the production process, need carry out the concentrated operation to the liquid material to satisfy the needs of xylo-oligosaccharide production shaping processing operation, to this production needs, current although have multiple type to get the concentrator can satisfy the operation needs, but the numerous concentrator that use at present often all has all defects such as the structure is bulky, the structure is complicated in the different degree, for example patent application number is: "201720135886. X" is a purification and concentration device for xylo-oligosaccharide ", so that on one hand, the installation operation of the current concentration device needs to occupy larger field space, the construction and use flexibility and the convenience are poor, and meanwhile, the workload and the labor intensity of the equipment maintenance and management operation are large; on the other hand, the material circulation path of the concentration operation is long, the working efficiency of the concentration operation is seriously influenced, the concentration purity of the material is relatively low during the concentration operation, beneficial components such as xylo-oligosaccharide with higher content are still contained in the production waste liquid after concentration, so that the serious material waste is caused, the production efficiency, the quality and the yield of the xylo-oligosaccharide are greatly influenced, and the serious pollution to the environment is caused due to the high content of the components such as the xylo-oligosaccharide in the waste liquid after concentration.
Therefore, in order to solve the above problems, it is urgently needed to develop a brand new xylo-oligosaccharide concentration device to meet the needs of practical use.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects in the prior art, the utility model provides a self-circulation type xylo-oligosaccharide concentration mechanism, which has simple structure, compact and reasonable layout and flexible and convenient use, greatly simplifies the structure and volume of equipment compared with the traditional xylo-oligosaccharide concentration equipment, improves the convenience and the working efficiency of equipment installation and maintenance, and greatly reduces the cost and the labor intensity of equipment construction, operation and maintenance operation; on the other hand, the working efficiency of concentration operation and the automation degree of concentration operation are greatly improved, the comprehensive material recovery and utilization rate during concentration operation is effectively improved, the concentration efficiency is improved, and meanwhile, the material loss and waste are effectively reduced, so that the production efficiency and the yield of xylo-oligosaccharide are greatly improved, and meanwhile, the pollution of production waste to the environment is effectively reduced.
In order to achieve the above purpose, the utility model discloses a realize through following technical scheme:
a self-circulation xylo-oligosaccharide concentration mechanism comprises bearing keels, concentration operation tanks, a negative pressure fan, flow dividing pipes, a collecting pipe, a main booster pump, a pressure sensor, a concentration sensor, a temperature sensor and a control circuit, wherein at least two concentration operation tanks are uniformly distributed in the bearing keels around the axis of the bearing keels and are distributed in parallel with the axis of the bearing keels, each concentration operation tank is communicated with the main booster pump through the flow dividing pipe and is communicated with the negative pressure fan through the collecting pipe, each concentration operation tank comprises a tank body, a molecular sieve filter, a flow guiding pipe, a drainage pipe, an electric heating device, an auxiliary booster pump and a circulating pump, the tank body is of a closed cavity structure, the molecular sieve filters are embedded in the tank body and are coaxially distributed with the tank body, the tank body is divided into two cavities, namely a concentration separation cavity and a concentration bearing cavity from top to, and the concentration separation cavity and the concentration bearing cavity are internally provided with at least one temperature sensor and at least one concentration sensor, the lower end surface and the lower end surface of the molecular sieve filter are respectively provided with an auxiliary booster pump, the interior of the auxiliary booster pump is provided with at least one pressure sensor, the auxiliary booster pump positioned on the lower end surface of the molecular sieve filter is communicated with the bottom of the concentration bearing cavity through a drainage tube, the auxiliary booster pump positioned on the upper end surface of the molecular sieve filter is communicated with the concentration separation cavity through a drainage tube, the drainage tube is of a tubular structure coaxially distributed with the concentration separation cavity, the height of the drainage tube is 1/3-2/3 of the height of the concentration separation cavity, at least two electric heating devices are uniformly distributed on the outer surface of the drainage tube around the axis of the drainage tube, at least three drainage tubes are uniformly distributed on the outer side, the other end is communicated with the upper end surface of the tank body concentration bearing cavity, the upper end surface and the lower end surface of the tank body are respectively provided with a flow guide port, the upper end surface flow guide port is communicated with a collecting pipe, the lower end surface flow guide port is communicated with a flow dividing pipe, and a control circuit is connected with the outer surface of the bearing keel and is respectively and electrically connected with a negative pressure fan, a main booster pump, a pressure sensor, a concentration sensor, a temperature sensor and an electric heating device, an auxiliary booster pump and a circulating pump of the concentration operation tank.
Further, bear the keel and be axis and horizontal plane vertical distribution's frame construction to be connected through spout and concentrated operation jar outer surface, and every concentrated operation jar all through two at least spouts and bear keel sliding connection.
Further, negative-pressure air fan with bear fossil fragments up end and be connected, main booster pump with bear fossil fragments down end connection to be located under each concentrated operation jar, just main booster pump and negative-pressure air fan all are located and bear fossil fragments axis position department.
Furthermore, the molecular sieve filter is in sliding connection with the inner surface of the tank body through at least three sliding grooves, and at least two elastic sealing rings are arranged on the outer surface of the molecular sieve filter and are in sealing connection with the inner surface of the tank body through the elastic sealing rings.
Furthermore, the electric heating device is any one or two of an electric heating wire and a microwave heating device which are used together, and when the electric heating wire is used, the length of the electric heating wire is 50% -95% of the length of the flow guide pipe, and the electric heating wire is distributed around the axis of the flow guide pipe in a spiral structure.
Furthermore, the diameter of the flow guide pipe is 10% -50% of the inner diameter of the concentration separation cavity, the axial section of the flow guide pipe is in any one of a rectangular structure and an isosceles trapezoid structure, a plurality of through holes with the diameter of 0.1-1 mm are uniformly distributed on the side wall of the flow guide pipe, and the total area of the through holes is 10% -50% of the area of the side surface of the flow guide pipe.
Furthermore, the control circuit is a circuit structure which is based on any one or two of an industrial single chip microcomputer and a programmable controller and is used as a core circuit, wherein when the control circuit is the circuit structure used by the industrial single chip microcomputer and the programmable controller, the industrial single chip microcomputer and the programmable controller are connected with each other through a data bus, and the control circuit is additionally provided with at least one data communication port.
The utility model has simple structure, compact and reasonable layout and flexible and convenient use, greatly simplifies the equipment structure and volume compared with the traditional xylo-oligosaccharide concentration equipment on the one hand, improves the convenience and the working efficiency of equipment installation and maintenance, and greatly reduces the equipment construction, operation and maintenance operation cost and labor intensity; on the other hand, the working efficiency of concentration operation and the automation degree of concentration operation are greatly improved, the comprehensive material recovery and utilization rate during concentration operation is effectively improved, the concentration efficiency is improved, and meanwhile, the material loss and waste are effectively reduced, so that the production efficiency and the yield of xylo-oligosaccharide are greatly improved, and meanwhile, the pollution of production waste to the environment is effectively 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 a concentrated mechanism of self-loopa xylo-oligosaccharide, including bearing fossil fragments 1, concentrated operation jar 2, negative-pressure air fan 3, shunt tubes 4, collecting pipe 5, main booster pump 6, pressure sensor 7, concentration sensor 8, temperature sensor 9 and control circuit 10, concentrated operation jar 2 is two at least, encircle and bear fossil fragments 1 axis equipartition in bearing fossil fragments 1 to with bear fossil fragments 1 axis parallel distribution, each concentrated operation jar 2 passes through shunt tubes 4 and main booster pump 6 intercommunication, communicate with negative-pressure air fan 3 through collecting pipe 5.
In this embodiment, the concentration operation tank 2 includes a tank 21, a molecular sieve filter 22, a flow guide tube 23, a drainage tube 24, an electric heating device 25, an auxiliary booster pump 26 and a circulation pump 27, wherein the tank 21 is a sealed cavity structure, the molecular sieve filter 22 is embedded in the tank 21 and coaxially distributed with the tank 21, and the tank 21 is divided into two chambers, from top to bottom, of a concentration separation chamber 101 and a concentration bearing chamber 102, the concentration separation chamber 101 and the concentration bearing chamber 102 are communicated with each other through the molecular sieve filter 22, at least one temperature sensor 9 and at least one concentration sensor 8 are respectively disposed in the concentration separation chamber 101 and the concentration bearing chamber 102, the auxiliary booster pump 26 is disposed on the lower end surface and the lower end surface of the molecular sieve filter 22, at least one pressure sensor 7 is disposed inside the concentration separation chamber 101 and the concentration bearing chamber 102, the auxiliary booster pump 26 disposed on the lower end surface of the molecular sieve, the auxiliary booster pump 26 positioned on the upper end face of the molecular sieve filter 22 is communicated with the concentration separation cavity 101 through a guide pipe 23, the guide pipe 23 is of a tubular structure which is coaxially distributed with the concentration separation cavity 101, the height of the guide pipe 23 is 1/3-2/3 of the height of the concentration separation cavity 101, at least two electric heating devices 25 are uniformly distributed on the outer surface of the guide pipe 23 around the axis of the guide pipe 23, at least three guide pipes 24 are uniformly distributed on the outer side of the tank body 21 around the axis of the tank body 21, one end of each guide pipe 24 is communicated with the bottom of the concentration separation cavity 101 of the tank body 21 through a circulating pump 27, the other end of each guide pipe is communicated with the upper end face of the concentration bearing cavity 102 of the tank body 21, the upper end face and the lower end face of the tank body 21 are respectively provided.
In this embodiment, the control circuit 10 is connected to the outer surface of the bearing keel 1, and is electrically connected to the negative pressure fan 3, the main booster pump 6, the pressure sensor 7, the concentration sensor 8, the temperature sensor 9, the electric heating device 25 of the concentration operation tank 2, the auxiliary booster pump 26, and the circulation pump 27, respectively.
Wherein, bear fossil fragments 1 be axis and horizontal plane vertical distribution's frame construction to through spout 12 and 2 surface connections of concentrated operation jar, and every concentrated operation jar 2 all through two at least spout 12 and bear fossil fragments 1 sliding connection.
Simultaneously, negative-pressure air fan 3 with bear 1 up end of fossil fragments and be connected, main booster pump 6 with bear 1 end of fossil fragments under the end-face be connected to be located under each concentrated operation jar 2, just main booster pump 6 and negative-pressure air fan 3 all are located and bear 1 axis position department of fossil fragments.
It should be noted that the molecular sieve filter 22 is slidably connected to the inner surface of the tank 21 through at least three sliding grooves 12, and the outer surface of the molecular sieve filter 22 is provided with at least two elastic sealing rings 13, and is hermetically connected to the inner surface of the tank 21 through the elastic sealing rings 13.
Preferably, the electric heating device 25 is one or two of an electric heating wire and a microwave heating device, and when the electric heating wire is used, the length of the electric heating wire is 50% -95% of the length of the draft tube 23, and the electric heating wire is distributed around the axis of the draft tube 23 in a spiral structure; meanwhile, the diameter of the draft tube 23 is 10% -50% of the inner diameter of the concentration separation cavity 101, the axial section of the draft tube 23 is any one of a rectangular structure and an isosceles trapezoid structure, a plurality of through holes 14 with the diameter of 0.1-1 mm are uniformly distributed on the side wall of the draft tube 23, and the total area of the through holes 14 is 10% -50% of the area of the side surface of the draft tube 23.
In this embodiment, the control circuit 10 is a circuit structure based on any one or two of an industrial single chip microcomputer and a programmable controller, which is a core circuit, wherein when the circuit structure is shared by the industrial single chip microcomputer and the programmable controller, the industrial single chip microcomputer and the programmable controller are connected to each other through a data bus, 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, concentrated operation jar, negative-pressure air fan, shunt tubes, collector pipe, main booster pump, pressure sensor, consistency transmitter, temperature sensor and control circuit assemble, then will assemble the back this neotype and fix at appointed operating position through bearing fossil fragments, and make main booster pump and outside treat concentrated material supply line intercommunication, make negative-pressure air fan and outside waste recycling pipeline intercommunication, be connected control circuit and external power system and monitored control system at last, thereby accomplish this novel equipment.
During concentration, firstly, a main booster pump boosts external materials to be concentrated and then conveys the materials to a concentration bearing cavity of a concentration operation tank, and then on one hand, liquid materials in the concentration bearing cavity continuously carry out temperature and concentration detection through a concentration sensor and a temperature sensor; on the other hand, the liquid material in the concentration bearing cavity is secondarily pressurized by the auxiliary booster pump and is conveyed to the molecular sieve filter for separation and filtration, the xylo-oligosaccharide in the liquid material is separated from the water, the separated water containing part of the xylo-oligosaccharide is conveyed to the flow guide pipe by the auxiliary booster pump on the upper end surface of the molecular sieve filter and is conveyed to the concentration separation cavity by the flow guide pipe, meanwhile, when the water flows along the flow guide pipe, the material in the flow guide pipe is heated by the electric heating device to evaporate the water, then the water vapor is conveyed to an external waste recycling pipeline by the negative pressure fan, the loss of xylo-oligosaccharide components is prevented, the content of xylo-oligosaccharide in the waste is reduced, the material loss and the environmental pollution caused by the waste are reduced, the residual material after evaporation and concentration falls back into the concentration separation cavity and flows back into the concentration bearing cavity again along the flow guide pipe, thereby carry out the concentrated operation of circulation to stop concentrated operation after concentration detection concentration bears intracavity material concentration and reaches the service standard, then with concentrated bearing chamber in the qualified back material carry to next process equipment can, and after concentrated bearing chamber material discharges and finishes, carry the concentrated bearing chamber of carrying after treating concentrated material pressure boost with the outside again, carry out the concentration of circulation again.
The utility model has simple structure, compact and reasonable layout and flexible and convenient use, greatly simplifies the equipment structure and volume compared with the traditional xylo-oligosaccharide concentration equipment on the one hand, improves the convenience and the working efficiency of equipment installation and maintenance, and greatly reduces the equipment construction, operation and maintenance operation cost and labor intensity; on the other hand, the working efficiency of concentration operation and the automation degree of concentration operation are greatly improved, the comprehensive material recovery and utilization rate during concentration operation is effectively improved, the concentration efficiency is improved, and meanwhile, the material loss and waste are effectively reduced, so that the production efficiency and the yield of xylo-oligosaccharide are greatly improved, and meanwhile, the pollution of production waste to the environment is effectively 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 (7)
1. The utility model provides a concentrated mechanism of self-loopa formula xylo-oligosaccharide which characterized in that: the self-circulation xylo-oligosaccharide concentration mechanism comprises a bearing keel, concentration operation tanks, a negative pressure fan, flow dividing pipes, collecting pipes, a main booster pump, a pressure sensor, a concentration sensor, a temperature sensor and a control circuit, wherein at least two concentration operation tanks are uniformly distributed in the bearing keel around the axis of the bearing keel and are distributed in parallel with the axis of the bearing keel, each concentration operation tank is communicated with the main booster pump through the flow dividing pipe and is communicated with the negative pressure fan through the collecting pipe, each concentration operation tank comprises a tank body, a molecular sieve filter, a flow guiding pipe, an electric heating device, an auxiliary booster pump and a circulating pump, wherein the tank body is of a closed cavity structure, the molecular sieve filter is embedded in the tank body and is coaxially distributed with the tank body, the tank body is divided into two cavities of a concentration separation cavity and a concentration bearing cavity from top to bottom, and the concentration separation cavity, and concentration separation chamber and concentration bear the weight of intracavity and all establish at least one temperature sensor and at least one concentration sensor, a supplementary booster pump is all established to terminal surface and lower terminal surface under the molecular sieve filter, its inside establishes at least one pressure sensor, wherein lie in the supplementary booster pump of terminal surface under the molecular sieve filter and pass through drainage tube and concentration bear the weight of the chamber bottom intercommunication, lie in the supplementary booster pump of molecular sieve filter up end and pass through honeycomb duct and concentration separation chamber intercommunication, the honeycomb duct is the tubular structure with concentration separation chamber coaxial distribution, its height is 1/3-2/3 of concentration separation chamber height, electric heater unit is at least two, encircle the honeycomb duct axis equipartition at the honeycomb duct surface, at least three drainage tubes encircle jar body axis equipartition and in jar body outside, and each drainage tube one end is through circulating pump and jar body's concentration separation chamber bottom intercommunication, the other end is communicated with the upper end face of the tank body concentration bearing cavity, a flow guide port is respectively arranged on the upper end face and the lower end face of the tank body, the flow guide port on the upper end face is communicated with a collecting pipe, the flow guide port on the lower end face is communicated with a flow dividing pipe, and a control circuit is connected with the outer surface of the bearing keel and is respectively electrically connected with a negative pressure fan, a main booster pump, a pressure sensor, a concentration sensor, a temperature sensor and an electric heating device, an auxiliary booster pump and a circulating pump of the concentration operation tank.
2. The self-circulation xylo-oligosaccharide concentrating mechanism of claim 1, wherein the bearing keel is a frame structure with an axis vertical to the horizontal plane and is connected with the outer surface of the concentrating operation tank through a chute, and each concentrating operation tank is slidably connected with the bearing keel through at least two chutes.
3. The self-circulation xylo-oligosaccharide concentrating mechanism of claim 1, wherein the negative pressure fan is connected with the upper end surface of the bearing keel, the main booster pump is connected with the lower end surface of the bearing keel and is positioned under each concentrating operation tank, and the main booster pump and the negative pressure fan are both positioned at the axial position of the bearing keel.
4. The self-circulation xylo-oligosaccharide concentration mechanism according to claim 1, wherein the molecular sieve filter is slidably connected with the inner surface of the tank body through at least three chutes, and the outer surface of the molecular sieve filter is provided with at least two elastic sealing rings which are hermetically connected with the inner surface of the tank body through the elastic sealing rings.
5. The self-circulation xylo-oligosaccharide concentrating mechanism of claim 1, wherein the electric heating device is one or two of an electric heating wire and a microwave heating device, and when the electric heating wire is used, the length of the electric heating wire is 50% -95% of the length of the flow guide pipe and is distributed in a spiral structure around the axis of the flow guide pipe.
6. The self-circulation xylo-oligosaccharide concentrating mechanism as claimed in claim 1, wherein the diameter of the flow guide tube is 10% -50% of the inner diameter of the concentrating and separating chamber, the axial section of the flow guide tube is any one of rectangular and isosceles trapezoid structure, and a plurality of through holes with the diameter of 0.1-1 mm are uniformly distributed on the side wall of the flow guide tube, and the total area of the through holes is 10% -50% of the side surface area of the flow guide tube.
7. The self-circulation xylo-oligosaccharide concentrating mechanism of claim 1, wherein the control circuit is a circuit structure based on any one or two of an industrial single chip microcomputer and a programmable controller as a core circuit, wherein when the circuit structure is shared by the industrial single chip microcomputer and the programmable controller, the industrial single chip microcomputer and the programmable controller are connected with each other through a data bus, and the control circuit is further provided with at least one data communication port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921469975.3U CN210845304U (en) | 2019-09-05 | 2019-09-05 | Self-circulation xylo-oligosaccharide concentration mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921469975.3U CN210845304U (en) | 2019-09-05 | 2019-09-05 | Self-circulation xylo-oligosaccharide concentration mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210845304U true CN210845304U (en) | 2020-06-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921469975.3U Expired - Fee Related CN210845304U (en) | 2019-09-05 | 2019-09-05 | Self-circulation xylo-oligosaccharide concentration mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210845304U (en) |
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2019
- 2019-09-05 CN CN201921469975.3U patent/CN210845304U/en not_active Expired - Fee Related
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200626 Termination date: 20210905 |
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| CF01 | Termination of patent right due to non-payment of annual fee |