CN210945065U - Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water - Google Patents
Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water Download PDFInfo
- Publication number
- CN210945065U CN210945065U CN201921469940.XU CN201921469940U CN210945065U CN 210945065 U CN210945065 U CN 210945065U CN 201921469940 U CN201921469940 U CN 201921469940U CN 210945065 U CN210945065 U CN 210945065U
- Authority
- CN
- China
- Prior art keywords
- bearing frame
- tank
- bearing
- communicated
- hydrocyclone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- External Artificial Organs (AREA)
Abstract
The utility model relates to a xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water, including bearing frame, hydrocyclone, main knockout drum, supplementary knockout drum, jet pump, circulating pump, solid-liquid separation equipment and control circuit, main knockout drum inlays in bearing frame, with bearing frame coaxial distribution and with bearing frame bottom connection, hydrocyclone encircles bearing frame axis equipartition and with bearing frame lateral wall internal surface connection, each hydrocyclone's feed inlet is through jet pump and outside dialysis water recovery pipeline intercommunication; the overflow port of the hydrocyclone is communicated with the auxiliary separating tank through a guide pipe; the bottom flow port of the hydrocyclone is communicated with the main separation tank through a guide pipe. This novel very big powdered material recovery plant structure and volume of having simplified to reduce the cost and the intensity of labour of equipment use, maintenance operation, very big improvement equipment integration degree, and improve solid impurity filtration purification and waste heat resource recovery utilization efficiency in the dialysis water.
Description
Technical Field
The utility model relates to a xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water belongs to concentrator technical field.
Background
The xylo-oligosaccharide production activity can generate dialysis water containing a large amount of waste heat and solid impurities, and when the xylo-oligosaccharide dialysis water is recycled, often needs to run through a plurality of solid-liquid separation devices and waste heat recovery devices in sequence to meet the requirements of recycling and reusing dialysis water resources, although the prior xylo-oligosaccharide production dialysis water recovery equipment can meet the use requirements, on one hand, the equipment has complex structure and large occupied area, thereby causing the defects of large labor intensity, high cost and the like in the operation, maintenance and other work of the equipment, on the other hand, as a plurality of solid-liquid separation equipment and waste heat recovery equipment are required to operate together, meanwhile, the water path circulation path is long when the dialysis water is recycled, and the number of devices is large, so that the defects that the operation energy consumption of the dialysis water recycling operation is high and the recycling efficiency is low are caused.
Therefore, in order to solve the above problems, a brand new xylo-oligosaccharide powder dialysis water recovery device is urgently needed to be developed so as to meet the needs 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 generates with high-efficient recovery unit of dialysis water, this utility model structure is simple, and overall arrangement is compact reasonable, and it is nimble convenient to use, and the operation energy consumption is cheap, simultaneously very big simplification powdery material recovery plant structure and volume to reduce the cost and the intensity of labour of equipment use, maintenance operation, very big improvement equipment integration degree, and improving solid impurity filtration purification and waste heat resource recycle efficiency in to the dialysis water.
In order to achieve the above purpose, the utility model discloses a realize through following technical scheme:
a high-efficiency dialyzing water recovery device for xylo-oligosaccharide generation comprises a bearing rack, hydrocyclones, main separating tanks, auxiliary separating tanks, a jet pump, a circulating pump, a solid-liquid separation device and a control circuit, wherein the bearing rack is of a columnar frame structure with the axis vertical to the horizontal plane, the hydrocyclones and the main separating tanks are embedded in the bearing rack, the main separating tanks are embedded in the bearing rack and coaxially distributed with the bearing rack and are connected with the bottom of the bearing rack, the distance between the upper end surface of the main separating tank and the upper end surface of the bearing rack is 1/3-2/3 of the height of the bearing rack, at least three hydrocyclones are uniformly distributed around the axis of the bearing rack and are connected with the inner surface of the side wall of the bearing rack, the hydrocyclones are mutually connected in parallel, and feed inlets of the hydrocyclones are communicated with; the overflow port of the hydrocyclone is communicated with the auxiliary separating tank through a guide pipe; the bottom flow port of the hydraulic cyclone is communicated with the main separation tank through a flow guide pipe, the number of the auxiliary separation tanks is at least two, the auxiliary separation tanks are uniformly distributed on the outer surface of the bearing frame around the axis of the bearing frame, the main separation tank and the auxiliary separation tanks are connected in parallel and are communicated with the solid-liquid separation device through circulating pumps respectively, the solid-liquid separation device is communicated with a water inlet of the jet pump through a circulating pump, the jet pump and the solid-liquid separation device are connected with the upper end face of the bearing frame, the circulating pumps are connected with the outer surfaces of the main separation tank and the auxiliary separation tank respectively, and a control circuit is connected with the outer surface of the bearing frame and is electrically connected with the main separation tank, the auxiliary separation tanks, the jet pump.
Furthermore, the hydrocyclone is hinged with the bearing rack through a turntable mechanism, the axis of the hydrocyclone and the axis of the bearing rack form an included angle of 0-60 degrees, and the turntable mechanism is electrically connected with the control circuit.
Further, the main separation tank and the auxiliary separation tank respectively comprise a bearing column, a tank body, heat exchangers, plate filters and a negative pressure pump, wherein the tank body is of an inverted conical closed cavity structure, a liquid inlet is formed in the upper end surface of the tank body, a liquid outlet is formed in the lower end surface of the tank body, at least three bearing columns are uniformly distributed around the axis of the tank body and are connected with the lower end of the tank body, the plate filters are embedded in the tank body and are coaxially distributed with the tank body, the tank body is divided into a bearing chamber and a water return chamber by the plate filters from top to bottom, the volume of the bearing chamber is 1.5-5 times of that of the water return chamber, the bearing chamber and the water return chamber are mutually communicated through the plate filters, the negative pressure pump is positioned in the water return chamber, the plate filters are communicated with the water return chamber through the negative pressure pump, the water return chamber is communicated with a circulating pump through the liquid outlet, the, at least one heat exchanger is embedded in the backwater chamber and uniformly distributed around the axis of the tank body.
Furthermore, the upper end surface of the plate-type filter is provided with a flow guide cover with an axial end surface in an inverted isosceles trapezoid structure, the flow guide cover is communicated with the bearing chamber through the flow guide cover, the lower end surface of the flow guide cover is connected with the upper end surface of the plate-type filter, and the side surface of the flow guide cover is connected with the inner surface of the side wall of the tank body and is coaxially distributed with the tank body.
Furthermore, the control circuit is a circuit structure based on a programmable controller as a core circuit, and the control circuit is additionally provided with at least one serial port data communication port.
The utility model discloses simple structure, overall arrangement is compact reasonable, and it is nimble convenient to use, and the operation energy consumption is cheap, the while very big powdery material recovery plant structure and volume of having simplified to reduce the cost and the intensity of labour of equipment use, maintenance operation, very big improvement the equipment degree of integrating, and improve solid impurity filtration purification and waste heat resource recycle efficiency in to the dialysis water.
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 high-efficiency recycling device of the dialyzing water for producing the xylo-oligosaccharide comprises a bearing frame 1, a hydrocyclone 2, a main separating tank 3, an auxiliary separating tank 4, a jet pump 5, a circulating pump 6, a solid-liquid separating device 7 and a control circuit 8, wherein the bearing frame 1 is a columnar frame structure with the axis vertical to the horizontal plane, the hydraulic cyclone 2 and the main separation tank 3 are both embedded in the bearing frame 1, the main separation tank 3 is embedded in the bearing frame 1, the device is coaxially distributed with the bearing frame 1 and connected with the bottom of the bearing frame 1, the distance between the upper end surface of the main separation tank 3 and the upper end surface of the bearing frame 1 is 1/3-2/3 of the height of the bearing frame 1, at least three hydrocyclones 2 are uniformly distributed around the axis of the bearing frame 1 and connected with the inner surface of the side wall of the bearing frame 1, the hydrocyclones 2 are mutually connected in parallel, and the feed inlet of each hydrocyclone 2 is communicated with an external dialysis water recovery pipeline through a jet pump 5; the overflow port of the hydrocyclone 2 is communicated with the auxiliary separating tank 4 through a guide pipe 9; the bottom flow port of the hydraulic cyclone 2 is communicated with the main separation tank 3 through a flow guide pipe 9, the number of the auxiliary separation tanks 4 is at least two, the auxiliary separation tanks are uniformly distributed on the outer surface of the bearing frame 1 around the axis of the bearing frame 1, the main separation tank 3 and the auxiliary separation tanks 4 are connected in parallel and are communicated with a solid-liquid separation device 7 through a circulating pump 6 respectively, the solid-liquid separation device 7 is communicated with a water inlet of a jet pump 5 through the circulating pump 6, the jet pump 5 and the solid-liquid separation device 7 are both connected with the upper end face of the bearing frame 1, the circulating pump 6 is connected with the outer surface of the main separation tank 3 and the outer surface of the auxiliary separation tank 4 respectively, and a control circuit 8 is connected with the outer surface of the bearing frame 1 and is electrically connected with the main separation tank 3, the auxiliary separation tank 4.
The hydrocyclone 2 is hinged with the bearing rack 1 through a turntable mechanism 10, the axis of the hydrocyclone 2 forms an included angle of 0-60 degrees with the axis of the bearing rack 1, and the turntable mechanism 10 is electrically connected with the control circuit 8.
It is important to point out that the main separation tank 3 and the auxiliary separation tank 4 both include a bearing column 101, a tank 102, a heat exchanger 103, a plate filter 104, and a negative pressure pump 105, wherein the tank 102 is an inverted cone-shaped closed cavity structure, a liquid inlet 106 is provided on the upper end surface, a liquid outlet 107 is provided on the lower end surface, at least three bearing columns 101 are uniformly distributed around the axis of the tank 102 and connected with the lower end of the tank 102, the plate filter 104 is embedded in the tank 102 and coaxially distributed with the tank 102, and the plate filter 104 divides the tank 102 into a bearing chamber 108 and a water return chamber 109 from top to bottom, wherein the volume of the bearing chamber 108 is 1.5-5 times of the volume of the water return chamber 109, the bearing chamber 108 and the water return chamber 109 are communicated with each other through the plate filter 104, the negative pressure pump 105 is located in the water return chamber 109, the plate filter 104 is communicated with the water return chamber 109 through the negative pressure pump 105, and the water return, the bearing chamber 108 is communicated with the liquid inlet 106, at least one sewage draining exit 100 is arranged on the side wall of the tank body 102 corresponding to the bearing chamber 108, and at least one heat exchanger 103 is embedded in the water return chamber 109 and is uniformly distributed around the axis of the tank body 102.
Preferably, the upper end surface of the plate filter 104 is provided with a guide cover 11 with an axial end surface in an inverted isosceles trapezoid structure, and the guide cover 11 is communicated with the bearing chamber 108, the lower end surface of the guide cover 11 is connected with the upper end surface of the plate filter 104, and the side surface of the guide cover is connected with the inner surface of the side wall of the tank 102 and is coaxially distributed with the tank 102.
In addition, the control circuit 8 is a circuit structure based on a programmable controller as a core circuit, and the control circuit is additionally provided with at least one serial port data communication port.
This is novel in concrete implementation, at first to constituting this neotype frame that bears, hydrocyclone, main knockout drum, supplementary knockout drum, the jet pump, the circulating pump, solid-liquid separation equipment and control circuit assemble, then will assemble this novel fixing at appointed operating position through bearing the frame, simultaneously with jet pump and outside dialysis water recovery pipeline intercommunication, with main knockout drum, the leakage fluid dram of supplementary knockout drum passes through solid-liquid separation equipment and outside dialysis water recovery system intercommunication, main knockout drum, the drain and the solid waste collection system intercommunication of supplementary knockout drum, with main knockout drum, supplementary knockout drum heat exchanger and outside waste heat recovery system intercommunication, at last with control circuit and external power supply circuit and monitor circuit electrical connection, thereby accomplish this novel assembly.
In the specific implementation of the novel dialysis water treatment device, firstly, dialysis water produced in an external dialysis water recovery pipeline is pressurized and then is conveyed to each hydrocyclone, the dialysis water is separated for the first time through the hydrocyclones, and the separated low-impurity dialysis water is conveyed to an auxiliary separation tank; high impurity dialysis water is directly carried to main knockout drum in, dialysis water enters into main knockout drum, back in the auxiliary separation jar, at first by main knockout drum, the internal plate filter of auxiliary separation jar carries out secondary filter separation, clear away solid impurity in the water, then assemble the dialysis water after purifying in the return water room of jar body bottom, and carry out the waste heat resource recovery operation to dialysis water through the heat exchanger in the return water room and outside waste heat recovery system intercommunication, discharge dialysis water through the leakage fluid dram at last, the back is purified through solid-liquid separation equipment end to the discharged dialysis water, can directly carry out follow-up production as required and use, also can carry to the efflux pump end of intaking once more through the circulating pump, carry out the circulation purification.
The utility model discloses simple structure, overall arrangement is compact reasonable, and it is nimble convenient to use, and the operation energy consumption is cheap, the while very big powdery material recovery plant structure and volume of having simplified to reduce the cost and the intensity of labour of equipment use, maintenance operation, very big improvement the equipment degree of integrating, and improve solid impurity filtration purification and waste heat resource recycle efficiency in to the dialysis water.
The utility model discloses simple structure, the overall arrangement is compact reasonable, and it is nimble convenient to use, very big simplification powdery material recovery plant structure and volume to reduce the cost and the intensity of labour of plant use, maintenance operation, simultaneously very big improvement the equipment degree of integrating, and when improving material recovery operating efficiency, effectively reduced the operation energy consumption of retrieving the operation.
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 generates with high-efficient recovery unit of dialysis water which characterized in that: the high-efficiency dialyzing water recovery device for generating xylo-oligosaccharide comprises a bearing frame, a hydrocyclone, a main separating tank, an auxiliary separating tank, a jet pump, a circulating pump, a solid-liquid separating device and a control circuit, wherein the bearing frame is a columnar frame structure with the axis vertical to the horizontal plane, the hydrocyclone and the main separating tank are all embedded in the bearing frame, wherein the main separating tank is embedded in the bearing frame, is coaxially distributed with the bearing frame and is connected with the bottom of the bearing frame, and the distance between the upper end surface of the main separation tank and the upper end surface of the bearing rack is 1/3-2/3 of the height of the bearing rack, at least three hydrocyclones are uniformly distributed around the axis of the bearing frame and connected with the inner surface of the side wall of the bearing frame, the hydrocyclones are connected in parallel, and the feed inlet of each hydrocyclone is communicated with an external dialysis water recovery pipeline through a jet pump; the overflow port of the hydrocyclone is communicated with the auxiliary separating tank through a guide pipe; the bottom flow ports of the hydraulic cyclone are communicated with the main separation tank through a flow guide pipe, the auxiliary separation tanks are at least two and are uniformly distributed on the outer surface of the bearing frame around the axis of the bearing frame, the main separation tank and the auxiliary separation tanks are connected in parallel and are communicated with the solid-liquid separation device through circulating pumps respectively, the solid-liquid separation device is communicated with a water inlet of the jet pump through a circulating pump, the jet pump and the solid-liquid separation device are connected with the upper end face of the bearing frame, the circulating pumps are connected with the outer surfaces of the main separation tank and the auxiliary separation tanks respectively, and the control circuit is connected with the outer surface of the bearing frame and is electrically connected with the main separation tank, the auxiliary separation tank, the jet pump, the circulating pump and the solid-liquid separation device respectively.
2. The device for efficiently recycling the dialyzing water for the production of xylo-oligosaccharide according to claim 1, wherein the hydrocyclone is hinged with the carrier frame through a turntable mechanism, the axis of the hydrocyclone forms an included angle of 0-60 degrees with the axis of the carrier frame, and the turntable mechanism is electrically connected with the control circuit.
3. The high-efficiency recycling device for the dialyzed water for producing the xylo-oligosaccharide according to claim 1, characterized in that the main separating tank and the auxiliary separating tank respectively comprise a bearing column, a tank body, a heat exchanger, a plate filter and a negative pressure pump, wherein the tank body is an inverted conical closed cavity structure, the upper end surface of the tank body is provided with a liquid inlet, the lower end surface of the tank body is provided with a liquid outlet, at least three bearing columns are uniformly distributed around the axis of the tank body and are connected with the lower end of the tank body, the plate filters are embedded in the tank body and are coaxially distributed with the tank body, the tank body is divided into a bearing chamber and a water return chamber from top to bottom by the plate filters, the volume of the bearing chamber is 1.5-5 times of the volume of the water return chamber, the bearing chamber and the water return chamber are mutually communicated through the plate filters, the negative pressure pump is, the water return chamber is communicated with the circulating pump through a liquid outlet, the bearing chamber is communicated with the liquid inlet, at least one drain outlet is formed in the side wall of the tank body corresponding to the bearing chamber, and at least one heat exchanger is embedded in the water return chamber and uniformly distributed around the axis of the tank body.
4. The device for efficiently recycling the dialyzing water for the production of xylo-oligosaccharide according to claim 3, wherein the upper end surface of the plate filter is provided with a flow guide cover with an axial end surface in an inverted isosceles trapezoid structure, the flow guide cover is communicated with the bearing chamber through the flow guide cover, the lower end surface of the flow guide cover is connected with the upper end surface of the plate filter, and the side surface of the flow guide cover is connected with the inner surface of the side wall of the tank body and is coaxially distributed with the tank body.
5. The device for efficiently recycling dialysis water for xylo-oligosaccharide generation according to claim 1, wherein said control circuit is a circuit structure based on a programmable controller as a core circuit, and said control circuit is further provided with at least one serial data communication port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921469940.XU CN210945065U (en) | 2019-09-05 | 2019-09-05 | Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921469940.XU CN210945065U (en) | 2019-09-05 | 2019-09-05 | Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210945065U true CN210945065U (en) | 2020-07-07 |
Family
ID=71391288
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921469940.XU Expired - Fee Related CN210945065U (en) | 2019-09-05 | 2019-09-05 | Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210945065U (en) |
-
2019
- 2019-09-05 CN CN201921469940.XU patent/CN210945065U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210945065U (en) | Xylo-oligosaccharide generates with high-efficient recovery unit of dialysis water | |
| CN205247914U (en) | Novel photocatalytic treatment uranium waste water device | |
| CN111088726B (en) | Plant fiber tableware forming system and forming method | |
| CN207405061U (en) | A kind of vertical sludge filter press | |
| CN203494498U (en) | High-efficiency mass transferring tray of urea synthesis tower | |
| CN202766357U (en) | Anaerobic treatment device of acrylic acid and ester mixing production waste water | |
| CN105692897A (en) | Combined anaerobic baffle plate sewage treatment device | |
| CN202465408U (en) | System for concentrating and recycling residual polyethyleneglycol in condensation waste water | |
| CN205953707U (en) | Solar energy water body pollution purifies ship | |
| CN214060100U (en) | Novel reverse osmosis of high rate of recovery device | |
| CN210764555U (en) | Anaerobic three-phase separator | |
| CN104157319B (en) | Nuclear reactor primary coolant circuit coolant water quality cyclone purifying method and device | |
| CN210728834U (en) | Concrete waste water waste residue's splitter | |
| CN202755247U (en) | Closed type flotation stripping machine | |
| CN206502733U (en) | A kind of sludge press filtration device for sewage disposal | |
| CN203648171U (en) | Full-automatic hair and dirt filtering device for recycling reclaimed water | |
| CN105084679A (en) | Sewage treatment equipment with water and sludge separation function | |
| CN207204061U (en) | A kind of integrated fixed bed equipressure feed liquor resin reaction device | |
| CN106190794A (en) | A kind of recycle device of the ease liquid that ferments | |
| CN207203727U (en) | A kind of energy-saving circulating purifying column | |
| CN220852112U (en) | Coal electric steam heat recovery processing device | |
| CN208032075U (en) | A kind of environment-friendly type pharmaceutical waste liquor recycling device | |
| CN209428186U (en) | A kind of trade effluent ultrafiltration apparatus | |
| CN209848404U (en) | Security filter convenient to maintain and do not influence work efficiency | |
| CN217431270U (en) | Waste gas purifying equipment |
Legal Events
| 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: 20200707 Termination date: 20210905 |