CN201135792Y - Accurate liquid-solid separating device - Google Patents
Accurate liquid-solid separating device Download PDFInfo
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- CN201135792Y CN201135792Y CNU2007201584674U CN200720158467U CN201135792Y CN 201135792 Y CN201135792 Y CN 201135792Y CN U2007201584674 U CNU2007201584674 U CN U2007201584674U CN 200720158467 U CN200720158467 U CN 200720158467U CN 201135792 Y CN201135792 Y CN 201135792Y
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- guiding subassembly
- tank body
- solid
- accurate liquid
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Abstract
The utility model discloses a precise solid-liquid separator, which comprises a tank body. An outer close cover is arranged at the upper part of the tank body, a discharge device is arranged at the lower part, a feeding pipe is arranged on the outer close cover, the feeding pipe extends into the cavity of the tank body and is communicated with the cavity of the tank body, a cone-shaped upper guiding component and a lower guiding component with identical axle cores are arranged in the cavity of the tank body, the separation clearance is arranged between the upper guiding component and the lower guiding component, the feeding pipe extends into one end inside the cavity of the tank body and is connected with the top part of the upper guiding component, and is communicated with the separation clearance, and a plurality of discharge tanks are arranged on the lower guiding component. The precise solid-liquid separator has the advantages that the sedimentation time is short, the manufacture cost is low, the occupation area is small, the structure is simple, the collection rate is high, and the precise solid-liquid separator is particularly suitable for solid-liquid mixture which has 0.1 to 8 percent of solid content, has above 3 g/cm3 solid density of single particle and has 1 to 20 mu m particle dimension, therefore, during the separating process, the abrasion between the fluid and the equipment can be reduced, the impurity is prevented from interfusing, and the collection rate of products is improved.
Description
Technical field
The utility model relates to a kind of separator of liquid-solid mixture, and especially a kind of solid content that is suitable for is 0.1%-8%, and solid individual particle density is greater than 3g/cm
3, size is between the accurate liquid-solid separator of the liquid-solid mixture of 1um-20um.
Background technology
At present, liquid-solid separator commonly used mostly is natural subsidence formula separator, cyclone and filter etc., and natural subsidence formula separator is because the material sedimentation time is long, and the sedimentation container volume that needs is big, quantity many and floor space is big; Cyclone is very high to the stability requirement of input fluid, needs the current stabilization facility, and not high to the collection efficiency of tiny solid particle, collecting effect is not obvious, and filter then costs an arm and a leg, maintenance inconvenience and expense height.
Summary of the invention
Technical problem to be solved in the utility model is at above defective, provide a kind of material sedimentation time short, low cost of manufacture, the accurate liquid-solid separator that floor space is little, simple in structure, collection efficiency is high, being particularly suitable for solid content is 0.1%-8%, and solid individual particle density is greater than 3g/cm
3, size in separation, can alleviate the wearing and tearing between fluid and the equipment between the liquid-solid mixture of 1um-20um, has prevented that impurity from sneaking into, improving the collection rate of product.
For addressing the above problem, the utility model adopts following technical scheme:
A kind of accurate liquid-solid separator, comprise tank body, the top of described tank body is provided with outer seal, the bottom is provided with removal device, described outer seal is provided with passage, described passage extend in the tank body cavity and with it and is communicated with, it is characterized in that: be provided with guiding subassembly and following guiding subassembly in the taper of concentric in the cavity of described tank body, described going up between guiding subassembly and the following guiding subassembly has Separation, the end that described passage extend in the tank body cavity is connected with the top of last guiding subassembly and is communicated with Separation, and described guiding subassembly down is provided with several blow tanks.
Below be the utility model to further improvement in the technical proposal:
Described blow tank groove width is 0.1～0.5mm, is arranged near lower limb 5～10mm position.
Described several blow tank circular array and interlaced setting.
Be provided with the adjusting device that is used for regulating Separation between described guiding subassembly down and the passage.
Described adjusting device comprises the adjusting screw(rod) that is arranged on the nut in the passage and is arranged on down the top of guiding subassembly, described adjusting screw(rod) is connected with nut thread, to adapt to the separation of different solid particles, make fluid generation Laminar Flow, make the liquid-solid lower leaf that in flowing, produces.
Described Separation is 0.5～2mm.
The described cone angle of going up guiding subassembly and following guiding subassembly is 120 °～150 °.
The described roughness that goes up the guiding subassembly lower surface is Ra0.04～0.08 μ m, the roughness of guiding subassembly upper surface is Ra0.63～1.25 μ m down.
Because the coarse influence of upper surface of guiding subassembly under the separator, the solid particle of fluid lower floor is obstructed, and flow velocity is slower, and upward the lower surface fineness of guiding subassembly is very high, and it is very little that the supernatant liquid in the fluid is obstructed, thereby make flow velocity fast relatively.
The top of described tank body is that cylinder, bottom are cone, the upper end of cylinder is provided with the interior capping of taper, the lower limb and the cylinder of capping are tightly connected in described, and the top of described interior capping has gap, and described passage passes gap and is connected with last guiding subassembly with outer seal respectively.
Be connected to form a spilling water chamber between capping and the outer seal in described, the edge lower part of described outer seal is provided with discharging tube, and described discharging tube is communicated with the spilling water chamber.
Beneficial effect
The utility model adopts technique scheme, during use, solid-liquid mixed fluid is flowed through after passage enters separator, restricted by Separation, fluid generation Laminar Flow, liquid-solid lower leaf in the generation in flowing, fluid looses downwards along Separation and flows simultaneously, the section streamwise area of flowing through constantly increases, thereby flow velocity constantly reduces, on the other hand, be subjected to that the guiding subassembly upper surface is coarse under the separator influences, the solid particle of fluid lower floor is obstructed, flow velocity is slower, and the lower surface fineness that goes up guiding subassembly is very high, supernatant liquid in the fluid is obstructed very little, thereby flow velocity is fast relatively, when the guiding subassembly working face flows to the lower end under the solid particle edge, be settled down to the bottom of tank body in the blow tank, at last by outside the removal device drain tank, the solid moisture content of collecting is 5%-10%, and then the be stressed influence of difference and inertia of liquid flows into interior capping top by the outlet of Separation, last by outside the discharging tube drain tank on the outer seal, realize liquid-solid separation, reach the purpose of collecting solid, the utility model sedimentation time is short, low cost of manufacture, floor space is little, simple in structure, the collection efficiency height, being particularly suitable for solid content is 0.1%-8%, solid individual particle density is greater than 3g/cm
3, size in separation, can alleviate the wearing and tearing between fluid and the equipment between the liquid-solid mixture of 1um-20um, has prevented that impurity from having sneaked into, having improved the collection rate of product.
Below in conjunction with drawings and Examples the utility model is further described:
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment;
Fig. 2 is the cross-sectional view that goes up guiding subassembly and following guiding subassembly among the utility model embodiment;
Fig. 3 is the vertical view of following guiding subassembly among the utility model embodiment.
Among the figure: guiding subassembly, 7-removal device, 8-gap, 9-discharging tube, 10-nut, 11-adjusting screw(rod), 12-blow tank, 13-Separation, 14-cone, 15-spilling water chamber, 16-cylinder under capping in 1-passage, 2-outer seal, the 3-, 4-tank body, the last guiding subassembly of 5-, the 6-.
The specific embodiment
Embodiment 1, as shown in Figure 1, a kind of accurate liquid-solid separator, comprise tank body 4, the top of tank body 4 is provided with outer seal 2, the bottom is provided with removal device 7, outer seal 2 is provided with passage 1, passage 1 extend in tank body 4 cavitys and with it and is communicated with, the top of tank body 4 is cylinder 16, the bottom is a cone 14, the upper end of cylinder 16 is provided with the interior capping 3 of taper, and the lower limb of interior capping 3 and cylinder 16 are tightly connected, and the top of interior capping 3 has gap 8, be provided with guiding subassembly 5 and following guiding subassembly 6 in the taper of concentric in the cavity of tank body 4, be connected to form a spilling water chamber 15 between interior capping 3 and the outer seal 2, the edge lower part of outer seal 2 is provided with discharging tube 9, and discharging tube 9 is communicated with spilling water chamber 15.
As shown in Figure 2, the cone angle of last guiding subassembly 5 and following guiding subassembly 6 is 120 °, the roughness of last guiding subassembly 5 lower surfaces is Ra0.04 μ m, the roughness of following guiding subassembly 6 upper surfaces is Ra0.635 μ m, passage 1 passes gap 8 and is connected with last guiding subassembly 5 with outer seal 2 respectively, the Separation 13 that has 0.5mm between last guiding subassembly 5 and the following guiding subassembly 6, the end that passage 1 extend in tank body 4 cavitys is connected with the top of last guiding subassembly 5 and is communicated with Separation 13, be provided with the adjusting device that is used for regulating Separation 13 between following guiding subassembly 6 and the passage 1, adjusting device comprises nut 10 that is arranged in the passage 1 and the adjusting screw(rod) 11 that is arranged on down the top of guiding subassembly 6, adjusting screw(rod) 11 is threaded with nut 10, close lower limb 5mm position is provided with several blow tank 12 on the following guiding subassembly 6, the groove width of blow tank 12 is 0.1mm, as shown in Figure 3, several blow tank 12 circular array and interlaced settings.
During use, solid-liquid mixed fluid is flowed through after passage 1 enters tank body 4, be subjected to Separation 13 restrictions, fluid generation Laminar Flow, liquid-solid lower leaf in the generation in flowing, fluid looses downwards along Separation 13 and flows simultaneously, the section streamwise area of flowing through constantly increases, thereby flow velocity constantly reduces, on the other hand, be subjected to down coarse influence of guiding subassembly 6 upper surfaces, the solid particle of fluid lower floor is obstructed, flow velocity is slower, and the lower surface fineness that goes up guiding subassembly 5 is very high, and it is very little that the supernatant liquid in the fluid is obstructed, thereby flow velocity is fast relatively, when the guiding subassembly working face flows to the lower end under the solid particle edge, be settled down to the bottom of tank body in the blow tank 12, by outside removal device 7 drain tanks, the solid moisture content of collection is 5%-10% at last, liquid then the be stressed difference and the influence of inertia, outlet by Separation 13 flows into interior capping 3 tops, and is last by outside 9 drain tanks of the discharging tube on the outer seal 2, realizes liquid-solid separation, reach the purpose of collecting solid, the utility model sedimentation time is short, low cost of manufacture, floor space is little, and is simple in structure, the collection efficiency height, being particularly suitable for solid content is 0.1%-8%, and solid individual particle density is greater than 3g/cm
3, size in separation, can alleviate the wearing and tearing between fluid and the equipment between the liquid-solid mixture of 1um-20um, has prevented that impurity from having sneaked into, having improved the collection rate of product.
As shown in Figure 2, the cone angle of last guiding subassembly 5 and following guiding subassembly 6 is 135 °, the roughness of last guiding subassembly 5 lower surfaces is Ra0.06 μ m, the roughness of following guiding subassembly 6 upper surfaces is Ra0.8 μ m, passage 1 passes gap 8 and is connected with last guiding subassembly 5 with outer seal 2 respectively, the Separation 13 that has 2mm between last guiding subassembly 5 and the following guiding subassembly 6, the end that passage 1 extend in tank body 4 cavitys is connected with the top of last guiding subassembly 5 and is communicated with Separation 13, be provided with the adjusting device that is used for regulating Separation 13 between following guiding subassembly 6 and the passage 1, adjusting device comprises nut 10 that is arranged in the passage 1 and the adjusting screw(rod) 11 that is arranged on down the top of guiding subassembly 6, adjusting screw(rod) 11 is threaded with nut 10, close lower limb 8mm position is provided with several blow tank 12 on the following guiding subassembly 6, the groove width of blow tank 12 is 0.25mm, as shown in Figure 3, several blow tank 12 circular array and interlaced settings.
During use, solid-liquid mixed fluid is flowed through after passage 1 enters tank body 4, be subjected to Separation 13 restrictions, fluid generation Laminar Flow, liquid-solid lower leaf in the generation in flowing, fluid looses downwards along Separation 13 and flows simultaneously, the section streamwise area of flowing through constantly increases, thereby flow velocity constantly reduces, on the other hand, be subjected to down coarse influence of guiding subassembly 6 upper surfaces, the solid particle of fluid lower floor is obstructed, flow velocity is slower, and the lower surface fineness that goes up guiding subassembly 5 is very high, supernatant liquid in the fluid is obstructed very little, thereby flow velocity is fast relatively, when the guiding subassembly working face flows to the lower end under the solid particle edge, be settled down to the bottom of tank body in the blow tank 12, at last by outside removal device 7 drain tanks, the solid moisture content of collection is then the be stressed influence of difference and inertia of the liquid of 5%-10%, flows into interior capping 3 tops by the outlet of Separation 13, last by outside 9 drain tanks of the discharging tube on the outer seal 2, realize liquid-solid separation, reach the purpose of collecting solid, the utility model sedimentation time is short, low cost of manufacture, floor space is little, simple in structure, the collection efficiency height, being particularly suitable for solid content is 0.1%-8%, solid individual particle density is greater than 3g/cm
3, size in separation, can alleviate the wearing and tearing between fluid and the equipment between the liquid-solid mixture of 1um-20um, has prevented that impurity from having sneaked into, having improved the collection rate of product.
Embodiment 3, as shown in Figure 1, a kind of accurate liquid-solid separator, comprise tank body 4, the top of tank body 4 is provided with outer seal 2, the bottom is provided with removal device 7, outer seal 2 is provided with passage 1, passage 1 extend in tank body 4 cavitys and with it and is communicated with, the top of tank body 4 is cylinder 16, the bottom is a cone 14, the upper end of cylinder 16 is provided with the interior capping 3 of taper, and the lower limb of interior capping 3 and cylinder 16 are tightly connected, and the top of interior capping 3 has gap 8, be provided with guiding subassembly 5 and following guiding subassembly 6 in the concentric taper in the cavity of tank body 4, be connected to form a spilling water chamber 15 between interior capping 3 and the outer seal 2, the edge lower part of outer seal 2 is provided with discharging tube 9, and discharging tube 9 is communicated with spilling water chamber 15.
As shown in Figure 2, the cone angle of last guiding subassembly 5 and following guiding subassembly 6 is 150 °, the roughness of last guiding subassembly 5 lower surfaces is Ra0.08 μ m, the roughness of following guiding subassembly 6 upper surfaces is Ra1.25 μ m, passage 1 passes gap 8 and is connected with last guiding subassembly 5 with outer seal 2 respectively, has 1.5mm Separation 13 between last guiding subassembly 5 and the following guiding subassembly 6, passage 1 extend into that a end in tank body 4 cavitys is connected with the top of last guiding subassembly 5 and is communicated with between time guiding subassembly 6 and the passage 1 with Separation 13 and is provided with the adjusting device that is used for regulating Separation 13, adjusting device comprises nut 10 that is arranged in the passage 1 and the adjusting screw(rod) 11 that is arranged on down the top of guiding subassembly 6, adjusting screw(rod) 11 is threaded with nut 10, close lower limb 10mm position is provided with several blow tank 12 on the following guiding subassembly 6, the groove width of blow tank 12 is 0.5mm, as shown in Figure 3, several blow tank 12 circular array and interlaced settings.
During use, solid-liquid mixed fluid is flowed through after passage 1 enters tank body 4, be subjected to Separation 13 restrictions, fluid generation Laminar Flow, liquid-solid lower leaf in the generation in flowing, fluid looses downwards along Separation 13 and flows simultaneously, the section streamwise area of flowing through constantly increases, thereby flow velocity constantly reduces, on the other hand, be subjected to down coarse influence of guiding subassembly 6 upper surfaces, the solid particle of fluid lower floor is obstructed, flow velocity is slower, and the lower surface fineness that goes up guiding subassembly 5 is very high, and it is very little that the supernatant liquid in the fluid is obstructed, thereby flow velocity is fast relatively, when the guiding subassembly working face flows to the lower end under the solid particle edge, be settled down to the bottom of tank body in the blow tank 12, by outside removal device 7 drain tanks, the solid moisture content of collection is 5%-10% at last, liquid then the be stressed difference and the influence of inertia, outlet by Separation 13 flows into interior capping 3 tops, and is last by outside 9 drain tanks of the discharging tube on the outer seal 2, realizes liquid-solid separation, reach the purpose of collecting solid, the utility model sedimentation time is short, low cost of manufacture, floor space is little, and is simple in structure, the collection efficiency height, being particularly suitable for solid content is 0.1%-8%, and solid individual particle density is greater than 3g/cm
3, size in separation, can alleviate the wearing and tearing between fluid and the equipment between the liquid-solid mixture of 1um-20um, has prevented that impurity from having sneaked into, having improved the collection rate of product.
Claims (10)
1, a kind of accurate liquid-solid separator, comprise tank body (4), the top of described tank body (4) is provided with outer seal (2), the bottom is provided with removal device (7), described outer seal (2) is provided with passage (1), described passage (1) extend in tank body (4) cavity and with it and is communicated with, it is characterized in that: be provided with guiding subassembly (5) in the taper of concentric in the cavity of described tank body (4), following guiding subassembly (6), described going up between guiding subassembly (5) and the following guiding subassembly (6) has Separation (13), the end that described passage (1) extend in tank body (4) cavity is connected with the top of last guiding subassembly (5) and is communicated with Separation (13), and described guiding subassembly (6) down is provided with several blow tanks (12).
2, accurate liquid-solid separator according to claim 1 is characterized in that: described blow tank (12) groove width is 0.1～0.5mm, is arranged near lower limb 5～10mm position.
3, accurate liquid-solid separator according to claim 1 and 2 is characterized in that: described several blow tanks (12) circular array and interlaced setting.
4, accurate liquid-solid separator according to claim 1 is characterized in that: be provided with the adjusting device that is used for regulating Separation (13) between described guiding subassembly (6) down and the passage (1).
5, accurate liquid-solid separator according to claim 4, it is characterized in that: described adjusting device comprises the adjusting screw(rod) (11) that is arranged on the nut (10) in the passage (1) and is arranged on down the top of guiding subassembly (6), and described adjusting screw(rod) (11) is threaded with nut (10).
6, a kind of accurate liquid-solid separator according to claim 4, it is characterized in that: described Separation (13) is 0.5～2mm.
7, a kind of accurate liquid-solid separator according to claim 1 is characterized in that: the described cone angle of going up guiding subassembly (5) and following guiding subassembly (6) is 120 °～150 °.
8, according to claim 1 or 6 described accurate liquid-solid separators, it is characterized in that: the described roughness that goes up guiding subassembly (5) lower surface is Ra0.04～0.08 μ m, the roughness of guiding subassembly (6) upper surface is Ra0.63～1.25 μ m down.
9, accurate liquid-solid separator according to claim 1, it is characterized in that: the top of described tank body (4) is that cylinder (16), bottom are cone (14), the upper end of cylinder (16) is provided with the interior capping (3) of taper, the lower limb and the cylinder (16) of capping (3) are tightly connected in described, the top of capping (3) has gap (8) in described, and described passage (1) passes gap (8) and is connected with last guiding subassembly (5) with outer seal (2) respectively.
10, accurate liquid-solid separator according to claim 8, it is characterized in that: be connected to form a spilling water chamber (15) between capping (3) and the outer seal (2) in described, the outward flange bottom of described outer seal (2) is provided with discharging tube (9), and described discharging tube (9) is communicated with spilling water chamber (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201584674U CN201135792Y (en) | 2007-12-18 | 2007-12-18 | Accurate liquid-solid separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201584674U CN201135792Y (en) | 2007-12-18 | 2007-12-18 | Accurate liquid-solid separating device |
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|---|---|
| CN201135792Y true CN201135792Y (en) | 2008-10-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2007201584674U Expired - Fee Related CN201135792Y (en) | 2007-12-18 | 2007-12-18 | Accurate liquid-solid separating device |
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| CN (1) | CN201135792Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527107A (en) * | 2011-12-22 | 2012-07-04 | 桂林兴松林化有限责任公司 | High pot for rosin production |
| CN105013218A (en) * | 2015-08-05 | 2015-11-04 | 安吉捷达贸易有限公司 | Depositing tank used for accurate separation of 1, 3-cyclohexanedione solid and liquid |
| CN109307615A (en) * | 2018-12-07 | 2019-02-05 | 重庆科技学院 | A kind of opposite-flushing type solid-liquor separation and real time measure device |
| CN113304664A (en) * | 2021-05-31 | 2021-08-27 | 广州蓝涛水处理有限公司 | Emulsification device optimized through high-frequency ultrasonic action and laminar flow sedimentation |
-
2007
- 2007-12-18 CN CNU2007201584674U patent/CN201135792Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527107A (en) * | 2011-12-22 | 2012-07-04 | 桂林兴松林化有限责任公司 | High pot for rosin production |
| CN102527107B (en) * | 2011-12-22 | 2013-11-06 | 桂林兴松林化有限责任公司 | High pot for rosin production |
| CN105013218A (en) * | 2015-08-05 | 2015-11-04 | 安吉捷达贸易有限公司 | Depositing tank used for accurate separation of 1, 3-cyclohexanedione solid and liquid |
| CN109307615A (en) * | 2018-12-07 | 2019-02-05 | 重庆科技学院 | A kind of opposite-flushing type solid-liquor separation and real time measure device |
| CN113304664A (en) * | 2021-05-31 | 2021-08-27 | 广州蓝涛水处理有限公司 | Emulsification device optimized through high-frequency ultrasonic action and laminar flow sedimentation |
| CN113304664B (en) * | 2021-05-31 | 2023-09-05 | 广州兰德环保资源科技有限公司 | Emulsifying device optimized through high-frequency ultrasonic action and laminar sedimentation |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081022 Termination date: 20121218 |