CN111729390A - Flowing type liquid impurity gradual separation device - Google Patents
Flowing type liquid impurity gradual separation device Download PDFInfo
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- CN111729390A CN111729390A CN202010792640.6A CN202010792640A CN111729390A CN 111729390 A CN111729390 A CN 111729390A CN 202010792640 A CN202010792640 A CN 202010792640A CN 111729390 A CN111729390 A CN 111729390A
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- pipeline hole
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
- B01D36/045—Combination of filters with centrifugal separation devices
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Abstract
The invention discloses a flowing type liquid impurity gradual separation device which comprises a rectangular shell. The device can separate the liquid mixed with the solid impurities, so that the impurities with different sizes are separated to different parts, the filter paper filter can conveniently and independently filter, the device can enable the impurities in the liquid to generate a centrifugal phenomenon when the device turns by utilizing the flowing speed of the liquid, so that the impurities are separated at the turning part, the single collection amount of the impurities is improved, then, the water flow speed is reduced due to the reduction of the water flow, and when the low-speed water flow turns, the impurities can be driven to generate the centrifugal phenomenon to be collected again, so that the device can perform the size type separation effect on the impurities, and the working efficiency is improved.
Description
Technical Field
The invention relates to the technical field of impurity separation devices, in particular to a flowing type liquid impurity gradual separation device.
Background
At present, when there is impurity in the liquid, all can separate, current separator includes filter paper filtration and centrifugal filtration, but because the granule size that exists impurity in the liquid is inconsistent, and general filter paper mode is poured the filtration into with whole, and efficiency is very low to, the emergence of easy emergence blocking phenomenon.
Disclosure of Invention
The present invention aims at providing a flowing type liquid impurity gradual separation device to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme: a flowing type liquid impurity gradual separation device comprises a rectangular shell, wherein a main injection connecting port is arranged at the top of one side of the rectangular shell, a first cylindrical pipeline hole is arranged at one side of the main injection connecting port, a first annular pipeline hole is arranged at the end part of the first cylindrical pipeline hole, a first conical compression space is arranged at the bottom end part of the first annular pipeline hole, a second cylindrical pipeline hole is arranged at the port of the first conical compression space, a second annular pipeline hole is arranged at the end part of the second annular pipeline hole, a second conical compression space is arranged at the bottom end part of the second annular pipeline hole, a third cylindrical pipeline hole is arranged at the port of the second conical compression space, a third annular pipeline hole is arranged at the end part of the third cylindrical pipeline hole, and a third conical compression space is arranged at the bottom end part of the third annular pipeline hole, the port in third toper compression space is equipped with third cylinder pipeline hole, the tip in third cylinder pipeline hole communicates external space, the inner wall in first cylinder pipeline hole, second cylinder pipeline hole, third cylinder pipeline hole and third cylinder pipeline hole all is equipped with vortex groove structure, the rectangle shell is being located the inner wall of first annular pipeline hole, second annular pipeline hole and third annular pipeline hole outer loop is equipped with first partition plate structure, second partition plate structure and the third partition plate structure of integral type structure respectively, the pipeline region that first partition plate structure, second partition plate structure and third partition plate structure formed communicates with main first discharge hole, main second discharge hole and the main third discharge hole that set up in the rectangle shell inside respectively.
Further, the first dividing plate structure, the second dividing plate structure and the third dividing plate structure are obliquely upward structures.
Further, the vortex groove structure is a plurality of annular array vortex groove structures.
Further, the top portions of the first, second, and third partition plate structures divide the middle portions of the first, second, and third annular duct holes into two, respectively.
Further, the first partition plate structure, the second partition plate structure and the third partition plate structure are respectively located on the inner sides of the outer rings of the first annular duct hole, the second annular duct hole and the third annular duct hole.
Compared with the prior art, the invention has the beneficial effects that: the device can separate the liquid mixed with the solid impurities, so that the impurities with different sizes are separated to different parts, the filter paper filter can conveniently and independently filter, the device can enable the impurities in the liquid to generate a centrifugal phenomenon when the device turns by utilizing the flowing speed of the liquid, so that the impurities are separated at the turning part, the single collection amount of the impurities is improved, then, the water flow speed is reduced due to the reduction of the water flow, and when the low-speed water flow turns, the impurities can be driven to generate the centrifugal phenomenon to be collected again, so that the device can perform the size type separation effect on the impurities, and the working efficiency is improved.
Drawings
FIG. 1 is a schematic diagram of a flow type liquid impurity gradual separation device according to the present invention;
FIG. 2 is a schematic top view of the middle portion of the first annular pipe hole in the apparatus for stepwise separating impurities from a flowing liquid according to the present invention;
in the figure: 1, rectangular housing, 2, main injection connection port, 3, first cylindricality pipeline hole, 4, vortex groove structure, 5, first annular pipeline hole, 6, first toper compression space, 7, second cylindricality pipeline hole, 8, second annular pipeline hole, 9, second toper compression space, 10, third cylindricality pipeline hole, 11, third annular pipeline hole, 12, third toper compression space, 13, third cylindricality pipeline hole, 14, first division plate structure, 15, main first discharge hole, 16, second division plate structure, 17, main second discharge hole, 18, third division plate structure, 19, main third discharge hole.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1 and 2, an embodiment of the present invention is shown: comprises a rectangular shell 1, a main injection connecting port 2 is arranged at the top of one side of the rectangular shell 1, a first cylindrical pipeline hole 3 is arranged at one side of the main injection connecting port 2, a first annular pipeline hole 5 is arranged at the end part of the first cylindrical pipeline hole 3, a first conical compression space 6 is arranged at the bottom end part of the first annular pipeline hole 5, a second cylindrical pipeline hole 7 is arranged at the port of the first conical compression space 6, a second annular pipeline hole 8 is arranged at the end part of the second annular pipeline hole 7, a second conical compression space 9 is arranged at the bottom end part of the second annular pipeline hole 8, a third cylindrical pipeline hole 10 is arranged at the port of the second conical compression space 9, a third annular pipeline hole 11 is arranged at the end part of the third cylindrical pipeline hole 10, and a third conical compression space 12 is arranged at the bottom end part of the third annular pipeline hole 11, the port of third toper compression space 12 is equipped with third cylinder pipeline hole 13, the tip intercommunication external space of third cylinder pipeline hole 13, the inner wall of first cylinder pipeline hole 3, second cylinder pipeline hole 7, third cylinder pipeline hole 10 and third cylinder pipeline hole 13 all is equipped with vortex groove structure 4, rectangular shell 1 is lieing in the inner wall of first annular pipeline hole 5, second annular pipeline hole 8 and third annular pipeline hole 11 outer ring is equipped with first partition plate structure 14, second partition plate structure 16 and the third partition plate structure 18 of integral type structure respectively, the pipeline region that first partition plate structure 14, second partition plate structure 16 and third partition plate structure 18 formed communicates with main first discharge hole 15, main second discharge hole 17 and the main third discharge hole 19 that set up at rectangular shell 1 inside respectively.
The first, second and third dividing panel structures 14, 16, 18 are diagonally upward structures.
The vortex groove structure 4 is a plurality of annular array vortex groove structures.
The tops of the first, second, and third partition plate structures 14, 16, and 18 divide the middle portions of the first, second, and third annular duct holes 5, 8, and 11, respectively, in two.
The first, second and third split plate structures 14, 16 and 18 are located inside the outer rings of the first, second and third annular duct holes 5, 8 and 11, respectively.
The specific use mode is as follows: in the operation of the invention, the main injection connecting port 2 is butted with a pipeline for discharging liquid, then a plurality of storage tanks for storing separated liquid are respectively communicated with the main first discharge hole 15, the main second discharge hole 17, the main third discharge hole 19 and the main fourth discharge hole 13, when impurities with different sizes enter the first cylindrical pipeline hole 3, the liquid and the liquid are accelerated under the action of the vortex groove structure 4, when the liquid enters the first annular pipeline hole 5, the liquid with a large amount of impurities can be turned due to the limitation of the pipeline holes, when the liquid is turned, the impurities in the liquid can generate a centrifugal phenomenon, the centrifugal phenomenon enables the impurities with the speed to move outwards and further enter the inner side of the partition plate structure 14, and then the impurities with the size smaller than the centrifugal phenomenon can enter the inner side of the second cylindrical pipeline hole 7, and in the same way, the liquid with different impurity sizes enters different areas, and then the liquid in different areas is filtered by using the filter paper with corresponding filter holes.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (5)
1. A flow-type liquid impurity gradual separation device comprising a rectangular housing (1), characterized in that: the top of one side of the rectangular shell (1) is provided with a main injection connecting port (2), one side of the main injection connecting port (2) is provided with a first cylindrical pipeline hole (3), the end part of the first cylindrical pipeline hole (3) is provided with a first annular pipeline hole (5), the bottom end part of the first annular pipeline hole (5) is provided with a first conical compression space (6), the port of the first conical compression space (6) is provided with a second cylindrical pipeline hole (7), the end part of the second cylindrical pipeline hole (7) is provided with a second annular pipeline hole (8), the bottom end part of the second annular pipeline hole (8) is provided with a second conical compression space (9), the port of the second conical compression space (9) is provided with a third cylindrical pipeline hole (10), the end part of the third cylindrical pipeline hole (10) is provided with a third annular pipeline hole (11), the bottom position of third annular pipeline hole (11) is equipped with a third toper compression space (12), the port of third toper compression space (12) is equipped with third cylindrical pipeline hole (13), the tip intercommunication external space of third cylindrical pipeline hole (13), the inner wall of first cylindrical pipeline hole (3), second cylindrical pipeline hole (7), third cylindrical pipeline hole (10) and third cylindrical pipeline hole (13) all is equipped with vortex groove structure (4), rectangle shell (1) is lieing in the inner wall of first annular pipeline hole (5), second annular pipeline hole (8) and third annular pipeline hole (11) outer loop is equipped with first partition plate structure (14), second partition plate structure (16) and third partition plate structure (18) of integral type structure respectively, the pipeline region that first partition plate structure (14), second partition plate structure (16) and third partition plate structure (18) formed respectively with set up at the shell rectangle shell with the setting (1) The inner main first discharge hole (15), the main second discharge hole (17) and the main third discharge hole (19) are communicated.
2. A flow-type liquid impurity progressive separation device according to claim 1, wherein: the first, second and third dividing plate structures (14, 16, 18) are obliquely upward structures.
3. A flow-type liquid impurity progressive separation device according to claim 1, wherein: the vortex groove structure (4) is a plurality of annular array vortex groove structures.
4. A flow-type liquid impurity gradual separation device as claimed in claim 2, wherein: the tops of the first, second and third division plate structures (14, 16, 18) divide the middle of the first, second and third annular duct holes (5, 8, 11), respectively, in two.
5. A flow-type liquid impurity gradual separation device according to claim 4, characterized in that: the first, second and third split plate structures (14, 16, 18) are located inside outer rings of the first, second and third annular duct holes (5, 8, 11), respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010792640.6A CN111729390A (en) | 2020-08-09 | 2020-08-09 | Flowing type liquid impurity gradual separation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010792640.6A CN111729390A (en) | 2020-08-09 | 2020-08-09 | Flowing type liquid impurity gradual separation device |
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| Publication Number | Publication Date |
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| CN111729390A true CN111729390A (en) | 2020-10-02 |
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| CN202010792640.6A Pending CN111729390A (en) | 2020-08-09 | 2020-08-09 | Flowing type liquid impurity gradual separation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113546465A (en) * | 2021-08-18 | 2021-10-26 | 兰振彦 | Rotary centrifugal liquid filtering device |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3707068A (en) * | 1970-02-25 | 1972-12-26 | Worthington Corp | Multistage liquid and gas separator |
| CN201195137Y (en) * | 2008-04-23 | 2009-02-18 | 中国大唐集团科技工程有限公司 | A nozzle |
| CN202860179U (en) * | 2012-09-07 | 2013-04-10 | 中国五环工程有限公司 | Efficient liquid-liquid separation equipment |
| CN104971830A (en) * | 2015-05-27 | 2015-10-14 | 上海理工大学 | Coupling type inertial cyclone fluid particle heterogeneous separation device and method |
| KR101609133B1 (en) * | 2015-09-02 | 2016-04-05 | 주식회사 청우이엔이 | Filtering Sortor Having Double Drum of Concentric Rotation Type |
| CN105797481A (en) * | 2016-03-14 | 2016-07-27 | 夏士桀 | Filter system for hydraulic and hydro-power engineering |
| CN206235374U (en) * | 2016-11-12 | 2017-06-09 | 陈娜 | A kind of oil recovery anti-clogging collection transportation metering device |
| CN206903959U (en) * | 2017-06-19 | 2018-01-19 | 江苏如克环保设备有限公司 | Sludge reflux pump |
| CN108144534A (en) * | 2018-01-08 | 2018-06-12 | 深圳市伟力低碳股份有限公司 | Two-fluid electric hybrid module and dynamic ice-making machine |
| CN209752494U (en) * | 2019-01-25 | 2019-12-10 | 武汉蓝特环保有限公司 | High-efficient hydrogen chloride impurity separation device |
| CN110608194A (en) * | 2019-09-16 | 2019-12-24 | 华中科技大学 | Centrifugal fan turns to spiral case |
-
2020
- 2020-08-09 CN CN202010792640.6A patent/CN111729390A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3707068A (en) * | 1970-02-25 | 1972-12-26 | Worthington Corp | Multistage liquid and gas separator |
| CN201195137Y (en) * | 2008-04-23 | 2009-02-18 | 中国大唐集团科技工程有限公司 | A nozzle |
| CN202860179U (en) * | 2012-09-07 | 2013-04-10 | 中国五环工程有限公司 | Efficient liquid-liquid separation equipment |
| CN104971830A (en) * | 2015-05-27 | 2015-10-14 | 上海理工大学 | Coupling type inertial cyclone fluid particle heterogeneous separation device and method |
| KR101609133B1 (en) * | 2015-09-02 | 2016-04-05 | 주식회사 청우이엔이 | Filtering Sortor Having Double Drum of Concentric Rotation Type |
| CN105797481A (en) * | 2016-03-14 | 2016-07-27 | 夏士桀 | Filter system for hydraulic and hydro-power engineering |
| CN206235374U (en) * | 2016-11-12 | 2017-06-09 | 陈娜 | A kind of oil recovery anti-clogging collection transportation metering device |
| CN206903959U (en) * | 2017-06-19 | 2018-01-19 | 江苏如克环保设备有限公司 | Sludge reflux pump |
| CN108144534A (en) * | 2018-01-08 | 2018-06-12 | 深圳市伟力低碳股份有限公司 | Two-fluid electric hybrid module and dynamic ice-making machine |
| CN209752494U (en) * | 2019-01-25 | 2019-12-10 | 武汉蓝特环保有限公司 | High-efficient hydrogen chloride impurity separation device |
| CN110608194A (en) * | 2019-09-16 | 2019-12-24 | 华中科技大学 | Centrifugal fan turns to spiral case |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113546465A (en) * | 2021-08-18 | 2021-10-26 | 兰振彦 | Rotary centrifugal liquid filtering device |
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Application publication date: 20201002 |