CN105363570A - Three-phase disk centrifuge - Google Patents
Three-phase disk centrifuge Download PDFInfo
- Publication number
- CN105363570A CN105363570A CN201510937327.6A CN201510937327A CN105363570A CN 105363570 A CN105363570 A CN 105363570A CN 201510937327 A CN201510937327 A CN 201510937327A CN 105363570 A CN105363570 A CN 105363570A
- Authority
- CN
- China
- Prior art keywords
- rotary drum
- phase
- distributor
- machine body
- heavy
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
- B04B1/08—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/02—Continuous feeding or discharging; Control arrangements therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/02—Casings; Lids
- B04B7/04—Casings facilitating discharge
Landscapes
- Centrifugal Separators (AREA)
Abstract
The invention discloses a three-phase disk centrifuge comprising a machine body, a distributor arranged in the machine body, a disk located inside the machine body and connected to the outer wall of the distributor and a rotary drum connected with the inside of the machine body, wherein the rotary drum is provided with a rotary drum cover, the rotary drum cover is arranged on the outer wall of the machine body, a liquid outlet pipe is arranged in the rotary drum cover, one end of the liquid outlet pipe stretches into the machine body, the other end of the liquid outlet pipe communicates with a heavy phase outlet, a heavy phase spray nozzle is arranged at the connected part of the lower end of the rotary drum and the outer wall of the machine body, and a light phase passage is arranged between the rotary drum cover and the distributor. The three-phase disk centrifuge is directly upgraded and transformed on the basis of the existing two-phase disk separator, additional machining and manufacture of the rotary drum, the distributor and the disk are not needed, and an independent heavy phase passage can be added just by improving the rotary drum cover and adding the liquid outlet pipe and a heavy phase centripetal pump, thus realizing the function of three-phase separation, greatly lowering manufacture cost and being easy to maintain.
Description
Technical field
The present invention relates to a kind of centrifuge instrument, particularly a kind of three-phase disk centrifugal separator.
Background technology
The centrifugal force that disk centrifuge utilizes High Rotation Speed to produce, realizes being separated by the multiple immiscible and material that density is different.Existing nozzle deslagging disc type separator mostly is two-phase seperator, mainly comprises the video disc group that rotary drum body, distributor are coaxial with distributor.During real work, mixed liquor enters on the video disc of centrifuge by distributor inner circumferential passage, the drum assembly of High Rotation Speed produces powerful centrifugal force, heavy phase large for mixed liquor Midst density is deposited to rotary drum body inwall, by the heavy phase nozzle on rotatory drum wall, the solid phase being deposited on drum inner wall is discharged rotary drum continuously, light phase liquid after separation upwards climbs from the centripetal discharge pump of centrifuge along video disc and discharges, thus realizes the separation of proportion different liquids.But above-mentioned centrifuge is difficult to carry out three phase separation to three-phase mixed liquor.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, provides a kind of three-phase disk centrifugal separator that can realize carrying out three-phase mixed liquor three phase separation.
Technical scheme: for achieving the above object, the invention provides a kind of three-phase disk centrifugal separator, comprise body, be arranged on the distributor of internal body, be positioned at the video disc that internal body is connected to distributor outer wall and the rotary drum body be connected with internal body, described rotary drum body is provided with rotary drum lid, described rotary drum lid is arranged on the outer wall of body, drain pipe is provided with in described rotary drum lid, one end of described drain pipe extend into internal body, the other end is connected with heavy out, the lower end of described rotary drum body and the junction of body outer wall are provided with heavy phase nozzle, light phase passage is provided with between described rotary drum lid with distributor.
Preferably, the quantity of described drain pipe is 9.
Preferably, described heavy out is connected to heavy phase centripetal discharge pump.
Preferably, described light phase passage is connected to light phase centripetal discharge pump.
Preferably, described video disc and distributor adopt coaxial setting.
Preferably, the exit of described heavy out is provided with plugging block, utilizes the clogging heavy out of plugging block, thus can reach the switching from three phase separation to two-phase laminated flow.
Beneficial effect: the present invention compared with prior art, based on the direct upgrading of existing two-phase disk centrifuge, rotary drum body, distributor and video disc is manufactured without the need to additional processing, only need to improve rotary drum lid, increase drain pipe, heavy phase centripetal discharge pump, namely can increase and independently heavy phase channels, realize the function of three phase separation, greatly reduce manufacturing cost, be easy to safeguard.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, illustrate the present invention further, these embodiments should be understood only be not used in for illustration of the present invention and limit the scope of the invention, after having read the present invention, the amendment of those skilled in the art to the various equivalent form of value of the present invention has all fallen within the application's claims limited range.
As shown in Figure 1, the invention provides a kind of three-phase disk centrifugal separator, comprise body, be arranged on the distributor 1 of internal body, be positioned at the video disc 3 that internal body is connected to distributor 1 outer wall and the rotary drum body 2 be connected with internal body, described rotary drum body 2 is provided with rotary drum lid 6, described rotary drum lid 6 is arranged on the outer wall of body, drain pipe 8 is provided with in described rotary drum lid 6, one end of described drain pipe 8 extend into internal body, the other end is connected with heavy out 5, the lower end of described rotary drum body 2 and the junction of body outer wall are provided with heavy phase nozzle 4, light phase passage 9 is provided with between described rotary drum lid 6 with distributor 1, the quantity of described drain pipe 8 is 9, described heavy out 5 is connected to heavy phase centripetal discharge pump 10, described light phase passage 9 is connected to light phase centripetal discharge pump 11, described video disc 3 and distributor 1 adopt coaxial setting, the exit of described heavy out 5 is provided with plugging block 7.
In the present invention, mixed liquor enters internal body by distributor 1, the high-speed rotation of rotary drum body 2 produces powerful centrifugal force, the solid phase that mixed liquor Midst density is larger and heavy phase liquid are thrown to internal body lower end, solid phase liquid is discharged continuously by heavy phase nozzle 4, heavy phase then enters the drain pipe 8 in rotary drum lid 6, then discharge under the effect of heavy phase centripetal discharge pump 10, light then upwards climbing along video disc 3 mutually enters light phase passage 9, then discharges under the effect of light phase centripetal discharge pump 11.
When only carrying out mutually light and solid phase two-phase laminated flow, then plugging block 7 can be positioned over the exit of heavy out 5, clogging heavy out 5, then can realize the operation of two-phase laminated flow.
Claims (6)
1. a three-phase disk centrifugal separator, comprise body, be arranged on the distributor (1) of internal body, be positioned at the video disc (3) that internal body is connected to distributor (1) outer wall and the rotary drum body (2) be connected with internal body, it is characterized in that: described rotary drum body (2) is provided with rotary drum lid (6), described rotary drum lid (6) is arranged on the outer wall of body, drain pipe (8) is provided with in described rotary drum lid (6), one end of described drain pipe (8) extend into internal body, the other end is connected with heavy out (5), the lower end of described rotary drum body (2) and the junction of body outer wall are provided with heavy phase nozzle (4), light phase passage (9) is provided with between described rotary drum lid (6) with distributor (1).
2. a kind of three-phase disk centrifugal separator according to claim 1, is characterized in that: the quantity of described drain pipe (8) is 9.
3., according to claim 1 or 2 heavy phase centripetal discharge pump phase disk centrifugal separators, it is characterized in that: described heavy out (5) is connected to heavy phase centripetal discharge pump (10).
4. a kind of three-phase disk centrifugal separator according to claim 1, is characterized in that: described light phase passage (9) is connected to light phase centripetal discharge pump (11).
5. a kind of three-phase disk centrifugal separator according to claim 1, is characterized in that: described video disc (3) and distributor (1) adopt and coaxially arrange.
6. a kind of three-phase disk centrifugal separator according to claim 1, is characterized in that: the exit of described heavy out (5) is provided with plugging block (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510937327.6A CN105363570A (en) | 2015-12-15 | 2015-12-15 | Three-phase disk centrifuge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510937327.6A CN105363570A (en) | 2015-12-15 | 2015-12-15 | Three-phase disk centrifuge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105363570A true CN105363570A (en) | 2016-03-02 |
Family
ID=55366482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510937327.6A Pending CN105363570A (en) | 2015-12-15 | 2015-12-15 | Three-phase disk centrifuge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105363570A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107029900A (en) * | 2017-05-27 | 2017-08-11 | 宜兴市华鼎机械有限公司 | A kind of disk centrifugal separator |
| CN107185737A (en) * | 2017-05-27 | 2017-09-22 | 宜兴市华鼎机械有限公司 | A kind of disk centrifugal separator for eliminating bubble |
| CN108176520A (en) * | 2017-12-25 | 2018-06-19 | 江苏巨能机械有限公司 | Three-phase disc separator |
| CN108889460A (en) * | 2018-08-30 | 2018-11-27 | 镇江市长江机电设备厂有限公司 | A kind of disk centrifugal separator from damping |
| CN109701754A (en) * | 2018-12-03 | 2019-05-03 | 程微丽 | Disc separator for corn starch gluten concentration |
| CN114401793A (en) * | 2019-09-25 | 2022-04-26 | 阿法拉伐股份有限公司 | Centrifugal separator and method for controlling the same |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3410479A (en) * | 1965-08-23 | 1968-11-12 | Alfa Laval Ab | Sludge level indicating device for centrifugal separators |
| US3519200A (en) * | 1967-10-10 | 1970-07-07 | Alfa Laval Ab | Method for indicating changes of liquid pressure in a centrifugal separator |
| CN102712002A (en) * | 2010-01-29 | 2012-10-03 | 阿尔法拉瓦尔股份有限公司 | System comprising centrifugal separator and method for controlling such a system |
| CN103567085A (en) * | 2013-09-18 | 2014-02-12 | 浙江索纳克生物科技有限公司 | High-efficient environment-friendly disc separator |
| CN205323996U (en) * | 2015-12-15 | 2016-06-22 | 宜兴市华鼎机械有限公司 | Three -phase disk centrifuge |
-
2015
- 2015-12-15 CN CN201510937327.6A patent/CN105363570A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3410479A (en) * | 1965-08-23 | 1968-11-12 | Alfa Laval Ab | Sludge level indicating device for centrifugal separators |
| US3519200A (en) * | 1967-10-10 | 1970-07-07 | Alfa Laval Ab | Method for indicating changes of liquid pressure in a centrifugal separator |
| CN102712002A (en) * | 2010-01-29 | 2012-10-03 | 阿尔法拉瓦尔股份有限公司 | System comprising centrifugal separator and method for controlling such a system |
| CN103567085A (en) * | 2013-09-18 | 2014-02-12 | 浙江索纳克生物科技有限公司 | High-efficient environment-friendly disc separator |
| CN205323996U (en) * | 2015-12-15 | 2016-06-22 | 宜兴市华鼎机械有限公司 | Three -phase disk centrifuge |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107029900A (en) * | 2017-05-27 | 2017-08-11 | 宜兴市华鼎机械有限公司 | A kind of disk centrifugal separator |
| CN107185737A (en) * | 2017-05-27 | 2017-09-22 | 宜兴市华鼎机械有限公司 | A kind of disk centrifugal separator for eliminating bubble |
| CN108176520A (en) * | 2017-12-25 | 2018-06-19 | 江苏巨能机械有限公司 | Three-phase disc separator |
| CN108889460A (en) * | 2018-08-30 | 2018-11-27 | 镇江市长江机电设备厂有限公司 | A kind of disk centrifugal separator from damping |
| CN109701754A (en) * | 2018-12-03 | 2019-05-03 | 程微丽 | Disc separator for corn starch gluten concentration |
| CN114401793A (en) * | 2019-09-25 | 2022-04-26 | 阿法拉伐股份有限公司 | Centrifugal separator and method for controlling the same |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 214214, No. 888, Gao Yi Road, Yixing, Jiangsu, Wuxi Applicant after: YIXING HUADING FOOD MACHINE CO., LTD. Address before: 214214, No. 888, Gao Yi Road, Yixing, Jiangsu, Wuxi Applicant before: YIXING HUADING FOOD MACHINE CO., LTD. |
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| COR | Change of bibliographic data | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160302 |
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| WD01 | Invention patent application deemed withdrawn after publication |