CN202263648U - A spiral discharging centrifuge - Google Patents
A spiral discharging centrifuge Download PDFInfo
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- CN202263648U CN202263648U CN2011202859755U CN201120285975U CN202263648U CN 202263648 U CN202263648 U CN 202263648U CN 2011202859755 U CN2011202859755 U CN 2011202859755U CN 201120285975 U CN201120285975 U CN 201120285975U CN 202263648 U CN202263648 U CN 202263648U
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- baffle plate
- rotary drum
- light liquid
- helical
- liquid phase
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Abstract
The utility model discloses a spiral discharging centrifuge, comprising a rack, a material feeding pipe, a drum and a spiral material conveyor. A cavity chamber is disposed in the spiral material conveyor; the material feeding pipe is disposed on the drum and passes through the cavity chamber; an inflation pipe is disposed in the material feeding pipe and penetrates the material feeding pipe; the drum is provided with first baffle plates, second baffle plates, and third baffle plates; a conical portion of the drum is provided with fourth baffle plates; and the first baffle plates, the fourth baffle plates, a light liquid phase surface and a drum shaft axis form a pressure cavity. Through inflation from the inflation pipe to the cavity chamber, i.e., pressure application to the pressure cavity, the spiral discharging centrifuge can change thicknesses of the light liquid phase surface and a heavy liquid phase surface via pressure; and, when density difference between the light and heavy liquid phases is relatively small or separating medium fluctuates, corresponding air can be introduced in according to the difference of the densities of the light liquid phase and the heavy liquid phase for generating certain pressure and then relatively pure light liquid phase or heavy liquid phase can be obtained, so the spiral discharging centrifuge has relatively high separating efficiency.
Description
Technical field
The utility model relates to a kind of three-phase (light liquid phase/weight liquid/solid phases) separate control means, is specifically related to a kind of helical-conveyer centrifugal that is used for three phase separation.
Background technology
Liquid/liquid/(Gu light liquid phase/weight liquid/solid phases) three phase separation helical-conveyer centrifugal; To different separating mediums; According to light liquid mutually with the heavy-fluid density contrast of the two mutually; The overflow radius that often needs adjustment light liquid phase or heavy-fluid phase, the accuracy of overflow radius control is directly connected to the separating effect of weight two liquid phases, also is one of three phase separation helical-conveyer centrifugal core technology.
In the prior art, medium-sized three phase separation helical-conveyer centrifugal, its light liquid all is that press over system is discharged with heavy-fluid mutually, light liquid exports the overflow radius that exports mutually with heavy-fluid mutually, is controlled by overflow baffle (or overflow pipe).Another kind of for casting aside liquid type three phase separation helical-conveyer centrifugal; One of them liquid phase (light liquid phase or heavy-fluid phase) adopts casts aside liquid pipe (perhaps centripetal discharge pump) discharge; The overflow radius is by casting aside liquid management and control system, and another liquid phase is discharged with press over system, and the overflow radius is controlled by overflow baffle.
The shortcoming of plain edition three-phase centrifuge is: the overflow baffle of control light liquid phase or heavy-fluid phase overflow radius; Can't under the centrifuge running status, adjust; Must under stopped status, carry out; If run into separating medium fluctuation is arranged, need frequent shutdown adjustment overflow baffle size, even influence the centrifuge operate as normal.The shortcoming of casting aside liquid type three phase separation helical-conveyer centrifugal is: though need not to shut down, change the overflow radius that the liquid phase outlet just can be adjusted in the position of casting aside the liquid pipe, its control accuracy is lower, when separating medium has fluctuation, is difficult to realize dynamically control.
Therefore, a kind of less in weight two density of liquid phase differences, when separating medium has fluctuation, can accurately control the overflow radius, and can realize that the spiral conveyer centrifugal of dynamically control demands urgently proposing.
The utility model content
For solving the problems of the technologies described above, the purpose of the utility model be to provide a kind of less in weight two density of liquid phase differences, when separating medium has fluctuation, can accurately control the overflow radius, and can realize the dynamically spiral conveyer centrifugal of control.
For achieving the above object; The technical scheme of the utility model is following: a kind of helical-conveyer centrifugal, and be applied to three-phase (light liquid phase/weight liquid/solid phases) and separate, comprise frame, feed pipe, transmission device and differential drive device; Said frame is provided with rotary drum; Said rotary drum inboard is provided with screw input feeder, offers chamber in the said screw input feeder, and said feed pipe is arranged on the said rotary drum and passes said chamber;
Said rotary drum one end links to each other with said transmission device, and the other end links to each other with said differential drive device;
In said feed pipe, be equiped with gas tube, said gas tube is through said feed pipe;
Also be provided with first baffle plate on the said rotary drum, be used for the overflow of light liquid phase second baffle, be used for the 3rd baffle plate of heavy-fluid phase overflow, also be provided with the 4th baffle plate in the rotary drum tapering.
Preferably, the length of said first baffle plate and said the 4th baffle plate distance of all practising physiognomy to light liquid greater than said rotary drum axial line.
Preferably, said first baffle plate, the 4th baffle plate, light liquid is practised physiognomy and said rotary drum axial line between form a pressure chamber.
Preferably, said gas tube comprises air inlet and gas outlet, and said air inlet is arranged on the sidewall of said feed pipe.
Preferably, the outlet end of said gas tube exceeds the outlet end of said feed pipe.
Preferably, said first baffle plate, second baffle, the 3rd baffle plate, the 4th baffle plate all have two, and the face at every baffle plate place is all parallel, and per two baffle plates all are symmetrical set with said rotary drum axial line.
Preferably; Also comprise automaton, aerating device, density sensor and be used to detect said rotary drum axial line to weight liquidus surface and light liquid and the heavy-fluid alignment sensor of interface distance mutually, said automaton is connected with said sensor electrical with said aerating device.
Preferably, said automaton also is electrically connected with and shows and control panel.
Preferably, said first baffle plate is arranged in the middle of said second baffle and said the 3rd baffle plate.
Preferably, the distolateral solid phase that also is provided with in said rotary drum tapering exports.
Pass through technique scheme; The beneficial effect of the utility model technical scheme is: a kind of helical-conveyer centrifugal; Comprise frame, feed pipe, transmission device and differential drive device, said frame is provided with rotary drum, and said rotary drum inboard is provided with screw input feeder; Offer chamber in the said screw input feeder, said feed pipe is arranged on the said rotary drum and passes said chamber; In said feed pipe, be equiped with gas tube, said gas tube is through said feed pipe; Also be provided with first baffle plate on the said rotary drum, be used for the overflow of light liquid phase second baffle, be used for the 3rd baffle plate of heavy-fluid phase overflow, also be provided with the 4th baffle plate in the rotary drum tapering; Adopt the helical-conveyer centrifugal that the utility model provided; Said first baffle plate, the 4th baffle plate, light liquid is practised physiognomy and said rotary drum axial line between form a pressure chamber; Through in said chamber, inflating from gas tube; Promptly in pressure chamber, exert pressure, change the thickness that light liquid is practised physiognomy and heavy-fluid is practised physiognomy, promptly change the rotary drum axial line to light liquid phase and the mutually formed interfacial distance of heavy-fluid through pressure; When less or separating medium had fluctuation when the density contrast of weight two liquid phases, different with the heavy-fluid phase density mutually according to light liquid fed corresponding air, produce certain pressure, can obtain perhaps heavy-fluid phase of purer light liquid phase, and separative efficiency is higher.
Description of drawings
In order to be illustrated more clearly in the technical scheme in the utility model embodiment technology; To do to introduce simply to the accompanying drawing of required use in the embodiment technical description below; Obviously, the accompanying drawing in describing below only is some embodiment of the utility model, for those of ordinary skills; Under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of a kind of helical-conveyer centrifugal embodiment 1 of the utility model;
Fig. 2 is the partial schematic diagram of a kind of helical-conveyer centrifugal embodiment 1 of the utility model.
The represented corresponding component title of numeral among the figure:
1. frame 11. light liquids export 12. heavy-fluids mutually and export 2. feed pipes, 3. rotary drums, 31. first baffle plates, 32. second baffles 33. the 3rd baffle plate 34. the 4th baffle plate, 35. solid phases mutually and export 36. light liquid phase passages, 37. liquid collecting room, 38. heavy-fluid phase passages, 4. screw input feeders, 41. cloth holes, 5. differential drive devices, 6. gas tubes, 61. air inlets, 7. light liquids, 8. interfaces of practising physiognomy.
The specific embodiment
To combine the accompanying drawing among the utility model embodiment below, the technical scheme among the utility model embodiment is carried out clear, intactly description, obviously, described embodiment only is the utility model part embodiment, rather than whole embodiment.Based on the embodiment in the utility model, those of ordinary skills are not making the every other embodiment that is obtained under the creative work prerequisite, all belong to the scope of the utility model protection.
The utility model provide a kind of less in weight two density of liquid phase differences, when separating medium has fluctuation, can accurately control the overflow radius, and can realize the dynamically spiral conveyer centrifugal of control.
Like Fig. 1 and as shown in Figure 2; A kind of helical-conveyer centrifugal is applied to three-phase (light liquid phase/weight liquid/solid phases) and separates, and comprises frame 1, feed pipe 2, transmission device and differential drive device 5; Said frame 1 is provided with rotary drum 3; Said rotary drum 3 inboards are provided with screw input feeder 4, offer the chamber (not shown) in the said screw input feeder 4, and said feed pipe 2 is arranged on the said rotary drum 3 and passes said chamber; Said rotary drum 3 one ends link to each other with said transmission device, and the other end links to each other with said differential drive device 5, in said feed pipe 2, is equiped with gas tube 6, and said gas tube 6 is through said feed pipe 2, and the distolateral solid phase that also is provided with in said rotary drum 3 taperings exports 35.
Through installing said gas tube 6, in said chamber, feed gas, make that the pressure in the chamber becomes big, the center surface that makes centrifuge light liquid phase is by extra increase pressure Δ P (equaling the blowing pressure).
Also be provided with first baffle plate 31 on the said rotary drum 3, be used for the overflow of light liquid phase second baffle 32, be used for the 3rd baffle plate 33 of heavy-fluid phase overflow; Also be provided with the 4th baffle plate 34 in rotary drum 3 taperings; The length of said first baffle plate 31 and said the 4th baffle plate 34 all greater than said rotary drum axial line to practise physiognomy 7 distance of light liquid, simultaneously said first baffle plate 31, the 4th baffle plate 34, light liquid practise physiognomy 7 and said rotary drum axial line between pressure chamber of formation.
Through the pressure chamber of above-mentioned formation, the pressure through strengthening or reducing to inflate again can change light liquid and the heavy-fluid position of the branch face of the two mutually, thereby obtain highly purified light liquid phase or heavy-fluid phase.When strengthening the blowing pressure, light liquid outwards moves the position of interface 8 with heavy-fluid mutually, and the thickness of light liquid phase is strengthened, and the thickness of heavy-fluid phase reduces, and can obtain purer light liquid phase; Otherwise when reducing the blowing pressure, light liquid moves to the center position of interface 8 with heavy-fluid mutually, and the thickness of light liquid phase is reduced, and the thickness of heavy-fluid phase is strengthened, and can obtain purer heavy-fluid phase.
Said gas tube 6 comprises air inlet 61 and gas outlet (not shown), and said air inlet 61 is arranged on the sidewall of said feed pipe 2, places the outlet end of the said gas tube 6 in the said chamber to exceed the outlet end of said feed pipe 2.
Said first baffle plate 31, second baffle 32, the 3rd baffle plate 33, the 4th baffle plate 34 all have two, and the face at every baffle plate place is all parallel, and per two baffle plates all are symmetrical set with said rotary drum axial line; It is middle with said the 3rd baffle plate 33 that said first baffle plate 31 is arranged at said second baffle 32.
In the such scheme; When light liquid that the three phase separation helical-conveyer centrifugal is separated mutually or during the density contrast less (separation difficulty) of the purity requirement of heavy-fluid phase when higher, weight two liquid phases; When perhaps separating medium has fluctuation; The pressure of adjustment inflation can carry out under the centrifuge running status, can dynamically adjust and control by the situation of separating medium.
Its operation principle is: separating medium (mixed serum of light liquid phase/weight liquid/solid phases); The cloth hole 41 that gets into centrifuge screw input feeder 4 from feed pipe 2 gets in the rotary drum 3, and under the effect of centrifugal force field, light liquid phase/weight liquid/solid phases is by layering; Light liquid is at nexine; Heavy-fluid is at skin, and heavy-fluid and light liquid form interface 8 between mutually, and solid phase sinks on rotary drum 3 inwalls.
Light liquid flows into liquid collecting room 37 through light liquid phase passage 36, overflows through second plate washer 32 that is used for the overflow of light liquid phase again, and liquid phase outlet 11 is discharged on the lenient side; Heavy-fluid is overflowed through the third gear plate 33 that is used for the overflow of heavy-fluid phase mutually then from heavy-fluid phase passage 38, exports 12 mutually from heavy-fluid and discharges, and sinks to the solid phase outlet 35 that the solid phase on rotary drum 3 inwalls pushed to rotary drum 3 small ends by screw input feeder 4 and discharges.If seek out purer light liquid phase, then, in said chamber, feed gas through gas tube 21; Strengthen the blowing pressure, light liquid outwards moves the position of interface 8 with heavy-fluid mutually, and the thickness of light liquid phase is strengthened; The thickness of heavy-fluid phase reduces, and can obtain purer light liquid phase; If seek out purer heavy-fluid phase; Then reduce the blowing pressure, light liquid moves to the center position of interface 8 with heavy-fluid mutually, and the thickness of light liquid phase is reduced; The thickness of heavy-fluid phase is strengthened; Can obtain purer heavy-fluid phase, accomplish the density contrast of weight two liquid phases less (being separation difficulty), the three phase separation when perhaps separating medium has fluctuation with this.
Adopt the helical-conveyer centrifugal that the utility model provided; Said first baffle plate 31, the 4th baffle plate 34, light liquid practise physiognomy 7 and said rotary drum axial line between form a pressure chamber; Through in said chamber, inflating from gas tube 6; Promptly in pressure chamber, exert pressure, change the thickness that light liquid is practised physiognomy and heavy-fluid is practised physiognomy, promptly change the distance of rotary drum axial line to light liquid phase and the mutually formed interface 8 of heavy-fluid through pressure; When less or separating medium had fluctuation when the density contrast of weight two liquid phases, different with the heavy-fluid phase density mutually according to light liquid fed corresponding air, produce certain pressure, can obtain perhaps heavy-fluid phase of purer light liquid phase, and separative efficiency is higher.
All the other are same as the previously described embodiments; Difference is; Said helical-conveyer centrifugal also comprises automaton (not shown), aerating device (not shown), density sensor and is used to detect said rotary drum axial line practises physiognomy and light liquid and the heavy-fluid alignment sensor (not shown) of interface 8 distances mutually to light liquid; Said automaton is connected with said sensor electrical with said aerating device, and simultaneously, said automaton also is electrically connected with and shows and control panel.
Its operation principle is: starting device, and separating medium (mixed serum of light liquid phase/weight liquid/solid phases), the cloth hole 41 that gets into centrifuge screw input feeder 4 from feed pipe 2 gets in the rotary drum 3; Under the effect of centrifugal force field; Light liquid phase/weight liquid/solid phases is by layering, and light liquid is at nexine, and heavy-fluid is at skin; Heavy-fluid and light liquid form interface 8 between mutually, and solid phase sinks on rotary drum 3 inwalls.
If want to obtain purer light liquid phase, demonstration and control panel are operated, at this moment; Automaton receives signal, adopts said density sensor to measure light liquid phase and heavy-fluid density mutually, detects from the rotary drum axial line to the weight liquidus surface and the distance of interface 8 with alignment sensor; Corresponding signal is passed to automaton, through automaton control aerating device, feed corresponding air again; Make to reach corresponding pressure in the said chamber, obtain purer light liquid phase component; If want to obtain purer heavy-fluid phase, then demonstration and control panel are operated, at this moment; Through behind a series of collection signal; Automaton control aerating device reduces the blowing pressure, and light liquid moves to the center position of interface 8 with heavy-fluid mutually, and the thickness of light liquid phase is reduced; The thickness of heavy-fluid phase is strengthened, and can obtain purer heavy-fluid phase.
Adopt the present embodiment technical scheme; Except can reach less in weight two density of liquid phase differences, when separating medium has fluctuation; Can accurately control the overflow radius; And can realize outside the purpose of dynamically control, can also realize automation control, improve the precision of separation and the efficient of separation whole separation process.
Pass through technique scheme; The beneficial effect of the utility model technical scheme is: a kind of helical-conveyer centrifugal; Comprise frame 1, feed pipe 2, transmission device and differential drive device 5, said frame 1 is provided with rotary drum 3, and said rotary drum 3 inboards are provided with screw input feeder 4; Offer chamber in the said screw input feeder 4, said feed pipe 2 is arranged on the said rotary drum 3 and passes said chamber; In said feed pipe 2, be equiped with gas tube 6, said gas tube 6 is through said feed pipe 2; Also be provided with first baffle plate 31 on the said rotary drum 3, be used for the overflow of light liquid phase second baffle 32, be used for the 3rd baffle plate 33 of heavy-fluid phase overflow, also be provided with the 4th baffle plate 34 in rotary drum 3 taperings; Adopt the helical-conveyer centrifugal that the utility model provided; Said first baffle plate 31, the 4th baffle plate 34, light liquid practise physiognomy 7 and said rotary drum axial line between form a pressure chamber; Through in said chamber, inflating from gas tube 6; Promptly in pressure chamber, exert pressure, change the thickness that light liquid is practised physiognomy and heavy-fluid is practised physiognomy, promptly change the distance of rotary drum axial line to light liquid phase and the mutually formed interface 8 of heavy-fluid through pressure; When less or separating medium had fluctuation when the density contrast of weight two liquid phases, different with the heavy-fluid phase density mutually according to light liquid fed corresponding air, produce certain pressure, can obtain perhaps heavy-fluid phase of purer light liquid phase, and separative efficiency is higher.
To the above-mentioned explanation of the disclosed embodiments, make this area professional and technical personnel can realize or use the utility model.Multiple modification to these embodiment will be conspicuous concerning those skilled in the art, and defined General Principle can realize under the situation of spirit that does not break away from the utility model or scope in other embodiments among this paper.Therefore, the utility model will can not be restricted to these embodiment shown in this paper, but will meet and principle disclosed herein and features of novelty the wideest corresponding to scope.
Claims (10)
1. helical-conveyer centrifugal; Be applied to light liquid phase/weight liquid/solid phases and separate, it is characterized in that, comprise frame, feed pipe, transmission device and differential drive device; Said frame is provided with rotary drum; Said rotary drum inboard is provided with screw input feeder, offers chamber in the said screw input feeder, and said feed pipe is arranged on the said rotary drum and passes said chamber;
Said rotary drum one end links to each other with said transmission device, and the other end links to each other with said differential drive device;
In said feed pipe, be equiped with gas tube, said gas tube is through said feed pipe;
Also be provided with first baffle plate on the said rotary drum, be used for the overflow of light liquid phase second baffle, be used for the 3rd baffle plate of heavy-fluid phase overflow, also be provided with the 4th baffle plate in the rotary drum tapering.
2. helical-conveyer centrifugal according to claim 1 is characterized in that, the distance that the length of said first baffle plate and said the 4th baffle plate is all practised physiognomy to light liquid greater than said rotary drum axial line.
3. helical-conveyer centrifugal according to claim 2 is characterized in that, said first baffle plate, the 4th baffle plate, light liquid is practised physiognomy and said rotary drum axial line between form a pressure chamber.
4. helical-conveyer centrifugal according to claim 3 is characterized in that said gas tube comprises air inlet and gas outlet, and said air inlet is arranged on the sidewall of said feed pipe.
5. helical-conveyer centrifugal according to claim 4 is characterized in that, the outlet end of said gas tube exceeds the outlet end of said feed pipe.
6. helical-conveyer centrifugal according to claim 5; It is characterized in that; Said first baffle plate, second baffle, the 3rd baffle plate, the 4th baffle plate all have two, and the face at every baffle plate place is all parallel, and per two baffle plates all are symmetrical set with said rotary drum axial line.
7. helical-conveyer centrifugal according to claim 6; It is characterized in that; Also comprise automaton, aerating device, density sensor and be used to detect said rotary drum axial line to weight liquidus surface and light liquid and the heavy-fluid alignment sensor of interface distance mutually, said automaton is connected with said sensor electrical with said aerating device.
8. helical-conveyer centrifugal according to claim 7 is characterized in that, said automaton also is electrically connected with and shows and control panel.
9. according to each described helical-conveyer centrifugal of claim 1-8, it is characterized in that said first baffle plate is arranged in the middle of said second baffle and said the 3rd baffle plate.
10. helical-conveyer centrifugal according to claim 9 is characterized in that, the distolateral solid phase that also is provided with in said rotary drum tapering exports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202859755U CN202263648U (en) | 2011-08-09 | 2011-08-09 | A spiral discharging centrifuge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202859755U CN202263648U (en) | 2011-08-09 | 2011-08-09 | A spiral discharging centrifuge |
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| Publication Number | Publication Date |
|---|---|
| CN202263648U true CN202263648U (en) | 2012-06-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202859755U Withdrawn - After Issue CN202263648U (en) | 2011-08-09 | 2011-08-09 | A spiral discharging centrifuge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202263648U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102921562A (en) * | 2011-08-09 | 2013-02-13 | 苏州优耐特机械制造有限公司 | Spiral discharging centrifuge |
| CN109013071A (en) * | 2018-09-13 | 2018-12-18 | 安徽普源分离机械制造有限公司 | Gu a kind of liquid-liquid efficiently separated-three-phase high speed horizontal-spiral centrifuge |
| CN113769899A (en) * | 2021-09-28 | 2021-12-10 | 南京中船绿洲机器有限公司 | Anti-phase-crossing structure of three-phase disc separator |
-
2011
- 2011-08-09 CN CN2011202859755U patent/CN202263648U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102921562A (en) * | 2011-08-09 | 2013-02-13 | 苏州优耐特机械制造有限公司 | Spiral discharging centrifuge |
| CN102921562B (en) * | 2011-08-09 | 2015-03-11 | 苏州优耐特机械制造有限公司 | Spiral discharging centrifuge |
| CN109013071A (en) * | 2018-09-13 | 2018-12-18 | 安徽普源分离机械制造有限公司 | Gu a kind of liquid-liquid efficiently separated-three-phase high speed horizontal-spiral centrifuge |
| CN113769899A (en) * | 2021-09-28 | 2021-12-10 | 南京中船绿洲机器有限公司 | Anti-phase-crossing structure of three-phase disc separator |
| CN113769899B (en) * | 2021-09-28 | 2024-03-29 | 南京中船绿洲机器有限公司 | Three-phase disc separator prevents cluster looks structure |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20120606 Effective date of abandoning: 20150311 |
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| RGAV | Abandon patent right to avoid regrant |