CN203664031U - Vacuum bubble centrifugal separation device - Google Patents
Vacuum bubble centrifugal separation device Download PDFInfo
- Publication number
- CN203664031U CN203664031U CN201320883506.2U CN201320883506U CN203664031U CN 203664031 U CN203664031 U CN 203664031U CN 201320883506 U CN201320883506 U CN 201320883506U CN 203664031 U CN203664031 U CN 203664031U
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- Prior art keywords
- knockout drum
- vacuum
- bubble
- valve
- transfer tank
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- Expired - Lifetime
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- 238000000926 separation method Methods 0.000 title abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 47
- 238000004140 cleaning Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000009471 action Effects 0.000 description 9
- 239000002994 raw material Substances 0.000 description 8
- 230000005484 gravity Effects 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 238000007872 degassing Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000009795 derivation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model relates to a material bubble separation device, in particular to a vacuum bubble centrifugal separation device for bubble separation inside a sealed containing cavity. The vacuum bubble centrifugal separation device comprises a separation tank, a motor, a material throwing disc, a feeding pipe, a separation tank air inlet and a separation tank vacuum valve, wherein the separation tank is fixed to the interior of a machine shell, the motor is arranged on the top of the separation tank, the material throwing disc is arranged inside the separation tank and driven by the motor, and the feeding pipe is installed at the upper portion of the separation tank and extends into the material throwing disc. A material collecting segment is arranged at the lower portion of the separation tank. A discharging pipe is arranged at the lower end of the separation tank. According to the vacuum bubble centrifugal separation device, residual bubbles remaining in the materials can be removed within sufficient time, and the bubble removal effect is ideal. The vacuum bubble centrifugal separation device is high in bubble removal processing efficiency, the materials are saved, secondary pollution of the materials is avoided, the structure is simple, the manufacturing cost is reduced, and the bubble removal effect is good.
Description
Technical field
The utility model relates to a kind of material bubble detaching device, particularly in closed containing cavity, in deaeration process, carries out the bubbles of vacuum centrifugal separating device of separate bubbles.
Background technology
Make at current fine chemistry industry, raw material, electron trade, battery industry and field of novel, through stirring or pre-treatment after raw material, need to carry out the mask work of air entrapment, finally tinning or be applied in subsequent production.The deaeration processing of present stage is the discontinuity operation of single small lot ground, and at the bottom of its production capacity utmost point, it is high that raw material are subject to the probability of secondary pollution, and raw-material waste is extremely serious again.Chinese patent 200820062126.1 discloses a kind of " agitator ", and Chinese patent 200820223477.6 discloses a kind of " stepless balance-adjustable bubble eliminating agitator ".Above-mentioned patent comprises casing, is fixed on the motor on casing, and by the pallet of driven by motor, activity is connected in the saucer on pallet, and pallet is revolved round the sun by driven by motor, and saucer drives saucer rotation through transmission mechanism.Above-mentioned patent can conveniently be mixed and deaeration several raw materials, and it still exists the discontinuity operation of single small lot ground, and at the bottom of its production capacity, it is high that raw material are subject to the probability of secondary pollution, raw-material waste extremely serious problem again.Chinese patent 03100089.4 discloses a kind of " centrifugal rotary supergravity-membrane separating technology ", and above-mentioned patent mainly relies on diffusion barrier to carry out the particulate material that material goes out to need from the separation of particles in 10 ~ 0.0001 scopes.Chinese patent 02140838.6 discloses a kind of " drum centrifugal separator ", this patent by front with belt pulley, back hopper, in establish the rotary barrel of speeding-up blade and front diffluence pass, rear overfall, middle shutoff, the center tubular axis that supports scraper conveyer by interior bottom forms, by the varigrained slurry of blade acceleration centrifugation.Appeal patent can be conveniently to varigrained raw material by being separated for centrifugation mode, due to structure cause being applied to the continuous separate of slurry air entrapment from.Chinese patent 201110451094.0 discloses a kind of " online continuous degassing device ", this patent comprises vacuum chamber, by driven by motor and reach the transmission main shaft in vacuum chamber, the discrete tank of the circle drum being driven by transmission main shaft in vacuum chamber, the rim of a cup that is characterized in discrete tank is connected with lid, covers to have to cover hole, and feed pipe reaches in discrete tank through vacuum chamber and lid hole, discharge nozzle reaches in discrete tank through vacuum chamber and lid hole, and the gas phase discharge pipe being connected with aspiration pump reaches in vacuum chamber.This utility model reaches feed pipe and the discharge nozzle in discrete tank by setting, arranges and reaches the gas phase discharge pipe of vacuum chamber, thereby realized continuous feed, discharging and exhaust, has formed online continuous degassing.Appeal patent can realize online continuous degassing easily, but there is degassed deficiency of time for the large slurry of surface tension, for the slurry having taken off after gas, the phenomenon that easily again produces bubble at the shock of the discharge nozzle mouth of pipe cannot be avoided, and finally causes having some limitations in slurry sector application.
Utility model content
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art, obviously increases the degassed time and makes its fully degassed bubbles of vacuum centrifugal separating device thereby provide a kind of in larger capillary material degassing process.
The purpose of this utility model solution is: a kind of bubbles of vacuum centrifugal separating device, comprise the knockout drum being fixed in casing, be placed in the motor at knockout drum top, in knockout drum, by the batch mixing pan of driven by motor, the feed pipe reaching in batch mixing pan is installed on knockout drum top, and knockout drum air inlet and knockout drum vacuum valve, it is characterized in that the section of gathering materials is arranged at knockout drum bottom, knockout drum lower end is provided with discharge nozzle, is characterized in that the section of gathering materials is arranged at knockout drum bottom, and knockout drum lower end is provided with knockout drum discharge nozzle.
Its course of work is: first knockout drum is vacuumized, by feed pipe injecting material, then open motor, batch mixing pan is rotated, material enter under centrifugal action, slide from central authorities toward batch mixing pan edge after batch mixing pan also degassed, material gets rid of material to knockout drum inwall in the time of batch mixing pan edge under centrifugal action, the material that arrives inwall becomes film liquid state, under Action of Gravity Field, slide along knockout drum inwall, slide and carry out degassed to residual bubble simultaneously in the long period, finally arriving the vacuum separation pot bottom section of gathering materials stores, when having stored disable motor after a certain amount of degassed material, open knockout drum air valve, air is entered, under Action of Gravity Field, degassed material is derived from knockout drum discharging opening.Because material slides along knockout drum inwall under Action of Gravity Field, the long period slide residual bubble is carried out simultaneously degassed, thereby have the sufficient time degassed to residuing in remaining bubble in material, reach desirable degasifying effect.
A middle rotary valve is set in solution of the present utility model after discharge nozzle, connects transfer tank after middle rotary valve, transfer canister incoming gas mouth and transfer tank vacuum valve are installed in transfer tank top, and transfer tank rear portion is provided with transfer tank discharge nozzle.
Its course of work is: first knockout drum is vacuumized, injecting material, then open motor, batch mixing pan is rotated, and material enters and under centrifugal action, is slided after batch mixing pan also degassedly from central authorities toward web, and material gets rid of material to knockout drum inwall in the time of batch mixing pan edge under centrifugal action, the material that arrives inwall becomes film liquid state, under Action of Gravity Field, slide along separating tank skin, slide and residual bubble is carried out degassedly simultaneously in the long period, finally arrive vacuum separation pot bottom and gather materials mouthful and to store.When having stored disable motor after certain degassed material, start vavuum pump transfer tank is vacuumized and opens knockout drum air valve simultaneously and make knockout drum pressure obviously be greater than transfer tank, then open after transfer valve material enters transfer tank and temporarily store by transfer tank.Enter and close middle rotary valve after transfer tank and open transfer ullage air valve etc. degassed material, then opening outlet valve will become material to derive by discharging opening, open vavuum pump in the derivation of one-tenth material simultaneously and knockout drum is vacuumized and then opened motor, importing material carries out next time degassed, and enter the transfer of transfer tank and derivation, so circulation, thus realize the continuous processing of bubble.
Solution intermediate pump of the present utility model is linked respectively on knockout drum vacuum valve and transfer tank vacuum valve by vacuum tube.Its objective is and adopt a set of vavuum pump to vacuumize knockout drum and transfer tank respectively.
Solution transfer tank afterbody of the present utility model is provided with cleaning valve and scavenge pipe, its objective is and is convenient to clean transfer tank.
Inlet valve is installed in solution of the present utility model on feed pipe, when its object, controls mass flow flow velocity.
The section of gathering materials in solution of the present utility model in knockout drum is conical or semicircle, its objective is and gathers materials and increase material flowing time.
Advantage of the present utility model: the utility model is filled with bottom in separation and established knockout drum discharging opening, when material is slided along knockout drum inwall under Action of Gravity Field, slide and carry out degassed to residual bubble simultaneously in the long period, thereby there is the sufficient time degassed to residuing in remaining bubble in material, reach desirable degasifying effect.After knockout drum discharging opening, be connected with transfer tank, carry out continuous operation by the effective cooperation between knockout drum and transfer tank and each valve, and realize a set of vacuum system and carried out time-sharing multiplex, simplify complete machine structure, form on the whole continuous feed, discharging and exhaust, formed continuous centrifugal bubble separation process.The utility model deaeration treatment effeciency is high, saves material, has avoided the secondary pollution of material, simple in structure, has reduced cost, and deaeration is effective.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1, lower margin; 2, casing; 3, the mouth that gathers materials; 4, the section of gathering materials; 5, knockout drum; 6, centrifugal pan; 7, inlet valve; 8, charging aperture; 9, motor; 10, knockout drum air scoop; 11, knockout drum vacuum valve; 12, vavuum pump; 13, vacuum tube; 14, transfer tank vacuum valve; 15, transfer tank; 16, transfer ullage gas port; 17, discharge pump; 18, outlet valve; 19, discharging opening; 20, middle rotary valve; 21, clean blowoff valve.
The specific embodiment
The utility model specific embodiment is as shown in Figure 1: a kind of bubbles of vacuum centrifugal separating device, comprise the knockout drum 5 being fixed in casing 2, be placed in the motor 9 at knockout drum 5 tops, the batch mixing pan 6 being driven by motor 9 in knockout drum 5, the feed pipe 8 reaching in batch mixing pan 6 is installed on knockout drum 5 tops, inlet valve 7 on feed pipe 8, and knockout drum air inlet 10 and knockout drum vacuum valve 11, the section of gathering materials 4 is arranged at knockout drum 5 bottoms, knockout drum 5 lower ends are provided with knockout drum discharge nozzle 3, a middle rotary valve 20 is set after discharge nozzle 3, the rear connection transfer of middle rotary valve 20 tank 15, transfer canister incoming gas mouth 16 and transfer tank vacuum valve 14 are installed in transfer tank 15 tops, transfer tank 15 rear portions are provided with transfer tank discharge nozzle 19.Vavuum pump 12 is linked on knockout drum 5 and transfer tank 15 through knockout drum vacuum valve 11 and transfer tank vacuum valve 14 respectively by vacuum tube 13.On transfer tank discharge nozzle 19, there are blow-off valve 18 and discharge pump 17.Transfer tank 15 afterbodys are provided with scavenge pipe and cleaning valve 21.Casing 2 is supported by lower margin 1.
Claims (6)
1. a bubbles of vacuum centrifugal separating device, comprise the knockout drum (5) being fixed in casing (2), be placed in the motor (9) at knockout drum (5) top, the batch mixing pan (6) being driven by motor (9) in knockout drum (5), the feed pipe (8) reaching in batch mixing pan (6) is installed on knockout drum (5) top, and knockout drum air inlet (10) and knockout drum vacuum valve (11), it is characterized in that the section of gathering materials (4) is arranged at knockout drum (5) bottom, knockout drum (5) lower end is provided with knockout drum discharge nozzle (3).
2. bubbles of vacuum centrifugal separating device according to claim 1, it is characterized in that arranging a middle rotary valve (20) after discharge nozzle (3), after middle rotary valve (20), connect transfer tank (15), transfer canister incoming gas mouth (16) and transfer tank vacuum valve (14) are installed in transfer tank (15) top, and transfer tank (15) rear portion is provided with transfer tank discharge nozzle (19).
3. bubbles of vacuum centrifugal separating device according to claim 1, is characterized in that vavuum pump (12) links on knockout drum vacuum valve (11) and transfer tank vacuum valve (14) by vacuum tube (13).
4. bubbles of vacuum centrifugal separating device according to claim 1, is characterized in that transfer tank (15) afterbody is provided with cleaning valve (21).
5. bubbles of vacuum centrifugal separating device according to claim 1, is characterized in that being provided with on feed pipe (8) inlet valve (7).
6. bubbles of vacuum centrifugal separating device according to claim 1, is characterized in that the section of gathering materials (4) of knockout drum (5) is for conical or semicircle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320883506.2U CN203664031U (en) | 2013-12-31 | 2013-12-31 | Vacuum bubble centrifugal separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320883506.2U CN203664031U (en) | 2013-12-31 | 2013-12-31 | Vacuum bubble centrifugal separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203664031U true CN203664031U (en) | 2014-06-25 |
Family
ID=50960365
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320883506.2U Expired - Lifetime CN203664031U (en) | 2013-12-31 | 2013-12-31 | Vacuum bubble centrifugal separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203664031U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103721866A (en) * | 2013-12-31 | 2014-04-16 | 绵阳世诺科技有限公司 | Vacuum bubble centrifugal separation device |
| CN105002374A (en) * | 2015-07-30 | 2015-10-28 | 云南驰宏锌锗股份有限公司 | Zinc sulfate solution super-gravity field purification device |
| CN105773995A (en) * | 2014-12-24 | 2016-07-20 | 中材科技风电叶片股份有限公司 | Defoaming device of single-component liquid resin and defoaming method |
-
2013
- 2013-12-31 CN CN201320883506.2U patent/CN203664031U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103721866A (en) * | 2013-12-31 | 2014-04-16 | 绵阳世诺科技有限公司 | Vacuum bubble centrifugal separation device |
| CN105773995A (en) * | 2014-12-24 | 2016-07-20 | 中材科技风电叶片股份有限公司 | Defoaming device of single-component liquid resin and defoaming method |
| CN105773995B (en) * | 2014-12-24 | 2018-08-14 | 中材科技风电叶片股份有限公司 | The liquid resinous defoaming device of one-component and defoaming method |
| CN105002374A (en) * | 2015-07-30 | 2015-10-28 | 云南驰宏锌锗股份有限公司 | Zinc sulfate solution super-gravity field purification device |
| CN105002374B (en) * | 2015-07-30 | 2017-03-29 | 云南驰宏锌锗股份有限公司 | A kind of solution of zinc sulfate super gravity field purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140625 |
|
| CX01 | Expiry of patent term |