CN106824556A - A kind of weight liquid separation horizontal type coil pipe centrifuge - Google Patents
A kind of weight liquid separation horizontal type coil pipe centrifuge Download PDFInfo
- Publication number
- CN106824556A CN106824556A CN201710078720.3A CN201710078720A CN106824556A CN 106824556 A CN106824556 A CN 106824556A CN 201710078720 A CN201710078720 A CN 201710078720A CN 106824556 A CN106824556 A CN 106824556A
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- Prior art keywords
- coil pipe
- rotary drum
- storage compartment
- sub
- horizontal type
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- 239000007788 liquid Substances 0.000 title claims abstract description 105
- 238000000926 separation method Methods 0.000 title claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 66
- 238000005119 centrifugation Methods 0.000 claims abstract description 8
- 230000004888 barrier function Effects 0.000 claims description 15
- 230000002787 reinforcement Effects 0.000 claims description 6
- 238000003825 pressing Methods 0.000 claims description 4
- 239000012530 fluid Substances 0.000 abstract description 25
- 238000003973 irrigation Methods 0.000 abstract 1
- 230000002262 irrigation Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 13
- 239000000203 mixture Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000006071 cream Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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
-
- 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
- B04B7/08—Rotary bowls
Landscapes
- Centrifugal Separators (AREA)
Abstract
The invention discloses a kind of weight liquid separation horizontal type coil pipe centrifuge, its drip irrigation device is to include rotary drum, feed pipe, cavity is provided with inside rotary drum, one end of rotary drum is provided with the centrifugation pump head connected with feed pipe, rotary drum is provided with the sub-material room connected with feed pipe near one end of centrifugation pump head, closed by end flanges one sub-material room, the other end of rotary drum is provided with storage compartment, closed by end flanges two storage compartment, retainer ring is arranged with coil pipe on the outside of rotary drum, coil pipe is connected near one end of sub-material room with sub-material room, one end near storage compartment connects with storage compartment, the edge of end flanges two is provided with the heavy liquid exit connected with storage compartment, the center of end flanges two is provided with the light liquid outlet connected with storage compartment.This weight liquid separation horizontal type coil pipe centrifuge realizes the mask work of weight liquid, improves light, heavy-fluid separative efficiency；During material is separated, reduce and separate link and energy ezpenditure, save separation equipment and manapower allocation.
Description
Technical field
The present invention relates to a kind of centrifuge, more specifically, it relates to a kind of weight liquid separation horizontal type coil pipe centrifuge.
Background technology
Centrifuge is to utilize centrifugal force, separates the machine of each component in mixture of the liquid with solid particle or liquid with liquid
Tool.Centrifuge is mainly used in separating the solid particle in suspension and liquid, or by two kinds of density differences in emulsion, and mutually
Immiscible liquid is separated（Cream is for example isolated from milk）；It can also be used for excluding the liquid in wet solid, for example, use
Washing machine dries wet clothes；Special hypervelocity channel separator also can be separated the admixture of gas of different densities；It is close using difference
The characteristics of sinking speed is different in a liquid, some sedimentation centrifuges can also be to solid particle by close for the solid particle of degree or granularity
Degree or granularity are classified.
Notification number discloses a kind of high throughput horizontal spiral centrifuge for the Chinese patent of CN204148005U, and it includes
Frame, it is characterised in that described frame one end is connected with main motor, main motor is connected with small end axle, small end by main pulley
Axle is connected with outer drum, and the outer drum other end is connected with big end axle, and the other end of frame is provided with stand-by motor, and stand-by motor passes through
Auxiliary belt pulley is connected with satellite differential, and satellite differential is connected with splined shaft, and splined shaft connects inside spin part,
Small end axle is also worn and is connected to feed arrangement.Although this high throughput horizontal spiral centrifuge can be solved existing for prior art
Treating capacity is small, and separating effect is poor, the technical problem of energy consumption grade higher, but treatment liquid and liquid mask work when
Wait, it is impossible to reach good effect.
The content of the invention
In view of the shortcomings of the prior art, it is centrifuged it is an object of the invention to provide a kind of weight liquid separation horizontal type coil pipe
Machine, the advantage is that realization weight, the separation of light liquid, improve light, heavy-fluid separative efficiency.
To achieve the above object, the invention provides following technical scheme：A kind of weight liquid separation horizontal type coil pipe centrifuge,
Including rotary drum, feed pipe, cavity is provided with inside the rotary drum, one end of the rotary drum is provided with the centrifugal pump connected with feed pipe
Head, the rotary drum is provided with the sub-material room connected with feed pipe near one end of centrifugation pump head, and the sub-material room passes through end flanges one
Closing, the other end of the rotary drum is provided with storage compartment, and the storage compartment is closed by end flanges two, and the end flanges two are provided with
The belt pulley of rotary drum high-speed rotation is driven, retainer ring is arranged with coil pipe on the outside of the rotary drum, the coil pipe is close to the one of sub-material room
End connects with sub-material room, and the one end near storage compartment connects with storage compartment, and the edge of the end flanges two is provided with and storage compartment
The heavy liquid exit of connection, the center of the end flanges two is provided with the light liquid outlet connected with storage compartment.
By using above-mentioned technical proposal, material to be separated is injected into sub-material room by pump from feed pipe, be centrifuged
The pressure that pump head is provided causes material from sub-material room the inside to disk in-pipe, and material is under the effect of the pressure along the spiral shell of coil pipe
Rotation direction moves, and material weight liquid during high-speed mobile can occur certain dividing under the influence of centrifugal force
From, rotation at a high speed is also carried out under the drive of belt pulley in rotary drum during carrying out feed separation, now moved in coil pipe
Material receive again rotary drum transmission come centrifugal force, the separating effect of weight liquid is further improve, by material in disk
Itself screw in pipe produces the centrifugal force that centrifugal force and rotary drum are provided, and double action improves the matter of weight liquid separation
Amount, light, the heavy-fluid for separating is entered into storage compartment, and heavy-fluid is discharged from heavy liquid exit, and light liquid is exported from light liquid and discharged.
The present invention is further arranged to：Described coil pipe is provided with reinforcement with the junction of rotary drum.
By using above-mentioned technical proposal, coil pipe surround and is fixedly connected on rotary drum, due to coil pipe and the contact surface of rotary drum
Product is limited, and reinforcement increased the connection area of coil pipe and rotary drum, advantageously ensure that stable connection between coil pipe and rotary drum.
The present invention is further arranged to：Described heavy liquid exit is provided with two.
By using above-mentioned technical proposal, two heavy liquid exits accelerate heavy-fluid and are emitted from storage compartment, are conducive to
Follow-up material realizes mask work.
The present invention is further arranged to：Liquid barrier is slidably connected at described heavy liquid exit, the liquid barrier is by pressure
Plate is fixed.
By using above-mentioned technical proposal, heavy-fluid during discharge, by adjusting liquid barrier at heavy liquid exit
Position, realizes that heavy liquid exit can adjust, and reduces the situation that light liquid is discharged from heavy liquid exit, while pressing plate carries out effectively liquid barrier
Fixation, reduce centrifuge and be moved the position of liquid barrier during work.
The present invention is further arranged to：The centripetal discharge pump for light liquid to be extracted out is provided with described storage compartment.
By using above-mentioned technical proposal, centripetal discharge pump extracts light liquid from storage compartment, improves the discharge of light liquid
Speed out.
The present invention is further arranged to：The entrance of described centripetal discharge pump is higher than heavy liquid exit.
By using above-mentioned technical proposal, can effectively ensure that centripetal discharge pump is extracting the process of light liquid, reduce heavy-fluid
Situation about extracting, is conducive to reducing light, heavy-fluid appearance mixing the situation separated.
The present invention is further arranged to：The side wall of described sub-material room is recessed towards with coil pipe connectivity part.
After entering into sub-material room from feed pipe by using above-mentioned technical proposal, material, in the effect of pressure and centrifugal force
Under enter into the inside of coil pipe, the side wall of sub-material room is recessed to coil pipe connectivity part, and the material for effectively reducing sub-material room is residual
Stay, improve the utilization rate of material.
In sum, the invention has the advantages that：
1st, by the effect of dual centrifugal force, weight, the mask work of light liquid are realized, is conducive to improving light, heavy-fluid separative efficiency；
2nd, during material is separated, reduce and separate link and energy ezpenditure, save separation equipment and manapower allocation.
Brief description of the drawings
Fig. 1 is the structural representation of weight liquid separation horizontal type coil pipe centrifuge；
Fig. 2 is the partial enlarged drawing of A in Fig. 1.
Reference：1st, rotary drum；11st, coil pipe；12nd, reinforcement；2nd, feed pipe；3rd, cavity；4th, sub-material room；41st, end flanges
One；5th, storage compartment；51st, end flanges two；511st, belt pulley；512nd, heavy liquid exit；513rd, light liquid outlet；52nd, centripetal discharge pump；6th, it is centrifuged
Pump head；7th, liquid barrier；8th, pressing plate.
Specific embodiment
The present invention is described in further detail below in conjunction with accompanying drawing.
Embodiment：A kind of weight liquid separation horizontal type coil pipe centrifuge, as shown in figure 1, can effectively solve and liquid
Mixture realizes separate work, including rotary drum 1, feed pipe 2, and cavity 3 is provided with the inside of rotary drum 1, and one end of rotary drum 1 is provided with
The centrifugation pump head 6 connected with feed pipe 2, rotary drum 1 is provided with the sub-material room 4 connected with feed pipe 2 near one end of centrifugation pump head 6,
Sub-material room 4 is closed by end flanges 1, and the other end of rotary drum 1 is provided with storage compartment 5, and storage compartment 5 is closed by end flanges 2 51,
Ensure that rotary drum 1 can realize rotation at a high speed in order to effective, the belt for driving the high-speed rotation of rotary drum 1 is provided with end flanges 2 51
Wheel 511, coil pipe 11 is arranged with the outside retainer ring of rotary drum 1, and coil pipe 11 is connected with sub-material room 4 near one end of sub-material room 4, leaned on
One end of nearly storage compartment 5 connects with storage compartment 5, and coil pipe 11 completes mask work in the helically formula distribution of the outside of rotary drum 1, material
It is pooled to afterwards in storage compartment 5, the heavy liquid exit 512 connected with storage compartment 5, end flanges is provided with the edge of end flanges 2 51
2 51 center is provided with the light liquid outlet 513 connected with storage compartment 5, and light, heavy-fluid is discharged from corresponding outlet, to continue thing
The mask work of material.
Specific work process：From charging aperture be transported in feed pipe 2 material to be separated by operator, is set at charging aperture
The high-pressure pump of promising material conveying, material under the effect of the pressure, is entered into sub-material room 4 by feed pipe 2, into sub-material room
4 material under the effect of the pressure, from sub-material room 4, into coil pipe 11 move by interior discharge, and charging aperture continues voltage supply and causes material edge
Coil pipe 11 the hand of spiral movement, material helically thread path move during, weight liquid meeting under the influence of centrifugal force
Occur separate situation, can be preliminary reach weight liquid separation effect, but separate effect it is undesirable；Material is in coil pipe
Rotary drum 1 can also occur high speed rotary motion under the drive of belt pulley 511 when being moved in 11, and the cavity 3 inside rotary drum 1 has
What is imitated reduces the own wt of rotary drum 1, while also reducing belt pulley 511 for rotary drum 1 rotates the torsion for providing, is conducive to skin
Belt wheel 511 drives rotary drum 1 to realize high-speed rotation, and the rotary drum 1 of the high-speed rotation coil pipe 11 during rotation can also occur therewith
Rotation, the centrifugal force that now rotary drum 1 is produced can be also applied on the material in coil pipe 11, the material for now being moved in coil pipe 11
The centrifugal force that the transmission of rotary drum 1 comes is received again, the separating effect of weight liquid is further improve, by material in coil pipe 11
Itself screw produce the centrifugal force that centrifugal force and rotary drum 1 provide, double action improves the quality of weight liquid separation.By
It is fastened around on rotary drum 1 in coil pipe 11, coil pipe 11 and rotary drum 1 are cylinder, both are when being fixedly connected
Contact area is limited, and the coil pipe 11 itself during high speed rotates of rotary drum 1 can also receive the effect of centrifugal force, and centrifuge is more
After secondary use it is possible that coil pipe 11 comes off from rotary drum 1 situation of separation, in order to it is effective ensure coil pipe 11 and rotary drum 1 it
Between stable connection, so be provided with reinforcement 12 in the junction of coil pipe 11 and rotary drum 1, by reinforcement 12 increased coil pipe 11 with
The connection area of rotary drum 1, advantageously ensures that stable connection between coil pipe 11 and rotary drum 1.
In interior light, the heavy-fluid for completing to separate of coil pipe 11 enters into storage compartment 5 under the effect of the pressure, in storage compartment 5
In light, heavy-fluid be in separate state under the influence of centrifugal force, heavy-fluid discharges from heavy liquid exit 512, and light liquid is from light
Liquid outlet 513 is discharged, and realizes separating light, the heavy-fluid discharge from storage compartment 5 for completing for convenience, and heavy liquid exit 512 is provided with
Two, two heavy liquid exits 512 accelerate heavy-fluid and are emitted from storage compartment 5, are conducive to follow-up material to realize separating work
Make.
During heavy-fluid is discharged, when different weight liquid mixtures are separated, the amount of heavy-fluid can be deposited centrifuge
In difference, when the amount of heavy-fluid is less, it is light that larger heavy liquid exit 512 may result in part when heavy-fluid is discharged
Liquid is also discharged from heavy liquid exit 512, so as to cause separate quality and efficiency reduction, in order to ensure the quality that light, heavy-fluid is separate,
Liquid barrier 7 is slidably connected at heavy liquid exit 512（As shown in Figure 2）, heavy-fluid during discharge, by adjusting liquid barrier
7 position at heavy liquid exit 512, realizes that heavy liquid exit 512 can adjust, and effectively avoids that heavy liquid exit 512 is larger to be caused
The situation that light liquid can also be discharged from heavy liquid exit 512, grasps ratio of the person according to weight liquid mixture, regulates liquid barrier 7
Position after, centrifugation liquid barrier 7 also can be subject to centrifugal forces during work, in order to ensure the position of liquid barrier 7
Stabilization is put, the position of liquid barrier 7 is fixed using pressing plate 8, be conducive to the position of centrifuge liquid barrier 7 during work
Put fixation.
When light liquid is discharged from inside to outside from storage compartment 5, the centripetal discharge pump for light liquid to be extracted out is provided with storage compartment 5
52, centripetal discharge pump 52 provides certain power for the extraction of light liquid, can quickly realize the row of extraction from centrifuge of light liquid
Put, improve the speed for emitting of light liquid.Centrifugal pump has certain suction during light liquid is extracted, light extracting
In order to effectively avoid also extracting heavy-fluid during liquid, light, heavy-fluid is caused to re-mix together, so will be centripetal
The entrance of pump 52 is higher than heavy liquid exit 512, can effectively ensure that centripetal discharge pump 52 is extracting the process of light liquid, reduces and takes out heavy-fluid
Situation about taking out, is conducive to reducing light, heavy-fluid appearance mixing the situation separated.
Material to be separated in sub-material room 4 is entered into, the pressure and rotary drum 1 that high-pressure pump is provided at charging aperture turn at a high speed
To being moved in coil pipe 11 in the presence of the centrifugal force of movable property life, centrifuge during feed separation is realized, meeting in sub-material room 4
There is a certain amount of material to remain, in order to reduce the residual quantity of material in sub-material room 4, so by the side wall of sub-material room 4 towards and disk
The connectivity part of pipe 11 is recessed, and material is moved in the presence of pressure and centrifugal force to the side wall of sub-material room 4, on the side wall of sub-material room 4
Mobile material, can postpone for being recessed moved in coil pipe 11, effectively reduces the material residual of sub-material room 4, improves thing
The utilization rate of material, reduces and separates link and energy ezpenditure, saves separation equipment and manapower allocation.
This specific embodiment is only explanation of the invention, and it is not limitation of the present invention, people in the art
Member can make the modification without creative contribution to the present embodiment as needed after this specification is read, but as long as at this
All protected by Patent Law in the right of invention.
Claims (7)
1. a kind of weight liquid separation horizontal type coil pipe centrifuge, including rotary drum（1）, feed pipe（2）, it is characterized in that：The rotary drum（1）
Inside is provided with cavity（3）, the rotary drum（1）One end be provided with the centrifugation pump head connected with feed pipe（6）, the rotary drum（1）Lean on
Nearly centrifugation pump head（6）One end be provided with and feed pipe（2）The sub-material room of connection（4）, the sub-material room（4）By end flanges one
（41）Closing, the rotary drum（1）The other end be provided with storage compartment（5）, the storage compartment（5）By end flanges two（51）Closing,
The end flanges two（51）It is provided with drive rotary drum（1）The belt pulley of high-speed rotation（511）, the rotary drum（1）Outside retainer ring
It is arranged with coil pipe（11）, the coil pipe（11）Near sub-material room（4）One end and sub-material room（4）Connection, near storage compartment（5）'s
One end and storage compartment（5）Connection, the end flanges two（51）Edge be provided with and storage compartment（5）The heavy liquid exit of connection
（512）, the end flanges two（51）Center be provided with and storage compartment（5）The light liquid outlet of connection（513）.
2. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 1, it is characterized in that：The coil pipe（11）With
Rotary drum（1）Junction be provided with reinforcement（12）.
3. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 2, it is characterized in that：The heavy liquid exit
（512）It is provided with two.
4. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 3, it is characterized in that：The heavy liquid exit
（512）Place slidably connects liquid barrier（7）, the liquid barrier（7）By pressing plate（8）It is fixed.
5. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 4, it is characterized in that：The storage compartment（5）
Inside it is provided with the centripetal discharge pump for light liquid to be extracted out（52）.
6. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 5, it is characterized in that：The centripetal discharge pump（52）
Entrance be higher than heavy liquid exit（512）.
7. a kind of weight liquid separation horizontal type coil pipe centrifuge according to claim 6, it is characterized in that：The sub-material room（4）
Side wall towards and coil pipe（11）Connectivity part is recessed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710078720.3A CN106824556A (en) | 2017-02-14 | 2017-02-14 | A kind of weight liquid separation horizontal type coil pipe centrifuge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710078720.3A CN106824556A (en) | 2017-02-14 | 2017-02-14 | A kind of weight liquid separation horizontal type coil pipe centrifuge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106824556A true CN106824556A (en) | 2017-06-13 |
Family
ID=59128056
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710078720.3A Pending CN106824556A (en) | 2017-02-14 | 2017-02-14 | A kind of weight liquid separation horizontal type coil pipe centrifuge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106824556A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114894935A (en) * | 2022-05-23 | 2022-08-12 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2730299A (en) * | 1953-11-27 | 1956-01-10 | Combined Metals Reduction Comp | Coiled tube continuous centrifuge |
| GB873494A (en) * | 1957-03-08 | 1961-07-26 | Selahaddin Rastgeldi | Method and means for centrifuging |
| US3706383A (en) * | 1970-05-21 | 1972-12-19 | James R Palma | Fluid separator |
| US4287061A (en) * | 1978-10-26 | 1981-09-01 | National Research Development Corporation | Rotating coil centrifuge |
| CN2664781Y (en) * | 2003-11-04 | 2004-12-22 | 靳清河 | Roller type nonuniform phase liquid-liquid centrifuge |
| CN101965218A (en) * | 2008-01-31 | 2011-02-02 | 索尔博水技术公司 | Be used to separate the method and apparatus and the application thereof of heterogeneous fluid |
| CN103055608A (en) * | 2012-12-22 | 2013-04-24 | 天津天雷科技有限公司 | Novel horizontal type gas-liquid separator |
| JP2014097484A (en) * | 2012-07-30 | 2014-05-29 | Matsumoto Kikai Seisakusho:Kk | Centrifuge |
| CN203695229U (en) * | 2014-02-26 | 2014-07-09 | 邢学进 | Horizontal three-phase combination centrifugal separator |
| CN105664536A (en) * | 2016-03-22 | 2016-06-15 | 沈阳化工大学 | Continuous separating device for heterogeneous-phase mixed liquid and method for applying continuous separating device |
| CN205761832U (en) * | 2016-05-24 | 2016-12-07 | 中石化石油工程技术服务有限公司 | A kind of centrifuge liquid level regulation apparatus |
| CN206519255U (en) * | 2017-02-14 | 2017-09-26 | 南京莫尼亚离心机科技发展有限公司 | A kind of weight liquid separation horizontal type coil pipe centrifuge |
-
2017
- 2017-02-14 CN CN201710078720.3A patent/CN106824556A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2730299A (en) * | 1953-11-27 | 1956-01-10 | Combined Metals Reduction Comp | Coiled tube continuous centrifuge |
| GB873494A (en) * | 1957-03-08 | 1961-07-26 | Selahaddin Rastgeldi | Method and means for centrifuging |
| US3706383A (en) * | 1970-05-21 | 1972-12-19 | James R Palma | Fluid separator |
| US4287061A (en) * | 1978-10-26 | 1981-09-01 | National Research Development Corporation | Rotating coil centrifuge |
| CN2664781Y (en) * | 2003-11-04 | 2004-12-22 | 靳清河 | Roller type nonuniform phase liquid-liquid centrifuge |
| CN101965218A (en) * | 2008-01-31 | 2011-02-02 | 索尔博水技术公司 | Be used to separate the method and apparatus and the application thereof of heterogeneous fluid |
| JP2014097484A (en) * | 2012-07-30 | 2014-05-29 | Matsumoto Kikai Seisakusho:Kk | Centrifuge |
| CN103055608A (en) * | 2012-12-22 | 2013-04-24 | 天津天雷科技有限公司 | Novel horizontal type gas-liquid separator |
| CN203695229U (en) * | 2014-02-26 | 2014-07-09 | 邢学进 | Horizontal three-phase combination centrifugal separator |
| CN105664536A (en) * | 2016-03-22 | 2016-06-15 | 沈阳化工大学 | Continuous separating device for heterogeneous-phase mixed liquid and method for applying continuous separating device |
| CN205761832U (en) * | 2016-05-24 | 2016-12-07 | 中石化石油工程技术服务有限公司 | A kind of centrifuge liquid level regulation apparatus |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114894935A (en) * | 2022-05-23 | 2022-08-12 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
| CN114894935B (en) * | 2022-05-23 | 2023-11-21 | 湖南省长康实业有限责任公司 | Sesame oil adulteration prevention rapid detection method and device |
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Application publication date: 20170613 |