CN209020595U - A kind of double export-oriented three-phase cyclone separators in top - Google Patents

A kind of double export-oriented three-phase cyclone separators in top Download PDF

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Publication number
CN209020595U
CN209020595U CN201821734932.9U CN201821734932U CN209020595U CN 209020595 U CN209020595 U CN 209020595U CN 201821734932 U CN201821734932 U CN 201821734932U CN 209020595 U CN209020595 U CN 209020595U
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China
Prior art keywords
phase
adapter tube
inner layer
mentioned
export
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Expired - Fee Related
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CN201821734932.9U
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Chinese (zh)
Inventor
刘雷
孟凡志
霍建伟
房佩文
张颢腾
王振波
巩志强
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China University of Petroleum East China
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China University of Petroleum East China
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Priority to CN201821734932.9U priority Critical patent/CN209020595U/en
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Expired - Fee Related legal-status Critical Current
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Abstract

The utility model relates to a kind of double export-oriented three-phase cyclone separators in top, which includes outer swirler, guide vane, inner layer cylinder, axial admission adapter tube, heavy out adapter tube, middle phase catch box, middle phase discharge connection, light phase export adapter tube.When work, charging enters the outer swirler of three-phase cyclone separator along axial feed inlet, centrifugal movement occurs under the action of guide vane, heavy phase liquid enters Taper Pipe, along heavy out adapter tube bleeder.Middle phase liquid and light phase liquid enter inner layer cylinder, and centrifugal movement occurs in inner layer cylinder, and light phase liquid is directly entered light phase export adapter tube and bleeder.Middle phase liquid flows up into middle phase catch box, along middle phase discharge connection bleeder.The apparatus structure is simple, equipment volume is small, separative efficiency is high, is of great significance for the development of multiphase flow splitting device.

Description

A kind of double export-oriented three-phase cyclone separators in top
Technical field
The utility model relates to a kind of double export-oriented three-phase cyclone separators in top, belong to multiphase flow separation field.
Background technique
In fields such as petroleum, chemical industry, there is a large amount of solid-liquid-gas and liquid-liquid-gas three phase separation processing, currently, Gravity type settling tank is mainly used for three phase separation processing.By prolonged application, it is found that gravity type precipitation apparatus has volume Greatly, the defects of structure is complicated and the processing time is long, work is discontinuous, has seriously affected the development of petrochemical industry.Eddy flow Separation belongs to a kind of multiphase flow isolation technics, it is under the influence of centrifugal force according to the density contrast between two-phase or multiphase come real It is separated between existing different phases.Cyclone separator due to the advantages that occupied area is small, liquid residence time is short, separative efficiency is high, The extensive concern of petrochemical industry is obtained.Since China is relatively slower in terms of the development of three-phase cyclone separator, device Structure type is relatively simple, and aggregate level is well below technology leading in the world, therefore, develops three-phase with independent intellectual property rights Cyclone separator has great importance.
Utility model content
In order to solve the above technical problems, the utility model provides a kind of double export-oriented three-phase cyclone separators in top, it can To be used for gas, liquid, solid three phase separation or Oil, Water, Gas three phase separation, which has separative efficiency height, equipment The advantages that small in size, compact-sized, easy to use.
In order to achieve the above objectives, the technical solution of the utility model is as follows: a kind of double export-oriented three-phase cyclone separation in top Device include outer swirler, guide vane, inner layer cylinder, axial admission adapter tube, heavy out adapter tube, middle phase catch box, middle phase outlet connect Pipe, light phase export adapter tube.Above-mentioned inner layer cylinder is mounted on the bottom surface of phase catch box among the above;Above-mentioned light phase export adapter tube peace turns Phase liquid collecting upper box part among the above, and it is deep into the inside of above-mentioned inner layer cylinder;Above-mentioned outer swirler and above-mentioned inner layer cylinder, on It states middle phase catch box and keeps centering;Above-mentioned guide vane is mounted on the lower part of above-mentioned inner layer cylinder, and together with above-mentioned inner layer cylinder It is mounted on the inside of above-mentioned outer swirler;Vertical pacify of above-mentioned axial admission adapter tube turns axially to open in the direct tube section of above-mentioned outer swirler At hole.
Further, above-mentioned outer swirler is cylindrical section, the combination for boring section and direct tube section, cylindrical section and cone section, cone section and straight Cylinder section is transition connection, reduces the resistance that fluid is subject to during moving downward, the cylindrical section side of above-mentioned outer swirler Face is equipped with axial aperture, and aperture welds together with above-mentioned axial admission pipe, guarantees the inflow of mixing liquid;
Further, among the above phase catch box be it is columnar structured, be equipped at the center of phase liquid collecting upper box part end socket among the above Circular hole is used to take over connection with above-mentioned light phase export, is equipped with circular hole at the center of the bottom head of phase catch box among the above, is used to It is connect with above-mentioned inner layer cylinder, the side of phase catch box is equipped with aperture among the above, is used to connect with phase outlet among the above.
The working principle of the utility model is: feeding when work and entering the outer of three-phase cyclone separator along axial feed inlet Centrifugal movement occurs under the action of guide vane for cyclone, and heavy phase liquid enters Taper Pipe, along heavy out adapter tube bleeder.In Phase liquid and light phase liquid enter inner layer cylinder, and centrifugal movement occurs in inner layer cylinder, and light phase liquid is directly entered light phase Discharge connection and bleeder.Middle phase liquid flows up into middle phase catch box, along middle phase discharge connection bleeder.
Compared with prior art, the utility model has the beneficial effect that
The utility model provides a kind of double export-oriented three-phase cyclone separators in top, only for existing hydrocyclone Two-phase substance can be separated, the present apparatus can be used for separating gas, liquid, solid three phase separation or Oil, Water, Gas three phase separation, three-phase rotation Stream separator has many advantages, such as that separative efficiency is high, equipment volume is small, compact-sized, easy to use.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will to example or Attached drawing needed to be used in the description of the prior art is briefly described.
Fig. 1 is a kind of overall structure diagram of the double export-oriented three-phase cyclone separators in top of the utility model.
1, heavy out adapter tube 2, outer swirler 3, guide vane
4, inner layer cylinder 5, axial admission adapter tube 6, middle phase catch box
7, light phase export adapter tube 8, middle phase discharge connection
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model Clearly and completely describe.As shown in Figure 1, the utility model provides a kind of double export-oriented three-phase cyclone separators in top, the device Go out including outer swirler 2, guide vane 3, inner layer cylinder 4, axial admission adapter tube 5, heavy out adapter tube 1, middle phase catch box 6, middle phase Mouth adapter tube 8, light phase export adapter tube 7.Above-mentioned inner layer cylinder 4 is mounted on the bottom surface of phase catch box 6 among the above;Above-mentioned light phase export connects The peace of pipe 7 turns on 6 top of phase catch box among the above, and is deep into the inside of above-mentioned inner layer cylinder 4;Above-mentioned outer swirler 2 with it is upper State inner layer cylinder 4, the among the above holding of phase catch box 6 centering;Above-mentioned guide vane 3 is mounted on the lower part of above-mentioned inner layer cylinder 4, and with it is upper State the inside that inner layer cylinder 4 is installed along with above-mentioned outer swirler 2;Vertically peace turns in above-mentioned outward turning above-mentioned axial admission adapter tube 5 At the direct tube section axial aperture for flowing device 2.
Outer swirler 2 is cylindrical section, the combination for boring section and direct tube section, and cylindrical section and cone section, cone section and direct tube section were Cross connection;The cylindrical section side of outer swirler 2 is equipped with axial aperture, and aperture welds together with axial admission pipe 5, guarantees mixing The inflow of liquid;
Middle phase catch box 6 be it is columnar structured, at the center of middle 6 top end socket of phase catch box, at the center of bottom head And side is equipped with aperture, guarantees the connection of adapter tube and the outflow of liquid.
The working principle of the utility model is: the working principle of the utility model is: charging connects along axial admission when working Pipe 5 enters the outer swirler 3 of three-phase cyclone separator, centrifugal movement occurs under the action of guide vane 3, heavy phase liquid enters cone Pipe, along heavy out adapter tube bleeder.Middle phase liquid and light phase liquid enter inner layer cylinder 4, and occur in inner layer cylinder 4 Centrifugal movement, light phase liquid enter light phase export adapter tube 7 and bleeder.Middle phase liquid flows up into middle phase catch box 6, edge Middle 8 bleeder of phase outlet.
A kind of double export-oriented three-phase cyclone separators in top provided by the utility model, mixed liquor pass through in different cylinders Centrifugal movement is inside done, to complete the separation of three-phase fluid, device design is reasonable, easy to use.To the disclosed embodiments Above description, can be realized all personnel or using the utility model.Various modifications to these embodiments are to owner It will be apparent for member, the general principles defined herein can be in the spirit or scope for not departing from the utility model In the case where, it realizes in other embodiments.Therefore, the utility model is not intended to be limited to these implementations shown in this article Example, and it is to fit to the widest scope consistent with the principles and novel features disclosed herein.

Claims (3)

1. a kind of double export-oriented three-phase cyclone separators in top, including outer swirler, guide vane, inner layer cylinder, axial admission adapter tube, Heavy out adapter tube, middle phase catch box, middle phase discharge connection, light phase export adapter tube;It is characterized by: above-mentioned inner layer cylinder installation In the bottom surface of phase catch box among the above;Above-mentioned light phase export adapter tube peace turns in phase liquid collecting upper box part among the above, and is deep into State the inside of inner layer cylinder;Above-mentioned outer swirler with above-mentioned inner layer cylinder, among the above phase catch box keep centering;Above-mentioned guide vane peace Mounted in the lower part of above-mentioned inner layer cylinder, and it is installed along with above-mentioned inner layer cylinder the inside of above-mentioned outer swirler;Above-mentioned axial direction Charging adapter tube is vertically mounted at the direct tube section axial aperture of above-mentioned outer swirler.
2. a kind of double export-oriented three-phase cyclone separators in top according to claim 1, it is characterised in that: outer swirler is Cylindrical section, the combination for boring section and direct tube section, cylindrical section and cone section, cone section are that transition connects with direct tube section;The circle of outer swirler Cylinder section side is equipped with axial aperture.
3. a kind of double export-oriented three-phase cyclone separators in top according to claim 1, it is characterised in that: middle phase catch box To be columnar structured, at the center of middle phase liquid collecting upper box part end socket, it is equipped with aperture at the center of bottom head, is mutually exported in connection Adapter tube, the side of middle phase catch box are equipped with aperture, connection light phase export adapter tube.
CN201821734932.9U 2018-10-25 2018-10-25 A kind of double export-oriented three-phase cyclone separators in top Expired - Fee Related CN209020595U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821734932.9U CN209020595U (en) 2018-10-25 2018-10-25 A kind of double export-oriented three-phase cyclone separators in top

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821734932.9U CN209020595U (en) 2018-10-25 2018-10-25 A kind of double export-oriented three-phase cyclone separators in top

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CN209020595U true CN209020595U (en) 2019-06-25

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111035995A (en) * 2019-12-26 2020-04-21 中国石油大学(华东) Gas-liquid-solid three-phase separator of slurry bed reactor
CN112047602A (en) * 2020-09-30 2020-12-08 中国石油天然气股份有限公司 Oily sludge cyclone sedimentation separation device
CN113333185A (en) * 2021-06-01 2021-09-03 中国石油大学(华东) Three-phase cyclone separator with flow guide cone at center

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111035995A (en) * 2019-12-26 2020-04-21 中国石油大学(华东) Gas-liquid-solid three-phase separator of slurry bed reactor
CN111035995B (en) * 2019-12-26 2021-07-23 中国石油大学(华东) Gas-liquid-solid three-phase separator of slurry bed reactor
CN112047602A (en) * 2020-09-30 2020-12-08 中国石油天然气股份有限公司 Oily sludge cyclone sedimentation separation device
CN113333185A (en) * 2021-06-01 2021-09-03 中国石油大学(华东) Three-phase cyclone separator with flow guide cone at center
CN113333185B (en) * 2021-06-01 2022-03-04 中国石油大学(华东) Three-phase cyclone separator with flow guide cone at center

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190625

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CF01 Termination of patent right due to non-payment of annual fee