CN201572543U - Vertical phase separator - Google Patents
Vertical phase separator Download PDFInfo
- Publication number
- CN201572543U CN201572543U CN 200920209550 CN200920209550U CN201572543U CN 201572543 U CN201572543 U CN 201572543U CN 200920209550 CN200920209550 CN 200920209550 CN 200920209550 U CN200920209550 U CN 200920209550U CN 201572543 U CN201572543 U CN 201572543U
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- China
- Prior art keywords
- knockout drum
- guide shell
- separation
- fluid container
- phase
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Abstract
The utility model relates to a vertical phase separator, which comprises a stock solution tank, a separating tank, a pressure-resisting sleeve-type fiber bed and a guide cylinder. The stock solution tank is in sealing connection with the separating tank. The pressure-resisting sleeve-type fiber bed which can carry out multi-phase separation and the guide cylinder are arranged in the separation tank. Mixed solution is discharged from a discharge port of the guide cylinder. The discharge port is positioned on the lateral surface of the guide cylinder. The top (bottom) part of the separation tank is provided with a separation light (heavy) phase region with a light (heavy) phase outlet. The lateral surface of the guide cylinder is a heave (light) phase region and is provided with a heavy (light) phase outlet. Microcosmic fibers on the pressure-resisting sleeve-type fiber bed of the utility model have coacervation action, coacervate dispersed phase droplets into big drops, quicken sedimentation velocity, improve separating efficiency and make content of the dispersed phases in a main phase achieve physical separation limit (solubility) thereof, even micrometers of droplets and mediums with high viscosity. As long as two mediums are not dissolved mutually and have density difference, the two mediums can be separated. The separating efficiency relates to physical properties of the mediums and the maximum separating efficiency can reach dozens of parts per million to a plurality of parts per million.
Description
Technical field
The utility model relates to a kind of separator that is applied in oil or the petrochemical industry, and specifically a kind of fast and high quality is separated the phase separator of two kinds of immiscible media.
Background technology
Liquid-liquid separation method commonly used on the current industrial mainly contains three kinds:
A kind of is that the device that is called centrifugal extractor separates immiscible liquid.The speed rotation that the rotary drum of centrifugal extractor changes with per minute 2000--5000 around a sleeve shaft, and make rotary drum around self axis hypervelocity rotation.Form powerful centrifugal force field.Material is injected by the bottom inlet, and centrifugal force forces feed liquid upwards to flow along drum inner wall, and because of the density contrast layering of feed liquid different component.The liquid phase that density is big forms outer shroud, and the liquid phase that density is light forms interior ring, flow to rotary drum top leakage fluid dram separately and discharges.The major defect of this kind method is energy consumption and fault rate height, is difficult for realizing continuous large-scale production.
Second kind is Inclined Plate Gravity Settler, adopts 45 ° of swash plates usually.It with shallow pool principle and coalescence principle in conjunction with and design.Because the adding of swash plate shortens the droplet settling time, thereby improve separative efficiency.The liquid-liquid diphasic flow of bottom horizontal flow sheet arrives swash plate at last and begins wetting swash plate because of buoyancy begins to rise by light phase drop behind the swash plate, forms big drop, and interacts with swash plate, forms the tunic that flows at last.Dispersed phase drop interacts with the tunic that flows along swash plate and is flocked at last on the tunic that flows, and finishes agglomeration process, is discharged by the Inclined Plate Gravity Settler light phase export at last.Continuous phase sedimentation under the gravity effect is flowed out by the swash plate bottom, realizes that at last two are separated.The major defect of this kind method is that contour size of the unit(s) is big, and separating effect is not good enough.
The third is a membrane separation technique, and it is a separation technology that emerges rapidly that film separates.Though membrane separation technique has obtained huge progress, it still is in the waxing development stage after all, also has certain limitation for the media processes of seriously corroded in the chemical industry.
The utility model content
Technical problem to be solved in the utility model is: at prior art and the existing defective of equipment and a kind of vertical phase separator is provided, solve the energy consumption and the fault rate height of prior art, be difficult for to realize that continuous large-scale production, contour size of the unit(s) are big, separating effect is not good enough, the problem of seriously corroded and insufficient space.
The technical scheme that its technical problem that solves the utility model adopts is:
A kind of vertical phase separator, it is characterized in that: comprise original fluid container, knockout drum, withstand voltage telescopic fibre bed and guide shell, described original fluid container and knockout drum are tightly connected and described original fluid container is positioned at the bottom of described knockout drum, withstand voltage telescopic fibre bed that can heterogeneous separation and guide shell is arranged in the knockout drum and described guide shell is positioned at the top of described withstand voltage telescopic fibre bed, be provided with the guide shell leakage fluid dram in the side of described guide shell, mixed liquor flows out from the guide shell leakage fluid dram; The top of described knockout drum is provided with offers the light phase region of the separation that has light phase export, and then for separating the heavy phase district, this separation heavy phase district offers heavy out to described guide shell lateral space.
A kind of vertical phase separator, it is characterized in that: comprise original fluid container, knockout drum, withstand voltage telescopic fibre bed and guide shell, described original fluid container and knockout drum are tightly connected and described original fluid container is positioned at the top of described knockout drum, withstand voltage telescopic fibre bed that can heterogeneous separation and guide shell is arranged in the knockout drum and described guide shell is positioned at the bottom of described withstand voltage telescopic fibre bed, be provided with the guide shell leakage fluid dram in the side of described guide shell, mixed liquor flows out from the guide shell leakage fluid dram; The top of described knockout drum is provided with offers the separation heavy phase district that has heavy out, and then for separating light phase region, this separates light phase region and offers light phase export described guide shell lateral space.
Also be connected with differential pressure transmitter between described original fluid container and the knockout drum.
Offer import on the described original fluid container, the separation heavy phase district of described knockout drum offers visor with the correspondence position that separates light phase region.
All offer evacuation port on described original fluid container and the knockout drum.
The separation heavy phase district of described guide shell lateral space or separate on the light phase region flange port is set, first liquid level gauge is set in this flange port, in this first liquid level gauge, be provided with the thermometer in the guide shell lateral space of inserting knockout drum, the separation heavy phase district of the light phase region of separation at described knockout drum top or knockout drum bottom offers standby mouthful, in described standby mouthful second liquid level gauge is set.
Described knockout drum side is provided with the support that is used for fixing or/and the hanger that is used to install.
The beneficial effects of the utility model are: the microscopic fibers on the withstand voltage telescopic fibre bed has cohesion, and their absorption is reached maximum meltage by decentralized photo, even have only drop and the full-bodied medium of a few μ m.Separative efficiency and flow velocity are to be determined by following parameters: medium rerum natura, fibre bed volume, fibre diameter and porosity etc.As long as two media is immiscible, and density contrast can separate greater than 2%, and separative efficiency is relevant with the rerum natura of medium, reaches as high as tens of several ppM of arriving.A kind of phase separator of the present utility model almost energy free consumption in realizing liquid liquid separation process efficiently, it is mainly used in the petrochemical production process needed heterogeneous separation and comprises between immiscible liquid and liquids and gases etc., and the sewage disposal of vast petroleum and petrochemical industry and chemical enterprise, as oil field extracted water, Refinery Coking water, acid water, chemical enterprise contains organic wastewater treatment etc.The vertical placement of the utility model, the strong phase separator of shared plane space is little, is specially adapted to the situation that old top order is transformed the time space deficiency.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is further specified.
Fig. 1 is the structural representation that a kind of heavy phase of the present utility model is removed light mutually vertical strong phase separator.
Fig. 2 is the structural representation of a kind of vertical strong phase separator of heavy phase that gently is divided by of the present utility model.
Wherein: 1, import; 2, original fluid container; 3, evacuation port; 4, bolt; 5, flange port; 6, flange port; 7, differential pressure transmitter; 8, flange port; 9, knockout drum; 10, withstand voltage telescopic fibre bed; 11, support; 12, guide shell; 13, separate the heavy phase district, 13a, separate light phase region; 14, visor; 15, guide shell leakage fluid dram; 16, hanger; 17, visor; 18, separate light phase region, 18a, separation heavy phase district; 19, light phase export, 19a, heavy out; 20, evacuation port; 21, second liquid level gauge; 22, standby mouthful; 23, the highest liquid level; 24, standard liquid level; 25, minimum liquid level; 26, heavy out, 26a, light phase export; 27, thermometer, 27a, first liquid level gauge.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete example, further set forth the utility model.
Referring to Fig. 1, a kind of heavy phase shown in Figure 1 is removed gently mutually vertical phase separator, comprise original fluid container 2, knockout drum 9, withstand voltage telescopic fibre bed 10 and guide shell 12, be tightly connected by bolt 4 between original fluid container 2 and the knockout drum 9 and original fluid container 2 is positioned at the bottom of knockout drum 9, original fluid container 2 is provided with import 1, evacuation port 3 and flange port 5, and evacuation port 3 is provided with the thermometer 27 that inserts in original fluid container 2 inner chambers.The hanger 16 that knockout drum 9 is provided with flange port 6, form 14, the support 11 that is used for fixing and is used to install also is connected with differential pressure transmitter 7 between the flange port 5 of original fluid container 2 and the flange port 6 of knockout drum 9.Withstand voltage telescopic fibre bed 10 and guide shell 12 that can heterogeneous separation be arranged in the knockout drum 9, guide shell 12 is positioned at the top of withstand voltage telescopic fibre bed 10, be provided with guide shell leakage fluid dram 15 in the side of guide shell 12, mixed liquor flows out from guide shell leakage fluid dram 15, be provided with the light phase region 18 of separation at knockout drum 9 tops, also be connected between the tank body that separates light phase region 18 and the knockout drum 9 by bolt 4, on the tank body that separates light phase region 18, offer and have light phase export 19, evacuation port 20, standby mouthful 22 and form 17, in standby mouthful 22, second liquid level gauge 21 is set, guide shell 12 lateral space are for separating heavy phase district 13, on the tank body that separates heavy phase district 13, offer heavy out 26 and flange port 8, at flange port 8 the first liquid level gauge 27a is set, in this first liquid level gauge 27a, is provided with the thermometer 27 in the guide shell lateral space of inserting knockout drum 9.
By form 17, can observe the highest liquid level 23, standard liquid level 24, the minimum liquid level 25 that separate light phase region 18.
Referring to Fig. 2, a kind of vertical phase separator of heavy phase that gently is divided by shown in Figure 2, comprise original fluid container 2, knockout drum 9, withstand voltage telescopic fibre bed 10 and guide shell 12, be tightly connected by bolt 4 between original fluid container 2 and the knockout drum 9 and original fluid container 2 is positioned at the top of knockout drum 9, original fluid container 2 is provided with import 1, evacuation port 3 and flange port 5, and evacuation port 3 is provided with the thermometer 27 that inserts in original fluid container 2 inner chambers.The hanger 16 that knockout drum 9 is provided with flange port 6, form 14, the support 11 that is used for fixing and is used to install also is connected with differential pressure transmitter 7 between the flange port 5 of original fluid container 2 and the flange port 6 of knockout drum 9.Withstand voltage telescopic fibre bed 10 and guide shell 12 that can heterogeneous separation be arranged in the knockout drum 9, guide shell 12 is positioned at the bottom of withstand voltage telescopic fibre bed 10, be provided with guide shell leakage fluid dram 15 in the side of guide shell 12, mixed liquor flows out from guide shell leakage fluid dram 15, be provided with separation heavy phase district 18a in knockout drum 9 bottoms, also be connected between the tank body that separates heavy phase district 18a and the knockout drum 9 by bolt 4, on the tank body that separates heavy phase district 18a, offer and have heavy out 19a, evacuation port 20, standby mouthful 22 and form 17, in standby mouthful 22, second liquid level gauge 21 is set, guide shell 12 lateral space are for separating light phase region 13a, on the tank body that separates light phase region 13a, offer light phase export 26a and flange port 8, at flange port 8 the first liquid level gauge 27a is set, in this first liquid level gauge 27a, is provided with the thermometer 27 in the guide shell lateral space of inserting knockout drum 9.
Phase separator of the present utility model is easily stopped up by solid particle in view of its withstand voltage telescopic fibre bed 10, as containing particle in the material, must add filter before the import 1 of original fluid container 2.
The tank shell of phase separator is made according to the GB150-1998 pressure vessel; The tube sheet connecting bolt of internals and after-poppet material are engineering plastics such as stainless steel or fluoropolymer material, and withstand voltage telescopic fibre bed 10 material categorys comprise fluoropolymer polymer, glass fibre, stainless steel etc.
Claims (12)
1. vertical phase separator, it is characterized in that: comprise original fluid container, knockout drum, withstand voltage telescopic fibre bed and guide shell, described original fluid container and knockout drum are tightly connected and described original fluid container is positioned at the bottom of described knockout drum, withstand voltage telescopic fibre bed that can heterogeneous separation and guide shell is arranged in the knockout drum and described guide shell is positioned at the top of described withstand voltage telescopic fibre bed, be provided with the guide shell leakage fluid dram in the side of described guide shell, mixed liquor flows out from the guide shell leakage fluid dram; The top of described knockout drum is provided with offers the light phase region of the separation that has light phase export, and then for separating the heavy phase district, this separation heavy phase district offers heavy out to described guide shell lateral space.
2. vertical phase separator as claimed in claim 1 is characterized in that: also be connected with differential pressure transmitter between described original fluid container and the knockout drum.
3. vertical phase separator as claimed in claim 1 is characterized in that: offer import on the described original fluid container, the separation heavy phase district of described knockout drum offers visor with the correspondence position that separates light phase region.
4. vertical phase separator as claimed in claim 1 is characterized in that: all offer evacuation port on described original fluid container and the knockout drum.
5. vertical phase separator as claimed in claim 1, it is characterized in that: offer flange port in the separation heavy phase district of described guide shell lateral space, first liquid level gauge is set in this flange port, in this first liquid level gauge, be provided with the thermometer in the guide shell lateral space of inserting knockout drum, the light phase region of separation at described knockout drum top offers standby mouthful, in described standby mouthful second liquid level gauge is set.
6. vertical phase separator as claimed in claim 1 is characterized in that: described knockout drum side is provided with the support that is used for fixing or/and the hanger that is used to install.
7. vertical phase separator, it is characterized in that: comprise original fluid container, knockout drum, withstand voltage telescopic fibre bed and guide shell, described original fluid container and knockout drum are tightly connected and described original fluid container is positioned at the top of described knockout drum, withstand voltage telescopic fibre bed that can heterogeneous separation and guide shell is arranged in the knockout drum and described guide shell is positioned at the bottom of described withstand voltage telescopic fibre bed, be provided with the guide shell leakage fluid dram in the side of described guide shell, mixed liquor flows out from the guide shell leakage fluid dram; The top of described knockout drum is provided with offers the separation heavy phase district that has heavy out, and then for separating light phase region, this separates light phase region and offers light phase export described guide shell lateral space.
8. vertical phase separator as claimed in claim 7 is characterized in that: also be connected with differential pressure transmitter between described original fluid container and the knockout drum.
9. vertical phase separator as claimed in claim 7 is characterized in that: offer import on the described original fluid container, the separation heavy phase district of described knockout drum offers visor with the correspondence position that separates light phase region.
10. vertical phase separator as claimed in claim 7 is characterized in that: all offer evacuation port on described original fluid container and the knockout drum.
11. vertical phase separator as claimed in claim 1, it is characterized in that: offer flange port on the light phase region of the separation of described guide shell lateral space, first liquid level gauge is set in this flange port, in this first liquid level gauge, be provided with the thermometer in the guide shell lateral space of inserting knockout drum, the separation heavy phase district at described knockout drum top offers standby mouthful, in described standby mouthful second liquid level gauge is set.
12. vertical phase separator as claimed in claim 7 is characterized in that: described knockout drum side is provided with the support that is used for fixing or/and the hanger that is used to install.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200920209550 CN201572543U (en) | 2009-09-11 | 2009-09-11 | Vertical phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200920209550 CN201572543U (en) | 2009-09-11 | 2009-09-11 | Vertical phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201572543U true CN201572543U (en) | 2010-09-08 |
Family
ID=42692422
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200920209550 Expired - Lifetime CN201572543U (en) | 2009-09-11 | 2009-09-11 | Vertical phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201572543U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114367246A (en) * | 2022-01-13 | 2022-04-19 | 沈齐晖 | Continuous melting and multi-phase separation system |
-
2009
- 2009-09-11 CN CN 200920209550 patent/CN201572543U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114367246A (en) * | 2022-01-13 | 2022-04-19 | 沈齐晖 | Continuous melting and multi-phase separation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 201201 Shanghai, Pudong New Area Jin Tang Road, No. 2, block B, 145 Patentee after: SHANGHAI ANHORN ENVIRONMENTAL TECHNOLOGY CO., LTD. Address before: 201201 Shanghai, Pudong New Area Jin Tang Road, No. 2, block B, 145 Patentee before: Shanghai Anhorn Mechanical Equipment Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20100908 |
|
| CX01 | Expiry of patent term |