CN204073512U - A kind of experimental rig solution-air-liquid three phase separator - Google Patents
A kind of experimental rig solution-air-liquid three phase separator Download PDFInfo
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- CN204073512U CN204073512U CN201420465076.7U CN201420465076U CN204073512U CN 204073512 U CN204073512 U CN 204073512U CN 201420465076 U CN201420465076 U CN 201420465076U CN 204073512 U CN204073512 U CN 204073512U
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Abstract
The utility model provides a kind of experimental rig solution-air-liquid three phase separator, and it comprises: gas-liquid separation assembly, the liquid be connected with this gas-liquid separation assembly-liquid separation assembly, and temperature regulating device; Described gas-liquid separation assembly comprises: the cohesion of gas-liquid separation cylindrical shell, charging aperture, gas export mouth, drop net, charging baffle plate and supporting guide plate; Described liquid-liquid separation assembly comprises: sedimentation separation pipe, light liquid collecting pipe, heavy-fluid export mouth, light liquid export mouth and light liquid overflow launder; Described temperature regulating device comprises: the gas-liquid separation temperature regulating device connected by pipeline successively, liquid-liquid is separated temperature regulating device and refrigerating/heating liquid circulator.The utility model is specially adapted to middle-size and small-size experimental rig, and the situation that in gas-liquid mixed material to be separated, amount of liquid is less, stable Liquid level and continuous blow-down can be carried out to the gas after separation and liquid material, realize the three phase separation of accurate gas-heavy-fluid-light liquid.
Description
Technical field
The utility model relates to a kind of solution-air-liquid three phase separator, specifically refers to a kind of solution-air-liquid three phase separator being applied to middle-size and small-size exerciser, belongs to solution-air-liquid three phase separation technical field.
Background technology
Solution-air-liquid three phase separator, in the technological development and industrial production of the various technical processes in the fields such as crude oil production, petroleum refining, petrochemical industry, environmental protection, has and applies very widely.Solution-air-liquid three phase separator structurally all be unable to do without gas-liquid separation part and liquid collecting discharge portion, its general principle is: described liquid collecting discharge portion generally becomes heavy liquid collecting chamber and light liquids collecting chamber by barrier partitions, the mouth of pipe connecting fluid level controlling system of each room.After material enters the gas-liquid separation part of three phase separator, first gas-liquid separation is carried out, density based on stream components is different, and material enters the pressure vessel of a volume sudden enlargement from pipeline, and the flow velocity of logistics reduces, carry out full flashing separation, the flow direction of stream components changes, and under the effect of density contrast, gas group branch upwards flows, from the top exit pipeline of separator, discharged by the pressure control loop be arranged on pipeline.And the fine droplet carried in liquid component flows downward, enter liquid collecting discharge portion, liquid-liquid sedimentation separation is carried out in the effect of the density contrast between recycling liquid component, the heavy liquid that density is larger is settled down to the bottom of heavy liquid collecting chamber, it it is the light liquids that density is less, by baffle plate overflow to light liquids collecting chamber, by detecting the liquid level of heavy/light liquids interfacial level and light liquids, control the aperture of discharge fluid level control valve, realize not dissolving each other gently, liquid between heavy-fluid-liquid is separated, thus reach and be continuously separated, the object that liquid level stabilizing controls.
Gas-liquid separation is always wished to be separated with liquid by gas as much as possible, but because the relation of vapor liquid equilibrium, the separative efficiency of separator can not reach 100%.By actual conditions, according to character, the separation requirement of material to be separated, need select or design gas-liquid separator.And the multi-form separation methods such as current used gravity settling separation, baffling separation, cyclonic separation, filler separation, silk screen separation, micro porous filtration separation, each variant on separating effect.Along with the development of modern petrochemical technology, the solution-air-liquid three phase separation of industrial different operating mode all can find suitable solution.
But carry out catalyst development in laboratory, explore in the research process such as new process route, the medium and small experimental rig used and micro-test device, material treating capacity is little.Realize three-phase to be continuously separated, if continue to use the structural design of industrial three phase separator, because the volume of separator is large, be difficult to set up, also cannot realize continuous pulp discharge and the stability contorting to liquid level sensitivity.Therefore, three phase separator is often made gas-liquid separation collector by experimental rig, in process of the test, all liquid phase materials are collected in the separator, by the manual discharge of interval, manual discharge all can upset the quiet run of reaction system each time, cannot be difficult to realize the smooth operation under technological parameter stable condition.In addition, numerous and diverse manual operation, had both added the labour intensity of operating personnel, and also add the uncertainty of man's activity experimental result, the GRR of experimental result is poor, is difficult to obtain representational experimental result simultaneously.
Utility model content
The purpose of this utility model is to provide a kind of experimental rig solution-air-liquid three phase separator, be specially adapted to middle-size and small-size experimental rig, and the situation that in gas-liquid mixed material to be separated, amount of liquid is less, stable Liquid level and continuous blow-down can be carried out to the gas after separation and liquid material, realize the three phase separation of accurate gas-heavy-fluid-light liquid.
For achieving the above object, the utility model provides a kind of experimental rig solution-air-liquid three phase separator, and it comprises: gas-liquid separation assembly, the liquid be connected with this gas-liquid separation assembly-liquid separation assembly, and temperature regulating device; Described gas-liquid separation assembly comprises: gas-liquid separation cylindrical shell, is necking down end socket bottom it; Charging aperture, it is opened in the sidepiece of described gas-liquid separation cylindrical shell; Gas export mouth, it is opened in the top of described gas-liquid separation cylindrical shell; Drop cohesion net, it is arranged on the inner upper of described gas-liquid separation cylindrical shell; Charging baffle plate, it is fixed on the inwall of the close charging aperture of described gas-liquid separation cylindrical shell by supporting guide plate; Described liquid-liquid separation assembly comprises: sedimentation separation pipe, and it is welded on the bottom necking down end socket of described gas-liquid separation cylindrical shell; Light liquid collecting pipe, it is arranged on the inside of described sedimentation separation pipe, and its outer wall is near the side inwall of sedimentation separation pipe; Heavy-fluid export mouth, it is arranged on bottom the side of described sedimentation separation pipe; Light liquid export mouth, it is arranged on the bottom of described light liquid collecting pipe; Light liquid overflow launder, it is arranged on the center of the inner tip of described light liquid collecting pipe; Described temperature regulating device comprises: the gas-liquid separation temperature regulating device connected by pipeline successively, liquid-liquid is separated temperature regulating device and refrigerating/heating liquid circulator; Described gas-liquid separation temperature regulating device is arranged on the outside of gas-liquid separation cylindrical shell; Described liquid-liquid is separated the outside that temperature regulating device is arranged on sedimentation separation pipe.
Described charging baffle plate is curved baffle; Described supporting guide plate is fan-shaped deflector, it is obliquely installed, the fan-shaped arc tips of this supporting guide plate and the lower edge of described charging baffle plate are by being welded to connect, and the fan-shaped summit of this supporting guide plate is welded on the inwall of the close charging aperture of described gas-liquid separation cylindrical shell.
The rational height on the upper edge of described charging baffle plate is higher than charging aperture; Gap between the arc both sides of the edge of this charging baffle plate and the inwall of gas-liquid separation cylindrical shell is not less than the diameter of charging aperture.
The bottom of described sedimentation separation pipe is flat-plate closure, and this flat-plate closure offers the through hole consistent with the diameter of light liquid collecting pipe, and the bottom of this light liquid collecting pipe through described through hole, and is fixedly connected by welding with sedimentation separation pipe.
The top edge of described light liquid overflow launder flushes with the top edge of light liquid collecting pipe, and the interior area of section of this light liquid overflow launder should be less than the interior area of section of light liquid collecting pipe; The top of this light liquid collecting pipe and light liquid overflow launder is provided with cover plate; The top of this light liquid collecting pipe is not higher than the top edge of sedimentation separation pipe.
Described liquid-liquid separation assembly also comprises: heavy-fluid liquid level control loop and light liquid liquid level control loop; Described heavy-fluid liquid level control loop is arranged on the pipeline that is connected with described heavy-fluid export mouth, comprises the first fluid level control valve, the first liquid level converter and the first liquid level sensor that connect successively, the liquid level of the heavy liquid in control settlement separator tube; Described light liquid liquid level control loop is arranged on the pipeline that is connected with described light liquid export mouth, comprises the second fluid level control valve, the second liquid level converter and the second liquid level sensor that connect successively, controls the liquid level of the light liquids in light liquid collecting pipe.
Described gas-liquid separation temperature regulating device comprises: the first temperature control chuck, and it is set in the outside of described gas-liquid separation cylindrical shell, forms the first chuck chamber between this first temperature control chuck and gas-liquid separation cylindrical shell; First temperature control circulation fluid entrance, it is arranged on bottom the side of the first described temperature control chuck; First temperature control circulation fluid outlet, it is arranged on the side top of the first described temperature control chuck.
Described liquid-liquid is separated temperature regulating device and comprises: the second temperature control chuck, and it is set in the outside of described sedimentation separation pipe, forms the second chuck chamber between this second temperature control chuck and sedimentation separation pipe; Second temperature control circulation fluid entrance, it is arranged on bottom the side of the second described temperature control chuck; Second temperature control circulation fluid outlet, it is arranged on the side top of the second described temperature control chuck.
Connected by pipeline between the first described temperature control circulation fluid outlet and the second temperature control circulation fluid entrance, and described refrigerating/heating liquid circulator is arranged on this pipeline; Connected by pipeline between the first described temperature control circulation fluid entrance and the second temperature control circulation fluid entrance.
Solution-air of the present invention-liquid three phase separator also comprises: pressure control loop, it is arranged on the pipeline that is connected with described gas export mouth, comprise the pressure indicator and pressure-control valve that connect successively, control and indicate the backpressure operation of solution-air-liquid three phase separator.
In sum, experimental rig solution-air-liquid three phase separator described in the utility model, be particularly useful for middle-size and small-size experimental rig, and the situation that in gas-liquid mixed material to be separated, amount of liquid is less, stable Liquid level and continuous blow-down can be carried out to the gas after separation and liquid material, realize the three phase separation of accurate gas-heavy-fluid-light liquid.
Experimental rig solution-air-liquid three phase separator described in the utility model; structure is simple, cost is low, efficiency is high; not only realize the process that industrial continuous control simulated by experimental rig; improve automatization level; and eliminate the manually artificial disturbance of sampling to system; decrease the experiment factors of instability, in the scientific research test that the catalyst development in fields such as petroleum refining, petrochemical industry, environmental protection, new technology route are explored, there is great practical value.
Accompanying drawing explanation
Fig. 1 is the structural representation of experimental rig of the present utility model solution-air-liquid three phase separator;
Fig. 2 is the plan structure schematic diagram of charging baffle plate of the present utility model;
Fig. 3 is the structural representation of liquid of the present utility model-liquid separation assembly;
Fig. 4 is the plan structure schematic diagram of liquid of the present utility model-liquid separation assembly;
Fig. 5 is the application schematic diagram of experimental rig of the present utility model solution-air-liquid three phase separator.
Detailed description of the invention
Below in conjunction with Fig. 1 ~ Fig. 5, describe a preferred embodiment of the present utility model in detail.
As shown in Figure 1, experimental rig solution-air-liquid three phase separator provided by the utility model, it comprises: gas-liquid separation assembly, the liquid be connected with this gas-liquid separation assembly-liquid separation assembly, and temperature regulating device.
Described gas-liquid separation assembly comprises: gas-liquid separation cylindrical shell 1, and be necking down end socket bottom it, the volume of this gas-liquid separation cylindrical shell 1 is according to determining from the gas content in the gas-liquid mixed material to be separated of experimental rig reaction system; Charging aperture 6, it is opened in the sidepiece of described gas-liquid separation cylindrical shell 1; Gas export mouth 7, it is opened in the top of described gas-liquid separation cylindrical shell 1; Drop cohesion net 5, it is arranged on the inner upper of described gas-liquid separation cylindrical shell 1; Charging baffle plate 3, it is fixed on by supporting guide plate 4 on the inwall of the close charging aperture 6 of described gas-liquid separation cylindrical shell 1.
As shown in Figure 2, described charging baffle plate 3 is curved baffle; Described supporting guide plate 4 is fan-shaped deflector, it is obliquely installed, the fan-shaped arc tips of this supporting guide plate 4 and the lower edge of described charging baffle plate 3 are by being welded to connect, and the fan-shaped summit of this supporting guide plate 4 is welded on the inwall of the close charging aperture 6 of described gas-liquid separation cylindrical shell 1.
The rational height on the upper edge of described charging baffle plate 3 is higher than charging aperture 6.
Gap 31 between the arc both sides of the edge of described charging baffle plate 3 and the inwall of gas-liquid separation cylindrical shell 1 is not less than the diameter of charging aperture 6.
As shown in figures 1 and 3, described liquid-liquid separation assembly comprises: sedimentation separation pipe 12, and it is welded on the bottom necking down end socket of described gas-liquid separation cylindrical shell 1; Light liquid collecting pipe 14, as shown in Figure 4, it is arranged on the inside of described sedimentation separation pipe 12, and its outer wall is near the side inwall of sedimentation separation pipe 12; Heavy-fluid export mouth 16, it is arranged on bottom the side of described sedimentation separation pipe 12; Light liquid export mouth 17, it is arranged on the bottom of described light liquid collecting pipe 14; Light liquid overflow launder 15, it is arranged on the center of the inner tip of described light liquid collecting pipe 14, the top edge of this light liquid overflow launder 15 flushes with the top edge of light liquid collecting pipe 14, and the interior area of section of this light liquid overflow launder 15 should be less than the interior area of section of light liquid collecting pipe 14.
The bottom of described sedimentation separation pipe 12 is flat-plate closure, and this flat-plate closure offers the through hole consistent with the diameter of light liquid collecting pipe 14, and the bottom of this light liquid collecting pipe 14 through described through hole, and is fixedly connected by welding with sedimentation separation pipe 12.
The top of described light liquid collecting pipe 14 is not higher than the top edge of sedimentation separation pipe 12.
As shown in Figure 3, described light liquid collecting pipe 14 and the top of light liquid overflow launder 15 are provided with cover plate 22, prevent the liquid after gas-liquid separation from directly falling in light liquid collecting pipe 14.
As shown in Figure 5, described liquid-liquid separation assembly also comprises: heavy-fluid liquid level control loop, it is arranged on the pipeline that is connected with described heavy-fluid export mouth 16, comprise the first fluid level control valve LV-1, the first liquid level converter LY-1 and the first liquid level sensor LT-1 that connect successively, for controlling the liquid level of the heavy liquid in sedimentation separation pipe 12, thus realize the continuous blow-down operation of the heavy liquid under level stability controls.
As shown in Figure 5, described liquid-liquid separation assembly also comprises: light liquid liquid level control loop, it is arranged on the pipeline that is connected with described light liquid export mouth 17, comprise the second fluid level control valve LV-2, the second liquid level converter LY-2 and the second liquid level sensor LT-2 that connect successively, for controlling the liquid level of the light liquids in light liquid collecting pipe 14, thus realize the continuous blow-down operation of the light liquids under level stability controls.
The inside of described light liquid collecting pipe 14 is light liquids collecting region 21, and the volume of this light liquid collecting pipe 14 is determined according to the flow of the less light liquids of density, the general time of staying maintaining light liquid phase 10-30 minute; The diameter of this light liquid collecting pipe 14 is generally not less than 6mm; Because in light liquid collecting pipe 14, area of section is relatively little, make less amount of liquid to set up higher liquid level, be conducive to the precision and the sensitivity that improve Liquid level.
The space formed between described sedimentation separation pipe 12 and light liquid collecting pipe 14 is the sedimentation separation district 20 of heavy liquid and light liquids, and its volume is determined according to the flow of liquid to be separated, the general time of staying maintaining heavy liquid 10-30 minute.
Described temperature regulating device comprises: the gas-liquid separation temperature regulating device connected by pipeline successively, liquid-liquid is separated temperature regulating device and refrigerating/heating liquid circulator 24; Described gas-liquid separation temperature regulating device is arranged on the outside of gas-liquid separation cylindrical shell 1; Described liquid-liquid is separated the outside that temperature regulating device is arranged on sedimentation separation pipe 12.
As shown in Figure 1 and Figure 5, described gas-liquid separation temperature regulating device comprises: the first temperature control chuck 2, and it is set in the outside of described gas-liquid separation cylindrical shell 1, forms the first chuck chamber 11 between this first temperature control chuck 2 and gas-liquid separation cylindrical shell 1; First temperature control circulation fluid entrance 8, it is arranged on bottom the side of the first described temperature control chuck 2; First temperature control circulation fluid outlet 9, it is arranged on the side top of the first described temperature control chuck 2.
Described liquid-liquid is separated temperature regulating device and comprises: the second temperature control chuck 13, and it is set in the outside of described sedimentation separation pipe 12, forms the second chuck chamber 23 between this second temperature control chuck 13 and sedimentation separation pipe 12; Second temperature control circulation fluid entrance 18, it is arranged on bottom the side of the second described temperature control chuck 13; Second temperature control circulation fluid outlet 19, it is arranged on the side top of the second described temperature control chuck 13.
Connected by pipeline between the first described temperature control circulation fluid outlet 9 and the second temperature control circulation fluid entrance 18, and described refrigerating/heating liquid circulator 24 is arranged on this pipeline; Connected by pipeline between the first described temperature control circulation fluid entrance 8 and the second temperature control circulation fluid entrance 18; Refrigerating/heating medium is flowed in the second chuck chamber 23 by the second temperature control circulation fluid entrance 18, flow out from the second temperature control circulation fluid outlet 19, flow in the first chuck chamber 11 by the first temperature control circulation fluid entrance 8 after pipeline connects, flow out from the first temperature control circulation fluid outlet 9 again, after the refrigerating/heating again of refrigerating/heating liquid circulator 24, circulation inflow second temperature control circulation fluid entrance 18, thus formation closed circuit, respectively regulable control is carried out to the operating temperature of gas-liquid separation assembly and liquid-liquid separation assembly.
As shown in Figure 5, solution-air of the present invention-liquid three phase separator also comprises: pressure control loop, it is arranged on the pipeline that is connected with described gas export mouth 7, comprise the pressure indicator PI-1 and pressure-control valve PCV-1 that connect successively, be respectively used to back pressure (upstream) operation controlling and indicate solution-air-liquid three phase separator.
Experimental rig solution-air-liquid three phase separator described in the utility model, its specific works principle and the course of work as described below.As shown in Figure 5, temperature regulating device and its circulation line is utilized to carry out regulable control to the operating temperature of gas-liquid separation assembly and liquid-liquid separation assembly respectively.From experimental rig reaction system gas-liquid mixed material to be separated through water cooler HE-1 cool after, entered in the gas-liquid separation cylindrical shell 1 of solution-air-liquid three phase separator by charging aperture 6, wherein partially liq material can flow downward along the inwall of gas-liquid separation cylindrical shell 1, and carries out gas-liquid separation in flow process.The gas material of all the other carrying liqs is fed baffle plate 3 to be stopped, thus changes its flow direction, and carries out gas-liquid separation on the surface of charging baffle plate 3.The gas be separated rises on the top of gas-liquid separation cylindrical shell 1, and because the large flow velocity of circulation area reduces, partial drop is by sedimentation separation under gravity.Remaining gas continues up, and by the drop cohesion net 5 of gas-liquid separation cylindrical shell 1 inner upper, the drop that do not condense still entrained in gas will be flutterred collection interception by this drop cohesion net 5, thus by gas-liquid separation completely.Separated gas is discharged by the gas export mouth 7 at gas-liquid separation cylindrical shell 1 top and pressure control loop.And the overwhelming majority of separated liquid material along the inwall of gas-liquid separation cylindrical shell 1, charging baffle plate 3, supporting guide plate 4 Surface Subsidence and flow in sedimentation separation pipe 12, the disturbance that effectively can prevent and avoid the gas-liquid mixed material entered by charging aperture 6 to be separated follow-up liquid-liquid, strengthens balance-dividing from effect.
Liquid (light liquid and heavy-fluid) mixed material after gas-liquid separation flows in sedimentation separation pipe 12, sedimentation separation is carried out by the density contrast between light liquids and heavy liquid, in the sedimentation separation district 20 of heavy liquid and light liquids, heavy liquid is deposited in the middle and lower part of sedimentation separation pipe 12 gradually, control liquid level by heavy-fluid liquid level control loop, and pass through the stable continuous discharge of heavy-fluid export mouth 16.And in the sedimentation separation district 20 of heavy liquid and light liquids, light liquids is positioned at the top of sedimentation separation pipe 12, it passes through light liquid overflow launder 15 overflow in light liquid collecting pipe 14, light liquids after separation controls liquid level by light liquid liquid level control loop, and passes through the stable continuous discharge of light liquid export mouth 17.Thus, the gas-liquid mixed material to be separated from experimental rig reaction system has been carried out the three phase separation of gas-heavy-fluid-light liquid by the utility model.
Experimental rig solution-air-liquid three phase separator described in the utility model, be particularly useful for middle-size and small-size experimental rig, and the situation that in gas-liquid mixed material to be separated, amount of liquid is less, stable Liquid level and continuous blow-down can be carried out to the gas after separation and liquid material, realize the three phase separation of accurate gas-heavy-fluid-light liquid.
Experimental rig solution-air-liquid three phase separator described in the utility model; structure is simple, cost is low, efficiency is high; not only realize the process that industrial continuous control simulated by experimental rig; improve automatization level; and eliminate the manually artificial disturbance of sampling to system; decrease the experiment factors of instability, in the scientific research test that the catalyst development in fields such as petroleum refining, petrochemical industry, environmental protection, new technology route are explored, there is great practical value.
Although content of the present utility model has done detailed introduction by above preferred embodiment, will be appreciated that above-mentioned description should not be considered to restriction of the present utility model.After those skilled in the art have read foregoing, for multiple amendment of the present utility model and substitute will be all apparent.Therefore, protection domain of the present utility model should be limited to the appended claims.
Claims (10)
1. experimental rig solution-air-liquid three phase separator, comprises: gas-liquid separation assembly, the liquid be connected with this gas-liquid separation assembly-liquid separation assembly, and temperature regulating device; It is characterized in that,
Described gas-liquid separation assembly comprises: gas-liquid separation cylindrical shell (1), is necking down end socket bottom it; Charging aperture (6), it is opened in the sidepiece of described gas-liquid separation cylindrical shell (1); Gas export mouth (7), it is opened in the top of described gas-liquid separation cylindrical shell (1); Drop cohesion net (5), it is arranged on the inner upper of described gas-liquid separation cylindrical shell (1); Charging baffle plate (3), it is fixed on the inwall of the close charging aperture (6) of described gas-liquid separation cylindrical shell (1) by supporting guide plate (4);
Described liquid-liquid separation assembly comprises: sedimentation separation pipe (12), and it is welded on the bottom necking down end socket of described gas-liquid separation cylindrical shell (1); Light liquid collecting pipe (14), it is arranged on the inside of described sedimentation separation pipe (12), and its outer wall is near the side inwall of sedimentation separation pipe (12); Heavy-fluid export mouth (16), it is arranged on bottom the side of described sedimentation separation pipe (12); Light liquid export mouth (17), it is arranged on the bottom of described light liquid collecting pipe (14); Light liquid overflow launder (15), it is arranged on the center of the inner tip of described light liquid collecting pipe (14);
Described temperature regulating device comprises: the gas-liquid separation temperature regulating device connected by pipeline successively, liquid-liquid is separated temperature regulating device and refrigerating/heating liquid circulator (24); Described gas-liquid separation temperature regulating device is arranged on the outside of gas-liquid separation cylindrical shell (1); Described liquid-liquid is separated the outside that temperature regulating device is arranged on sedimentation separation pipe (12).
2. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, described charging baffle plate (3) is curved baffle; Described supporting guide plate (4) is fan-shaped deflector, it is obliquely installed, the fan-shaped arc tips of this supporting guide plate (4) and the lower edge of described charging baffle plate (3) are by being welded to connect, and the fan-shaped summit of this supporting guide plate (4) is welded on the inwall of the close charging aperture (6) of described gas-liquid separation cylindrical shell (1).
3. experimental rig solution-air-liquid three phase separator as claimed in claim 2, it is characterized in that, the rational height on the upper edge of described charging baffle plate (3) is higher than charging aperture (6); Gap (31) between the arc both sides of the edge of this charging baffle plate (3) and the inwall of gas-liquid separation cylindrical shell (1) is not less than the diameter of charging aperture (6).
4. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, the bottom of described sedimentation separation pipe (12) is flat-plate closure, this flat-plate closure offers the through hole consistent with the diameter of light liquid collecting pipe (14), the bottom of this light liquid collecting pipe (14) through described through hole, and is fixedly connected by welding with sedimentation separation pipe (12).
5. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, the top edge of described light liquid overflow launder (15) flushes with the top edge of light liquid collecting pipe (14), and the interior area of section of this light liquid overflow launder (15) is less than the interior area of section of light liquid collecting pipe (14); The top of this light liquid collecting pipe (14) and light liquid overflow launder (15) is provided with cover plate (22); The top of this light liquid collecting pipe (14) is not higher than the top edge of sedimentation separation pipe (12).
6. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, described liquid-liquid separation assembly also comprises: heavy-fluid liquid level control loop and light liquid liquid level control loop;
Described heavy-fluid liquid level control loop is arranged on the pipeline that is connected with described heavy-fluid export mouth (16), comprises the first fluid level control valve (LV-1), the first liquid level converter (LY-1) and the first liquid level sensor (LT-1) that connect successively;
Described light liquid liquid level control loop is arranged on the pipeline that is connected with described light liquid export mouth (17), comprises the second fluid level control valve (LV-2), the second liquid level converter (LY-2) and the second liquid level sensor (LT-2) that connect successively.
7. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, described gas-liquid separation temperature regulating device comprises: the first temperature control chuck (2), it is set in the outside of described gas-liquid separation cylindrical shell (1), forms the first chuck chamber (11) between this first temperature control chuck (2) and gas-liquid separation cylindrical shell (1); First temperature control circulation fluid entrance (8), it is arranged on bottom the side of the first described temperature control chuck (2); First temperature control circulation fluid outlet (9), it is arranged on the side top of the first described temperature control chuck (2).
8. experimental rig solution-air-liquid three phase separator as claimed in claim 7, it is characterized in that, described liquid-liquid is separated temperature regulating device and comprises: the second temperature control chuck (13), it is set in the outside of described sedimentation separation pipe (12), forms the second chuck chamber (23) between this second temperature control chuck (13) and sedimentation separation pipe (12); Second temperature control circulation fluid entrance (18), it is arranged on bottom the side of the second described temperature control chuck (13); Second temperature control circulation fluid outlet (19), it is arranged on the side top of the second described temperature control chuck (13).
9. experimental rig solution-air-liquid three phase separator as claimed in claim 8, it is characterized in that, connected by pipeline between the first described temperature control circulation fluid outlet (9) and the second temperature control circulation fluid entrance (18), and described refrigerating/heating liquid circulator (24) is arranged on this pipeline; Connected by pipeline between the first described temperature control circulation fluid entrance (8) and the second temperature control circulation fluid entrance (18).
10. experimental rig solution-air-liquid three phase separator as claimed in claim 1, it is characterized in that, also comprise pressure control loop, it is arranged on the pipeline that is connected with described gas export mouth (7), comprise the pressure indicator (PI-1) and pressure-control valve (PCV-1) that connect successively, control and indicate the backpressure operation of solution-air-liquid three phase separator.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420465076.7U CN204073512U (en) | 2014-08-18 | 2014-08-18 | A kind of experimental rig solution-air-liquid three phase separator |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420465076.7U CN204073512U (en) | 2014-08-18 | 2014-08-18 | A kind of experimental rig solution-air-liquid three phase separator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689604A (en) * | 2015-01-22 | 2015-06-10 | 大庆航天三沃新技术产业有限责任公司 | Multilevel gas-liquid two-phase separation device |
| CN109621470A (en) * | 2018-12-27 | 2019-04-16 | 合肥艾普拉斯环保科技有限公司 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
-
2014
- 2014-08-18 CN CN201420465076.7U patent/CN204073512U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689604A (en) * | 2015-01-22 | 2015-06-10 | 大庆航天三沃新技术产业有限责任公司 | Multilevel gas-liquid two-phase separation device |
| CN109621470A (en) * | 2018-12-27 | 2019-04-16 | 合肥艾普拉斯环保科技有限公司 | The gas-liquid separator that can be used in acrylamide group methyl propane sulfonic acid distillation equipment |
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