WO2021088827A1 - 一种测试泡沫流体性能和消泡分离效果的实验装置及方法 - Google Patents

一种测试泡沫流体性能和消泡分离效果的实验装置及方法 Download PDF

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WO2021088827A1
WO2021088827A1 PCT/CN2020/126250 CN2020126250W WO2021088827A1 WO 2021088827 A1 WO2021088827 A1 WO 2021088827A1 CN 2020126250 W CN2020126250 W CN 2020126250W WO 2021088827 A1 WO2021088827 A1 WO 2021088827A1
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foam
gas
fluid
defoaming
experimental
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PCT/CN2020/126250
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English (en)
French (fr)
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李玉星
胡其会
刘翠伟
王武昌
孟令雅
王婧涵
马宏涛
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中国石油大学(华东)
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Priority to US17/774,037 priority Critical patent/US20220412862A1/en
Publication of WO2021088827A1 publication Critical patent/WO2021088827A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/02—Foam dispersion or prevention
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N13/00—Investigating surface or boundary effects, e.g. wetting power; Investigating diffusion effects; Analysing materials by determining surface, boundary, or diffusion effects
    • G01N13/02—Investigating surface tension of liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0042—Degasification of liquids modifying the liquid flow
    • B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • B01D19/0057—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0063—Regulation, control including valves and floats
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/235—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids for making foam
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G01N15/02—Investigating particle size or size distribution
    • G01N15/0205—Investigating particle size or size distribution by optical means
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G01N15/02—Investigating particle size or size distribution
    • G01N15/0205—Investigating particle size or size distribution by optical means
    • G01N15/0227—Investigating particle size or size distribution by optical means using imaging; using holography
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N13/00—Investigating surface or boundary effects, e.g. wetting power; Investigating diffusion effects; Analysing materials by determining surface, boundary, or diffusion effects
    • G01N13/02—Investigating surface tension of liquids
    • G01N2013/0241—Investigating surface tension of liquids bubble, pendant drop, sessile drop methods
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G01N2015/0023—Investigating dispersion of liquids
    • G01N2015/0026—Investigating dispersion of liquids in gas, e.g. fog
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G01N2015/0042—Investigating dispersion of solids
    • G01N2015/0046—Investigating dispersion of solids in gas, e.g. smoke

Definitions

  • the present disclosure belongs to the technical field of oil and gas separation test experiments in an oil and gas gathering and transportation system, and specifically relates to an experimental device and method for testing foam fluid performance and defoaming separation effects.
  • CO 2 flooding is by injecting CO 2 into the oil layer and using CO 2 as the oil displacing agent.
  • CO 2 as the oil displacing agent.
  • it can achieve the effects of reducing displacement resistance, lowering crude oil viscosity, promoting crude oil volume expansion and miscibility effects to improve crude oil recovery. Therefore, CO 2 gas can be used reasonably to reduce greenhouse gas emissions, which has broad application prospects.
  • CO 2 has higher solubility in oil and water and greater solubility in oil, which makes the CO 2 flooding produced fluid present the characteristics of high foam content.
  • foams will cause harm to the gathering and transportation of crude oil in many aspects: the foam will cause incomplete oil and gas separation and reduce the processing capacity; increase the error of meter measurement; the existence of a large amount of foam in the separator will squeeze the gas phase space of the separator. It seriously affects the effect of gas-liquid separation and increases the separation time; the presence of a large amount of foam can also cause crude oil to tank.
  • testing the performance of the foamed fluid produced by CO 2 flooding, optimizing and upgrading defoaming separation technology, and providing a more comprehensive and reasonable separation effect evaluation method can provide a strong guarantee for the safe operation of subsequent oil and gas gathering and transportation equipment, and for the development of CO 2 flooding oilfields.
  • the prior art has insufficient analysis of foam fluid.
  • the present disclosure proposes an experimental device and method for testing foam fluid performance and defoaming separation effect.
  • the first objective of the present disclosure is to provide an experimental device for testing foam fluid performance and defoaming separation effect.
  • the experimental device will produce and fully developed foam fluid for performance measurement and defoaming separation effect evaluation.
  • the second objective of the present disclosure is to provide a foam generating module that can generate fluid foams with different gas-liquid mixing ratios, and to enable an experimental device to measure fluid foams with different gas-liquid mixing ratios under different conditions.
  • the third object of the present disclosure is to provide an experimental method of an experimental device for testing foam fluid performance and defoaming separation effect. According to the experimental method, the foam fluid performance and defoaming separation effect can be accurately and conveniently measured.
  • An experimental device for testing foam fluid performance and defoaming separation effect including a foam generation module for generating foam fluid, and an experimental loop for transporting foam fluid and fully developing foam fluid in the loop, used for testing foam fluid Performance foam performance test module, foam separation processing module used to separate foam from fluid and gas, and defoaming result evaluation module used to test and evaluate defoaming results.
  • the end of the foam generating module is connected to the experimental loop, and input at the same time as the foam generating module Oil and water are mixed with liquid and CO 2 gas and mixed into different proportions of oil, water and gas to form a foam fluid.
  • the foam fluid formed after mixing is transported to the experimental loop, from the experimental loop to the foam performance test module and foam at the end of the experimental loop.
  • the separation processing module in the foam performance test module, the fully developed foam fluid input from the experimental loop is measured and analyzed to obtain the foam volume, foam half-life and foam quality of the foam fluid.
  • the test loop The fully developed foam fluid input in the channel is separated into gas and liquid.
  • the foam separation processing module is equipped with a defoaming result evaluation module.
  • the defoaming result evaluation module analyzes the gas separated by the foam separation processing module to obtain the liquid content of the gas, The size of the droplets in the gas and the oil content in the gas.
  • the foam generating module includes: an oil-water mixing kettle, a CO 2 gas cylinder, and a foam generating device.
  • the foam generating device is connected to the oil-water mixing kettle and the CO 2 gas cylinder through a connecting pipeline.
  • the connecting pipeline from the oil-water mixing kettle to the foam generating device is in accordance with The second centrifugal pump and the first flow meter are arranged in the direction of liquid flow.
  • the connecting pipeline from the CO 2 gas cylinder to the foam generating device is provided with a gas storage tank and the first gas flow meter in sequence according to the gas flow direction.
  • control water mixing kettle liquid in mixing water and CO 2 cylinder is calculated in the flowmeter a first CO 2 gas through gas inlet conduit means and inlet conduit sidewall liquid foam generating foam generating apparatus bottom entry Inside the foam generating device, foam fluids with different gas-liquid mixing ratios are formed.
  • a stainless steel wire mesh with meshes is arranged inside the foam generating device, and the gas phase pipe inlet and the liquid phase pipe inlet of the foam generating device are arranged at 90° spatially, and a wire is arranged above the liquid phase pipe inlet.
  • Layer of thermal insulation fiber, thermal insulation fiber is arranged inside the foam generating device.
  • the heated gas enters the foam generating device and mixes with oil and water to produce foam fluid.
  • the generated foam fluid also needs thermal insulation.
  • the thermal insulation fiber is distributed There are several fiber thorns, and the oil-water mixed liquid is pumped into the foam generating device by the second centrifugal pump. These oil-water mixed liquids collide with each other in the pipeline, causing the oil-water mixed liquid to carry a lot of bubbles and foam.
  • the insulation fiber can reduce the bubbles and bubbles in the oil-water mixed liquid. Carrying capacity of foam.
  • the foam performance test module includes an analysis tank, the lower end of the analysis tank is provided with a liquid phase outlet, the side wall of the analysis tank is provided with a gas outlet, and the first absorption box and the first sampling valve are installed in sequence to the outside of the gas outlet.
  • the water-absorbing and oil-absorbing material is placed, and the quality difference before and after the water-absorbing and oil-absorbing material in the first absorption box is measured.
  • the first sampling valve is connected to a gas collection bag through a pipeline.
  • the analysis tank is a visualization tank, and a standard scale is set on the side wall of the tank.
  • the foam separation processing module includes a horizontal separator.
  • the horizontal separator is a visualization tank.
  • the side wall of the tank is provided with a standard scale.
  • the lower end of the horizontal separator is provided with a liquid phase outlet.
  • Covered with a second heating jacket the upper end of the horizontal separator is provided with a gas phase outlet, and the gas phase outlet is connected to the defoaming result evaluation module.
  • the upper end of the horizontal separator is also provided with a tubular column type cyclone separator and a tubular column type cyclone separator.
  • the lower end is connected to the horizontal separator.
  • the main pipe at the end of the experimental loop is also provided with a third bypass pipeline.
  • the third bypass pipeline is connected to the column type cyclone separator.
  • the foam fluid passes through the third bypass pipe of the experimental loop.
  • the path enters the tubular cyclone separator, and then flows into the horizontal separator from the tubular cyclone separator.
  • the foam fluid inlet of the tubular cyclone separator is equipped with a gas phase outlet.
  • the gas phase outlet is connected to the gas phase outlet of the horizontal separator through a gas pipe, and the gas phase outlet of the horizontal separator is connected to the defoaming result evaluation module, which provides direct access to the horizontal separator for separation and the column type cyclone separator before entering the horizontal
  • the type separator separates two different separation devices, which represents a single separation device and two different processing ideas of pre-separation and then separation. The better separation method of the two can be selected according to the defoaming separation effect after the measurement.
  • the defoaming result evaluation module includes a droplet size observation window and a second absorption box at the end of the droplet size observation window.
  • the gas separated by the foam separation processing module sequentially passes through the droplet size observation window and the second absorption box.
  • the outlet of the second absorption box is provided with two pipelines, the first pipeline is connected to the atmosphere, the first pipeline is provided with a second gas phase flow meter, and the second pipeline is provided with a second sampling valve and a second sampling valve
  • the gas collection bag is connected through a trachea, and a water-absorbing and oil-absorbing material is placed in the second absorption box.
  • the quality difference can be obtained by weighing the water-absorbing and oil-absorbing material before and after the experiment; reading the reading of the second gas-phase flowmeter at the gas-phase outlet of the horizontal separator can calculate the liquid content in the separated gas Rate; use a high-speed camera device to shoot the foam layer of the horizontal separator to complete the statistics of the bubble size distribution; use a laser particle size analyzer to detect the droplet size observation window at the gas phase outlet of the horizontal separator to achieve The droplet size in the gravity sedimentation zone is analyzed, the pressure difference before and after separation in the foam separation processing module is calculated, and the pressure difference during separation is calculated.
  • the present disclosure provides an experimental method for testing foam fluid performance and defoaming separation effect:
  • the first step preparation stage: pass CO 2 gas into the entire experimental device to remove impurities in the tube;
  • the second step the foam fluid generation stage: the CO 2 gas with the required gas flow rate is passed into the foam generating device, and the oil-water mixed liquid with the required liquid flow rate is transported to the foam generating device, mixed and produced in the foam generating device Foam fluid
  • Step 3 Foam fluid delivery stage: Foam fluid enters the experimental loop, connects to the first bypass pipeline, and discharges unstable and underdeveloped foam. After the foam fluid output is stable, connect to the second bypass pipeline to remove The foam fluid is input into the foam performance test module;
  • Step 4 Foam fluid defoaming stage: Connect the main pipe at the end of the experimental loop, and the foam fluid enters the horizontal separator until the foam fluid level reaches half the height of the separator, close the foam fluid input so that the foam fluid no longer enters In the horizontal separator;
  • Step 5 Test stage: Measure the volume of the foam in the foam performance test module, analyze the half-life of the foam and measure the quality of the foam; the quality difference is obtained by weighing the water-absorbing and oil-absorbing material before and after the experiment; the second at the gas phase outlet of the horizontal separator The reading of the gas flow meter can calculate the liquid content of the separated gas; use a high-speed camera device to photograph the foam layer of the horizontal separator to complete the statistics of the bubble size distribution; use a laser particle size analyzer to The droplet size observation window at the gas phase outlet of the horizontal separator is detected to realize the analysis of the droplet size in the gravity sedimentation zone, and the pressure difference before and after separation in the foam separation processing module is calculated to calculate the pressure difference during separation. .
  • the present disclosure provides another defoaming method.
  • the foam fluid enters the tubular cyclone separator and then enters the horizontal separator until the foam fluid
  • the foam fluid input is closed so that the foam fluid no longer enters the horizontal separator.
  • the foam generation module of the present disclosure can generate foam fluids in different proportions through different ratios of input gas and liquid, and measure and evaluate the transportation, performance, and defoaming separation effects of different foam fluids.
  • the foam generating device of the present disclosure can statically mix gas and liquid under the action of the stainless steel wire mesh, and avoid the influence of dynamic mixing devices such as stirring impeller on the foam fluid state.
  • a layer of thermal insulation fiber is arranged above the inlet of the liquid phase pipeline of the foam generating device of the present disclosure, and the thermal insulation fiber is arranged inside the foam generating device to reduce the amount of bubbles and foam carried in the oil-water mixed liquid and provide heat insulation for the oil-water mixed liquid.
  • the experimental loop of the present disclosure can fully develop the foam fluid and transport the fully developed foam fluid to the corresponding measuring device.
  • the present disclosure provides two ideas for defoaming separation, and can be tested separately.
  • This set of experimental testing equipment is of great significance to the study of special problems that occur in the gas-liquid separation process of CO 2 flooding produced fluid.
  • the present disclosure can simulate and carry out visual foam performance testing of CO 2 flooding produced fluid, optimization of separator defoaming components, and defoaming separation effect evaluation.
  • FIG. 1 is a schematic diagram of the structure of the disclosed experimental device for measuring foam fluid performance and defoaming separation effect.
  • Foam generation module 200, foam performance testing module, 300, foam separation processing module, 400, defoaming result evaluation module.
  • azimuth or positional relationship is based on the azimuth or positional relationship shown in the drawings, and is only a relationship term determined to facilitate the description of the structural relationship of the components or elements in the present disclosure. Disclosure restrictions.
  • the present disclosure provides an experimental device for testing foam fluid performance and defoaming separation effect, which is used to test and evaluate the foam performance and defoaming separation effect of CO 2 flooding produced fluid in gathering and transportation separation.
  • the experimental device includes a device for generating foam Fluid foam generation module 100, experimental loop 50 for transporting foam fluid and fully developing the foam fluid in the loop, foam performance testing module 200 for testing the performance of foam fluid, foam for separating foam from fluid and gas
  • foam performance testing module 200 for testing the performance of foam fluid
  • the separation processing module 300 and the defoaming result evaluation module 400 for testing and evaluating the defoaming result are described in detail here:
  • the foam generating module 100 generates foam fluid for simulating the foam fluid produced by mixing CO 2 and the oil layer in a certain proportion under real work.
  • the foam generating module 100 includes an oil-water mixing tank 5, a gas storage tank 17 connected to a CO 2 gas cylinder 12, and A foam generating device 24 connected with the oil-water mixing kettle 5 and the gas storage tank 17.
  • the oil-water mixing kettle 5 is equipped with a variable frequency stirring motor and a heating rod that can control the heating temperature.
  • the upper end of the oil-water mixing kettle 5 is equipped with a liquid phase reflux inlet, and the liquid phase reflux inlet is provided with a third valve 7 for heating
  • the liquid after the test is recirculated to the oil-water mixing tank 5 so that the liquid can be recycled.
  • the oil-water mixing kettle 5 is equipped with a first temperature sensor 4 on the kettle body.
  • the first temperature sensor 4 is used to measure the temperature of the liquid in the kettle and obtain and display it in real time.
  • a sewage outlet is installed at the bottom of the kettle, and a first valve 3 is installed on the sewage outlet.
  • a valve 3 can discharge the liquid in the oil-water mixing kettle 5 to the outside for further processing.
  • the connecting pipeline between the liquid outlet at the lower end of the oil-water mixing kettle 5 and the inlet of the liquid phase pipeline at the bottom of the foam generating device 24 is sequentially installed
  • the second valve 6, the second centrifugal pump 8, the fourth valve 9, the first liquid flow meter 10, the fifth valve 11, open the second valve 6, the second centrifugal pump 8, the fourth valve 9, and the fifth valve 11 Close the first valve 3, and pump the liquid in the oil-water mixing kettle 5 into the foam generating device 24 under the action of the second centrifugal pump 8.
  • the oil-water mixing kettle 5 pumps water from the water tank through the first centrifugal pump 2, and the oil-water mixing kettle 5 pumps water from the water tank through the first centrifugal pump 2. In the kettle 5, liquids with different oil-water ratios are formed.
  • the gas in the CO 2 gas cylinder 12 is transported to the gas storage tank 17 through a gas pipeline, so that the high-pressure gas in the CO 2 gas bottle 12 is expanded into CO 2 gas under a stable pressure.
  • the lower end of the gas storage tank 17 is covered with A heating jacket 18 is used to raise the temperature of the gas in the gas storage tank 17 so that the gas storage tank 17 can provide gases of different temperatures.
  • the gas storage tank 17 is equipped with a first pressure sensor 15 and a second temperature sensor 16 for use To detect the pressure and temperature of the gas in the gas storage tank 17 in real time, a sixth valve 13 and a seventh valve 14 are installed in sequence between the CO 2 gas cylinder and the gas storage tank 17, and the sixth valve 13 is installed in the CO 2 gas cylinder and the storage tank.
  • the seventh valve 14 is installed on the bypass on the main gas transmission line.
  • the sixth valve 13 is opened and the seventh valve 14 is closed .
  • the gas in the CO 2 cylinder enters the gas storage tank and is closed.
  • the sixth valve 13 opens the seventh valve 14, the gas in the CO 2 cylinder is discharged into the atmosphere, and the gas in the gas storage tank 17 passes through the eighth valve 19, the ninth valve 20, the first gas phase flow meter 22, and the tenth valve 23 enters the foam generating device 24, and a second pressure sensor 21 is installed on the gas pipeline between the ninth valve 20 and the first gas phase flow meter 22 to detect the pressure of the gas input to the foam generating device 24 from the gas storage tank 17.
  • the foam generating device 24 is used to mix and agitate the gas and liquid phases under different conditions to form a foamed fluid.
  • the overall shape of the device is cylindrical, and the internal chamber is a cylindrical cavity.
  • the foam generating device 24 is used for the inlet of the gas phase pipeline.
  • the gas-phase pipeline inlet is connected to the gas storage tank 17.
  • the gas-phase pipeline inlet is preferably opened on the side wall of the foam generating device 24, and the lower end of the foam generating device 24 is provided with a liquid pipeline inlet for communication with
  • the oil-water mixing kettle 5 is connected, the gas-phase pipeline inlet and the liquid-phase pipeline inlet are spaced at 90°, and the foam generating device 24 is filled with perforated stainless steel wire mesh, and the foam generating device 24 is filled with liquid and gas.
  • the foam fluid Under the action of the stainless steel wire mesh, the foam fluid is fully mixed and generated, and enters the experimental loop 50 through the mixed phase outlet at the bottom of the foam generating device 24, and the gas and different conditions under different pressure, temperature, flow, etc. are completed in the foam generating device 24.
  • the mixing of liquids under the conditions of temperature, flow, etc. forms a variety of different foam fluids and outputs.
  • a layer of thermal insulation fiber is arranged above the inlet of the liquid phase pipeline of the foam generating device 24.
  • the thermal insulation fiber is arranged inside the foam generating device.
  • the heated gas enters the foam generating device and mixes with oil and water to produce foam fluid. It also needs heat preservation.
  • the oil-water mixed liquid is pumped into the foam generator by the second centrifugal pump. These oil-water mixed liquids collide with each other in the pipeline, causing the oil-water mixed liquid to carry a lot of bubbles
  • thermal insulation fiber can greatly reduce the amount of bubbles and foam carried in the oil-water mixed liquid.
  • the experimental loop 50 of the present disclosure is used to transport foam fluid to the foam performance testing module 200 and the foam separation processing module 300 and to develop the foam fluid in the experimental loop 50.
  • the starting point of the experimental loop 50 is the mixing of the foam generating device 24
  • the phase outlet starts to calculate, and the end point is at the mixed phase inlet leading to the foam separation processing module 300.
  • the experimental loop 50 is set as a visualization pipeline for observing the state of the foam fluid in the experimental loop 50 and the interaction of different flow patterns and foams. Function:
  • the main pipe at the end of the experimental loop 50 is provided with two bypass pipelines, which are the first bypass pipeline and the second bypass pipeline in sequence according to the flow direction of the foam fluid in the experimental loop 50.
  • the eleventh valve 25 is installed on the first bypass pipeline.
  • the eleventh valve 25 When only the eleventh valve 25 is opened, only the first bypass pipeline is opened, which will discharge the insufficiently developed and stable foam fluid in the experimental loop 50 of the experimental equipment stage , These foam fluids are not fully developed, so the preliminary testing and evaluation of the foam fluid is meaningless; the second bypass pipeline is connected to the foam performance test module 200, and the twelfth valve 26 is installed on the second bypass pipeline.
  • the twelfth valve 26 is opened, and the fully developed foam fluid is delivered to the foam performance testing module 200, and then the performance of the foam fluid is analyzed and tested.
  • the foam performance test module 200 is used to test and analyze the foam fluid output from the second bypass pipeline of the experimental loop 50, and includes an analysis tank 27.
  • the analysis tank 27 is located in the foam separation process before the foam defoaming separation process. Before the module 300, test the foam performance in the analysis tank 27 including foam volume, foam half-life and foam quality.
  • the foam performance test module 200 includes an analysis tank 27.
  • the analysis tank 27 uses a visual analysis tank 27 with a standard scale and an experimental loop. 50
  • the developed foam fluid enters the analysis tank 27 through the second bypass pipeline, and reads the foam volume through the scale on the analysis tank 27.
  • the side wall of the analysis tank 27 is equipped with a gas outlet, and the gas outlet of the analysis tank 27 is installed outwards in sequence
  • the first absorption box 29, the thirteenth valve 31, the main line between the first absorption box 29 and the thirteenth valve 31 is equipped with a first sampling valve 30, and the first absorption box 29 is built with water and oil absorbing materials.
  • the valve 31 discharges the gas in the analysis tank 27 into the atmosphere.
  • the pipeline after the first sampling valve 30 is preferably a rubber hose.
  • the lower end of the analysis tank 27 is equipped with a liquid outlet, and the liquid outlet is installed with a tenth
  • the fourth valve 32 opens the fourteenth valve 32 to discharge the liquid in the analysis tank 27 into the oil-water mixing tank 5 again to realize the reuse of the liquid.
  • the foam separation processing module 300 includes a visual horizontal separator 40.
  • a variety of defoaming separation components can be installed and disassembled. Different foam separation treatments can be obtained through the combination of different defoaming separation components.
  • the separator 40 has a standard scale.
  • the foam separation processing method of the foam separation processing module 300 is as follows: the foam fluid passes through the end main pipe of the experimental loop 50 and directly enters the horizontal separator 40, and the foam is adjusted by the scale on the horizontal separator 40. The volume is measured. The lower end of the horizontal separator 40 is covered with a second heating jacket 41 for heating the foam fluid in the horizontal separator 40.
  • the upper end of the horizontal separator 40 is equipped with a gas phase outlet, and the horizontal separator 40
  • the third temperature sensor 51 and the seventh pressure sensor 39 are used to measure the temperature in the horizontal separator 40.
  • the lower end of the horizontal separator 40 is equipped with a liquid phase outlet, and an eighteenth valve 42 is installed on the liquid phase outlet. , Open the eighteenth valve 42 and input the separated liquid into the oil-water mixing kettle 5 to realize the circulation of the liquid.
  • the defoaming result evaluation module 400 observes, absorbs, collects and measures the exit of the foam separation processing module 300 to complete the analysis of the defoaming separation results, including the droplet size observation window at the gas phase exit of the foam separation processing module 300 43 and the second absorption box 44 installed at the end of the droplet size observation window 43, the gas phase outlet of the foam separation processing module 300 refers to the total gas phase outlet after the gas phase outlets of the horizontal separator 40 and the column cyclone separator 52 are combined.
  • the second absorption box 44 also contains water-absorbent and oil-absorbing materials. There are two pipelines at the outlet of the second absorption box 44. A nineteenth valve 45 and a second gas-phase flow meter 46 are installed on the first pipeline in the order of gas flow.
  • the gas is discharged into the atmosphere through this pipeline.
  • the purpose of this pipeline is to measure the gas flow through the first pipeline through the second gas phase flow meter 46.
  • the second pipeline is equipped with a twentieth valve 48 and a second sampling.
  • the valve 47 and the second sampling valve 47 are connected to the gas collection bag through a gas pipe.
  • the gas pipe is preferably a rubber hose.
  • the twentieth valve 48 can be opened to discharge the gas into the atmosphere.
  • the liquid discharged from the horizontal separator 40 and the liquid discharged from the analysis tank 27 pass through a pipeline to the second centrifugal pump 8.
  • the pipeline is provided with the twenty-first valve 49, the third valve 7 is opened, and the second centrifugal pump Driven by the pump 8, the liquid discharged from the horizontal separator 40 and the liquid discharged from the analysis tank 27 are recirculated into the oil-water mixing tank 5 through the liquid phase reflux inlet on the oil-water mixing tank 5 to complete the liquid circulation.
  • valves can use multiple types or models of valves, including the first valve 3, the second valve 6, the third valve 7, the eleventh valve 25, the twelfth valve 26, the thirteenth valve 31, and the fourteenth valve.
  • the valve 32, the fifteenth valve 33, the seventeenth valve 38, the eighteenth valve 42, the nineteenth valve 45, the twentieth valve 48, and the twenty-first valve 49 all preferentially adopt ball valves to realize the corresponding
  • the opening and closing of the pipeline in addition, there are some more special valves, which can only use valves of the same function type, the fourth valve 9 uses a gate valve so that the second flow pump 8 can only be pumped into the foam generating device 24.
  • the fifth valve 11 uses a check valve to prevent fluid from flowing back to the first liquid flow meter 10
  • the fourth valve 9 uses a gate valve
  • the fifth valve 11 uses a check valve
  • the two valves cooperate so that the first liquid phase flow meter 10 accurately measures the flow rate of the fluid pumped into the foam generating device 24 by the second flow pump 8, and is not affected by valve flow adjustment and return flow.
  • the sixth valve 13 Use a pressure reducing valve to reduce the outlet pressure of the CO 2 cylinder to the required pressure, and rely on the energy of the CO 2 itself to automatically maintain the pressure stable, so that the CO 2 enters the gas storage tank at a stable pressure.
  • the seventh valve 14 uses a vent valve
  • the eighth valve 19 uses a pressure reducing valve
  • the tenth valve 20 uses a needle valve
  • the eleventh valve 23 uses a check valve.
  • Three types of valves are used in conjunction with the gas tank 17 to make the second pressure sensor 21, the first pressure sensor 21, and the first pressure sensor 21.
  • the pressure and gas flow measured by the gas-phase flowmeter 22 are very accurate, so as to avoid inaccurate measurement results caused by unstable gas flow.
  • the foam separation processing module 300 of the present disclosure adopts the second technical solution, which adds a tubular column type cyclone separator 52 on the basis of Embodiment 1.
  • the tubular column type cyclone separator 52 is installed at the upper end of the horizontal separator 40,
  • the main pipeline at the end of the experimental loop 50 is provided with three bypass pipelines, and according to the flow direction of the foam fluid in the experimental loop 50, they are the first bypass pipeline, the second bypass pipeline, and the third bypass pipeline.
  • the third bypass pipeline is connected to the column type cyclone separator 52 in the foam separation processing module 300, and the sixteenth valve 35, the sixteenth valve 35 and the column type cyclone are installed on the third bypass pipe
  • a fifth pressure sensor 36 is installed on the third bypass line between the separators 52, the sixteenth valve 35 is opened, and the foam fluid enters the column type cyclone separator 52 through the third bypass line.
  • the experimental loop The main pipe at the end of 50 is connected to the horizontal separator 40, the main pipe at the end of the experimental loop 50 is equipped with a fifteenth valve 33, and the fourth pressure sensor 34 is installed between the fifteenth valve 33 and the horizontal separator 40
  • the sixteenth valve 35 adopts a ball valve.
  • the foam separation processing method of the foam separation processing module 300 is as follows: the foam fluid enters the column type cyclone separator 52 through the third bypass pipe of the experimental loop 50, and then flows into the horizontal separation type from the column type cyclone separator 52
  • a sixth pressure sensor 37 is installed on the column type cyclone separator 52, and the gas phase outlet is installed at the inlet of the column type cyclone separator 52 for entering the foam fluid.
  • the column type cyclone separator 52 The gas-phase outlet of the gas pipe is connected to the gas-phase outlet of the horizontal separator 40 through a gas pipe, and a seventeenth valve 38 is installed on the gas pipe.
  • the present disclosure can select the effects of two different inlets and different defoaming components on the results of defoaming separation tests described in Embodiment 1 and Embodiment 2 according to different degrees of oil foaming conditions.
  • the present disclosure provides an experimental method for testing foam fluid performance and defoaming separation effect.
  • the experimental device disclosed in the first embodiment of the present disclosure is used for measurement.
  • the experimental operation process is as follows:
  • Step 1 Preparation phase: CO 2 is the cylinder CO 2 in the gas to a gas storage tank 17, the whole experiment a CO 2 gas tank 17 through the apparatus, remove the inner tube of impurities, adjusting the horizontal separator 40 The valve is opened, in which the gas phase outlet of the horizontal separator 40 is opened, and the liquid phase outlet of the horizontal separator 40 is closed.
  • the second step the stage of producing foam fluid: adjust the eighth valve 19 to adjust the CO 2 gas to the required gas flow rate, the CO 2 gas is passed into the foam generating device 24, and the second ball valve 6 at the lower end of the oil-water mixing tank 5 is opened at the same time, Close the third ball valve 7, open the second centrifugal pump 8 and the fourth valve 9, according to the output power of the second centrifugal pump 8 to deliver the required flow of liquid to the foam generating device 24, the liquid is a mixture of oil and water, the design flow rate The CO 2 gas and the liquid with the designed flow rate are mixed in the foam generating device 24 to generate foam fluid.
  • Step 3 Foam fluid delivery stage: Foam fluid enters the experimental loop 50, first open the eleventh valve 25 to discharge the unstable and underdeveloped foam, after the foam fluid output stabilizes, close the eleventh valve 25 and open The twelfth valve 26 inputs the foam fluid into the analysis tank 27, and closes the twelfth valve 26 after waiting for a specified time.
  • Step 4 Foam fluid defoaming stage: While closing the twelfth valve 26, open the fifteenth valve 33 to allow the foam fluid to enter the horizontal separator 40 until the foam fluid level reaches half the height of the separator, close the eighth Valve 19, ninth valve 20, second valve 6, fourth valve 9 and fifteenth valve 33 prevent CO 2 gas and oil-water mixed liquid from entering the foam generating device 24, and the foam fluid no longer enters the horizontal separation ⁇ 40 ⁇ .
  • Step 5 Test stage: Test the foam performance in the analysis tank 27, including reading the volume of the foam through the scale, analyzing the half-life of the foam and measuring the quality of the foam in the analysis tank 27; by comparing the first absorption box 29 and the second absorption box 44 The internal water-absorbing and oil-absorbing material is weighed before and after the experiment to obtain poor quality; reading the reading of the second gas-phase flow meter 46 at the gas-phase outlet of the horizontal separator 40 can calculate the liquid content of the separated gas; using a high-speed camera device Take a picture of the foam layer of the horizontal separator 40 to complete the statistics of the bubble size distribution; use a laser particle size analyzer to detect the droplet size observation window 43 at the gas phase outlet of the horizontal separator 40 to realize the gravity sedimentation area Analyze the size of the droplets and calculate the pressure difference during separation based on the pressure measured by the seventh pressure sensor 39 before and after the separation
  • Step 6 Liquid recovery stage: After the experiment is over, open the eighteenth valve 42, the fourteenth valve 32, the twenty-first valve 49 and the third valve 7, and start the second centrifugal pump 8. The liquid in the type separator 10 is pumped back into the oil-water mixing tank 5.
  • the present disclosure provides an experimental method for testing foam fluid performance and defoaming separation effect.
  • the experimental device disclosed in the second embodiment of the present disclosure is used for measurement.
  • the experimental operation process is as follows:
  • Step 1 Preparation phase: CO 2 is the cylinder CO 2 in the gas to a gas storage tank 17, the whole experiment a CO 2 gas tank 17 through the apparatus, remove the inner tube of impurities, adjusting the horizontal separator 40 The valve is opened, in which the gas phase outlet of the horizontal separator 40 is opened, and the liquid phase outlet of the horizontal separator 40 is closed.
  • the second step the stage of producing foam fluid: adjust the eighth valve 19 to adjust the CO 2 gas to the required gas flow rate, the CO 2 gas is passed into the foam generating device 24, and the second ball valve 6 at the lower end of the oil-water mixing tank 5 is opened at the same time, Close the third ball valve 7, open the second centrifugal pump 8 and the fourth valve 9, according to the output power of the second centrifugal pump 8 to deliver the required flow of liquid to the foam generating device 24, the liquid is a mixture of oil and water, the design flow rate The CO 2 gas and the liquid with the designed flow rate are mixed in the foam generating device 24 to generate foam fluid.
  • Step 3 Foam fluid delivery stage: Foam fluid enters the experimental loop 50, first open the eleventh valve 25 to discharge the unstable and underdeveloped foam, after the foam fluid output stabilizes, close the eleventh valve 25 and open The twelfth valve 26 inputs the foam fluid into the analysis tank 27, and closes the twelfth valve 26 after waiting for a specified time.
  • Step 4 Foaming fluid defoaming stage: closing the twelfth valve 26 and opening the sixteenth valve 35, so that the foam fluid enters the tubular cyclone separator 52, and enters the horizontal through the tubular cyclone separator 52 Type separator 40, until the foam fluid level reaches half the height of the separator, the eighth valve 19, the ninth valve 20, the second valve 6, the fourth valve 9 and the fifteenth valve 33 are closed to make CO 2 gas and oil water The mixed liquid no longer enters the foam generating device 24, and the foam fluid no longer enters the horizontal separator 40.
  • Step 5 Test stage: Test the foam performance in the analysis tank 27, including reading the volume of the foam through the scale, calculating the half-life of the foam and measuring the quality of the foam; Weigh before and after the experiment to get the quality difference; read the reading of the second gas phase flow meter 46 at the gas phase outlet of the horizontal separator 40 to calculate the liquid content of the separated gas; use a high-speed camera device to compare the horizontal separator The foam layer of 40 is photographed to complete the statistics of the bubble size distribution; the laser particle size analyzer is used to detect the droplet size observation window 43 at the gas phase outlet of the horizontal separator 40 to realize the droplet size in the gravity sedimentation zone Analyze; calculate the pressure difference during separation by the pressure before and after the separation of the fifth pressure sensor 36, the sixth pressure sensor 37, and the seventh pressure sensor 39.
  • Step 6 Liquid recovery stage: After the experiment is over, open the eighteenth valve 42, the fourteenth valve 32, the twenty-first valve 49 and the third valve 7, and start the second centrifugal pump 8. The liquid in the type separator 10 is pumped back into the oil-water mixing tank 5.

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Abstract

一种测试泡沫流体性能和消泡分离效果的实验装置及方法，实验装置包括用于产生泡沫流体的泡沫发生模块（100）、用于输送泡沫流体并使泡沫流体在环道内充分发展的实验环道（50），用于测试泡沫流体性能的泡沫性能测试模块（200），用于泡沫与流体、气体分离的泡沫分离处理模块（300）以及用于测试评估消泡结果的消泡结果评估模块（400），方法通过在泡沫发生模块（100）内产生不同的泡沫流体，经实验环道（50）输送至泡沫性能测试模块（200）和不同的泡沫分离处理模块（300），利用泡沫性能测试模块（200）和与泡沫分离处理模块（300）连接的消泡结果评估模块（400）测量泡沫流体的泡沫性能及消泡分离效果。

Description

一种测试泡沫流体性能和消泡分离效果的实验装置及方法 技术领域
本公开属于油气集输系统中的油气分离测试实验技术领域，具体涉及一种测试泡沫流体性能和消泡分离效果的实验装置及方法。
背景技术
本部分的陈述仅仅是提供了与本公开相关的背景技术信息，不必然构成在先技术。
CO 2驱油是通过将CO 2注入油层并以CO 2作为驱油剂，在原油采集过程中能够达到减少驱替阻力、降低原油黏度、促进原油体积膨胀和混相效应等效果以提高原油采收率，并且CO 2气体被合理利用也可以减少温室气体排放,具有广阔的应用前景。
CO 2在油中和水中都有较高的溶解度且在油中的溶解度更大，使CO 2驱采出流体呈现出高含泡沫的特点。这些泡沫对原油的集输会形成很多方面的危害：泡沫会造成油气分离不彻底、处理量减少；增大了仪表计量的误差；分离器中大量泡沫的存在，会挤占分离器的气相空间，严重影响气液分离效果，增加了分离时间；大量泡沫的存在还会导致原油冒罐。
因此，测试CO 2驱采出泡沫流体性能、优化提升消泡分离技术以及提供比较全面合理的分离效果评价方法，能够为后续油气集输处理设备的安全运行提供有力保障，为CO 2驱油田开发提供重要的技术支撑，通过对CO 2驱采出泡沫流体性能的测量分析可以较为明确的得到如何进行油气混合，通过对消泡分离效果的测试可以得到消泡分离效果，并对分离器进行相应方向的改进，优化提升分离器内的消泡分离效果。
现有技术中对泡沫流体的分析不足，第一、没有定量解决CO 2气体与油水混合液体的混合比例对泡沫性能以及消泡分离时的影响，第二、其测量手段较为单一，仅考虑一种分离装置对消泡分离效果的影响，第三、现有技术中存在未解决的多余变量的输入对泡沫流体产生过程的影响，第四、未对CO 2驱采出液在气液分离过程中出现的特殊问题进行重点研究。
发明内容
本公开为了解决上述问题，提出一种测试泡沫流体性能和消泡分离效果的实验装置及方法。
本公开的第一目的是提供一种一种测试泡沫流体性能和消泡分离效果的实验装置，该实验装置将产生并充分发展的泡沫流体进行性能测量以及消泡分离效果的评估。
本公开的第二目的是提供一种可以产生不同气液混合比例的流体泡沫的泡沫发生模块，且使一个实验装置能够在不同条件下测量不同气液混合比例的流体泡沫。
本公开的第三目的是提供一种一种测试泡沫流体性能和消泡分离效果的实验装置的实验方法，按照实验方法可以准确方便的测量泡沫流体的性能和消泡分离效果。
为实现上述目的，本公开采用如下技术方案：
一种测试泡沫流体性能和消泡分离效果的实验装置，包括用于产生泡沫流体的泡沫发生模块、用于输送泡沫流体并使泡沫流体在环道内充分发展的实验环道，用于测试泡沫流体性能的泡沫性能测试模块，用于泡沫与流体、气体分离的泡沫分离处理模块以及用于测试评估消泡结果的消泡结果评估模块，泡沫发生模块末端连接实验环道，在泡沫发生模块同时输入 油水混合液体和CO 2气体并混合成不同比例的油水和气体形成泡沫流体，混合后形成的泡沫流体输送至实验环道内，由实验环道分别输送至实验环道末端的泡沫性能测试模块、泡沫分离处理模块内，在泡沫性能测试模块内，对从实验环道内输入的充分发展的泡沫流体测量分析获得泡沫流体的泡沫体积，泡沫半衰期以及泡沫质量，在泡沫分离处理模块内，将从实验环道内输入的充分发展的泡沫流体分离为气体和液体，泡沫分离处理模块上设置消泡结果评估模块，消泡结果评估模块对泡沫分离处理模块分离后的气体进行分析，获得气中含液率、气中液滴粒径、气中含油量。
进一步的，泡沫发生模块包括：油水混合釜、CO 2气瓶以及泡沫发生装置，泡沫发生装置通过连接管路连接油水混合釜、CO 2气瓶，油水混合釜至泡沫发生装置的连接管路上按照液体流动方向依次设置有第二离心泵和第一流量计，CO 2气瓶至泡沫发生装置的连接管路上按照气体流动方向依次设置有储气罐、第一气相流量计，被第二离心泵控制的油水混合釜中的油水混合液体和被第一流量计计算的CO 2气瓶中的CO 2气体通过泡沫发生装置底部的液相管路入口和泡沫发生装置侧壁的气相管路入口进入泡沫发生装置内部，形成不同气液混合比例的泡沫流体。
作为优选的，泡沫发生装置内部设置有带网孔的不锈钢丝网，泡沫发生装置的气相管路入口和液相管路入口在空间上呈90°布置，并在液相管路入口上方布设一层保温纤维，保温纤维布设在泡沫发生装置内部，一方面，被加温的气体进入泡沫发生装置内部混合油水液产生泡沫流体，产生的泡沫流体同样需要保温，另一方面，保温纤维内分布着若干纤维刺，油水混合液体由第二离心泵泵入泡沫发生装置内部，这些油水混合液体在管路中相互碰撞使油水混合液体携带有大量气泡以及泡沫，保温纤维可以减少油水混合液体内气泡和泡沫的携带量。
进一步的，泡沫性能测试模块包括分析罐，分析罐下端设置有液相出口，分析罐侧壁设置有气体出口，气体出口向外依次安装第一吸收盒、第一取样阀，第一吸收盒内放置有吸水吸油材料，测量第一吸收盒内吸水吸油材料前后的质量差，第一取样阀通过管路连接气体收集袋，分析罐为可视化罐体，罐体侧壁上设置有标准刻度。
进一步的，泡沫分离处理模块包括卧式分离器，卧式分离器为可视化罐体，罐体侧壁上设置有标准刻度，卧式分离器下端设置有液相出口，卧式分离器下端外周包覆有第二加热套，卧式分离器上端设置有气相出口，气相出口连接消泡结果评估模块，卧式分离器的上端还设置有管柱式旋流分离器，管柱式旋流分离器下端连通卧式分离器，实验环道末端主管路上还设置有第三旁通管路，第三旁通管路连接管柱式旋流分离器，泡沫流体经过实验环道的第三旁通管路进入管柱式旋流分离器，再由管柱式旋流分离器流入卧式分离器中，管柱式旋流分离器的泡沫流体入口处设置气相出口，管柱式旋流分离器的气相出口通过气管连通至卧式分离器的气相出口，卧式分离器的气相出口连接消泡结果评估模块，其提供了直接进入卧式分离器分离和先进入管柱式旋流分离器后进入卧式分离器分离两种不同的分离装置，这代表了单个分离装置以及预先分离再分离两种不同的处理思路，根据测量后的消泡分离效果可以选择两者中更好的分离方法。
进一步的，消泡结果评估模块包括液滴粒径观察视窗以及液滴粒径观察视窗末端的第二 吸收盒，泡沫分离处理模块分离后的气体依次经过液滴粒径观察视窗、第二吸收盒，第二吸收盒出口设置有两条管路，第一条管路连通大气，第一条管路上设置有第二气相流量计，第二条管路上设置有第二取样阀，第二取样阀通过气管连接气体收集袋，第二吸收盒内放置有吸水吸油材料。
作为优选的，本公开可以通过对吸水吸油材料在实验前后称重得到质量差；对卧式分离器气相出口处的第二气相流量计的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器的泡沫层进行拍摄，完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器气相出口处的液滴粒径观察视窗进行检测实现对重力沉降区的液滴粒径进行分析，对泡沫分离处理模块中分离前后的压力差进行计算，计算出分离时的压差。
利用上述公开的技术方案，本公开提供一种用于测试泡沫流体性能和消泡分离效果的实验方法：
第一步：准备阶段：将CO 2气体通入整个实验装置中，清除管内杂质；
第二步：产生泡沫流体阶段：将所需气体流量的CO 2气体通入泡沫发生装置中，同时将所需液体流量的油水混合液体输送至泡沫发生装置中，在泡沫发生装置内混合并产生泡沫流体；
第三步：泡沫流体输送阶段：泡沫流体进入实验环道，连通第一旁通管路，排出不稳定且没有充分发展的泡沫，待泡沫流体输出稳定后，连通第二旁通管路，将泡沫流体输入至泡沫性能测试模块中；
第四步：泡沫流体消泡阶段：连通实验环道末端的主管路，泡沫流体进入卧式分离器，直到泡沫流体液面达到分离器一半高度时，关闭泡沫流体输入，使泡沫流体不再进入卧式分离器中；
第五步：测试阶段：测量泡沫性能测试模块内的泡沫体积，分析泡沫半衰期以及测量泡沫质量；通过对吸水吸油材料在实验前后称重得到质量差；对卧式分离器气相出口处的第二气相流量计的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器的泡沫层进行拍摄，完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器气相出口处的液滴粒径观察视窗进行检测实现对重力沉降区的液滴粒径进行分析，对泡沫分离处理模块中分离前后的压力差进行计算，计算出分离时的压差。
进一步的，在泡沫流体消泡阶段，本公开提供另一种消泡方法，通过连通第三旁通管路，泡沫流体进入管柱式旋流分离器后再进入卧式分离器，直到泡沫流体液面达到分离器一半高度时，关闭泡沫流体输入，使泡沫流体不再进入卧式分离器中。
与现有技术相比，本公开的有益效果为：
1.本公开的泡沫发生模块能够通过输入气体和液体比例的不同产生不同比例的泡沫流体，针对不同的泡沫流体的输送、性能及消泡分离效果进行测量评估。
2、本公开的泡沫发生装置能够在不锈钢丝网的作用下将气体和液体进行静态混合，避免搅拌叶轮等动态混合装置对泡沫流体状态的影响。
3、本公开的泡沫发生装置的液相管路入口上方布设一层保温纤维，保温纤维布设在泡沫发生装置内部，减少油水混合液体内气泡和泡沫的携带量且为油水混合液体提供保温。
4、本公开的实验环道可以使泡沫流体充分发展，并将充分发展后的泡沫流体输送至相应 的测量装置内。
5、本公开提供两种消泡分离的思路，并可以分别进行实验测量，本套实验测试装置对CO 2驱采出液在气液分离过程中出现的特殊问题进行研究具有重要意义，能够有针对性的对传统分离器进行结构优化，测试预期气液分离效果，为油田气液分离器的设计、运行提供参考。
6、本公开可以模拟开展可视化含CO 2驱采出流体的泡沫性能测试、分离器消泡构件优化、消泡分离效果评估。
附图说明
构成本申请的一部分的说明书附图用来提供对本申请的进一步理解，本申请的示意性实施例及其说明用于解释本申请，并不构成对本申请的不当限定。
图1为本公开的测量泡沫流体性能和消泡分离效果的实验装置的结构示意图。
其中：1、水箱，2、第一离心泵，3、第一阀门，4、第一温度传感器，5、油水混合釜，6、第二阀门，7、第三阀门，8、第二离心泵，9、第四阀门，10、第一液相流量计，11、第五阀门，12、CO 2气瓶，13、第六阀门，14、第七阀门，15、第一压力传感器，16、第二温度传感器，17、储气罐，18、第一加热套，19、第八阀门，20、第九阀门，21、第二压力传感器，22、第一气相流量计，23、第十阀门，24、泡沫发生装置，25、第十一阀门，26、第十二阀门，27、分析罐，28、第三压力传感器，29、第一吸收盒，30、第一取样阀，31、第十三阀门，32、第十四阀门，33、第十五阀门，34、第四压力传感器，35、第十六阀门，36、第五压力传感器，37、第六压力传感器，38、第十七阀门，39、第七压力传感器，40、卧式分离器，41、第二加热套，42、第十八阀门，43、液滴粒径观察视窗，44、第二吸收盒，45、第十九阀门，46、第二气相流量计，47、第二取样阀，48、第二十阀门，49、第二十一阀门，50、实验环道，51、第三温度传感器，52、管柱式旋流分离器；
100、泡沫发生模块，200、泡沫性能测试模块，300、泡沫分离处理模块，400、消泡结果评估模块。
具体实施方式：
下面结合附图与实施例对本公开作进一步说明。
应该指出，以下详细说明都是例示性的，旨在对本申请提供进一步的说明。除非另有指明，本文使用的所有技术和科学术语具有与本申请所属技术领域的普通技术人员通常理解的相同含义。
需要注意的是，这里所使用的术语仅是为了描述具体实施方式，而非意图限制根据本申请的示例性实施方式。如在这里所使用的，除非上下文另外明确指出，否则单数形式也意图包括复数形式，此外，还应当理解的是，当在本说明书中使用术语“包含”和/或“包括”时，其指明存在特征、步骤、操作、器件、组件和/或它们的组合。
在本公开中，术语如“上”、“下”、“左”、“右”、“前”、“后”、“竖直”、“水平”、“侧”、“底”等指示的方位或位置关系为基于附图所示的方位或位置关系，只是为了便于叙述本公开各部件或元件结构关系而确定的关系词，并非特指本公开中任一部件或元件，不能理解为对本公开的限制。
本公开中，术语如“固接”、“相连”、“连接”等应做广义理解，表示可以是固定连 接，也可以是一体地连接或可拆卸连接；可以是直接相连，也可以通过中间媒介间接相连。对于本领域的相关科研或技术人员，可以根据具体情况确定上述术语在本公开中的具体含义，不能理解为对本公开的限制。
实施例1
本公开提供一种测试泡沫流体性能和消泡分离效果的实验装置，用于测试评价CO 2驱采出流体在集输分离中的泡沫性能及消泡分离效果，该实验装置包括用于产生泡沫流体的泡沫发生模块100、用于输送泡沫流体并使泡沫流体在环道内充分发展的实验环道50，用于测试泡沫流体性能的泡沫性能测试模块200，用于泡沫与流体、气体分离的泡沫分离处理模块300以及用于测试评估消泡结果的消泡结果评估模块400，在此详细说明：
泡沫发生模块100，产生泡沫流体用于模拟真实工作下CO 2与油层呈一定比例混合后产生的泡沫流体，泡沫发生模块100包括油水混合釜5、连接CO 2气瓶12的储气罐17以及与油水混合釜5、储气罐17连接的泡沫发生装置24。
油水混合釜5中安装有变频搅拌电机和可控制加热温度的加热棒，油水混合釜5上端的釜盖上设置有液相回流入口，液相回流入口上设置有第三阀门7，用于将测试结束后的液体重新循环至油水混合釜5中，使液体能够被循环利用。油水混合釜5的釜体上安装有第一温度传感器4，第一温度传感器4用于测量釜内液体温度并实时获取和显示，釜底安装排污口，排污口上安装第一阀门3，打开第一阀门3即可将油水混合釜5内的液体排放至外界进行下一步处理，油水混合釜5下端出液口与泡沫发生装置24底部的液相管路入口之间的连接管路上依次安装有第二阀门6、第二离心泵8、第四阀门9、第一液相流量计10、第五阀门11，打开第二阀门6、第二离心泵8、第四阀门9、第五阀门11，关闭第一阀门3，在第二离心泵8的作用下将油水混合釜5内的液体抽至泡沫发生装置24内，油水混合釜5通过第一离心泵2从水箱内抽水，在油水混合釜5内形成不同油水配比的液体。
CO 2气瓶12中的气体通过输气管路输送至储气罐17中，使CO 2气瓶12中的高压气体通过扩容成为稳定压力下的CO 2气体，储气罐17下端包覆有第一加热套18，用于对储气罐17内的气体进行升温，使储气罐17能够提供不同温度的气体，储气罐17上安装有第一压力传感器15和第二温度传感器16，用于实时检测储气罐17内气体的压力和温度，CO 2气瓶和储气罐17之间依次安装有第六阀门13和第七阀门14，第六阀门13安装在CO 2气瓶和储气罐17之间的输气主管路上，第七阀门14安装在输气主管路上的旁路上，打开第六阀门13，关闭第七阀门14，CO 2气瓶中的气体进入储气罐，关闭第六阀门13，打开第七阀门14，CO 2气瓶中的气体排入大气，储气罐17内的气体经过第八阀门19、第九阀门20、第一气相流量计22，第十阀门23进入泡沫发生装置24中，第九阀门20、第一气相流量计22之间的输气管路上安装第二压力传感器21，用于检测储气罐17输入至泡沫发生装置24的气体的压力。
泡沫发生装置24用于使气液两相在不同条件下混合搅动形成泡沫流体，该装置外形整体呈圆柱体型，内部腔室为圆柱形腔体，泡沫发生装置24上开设的气相管路入口用于进CO 2气体，该气相管路入口与储气罐17连接，气相管路入口优选的开设在泡沫发生装置24的侧壁上，泡沫发生装置24下端开设液相管路入口，用于与油水混合釜5相连，气相管路入口和液相管路入口在空间上呈90°，并在泡沫发生装置24内填充满带孔的不锈钢丝网，泡沫发生 装置24内通入液体和气体并在不锈钢丝网的作用下充分混合并产生泡沫流体，经由泡沫发生装置24底部的混合相出口进入实验环道50，在泡沫发生装置24内完成不同压力、温度、流量等条件下的气体和不同温度、流量等条件下的液体的混合，形成多种不同的泡沫流体并输出。
泡沫发生装置24的液相管路入口上方布设一层保温纤维，保温纤维布设在泡沫发生装置内部，一方面，被加温的气体进入泡沫发生装置内部混合油水液产生泡沫流体，产生的泡沫流体同样需要保温，另一方面，保温纤维内分布着若干纤维刺，油水混合液体由第二离心泵泵入泡沫发生装置内部，这些油水混合液体在管路中相互碰撞使油水混合液体携带有大量气泡以及泡沫，保温纤维可以大幅减少油水混合液体内气泡和泡沫的携带量。
本公开的实验环道50用于输送泡沫流体至泡沫性能测试模块200以及泡沫分离处理模块300内并使泡沫流体在实验环道50内发展，实验环道50的起点自泡沫发生装置24的混合相出口开始计算，结束点位于通往泡沫分离处理模块300的混合相入口，实验环道50设置为可视化管道，用于观察实验环道50内泡沫流体的状态以及观察不同流型和泡沫的相互作用，实验环道50的末端主管道设置有两条旁通管路，按照泡沫流体在实验环道50内的流动方向依次为第一旁通管路、第二旁通管路。
第一旁通管路上安装第十一阀门25，仅打开第十一阀门25时，仅第一旁通管路开启，将实验装备阶段实验环道50内没有充分发展且没有稳定的泡沫流体排出，这些泡沫流体因没有充分发展导致泡沫流体的前期测试和评估没有意义；第二旁通管路连接泡沫性能测试模块200，第二旁通管路上安装第十二阀门26，待泡沫流体充分发展后，打开第十二阀门26，将充分发展后的泡沫流体输送至泡沫性能测试模块200，进而对泡沫流体的性能进行分析测试。
泡沫性能测试模块200，用于对实验环道50第二旁通管路输出的泡沫流体进行测试分析，包括分析罐27，该分析过程在泡沫消泡分离处理前，分析罐27位于泡沫分离处理模块300前，在分析罐27中测试泡沫性能包括泡沫体积，泡沫半衰期以及泡沫质量，泡沫性能测试模块200包括分析罐27，分析罐27采用可视化的带有标准刻度的分析罐27，实验环道50发展后的泡沫流体经第二旁通管路进入分析罐27中，通过分析罐27上的刻度读出泡沫体积，分析罐27侧壁安装气体出口，分析罐27的气体出口向外依次安装第一吸收盒29、第十三阀门31，第一吸收盒29、第十三阀门31之间的主管路安装有第一取样阀30，第一吸收盒29内置有吸水吸油材料，第十三阀门31将分析罐27内的气体排入大气。通过第一取样阀30使分析罐27内的气体经过管路进入气体收集袋，第一取样阀30后的管路优先采用橡胶软管，分析罐27下端安装液体出口，液体出口上安装第十四阀门32，打开第十四阀门32，将分析罐27内的液体再次排入油水混合罐5中，实现液体的重复利用。
泡沫分离处理模块300包括一个可视化的卧式分离器40，卧式分离器40内部可进行多种消泡分离构件的安装拆卸，通过不同消泡分离构件的组合得到不同的泡沫分离处理，卧式分离器40上具有标准刻度，泡沫分离处理模块300的泡沫分离处理方式为：泡沫流体经过实验环道50的末端主管路直接进入卧式分离器40，通过卧式分离器40上的刻度对泡沫体积进行计量，卧式分离器40下端包覆有第二加热套41，用于对卧式分离器40内的泡沫流体进行加热，卧式分离器40的上端安装气相出口，卧式分离器40上安装的第三温度传感器51、第 七压力传感器39用于测量卧式分离器40内的温度，另外，卧式分离器40下端安装有液相出口，液相出口上安装第十八阀门42，打开第十八阀门42，将分离后的液体输入至油水混合釜5中，实现液体的循环使用。
消泡结果评估模块400对泡沫分离处理模块300出口处进行观测、吸收、收集和计量，用于完成对消泡分离结果的分析，包括泡沫分离处理模块300气相出口处的液滴粒径观察视窗43和液滴粒径观察视窗43末端安装的第二吸收盒44，泡沫分离处理模块300气相出口指卧式分离器40和管柱式旋流分离器52的气相出口汇集后的总气相出口，第二吸收盒44内同样内置吸水吸油材料，第二吸收盒44出口处具有两条管路，第一条管路上按照气体流动顺序依次安装有第十九阀门45、第二气相流量计46，气体通过这条管路排入大气中，该管路目的在于通过第二气相流量计46测量通过第一条管路的气体流量，第二条管路安装有第二十阀门48和第二取样阀47，第二取样阀47通过气管连接气体收集袋，该气管优选采用橡胶软管，打开第二十阀门48可以将气体排入大气中。
卧式分离器40排出的液体和分析罐27排出的液体经过一根管路通往第二离心泵8，该管路上设置有第二十一阀门49，打开第三阀门7，在第二离心泵8的带动下将卧式分离器40排出的液体和分析罐27排出的液体通过油水混合釜5上的液相回流入口重新循环进入油水混合釜5，完成液体循环。
上述部分阀门可采用多种类型或型号的阀门，其中第一阀门3、第二阀门6，第三阀门7、第十一阀门25、第十二阀门26、第十三阀门31、第十四阀门32、第十五阀门33、第十七阀门38、第十八阀门42、第十九阀门45、第二十阀门48、第二十一阀门49均优先采用球阀，用于实现对相应的管路的开通和关闭，另外，还有部分较为特殊的阀门，其仅能采用同功能类型的阀门，第四阀门9采用闸阀使第二流量泵8泵入泡沫发生装置24的流体只能实现流通或不流通，无法实现流量的调节，第五阀门11采用止回阀，防止流体流回第一液相流量计10处，第四阀门9采用的闸阀和第五阀门11采用的止回阀两个阀门配合使第一液相流量计10准确测量的便为第二流量泵8泵入泡沫发生装置24的流体的流量，不受阀门流量调节和回流对流体流量测量的影响，第六阀门13采用减压阀，将CO 2气瓶的出口压力减至需要的压力，并依靠CO 2本身的能量，使压力自动保持稳定，使CO 2以稳定压力进入储气罐17中，第七阀门14采用放空阀，第八阀门19采用减压阀，第十阀门20采用针阀，第十一阀门23采用止回阀，三种阀门配合储气罐17使用使第二压力传感器21、第一气相流量计22所测量的压力和气体流量都非常准确，避免气流不稳定造成的测量结果的不准确。
本公开所记载的气体收集袋为多个，用于收集多个气体出口的气体，避免气体混合在一个气体收集袋中。
上述的所有的压力传感器、液相流量计、气相流量计、温度传感器等均接入数据采集系统中，对压力、温度、流量等进行准确收集并记录。
实施例2
本公开的泡沫分离处理模块300采用第二种技术方案，其在实施例1的基础上增设管柱式旋流分离器52，管柱式旋流分离器52安装在卧式分离器40上端，实验环道50的末端主管道设置有三条旁通管路，并按照泡沫流体在实验环道50内的流动方向依次为第一旁通管路、 第二旁通管路、第三条旁通管路，第三旁通管路连接泡沫分离处理模块300内的管柱式旋流分离器52，第三旁通管路上安装第十六阀门35，第十六阀门35与管柱式旋流分离器52之间的第三旁通管路上安装有第五压力传感器36，打开第十六阀门35，泡沫流体通过第三旁通管路进入管柱式旋流分离器52内，实验环道50的末端主管道接入卧式分离器40内，实验环道50的末端主管道上安装有第十五阀门33，第四压力传感器34安装在第十五阀门33和卧式分离器40之间的主管道上，第十六阀门35采用球阀。
泡沫分离处理模块300的泡沫分离处理方式为：泡沫流体经过实验环道50的第三旁通管路进入管柱式旋流分离器52，再由管柱式旋流分离器52流入卧式分离器40中，管柱式旋流分离器52上安装有第六压力传感器37，管柱式旋流分离器52用于进泡沫流体的入口处安装有气相出口，管柱式旋流分离器52的气相出口通过气管连通至卧式分离器40的气相出口处，该气管上安装第十七阀门38。
上述的所有的压力传感器、液相流量计、气相流量计、温度传感器等均接入数据采集系统中，对压力、温度、流量等进行准确收集并记录。
本公开可以根据不同程度的油品发泡情况，选取实施例一和实施例二所记载的两种不同入口和不同消泡构件对消泡分离测试结果的影响。
实施例3
本公开提供一种用于测试泡沫流体性能和消泡分离效果的实验方法，利用本公开的实施例一公开的实验装置进行测量，实验操作过程如下：
第一步：准备阶段：将CO 2气瓶中的CO 2气体输送至储气罐17中，CO 2气体由储气罐17通入整个实验装置中，清除管内杂质，调整卧式分离器40的阀门开启状态，其中，开启卧式分离器40的气相出口，关闭卧式分离器40的液相出口。
第二步：产生泡沫流体阶段：调节第八阀门19，将CO 2气体调节至所需气体流量，CO 2气体通入泡沫发生装置24中，同时打开油水混合釜5下端的第二球阀6，关闭第三球阀7，开启第二离心泵8和第四阀门9，根据第二离心泵8的输出功率将所需流量的液体输送至泡沫发生装置24中，该液体为油水混合物，设计流量的CO 2气体和设计流量的液体在泡沫发生装置24内混合并产生泡沫流体。
第三步：泡沫流体输送阶段：泡沫流体进入实验环道50，先打开第十一阀门25，排出不稳定且没有充分发展的泡沫，待泡沫流体输出稳定后，关闭第十一阀门25，开启第十二阀门26，将泡沫流体输入至分析罐27中，等待指定时间后关闭第十二阀门26。
第四步：泡沫流体消泡阶段：关闭第十二阀门26的同时打开第十五阀门33，使泡沫流体进入卧式分离器40，直到泡沫流体液面达到分离器一半高度时，关闭第八阀门19、第九阀门20和第二阀门6、第四阀门9以及第十五阀门33，使CO 2气体和油水混合液体均不再输入泡沫发生装置24，且泡沫流体不再进入卧式分离器40中。
第五步：测试阶段：在分析罐27中测试泡沫性能，包括通过刻度读取泡沫体积，在分析罐27内分析泡沫半衰期以及测量泡沫质量；通过对第一吸收盒29、第二吸收盒44内吸水吸油材料在实验前后称重得到质量差；对卧式分离器40气相出口处的第二气相流量计46的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器40的泡沫层进行拍摄， 完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器40气相出口处的液滴粒径观察视窗43进行检测实现对重力沉降区的液滴粒径进行分析，对分离前后的第七压力传感器39测量的压力计算分离时的压差
第六步：液体回收阶段：实验结束后，打开第十八阀门42、第十四阀门32、第二十一阀门49和第三阀门7，启动第二离心泵8，将分析罐27和卧式分离器10内的液体抽回油水混合釜5中。
实施例4
本公开提供一种用于测试泡沫流体性能和消泡分离效果的实验方法，利用本公开的实施例二公开的实验装置进行测量，实验操作过程如下：
第一步：准备阶段：将CO 2气瓶中的CO 2气体输送至储气罐17中，CO 2气体由储气罐17通入整个实验装置中，清除管内杂质，调整卧式分离器40的阀门开启状态，其中，开启卧式分离器40的气相出口，关闭卧式分离器40的液相出口。
第二步：产生泡沫流体阶段：调节第八阀门19，将CO 2气体调节至所需气体流量，CO 2气体通入泡沫发生装置24中，同时打开油水混合釜5下端的第二球阀6，关闭第三球阀7，开启第二离心泵8和第四阀门9，根据第二离心泵8的输出功率将所需流量的液体输送至泡沫发生装置24中，该液体为油水混合物，设计流量的CO 2气体和设计流量的液体在泡沫发生装置24内混合并产生泡沫流体。
第三步：泡沫流体输送阶段：泡沫流体进入实验环道50，先打开第十一阀门25，排出不稳定且没有充分发展的泡沫，待泡沫流体输出稳定后，关闭第十一阀门25，开启第十二阀门26，将泡沫流体输入至分析罐27中，等待指定时间后关闭第十二阀门26。
第四步：泡沫流体消泡阶段：关闭第十二阀门26的同时打开第十六阀门35，使泡沫流体进入管柱式旋流分离器52，并通过管柱式旋流分离器52进入卧式分离器40，直到泡沫流体液面达到分离器一半高度时，关闭第八阀门19、第九阀门20和第二阀门6、第四阀门9以及第十五阀门33，使CO 2气体和油水混合液体均不再输入泡沫发生装置24，且泡沫流体不再进入卧式分离器40中。
第五步：测试阶段：在分析罐27中测试泡沫性能，包括通过刻度读取泡沫体积，计算泡沫半衰期以及测量泡沫质量；通过对第一吸收盒29、第二吸收盒44内吸水吸油材料在实验前后称重得到质量差；对卧式分离器40气相出口处的第二气相流量计46的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器40的泡沫层进行拍摄，完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器40气相出口处的液滴粒径观察视窗43进行检测实现对重力沉降区的液滴粒径进行分析；通过第五压力传感器36、第六压力传感器37、第七压力传感器39分离前后的压力计算分离时的压差。
第六步：液体回收阶段：实验结束后，打开第十八阀门42、第十四阀门32、第二十一阀门49和第三阀门7，启动第二离心泵8，将分析罐27和卧式分离器10内的液体抽回油水混合釜5中。
以上仅为本申请的优选实施例而已，并不用于限制本申请，对于本领域的技术人员来说，本申请可以有各种更改和变化。凡在本申请的精神和原则之内，所作的任何修改、等同替换、改进等，均应包含在本申请的保护范围之内。
上述虽然结合附图对本公开的具体实施方式进行了描述，但并非对本公开保护范围的限制，所属领域技术人员应该明白，在本公开的技术方案的基础上，本领域技术人员不需要付出创造性劳动即可做出的各种修改或变形仍在本公开的保护范围以内。

Claims (10)

  1. 一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，包括泡沫发生模块、实验环道、泡沫性能测试模块、泡沫分离处理模块、消泡结果评估模块；
    所述泡沫发生模块末端连接实验环道，泡沫发生模块混合不同比例的油水和CO 2气体形成泡沫流体，并将泡沫流体输送至实验环道内；
    所述实验环道内部的泡沫流体分别输送至实验环道末端的泡沫性能测试模块、泡沫分离处理模块；
    所述泡沫性能测试模块接收实验环道内充分发展的泡沫流体并分析泡沫流体的泡沫体积，泡沫半衰期以及泡沫质量；
    所述泡沫分离处理模块接收实验环道内充分发展的泡沫流体并将泡沫流体分离为气体和液体；
    所述泡沫分离处理模块上设置有消泡结果评估模块，消泡结果评估模块对泡沫分离处理模块分离后的气体进行分析，获得气中含液率、气中液滴粒径、气中含油量。
  2. 如权利要求1所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述泡沫发生模块包括：油水混合釜、CO 2气瓶以及泡沫发生装置，泡沫发生装置通过两条连接管路分别连接油水混合釜、CO 2气瓶；
    所述油水混合釜至泡沫发生装置的连接管路上按照液体流动方向依次设置有第二离心泵和第一流量计，所述CO 2气瓶至泡沫发生装置的连接管路上按照气体流动方向依次设置有储气罐、第一气相流量计，油水混合釜中的油水混合液体和CO 2气瓶中的CO 2气体通过泡沫发生装置底部的液相管路入口和泡沫发生装置侧壁的气相管路入口进入泡沫发生装置内部。
  3. 如权利要求2所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述泡沫发生装置内部设置有带网孔的不锈钢丝网；
    所述泡沫发生装置的气相管路入口和液相管路入口在空间上呈90°布置。
  4. 如权利要求2所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述泡沫发生装置连接实验环道，所述实验环道的末端按照泡沫流体流动方向依次设置有第一旁通管路、第二旁通管路，实验环道末端的主管路连接泡沫分离处理模块；
    所述第一旁通管路连接大气，排出实验环道内未充分发展的泡沫流体；
    所述第二旁通管路连接泡沫性能测试模块，将实验环道内充分发展的泡沫流体排入泡沫性能测试模块。
  5. 如权利要求1所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述泡沫性能测试模块包括分析罐，分析罐下端设置有液相出口，分析罐侧壁设置有气体出口，气体出口向外依次安装第一吸收盒、第一取样阀，第一吸收盒内放置有吸水吸油材料，第一取样阀通过管路连接气体收集袋；
    所述分析罐为可视化罐体，罐体侧壁上设置有标准刻度。
  6. 如权利要求4所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，泡沫分离处理模块包括卧式分离器，所述卧式分离器为可视化罐体，罐体侧壁上设置有标准刻度；
    所述卧式分离器下端设置有液相出口，卧式分离器下端外周包覆有第二加热套，卧式分离器上端设置有气相出口，所述卧式分离器上的气相出口连接消泡结果评估模块；
    所述卧式分离器的上端还设置有管柱式旋流分离器，管柱式旋流分离器下端连通卧式分离器，所述实验环道末端主管路上还设置有第三旁通管路，第三旁通管路连接管柱式旋流分离器，泡沫流体经过实验环道的第三旁通管路进入管柱式旋流分离器，再由管柱式旋流分离器流入卧式分离器中；
    管柱式旋流分离器的泡沫流体入口处设置气相出口，管柱式旋流分离器的气相出口通过气管连通至卧式分离器的气相出口；
    所述卧式分离器的气相出口连接消泡结果评估模块。
  7. 如权利要求6所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述消泡结果评估模块包括液滴粒径观察视窗以及液滴粒径观察视窗末端的第二吸收盒；
    所述泡沫分离处理模块分离后的气体依次经过液滴粒径观察视窗、第二吸收盒，第二吸收盒出口设置有两条管路，第一条管路连通大气，第一条管路上设置有第二气相流量计，第二条管路上设置有第二取样阀，第二取样阀通过气管连接气体收集袋；
    所述第二吸收盒内放置有吸水吸油材料。
  8. 如权利要求2所述的一种测试泡沫流体性能和消泡分离效果的实验装置，其特征是，所述的油水混合釜的釜盖上设置有液相回流入口，泡沫性能测试模块和泡沫分离处理模块中剩余的液体循环流回油水混合釜内部。
  9. 如权利要求7所述的一种测试泡沫流体性能和消泡分离效果的实验装置的实验方法，其特征是，
    第一步：准备阶段：将CO 2气体通入整个实验装置中，清除管内杂质；
    第二步：产生泡沫流体阶段：将所需气体流量的CO 2气体通入泡沫发生装置中，同时将所需液体流量的油水混合液体输送至泡沫发生装置中，在泡沫发生装置内混合并产生泡沫流体；
    第三步：泡沫流体输送阶段：泡沫流体进入实验环道，连通第一旁通管路，排出不稳定且没有充分发展的泡沫，待泡沫流体输出稳定后，连通第二旁通管路，将泡沫流体输入至泡沫性能测试模块中；
    第四步：泡沫流体消泡阶段：连通实验环道末端的主管路，泡沫流体进入卧式分离器，直到泡沫流体液面达到分离器一半高度时，关闭泡沫流体输入，使泡沫流体不再进入卧式分离器中；
    第五步：测试阶段：测量泡沫性能测试模块内的泡沫体积，分析泡沫半衰期以及测量泡沫质量；通过对吸水吸油材料在实验前后称重得到质量差；对卧式分离器气相出口处的第二气相流量计的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器的泡沫层进行拍摄，完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器气相出口处的液滴粒径观察视窗进行检测实现对重力沉降区的液滴粒径进行分析，对泡沫分离处理模块中分离前后的压力差进行计算，计算出分离时的压差。
  10. 如权利要求7所述的一种测试泡沫流体性能和消泡分离效果的实验装置的实验方法，其特征是，
    第一步：准备阶段：将CO 2气体通入整个实验装置中，清除管内杂质；
    第二步：产生泡沫流体阶段：将所需气体流量的CO 2气体通入泡沫发生装置中，同时将所需液体流量的油水混合液体输送至泡沫发生装置中，在泡沫发生装置内混合并产生泡沫流体；
    第三步：泡沫流体输送阶段：泡沫流体进入实验环道，连通第一旁通管路，排出不稳定且没有充分发展的泡沫，待泡沫流体输出稳定后，连通第二旁通管路，将泡沫流体输入至泡沫性能测试模块中；
    第四步：泡沫流体消泡阶段：连通第三旁通管路，泡沫流体进入管柱式旋流分离器后再进入卧式分离器，直到泡沫流体液面达到分离器一半高度时，关闭泡沫流体输入，使泡沫流体不再进入卧式分离器中；
    第五步：测试阶段：测量泡沫性能测试模块内的泡沫体积，分析泡沫半衰期以及测量泡沫质量；通过对吸水吸油材料在实验前后称重得到质量差；对卧式分离器气相出口处的第二气相流量计的示数读取可计算出分离后的气中含液率；使用高速摄像装置对卧式分离器的泡沫层进行拍摄，完成对气泡粒径分布的统计；使用激光粒度分析仪对卧式分离器气相出口处的液滴粒径观察视窗进行检测实现对重力沉降区的液滴粒径进行分析，对泡沫分离处理模块中分离前后的压力差进行计算，计算出分离时的压差。
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