CN106814177A - The test device and method of a kind of gas physical parameter in super-viscous oil - Google Patents

The test device and method of a kind of gas physical parameter in super-viscous oil Download PDF

Info

Publication number
CN106814177A
CN106814177A CN201611177620.8A CN201611177620A CN106814177A CN 106814177 A CN106814177 A CN 106814177A CN 201611177620 A CN201611177620 A CN 201611177620A CN 106814177 A CN106814177 A CN 106814177A
Authority
CN
China
Prior art keywords
gas
super
viscous oil
physical parameter
unit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201611177620.8A
Other languages
Chinese (zh)
Other versions
CN106814177B (en
Inventor
张胜飞
金瑞凤
王超
王福顺
徐振华
沈德煌
李秀峦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Natural Gas Co Ltd
Original Assignee
China Petroleum and Natural Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum and Natural Gas Co Ltd filed Critical China Petroleum and Natural Gas Co Ltd
Priority to CN201611177620.8A priority Critical patent/CN106814177B/en
Publication of CN106814177A publication Critical patent/CN106814177A/en
Application granted granted Critical
Publication of CN106814177B publication Critical patent/CN106814177B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/22Fuels, explosives

Abstract

The invention provides the test device and method of a kind of gas physical parameter in super-viscous oil.The device includes:HTHP sample mixing unit, density measurement unit, viscosity measurement unit, sampling unit, solubility measuring unit;HTHP sample mixing unit is connected with density measurement unit, viscosity measurement unit, sampling unit, solubility measuring unit respectively;Sampling unit is connected with density measurement unit, viscosity measurement unit, solubility measuring unit respectively;HTHP sample mixing unit includes sample equipment, control device, and sample equipment is provided with charging aperture and outlet, and control device includes heater.Present invention also offers the method for testing of the gas physical parameter in super-viscous oil completed using said apparatus.Said apparatus and method can the parameter such as solubility, density, viscosity carries out steady testing in super-viscous oil to gas at high temperature under high pressure.

Description

The test device and method of a kind of gas physical parameter in super-viscous oil
Technical field
Join the present invention relates to the physical property such as the solubility of non-condensing gas in super-viscous oil and water under a kind of high-temperature and high-pressure conditions Several test devices and method, belongs to technical field of petroleum extraction.
Background technology
During Thermal Recovery For Viscous Oil By Steam, can play reduction heat loss with a certain amount of non-condensing gas of note, keep The effect of steam injection pressure, the row's of helping production fluid.The conventional non-condensing gas of agent for improving oilfield recovery have nitrogen, carbon dioxide, flue gas, Natural gas, air.After non-condensing gas injection oil reservoir, oil-gas ratio can be significantly improved, greatly improve the utilization rate of energy, and one Determine the recovery ratio of raising crude oil in degree.
But non-condensing gas lacks to the dissolving viscosity reduction of viscous crude, solution gas output, the specific effect for improving recovery ratio etc. to be had The data supporting of effect, it is impossible to carry out corresponding theoretical calculation and numerical simulation analysis, so that carrying out the experimental study of correlation.
Physical data of the non-condensing gas under Room-temperature low-pressure relatively enriches, but more deficient under the conditions of HTHP steam injection It is weary.As during SAGD, steam injecting temperature at 250 DEG C or so, in 4MPa or so under such Temperature-pressure Conditions surveyed by pressure Examination is, it is necessary to tester can simultaneously meet the requirement of high temperature and high pressure, but the PVT device for testing and analyzing of routine cannot all meet Experiment needs.
Conventional PVT device for testing and analyzing belongs to more accurate equipment, it is adaptable in conventional thin oil low-temperature test.Internal The volume of piston structure control test fluid, but need to complete dynamic sealing.And connect with profit under long-term high temperature, condition of high voltage Under tactile operating mode, common dynamic sealing will become fragile, unreliable, cause the failure of an experiment.
The content of the invention
In order to solve the above-mentioned technical problem, can be right under high temperature, condition of high voltage it is an object of the invention to provide one kind Gas parameter such as solubility, density, viscosity in super-viscous oil realizes the experimental provision of steady testing.
In order to realize above-mentioned technical purpose, the invention provides a kind of test dress of gas physical parameter in super-viscous oil Put, gas test device of physical parameter in super-viscous oil includes:HTHP sample mixing unit, density measurement unit, viscosity Measuring unit, sampling unit, solubility measuring unit;
Wherein, the HTHP sample mixing unit respectively with the density measurement unit, viscosity measurement unit, described Sampling unit, solubility measuring unit connection;
The sampling unit is single with the density measurement unit, the viscosity measurement unit, solubility measurement respectively Unit's connection;
The HTHP sample mixing unit include sample equipment, control device, the sample equipment be provided with charging aperture and Outlet, the control device includes heater.
In super-viscous oil in the test device of physical parameter, charging aperture is on the top of sample equipment for the gas provided in the present invention End, exports in the bottom of sample equipment.
In super-viscous oil in the test device of physical parameter, charging aperture is on the top of sample equipment for the gas provided in the present invention End, exports in the bottom of sample equipment so that after raw material enters from the charging aperture on top, is sufficiently mixed, promotes oil, gas phase to put down Weighing apparatus, is then sampled from the outlet of bottom, can directly obtain the oil sample containing saturation solution gas, using fluid-tight, avoids gas Outlet is scurried into, the accuracy of subsequent analysis is influenceed.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that HTHP sample mixing Unit also includes gas mass flow gauge, check valve, pressure gauge;Wherein, gas mass flow gauge is connected with sample equipment, pressure Table is arranged between check valve and gas mass flow gauge.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that sample equipment includes PID temperature controller, thermocouple and pressure sensor, sample equipment are provided with heat-insulation layer, and sample device interior is provided with stirring Block.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that PID temperature controller For adjusting the temperature in sample equipment, thermocouple is used to detect the temperature change of sample equipment, and pressure sensor is used to monitor The pressure change of sample equipment.
In the present invention, PID is a kind of temperature feedback control algorithm, refers to line integral differential.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that stirring block is to carry The metal derby of honeycomb hole.
Specific embodiment of the invention, realizes that sample equipment rotates by control device, sample device interior Stirring block can promote VLE;In sample equipment rotary course, metal derby is fallen by Action of Gravity Field, in honeycomb hole Gas is fully contacted with viscous crude, makes gas and the maximum saturation of viscous crude.
In super-viscous oil in the test device of physical parameter, sample equipment needs heating in advance to the gas provided in the present invention To desired temperature, can be heated by heating plate;Preferably, HTHP sample mixing unit include also include heating plate, plus Backing is arranged on the lateral wall of sample equipment.
The gas provided in the present invention in super-viscous oil in the test device of physical parameter, the thermocouple inspection in sample equipment Survey heater outlet, the temperature in sample equipment, and temperature value fed back into control device, the heater in control device according to The temperature value of feedback adjusts the heating-up temperature of heater.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that density measurement unit Including liquid metering device.
The gas provided in the present invention in super-viscous oil in the test device of physical parameter, it is highly preferred that liquid meter sets It is standby to include collection cups and balance, wherein, collection cups are used to collect the liquid that intermediate receptacle displacement goes out, and collection cups are placed on balance On.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that viscosity measurement unit Including rheometer.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that sampling unit includes Intermediate receptacle, pressure gauge, back pressure control device;Wherein, pressure gauge is arranged between back pressure control device and intermediate receptacle.
Specific embodiment of the invention, intermediate receptacle is a high-pressure bottle with piston.The side of piston is Experimental Flowing Object, such as crude oil, opposite side are intermediate mediums, typically nitrogen gas and water etc., inject or discharge middle by opposite side Medium, so as to control the flowing of Experimental Flowing Object in intermediate receptacle;Back pressure control device is used to adjust back pressure.
The gas provided in the present invention in super-viscous oil in the test device of physical parameter, it is highly preferred that back pressure control is single Unit includes counterbalance valve, ISCO pumps.
Specific embodiment of the invention, counterbalance valve can import viscous crude from sample equipment to intermediate receptacle in the early stage During prevent the excessive generation splash of pressure.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that sampling unit is also wrapped Pressure gauge is included, pressure gauge is arranged between counterbalance valve and intermediate receptacle.Pressure gauge can monitor the pressure before counterbalance valve, and indirectly Monitor the pressure of intermediate receptacle.
The gas provided in the present invention is in super-viscous oil in the test device of physical parameter, it is preferable that solubility measurement is single Unit includes flash separator, check valve, gas mass flow gauge;Wherein, check valve is arranged on gas mass flow gauge and flash distillation Between separator.
Specific embodiment of the invention, flash separator is used for gas-liquid separation, is mainly dissolved in crude oil Gas under the conditions of high-temperature low-pressure quick separating;Gas mass flow is used for meter gaseous integrated flux, i.e. measurement is dissolved in Gas gross in crude oil.
The gas provided in the present invention in super-viscous oil in the test device of physical parameter, in HTHP sample mixing unit Intermediate receptacle in sample equipment and sampling unit can be heated to assigned temperature by heating unit, and sample equipment can be to super thick Oil carries out the sample mixing of oil gas.
The test device of the gas physical parameter in super-viscous oil provided in the present invention includes control valve, except counterbalance valve institute Branch road outside, all of control valve is all with the valve of high temperature high voltage resistant.
Present invention also offers a kind of method of testing of gas physical parameter in super-viscous oil, it is existed using above-mentioned gas The test device of physical parameter is completed in super-viscous oil, and the method for testing of gas physical parameter in super-viscous oil includes following step Suddenly:
180 DEG C -300 DEG C of preset temperature is adjusted the temperature to by control device, sample is mixed in sample equipment;
Sampled by sampling unit, density is measured using density measurement unit, it is viscous using viscosity measurement unit measurement Degree, solubility is measured using solubility measuring unit, completes the measure to gas physical parameter in super-viscous oil.
The present invention provide gas in super-viscous oil the method for testing and device of physical parameter can test different parameters it Between relation, including:Relation between density versus temperature-pressure, viscosity-temperature and pressure, solubility-temperature and pressure.
The method of testing of physical parameter, specifically includes following steps in super-viscous oil of the invention:
The viscous crude of saturation carbon dioxide mixed in sample equipment is imported into intermediate receptacle, by the back of the body after intermediate receptacle Pressure valve is slowly depressured, it is ensured that the viscous crude of full saturation carbon dioxide is led in intermediate receptacle;
Density measure:The viscous crude of the saturation carbon dioxide in intermediate receptacle is imported into beaker, it is full by balance measurement With the quality of the viscous crude of carbon dioxide;Wherein, the viscous crude volume of saturation carbon dioxide is obtained by intermediate receptacle, so as to obtain saturation The density of the viscous crude of carbon dioxide;
Viscosity measurement:The viscous crude of the saturation carbon dioxide in intermediate receptacle is imported into rheometer, is surveyed by rheometer The viscosity of thickened oil of saturation carbon dioxide is measured, during the viscous crude of saturation carbon dioxide is led, it is ensured that temperature, pressure value are constant;
Solubility is measured:The viscous crude of the saturation carbon dioxide in intermediate receptacle is imported into flash separator, flash distillation point Gas in device measures the content of carbon dioxide in the viscous crude of saturation carbon dioxide by flowmeter by flowmeter, passes through The volume of intermediate receptacle draws the viscous crude cumulative volume of saturation carbon dioxide, you can obtain solubility;Complete to gas in super-viscous oil The measure of middle physical parameter.
Above-mentioned gas are in the super-viscous oil in the method for testing of physical parameter, it is contemplated that temperature is to require that sample mixing is completed in experiment when Temperature;Viscous crude density measure is different and different according to experimental program (such as different viscous crude properties), can according to need and Distillation situation in distillation still is adjusted.
Above-mentioned gas are in the super-viscous oil in the method for testing of physical parameter, it is preferred that desired temperature is 180 DEG C -300 DEG C.
In the super-viscous oil in the method for testing of physical parameter, rheometer needs to carry out above-mentioned gas to the viscous crude amount for mixing Control, preferably viscous crude amount are 50mL, wherein, the viscous crude taken is obtained by intermediate receptacle.
The test device and method of gas of the invention physical parameter in super-viscous oil, Applicable temperature are 180 DEG C -300 DEG C, It is 0MPa-40MPa to be applicable pressure.The test device and method of gas of the invention physical parameter in super-viscous oil can be in experiments The balancing a survey of stabilization is realized in room, is accurately obtained density and pasting parameter, such that it is able to draw in note non-condensing gas crude oil extraction During the raising recovery ratio of non-condensing gas act on done contribution.
Brief description of the drawings
Fig. 1 is the structural representation of the test device of physical parameter in the super-viscous oil in embodiment 1.
Main Reference symbol description
The flowmeter 9 of 1 sample equipment, 2 balance, 3 gas cylinder, 4 intermediate receptacle, 56 outer gas cylinder of flash separator, 7 counterbalance valve 8 The gas mass flow gauge of 10 rheometer of pressure gauge, 11 computer 12
Specific embodiment
In order to be more clearly understood to technical characteristic of the invention, purpose and beneficial effect, now to skill of the invention Art scheme carry out it is described further below, but it is not intended that to it is of the invention can practical range restriction.
Embodiment 1
A kind of test device of gas physical parameter in super-viscous oil, structure are present embodiments provided as shown in figure 1, the gas Body test device of physical parameter in super-viscous oil includes:HTHP sample mixing unit, density measurement unit, viscosity measurement list Unit, sampling unit, solubility measuring unit;
Wherein, HTHP sample mixing unit respectively with density measurement unit, viscosity measurement unit, sampling unit, solubility Measuring unit is connected;Sampling unit respectively with HTHP sample mixing unit, density measurement unit, viscosity measurement unit, solubility Measuring unit is connected;
HTHP sample mixing unit includes sample equipment 1, control device, gas mass flow gauge 12, check valve, pressure gauge 9th, control valve, heating plate.Wherein, gas mass flow gauge 12 is connected with sample equipment 1, pressure gauge 9 be arranged on check valve with Between gas mass flow gauge 12.Sample equipment 1 is provided with charging aperture and outlet, and charging aperture is on the top of sample equipment 1, outlet In the bottom of sample equipment 1, control device includes heater.The external gas cylinder 3 of HTHP sample mixing unit.
Sample equipment 1 is provided with heat-insulation layer, PID temperature controller, thermocouple and pressure sensor, and sample device interior is set There is the stirring block with honeycomb hole;Heating plate is arranged on the lateral wall of sample equipment;The PID temperature controller of sample equipment 1 For adjusting the temperature in sample equipment, thermocouple and pressure sensor, for monitoring the pressure and temperature in sample equipment 1.
The rotation of sample equipment 1 is realized by control device, the stirring block inside sample equipment 1 can promote vapour-liquid to put down Weighing apparatus;During sample equipment 1 rotates, metal derby is fallen by Action of Gravity Field, and the gas in honeycomb hole fully connects with viscous crude Touch, make gas and the maximum saturation of viscous crude.
Sample equipment is carried out by heating plate be previously heated to desired temperature.
Density measurement unit includes liquid metering device, control valve;Wherein, liquid metering device includes collection cups and day Flat 2, wherein, collection cups are used to collect the liquid that the displacement of intermediate receptacle 4 goes out, and collection cups are placed on balance 2.
Viscosity measurement unit includes rheometer 10, control valve.
Sampling unit includes intermediate receptacle 4, pressure gauge, back pressure control device, control valve, pressure gauge;Back pressure control is single Unit includes counterbalance valve 7, ISCO pumps.Counterbalance valve is prevented during can importing viscous crude to intermediate receptacle from sample equipment in the early stage The excessive generation splash of pressure.Pressure gauge is arranged between counterbalance valve 7 and intermediate receptacle 4, and pressure gauge can monitor intermediate receptacle 4 Pressure.The external outer gas cylinder 6 of sampling unit, outer gas cylinder 6 is connected with counterbalance valve 7.
Solubility measuring unit includes flash separator 5, check valve, flowmeter 8, control valve, computer 11.
The gas provided in the present invention in super-viscous oil in the test device of physical parameter, except the branch road where counterbalance valve Outward, all of valve is all with the valve of high temperature high voltage resistant.
The present embodiment additionally provides the method for testing of the gas physical parameter in super-viscous oil completed using said apparatus, tool Body is comprised the following steps:
Illustrated by taking special thick oil under 250 DEG C, 4MPa pressure and the experiment of carbon dioxide sample mixing as an example, super-viscous oil:Xinjiang wind City, 50 DEG C of degassed crudes viscosity 100000mPaS, density 0.97g/mL;Sample body accumulates 1L;Intermediate receptacle 250mL;
Step one:500mL heavy oil heatings are first opened into sample equipment to 85 DEG C to flowable state, viscous crude is poured into and is matched somebody with somebody Then sample equipment configured muff.The carbon dioxide volume and pressure of axe body are injected under calculating normal temperature simultaneously.Injection gas Simultaneously, it is 250 DEG C to set heating mantle and sample mixing axe temperature to body pressure 1MPa.Stirring switch is opened, sample equipment carries out sample mixing.2 Pressure is seen after hour, tonifying Qi is carried out by gas cylinder if pressure does not arrive goal pressure, until goal pressure 4MPa.Sample mixing 24 is small When.
Step 2:Sampling unit is connected, the intermediate receptacle 60mL of sampling unit, gas cylinder pressure-reducing valve setting pressure 5MPa, will Intermediate receptacle piston is pushed into bottom, and pressure is down into 3.95MPa by adjusting counterbalance valve.
Step 3:Connection high temperature sample mixing device rotate to 90 ° it is vertical, upper, viscous crude is under, while pipeline and valve for piston Carry out heating tape and be heated to 250 DEG C, heat 60min, intermediate receptacle sets and is heated to 250 DEG C.Dioxide bottle is connect, gas cylinder subtracts Pressure valve is to 4MPa.Gas cylinder is set to be connected with sample mixing device, 60mL crude oil is transferred to intermediate receptacle by pressured difference.
Step 4:Density is measured by quality volumetric method.Pipeline and valve temperature are heated to 250 DEG C using heating tape. The HTHP crude oil of intermediate receptacle is imported into balance, mass metering.
Repeat step three;
Step 5:Vacuumized to rheometer using vavuum pump, heating-up temperature is to 250 DEG C.Using heating tape by pipeline and valve Door temperature is heated to 250 DEG C.Regulation gas cylinder is decompressed to 4MPa, and the HTHP crude oil of the saturated gas of intermediate receptacle is imported into stream Become instrument, survey viscosity of crude.
Repeat step three;
Step 6:By flash separator heating-up temperature to 250 DEG C.Pipeline and valve temperature are heated to using heating tape 250℃.Regulation gas cylinder is decompressed to 4MPa, and the HTHP crude oil of intermediate receptacle is imported into flash separator, is entered using flowmeter Row continuous gas flow collection, and by its total gas flow rate of computer statistics.Two of 60mL viscous crude under 250 DEG C, 4MPa can be obtained Carbon oxide gas solubility, completes the test of gas physical parameter in super-viscous oil, as a result as shown in table 1, table 2 and table 3.
The thick thing oiliness parameter of the saturation carbon dioxide of table 1, density versus temperature-pressure (T=250 DEG C, P=4MPA)
First group Second group 3rd group 4th group
Volume (mL) 237.29 237.29 237.29 237.29
Quality (g) 190.3066 192.2049 191.493 189.3574
Density (g/mL) 0.802 0.81 0.807 0.798
2 viscosity versus temperatures of table-pressure
Temperature (DEG C) Pressure (MPA) Viscosity (mPaS)
50 0.1 92600
100 0.1 1081
150 0.48 91.4
250 4 1.15
3 solubility of table-temperature and pressure (T=250 DEG C, P=4MPa)
First group Second group 3rd group 4th group
Crude quality (g) 234.91 237.27 232.33 230.22
Dissolved gas volume (L) 0.85 0.87 0.87 0.86
Quantity of dissolved gas (mol) 0.04 0.04 0.04 0.04
Solubility (* 1000mol/g) 0.16 0.16 0.17 0.17
Above example explanation, the test device and method of gas of the invention physical parameter in super-viscous oil, applicable for temperature It is 180 DEG C -300 DEG C to spend, and it is 0MPa-40MPa to be applicable pressure, can realize the balancing a survey of stabilization in laboratory, is accurately obtained Density and pasting parameter, such that it is able to draw the raising recovery ratio effect of the non-condensing gas during non-condensing gas crude oil extraction is noted The contribution done.

Claims (10)

1. a kind of test device of gas physical parameter in super-viscous oil, it is characterised in that gas physical property ginseng in super-viscous oil Several test devices include:HTHP sample mixing unit, density measurement unit, viscosity measurement unit, sampling unit, solubility are surveyed Amount unit;
Wherein, the HTHP sample mixing unit respectively with the density measurement unit, the viscosity measurement unit, the sampling Unit, solubility measuring unit connection;
The sampling unit connects with the density measurement unit, the viscosity measurement unit, the solubility measuring unit respectively It is logical;
The HTHP sample mixing unit includes sample equipment, control device, and the sample equipment is provided with charging aperture and outlet, The control device includes heater.
2. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the high temperature High pressure sample mixing unit also includes gas mass flow gauge, check valve, pressure gauge;Wherein, the gas mass flow gauge with it is described Sample equipment is connected, and the pressure gauge is arranged between the check valve and the gas mass flow gauge.
3. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the sample Equipment includes PID temperature controller, thermocouple and pressure sensor, and the sample equipment is provided with heat-insulation layer, and the sample sets It is standby to be internally provided with stirring block;Wherein, the PID temperature controller is used to adjust the temperature in sample equipment, and thermocouple is used for The temperature change of sample equipment is detected, pressure sensor is used to monitor the pressure change of sample equipment.
4. the test device of gas according to claim 3 physical parameter in super-viscous oil, it is characterised in that the stirring Block is the metal derby with honeycomb hole.
5. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the density Measuring unit includes liquid metering device.
6. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the viscosity Measuring unit includes rheometer.
7. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the sampling Unit include intermediate receptacle, pressure gauge, back pressure control device, wherein, the pressure gauge be arranged on the back pressure control device and Between the intermediate receptacle.
8. the test device of gas according to claim 1 physical parameter in super-viscous oil, it is characterised in that the dissolving Degree measuring unit includes flash separator, check valve, gas mass flow gauge;Wherein, check valve is arranged on gas mass flow Between meter and flash separator.
9. the method for testing of a kind of gas physical parameter in super-viscous oil, it is characterised in that it is any using claim 1-8 What the test device of the gas physical parameter in super-viscous oil described in was completed, the test of gas physical parameter in super-viscous oil Method is comprised the following steps:
180 DEG C -300 DEG C of preset temperature is adjusted the temperature to by control device, sample is mixed in sample equipment;
Sampled by sampling unit, density is measured using density measurement unit, viscosity, profit are measured using viscosity measurement unit Solubility is measured with solubility measuring unit, the measure to gas physical parameter in super-viscous oil is completed.
10. the relation between the method for testing test different parameters of the physical parameter in the super-viscous oil of the gas described in claim 9, Including:Density versus temperature-pressure, viscosity-temperature and pressure, solubility-temperature and pressure.
CN201611177620.8A 2016-12-19 2016-12-19 A kind of test device and method of gas physical parameter in super-viscous oil Active CN106814177B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611177620.8A CN106814177B (en) 2016-12-19 2016-12-19 A kind of test device and method of gas physical parameter in super-viscous oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611177620.8A CN106814177B (en) 2016-12-19 2016-12-19 A kind of test device and method of gas physical parameter in super-viscous oil

Publications (2)

Publication Number Publication Date
CN106814177A true CN106814177A (en) 2017-06-09
CN106814177B CN106814177B (en) 2019-10-11

Family

ID=59110625

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611177620.8A Active CN106814177B (en) 2016-12-19 2016-12-19 A kind of test device and method of gas physical parameter in super-viscous oil

Country Status (1)

Country Link
CN (1) CN106814177B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114414779A (en) * 2022-01-21 2022-04-29 西南石油大学 High-pressure dissolved gas wax-containing crude oil solubility, viscosity and wax precipitation process measuring device
CN115112817A (en) * 2021-03-19 2022-09-27 南通中智检测服务有限公司 Method for discriminating and detecting physical properties of underground biodegradable thickened oil

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201773053U (en) * 2010-01-11 2011-03-23 中国石油大学(华东) Pressurized saturated dissolved-gas crude oil rheological property measuring device
CN102121891A (en) * 2010-12-16 2011-07-13 西南石油大学 Device and method for testing molecular diffusion coefficients in multi-component oil-gas system under high temperature and high pressure
US20140067307A1 (en) * 2012-09-03 2014-03-06 Geoservices Equipements Method of Calibration Intended to Be Used in A Process of Determining The Content of A Plurality of Compounds Contained in A Drilling Fluid
CN203965275U (en) * 2014-06-30 2014-11-26 北京永兴精佳仪器有限公司 A kind of system of online detection crude oil
CN104406878A (en) * 2014-10-16 2015-03-11 中国石油天然气股份有限公司 Method and apparatus for measuring solubility of carbon dioxide in crude oil and water
CN104777071A (en) * 2014-01-15 2015-07-15 中国石油化工股份有限公司 Water-containing thickened oil PVT experiment method
CN105467102A (en) * 2016-01-07 2016-04-06 西南石油大学 Experimental device and method of ultra-thick crude oil oxygenated fuel deposition

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201773053U (en) * 2010-01-11 2011-03-23 中国石油大学(华东) Pressurized saturated dissolved-gas crude oil rheological property measuring device
CN102121891A (en) * 2010-12-16 2011-07-13 西南石油大学 Device and method for testing molecular diffusion coefficients in multi-component oil-gas system under high temperature and high pressure
US20140067307A1 (en) * 2012-09-03 2014-03-06 Geoservices Equipements Method of Calibration Intended to Be Used in A Process of Determining The Content of A Plurality of Compounds Contained in A Drilling Fluid
CN104777071A (en) * 2014-01-15 2015-07-15 中国石油化工股份有限公司 Water-containing thickened oil PVT experiment method
CN203965275U (en) * 2014-06-30 2014-11-26 北京永兴精佳仪器有限公司 A kind of system of online detection crude oil
CN104406878A (en) * 2014-10-16 2015-03-11 中国石油天然气股份有限公司 Method and apparatus for measuring solubility of carbon dioxide in crude oil and water
CN105467102A (en) * 2016-01-07 2016-04-06 西南石油大学 Experimental device and method of ultra-thick crude oil oxygenated fuel deposition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115112817A (en) * 2021-03-19 2022-09-27 南通中智检测服务有限公司 Method for discriminating and detecting physical properties of underground biodegradable thickened oil
CN114414779A (en) * 2022-01-21 2022-04-29 西南石油大学 High-pressure dissolved gas wax-containing crude oil solubility, viscosity and wax precipitation process measuring device

Also Published As

Publication number Publication date
CN106814177B (en) 2019-10-11

Similar Documents

Publication Publication Date Title
CN108592978B (en) Oil gas water multiphase flow on-line metering calibration device
CN104297126B (en) low permeability reservoir gas seepage starting pressure gradient measuring device and measuring method
CN103645126B (en) Stratum high-temperature high-pressure air-water phase percolation curve assay method
CN104101559B (en) Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic
CN105203705B (en) A kind of heavy component deposition causes the method for testing of reservoir damage
CN109443867B (en) The method that the physical parameter of a kind of pair of tight rock is continuously detected
CN102192864B (en) High-temperature, high-pressure, and acid-resisting apparatus for foam generation and dynamic evaluation
CN102866082B (en) Device and method for measuring rheological property of foaming oil
CN109883891B (en) Measuring device and method for injected gas-liquid phase diffusion coefficient of fracture-cavity oil reservoir
CN105784567B (en) A kind of device and method of testing rock core relative permeability
CN103512826A (en) Device and method for measuring solubility of polymers in supercritical carbon dioxide
CN206772756U (en) A kind of dissolved gas crude oil density, the evaluating apparatus of volume factor
CN105388254A (en) High-temperature high-pressure foam fracturing fluid leak-off damage experiment system
US11946327B2 (en) Automatic rheological parameter measuring system and use method for flowing drilling fluid with high temperature and high-pressure
CN108759951B (en) Method and device for measuring crude oil/natural gas/water three-phase flow on line
CN105928832B (en) The assay method of capillary viscosity analyzer and fluid viscosity
CN106814177B (en) A kind of test device and method of gas physical parameter in super-viscous oil
CN108663289A (en) Under a kind of condition of high voltage liquid CO is measured using capillary2/N2The device and its measurement method of two-phase system viscosity
CN105181222A (en) Device for measuring carbon dioxide minimum miscible pressure in multiple modes
CN112326877A (en) High-temperature high-pressure foam performance tester
CN114352238A (en) Device and method for testing flow conductivity of natural gas hydrate production increasing seam
CN206177778U (en) Penetrant unit of research porous medium whole area seepage flow mechanism
CN107389504A (en) For measuring the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic
WO2015112009A1 (en) Flow measurement system and method for determining at least one property of a medium
CN110924943B (en) Quantitative drainage and production experimental device for coal-bed gas well and drainage and production control method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant