CN104101559B - Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic - Google Patents
Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic Download PDFInfo
- Publication number
- CN104101559B CN104101559B CN201410350749.9A CN201410350749A CN104101559B CN 104101559 B CN104101559 B CN 104101559B CN 201410350749 A CN201410350749 A CN 201410350749A CN 104101559 B CN104101559 B CN 104101559B
- Authority
- CN
- China
- Prior art keywords
- carbon dioxide
- supercritical carbon
- fracturing fluid
- pressure
- tackifier
- 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.)
- Active
Links
Abstract
The invention belongs to unconventionaloil pool production technique field, in particular it relates to a kind of device and method measuring supercritical carbon dioxide fracturing fluid rheological characteristic.Measurement apparatus includes: supercritical carbon dioxide pressure charging system, tackifier inject hybrid system and the supercritical carbon dioxide fracturing fluid circulatory system;The critical carbon dioxide fracturing fluid circulatory system provides the closed circuit of Guan Bi under HTHP for supercritical carbon dioxide fracturing fluid, supercritical carbon dioxide pressure charging system for carbon dioxide provide required for experimental pressure, tackifier inject hybrid system tackifier are pumped in HTHP supercritical carbon dioxide pipeline.The present invention is capable of the measurement of bigger pressure and temperature wide-ultra critical carbon dioxide fracturing fluid rheological parameter, the constitutive relation of supercritical carbon dioxide fracturing fluid rheological behavior under available different temperatures, pressure condition;Device is simple to operate, and method is easy to implement, and feasibility is high;Measuring method science, it is possible to realize the parameter measurement of degree of precision.
Description
Technical field
The invention belongs to unconventionaloil pool production technique field, in particular it relates to a kind of measurement surpasses
The device and method of critical carbon dioxide fracturing fluid rheological characteristic.
Background technology
Unconventional gas resource includes coal bed gas, shale gas, compact sandstone gas and Water Soluble Gas
Deng, current unconventional petroleum resources plays key player in global energy structure.Non-
The reservoir properties of conventional gas and oil resource is the most poor, has low-porosity, low-permeability, low hole
The physical property characteristics such as larynx radius, the more conventional oil-gas reservoir of flow resistance of oil gas is big many, and along with
The intensification that reservoir buries, reservoir properties is deteriorated so that conventional production technique does not possess business exploitation
Being worth, determining unconventional petroleum resources needs to take fracture technology to improve well yield.
Hydraulic fracturing technology is applied to the exploitation of the unconventionaloil pool such as shale gas and tight gas Tibetan and can produce
The series of problems such as water-sensitive, reservoir pollution, and water resources shortage is also restriction fracturing
Key factor.
Supercritical carbon dioxide has the low viscosity of gas and high diffusivity coefficient and the height of liquid concurrently
Density and good dissolubility.Supercritical carbon dioxide pressure break is a kind of novel unconventional natural
Gas Reservoir renovation technique, compared with conventional hydraulic pressure break, supercritical carbon dioxide fracturing fluid has
Have low leak-off, height return row, little to reservoir pollution, prevent clay mineral hydration swelling etc. many excellent
Point.Therefore, supercritical carbon dioxide pressure break can improve unconventionaloil pool reservoir flow conductivity,
Realize one of effective means of business high-efficiency mining.Supercritical carbon dioxide fracturing fluid is tackifier
The compounding substances being dissolved in supercritical carbon dioxide.At present, by temperature, pressure influence, surpass and face
The Rheological Regularity of boundary's carbon dioxide pressure break liquid is considerably complicated, rarely has test data, for rheological characteristic
The explanation of mechanism also neither one system, thus become one of supercritical fluid research field
Difficult point.
Summary of the invention
For overcoming the defect existing for prior art, the present invention provides a kind of and measures overcritical dioxy
Change carbon pressure and split the device and method of liquid flow sex change, for quickly measuring under different Temperature-pressure Conditions
The rheological parameter of supercritical carbon dioxide fracturing fluid, and then network analysis supercritical carbon dioxide pressure
Split the rheological characteristic of liquid, provide experiment base for supercritical carbon dioxide FRACTURING DESIGN and theoretical research
Plinth.
For solving above-mentioned technical problem, the technical solution adopted in the present invention is as follows:
Measure the device of supercritical carbon dioxide fracturing fluid rheological characteristic, including: overcritical titanium dioxide
Carbon pressure charging system, tackifier inject hybrid system and supercritical carbon dioxide fracturing fluid cyclic system
System;The supercritical carbon dioxide fracturing fluid circulatory system provides height for supercritical carbon dioxide fracturing fluid
The closed circuit of Guan Bi under temperature high pressure, supercritical carbon dioxide pressure charging system provides for carbon dioxide
Required experimental pressure, tackifier are pumped into HTHP and surpass by tackifier injection hybrid system
In critical carbon dioxide pipeline.
The method measuring supercritical carbon dioxide fracturing fluid rheological characteristic, uses above-mentioned experimental provision,
When carrying out supercritical carbon dioxide fracturing fluid rheology tests, adjust carbon dioxide air source and enter
Mouth screws valve, tackifier entrance screws valve, the emptying of supercritical carbon dioxide fracturing fluid screws at valve
In closed mode, vavuum pump is utilized to get rid of the air in experiment pipeline;Open carbon dioxide air source
Entrance screws valve, circulating pump, makes carbon dioxide enter supercritical carbon dioxide fracturing fluid cyclic system
System, regulates gas boosting pump, oil bath heater, the temperature of experimental system, pressure is adjusted to
The temperature, pressure that experiment sets;Open tackifier entrance and screw valve, tackifier measuring pump, plunger
Tackifier in tackifier storage tank are pumped into the supercritical carbon dioxide fracturing fluid circulatory system by pump,
Fluid (tackifier, carbon dioxide) flows under circulating pump effect, and tackifier fill in clean mixed device
Divide and be dissolved in supercritical carbon dioxide;After parameter stability, carry out supercritical carbon dioxide pressure
Splitting the mensuration of liquid flow sex change, differential pressure pick-up record fluid is measuring the differential pressure of flow of line sections,
Mass flowmenter display supercritical carbon dioxide fracturing fluid mass flow, is calculated setting temperature
Supercritical carbon dioxide fracturing fluid Rheology Constitutive Equation under degree, pressure.
Relative to prior art, beneficial effects of the present invention is as follows:
(1), it is capable of bigger pressure and temperature wide-ultra critical carbon dioxide pressure break liquid flow
The measurement of variable element, supercritical carbon dioxide fracturing fluid under available different temperatures, pressure condition
The constitutive relation of rheological behavior;
(2), device simple to operate, method is easy to implement, and feasibility is high;
(3), measuring method science, it is possible to realize the parameter measurement of degree of precision.
Accompanying drawing explanation
Fig. 1 is the device schematic diagram for measuring supercritical carbon dioxide fracturing fluid rheological characteristic;
In figure: 11, carbon dioxide air source;12, gas buffer tank;13, gas boosting pump;
14, carbon dioxide gas source inlet screws valve;21, tackifier storage tank;22, tackifier measuring pump;
23, plunger displacement pump;24, tackifier entrance screws valve;31, intermediate receptacle;311, oil bath adds
Hot device;312, thermometer in intermediate receptacle;313, intermediate receptacle inner gauge;32, circulation
Pump;33, device is only mixed;34, line sections is measured;341, the import of carbon dioxide pressure break liquid is measured
Pressure gauge;342, thermometer is measured in the import of carbon dioxide pressure break liquid;343, line sections is measured poor
Pressure sensor;344, thermometer is measured in the outlet of carbon dioxide pressure break liquid;345, pressurized carbon dioxide
Split liquid outlet and measure pressure gauge;35, mass flowmenter;36, vavuum pump;37, overcritical two
The emptying of carbonoxide fracturing fluid screws valve.
Detailed description of the invention
As it is shown in figure 1, measure the device of supercritical carbon dioxide fracturing fluid rheological characteristic, including:
Supercritical carbon dioxide pressure charging system, tackifier inject hybrid system and supercritical carbon dioxide pressure
Split fluid circulation;The supercritical carbon dioxide fracturing fluid circulatory system is supercritical carbon dioxide pressure
Splitting liquid and provide the closed circuit of Guan Bi under HTHP, supercritical carbon dioxide pressure charging system is two
Experimental pressure required for carbonoxide offer, tackifier inject hybrid system and are pumped into by tackifier
In HTHP supercritical carbon dioxide pipeline.
Supercritical carbon dioxide pressure charging system, including: carbon dioxide air source 11, gas buffer
Tank 12, gas boosting pump 13, carbon dioxide gas source inlet screw valve 14, carbon dioxide air source
11, gas buffer tank 12, gas boosting pump 13, carbon dioxide gas source inlet screw valve 14 and depend on
Secondary connected by pipeline;Carbon dioxide air source 11 provides the carbon dioxide needed for experiment, gas
Surge tank 12 is for storing the carbon dioxide of high pressure, the titanium dioxide in gas buffer tank 12
Carbon flows to gas boosting pump 13, and gas boosting pump 13 is that carbon dioxide supercharging is with satisfied experiment pressure
Power requirement, carbon dioxide screws valve 14 by carbon dioxide gas source inlet and enters overcritical
Carbon dioxide pressure break fluid circulation.
Tackifier inject hybrid system, including: tackifier storage tank 21, tackifier measuring pump 22,
Plunger displacement pump 23, tackifier entrance screw valve 24;Tackifier storage tank 21, tackifier measuring pump 22,
Plunger displacement pump 23, tackifier entrance screw valve 24 and pass sequentially through pipeline connection;Tackifier storage tank 21
Built with being soluble in the solvent of supercritical carbon dioxide, for improving the viscous of supercritical carbon dioxide
Degree, tackifier measuring pump 22 to add thickening dosage carry out accurate measurement, plunger displacement pump 23 via
Tackifier entrance screws valve 24 and tackifier pumps into supercritical carbon dioxide fracturing fluid cyclic system
System.
The supercritical carbon dioxide fracturing fluid circulatory system, including: intermediate receptacle 31, mixes device only
33, line sections 34, mass flowmenter 35 are measured;Intermediate receptacle 31 port of export and clean mixed device
33 entrance points are connected by pipeline, clean mixed device 33 port of export and mass flowmenter 35 entrance point
It is connected by measuring line sections 34, mass flowmenter 35 port of export and intermediate receptacle 31 import
Hold and be connected, forming the closed circuit of a Guan Bi.
Intermediate receptacle 31 is provided with circulating pump 32, circulating pump with the connection pipeline of clean mixed device 33
32 provide the power needed for closed circulation for supercritical carbon dioxide fracturing fluid, and circulating pump 32 makes
Fluid is flowed to clean mixed device 33 direction by intermediate receptacle 31;Tackifier entrance screws valve 24 and leads to
Cross pipeline and access clean mixed pipeline between device 33 and circulating pump 32;Intermediate receptacle 31 faces super
Boundary's carbon dioxide pressure break liquid carries out buffer storage, and tackifier are sufficiently mixed dissolving by clean mixed device 33
In supercritical carbon dioxide, form supercritical carbon dioxide fracturing fluid fluid.
Intermediate receptacle 31 is placed in oil bath heater 311, and intermediate receptacle 31 is provided with intermediate receptacle
Interior thermometer 312, intermediate receptacle inner gauge 313;Oil bath heater 311 is to overcritical two
Carbonoxide fracturing fluid heats to reach experimental temperature requirement, and in intermediate receptacle, thermometer 312 is measured
Temperature in intermediate receptacle, intermediate receptacle inner gauge 313 measures the pressure in intermediate receptacle.
Measure on pipeline 34, by only mixing device 33 to mass flowmenter 35 direction, be sequentially provided with
Pressure gauge 341 is measured in carbon dioxide pressure break liquid import, temperature is measured in carbon dioxide pressure break liquid import
Temperature is measured in meter 342, measurement line sections differential pressure pick-up 343, the outlet of carbon dioxide pressure break liquid
Pressure gauge 345 is measured in the outlet of meter 344, carbon dioxide pressure break liquid;Carbon dioxide pressure break liquid import
Measure pressure gauge 341, the outlet of carbon dioxide pressure break liquid is measured pressure gauge 345 and is measured present position
Pipeline in pressure;Thermometer 342, carbon dioxide pressure break are measured in carbon dioxide pressure break liquid import
Temperature in the pipeline of liquid outlet measurement thermometer 344 real-time monitored present position;Measure line sections
Differential pressure pick-up 343 is used for measuring supercritical carbon dioxide fracturing fluid and flows through measurement line sections 34
The pressure differential produced;Measuring section line sections 24 is internal diameter 6mm, wall thickness 2mm, length 7.5m
The copper pipeline of external application heat-insulation layer.
The pipeline that mass flowmenter 35 is connected with intermediate receptacle 31 is provided with vavuum pump 36,
Carbon dioxide gas source inlet screws valve 14 by pipeline cut-in quality flowmeter 35 and intermediate receptacle
In pipeline between 31;Mass flowmenter 35 is for measuring supercritical carbon dioxide fracturing fluid
Mass flow, vavuum pump 36 is for getting rid of the air in experiment pipeline.Supercritical carbon dioxide
Fracturing fluid emptying screws valve 38 and accesses vavuum pump 36 and intermediate receptacle 31 connecting tube by pipeline
Lu Shang, it is super for being vented in experiment pipeline that the emptying of supercritical carbon dioxide fracturing fluid screws valve 38
Critical carbon dioxide fracturing fluid.
In close loop, all parts and the most pressure 60MPa of pipeline, temperature upper limit is
500K, can realize supercritical carbon dioxide supercritical carbon dioxide fracturing fluid at high temperature under high pressure
The experiment of rheological characteristic is measured.
The method measuring supercritical carbon dioxide fracturing fluid rheological characteristic, utilizes said apparatus, step
As follows:
(1) supercritical carbon dioxide circulation, is set up
Adjust that carbon dioxide gas source inlet screws valve 14, tackifier entrance screws valve 24, super face
Boundary's carbon dioxide pressure break liquid emptying screws valve 38 and is closed, and utilizes vavuum pump 36 to get rid of
Air in experiment pipeline;Open carbon dioxide gas source inlet and screw valve 14, circulating pump 32,
Carbon dioxide is made to be flowed out by carbon dioxide air source 11, regulation gas boosting pump 13, oil bath heating
Device 311, is adjusted to, by the temperature of experimental system, pressure, the temperature, pressure that experiment sets.
(2), tackifier are added
Open tackifier entrance and screw valve 24, tackifier measuring pump 22, plunger displacement pump 23, will increase
Tackifier in stick storage tank 21 pump into the supercritical carbon dioxide fracturing fluid circulatory system, fluid
(tackifier, carbon dioxide) flows under circulating pump 32 acts on, and tackifier are in clean mixed device 33
It is completely dissolved in supercritical carbon dioxide;After parameter stability, carry out supercritical carbon dioxide
The measurement of fracturing fluid rheological characteristic.
(3), supercritical carbon dioxide fracturing fluid mean temperature in line sections is calculated
Read supercritical carbon dioxide fracturing fluid import and measure temperature T of thermometer 3421, outlet
Measure temperature T of thermometer 3442, calculate supercritical carbon dioxide fracturing fluid in line sections
Mean temperature:
In formula, T is supercritical carbon dioxide mean temperature in measuring line sections pipe, K;
T1The temperature of line sections Guan Nei import department, K is being measured for supercritical carbon dioxide fracturing fluid;T2
The temperature at line sections pipe inner outlet, K is being measured for supercritical carbon dioxide fracturing fluid.
(4), supercritical carbon dioxide fracturing fluid average pressure in line sections is calculated
Read supercritical carbon dioxide fracturing fluid import and measure the pressure P of pressure gauge 3411, go out
The pressure P of mouth measurement pressure gauge 3452, calculate supercritical carbon dioxide fracturing fluid in line sections
Interior average pressure:
In formula, P is supercritical carbon dioxide average pressure in measuring line sections pipe, MPa;
P1The pressure of line sections Guan Nei import department, MPa is being measured for supercritical carbon dioxide fracturing fluid;
P2The pressure at line sections pipe inner outlet, MPa is being measured for supercritical carbon dioxide fracturing fluid.
(5) supercritical carbon dioxide fracturing fluid flow velocity in measuring line sections, is calculated
Supercritical carbon dioxide fracturing fluid mass flow Q of reading quality flowmeter 35, calculates
Supercritical carbon dioxide fracturing fluid flow velocity in measuring line sections 34:
Z3-(1-B)Z2+(A-3B2-2B)Z-(AB-B2-B3)=0 (3)
In formula, Z is compressibility factor, dimensionless;A, B are intermediate variable, expression formula such as formula
(4), shown in (5);prFor reduced pressure, dimensionless;TrFor reduced temperature, dimensionless;
W is the eccentric factor of carbon dioxide, dimensionless;ρCO2For the density of carbon dioxide, kg/m3;
xCO2For carbon dioxide ratio in supercritical carbon dioxide fracturing fluid, dimensionless;ρtFor increasing
The density of stick, kg/m3;ρ is the density of supercritical carbon dioxide fracturing fluid, kg/m3;xt
For tackifier ratio in supercritical carbon dioxide fracturing fluid, dimensionless;P is absolute pressure,
MPa;T is absolute temperature, K;MgFor the molecular weight of carbon dioxide, kg/m3;R is general
Gas constant, 0.008314MPa m3/(kmol·K);Q is supercritical carbon dioxide fracturing fluid
Mass flow, kg/s;D is for measuring line sections 34 diameter, m;U is overcritical titanium dioxide
Carbon fracturing fluid flow velocity in pipeline, m/s.
(6), wall shear stress is calculated
Read the pressure differential Δ p measuring line sections differential pressure pick-up 343, be calculated wall and cut
Shearing stress:
In formula, τwFor wall shear stress, Pa;Δ p is for measuring line sections differential pressure pick-up 21
Pressure differential, Pa;L is the length measuring line sections 34, m.
(7) constitutive relation of supercritical carbon dioxide fracturing fluid fluid rheology parameter, it is calculated
At τw—Draw logarithmic curve on coordinate, obtain corresponding different τwSlope of curve n',
And then obtain the constitutive relation of supercritical carbon dioxide fracturing fluid fluid rheology parameter:
In formula,For supercritical carbon dioxide fracturing fluid fluid shearing rate of deformation, s-1;N' is different
τwThe logarithmic coordinates slope of curve.
Change the temperature of experimental system, pressure, supercritical carbon dioxide pressure break liquid flow can be studied
Sex change is with temperature, the Changing Pattern of pressure;Thus study the stream of supercritical carbon dioxide fracturing fluid
Motivation is managed, and provides experiment basis for supercritical carbon dioxide FRACTURING DESIGN and theoretical research.
Claims (7)
1. measure a device for supercritical carbon dioxide fracturing fluid rheological characteristic, including: overcritical titanium dioxide
Carbon pressure charging system, tackifier inject hybrid system and the supercritical carbon dioxide fracturing fluid circulatory system;Its feature
It is: the supercritical carbon dioxide fracturing fluid circulatory system provides HTHP for supercritical carbon dioxide fracturing fluid
The closed circuit of lower Guan Bi, supercritical carbon dioxide pressure charging system for carbon dioxide provide required for experiment pressure
Power, tackifier inject hybrid system and are pumped into by tackifier in HTHP supercritical carbon dioxide pipeline;
Supercritical carbon dioxide pressure charging system, including: carbon dioxide air source, gas buffer tank, gas boosting
Pump, carbon dioxide gas source inlet screw valve, carbon dioxide air source, gas buffer tank, gas boosting pump, two
Carbonoxide air source inlet screw valve pass sequentially through pipeline be connected;Carbon dioxide is entered by carbon dioxide air source
Mouth screws valve and enters the supercritical carbon dioxide fracturing fluid circulatory system;
Tackifier inject hybrid system, including: tackifier storage tank, tackifier measuring pump, plunger displacement pump, thickening
Agent entrance screws valve;Tackifier storage tank, tackifier measuring pump, plunger displacement pump, tackifier entrance screw valve successively
Connected by pipeline;Tackifier storage tank built with being soluble in the solvent of supercritical carbon dioxide, plunger displacement pump via
Tackifier entrance screws valve and tackifier pumps into the supercritical carbon dioxide fracturing fluid circulatory system;
The supercritical carbon dioxide fracturing fluid circulatory system, including: intermediate receptacle, only mix device, measure line sections,
Mass flowmenter;The intermediate receptacle port of export is connected by pipeline with clean mixed device entrance point, the clean mixed device port of export and
Mass flowmenter entrance point is connected by measuring line sections, the mass flowmenter port of export and intermediate receptacle entrance point
Be connected, formed one Guan Bi closed circuit.
The device of measurement supercritical carbon dioxide fracturing fluid rheological characteristic the most according to claim 1, its
Being characterised by, intermediate receptacle is provided with circulating pump with the connection pipeline of clean mixed device, and tackifier entrance screws valve and leads to
Cross pipeline and access clean mixed pipeline between device and circulating pump;Intermediate receptacle is placed in oil bath heater, middle appearance
Device is provided with thermometer, intermediate receptacle inner gauge in intermediate receptacle;Measure on pipeline, by only mixing device to quality
Flowmeter direction, is sequentially provided with carbon dioxide pressure break liquid import and measures pressure gauge, carbon dioxide pressure break liquid import
Measure thermometer, measure line sections differential pressure pick-up, carbon dioxide pressure break liquid outlet measurement thermometer, dioxy
Change the outlet of carbon fracturing fluid and measure pressure gauge;The pipeline that mass flowmenter is connected with intermediate receptacle is provided with vacuum
Pump, carbon dioxide gas source inlet screws valve and accesses the pipeline between intermediate receptacle and mass flowmenter by pipeline
In.
The device of measurement supercritical carbon dioxide fracturing fluid rheological characteristic the most according to claim 2, its
Being characterised by, the emptying of supercritical carbon dioxide fracturing fluid screws valve by pipeline cut-in quality flowmeter with middle
On container connecting line.
The device of measurement supercritical carbon dioxide fracturing fluid rheological characteristic the most according to claim 3, its
Being characterised by, in supercritical carbon dioxide fracturing fluid circulatory system close loop, all parts and pipeline are equal
Pressure 60MPa, temperature upper limit is 500K.
The device of measurement supercritical carbon dioxide fracturing fluid rheological characteristic the most according to claim 4, its
Being characterised by, measuring section line sections is internal diameter 6mm, wall thickness 2mm, length 7.5m external application heat-insulation layer
Copper pipeline.
6. the method measuring supercritical carbon dioxide fracturing fluid rheological characteristic, uses one of claim 1-5 institute
The device measuring supercritical carbon dioxide fracturing fluid rheological characteristic stated, it is characterised in that specifically comprise the following steps that
(1) supercritical carbon dioxide circulation, is set up
Carbon dioxide gas source inlet screws valve, tackifier entrance screws valve, supercritical carbon dioxide pressure break in adjustment
Liquid emptying screws valve and is closed, and utilizes vavuum pump to get rid of the air in experiment pipeline;Open titanium dioxide
Carbon air source inlet screws valve, circulating pump, makes carbon dioxide be flowed out by carbon dioxide air source, regulates gas boosting
Pump, oil bath heater, be adjusted to, by the temperature of experimental system, pressure, the temperature, pressure that experiment sets.
(2), tackifier are added
Open tackifier entrance and screw valve, tackifier measuring pump, plunger displacement pump, by the thickening in tackifier storage tank
Agent pumps into the supercritical carbon dioxide fracturing fluid circulatory system, and fluid flows under circulating pump effect, and tackifier exist
It is completely dissolved in supercritical carbon dioxide in clean mixed device;After parameter stability, carry out supercritical carbon dioxide
The measurement of fracturing fluid rheological characteristic;
(3), supercritical carbon dioxide fracturing fluid mean temperature in line sections is calculated
Read supercritical carbon dioxide fracturing fluid import and measure temperature T of thermometer1, thermometer is measured in outlet
Temperature T2, calculating supercritical carbon dioxide fracturing fluid mean temperature in line sections:
In formula,
T is supercritical carbon dioxide mean temperature in measuring line sections pipe, K;
T1The temperature of line sections Guan Nei import department, K is being measured for supercritical carbon dioxide fracturing fluid;
T2The temperature at line sections pipe inner outlet, K is being measured for supercritical carbon dioxide fracturing fluid;
(4), supercritical carbon dioxide fracturing fluid average pressure in line sections is calculated
Read supercritical carbon dioxide fracturing fluid import and measure manometric pressure P1, pressure gauge is measured in outlet
Pressure P2, calculating supercritical carbon dioxide fracturing fluid average pressure in line sections:
In formula,
P is supercritical carbon dioxide average pressure in measuring line sections pipe, MPa;
P1The pressure of line sections Guan Nei import department, MPa is being measured for supercritical carbon dioxide fracturing fluid;
P2The pressure at line sections pipe inner outlet, MPa is being measured for supercritical carbon dioxide fracturing fluid;
(5) supercritical carbon dioxide fracturing fluid flow velocity in measuring line sections, is calculated
Supercritical carbon dioxide fracturing fluid mass flow Q of reading quality flowmeter, calculates overcritical titanium dioxide
Carbon fracturing fluid flow velocity in measuring line sections:
Z3-(1-B)Z2+(A-3B2-2B)Z-(AB-B2-B3)=0
In formula,
Z is compressibility factor, dimensionless;
prFor reduced pressure, dimensionless;
TrFor reduced temperature, dimensionless;
W is the eccentric factor of carbon dioxide, dimensionless;
ρCO2For the density of carbon dioxide, kg/m3;
xCO2For carbon dioxide ratio in supercritical carbon dioxide fracturing fluid, dimensionless;
ρtFor the density of tackifier, kg/m3;
ρ is the density of supercritical carbon dioxide fracturing fluid, kg/m3;
xtFor tackifier ratio in supercritical carbon dioxide fracturing fluid, dimensionless;
P is absolute pressure, MPa;
T is absolute temperature, K;
MgFor the molecular weight of carbon dioxide, kg/m3;
R is universal gas constant, 0.008314MPa m3/(kmol·K);
Q is the mass flow of supercritical carbon dioxide fracturing fluid, kg/s;
D is for measuring line sections diameter, m;
U is supercritical carbon dioxide fracturing fluid flow velocity in pipeline, m/s;
(6), wall shear stress is calculated
Read the pressure differential Δ p measuring line sections differential pressure pick-up, be calculated wall shear stress:
In formula,
τwFor wall shear stress, Pa;
Δ p is the pressure differential measuring line sections differential pressure pick-up, Pa;
L is the length measuring line sections, m.
(7) constitutive relation of supercritical carbon dioxide fracturing fluid fluid rheology parameter, it is calculated
At τw—Draw logarithmic curve on coordinate, obtain corresponding different τwSlope of curve n', and then obtain
The constitutive relation of supercritical carbon dioxide fracturing fluid fluid rheology parameter:
In formula,
For supercritical carbon dioxide fracturing fluid fluid shearing rate of deformation, s-1;
N' is different τwThe logarithmic coordinates slope of curve.
The method of measurement supercritical carbon dioxide fracturing fluid rheological characteristic the most according to claim 6, its
It is characterised by, changes the temperature of experimental system, pressure, thus study supercritical carbon dioxide fracturing fluid rheology
Property is with temperature, the Changing Pattern of pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410350749.9A CN104101559B (en) | 2014-07-22 | 2014-07-22 | Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410350749.9A CN104101559B (en) | 2014-07-22 | 2014-07-22 | Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104101559A CN104101559A (en) | 2014-10-15 |
CN104101559B true CN104101559B (en) | 2016-09-07 |
Family
ID=51669889
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410350749.9A Active CN104101559B (en) | 2014-07-22 | 2014-07-22 | Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104101559B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022023567A1 (en) * | 2020-07-30 | 2022-02-03 | CLEAR SOLUTIONS (HOLDINGS) lIMITED | Fluid property sensor |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104568699B (en) * | 2014-12-29 | 2017-08-11 | 中国石油大学(华东) | The method for measuring supercritical carbon dioxide fracturing fluid leak coefficient |
CN104880385B (en) * | 2015-06-16 | 2018-03-06 | 中国华能集团清洁能源技术研究院有限公司 | A kind of anhydrous fracturing fluid test system of carbon dioxide and method of testing |
CN104880386A (en) * | 2015-06-16 | 2015-09-02 | 中国华能集团清洁能源技术研究院有限公司 | System for testing friction resistance of carbon dioxide anhydrous fracturing fluid |
CN105353084B (en) | 2015-09-30 | 2016-09-07 | 中国石油大学(华东) | Measure the device of supercritical carbon dioxide fracturing fluid restriction coefficient under different viscosities |
CN105675445B (en) * | 2016-03-25 | 2018-06-05 | 中国石油大学(华东) | Supercritical carbon dioxide capillary viscometer and application method under a kind of high temperature and pressure |
CN107389504A (en) * | 2016-05-16 | 2017-11-24 | 中国石油化工股份有限公司 | For measuring the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic |
CN106556506B (en) * | 2016-11-29 | 2019-06-07 | 中国石油大学(华东) | Measure the device of flow pattern in supercritical carbon dioxide fracturing fracture |
CN106840966B (en) * | 2017-02-23 | 2020-08-28 | 中国石油大学(华东) | Device and method for evaluating tackifying effect of polymer in supercritical carbon dioxide |
CN107063931B (en) * | 2017-05-24 | 2023-08-18 | 中国石油天然气集团有限公司 | Device and method for evaluating rheological property of carbon dioxide dry fracturing fluid |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6428702B1 (en) * | 2001-08-01 | 2002-08-06 | Berger Instruments, Inc. | Method of sample introduction for supercritical fluid chromatography systems |
CN1959372A (en) * | 2006-11-28 | 2007-05-09 | 中北大学 | Rheological behavior mensuration instrument for system of supercutical fluid - polymer |
CN101710021A (en) * | 2009-11-20 | 2010-05-19 | 中国石油大学(华东) | Detection device of physical property of natural gas supercritical flow state |
CN103196796A (en) * | 2013-04-15 | 2013-07-10 | 中国石油大学(华东) | Experimental device and method for researching viscosity property of supercritical carbon dioxide in stratum |
CN103308551A (en) * | 2013-06-05 | 2013-09-18 | 中国石油大学(华东) | Experimental device and method for measuring surface coefficient of heat transfer of supercritical carbon dioxide |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AUPR007500A0 (en) * | 2000-09-13 | 2000-10-05 | Mulvaney, Paul | Micro cantilever rheometer |
JP2003100690A (en) * | 2001-09-25 | 2003-04-04 | Dainippon Screen Mfg Co Ltd | High-pressure treating device |
-
2014
- 2014-07-22 CN CN201410350749.9A patent/CN104101559B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6428702B1 (en) * | 2001-08-01 | 2002-08-06 | Berger Instruments, Inc. | Method of sample introduction for supercritical fluid chromatography systems |
CN1959372A (en) * | 2006-11-28 | 2007-05-09 | 中北大学 | Rheological behavior mensuration instrument for system of supercutical fluid - polymer |
CN101710021A (en) * | 2009-11-20 | 2010-05-19 | 中国石油大学(华东) | Detection device of physical property of natural gas supercritical flow state |
CN103196796A (en) * | 2013-04-15 | 2013-07-10 | 中国石油大学(华东) | Experimental device and method for researching viscosity property of supercritical carbon dioxide in stratum |
CN103308551A (en) * | 2013-06-05 | 2013-09-18 | 中国石油大学(华东) | Experimental device and method for measuring surface coefficient of heat transfer of supercritical carbon dioxide |
Non-Patent Citations (3)
Title |
---|
CO2泡沫压裂液两相流流动特性的试验研究;王树众 等;《西安交通大学学报》;20030930;第37卷(第9期);975-978 * |
GRF-CO2清洁泡沫压裂液流变特性实验研究;罗向荣 等;《西安石油大学学报(自然科学版)》;20140331;第29卷(第2期);84-85 * |
新型CO2清洁泡沫压裂液性能研究;吴金桥 等;《应用化工》;20140131;第43卷(第1期);16-19 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022023567A1 (en) * | 2020-07-30 | 2022-02-03 | CLEAR SOLUTIONS (HOLDINGS) lIMITED | Fluid property sensor |
Also Published As
Publication number | Publication date |
---|---|
CN104101559A (en) | 2014-10-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104101559B (en) | Measure the device and method of supercritical carbon dioxide fracturing fluid rheological characteristic | |
CN105353084B (en) | Measure the device of supercritical carbon dioxide fracturing fluid restriction coefficient under different viscosities | |
CN104297126B (en) | low permeability reservoir gas seepage starting pressure gradient measuring device and measuring method | |
CN105840187A (en) | Method for calculating staged fracturing productivity of compact reservoir horizontal well | |
CN104990906B (en) | A kind of fracturing fluid prop-carrying capacity test system and method for testing | |
CN103645126A (en) | Determining method for stratum high-temperature high-pressure gas-phase and water-phase relative permeability curve | |
CN104777086A (en) | Device and method for measuring three-phase permeability of supercritical CO2 emulsion by steady-state flow method | |
CN103940715B (en) | The natural percolation ability analogue experiment method of rock | |
CN204514769U (en) | A kind of steady state flow method measures supercritical CO 2the device of emulsion three phase permeability | |
CN103308551A (en) | Experimental device and method for measuring surface coefficient of heat transfer of supercritical carbon dioxide | |
CN106556506B (en) | Measure the device of flow pattern in supercritical carbon dioxide fracturing fracture | |
CN205027726U (en) | Multi -functional fracture conductivity test system | |
CN206772756U (en) | A kind of dissolved gas crude oil density, the evaluating apparatus of volume factor | |
CN113340928B (en) | Experimental device and method for developing shale oil through supercritical CO2/H2O mixed fluid throughput | |
CN103439356B (en) | The experimental provision measured for supercritical carbon dioxide specific heat at constant pressure and method | |
Liang et al. | A new approach to predict field-scale performance of friction reducer based on laboratory measurements | |
CN105675445B (en) | Supercritical carbon dioxide capillary viscometer and application method under a kind of high temperature and pressure | |
CN104775809A (en) | Simulation experiment system and method of water soluble gas reservoir development | |
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 | |
CN204789530U (en) | Sand capability test device is taken to clear water fracturing fluid | |
CN103726815B (en) | A kind of CO 2drive produced well pit shaft fluidised form is determined and parameter optimization method | |
CN103969160A (en) | High-temperature high-pressure foam liquid dynamic filtration evaluation system and method | |
CN105298488A (en) | Diversion capacity testing method under non-continuous filling mode | |
CN104897521A (en) | Carbon dioxide anhydrous fracturing liquid flow conductivity testing system | |
CN106802271A (en) | A kind of measurement apparatus and method of poly- oil reservoirs fluid neuron network free-boundary problem |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |