CN108627417A - The test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir - Google Patents

The test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir Download PDF

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Publication number
CN108627417A
CN108627417A CN201810503993.2A CN201810503993A CN108627417A CN 108627417 A CN108627417 A CN 108627417A CN 201810503993 A CN201810503993 A CN 201810503993A CN 108627417 A CN108627417 A CN 108627417A
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pressure
temperature
water
gas
natural gas
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雷霄
王雯娟
陈健
杨朝强
刘鹏超
成涛
韩鑫
张风波
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China National Offshore Oil Corp CNOOC
CNOOC China Ltd Zhanjiang Branch
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China National Offshore Oil Corp CNOOC
CNOOC China Ltd Zhanjiang Branch
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N7/00Analysing materials by measuring the pressure or volume of a gas or vapour
    • G01N7/02Analysing materials by measuring the pressure or volume of a gas or vapour by absorption, adsorption, or combustion of components and measurement of the change in pressure or volume of the remainder
    • G01N7/04Analysing materials by measuring the pressure or volume of a gas or vapour by absorption, adsorption, or combustion of components and measurement of the change in pressure or volume of the remainder by absorption or adsorption alone

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Abstract

The invention discloses the test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir, include the following steps:Live natural gas, stratum water sampling;Temperature and pressure are adjusted to specified temperature and pressure point, gas solubility data in water flooding are obtained;PVT constant temperature and pressure condition lower volume sizes before and after water sample are quantitatively injected in monitoring, and temperature, pressure are recorded after stablizing, after be adjusted to next temperature and pressure point, and measure the multigroup experimental data of acquisition;It builds and is saturated water vapour content computation model in natural gas, bring temperature, pressure, bulking value that experiment measures into saturated steam content calculation model, obtain the natural gas saturated steam content under different temperatures and pressure.High temperature and pressure natural gas saturated steam content accurately can be measured and be calculated with this method, while the demand to sample is few, metering is convenient and efficient, and metric results are reliable, which has stronger versatility.

Description

The test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir
Technical field
The present invention relates to the streams that in a kind of oil-gas exploration and development technology, high temperature and pressure gas reservoir condensation water content is tested and calculated The acquisition methods of water vapour content in body assessment technique, in particular to high temperature and pressure reservoir.
Background technology
High temperature and pressure gas reservoir is influenced by reservoir environment, and saturation has a certain amount of water flooding in natural gas, as failure is opened The cooling release of natural gas during adopting can cause saturation steam content in natural gas to change, generate condensation water.In order to bright True gas reservoir condensation water precipitation mechanism is provided fundamental basis, it is necessary to understand fully for the anticipation of condensation water hydrops risk and prevention and control countermeasure The size variation rule of gas reservoir and pit shaft inside natural gas condensation water content under different Temperature-pressure Conditions in production process.Due to gas Condensation water content often not necessarily can be especially high in phase, while further relating to high temperature and pressure, therefore the test of condensation water content is to instrument Precision and instrument temperature and pressure performance requirement are very high.However conventional test methodologies have following intrinsic defect:(1) it is needed when measuring A large amount of samplings, since condensation water content is smaller in gas phase, will reduce error, while reaching the test scope of balance, need from PVT Cylinder lower end largely samples, and causes experiment material waste larger, and cost increases, and sample and sample transfer number increase;(2) liquid in pipeline Water causes error big, due to being related to constant temperature and pressure sample transfer, necessarily refers to connecting pipeline during sample transfer, inevitable face in experimentation Lin Ningxishui is precipitated to influence condensation water content final test precision in pipeline;(3) pipeline dead volume causes error big, surveys Various pipelines will lead to a certain amount of dead volume in examination flow, and it is gentle that dead volume can cause to be difficult to accurately to detect condensation water quality Body volume, so that natively relatively low condensation water content can be lower, error becomes larger.
Invention content
It is accurate evaluation high temperature and pressure gas reservoir condensation water content and variation for these intrinsic defects of conventional test methodologies Rule, the technical solution adopted in the present invention are:The test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir, Include the following steps:
S1, gas well at HTHP sampling fluids:Using sample apparatus high temperature and pressure gas is obtained from high temperature and pressure gas field well site Well fluids sample;
S2 obtains gas solubility data in water flooding:Injecting water flooding and natural gas, stirred sample to PVT instrument makes Inner barrel temperature and pressure are balanced to test point temperature and pressure state, are sampled from PVT instrument lower end, and sample is cooled down and is precipitated in sampler Water Soluble Gas passes through testing flow meter water-soluble tolerance by electronic balance formation testing water.
S3 obtains multigroup PVT cylinders volume data:Appropriate natural gas is added to PVT instrument, monitors gas well at HTHP fluid-like Volume of the product under target temperature, pressure, record temperature, pressure, volume after balance;Appropriate water flooding is added to PVT, changes Temperature, record temperature, pressure, volume after balance;Obtain the multi-group data being made of volume, temperature parameter and pressure parameter;
S4 builds and is saturated water vapour content calculation formula in natural gas:It at high temperature under high pressure can be most using gas sample and water sample Reach air water balance eventually, the state change before and after water sample is added according to gas sample under constant Temperature-pressure Conditions, is based on material balance principle It builds and is saturated water vapour content calculation formula in natural gas;
S5 obtains condensation water content:According under the conditions of constant temperature and pressure monitor natural gas injection water flooding before and after volume, In conjunction with gas solubility test result in water flooding, you can accurately calculate natural gas saturated steam content.
As the preferred technical solution of the present invention, the step S2, S3 are measured in experiment, and equipment used is more Function high-temperature, high pressure fluid PVT analyzers.
As the preferred technical solution of the present invention, in the step S2, gas solubility measures in water flooding When inject excessive natural gas to PVT instrument and measure natural gas filling using high-precision gas flowmeter and enter amount.
As the preferred technical solution of the present invention, in the step S3, multi-group data is according to the temperature and pressure model of reservoir Setting is enclosed, upper limit temperature and pressure are reservoir temperature and pressure, and 10 DEG C of temperature interval, low temperature widens interval.
Water vapour content is saturated as the preferred technical solution of the present invention, in the step 4, in natural gas to calculate Formula is as follows:Wherein Vw is to be saturated water vapour content, mol/ in natural gas mol;P is pressure, MPa;Wg is saturated steam volume in natural gas;V1 is stable volume under the conditions of natural gas constant temperature and pressure, ml;W injects constant pressure and injects stratum water volume;The molal weight of Mw water;R is mol gas constant;Vg is natural gas in water flooding Content, ml;P is designated as standard state pressure, MPa.
Beneficial effects of the present invention:It is proved by actual production validity check, acquisition can be significantly improved using this method The accuracy of high temperature and pressure gas reservoir condensation water content, and then the prediction of high temperature and pressure gas reservoir condensation water content is improved based on experimental result Precision, have stronger versatility.The present invention provides more preferable more acurrate for the acquisition of high temperature and pressure gas field condensation water content Method.
Description of the drawings
Invention is further described in detail with reference to the accompanying drawings and detailed description:
Fig. 1 is the flow chart of the present invention.
Specific implementation mode
As shown in Figure 1, the test of condensation water content and calculating side under the conditions of a kind of high temperature and pressure gas reservoir described in the present embodiment Method, it includes the following steps:
S1, gas well at HTHP sampling fluids:Using sample apparatus high temperature and pressure gas is obtained from high temperature and pressure gas field well site Well fluids samples include stratum water sample and natural gas sample;
S2 obtains gas solubility data in water flooding:1. injecting excessive water flooding and natural gas to PVT instrument;2. will PVT temperature are adjusted to test temperature point;3. PVT pressure are adjusted to test pressure point;4. PVT instrument constant pressures, stirred sample, Inner barrel temperature and pressure are made to balance to test point temperature and pressure state;5. constant voltage mode is from PVT instrument lower end water sampling, test natural gas is on ground Solubility in layer water;6. adjusting next group of temperature and pressure, 2. -5. experimentation is repeated;7. obtaining being joined by solubility, temperature The multi-group data that number and pressure parameter are constituted.
S3 obtains multigroup PVT cylinders volume data:Appropriate natural gas first is added toward PVT instrument, monitors gas well at HTHP fluid Volume of the sample under target temperature, pressure, record temperature, pressure, volume after balance;Then appropriate stratum is added to PVT Water measures PVT cylinders product under set temperature and pressure, obtains being made of volume, temperature parameter and pressure parameter more respectively Group data;
S4 builds and is saturated water vapour content calculation formula in natural gas:It at high temperature under high pressure can be most using gas sample and water sample Reach air water balance eventually, the state change before and after water sample is added according to gas sample under constant Temperature-pressure Conditions, is based on material balance principle It builds and is saturated water vapour content calculation formula in natural gas.
Its specific implementation step is as follows:Since gas sample and water sample can be finally reached air water balance at high temperature under high pressure, in gas Main during water balance that two variations occur, part water sample evaporates into gas sample and gas sample dissolving in part enters water sample.Therefore, Volume of the gas sample under target temperature, pressure can be monitored, quantitative water sample is then added, volume change is monitored after balance.Respectively Part variation can be calculated in accordance with the following methods.Assuming that under the conditions of constant temperature and pressure:
It is Vw, mol/mol that water vapour content is saturated in natural gas;
Natural Gas content is Vg, ml in water flooding;
Stable volume is V1, ml under the conditions of natural gas constant temperature and pressure;
Constant pressure is injected stratum water volume and is injected for W, ml;
Volume is V2, ml after stablizing under same temperature and pressure after injection water flooding;
Inject liquid storage amount after water flooding constant temperature and pressure balances:L, ml;
The natural gas volume being dissolved into water flooding:Gw, ml;
Saturated steam volume in natural gas:Wg, ml;
The compressed coefficient of water is:Cw ,/MPa;
The molal weight of water:Mw, g/mol.
Therefore, PVT volume changes are after water sample is added in constant temperature and pressure:
Δ V=V2-V1=steam vapour amount-water-soluble tolerance+liquid storage amount=Wg-Gw+L(1)
Saturated steam volume is in natural gas:
Wg=(dry gas volume-water-soluble air volume) × Vw=(V1-Gw)×Vw(2)
The natural gas volume being dissolved into water flooding is:
After air water balance, PVT internal liquid volumes (liquid storage amount) are:
Due to injecting volume of water sample very little itself, the corresponding very little of dissolving gas sample volume, volume smaller after water-soluble liquid state, body Product can be ignored, therefore simultaneous equations (1) to (4) can obtain saturated steam volume in natural gas and be:
Water vapour content is saturated in natural gas is:
Natural gas can be calculated in spy by PVT constant temperature and pressure condition lower volume sizes before and after monitoring quantitatively injection water sample Determine the condensation water content under Temperature-pressure Conditions.
S5 obtains condensation water content:According under the conditions of constant temperature and pressure monitor natural gas injection water flooding before and after volume, In conjunction with gas solubility test result in water flooding, you can accurately calculate natural gas saturated steam content.
The above described is only a preferred embodiment of the present invention, be not intended to limit the present invention in any form, though So the present invention has been disclosed as a preferred embodiment, and however, it is not intended to limit the invention, any technology people for being familiar with this profession Member, without departing from the scope of the present invention, when the technology contents using the disclosure above make a little change or modification For the equivalent embodiment of equivalent variations, as long as being the content without departing from technical solution of the present invention, according to the technical essence of the invention To any simple modification, equivalent change and modification made by above example, in the range of still falling within technical solution of the present invention.

Claims (5)

1. the test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir, which is characterized in that include the following steps:
S1, gas well at HTHP sampling fluids:Using sample apparatus gas well at HTHP stream is obtained from high temperature and pressure gas field well site Body sample;
S2 obtains gas solubility data in water flooding:Water flooding and natural gas are injected to PVT instrument, makes inner barrel temperature and pressure Balance is sampled from PVT instrument lower end to test point temperature and pressure state, and sample is cooled down in sampler and be precipitated Water Soluble Gas, is passed through Electronic balance formation testing water, passes through testing flow meter water-soluble tolerance;
S3 obtains multigroup PVT cylinders volume data:Appropriate natural gas is added to PVT instrument, monitoring gas well at HTHP fluid sample exists Volume under target temperature, pressure, record temperature, pressure, volume after balance;Appropriate water flooding is added to PVT, changes temperature It spends, record temperature, pressure, volume after balance;Obtain the multi-group data being made of volume, temperature parameter and pressure parameter;
S4 builds and is saturated water vapour content calculation formula in natural gas:It can finally be reached at high temperature under high pressure using gas sample and water sample It is balanced to air water, the state change before and after water sample is added according to gas sample under constant Temperature-pressure Conditions, is built based on material balance principle Water vapour content calculation formula is saturated in natural gas;
S5 obtains condensation water content:According under the conditions of constant temperature and pressure monitor natural gas injection water flooding before and after volume, in conjunction with Gas solubility test result in water flooding, you can accurately calculate natural gas saturated steam content.
2. the test of condensation water content and computational methods, special under the conditions of a kind of high temperature and pressure gas reservoir according to claim 1 Sign is:The step S2, S3 are measured in experiment, and equipment used is multifunctional high-temperature high-pressure fluid PVT analyzers.
3. the test of condensation water content and computational methods, special under the conditions of a kind of high temperature and pressure gas reservoir according to claim 1 Sign is:In the S2, natural gas is injected to PVT instrument when gas solubility measures in water flooding and use high-precision gas Flowmeter measures natural gas filling and enters amount.
4. the test of condensation water content and computational methods, special under the conditions of a kind of high temperature and pressure gas reservoir according to claim 1 Sign is:In the step 3, multi-group data is set according to the temperature and pressure range of reservoir, and upper limit temperature and pressure are reservoir temperature and pressure, temperature interval 10 DEG C, low temperature widens interval, pressure intervals 10MPa.
5. the test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir according to claim 1,
It is characterized in that, it is as follows to be saturated water vapour content calculating formula in step s 4, in natural gas:
Wherein Vw is to be saturated water vapour content, mol/mol in natural gas;P is pressure, MPa;Wg is saturated steam in natural gas Volume;V1 is stable volume under the conditions of natural gas constant temperature and pressure, ml;W injects constant pressure and injects stratum water volume;Mole matter of Mw water Amount;R is mol gas constant;Vg is natural Gas content in water flooding, ml;P is designated as standard state pressure, MPa.
CN201810503993.2A 2018-05-23 2018-05-23 The test of condensation water content and computational methods under the conditions of a kind of high temperature and pressure gas reservoir Withdrawn CN108627417A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110378075A (en) * 2019-08-19 2019-10-25 西南石油大学 A kind of acid and nonacid natural gas water content amount prediction technique
CN111257533A (en) * 2020-02-13 2020-06-09 西南石油大学 Method for measuring content of water vapor in natural gas
CN115788385A (en) * 2022-12-29 2023-03-14 西南石油大学 Method for determining condensate water-gas ratio of high-temperature condensate gas reservoir
CN117009718A (en) * 2023-10-07 2023-11-07 西南石油大学 Water supplementing quantity calculation model and method for preventing salt formation of gas storage

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102135484A (en) * 2010-12-16 2011-07-27 西南石油大学 Device and method for testing gas-water ratio of underground sample with water gas reservoir and water soluble gas reservoir
US20140076553A1 (en) * 2010-12-30 2014-03-20 Eni S.P.A. Upstream-downstream integrated process for the upgrading of a heavy crude oil with capture of co2 and relative plant for the embodiment thereof
CN104775809A (en) * 2015-02-07 2015-07-15 中国石油大学(华东) Simulation experiment system and method of water soluble gas reservoir development
CN106568912A (en) * 2016-11-03 2017-04-19 西南石油大学 Method and apparatus for testing solubility of acidic gas in high temperature high pressure stratum water
CN107045671A (en) * 2017-03-22 2017-08-15 重庆科技学院 Water-producing gas well hydrops Risk Forecast Method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102135484A (en) * 2010-12-16 2011-07-27 西南石油大学 Device and method for testing gas-water ratio of underground sample with water gas reservoir and water soluble gas reservoir
US20140076553A1 (en) * 2010-12-30 2014-03-20 Eni S.P.A. Upstream-downstream integrated process for the upgrading of a heavy crude oil with capture of co2 and relative plant for the embodiment thereof
CN104775809A (en) * 2015-02-07 2015-07-15 中国石油大学(华东) Simulation experiment system and method of water soluble gas reservoir development
CN106568912A (en) * 2016-11-03 2017-04-19 西南石油大学 Method and apparatus for testing solubility of acidic gas in high temperature high pressure stratum water
CN107045671A (en) * 2017-03-22 2017-08-15 重庆科技学院 Water-producing gas well hydrops Risk Forecast Method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
任星明: "东方13-1高温高压气藏凝析水析出规律及积液风险研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
范泓澈 等: "高温高压条件下甲烷和二氧化碳溶解度试验", 《中国石油大学学报(自然科学版)》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110378075A (en) * 2019-08-19 2019-10-25 西南石油大学 A kind of acid and nonacid natural gas water content amount prediction technique
CN110378075B (en) * 2019-08-19 2022-02-25 西南石油大学 Method for predicting water content of acidic and non-acidic natural gas
CN111257533A (en) * 2020-02-13 2020-06-09 西南石油大学 Method for measuring content of water vapor in natural gas
CN115788385A (en) * 2022-12-29 2023-03-14 西南石油大学 Method for determining condensate water-gas ratio of high-temperature condensate gas reservoir
CN115788385B (en) * 2022-12-29 2024-05-24 西南石油大学 Determination method for condensate water-gas ratio of high Wen Ningxi gas reservoir
CN117009718A (en) * 2023-10-07 2023-11-07 西南石油大学 Water supplementing quantity calculation model and method for preventing salt formation of gas storage
CN117009718B (en) * 2023-10-07 2023-12-12 西南石油大学 Water supplementing quantity calculation model and method for preventing salt formation of gas storage

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