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Method for measuring diffusion coefficient of carbon dioxide in crude oil

A carbon dioxide and diffusion coefficient technology, applied in diffusion analysis, measuring devices, instruments, etc., can solve problems such as difficulty in realization, lack of gas chromatography, adverse effects of oil production, etc., and achieve the effect of automatic control and easy operation.

Active Publication Date: 2018-11-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the process of establishing the model, the expansion of the liquid phase volume caused by the diffusion of carbon dioxide was not considered.
[0006] The standard for the determination of the diffusion coefficient of hydrocarbon gases in rocks (Petroleum and Natural Gas Industry Standard of the People's Republic of China, SY / T 6129-1995), by fixing the core in the holder, the diffusion chambers at both ends of the core are respectively injected with nitrogen and hydrocarbons Gas, through gas chromatography to measure the composition of gas at both ends under different time conditions, and the diffusion coefficient of hydrocarbon gas in porous media can be obtained through processing. ; Second, sampling the gas in the diffusion chamber at both ends will destroy the diffusion balance and cause large experimental errors
In addition, none of these measurement methods can obtain an accurate diffusion coefficient of carbon dioxide gas, and therefore cannot accurately confirm the equilibration time of carbon dioxide gas in crude oil, thereby adversely affecting oil recovery

Method used

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  • Method for measuring diffusion coefficient of carbon dioxide in crude oil
  • Method for measuring diffusion coefficient of carbon dioxide in crude oil
  • Method for measuring diffusion coefficient of carbon dioxide in crude oil

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Embodiment approach

[0048] According to one embodiment of the present invention, the testing device that described method adopts, such as figure 1 As shown, the test device includes: a test airtight container 15, a carbon dioxide airtight container 14, a crude oil airtight container 29, a vacuum pump 21, a thermostat 16, a pressure sensor 17 and a data processing device 24,

[0049] The carbon dioxide airtight container 14 and the crude oil airtight container 29 are respectively connected to the test airtight container 15, and the carbon dioxide airtight container 14 and the test airtight container 15 are arranged in the thermostat 16, and the vacuum pump 21 is used for The test airtight container 15 is evacuated, and the pressure sensor 17 is used to measure the pressure of the test airtight container 15 and transmit the pressure signal to the data processing device 24 .

[0050] Preferably, the carbon dioxide airtight container 14 is connected to the top of the test airtight container 15 , and ...

Embodiment 1

[0057] This example is used to illustrate the method of the present invention for measuring the diffusion coefficient of carbon dioxide in crude oil.

[0058] Such as figure 1 Shown, the test device that adopts during mensuration comprises: test airtight container 15, be connected to the carbon dioxide airtight container 14 of test airtight container 15 tops, be connected to the crude oil airtight container 29 of test airtight container 15 bottoms, vacuum pump 21, be provided with temperature sensor 18 Thermostat 16, pressure sensor 17, data processing device 24, the carbon dioxide feed pump 22 that is connected on the carbon dioxide airtight container 14 and the crude oil feed pump 23 that is connected to the crude oil airtight container 29, described carbon dioxide airtight container 14 and test airtight container 15 Set in the thermostat 16 , the vacuum pump 21 is connected to the pipeline 19 through the pipeline 25 , and the pressure sensor 17 is connected to the pipeline ...

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Abstract

The invention belongs to the technical field of oil-gas field development and discloses a method for measuring diffusion coefficient of carbon dioxide in crude oil. The method includes following steps: 1), filling crude oil of V0 in volume into an airtight container of VC in volume; 2), maintaining the airtight container filled with the crude oil in the step 1) at measuring temperature T constantly; 3), feeding carbon dioxide gas into the constant-temperature airtight container in the step 2), and measuring pressure P (t) of the carbon dioxide gas once from starting time t0 every other delta ttime until balanced pressure is realized; 4), utilizing expansion coefficient beta of the crude oil dissolved with carbon dioxide and combining with a relation between diffusion time t and the pressure P (t) to obtain the diffusion coefficient DAB of carbon dioxide in the crude oil, wherein a formula in the step 4) is show as follows. The method takes the circumstance that the crude oil expands in volume after carbon dioxide is diffused into the crude oil into consideration, so that the diffusion coefficient of carbon dioxide in the crude oil can be measured more accurately.

Description

technical field [0001] The invention belongs to the technical field of oil and gas field development, in particular to a method for measuring the diffusion coefficient of carbon dioxide in crude oil. Background technique [0002] In the development of oil and gas fields, the use of carbon dioxide flooding can enhance the recovery of crude oil, so carbon dioxide oil recovery technology has been widely used. The steps of using carbon dioxide to recover oil are as follows: First, a certain amount of carbon dioxide gas is injected into the oil layer, then the well is shut down to balance the diffusion of carbon dioxide in the crude oil, and finally the well is opened for oil recovery. In order to predict the time when carbon dioxide reaches equilibrium in crude oil, it is necessary to know the diffusion coefficient of carbon dioxide in crude oil. If the diffusion coefficient is inaccurate, the equilibrium time cannot be accurately confirmed, which will adversely affect oil recov...

Claims

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Application Information

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IPC IPC(8): G01N13/00
CPCG01N13/00G01N2013/003
Inventor 王海涛伦增珉吕成远郎东江骆铭潘伟义王锐赵春鹏周霞赵淑霞王友启
Owner CHINA PETROLEUM & CHEM CORP
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