Exploitation method for wax precipitation oil reservoir

A technology of oil reservoir exploitation and wax type, which is applied in the direction of exploitation fluid, chemical instruments and methods, earthwork drilling and production, etc. It can solve the problem of exacerbating wax precipitation in crude oil, cannot effectively inhibit the growth of wax crystals, block the pores of oil layers, and cause heat loss. Avoid problems such as

Active Publication Date: 2010-09-22
盘锦河升大地石油科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the following disadvantages when directly applied to wax-type oil reservoirs: first, it is severely restricted by the complexity of the geological conditions of the oil reservoirs, and it is difficult to inject steam; It is difficult to use a large amount of high-temperature and high-pressure steam in a waxy oil reservoir; third, the temperature of the entire waxy oil reservoir and the crude oil must be kept much higher than the waxy temperature of crude oil during the entire oil recovery process, so not only must a large amount of steam be consumed , and because the heat capacity of the reservoir is huge, the loss of heat dissipation is serious and unavoidable, it is difficult to guarantee the reservoir temperature; fourth, the steam method is complicated, and it is difficult to control the steam temperature, dryness and reservoir temperature field; fifth, the method requires The higher the temperature of the steam, the better. The higher the steam temperature, the lower the corresponding cost. The steam below 200 °C is not only expensive but also less effective, and the high steam temperature will cause serious thermal expansion and contraction of the wellbore of ordinary oil wells, which will cause It will cause great damage to the wellbore structure of ordinary oil wells. The production test proves that it is difficult to directly use high-temperature steam above 200°C in ordinary oil wells; Sixth, in order to solve the problem of water scaling during steam production, it is necessary to specialize the water used to generate steam. softening, resulting in a substantial increase in the cost of steam production; Seventh, the generation of steam requires a large amount of energy, and a special thermal recovery well structure design must be adopted, which will double the construction costs of oil well drilling, cementing, and well completion, resulting in The cost of oil production has risen sharply, and the energy consumption has increased significantly
The direct application of this method to wax-type oil reservoirs has the following defects: First, due to the severe constraints of the geological conditions of the reservoir, the survival rate and reproduction rate of microorganisms in wax-type oil reservoirs are low, resulting in the limited ability of microorganisms to consume wax molecules. The method has limited effect on crude oil with high wax content; second, microorganisms need a long breeding period to effectively reduce the wax content of crude oil in the reservoir and then reduce the wax precipitation temperature, so this method will lead to a significant reduction in the effective production time of the oil well
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Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0415] A method for producing a wax-precipitating oil reservoir, comprising the following steps: adding chemical agents and thermal fluids to the oil layer, which melt the wax crystals in the oil layer, and simultaneously reduce the wax-precipitating temperature of the crude oil in the oil layer, so that the crude oil in the oil layer can be processed smoothly. Seepage into the well, from which the crude oil is lifted to the surface.

[0416] The chemical agent is mixed methylnaphthalene; the hot fluid is oilfield sewage at 95-100°C.

[0417] Take Jing 35-31-41 well and apply the present invention as example:

[0418] The public information of Liaohe Oilfield shows that Well Jing 35-31-41 belongs to the eastern oil well of Block Jing 35. It was completed and put into production on May 16, 1994. The well was shut down due to low fluid production and high water cut. The well was reopened in October 2006. The daily liquid production is 1-2 tons / day, the water content is 100%, an...

Embodiment 2

[0430] Repeat Example 1, the difference is that before adding chemical agents and thermal fluids to the oil reservoir, the preparatory steps for operations such as well washing, well opening, replacement of pipe strings, and maintenance have been taken:

[0431] Take Jing 35-30-38 well and apply the present invention as example.

[0432] According to the data of the well, the freezing point of the crude oil is 50°C. After the oil well shuts down, the crude oil in the tubing and casing may solidify, which makes it impossible to implement the technical scheme of adding chemical agents and thermal fluids to the oil layer through the casing or tubing of the well. According to this, after the oil well shuts down, the oilfield sewage above 80°C can be used to wash the well, and the 80°C oilfield sewage can be added to the casing of the well, and then let it come out of the oil pipe and enter the surface process, so that the oilfield sewage can be used to clean the well. Replace the ...

Embodiment 3

[0435] A method for producing a wax-type oil reservoir, comprising the following steps: in order to prevent the disadvantage of adding too much chemical agent and thermal fluid to the oil layer at one time, add the chemical agent and thermal fluid to the oil layer around the oil well, and then let the chemical agent and thermal fluid The thermal fluid returns to the oil well along with the seepage of crude oil in the oil layer and rises to the surface through the oil well, realizing the chemical agent-thermal fluid combined huff and puff oil recovery mode (or process) of the oil layer around the oil well, through the oil well, using existing methods (such as pumping ) Add chemical agents and thermal fluids into the oil layer around the oil well to melt (or melt) the wax crystals in the oil layer, reduce the wax precipitation temperature of crude oil in the oil layer, and make the mixture of crude oil, chemical agents and thermal fluid in the oil layer seep smoothly Return to th...

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Abstract

The invention discloses an exploitation method for a wax precipitation oil reservoir. The method comprises the step of adding a chemical agent and thermal fluid into an oil layer to make crude oil in the oil layer smoothly seep into an oil well and then rise to the ground surface. The method has the advantages of effectively solving the problem of wax precipitation of the crude oil in the oil layer and exploiting the wax precipitation oil reservoir, greatly reducing the exploitation cost of the wax precipitation oil reservoir, prolonging the production period and increasing the yield of the oil well and enhancing the final recovery efficiency of the oil reservoir, along with easy implementation, safety and reliability and obvious economic benefit.

Description

technical field [0001] The invention relates to a crude oil recovery method, in particular to a wax analysis type oil recovery method. Background technique [0002] At present, in crude oil production and exploitation, it is inevitable to exploit wax-type oil reservoirs. This type of waxy oil reservoir or because the original temperature is less than or equal to the waxy temperature of the crude oil contained in the oil reservoir, the contained crude oil has produced or precipitated wax crystals under the original conditions of the reservoir; or although this type of waxy oil reservoir is originally The temperature is higher than the wax precipitation temperature of the crude oil contained in the reservoir, but when the contained crude oil seeps in the reservoir, the temperature of the crude oil will be lower than the wax precipitation temperature due to the vaporization and heat absorption of light hydrocarbons and natural gas. Wax crystals are produced or precipitated in ...

Claims

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Application Information

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IPC IPC(8): E21B43/16E21B43/22E21B43/24C09K8/592C09K8/588C09K8/584
Inventor 李向东
Owner 盘锦河升大地石油科技有限公司
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