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A kind of defoamer for oil and gas separation

A defoaming agent and defoaming technology, which is applied in the field of preparation of crude oil defoaming agent and defoaming agent for oil and gas separation in heavy oil oil fields, can solve the problems of poor degassing effect, achieve the reduction of foam interface strength and continuous degassing effect of effect

Active Publication Date: 2018-10-09
CHINA NAT OFFSHORE OIL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] In order to solve the problems existing in the prior art, the object of the present invention is to develop a high-efficiency crude oil-gas separation defoamer modified by polyether silicone oil, to overcome the degassing effect of ordinary crude oil defoamers in the prior art on heavy oil fields bad question

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  • A kind of defoamer for oil and gas separation
  • A kind of defoamer for oil and gas separation
  • A kind of defoamer for oil and gas separation

Examples

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example 1

[0039] Based on the synthesis of a high-efficiency crude oil-gas separation defoamer, the mass fraction is 7.19% of hydrogen-containing polydimethylsiloxane, 14.39% of allyl polyoxyethylene-polyoxypropylene ether, mass fraction of 25.61% organic solvent, 0.06% mass fraction of platinum catalyst, 1.92% mass fraction of low-molecular siloxane, 3.46% mass fraction of defoaming synergist, and 47.37% mass fraction of dispersant , the synthesis steps are as follows:

[0040] (1) First mix 56.2g of hydrogen-containing polydimethylsiloxane, 112.4g of allyl polyoxyethylene-polyoxypropylene ether, and 200g of xylene, blow in nitrogen for protection, and heat up to 100°C; add 0.5g 1% chloroplatinic acid-isopropanol solution, the temperature is controlled at 110°C, and the reaction is continued for 3 hours;

[0041] (2) Add 15 g of heptamethyltrisilane to the reaction product in step (1), control the temperature at 90° C., and continue the reaction for 1 hour;

[0042] (3) Add 17g tribu...

example 2

[0044] Based on the synthesis of a high-efficiency crude oil-gas separation defoamer, the mass fraction is 5% hydrogen-containing polydimethylsiloxane, 5% allyl polyoxyethylene-polyoxypropylene ether, mass fraction 30% organic solvent, 0.01% mass fraction of platinum catalyst, 1% mass fraction of low-molecular siloxane, 5% mass fraction of antifoam synergist, and 53.99% mass fraction of dispersant , the synthesis steps are as follows:

[0045] (1) First mix 50g of hydrogen-containing polydimethylsiloxane, 50g of allyl polyoxyethylene-polyoxypropylene ether, and 300g of toluene, blow in nitrogen for protection, and heat up to 120°C; add 0.1g of Pt— Divinyltetramethyldisiloxane complex, the temperature is controlled at 140°C, and the reaction is continued for 2 hours;

[0046] (2) Add 10 g of tetramethyldihydrodisiloxane to the reaction product in step (1), control the temperature at 100° C., and continue the reaction for 0.5 hours;

[0047] (3) Add 20 g of ethyl acetate, 30 g...

example 3

[0049] Based on the synthesis of a high-efficiency crude oil-gas separation defoamer, the mass fraction is 10% hydrogen-containing polydimethylsiloxane, 20% allyl polyoxyethylene-polyoxypropylene ether, mass fraction 20% organic solvent, 0.1% mass fraction of platinum catalyst, 5% mass fraction of low-molecular siloxane, 1% mass fraction of antifoam synergist, and 43.9% mass fraction of dispersant , the synthesis steps are as follows:

[0050](1) First mix 100g of hydrogen-containing polydimethylsiloxane, 200g of allyl polyoxyethylene-polyoxypropylene ether, and 200g of ethylene glycol, blow in nitrogen for protection, and heat up to 110°C; then add 0.5g Pt-divinyltetramethyldisiloxane complex and 0.5g of 1% chloroplatinic acid-isopropanol solution, the temperature is controlled at 125 ° C, and the reaction is continued for 2.5 hours;

[0051] (2) Add 30.4 g of tetramethyldihydrodisiloxane and 19.6 g of heptamethyltrisilane to the reaction product in step (1), control the tem...

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Abstract

The invention relates to a defoamer for oil-gas separation. The defoamer is prepared in the way of synthesizing polyether modified silicone firstly under the action of a catalyst based on organic solvent dispersion and nitrogen protection with hydrogen-containing polydimethylsiloxane and allyl polyoxyethylene-polyoxypropylene ether as raw materials, then conducting further modification by means of low-molecular siloxane, and finally conducting synergist and dispersant compounding. By the adoption of the defoamer, bubbles generated during oil-gas separation of crude oil can be eliminated quickly, and oil-gas separation effect in a thickened oil field is especially good. The defoamer can be directly added to foaming liquid to be used, and can also be added after being diluted by 5-20 times with varsol. Compared with other crude oil defoamers, the defoamer for oil-gas separation has the advantages of being low in usage amount, capable of achieving defoaming fast and good in foam inhibition effect. Especially for high-viscosity thickened oil fields, the defoamer has a more efficient, stable and durable degassing effect compared with ordinary organosilicone crude oil defoamers, polyether type crude oil defoamers and polyether silicon oil defoamers. The defoamer can be applied and popularized.

Description

technical field [0001] The invention belongs to the field of chemical defoaming, and relates to a crude oil defoaming agent, in particular to a preparation method of a defoaming agent for oil-gas separation in heavy oil oilfields. Background technique [0002] When crude oil is produced from the oil well, the associated gas originally dissolved in the crude oil is gradually separated from the crude oil due to pressure drop and temperature change. In the Bohai Oilfield, crude oil is generally characterized by waxy content, high asphaltenes, and high viscosity, which makes it difficult for associated gas to escape smoothly from the surface of crude oil. [0003] If the gas in the crude oil cannot be removed quickly and completely, after the oil-gas mixture enters the separator, the liquid level measurement of the separator will be inaccurate, which will cause fluctuations in the entire production process; the associated gas will carry a large number of oil droplets into the ga...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D19/04C10G31/00
CPCB01D19/0404B01D19/0409C10G31/00
Inventor 胡廷程艳张颖郭海军王磊逯学朝
Owner CHINA NAT OFFSHORE OIL CORP