|Publication number||USRE32742 E|
|Application number||US 06/910,290|
|Publication date||Sep 6, 1988|
|Filing date||Sep 17, 1986|
|Priority date||Aug 16, 1979|
|Also published as||CA1140324A, CA1140324A1, US4385935|
|Publication number||06910290, 910290, US RE32742 E, US RE32742E, US-E-RE32742, USRE32742 E, USRE32742E|
|Original Assignee||Elkem A/S|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (11), Referenced by (28), Classifications (19), Legal Events (3)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This is .Iadd.a continuation of application Ser. No. 739,181 filed May 30, 1985, abandoned, which is a reissue of Ser. No. 324,559 filed Nov. 24, 1981 which was .Iaddend.a continuation of application Ser. No. 198,668, filed Oct. 20, 1980, which was a continuation-in-part of application Ser. No. 177,872, filed Aug. 14, 1980, both now abandoned.
The invention relates to a method of producing a cement slurry of low specific weight suitable for use in the cementation of oil-and gas wells. It also relates to the composition of the cement slurry.
In the cementation of oil-or gas wells a cement slurry is pumped into the well through a form pipe. The slurry will gradually fill the empty space between the wall of the pipe and the wall of the well. The specific weight of the cement slurry is of the greatest importance in the process of cementation of the well. For instance, in drilling wells through high pressure zones, a cement slurry with a high specific weight is required in order to resist and control the flowing during the cementation process. However, in drilling wells through low pressure zones, as well as zones in which drilling mud may easily penetrate, it is necessary to utilize a cement slurry with a low specific weight. An object of the invention is to produce a cement slurry of low specific weight which is suitable for the cementation of oil and gas wells.
It is known that the specific weight of a cement slurry can be reduced by increasing the amount of water in the slurry. In order to absorb the increased quantity of water, other materials such as bentonite, pozzolan, diatomaceous earth, perlite, water glass and/or gilsonite are added. Of these materials, bentonite is today most frequently used in cement slurries, and usually employed in concentration constituting from 1-12% of the weight of the cement. By addition of 12% bentonite, one will obtain a specific weight of the slurry of 12.6 lbs./gallons corresponding to 15 kg/dm. When using water glass, pozzolan and diatomaceous earth, the relatively high content of silica in these materials will tend to bind that calcium hydroxide which is formed during the hardening of the cement and transform it to a more insoluble and stable component. Therefore, the employment of these materials will result in a relatively higher strength after hardening than is obtained through the use of bentonite.
It has been discovered that finely divided amorphous silica dust which has been obtained as an emission product during the electrothermal preparation of ferrosilicon and/or silicon metal can be used in the cement slurries for cementation of oil-gas wells.
In the method according to the invention, the amorphous silica dust are mixed with an API (American Petroleum Institute) approved oil-well cement. The amount of amorphous silica dust (obtained as an emission product) which is to be added is in the range of 1-50% by weight of the dry materials.
The emission products comprise amorphous silica in the range of from 82-95% of the total emission product. For example, the amorphous silica particles may comprise at least 82% by weight of SiO2, will have a real density of approximately 2.2-2.5 g/cm2 and will have a specific surface area of 18-22 m2 /g, the particles being substantially spherical, and wherein at least 60% by weight of the particles have a particle size less than 1 micron. It is, of course, well known that variation of these values is readily possible depending upon the parameters of the electrothermal processing.
The amorphous silica dust or the emission products comprising chiefly the amorphous SiO2 can either be mixed in the dry state with the oil well cement to which there is then added a sufficient quantity of water to obtain a slurry having specific densities in the range of 10-16 lbs./gallon corresponding to 1.19-1.91 kg/dm3. As is known, the amount of water can be reduced by the addition of dispersion materials. Of course, other known concrete additives may also be used as desired.
It will be appreciated that it is also possible to produce a slurry of the emission products and any dispersion components and to deliver this product as a slurry to a site where it will be mixed with the oil well cement. The ratio of mixture in this case and the specific weight will remain the same as when the emission products are mixed with the cement in the dry state.
By mixing a ratio of amorphous silica dust/cement of 33:67, there may be obtained specific weights in the range of 11.5-15.5 lbs./gallon corresponding to 1.37-1.85 kg/dm3 and a compressive strength of 3890 psi corresponding to 27.3 kg/cm2 with dispersion components and 440 psi corresponding to 30.93 kg/cm2 without additives. The compressive strength here referred to are obtained after 24 hours at 95° F. corresponding to 35° C. at atmospheric pressure. For instance, the addition of a quantity of water amounting to 92.7% of weight of the mixture will give a specific weight of the slurry of 12.6 lbs/gallon corresponding to 15 kg/dm2. If a higher specific density is desired a dispersion component must be added.
Upon hardening, the above described slurry will provide a tight concrete with few pores and high compression strength. The density is highly important, particularly in offshore operations, in order to prevent the penetration of the oil and gas in one formation into another formation.
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|Citing Patent||Filing date||Publication date||Applicant||Title|
|US5149370 *||Oct 21, 1991||Sep 22, 1992||Halliburton Company||Well cement compositions having improved properties and methods|
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|US5327968 *||Dec 30, 1992||Jul 12, 1994||Halliburton Company||Utilizing drilling fluid in well cementing operations|
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|US20100270016 *||Oct 28, 2010||Clara Carelli||Compositions and Methods for Servicing Subterranean Wells|
|US20100273912 *||Jul 9, 2010||Oct 28, 2010||Halliburton Energy Services, Inc.||Cement Compositions Comprising Latex and a Nano-Particle|
|U.S. Classification||106/812, 116/292, 106/607, 106/698, 106/633, 106/737, 106/631|
|International Classification||C09K8/46, C04B18/14, C09K8/42|
|Cooperative Classification||C04B28/02, C04B18/146, C09K8/46, C09K8/42, Y02W30/94|
|European Classification||C09K8/42, C04B18/14F, C09K8/46, C04B28/02|
|Nov 6, 1990||FPAY||Fee payment|
Year of fee payment: 8
|Jan 2, 1991||REMI||Maintenance fee reminder mailed|
|Sep 2, 1994||FPAY||Fee payment|
Year of fee payment: 12