# US 7,745,380 B2 · Additive for increasing the density of a fluid for casing annulus pressure control

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 7,745,380 B2
- Document ID: US7745380B2
- Status: Granted
- Kind: B2
- Application number: 12/354,205
- Filed: 2009-01-15
- Published: 2009-05-14
- Granted: 2010-06-29
- Earliest claimed: 1996-07-24
- Assignees: M-I L.L.C.
- Inventors: Andrew J. Bradbury; Christopher A. Sawdon; Sonny Clary; William M. Reid; Tom Heinz
- Web page: https://patentgrep.com/patent/US7745380B2

## CPC

- C09K 3/00: Materials not provided for elsewhere
- C09K 8/032: {Inorganic additives}
- C09K 8/16: characterised by the inorganic compounds other than clay
- C09K 8/32: Non-aqueous well-drilling compositions, e.g. oil-based
- Y10S 507/906: Solid inorganic additive in defined physical form
- C09K: MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- Y10S: TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

## Abstract

A method of treating a wellbore that includes circulating a wellbore fluid in the wellbore, wherein the wellbore fluid comprises an oleaginous base fluid and a wellbore additive colloidal solid material, and wherein the wellbore additive colloidal solid material is formed by grinding a solid particulate material and a polymeric dispersing agent for a sufficient time so that the polymeric dispersing agent is absorbed to the surface of the resulting colloidal solid particles and less than 10% of the resulting colloidal solid particles have a diameter greater than 10 microns, but not more than five percent of the particles are less than 0.2 micron in diameter, wherein the grinding is carried out in the presence of an oleaginous base fluid and wherein the grinding is carried out so that the wellbore additive colloidal solid material has a weight average particle diameter d50 less than 2.0 microns.

## Claims

### Claim 1

A method of treating a wellbore, the method comprising:
circulating a wellbore fluid in the wellbore, wherein the wellbore fluid comprises an oleaginous base fluid and a wellbore additive colloidal solid material,
wherein the wellbore additive colloidal solid material is formed by grinding a solid particulate material and a polymeric dispersing agent for a sufficient time so that the polymeric dispersing agent is absorbed to the surface of the resulting colloidal solid particles,
wherein the grinding is carried out in the presence of an oleaginous base fluid and a dispersing agent selected from the group consisting of oleic acid, polybasic fatty acids, alkylbenzene sulphonic acids, alkane sulphonic acids, linear alpha-olefin sulphonic acids, the alkaline earth metal salts of any of the above acids, phospholipids, synthetic polymers, and combinations thereof, and
wherein the grinding is carried out so that the wellbore additive colloidal solid material has a weight average particle diameter d90 less than 2.0 microns.

### Claim 2 (depends on 1)

The method of claim 1, further comprising selecting the solid particulate material to have specific gravity of at least 2.68.

### Claim 3 (depends on 1)

The method of claim 1, wherein the base fluid is selected from diesel oil, mineral oil, white oil, n-alkanes, synthetic oils, saturated and unsaturated polyalphaolefins, esters of fatty acid carboxylic acids and combinations thereof.

### Claim 4 (depends on 1)

The method of claim 1, wherein the grinding is carried out so that the colloidal solid material has a weight average particle diameter d50 of less than 1.5 microns.

### Claim 5

A method of treating a wellbore, the method comprising:
circulating a wellbore fluid in the wellbore, wherein the wellbore fluid comprises an base fluid and a wellbore additive colloidal solid material,
wherein the wellbore additive colloidal solid material is formed by grinding a solid particulate material and a polymeric dispersing agent for a sufficient time so that the polymer dispersing agent is absorbed to the surface of the resulting colloidal solid particles,
wherein the gringing is carried out in the presence of an aqueous base fluid and a dispersing agent comprises a homopolymer or copolymer of any monomers selected from the group consisting of acrylic acid, itaconic, maleic acid, maleic anhydride, hydroxypropyl acrylate vinylsulphonic acid, acrylamide 2-propane sulphonic acid, acrylamide, styrene sulphonic acid, acrylic phosphate esters, methyl vinyl ether, vinyl acetate, and combinations thereof, and
wherein the grinding is carried out that the wellbore additive colloidal solid material has a weight average particle diameter d90 less than 2.0 microns.

### Claim 6 (depends on 5)

The method of claim 5, further comprising selecting the solid particulate material to have specific gravity of at least 2.68.

### Claim 7 (depends on 5)

The method of claim 5, wherein the base fluid is selected from diesel oil, mineral oil, white oil, n-alkanes, synthetic oils, saturated and unsaturated polyalphaolefins, esters of fatty acid carboxylic acids and combinations thereof.

### Claim 8 (depends on 5)

The method of claim 5, wherein the polymeric dispersing agent is a polymer of molecular weight in the range of 10,000 to 200,000.

### Claim 9 (depends on 5)

The method of claim 5, wherein the grinding is carried out so that the colloidal solid material has a weight average particle diameter d50 of less than 1.5 microns.