The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Oct. 06, 2015

Filed:

Jun. 19, 2012
Applicants:

Mathieu Skrzypczak, Saint-Louis, FR;

Marc Maurer, Village-Neuf, FR;

Thomas Schmölzer, Villach, AT;

Inventors:

Mathieu Skrzypczak, Saint-Louis, FR;

Marc Maurer, Village-Neuf, FR;

Thomas Schmölzer, Villach, AT;

Assignee:

Omya International AG, Oftringen, CH;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C09C 1/02 (2006.01); C01F 11/18 (2006.01); C09D 7/12 (2006.01); C08K 3/26 (2006.01);
U.S. Cl.
CPC ...
C09D 7/1216 (2013.01); C01F 11/181 (2013.01); C08K 3/26 (2013.01); C09C 1/021 (2013.01); C01P 2004/03 (2013.01); C01P 2004/30 (2013.01); C01P 2004/38 (2013.01); C01P 2004/61 (2013.01); C01P 2006/12 (2013.01); C01P 2006/40 (2013.01); C08K 2003/265 (2013.01);
Abstract

The present invention relates to a process for the production of precipitated calcium carbonate, comprising the following steps: a) providing a reaction vessel containing an aqueous phase at an initial temperature; b) injecting a carbon dioxide generating compound into the aqueous phase until the pH of the aqueous phase is in the range of around 5 to around 7; and c) subsequently adding a calcium hydroxide slurry at an initial temperature to the reaction vessel while continuing the injection of the carbon dioxide generating compound, in order to obtain an aqueous slurry of the precipitated calcium carbonate. The addition rate of the calcium hydroxide slurry to the reaction vessel in step c) is such that an average electrical conductivity of the reaction contents in the reaction vessel during the reaction is in a range of 100 to 6 000 μS/cm.


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