发明名称 PROCESS FOR THE PRODUCTION OF PRECIPITATED CALCIUM CARBONATE, PRECIPITATED CALCIUM CARBONATE AND USES THEREOF
摘要 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.
申请公布号 US2015210559(A1) 申请公布日期 2015.07.30
申请号 US201514631168 申请日期 2015.02.25
申请人 Skrzypczak Mathieu;Maurer Marc;Schmölzer Thomas 发明人 Skrzypczak Mathieu;Maurer Marc;Schmölzer Thomas
分类号 C01F11/18;D21H19/12;D21H17/66;C08K3/26 主分类号 C01F11/18
代理机构 代理人
主权项 1. Prismatic, sealenohedral or colloidal precipitated calcium carbonate obtained by the process comprising the following steps: (a) providing a reaction vessel containing an aqueous water phase at an initial temperature; (b) injecting a carbon dioxide generating compound into the aqueous water phase until the pH of the aqueous phase is in the range of pH 5 to pH 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 precipitated calcium carbonate, wherein, in step (c) the addition rate of the calcium hydroxide slurry to the reaction vessel 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 6000 μS/cm, and wherein (i) prismatic precipitated calcium carbonate is obtained when the average electrical conductivity of the reaction contents in the reaction vessel during the reaction is in a range of 100 to 1200 μS/cm, (ii) scalenohedral precipitated calcium carbonate is obtained when the average electrical conductivity of the reaction contents in the reaction vessel during the reaction is in a range of 1200 to 6000 μS/cm, and (iii) colloidal precipitated calcium carbonate is obtained when the average electrical conductivity of the reaction contents in the reaction vessel during the reaction is in a range of 1200 to 6000 μS/cm and the aqueous water phase contains at least one additive to facilitate production of colloidal precipitated calcium carbonate.
地址 Saint-Louis FR