发明名称 Chlorine production catalyst and chlorine production process using the catalyst
摘要 The invention provides a chlorine production catalyst that shows excellent reaction activity in the oxidation reaction of hydrogen chloride with oxygen into chlorine, is inexpensive and can be supplied stably, and is suited for use in a fluidized-bed reactor. The invention also provides a chlorine production process using the catalyst. The chlorine production catalyst of the invention includes spherical particles containing copper element (A), an alkali metal element (B) and a lanthanoid element (C) and having an average sphericity of not less than 0.80. The lanthanoid element (C) has a bond dissociation energy with oxygen at 298 K of 100 to 185 kcal/mol. The content of the copper element (A) in the catalyst is 0.3 wt % to 4.5 wt %.
申请公布号 US9108845(B2) 申请公布日期 2015.08.18
申请号 US201013256623 申请日期 2010.03.25
申请人 MITSUI CHEMICALS, INC. 发明人 Nabeta Takashi;Horiuchi Nobuhiko;Sugimoto Kenichi;Iwata Kenji;Murakami Masami
分类号 C01B7/00;C01B7/04;B01J23/83;B01J35/00;B01J35/08;B01J35/10;B01J37/00;B01J37/02;B01J21/08;B01J35/02 主分类号 C01B7/00
代理机构 Foley & Lardner LLP 代理人 Foley & Lardner LLP
主权项 1. A chlorine production process comprising oxidizing hydrogen chloride with oxygen in a fluidized-bed reactor in the presence of a chlorine production catalyst, wherein the chlorine production catalyst comprises spherical particles containing copper element (A), an alkali metal element (B) and a lanthanoid element (C) and has an average sphericity of 0.90 or more, wherein the lanthanoid element (C) has a bond dissociation energy with oxygen at 298 K of 100 to 185 kcal/mol, wherein the content of the copper element (A) in the catalyst is 0.3 wt % to 4.5 wt %, wherein a terminal velocity of the catalyst in air calculated by the Stoke's law below is 0.10 m/sec to 1.0 m/sec and a particle density is 0.4 g/ml to 1.2 g/ml: Terminal velocity ut=g(ρs−ρg)dp2/18μ wherein g: gravity acceleration ρs: particle density, ρg: gas density, dp: average particle diameter, μ: gas viscosity), wherein a gas space velocity in the fluidized-bed reactor is 0.01 m/sec to 1.0 m/sec and the gas space velocity is not more than the terminal velocity of the catalyst.
地址 Tokyo JP