Process for preparing a multielement oxide comprising bismuth and tungsten by coprecipitation

Patent metadata

Field	Value
Publication number	US-2016346768-A1
Application number	US-201615164097-A
Country	US
Kind code	A1
Filing date	May 25, 2016
Priority date	May 27, 2015
Publication date	Dec 1, 2016
Grant date	—

Abstract

Shaped catalyst bodies comprising a multielement oxide I having the general stoichiometry I [Bi 1 W b O x ] a [Mo 12 Z 1 c Z 2 d Fe e Z 3 f Z 4 g Z 5 h O y ] 1 (I), where Z 1 =Ni or Co, Z 2 =alkali metal or alkaline earth metal, Z 3 =zinc, phosphorus, arsenic, boron, antimony, tin, cerium, vanadium, chromium or bismuth, Z 4 =silicon, aluminum, titanium, tungsten or zirconiurn, Z 5 =copper, silver, gold, yttrium, lanthanum and lanthanides, a=0.1 to 3, b=0.1 to 10, c=1 to 10, d=0.01 to 2, e=0.01 to 5, f=0 to 5, g=0 to 10, h=0 to 1 and x, y=numbers determined by the valence and abundance of the elements other than oxygen in I, as active composition are produced by preforming a mixed oxide Bi 1 W b O x by coprecipitation from an aqueous environment at a pH in the range from 1.5 to 3 and isolation of the precipitate by means of a mechanical separation process and mixing the preformed mixed oxide Bi 1 W b O x with a precursor having the stoichiometry [Mo 12 Z 1 c Z 2 d Fe e Z 3 f Z 4 g Z 5 h O y ], shaping the mixture to form shaped bodies and thermally treating and calcining the shaped bodies at elevated temperature to give the shaped catalyst bodies. The process leads to homogeneous precipitation products having a stoichiometric composition. It is an alternative to the energy-intensive production by spray drying.

First claim

1 : A process for producing a shaped catalyst body comprising a multi-element oxide formula I as an active composition,
[Bi 1 W b O x ] a [Mo 12 Z 1 c Z 2 d Fe e Z 3 f Z 4 g Z 5 h O y ] 1   (I),
wherein Z 1 is at least one element selected from the group consisting of nickel and cobalt, Z 2 is at least one element selected from the group consisting of alkali metals and alkaline earth metals, Z 3 is at least one element selected from the group consisting of zinc, phosphorus, arsenic, boron, antimony, tin, cerium, vanadium, chromium and bismuth, Z 4 is at least one element selected from the group consisting of silicon, aluminum, titanium, tungsten and zirconium, Z 5 is at least one element from the group consisting of copper, silver, gold, yttrium, lanthanum and the lanthanides, a=0.1 to 3, b=0.1 to 10, c=1 to 10, d=0.01 to 2, e=0.01 to 5, f=0 to 5, g=0 to 10, h=0 to 1, and x and y represent numbers which are determined by the valence and abundance of the elements other than oxygen in formula I, wherein the process comprises: preforming a mixed oxide Bi 1 W b O x , wherein the preformation of the mixed oxide Bi 1 W b O x comprises coprecipitation from an aqueous environment at a pH in the range from 1.5 to 3 to obtain a precipitate; and isolating the precipitate by a mechanical separation process.

2 : The process according to claim 1 , wherein an aqueous preparation of a bismuth source having a pH of from 1.5 to 3 is initially charged, an aqueous preparation of a tungsten source is added and the pH of the mixture is maintained in the range from 1.5 to 3 during the addition of the tungsten source.

3 : The process according to claim 2 , wherein a tungsten source is tungstic acid and/or tungsten oxide and the pH of the mixture is maintained in the range from 1.5 to 3 during the addition of the tungsten source by addition of a base.

4 : The process according to claim 3 , wherein the base is an aqueous solution of an alkali metal hydroxide.

5 : The process according to claim 1 , wherein the mechanical separation process is selected from the group consisting of filtration, centrifugation, sedimentation and floatation.

6 : The process according to claim 1 , wherein the precipitate is washed salt-free with a washing liquid.

7 : The process according to claim 6 , wherein the washing liquid is deionized water.

8 : The process according to claim 6 , wherein the electrical conductivity of the used washing liquid is determined.

9 : The process according to claim 1 , wherein the preformed mixed oxide Bi 1 W b O x has a particle diameter d 50 of from 2.8 to 3.6 μm.

10 : The process according to claim 1 ,
wherein the preformed mixed oxide Bi 1 W b O x is mixed with a precursor having the stoichiometry [Mo 12 Z 1 c Z 2 d Fe e Z 3 f Z 4 g Z 5 h O y ], the mixture is shaped to form a shaped body, and the shaped body is thermally treated and calcined at elevated temperature to obtain the shaped catalyst body.

Assignees

• Basf Se

Inventors

• Wrobel Stefan
• Hellerich Wolfgang
• Welker-Nieuwoudt Cathrin Alexandra
• Dobner Cornelia Katharina

Classifications

• B01J2235/15

  X-ray diffraction · CPC title

• B01J37/08

  Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J37/009

  Preparation by separation, e.g. by filtration, decantation, screening · CPC title

• B01J37/031

  Precipitation · CPC title

• B01J23/8885 Primary

  containing also molybdenum · CPC title