Preparation of iron (iii) oxide pigments

Patent metadata

Field	Value
Publication number	US-2017267544-A1
Application number	US-201515508158-A
Country	US
Kind code	A1
Filing date	Sep 4, 2015
Priority date	Sep 5, 2014
Publication date	Sep 21, 2017
Grant date	—

Abstract

The present invention relates to an improved process for producing iron oxide red pigments by the Penniman process using nitrate (also referred to as nitrate process or direct red process).

First claim

1 . A process for producing haematite pigments, the process comprising contacting iron, an aqueous haematite nucleus suspension containing haematite nuclei which have a particle size of 100 nm or less and a specific BET surface area of from 40 m 2 /g to 150 m 2 /g (measured in accordance with DIN 66131), and an iron(II) nitrate solution in the presence of at least one oxygen-containing gas at temperatures of from 70 to 99° C., to produce a suspension comprising haematite pigment.

2 . The process according to claim 1 , further comprising at least one of:
adding the iron(II) nitrate solution to the iron to produce a first mixture, and subsequently adding the haematite nucleus suspension to the first mixture to produce a reaction mixture; adding the iron(II) nitrate solution and the haematite nucleus suspension simultaneously to the iron to produce a reaction mixture; and adding the haematite nucleus suspension to the iron to produce a first mixture, and subsequently adding the iron(II) nitrate solution to the first mixture to produce a reaction mixture;
in such a way that the concentration of iron(II) nitrate in the reaction mixture from 0.1 to 25 g/l of liquid phase, preferably from 1 to 20 g/l of liquid phase, calculated on the basis of anhydrous Fe(NO 3 ) 2 .

3 . The process according to claim 1 , wherein the reaction is carried out until the haematite pigment has a desired colour shade.

4 . The process according to claim 1 , further comprising separating the haematite pigment from the haematite pigment suspension by conventional methods.

5 . The process according to claim 1 , wherein the haematite pigment has the α-Fe 2 O 3 modification.

6 . The process according to claim 1 , wherein at least iron is initially charged and the haematite nucleus suspension is then added to the iron.

7 . The process according to claim 1 , wherein a mixture of iron is initially charged and the haematite nucleus suspension is then added to the mixture of iron.

8 . The process according to claim 1 , wherein the haematite nucleus suspension is firstly added to at least iron at a temperature of from 10 to 99° C. and, after the addition is complete, the iron(II) nitrate solution is added at a temperature of the reaction mixture of from 70 to 99° C.

9 . A process for producing iron oxide red pigments, the process comprising contacting iron, haematite nucleus suspension containing haematite nuclei having a particle size of 100 nm or less and a specific BET surface area of from 40 m 2 /g to 150 m 2 /g (measured in accordance with DIN 66131), and iron(II) nitrate solution in the presence of at least one oxygen-containing gas at temperatures of from 70 to 99° C., wherein:
the haematite nucleus suspension is added to at least iron,
the iron(II) nitrate solution is added, either before the addition, after the addition, or simultaneously with the addition of the haematite nucleus suspension, in such a way that the concentration of iron(II) nitrate is from 0.1 to 25 g/l of liquid phase, preferably from 1 to 20 g/l of liquid phase, calculated on the basis of anhydrous Fe(NO 3 ) 2 ,
the reaction is carried out with mixing by means of mechanical and/or hydraulic mixing, and
the at least one oxygen-containing gas is introduced into the reaction mixture with a gas introduction volume of 6 m 3 of gas volume/m 3 of batch volume/hour or less, preferably from 0.2 to 6 m 3 of gas volume/ 3 of batch volume/hour, particularly preferably from 0.2 to 5 m 3 of gas volume/m 3 of batch volume/hour, very particularly preferably from 0.2 to 3 m 3 of gas volume/m 3 of batch volume/hour,

to produce a suspension of the haematite pigment.

10 . The process according to claim 9 , wherein the iron(II) nitrate solution is added before the addition of the haematite nucleus suspension, in such a way that the concentration of iron(II) nitrate is 1 to 20 g/l of liquid phase, calculated on the basis of anhydrous Fe(NO 3 ) 2 .

11 . The process according to claim 9 , wherein the iron(II) nitrate solution is added after the addition of the haematite nucleus suspension, in such a way that the concentration of iron(II) nitrate is 1 to 20 g/l of liquid phase, calculated on the basis of anhydrous Fe(NO 3 ) 2 .

12 . The process according to claim 9 , wherein the iron(II) nitrate solution is added simultaneously with the addition of the haematite nucleus suspension, in such a way that the concentration of iron(II) nitrate is 1 to 20 g/l of liquid phase, calculated on the basis of anhydrous Fe(NO 3 ) 2 .

13 . The process according to claim 9 , wherein the at least one oxygen-containing gas is introduced into the reaction mixture with a gas introduction volume of 0.2 to 6 m 3 of gas volume/m 3 of batch volume/hour.

14 . The process according to claim 9 , wherein the at least one oxygen-containing gas is introduced into the reaction mixture with a gas introduction volume of 0.2 to 3 m 3 of gas volume/m 3 of batch volume/hour.

Assignees

• Lanxess Deutschland Gmbh

Inventors

• Czaplik Waldemar
• Ketteler Guido
• Kischkewitz Jurgen

Classifications

• C09C1/24 Primary

  Oxides of iron · CPC title

• B82Y40/00

  Manufacture or treatment of nanostructures · CPC title

• C01G49/06 Primary

  Ferric oxide [Fe2O3] · CPC title

• B82Y30/00

  Nanotechnology for materials or surface science, e.g. nanocomposites · CPC title

• C01P2006/12

  Surface area · CPC title