SMS Siemag Process Technologies GmbH

Austria

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C01B 9/02 - Chlorides 1
C01G 49/06 - Ferric oxide [Fe2O3] 1
C01G 49/10 - Halides 1
C01G 53/09 - ChloridesOxychlorides 1
C22B 3/10 - Hydrochloric acid 1
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Found results for  patents

1.

METHOD FOR CONCENTRATING METAL CHLORIDES IN AND SEPARATING SAME FROM AN IRON(III) CHLORIDE-CONTAINING HYDROCHLORIC ACID SOLUTION

      
Application Number AT2012050195
Publication Number 2013/086555
Status In Force
Filing Date 2012-12-12
Publication Date 2013-06-20
Owner SMS SIEMAG PROCESS TECHNOLOGIES GMBH (Austria)
Inventor
  • Weissenbaeck, Herbert
  • Vogl, Dieter

Abstract

A method for concentrating metal chlorides in and separating same from an iron(III) chloride-containing hydrochloric acid solution is described, wherein iron is precipitated from the solution as iron oxide, preferably haematite and filtered off in a filtration device, and the now further concentrated non-hydrolysable metal chlorides are removed from at least a part of the hydrochloric acid filtrate.

IPC Classes  ?

2.

METHOD AND DEVICE FOR PRODUCING AN IRON(III) CHLORIDE SOLUTION

      
Application Number AT2010000484
Publication Number 2011/072318
Status In Force
Filing Date 2010-12-16
Publication Date 2011-06-23
Owner SMS SIEMAG PROCESS TECHNOLOGIES GMBH (Austria)
Inventor
  • Vogl, Dieter
  • Konlechner, David
  • Mach, Michaela
  • Bartel, Matthias
  • Weissenbaeck, Herbert

Abstract

The invention relates to a method and device for producing an iron(III) chloride solution having an iron(III) chloride concentration of 30 wt% to 55 wt%, preferably 35 wt% - 50 wt%, by oxidizing a starting solution of hydrochloric acid containing iron and having an iron(II) chloride concentration of 10 wt% - 30 wt%, preferably 15 wt% - 25 wt%, comprising at least one oxidation step and two concentration steps, in which concentration steps water is evaporated from the solution of hydrochloric acid containing iron by supplying thermal energy, wherein the concentration steps are performed at different pressures, wherein the condensation energy of the resulting vapor is fed from the concentration step performed at higher pressure to the evaporator of the concentration step performed at lower pressure.

IPC Classes  ?