REACTION TUBE AND HYDROTHERMAL PROCESSING FOR THE WET CHEMICAL CO-PRECIPITATION OF OXIDE POWDERS

• US 20110053758A1
• Filed: 02/28/2010
• Published: 03/03/2011
• Est. Priority Date: 02/27/2009
• Status: Abandoned Application

• Current Assignee: Eestor Inc. (FuelPositive Corp.)
• Original Assignee: Eestor Inc. (FuelPositive Corp.)
• Inventors: Nelson, Carl W., Weir, Richard D.
• Application Number:
  US12/714,537
• Publication Number:
  US 20110053758A1
• Time in Patent Office: Days
• US Class Current: 501/134
• CPC Class Codes: B01J 19/1812 Tubular reactors
• CPC Class Codes: B01J 19/2405 provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
• CPC Class Codes: B01J 2219/00065 Pressure measurement
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: B01J 2219/00166 controlling the residence time inside the reactor vessel
• CPC Class Codes: B01J 4/02 for feeding measured , i.e. prescribed quantities of reagents
• CPC Class Codes: C01B 13/363 Mixtures of oxides or hydroxides by precipitation
• CPC Class Codes: C01B 13/366 by hydrothermal processing
• CPC Class Codes: C01G 23/006 Alkaline earth titanates
• CPC Class Codes: C01P 2002/34 perovskite-type (ABO3)
• CPC Class Codes: C01P 2002/52 containing elements as dopants
• CPC Class Codes: C01P 2002/72 by d-values or two theta-values, e.g. as X-ray diagram
• CPC Class Codes: C01P 2004/52 highly monodisperse size distribution
• CPC Class Codes: C01P 2004/61 Micrometer sized, i.e. from 1-100 micrometer
• CPC Class Codes: C01P 2004/62 Submicrometer sized, i.e. from 0.1-1 micrometer
• CPC Class Codes: C01P 2006/40 Electric properties
• CPC Class Codes: C01P 2006/42 Magnetic properties
• CPC Class Codes: H01B 3/10 metallic oxides ceramics H01B3/12

Abstract

A reactor for the wet-chemical co-precipitation of oxide powders includes a cylindrical structure having first and second ends and a lumen extending the length of the tube. A central axis extends through the lumen. The first end is closed. The reactor also includes a first inlet port disposed proximal to the first end of the cylindrical structure and providing access through the cylindrical structure to inject a first reactant solution. The reactor further includes a second inlet port disposed proximal to the first end of the cylindrical structure and providing access through the cylindrical structure to inject a second reactant solution. The first and second inlet ports are disposed on opposite sides of the cylindrical structure and are coaxial relative to the central axis.

Claims

1. A method of forming a dielectric particulate, the method comprising:

contacting first and second process streams at a turbulence intensity of at least 1.5×

10⁷ cm/s³, the first process steam including tetraalkylammonium hydroxide or tetraalkylammonium oxalate, the second process stream including a metal ion nitrate and a metal ion chelate, the metal ion nitrate and the metal ion chelate coprecipitating in the presence of the tetraalkylammonium hydroxide or the tetraalkylammonium oxalate to form a particulate material; and

hydrothermally treating the particulate material.

2. The method of claim 1, wherein the turbulence intensity is at least 10⁸ cm/s³.

3. The method of claim 2, wherein the turbulence intensity is at least 10⁹ cm/s³.

6. The method of claim 1, wherein the metal ion nitrate includes barium nitrate.

7. The method of claim 6, further comprising calcium nitrate.

8. The method of claim 1, wherein the metal chelate includes a chelate of titanium.

9. The method of claim 8, further comprising a metal ion chelate including a metal or oxometal ion selected from the group consisting of zirconium, yttrium, manganese, neodymium, tin, zinc, vanadium, niobium, tantalum, molybdenum, tungsten, hafnium, chromium, and any combination thereof.

10. The method of claim 1, wherein the metal chelate includes a neutralized alpha-hydroxycarboxylic acid chelating agent.

11. The method of claim 10, wherein the alpha-hydroxycarboxylic acid chelating agent is selected from the group consisting of 2-hydroxyethanoic acid (glycolic acid), 2-hydroxybutanedioic acid (malic acid), 2,3-dihydroxybutanedioic acid (tartaric acid), 2-hydroxy-1,2,3-propanetricarboxylic acid (citric acid), 2-hydroxybutanoic acid, 2-hydroxypentanoic acid, and 2-hydroxyhexanoic acid.

12. The method of claim 11, wherein the alpha-hydroxycarboxylic acid chelating agent include citric acid.

13. The method of claim 1, wherein the first process stream including the tetraalkylammonium hydroxide and the tetraalkylammonium oxalate.

14. The method of claim 1, further comprising drying the particulate material.

15. The method of claim 1, further comprising heat treating the dried particulate material to form the dielectric particulate having a cubic perovskite structure.

4-5. -5. (canceled)

16. A method of forming a dielectric particulate, the method comprising:

contacting first and second process streams at a turbulence intensity of at least 1.5×

10⁷ cm/s³, the first process steam including tetraalkylammonium hydroxide or tetraalkylammonium oxalate, the second process stream including a metal ion nitrate and a metal ion chelate, the metal ion nitrate and the metal ion chelate coprecipitating in the presence of the tetraalkylammonium hydroxide or the tetraalkylammonium oxalate to form a particulate material;

hydrothermally treating the particulate material;

drying the hydrothermally treated particulate material; and

heat treating the dried particulate material to form the dielectric particulate material having a cubic perovskite structure.

17. The method of claim 16, wherein the turbulence intensity is at least 10⁸ cm/s³.

18. The method of claim 16, wherein the metal ion nitrate includes barium nitrate.

19. The method of claim 18, further comprising calcium nitrate.

20. The method of claim 16, wherein the metal chelate includes a chelate of titanium.

21. The method of claim 20, further comprising a metal ion chelate including a metal or oxometal ion selected from the group consisting of zirconium, yttrium, manganese, neodymium, tin, zinc, vanadium, niobium, tantalum, molybdenum, tungsten, hafnium, chromium, and any combination thereof.

22. The method of claim 16, wherein the metal chelate includes a neutralized alpha-hydroxycarboxylic acid chelating agent.

23-25. -25. (canceled)

26. A method of forming a dielectric particulate, the method comprising:

contacting first and second process streams at a turbulence intensity of at least 10⁸ cm/s³, the first process steam including tetraalkylammonium hydroxide and tetraalkylammonium oxalate, the second process stream including a barium nitrate, calcium nitrate, a titanium chelate, and at least one metal chelate including a metal or oxometal ion selected from the group consisting of zirconium, yttrium, manganese, neodymium, tin, zinc, vanadium, niobium, tantalum, molybdenum, tungsten, hafnium, chromium, and any combination thereof, the chelate of metal chelate being an alpha-hydroxycarboxylic acid chelating agent selected from the group consisting of 2-hydroxyethanoic acid, 2-hydroxybutanedioic acid, 2,3-dihydroxybutanedioic acid, 2-hydroxy-1,2,3-propanetricarboxylic acid, 2-hydroxybutanoic acid, 2-hydroxypentanoic acid, and 2-hydroxyhexanoic acid, the barium nitrate, calcium nitrate, titanium chelate and the at least one metal chelate coprecipitating in the presence of the tetraalkylammonium hydroxide and the tetraalkylammonium oxalate to form a homogenous particulate material;

hydrothermally treating the homogenous particulate material;

drying the hydrothermally treated homogenous particulate material; and

heat treating the dried homogenous particulate material to form the dielectric particulate material having a cubic perovskite structure.

27-53. -53. (canceled)