Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
233 words
A method for producing submicron, dispersible perovskite based products having substantially the formula: Ba.sub.(1-x-x'-x") Pb.sub.x Ca.sub.x' Sr.sub.x" Ti.sub.(1-y-y'-y") Sn.sub.y Zr.sub.y' Hf.sub.y" O.sub.3 where the mole fractions x, x', x", y, y', and y" each have independent values ranging from 0 to 0.3, and the sum of either (x+x'+x") or (y+y'+y") does not exceed 0.4, comprising: (a) Heating an agitated aqueous slurry containing x moles of PbO or Pb(OH) 2 , x' moles of CaO or Ca(OH) 2 , (1-y-y'-y") moles of hydrous TiO 2 , y moles of hydrous SnO 2 , y' moles of hydrous ZrO 2 and y" moles of hydrous HfO 2 to a temperature in the range of from about 100° to 200° C., (b) Adjusting the temperature of the aqueous agitated slurry to a temperature in the range between 50° and 200° C., (c) Adding to the agitated slurry of solution, having a temperature between 70° and 110° C., containing x" moles of Sr(OH) 2 and up to a 20% excess of the stoichiometric requirement, (1-x-x'-x"), of Ba(OH) 2 over a period from about 0.1 to about 5 minutes, (d) Holding the agitated slurry at the temperature used in step (b) for a period of 10 to 30 minutes, (e) Heating the agitated slurry to a temperature not exceeding 225° C. to ensure formation of a stoichiometric perovskite product, (f) Cooling the slurry and separating the perovskite product.
Claim 2
Independent Claim
233 words
A method for producing submicron, dispersible perovskite based products having substantially the formula: Ba.sub.(1-x-x'-x") Pb.sub.x Ca.sub.x' Sr.sub.x" Ti.sub.(1-y-y'-y") Sn.sub.y Zr.sub.y' Hf.sub.y" O.sub.3 where the mole fractions x, x', x", y, y', and y" each have independent values ranging from 0 to 0.3, and the sum of either (x+x'+x") or (y+y'+y") does not exceed 0.4, comprising: (a) Heating an agitated aqueous slurry containing x moles of PbO or Pb(OH) 2 , x' moles of CaO or Ca(OH) 2 , (1-y-y'-y") moles of hydrous TiO 2 , y moles of hydrous SnO 2 , y' moles of hydrous ZrO 2 and y" moles of hydrous HfO 2 to a temperature in the range of from about 100° to 200° C., (b) Adjusting the temperature of the aqueous agitated slurry to a temperature in the range between 50° and 200° C., (c) Adding to the agitated slurry of solution, having a temperature between 70° and 110° C., containing x" moles of Sr(OH) 2 and up to a 20% excess of the stoichiometric requirement, (1-x-x'-x"), of Ba(OH) 2 over a period from about 0.1 to about 5 minutes, (d) Holding the agitated slurry at the temperature used in step (b) for a period of 10 to 30 minutes, (e) Heating the agitated slurry to a temperature not exceeding 225° C. to ensure formation of a stoichiometric perovskite product, (f) Cooling the slurry and separating the perovskite product.
Claim 3
Dependent Claim
46 words
A method as defined in claim 1 wherein at least one dopant is added in step (a) in an amount such that the molar ratio of dopant to the sum of TiO 2 , SnO 2 , ZrO 2 and HfO 2 is less than 0.05.
Claim 4
Dependent Claim
27 words
A method as defined in claim 2 wherein the dopant is selected from the group consisting of Nb, La, Y, Ni, Mn, Fe, Co and mixtures thereof.
Claim 5
Dependent Claim
23 words
A method as defined in claim 2 wherein the dopant is selected from the group consisting of Mb, Co, Mn and mixtures thereof.
Claim 6
Dependent Claim
33 words
A method as defined in claim 1 or 2 wherein the sum of the moles of the tetravalent hydrous oxides per liter in the slurry in step (a) ranges from 0.14 to 0.7.
Claim 7
Dependent Claim
27 words
A method as defined in claim 1 or 2 wherein the separated solid perovskite product in step (f) is washed with 0.005 to 0.02M Ba(OH) 2 solution.
Claim 8
Dependent Claim
28 words
A method as defined in claim 1 wherein the hydrous TiO 2 , SnO 2 , ZrO 2 , and HfO 2 used in step (a) are coprecipitated.
Claim 9
Dependent Claim
32 words
A method as defined in claim 2 wherein the hydrous TiO 2 , SnO 2 , ZrO 2 , HfO 2 and the dopant or dopants used in step (a) are coprecipitated.
Claim 10
Dependent Claim
27 words
A method as defined in claim 1 or 2 wherein the temperature of the agitated slurry in step (b) is adjusted to between 60° and 150° C.
Claim 11
Dependent Claim
23 words
A process of claim 2 wherein the dopant is added in step (a) as aqueous solutions of nitrates, formates, acetates, and/or mixtures thereof.