摘要:
THE PRESENT APPLICATION IS A DIVISION OF APPLICATION SER. NO. 723,70, FILED APR. 24, 1968, AND RELATES TO A NOVEL METHOD FOR PRODUCING A RUTILE TIO2 PIGMENT BY A VAPOR PHASE PROCESS WHEREIN THE HEAT REQUIRED FOR THE REACTION OF THE GASEOUS TICL4 WITH OXYGEN IS PROVIDED BY A COLUMN OF HOT COMBUSTION GASES WHICH FILLS THE ENTIRE CROSSSECTION OF A PRE-COMBUSTION CHAMBER IMMEDIATELY PRECEDING A FEEDING RING DESIGNED TO INTRODUCE GASEOUS TICL4 INTO THE COLUMN OF HOT GASES FROM A MULTIPLICITY OF RADIAL APERTURES SURROUNDING THE COLUMN OF HOT COMBUSTION GASES AND LYING IN A COMMON PLANE SUBSTANTIALLY AT RIGHT ANGLES TO ITS LONGITUDINAL AXIS, THE REACTION THE TICL4 WITH THE O2 IN SAID HOT GASES TAKING PLACE WITHIN A RELATIVELY SHORT REACTION ZONE IMMEDIATELY SUCCEEDING THE TICL4 FEEDING RING THUS INSURING HIGH REACTION TEMPERATURES, SHORT REACTION TIME, UNIFORM RESIDENCE TIME AND NO REVERSE CURENTS IN THE REACTION ZONE.
摘要:
MEANS FOR PRODUCING PYROGENIC TITANIUM DIOXIDE BY REACTION OF GASEOUS TITANIUM TETRACHLORIDE AND OXYGEN IN THE PRESENCE OF HOT COMBUSTION GASES PRODUCED BY THE COMBUSTION OF CARBON MONOXIDE THE REACTION OF THE SEVERAL GASES BEING INITIATED BY FEEDING THE SEVERAL GASES FROM A TUBULAR BURNER ASSEMBLY INTO CONTACT WITH A ROTATING RELATIVELY COLD BODY WITHIN THE REACTION CHAMBER SAID COLD BODY ROTATING AT SPEEDS AT LEAST 50 TIMES TERRESTIAL ACCELERATION WHEREBY THE SEVERAL GASES ARE THROUGHLY MIXED AT REACTION AND THE TIO2 REACTION PRODUCT PRECLUDED FROM ADHERING TO SURFACES OF THE ASSEMBLY.
摘要:
1,254,729. Titanium dioxide. TITANG.m.b.H. 10 Feb:, 1969 [17 Feb., 1968], No. 7177/69. Heading C1N. 'Needle-shaped TiO 2 particles, or star-shaped agglomerates thereof, are made by (1) heating to 80-100‹ C. an HCl solution of titanium chloride (130-250. g. TiO 2 /l.) in which the molar ratio HCl not bonded to Fe : TiO 2 is 2-5 :1; (2) mixing this solution with a seed solution, heated to 70-100‹.C. and having a Ti content equivalent to 5-30 g. TiO 2 /l., the amount of seed being 1- 4% by wt. of the total amount of TiO 2 ; (3) heating the mixture at about 105‹ C. for 0À5-3 hours to hydrolyse the titanium chloride solution; (4) separating needle-shaped TiO 2 hydrate precipitate and calcining it at 800-900‹ C in presence of a growth-inhibiting compound of one or more of K, Rb, Cs, Ca, Sr, Ba, Al, S, P and Si; (5) grinding the calcined product under such mild conditions that the needles -are not destroyed. The initial titanium chloride solution may be one obtained by digestion of an ore with cone. HCl arid which has been freed of part of the iron initially present by crystallization. In examples, calcination is effected in presence of (1) 0À28% K 2 O and 0À5% SiO 2 ; (2) 0À28% K 2 O ; (3) 0À28% K 2 O and 0À6% P 2 O 5 . The initial titanium chloride solution, derived from ilmenite, contained Fe and Mg.
摘要:
THE INVENTION IS CONCERNED WITH A CO-CURRENT PROCESS FOR THE CONTINUOUS DIGESTION OF TITANIUM ORES, ESPECIALLY ILMENITE ORES, USING CONCENTRATED HYDROCHLORIC ACID AT ELEVATED TEMPERATURES AND AT ATMOSPHERIC PRESSURE.
摘要:
THE INVENTION IS CONCERNED WITH A PROCESS FOR THE MANUFACTURE OF ROUNDED-OFF RUTILE PIGMENT PARTICLES BY THE HYDROLYSIS OF HYDROCHLORIC ACID SOLUTIONS CONTAINING TITANIUM CHLORIDE SOLUTION, WHICH CONTAIN LESS THAN 0.2% SILICIC ACID.