摘要:
THE HYDROLYSIS OF TITANIUM SULFATE SOLUTIONS IS PERFORMED AND CONTROLLED BY HEATING A SEEDED TITANIUM SULFATE SOLUTION WITH AGITATION WHILE SIMULTANEOUSLY MEASURING THE REFLECTANCE OF THE RESULTING SUSPENSION, UNTIL A CRITICAL POINT IS ATTAINED AS INDICATED BY A SUBSTANTIAL CHANGE IN THE RATE OF REFLECTANCE PER UNIT OF HYDROLYSIS TIME, ALLOWING THE SOLUTION TO REMIAN QUIESCENT FOR FROM 5 TO 60 MINUTES, THEN RESUMING THE HEATING OF THE SOLUTION UNTIL THE HYDROLYSIS PRODUCES THE DESIRED YIELD OF TITANIUM HYDRATE. THE MEASUREMENT OF REFLECTANCE MAY BE
MADE BY PHOTOELECTRIC MEANS, AND THE POINT OF INFLECTION OF THE REFLECTANCE CURVE OR ITS FIRST OR SECOND DERIVATIVE WITH RESPECT TO TIME MAY BE USED TO CONTROL THE HYDROLYSIS PROCESS.
摘要:
This invention relates in general to a process for preparing a high quality titanium dioxide pigment in which the titanium dioxide is in the anatase crystal form. The process comprises hydrolyzing in a particular manner the titanium values from a titanium sulfate-ferrous sulfate solution in which the concentration of titanium is from 80 to 180 g.p.l. calculated as TiO2 and treating and calcining the hydrate so formed to produce a high grade anatase TiO2 pigment. Using the hydrolysis process of the instant invention, a high grade anatase titanium dioxide pigment may be produced from a titanium sulfate-ferrous sulfate solution without utilizing the conventional crystallization step for removing most of the iron values nor the concentration step for increasing the titanium content in the liquor to at least 200 g.p.l. TiO2.
摘要:
The process comprises hydrolysing a solution of titanium sulphate, washing the titanium dioxide hydrolysate, and then calcining the hydrolysate at a temperature from 750 to 1000*C. to yield titanium dioxide pigment having desirable properties in terms of brightness, opacity, and/or texture. A rutile-promoting seed is incorporated with the titanium sulphate solution and/or with the hydrolysate. In the process, the pH of the wet hydrolysate is in the range of from 6 to 10 immediately before calcination, and there is present in the hydrolysate immediately before calcination an ammonium compound that will be expelled, together with any decomposition products thereof, during calcination; a treating agent or agents selected from beryllium, aluminium, magnesium, zinc and compounds thereof, and a treating agent or agents selected from sodium potassium, rubidium, caesium, and compounds thereof, with the proviso that lithium and/or a lithium compound may be substituted for any or all of the agent or agents selected from the first-mentioned and/or second-mentioned group. The total quantity of the ammonium compound is at least 0.7 percent (calculated as ammonium sulphate); the total quantity of agents from the first-mentioned group is from 0.02 to 0.50 percent (calculated as the metal oxide or oxides); and the total quantity of agents from the secondmentioned group is from 0.05 to 1.0 percent (calculated as the alkali metal oxide or oxides). All the percentages are by weight and are based on the weight of titanium dioxide. The ammonium compound and the treating agent or agents may be incorporated with the hydrolysate in any order. Conveniently, any necessary pH adjustment is effected at least in part by using an alkaline ammonium compound.
摘要:
APPARATUS FOR IMPROVED SEPARATION OF LIQUIDS, GASES AND PARTICULATE SOLID MATERIALS IN A LIQUID-GAS CONTACTING PROCESS WHEREIN A LIQUID FEED AND GAS USUALLY HYDROGEN ARE PASSED UPWARDLY THROUGH A BED COMPOSED OF A PARTICULATE CONTACT AGENT, THE VELOCITY OF THE GAS AND THE LIQUID BEING SUCH THAT THE PARTICLES ARE PUT IN A STATE OF RANDOM MOTION AND THE VOLUME OF THE BED IS EXPANDED OVER ITS STATIC VOLUME AND WHEREIN AN AREA OF HIGH LIQUID GAS AND LIQUID TURBULENCE AND MIXING IS CREATED AND WHEREIN LIQUID EFFUENT AND GASEOUS EFFUENTS ARE REMOVED FROM THE CONTACT ZONE. THE METHOD CONSISTS OF EFFECTING ESSENTIALLY COMPLETE DISENGAGEMENT OF THE GAS FROM THE MIXTURE OF PARTICULATE SOLIDS AND LIQUID. THE GAS-FREE LIQUIDSOLID MIXTURE IS THEN INTRODUCED TO A ZONE OF RELATIVELY LOW TURBULENCE AND LIQUID IS THEN REMOVED FROM THIS ZONE AT A RATE WHOSE LINEAR VELOCITY IS LESS THAN THE SETTLING VELOCITY OF THE SOLID, THEREBY ALLOWING SUBSTANTIAL SETTLING OF THE SOLID AND RESULTING IN THE REMOVAL OF A CLARIFIED LIQUID. THE DISENGAGED GASEOUS EFFLUENT MAY THEN BE REMOVED SEPARATELY OR RECOMBINED AND REMOVED WITH THE LIQUID EFFLUENT. APPARATUS FOR EFFICIENTLY CARRYING OUT THIS PROCESS ARE DESCRIBED.
摘要:
This invention relates in general to a process for preparing a high-quality titanium dioxide pigment in which the titanium dioxide is in the anatase crystal form. The process comprises hydrolyzing in a particular manner the titanium values from a titanium sulfate-ferrous sulfate solution in which the concentration of titanium is from 80 to 180 g.p.l. TiO2 and the FeSO4/TiO2 ratio is from 2.20 to 2.75 and treating and calcining the hydrate so formed to produce a high-grade anatase TiO2 pigment. Using the hydrolysis process of the instant invention, a high-grade anatase titanium dioxide pigment may be produced from a solution which does not require the conventional crystallization step to remove most of the iron values and the concentration step to increase the titanium content in the liquor to at least 200 g.p.l. TiO2.
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:
In an improved process for the production of a finely divided oxide of a metal, silicon or mixtures thereof by the hydrolytic conversion of a corresponding volatile chloride of said metal, silicon or mixtures thereof in a flame; wherein said volatile chloride or said mixture of volatile chlorides in admixture with a combustible hydrogen-containing gas and air or oxygen are fed to a flame emitting from a burner into a reaction chamber to thereby form an oxide aerosol in waste gases from said burner; cooling said oxide and said waste gases; and separating said oxide from said waste gases; wherein the improvement comprises maintaining said waste gases substantially free of chlorine by reducing chlorine that forms during said conversion in said flame with hydrogen while cooling said waste gas below the temperature at which hydrogen and oxygen react in said waste gas.