摘要:
A PROCESS IS DISCLOSED FOR THE PURIFICATION OF TITANIUM TETRACHLORIDE FROM VANADIUM COMPOUNDS BY TREATMENT WITH H2S, WHEREIN THE HOT GASES COMING FROM THE CHLORINATION STEP OF THE TITANIFEROUS MATERIAL, CONTAINING TICL4 WITH IMPURITIES, ARE COOLED DOWN TO 130-180*C. BY INJECTION AND VAPORIZATION OF LIQUID TICL4 AND AT THE SAME TIME ARE TREATED WITH H2S, THEREBY OBTAINING A VANADIUM-FREE GASEOUS PHASE CONTAINING TICL4 AND A TICL4-FREE SOLID PHASE CONTAINING VANADIUM.
摘要:
A process for the purification of pyrite and pyrrhotite cinders from nonferrous metals, from arsenic and from sulfur. The process is characteristic in that the reduction of the hematite to magnetite is carried out in a fluid bed by direct injection of a hydrocarbon fuel and air in deficiency, at 850*-950* C. and with contact times from 15 to 45 minutes, up to a degree of reduction equal to from 10-90 percent, and in the presence of small quantities of HC1. The chlorination and reoxidation of the thus produced hot cinders is carried out in a fluid bed reactor with air and a chlorinating agent, at temperatures of from 650*1,000* C., preferably at 850*-950* C. with contact time from 20 to 150 minutes, and that the gases leaving the reactor contain less than 0.5 percent by volume of free oxygen.
摘要:
A continuous process is disclosed for producing barium or strontium ferrites, starting from iron oxide and barium or strontium carbonates, wherein A. A SLURRY CONSISTING OF IRON OXIDE, BARIUM OR STRONTIUM CARBONATE, WATER AND BINDER, IS DRIED AND GRANULATED, UTILIZING THE HOT GASES FLOWING FROM STEP (B) SUPPLEMENTED WITH HOT BURNT GASES OBTAINED SEPARATELY; B. THE GRANULES OBTAINED IN STEP (A) ARE CALCINED, FOR 0.5-4 HOURS AT 950*-1150*C, in a fluid bed reactor, heated by combustion, inside the fluid bed, of a carbonaceous, nonsulphurated fuel with air; and C. THE FERRITE OBTAINED IS COOLED AND WET GROUND. The atomic ratio between the iron and the barium or strontium ranges from 11.5:1 to 12:1. The iron oxide and the carbonate are preferably in the form of a submicronic powder.
摘要:
A PROCESS IS DISCLOSED FRO RECOVERING VANADIUM FROM SOLID TICL4-FREE RESIDUES OBTAINED IN THE PURIFICATION OF RAW TICL4 WITH H2S, WHEREIN THE SOLID RESIDUES ARE TREATED WITH OXYGEN OR AN OXYGEN-CONTAINING GS AT TEMPERATURES BETWEEN 150* AND 200*C., THEREBY OBTAINING A VOCL3CONTAINING GAS FROM WHICH THE VOCL3 IS SEPARATED IN A PRACTICALLY PURE STATE BY RECTIFICATION. THE SOLID TICL4-FREE RESIDUES ARE OBTAINED FROM THE PURIFICATION SLUDGES OF THE LIQUID RAW TICL4 BY DRYING SAME AT TEMPERATURE OF 150*180*C., IN A STREAM OF INERT GAS, PREFERABLY NITROGEN.
摘要:
A continuous process for obtaining zinc oxide of a grade higher than 75 percent from oxidized zinciferous ores, which comprises: Preheating the zinc-containing mineral and calcining it at temperatures above 800* C. (preferably at 900*-1,000* C.) by the combustion products of the gases leaving the reducing reactor. Treating the calcined ore in a fluidized bed at a temperature of from 1,000 to 1,200* C. with reducing gases obtained by direct injection of a hydrocarbon fuel and of an amount of air less than stoichiometric into the fluid bed and discharging the zinc-free residues. Burning the reducing gas of the reduction stage containing the metallic zinc vapors with air to produce a burnt gas containing CO2, H2O and ZnO. Using the burnt gas to preheat the air necessary for the partial combustion of the fuel by indirect heat exchange and the incoming zinciferous ore by direct heat exchange. Subjecting the off gases, after having released part of their heat to the air and to the ore, to separation in order to recover the zinc oxide.
摘要:
A PROCESS FOR OBTAINING CONCENTRATED SULFUROUS GASES AND MAGNETITE OR IRON SPONGE WITH HIGH IRON CONTENT, WHICH ARE VALUBLE PRODUCTS FOR THE IRON-METALLURGIC IN DUSTRY, FROM HEPTAHYDRATE FERROUS SULFATE. THE PROCESS IS BROADLY CHARACTERIZED BY THE FOLLOWING SEQUENCE; (A) DEHYDRATION OF THE HEPTAHYDRATE FERROUS SULFATE TO THE MONOHYDRATE FORM; (B) THERMAL DECOMPOSITION OF THE MONOHYDRATE FERROUS SULFATE IN A FLUIDIZED BED; (C) REDUCTION OF THE HOT HERMATITIC ASHES IN A FLUIDIZED BED OR IN A ROTARY FURNACE, TO MAGNETITE OR TO SPONGE IRON; (D) MAGNETIC CONCENTRATION OF THE PRODUCT OBTAINED IN (C) WITH CONSEQUENT ELIMNATION OF THE IMPURITIES UNDESIRABLE IN IRON METALLURGY AND OBTAINMENT OF A CONCENTRATE OF HIGH FE GRADE; (E) PREHEATING OF THE AIR NECESSARY FOR OPERATIONS (A), (B) AND (C) BY MEANS OF HEAT EXCHANGE WITH THE HOT SULFUROUS GASES PRODUCED IN (B); AND (F) UTILIZATION OF THE SENSIBLE AND CHEMICAL HEAT OF THE GASES LEAVING THE REDUCTION (C) FOR THE THERMAL DECOMPOSITON OF THE MONOHYDRATE FERROUS SULFATE AND/OR FOR THE DEHYDRATION OF THE HEPTAHYDRATE FERROUS SULFATE TO THE MONOHYDRATE FORM.