method u0433u0438u0434u0440u043eu0434u0435u0441u0443u043bu044cu0444u0443u0440u0430u0446u0438u0438, u0433u0438u0434u0440u043eu0434u0435u043du0438u0442u0440u043eu0433u0435u043du0438u0437u0430u0446u0438u0438, hydro or combinations thereof (variants) and a system for implementation of the method (variants)

摘要

by way of u0433u0438u0434u0440u043eu0434u0435u0441u0443u043bu044cu0444u0443u0440u0430u0446u0438u0438 through a dispersion of gas bubbles with an average diameter of less than u0432u043eu0434u043eu0440u043eu0434u0441u043eu0434u0435u0440u0436u0430u0449u0438u0435 1 microns, which u0434u0438u0441u043fu0435u0440u0433u0438u0440u043eu0432u0430u043du044b in liquid phasewith sulphur compounds.u0434u0435u0441u0443u043bu044cu0444u0443u0440u0430u0446u0438u044f liquid flow, comprising sulphur compounds is carried out by processing the mixture of gas and liquid u0432u043eu0434u043eu0440u043eu0434u0441u043eu0434u0435u0440u0436u0430u0449u0438u0439, p ri which set the speed shiftexceeding approximately 20000, to obtain the dispersion of hydrogen in the continuous phase liquid and the dispersion in the reactor are u0433u0438u0434u0440u043eu0434u0435u0441u0443u043bu044cu0444u0443u0440u0430u0446u0438u0438 unable to slo eatwhich then drives the reaction product. the presented system desulphurization.