FIELD: chemical technology.
SUBSTANCE: invention describes a method for realization of the multiphase reaction of hydroformylation of olefins in tube reactor wherein a catalyst is in the continuum liquid phase and at least one the parent product is in the dispersed phase. The hydroformylation reaction is carried out at the loading coefficient B 0.8 or above that is calculated as a quotient from the pressure fall PD length value and the static pressure PS value wherein PD = Cw x g/2 x w2/D and PS = (M/V) x g wherein Cw means a tube reactor resistance coefficient; D means diameter of tube reactor; W means a flow rate moving; S means a density value of flowing phase; M means a weight flow of all components in reactor; V means a volume flow; g = 9.81 m/c2.
EFFECT: improved method, enhanced output of process.
11 cl, 1 dwg, 9 ex
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