摘要:
A catalytically active composition suitable for reacting ethylene diamine and monoethanolamine to form linear polyethylene polyamines, having a low content of cyclic by-products, can be obtained by treating titania with a solution of phosphonitrilic chloride and an acid scavenging agent in a solvent under conditions to form titania containing an intermediate reaction product of said phosphonitrilic chloride with a portion of said titania, treating said intermediate reaction product with a solution of a diamine chelating agent and an acid scavenging agent in a solvent under conditions to form a final reaction product, and calcining said final reaction product to activate said final reaction product.
摘要:
Predominantly linear polyethylenepolyamines can be prepared by reacting ethylenediamine with monoethanolamine in the presence of a phosphorus/titania/zirconia catalyst. The catalysts are prepared by mixing solutions of a tetrasubstituted compound of titanium with a tetrasubstituted compound of zirconium, adding a hydrolysing agent to coprecipitate titania and zirconia, treating the coprecipitate with a compound of phosphorus to bond from 0.5 to 6 wt.% of phosphorus to the coprecipitate and then stabilizing the resultant catalyst by calcining it at 200 to 800°C. Alternatively, the catalyst can be dried at 20 to 150°C and stabilized by subsequent calcining at 200 to 900°C.
摘要:
A catalyst compositions based on titania pellets on which a minor amount of tungstophosphoric acid or molydbophosphoric acid is deposited is useful in a process for preparing predominantly linear polyethylenepolyamines from ethylenediamine and monoethanolamine.
摘要:
thylene diamine and monoethanolamine can be reacted to form predominantly linear polyethylene polyamines in the presence of a catalyst comprising titania pellets having fluorine and 0.01 to 5 wt.% of phosphorus bonded thereto. The catalyst pellets are obtained by immersing titania pellets in a solution of a fluorophosphoric acid, drying and calcining the impregnated pellets.
摘要:
Cumene hydroperoxide can be decomposed into phenol and acetone under mild conditions (a temperature of 20 to 150°C and a pressure of 0.1 to 7 MPa) by means of a heterogeneous catalyst selected from: a heteropoly acid on an inert support, an ion exchange resin with a sulfonic acid functionality, an acidic smectite clay, a fluorine-containing acid on an inert support, and montmorillonite clay modified by a heteropoly acid or by titanium, zirconium or aluminium.