Distillation of aqueous tertiary butyl hydroperoxide

Claim 1

A process for the preparation of an aqueous solution containing about 32 mol percent tertiary butyl hydroperoxide from an impure aqueous system comprising tertiary butyl hydroperoxide which process comprises: subjecting a stream of said dilute aqueous system comprising tertiary butyl hydroperoxide to a total distillation system for separating at least one stream containing impurities, more volatile than tertiary butyl hydroperoxide and for separating at least one stream containing impurities less volatile than tertiary butyl hydroperoxide, and for recovering from a distillation tower a stream containing H 2 O and more than 10 mol percent tertiary butyl hydroperoxide; subjecting said stream containing H 2 O and more than 10% tertiary butyl hydroperoxide to cooling and to decantation to recover an upper layer consiting of about 32 mol percent tertiary butyl hydroperoxide and about 68 mol percent water as the product of the process; coping with the flammability problem by providing flame arrestor devices at each of a plurality of locations downstream from said distillation tower, which locations are subjected to a stream of flammable vapor comprising H 2 O and more than 10 mol percent tertiary butyl hydroperoxide, such flame arrestor devices being positioned in those portions of said downstream locations containing said flammable vapors of a mixture comprising more than 10 mol percent tertiary butyl hydroperoxide and such flame arrestor devices being positioned at locations spaced apart from each other by from about ten to about thirty effective diameters of vapor lines containing said flammable vapor comprising more than 10 mol percent tertiary butyl hydroperoxide, whereby in the event of an accidental fire, such fire is initially confined to a zone between nearby flame arrestors during an alerting period appropriate for bringing such fire under control, said use of said flame arrestors permitting distillation of a vapor forming a condensate containing a larger concentration of tertiary butyl hydroperoxide than would be attainable from condensate from nonflammable vapors, thereby recovering a given quantity of 32 mol percent tertiary butyl hydroperoxide at both capital costs and operating costs lower than when condensate is obtained only from nonflammable vapors.

Claim 3

A system comprising: at least one distillation apparatus comprising a system for feeding an impure aqueous solution comprising tertiary butyl hydroperoxide to a central portion of a first distillation tower; corrosion-resistant packing in a lower portion of said first distillation tower; means for withdrawing an overhead stream of vapors from an upper portion of said distillation tower; means for condensing a portion of said vapors to provide a condensate; means for withdrawing uncondensed effluent from said overhead stream; means for recirculating a portion of said condensate to said first distillation tower; means for withdrawing a portion of said condensate; means for heating appropriate portions of said first distillation tower; means for directing a stream from a lower portion of said first distillation tower to a central portion of a second distillation tower; corrosion-resistant packing in an upper portion of said second distillation tower, said packing functioning both to promote localized equilibria between liquid and vapor and as a flame suppressor in a zone in which the water vapor concentration is low enough to provide flammable vapors comprising tertiary butyl hydroperoxide; means for withdrawing an aqueous system consisting of water and impurities less volatile than water from a lower portion of said second distillation tower; vapor line means for withdrawing an overhead stream from an upper portion said second distillation tower; a plurality of flame arrestors in said vapor line means, each flame arrestor being filled with corrosion-resistant packing at a density of at least about 5 pounds per cubic foot, and each flame arrestor having an effective length and an effective diameter of at least about six inches and at least about twice the effective diameter of said vapor line means, and each of said flame arrestors being spaced from a nearby flame arrestor a distance corresponding to from about 15 to about 30 effective diameters of said vapor line means, whereby any accidental conflagration of vapor in said line means is constrained between a pair of said flame arrestors during an interval normally sufficient to permit extinction of such conflagration; a condenser for condensing the vapor in said overhead stream from the second distillation tower to prepare a condensate from said second distillation tower; decantation means for separating condensate from said second distillation tower into an upper layer and a lower layer; means for recirculating said lower layer from the decantation means to an upper portion of said second distillation tower; and means for withdrawing from the upper layer of said decantation means a stream consisting of about 32 mol percent tertiary butyl hydroperoxide and about 68 mol percent water as the significant valuable product of the distillation process.

Claim 4

A system comprising: at least one distillation apparatus comprising a system for feeding an impure aqueous solution comprising tertiary butyl hydroperoxide to a central portion of a first distillation tower; corrosion-resistant packing in a lower portion of said first distillation tower; means for withdrawing an overhead stream of vapors from an upper portion of said distillation tower; means for condensing a portion of said vapors to provide a condensate; means for withdrawing uncondensed effluent from said overhead stream; means for recirculating a portion of said condensate to said first distillation tower; means for withdrawing a portion of said condensate; means for heating appropriate portions of said first distillation tower; means for directing a stream from a lower portion of said first distillation tower to a central portion of a second distillation tower; corrosion-resistant packing in an upper portion of said second distillation tower, said packing functioning both to promote localized equilibria between liquid and vapor and as a flame suppressor in a zone in which the water vapor concentration is low enough to provide flammable vapors comprising tertiary butyl hydroperoxide; means for withdrawing an aqueous system consisting of water and impurities less volatile than water from a lower portion of said second distillation tower; vapor line means for withdrawing an overhead stream from an upper portion said second distillation tower; a plurality of flame arrestors in said vapor line means, each flame arrestor being filled with corrosion-resistant packing at a density of at least about 5 pounds per cubic foot, and each flame arrestor having an effective length and an effective diameter of at least about six inches and at least about twice the effective diameter of said vapor line means, and each of said flame arrestors being spaced from a nearby flame arrestor a distance corresponding to from about 15 to about 30 effective diameters of said vapor line means, whereby any accidental conflagration of vapor in said line means is constrained between a pair of said flame arrestors during an interval normally sufficient to permit extinction of such conflagration; a condenser for condensing the vapor in said overhead stream from the second distillation tower to prepare a condensate from said second distillation tower; decantation means for separating condensate from said second distillation tower into an upper layer and a lower layer; means for recirculating said lower layer from the decantation means to an upper portion of said second distillation tower; and means for withdrawing from the upper layer of said decantation means a stream consisting of about 32 mol percent tertiary butyl hydroperoxide and about 68 mol percent water as the significant valuable product of the distillation process.