Abstract: Aspects of the present invention are directed to novel methods for making discrete polyethylene compounds selectively and specifically to a predetermined number of ethylene oxide units. Methods which can be used to build up larger dPEG compounds (a) containing a wider range of utility to make useful homo- and heterofunctional and branched species, and (b) under reaction configurations and conditions that are milder, more efficient, more diverse in terms of incorporating useful functionality, more controllable, and more versatile then any conventional method reported in the art to date. In addition, the embodiments of the invention allow for processes that allow for significantly improving the ability to purify the intermediates or final product mixtures, making these methods useful for commercial manufacturing dPEGs. Protecting groups and functional groups can be designed to make purification at large scale a practical reality.

Abstract: A process for producing ethyl tertiary butyl ether and for the substantially complete recovery by fractional distillation of the unreacted ethanol contained in an etherification reaction zone product stream as a product along with the ethyl tertiary butyl ether reaction product. This process utilizes methanol as a fractionator feed additive to enhance the recovery of ethanol as a bottoms product.

Abstract: Propene is reacted with water in a multi-stage, fluidized bed catalytic reactor to produce an oxygenate motor fuel additive containing a major proportion of isopropanol, a minor proportion of diisopropyl ether, and some water. The molar ratio of water to propene introduced into each catalytic stage of the multi-stage reactor is maintained within a range of from about 2:1 to about 6:1. The temperature of the reactants in each of the catalytic stages is maintained within a range of from about 250.degree. F. to about 320.degree. F. and the pressure at a level of from about 1200 psia to about 3600 psia. The temperature in each catalytic stage increases from the initial catalytic stage to the final catalytic stage with the temperature increase being limited to a value within a range of from about 8.degree. F. to about 1.degree. F.

Abstract: Propene is reacted with water in a multi-stage, fluidized bed catalytic reactor to produce an oxygenate motor fuel additive containing a major proportion of isopropanol (IPA), some diisopropyl ether (IPE) and some water. The molar ratio of water to propene introduced into each catalytic stage of the multi-stage reactor is maintained within a range of from about 2:1 to about 6:1. The temperature of the reactants in each of the catalytic stages is maintained within a range of from about 250.degree. F. to about 300.degree. F. and the pressure at a level of from about 1200 psia to about 3000 psia. The temperature in each catalytic stage increases from the initial catalytic stage to the final catalytic stage with the temperature increase being limited to a value within a range of from about 8.degree. F. to about 2.degree. F.

Abstract: Light olefins are catalytically converted to ethers, e.g., propylene is converted to diisopropyl ether, in a dual stage process in which product ether is recycled to a first stage reaction zone to significantly reduce the operating temperature of the olefin hydration/etherification reactions taking place in that zone. Alcohol produced in the first stage reaction zone undergoes conversion in the second stage reaction zone, e.g., by etherification with light olefin or by catalytic distillation, to provide additional product ether. The process contemplates the use of zeolites as olefin hydration/etherification catalysts.

Abstract: An improved process for indirect hydration of propylene to form di-isopropyl ether and isopropyl alcohol is provided in which propylene is absorbed in sulfuric acid to form an extract which is withdrawn from the absorbing zone; water in carefully controlled amounts is admixed with the extract and the resulting mixture is passed to an ether generating zone to form a vaporous ether product and a bottoms product depleted in di-isopropyl ether and containing sulfuric acid in a concentration at least equal to the acid concentration in the extract withdrawn from the absorbing zone. The withdrawn bottoms is then divided into two portions: a first portion is recycled to the absorber; and the second such portion is admixed with sufficient water to hydrate absorbed olefin values and the resulting mixture is fed to an alcohol generator for formation of isopropyl alcohol as overhead product and dilute sulfuric acid as bottoms product.

Abstract: Olefinic compounds, and particularly olefinic hydrocarbons, containing from 2 to about 4 carbon atoms may be subjected to a direct hydration process utilizing a dilute aqueous sulfuric acid to treat the olefin at reaction conditions which will include a temperature in the range of from about 100.degree. to about 300.degree. C. and a pressure in the range of from about 1 to about 250 atmospheres. In addition, if so desired, a transition metal sulfate may also be present in the reaction mixture.