Phenol Unit This unit is based on UOP s CUMOX process which is a commercially established Cumene per oxidation process for the economic and efficient production of phenol and acetone Capacity Phenol 40 000 TPA; Acetone 24 640 TPA; The CUMOX unit has been divided into the following process section
·Phenol is produced industrially by the Hock process which involves the oxidation of cumene It is the most widely used synthetic pathway accounting for a production rate of over million t/a of phenol and approximately million t/a of the coproduct is an economically competitive process supported by the demand for acetone
Currently phenol is produced by the Cumene process which also yields stoichiometric amounts of acetone However there are recent developments in the oxidation of benzene to phenol with aqueous hydroperoxides as oxidants TS 1 as the catalyst and sulfolane thiophene tetrahydro 1 1 dioxide as a cosolvent 204b
·% %âãÏÓ 1 0 obj > stream Adobe Illustrator CS2 2006 11 13T15 13 40 06 00 2006 11 13T22 14 07Z 2006 11 13T15 13 40 06 00 JPEG 256 80 /9j
·The history of designing and the evolution of the process for the joint production of phenol and acetone which is now the basic industrial method for the manufacture of these products the state of the art and parameters of its key steps in industrial facilities among world manufacturers of phenol are presented Special attention is given to the consideration of ways
·Since the 1950s the cumene to phenol process is the predominant synthetic route for the production of phenol with acetone as the co product Cumene is oxidized with oxygen to form cumene hydroperoxide CHP The peroxide is subsequently decomposed to phenol and acetone using sulfuric acid as a catalyst
DOI /0009 2509 92 87085 5 Corpus ID 94931127; Phenol acetone process cumene oxidation kinetics and industrial plant simulation article{Andrigo1992PhenolacetonePC title={Phenol acetone process cumene oxidation kinetics and industrial plant simulation} author={Pietro Andrigo and Alberto Caimi and P Cavalieri d oro and and Anna Fait and
·The history of designing and the evolution of the process for the joint production of phenol and acetone which is now the basic industrial method for the manufacture of these products the state
·Table Phenol by KBR process—Variable costs 41 Table Phenol by KBR process—Production costs 42 Table Environment footprints for the KBR phenol process 44 Figures Figure Phenol and Acetone key components in cumene value chain 5 Figure BFD of KBR Phenol process technology 7 Figure Block flow diagram for Badger process 8
The process according to claim 1 characterized in that the cleavage of dicumyl peroxide and dimethylphenylcarbinol is carried out in the tubular reactor in a reaction medium with a phenol acetone ratio range of 1 whereby the phenol acetone ratio is achieved either by removal of a part of the acetone or with the help of the
Broyage de calcaire en belgique
Dans des industries modernes, le poudre a une large application et l'industrie de fabrication de poudre…
La ligne de production de caillou et de basalte au Panama
Panama est l'un des marchés les plus importants de la Fabricant De Concasseur De Pierre SHBM en Amérique…
L’installation de concassage de granit au Sri Lanka
Le Sri Lanka est l'un des plus important marché d'Asie pour Fabricant De Concasseur De Pierre SHBM,…