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Olefin Conversion Technolog

OCT [Olefins conversion technology] A process for making propylene from mixed petrochemical feedstocks. Developed by Phillips and acquired by ABB Lummus Global in 1997. First installed at the Karlsruhe oil refinery of MineraloelrafFinerie Oberrhein (Miro) for startup in 2000. [Pg.193]

As mentioned above, the first metathesis reaction studied was the equilibrium between propylene and an ethylene 2-butene mixture. In the initial Phillips process this was used to convert excess propylene into ethylene and 2-butene (Scheme 5.55). When propylene demands surged, the process was reversed and is now known as olefins conversion technology (OCT). The OCT process is operated with a fixed-bed reactor, W03 on silica serves as a catalyst. In order to allow... [Pg.259]

Application To produce propylene from ethylene and butenes using Lummus olefin conversion technology (OCT). Other OCT process configurations involve interconversion of light olefins and production of C2— C5 mono-olefins. [Pg.175]

Triolefin Also called Phillips Triolefin. A process for disproportionating propylene into a mixture of ethylene and 2-butene. The reaction takes place at 160°C over a cobalt-molybdenum catalyst on an alumina base. Developed by the Phillips Petroleum Company from 1963. A commercial plant was built by Gulf Oil Canada in 1966 and operated by Shawinigan between 1966 and 1972 before closing for economic reasons. See also Olefin Conversion Technology, Meta-4. [Pg.372]

Olefin metathesis (Olefin Conversion Technology, OCT) of ethylene and 2-butene (manufaaured by isomerization of 1 -butene) yielding propylene. ... [Pg.191]

This process, called OCT (olefin conversion technology), formerly the Phillips Triolefin Process, which utilizes a heterogeneous catalyst system, was originally developed by Phillips Petroleum Co. for the conversion of propene into ethene and butene. The reaction takes place in a fixed-bed reactor over a mixture of the metathesis catalyst W03/S102 and the isomerization catalyst MgO at temperatures above 540 K and an overall pressure of approximately 30 bar [3]. 1-Butene present in the feedstock is isomerized to 2-butene as the original 2-butene is consumed in the metathesis reaction. [Pg.518]

Because olefin metathesis is an equilibrium reaction, the Triolefin Process can be mn in the reverse direction to produce propylene from 2-butene and ethylene. Lyondell licensed the Phillips Triolefin process and opened the first propylene plant based on this technology in 1984, eventually expanding capacity to 450 000 metric tons per year. In 1997, Lummus Technology, who engineered the first two applications under license from Phillips, purchased the technology from Phillips. The metathesis of ethylene and butenes to propylene is now commercialized as Olefins Conversion Technology (OCT )... [Pg.750]

Earls, D Ji., in Handbook of Petroleum Riming Processes, 3rd ed., Meyas, R. A, Ed., McGraw-Hill, New York, 2003,10.3. OCT See Olefins Conversion Technology. [Pg.248]

Olefins Conversion Technology [OCT] A process for converting mixtures of ethylene and butenes to propylene by metathesis (disproportionation). Based on technology developed by Phillips Petroleum in the... [Pg.249]

The Phillips triolefin process [56] developed at Phillips Petroleum, used a heterogeneous WOj/SiOj catalyst in metathesis reaction to convert propene 127 into mixture of ethene 125 and 2-butene 126. As it is a reversible reaetion (Scheme 9.32) and the price of propene rose high, the reverse reaction of Philips process offered is now by using Lummus teehnology to produce propene known as Olefin Conversion Technology (OCT). [Pg.351]


See other pages where Olefin Conversion Technolog is mentioned: [Pg.645]    [Pg.338]    [Pg.259]    [Pg.263]    [Pg.263]    [Pg.207]    [Pg.457]    [Pg.2465]    [Pg.154]    [Pg.98]    [Pg.164]    [Pg.249]    [Pg.351]   
See also in sourсe #XX -- [ Pg.338 ]




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