Conversion of oxygenate to propylene with selective hydrogen...

Chemistry of hydrocarbon compounds – Unsaturated compound synthesis – From nonhydrocarbon feed

Reexamination Certificate

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C585S639000

Reexamination Certificate

active

07405337

ABSTRACT:
The average cycle propylene selectivity of an oxygenate to propylene (OTP) process using one or more fixed or moving beds of a dual-function oxygenate conversion catalyst with recycle of one or more C4+ olefin-rich fractions is substantially enhanced by the use of selective hydrotreating technology on these C4+ olefin-rich recycle streams to substantially eliminate detrimental coke precursors such as dienes and acetylenic hydrocarbons. This hydrotreating step helps hold the build-up of detrimental coke deposits on the catalyst to a level which does not substantially degrade dual-function catalyst activity, oxygenate conversion and propylene selectivity, thereby enabling a substantial improvement in propylene average cycle yield. The propylene average cycle yield improvement enabled by the present invention over that achieved by the prior art using the same or a similar catalyst system but without the use of the hydrotreating step on the C4+ olefin-rich recycle stream is of the order of about 1.5 to 5.5 wt-% or more.

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Rothaemal et al., “Demonstrating the New Methanol to Propylene (MTP) Process”, Mar. 2003, ERTC Petrochemical Conference, Paris, France.
Paper “Insights into Gas to Propylene, GTP®/MTP® Technology” by Dr. Waldemar Liebner, Lurgi AG, Frankfurt am Main; Germany, presented at Propylene Trade & Derivatives Markets, Singapore, Oct. 24-25, 2005.

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