1 / 11

Fluid Bed Technology and Catalyst of Propane & Isobutane Dehydrogenation

Fluid Bed Technology and Catalyst of Propane & Isobutane Dehydrogenation. By ReZel Catalysts. Background.

kennan
Download Presentation

Fluid Bed Technology and Catalyst of Propane & Isobutane Dehydrogenation

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript

  1. Fluid Bed Technology and Catalyst of Propane & IsobutaneDehydrogenation By ReZel Catalysts

  2. Background • Propane and Isobutane are relatively cheap petrochemical products, whereas propylene and isobutene are high value added products.Therefore, propylene production via propane dehydrogenation; isobutene production via isobutane dehydrogenation and further MTBE production via further reaction with methanol have significant commercial value.

  3. Background-continued • ReZel has developed a new fluid bed technology and supporting catalyst for producing propylene and isobutene via propane and isobutane dehydrogenation, respectively.This technology use fluid bed reactor, continuously circulated and regenerated catalyst process similar to that of FCC process.

  4. Background-continued • ReZel’s patented fluid bed non-interrupted regenerated catalyst does not contain precious metal such as platinum (Pt) and palladium (Pd) and is therefore cost effective. This technology is called RGTP.

  5. Other company’s propane/isobutane dehydrogenation technology Conv.60-65% Sel.-95% Time：25Mins Conv.45-55% Sel.85-95% Time：8hs Catofin（LummusFixed Bed，Cr/Al） Star（PhillipsCombustion Tube，Pt-Sn/Al） Moving Bed Conv.45-55% Sel.-91% Time：2-7d Oleflex（UOP) Catalyst Regeneration（CCR，Pt/Al)

  6. Conv.50-55% Sel.85-91% Time：Continuous FBD-4（Russia）（Cr/Al） Reaction－Regeneration System Linde（ Conv.40-45%，Sel.91-95%，Time：9hrs） （Similar to Star）Different Catalyst（Cr/Al） Circulating Fluid Bed： Continuous operation，Variable size Stable operation，Low cost

  7. ReZelRGTPProcess Flow

  8. Reaction Temperature：560-600℃ • Reaction Pressure：0.1-0.2MPa • Catalyst Circulated Regeneration

  9. Industrial Unit Results Isobutane catalytic dehydrogenation Propane catalytic dehydrogenation

  10. Property of Propane ,Isobutane, Butane Dehydrogenation Catalyst

  11. Summary Catalyst has gone through lab, pilot and industrial preparation； Catalyst physical/chemical properties satisfy fluid bed operation requirement； Catalyst properties meet fluid bed design requirement； Catalyst meets technical standard for industrial application. Thank You！

More Related