Other

Otto P Strausz

Boleslaw L Ignasiak

Wanda Pawlak

Kazimierz Szymocha

Ali A Turak

Teresa Ignasiak

Jerzy Janiak

The catalyst comprises a mixture of hydrocracked residual asphaltene and metal-doped coke. The catalyst is produced by mixing an oil-soluble metal compound catalyst precursor (e.g. Mo or Ni soap) with heavy oil containing asphaltene and hydrocracking the mixture, producing solid coke as a byproduct. The residual asphaltene fraction in the hydrocracked oil is then precipitated, for example with n-pentane. The mixture of solid coke and precipitated asphaltene is separated and used as the catalyst for hydrocracking a new batch of non-hydrocracked oil. The coke and asphaltene mixture provides as effective a catalyst as the original metal soap catalyst precursor. The coke and asphaltene mixture recovered from a second stage of coke and asphaltene mixture catalysed hydrocracking of heavy oil is still an effective catalyst and can be used again without significant loss in catalytic activity. Similarly, coke and asphaltene mixture from non-catalytic hydrocracking of bitumen displays a catalytic effect which, however, is lower than that described above.

Process for hydrocracking heavy oil

A process for removing oil from coal fines that have been agglomerated or blended with heavy oil comprises the steps of heating the coal fines to temperatures over 350.degree. C. up to 450.degree. C. in an inert atmosphere, such as steam or nitrogen, to convert some of the heavy oil to lighter, and distilling and collecting the lighter oils. The pressure at which the process is carried out can be from atmospheric to 100 atmospheres. A hydrogen donor can be added to the oil prior to deposition on the coal surface to increase the yield of distillable oil.

Process for converting heavy oil deposited on coal to distillable oil in

Growing community of inventors

Edmonton, Canada

Otto P Strausz