Pilot plant for low and high pressure fluid catalyst bed reactions / J.P. Mogan, R.W. Taylor, and F.L. Booth, Fuels and Mining Practice Division. : M34-20/78E-PDF

“The construction details of a high-pressure fluid-catalyst pilot-plant are described in this report. This versatile unit will be used to study a variety of fluid-bed reaction schemes (cracking, hydrofining…) for the beneficiation of crude oils and bitumens. Of side-by-side configuration, the plant can operate from 15 to 1500 psi at up to 1200°F. The charge oil rate can be varied from 0.08 to 1.75 I mp gph. The oil reacts in the presence of a continuously regenerated recirculating catalyst flow of 7 to 25 lb per hour from a 6-lb inventory. An alternate once- through catalyst system circulates 32 lb of catalyst through the reactor from pressure storage vessels. The ancillary equipment--connecting lines, heaters, safety equipment, supports, and insulation--is also described"--Abstract, p. i.

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publications.gc.ca/pub?id=9.841192&sl=1

Renseignements sur la publication
Ministère/Organisme Canada. Natural Resources Canada.
Canada. Mines Branch.
Titre Pilot plant for low and high pressure fluid catalyst bed reactions / J.P. Mogan, R.W. Taylor, and F.L. Booth, Fuels and Mining Practice Division.
Titre de la série Technical bulletin ; TB 78
Type de publication Série - Voir l'enregistrement principal
Langue [Anglais]
Format Électronique
Document électronique
Note(s) Cover title.
"November 1965."
Digitized edition from print [produced by Natural Resources Canada].
Includes bibliographical references (p. 27).
Includes abstract in French.
Information sur la publication Ottawa : Queen's Printer, 1966.
Auteur / Contributeur Mogan, J. P.
Taylor, R. W.
Booth, F. L.
Description iv, 29 p. : ill.
Numéro de catalogue
  • M34-20/78E-PDF
Numéro de catalogue du ministère 299965
Descripteurs Petroleum
Processing
Equipment
Design
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