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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| Department/Agency | Canada. Natural Resources Canada. Canada. Mines Branch. |
|---|---|
| Title | 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. |
| Series title | Technical bulletin ; TB 78 |
| Publication type | Series - View Master Record |
| Language | [English] |
| Format | Electronic |
| Electronic document | |
| Note(s) | Cover title. "November 1965." Digitized edition from print [produced by Natural Resources Canada]. Includes bibliographical references (p. 27). Includes abstract in French. |
| Publishing information | Ottawa : Queen's Printer, 1966. |
| Author / Contributor | Mogan, J. P. Taylor, R. W. Booth, F. L. |
| Description | iv, 29 p. : ill. |
| Catalogue number |
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| Departmental catalogue number | 299965 |
| Subject terms | Petroleum Processing Equipment Design |
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