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.
Permanent link to this Catalogue record:
publications.gc.ca/pub?id=9.841192&sl=0
| Department/Agency |
|
|---|---|
| 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 |
|
| Publication type | Monograph - View Master Record |
| Language | [English] |
| Format | Digital text |
| Electronic document | |
| Note(s) |
|
| Publishing information |
|
| Author / Contributor |
|
| Description | iv, 29 p. : ill. |
| Catalogue number |
|
| Departmental catalogue number | 299965 |
| Subject terms |
Request alternate formats
To request an alternate format of a publication, complete the Government of Canada Publications email form. Use the form’s “question or comment” field to specify the requested publication.Page details
- Date modified: