000	00000nam 2200000za 4500
001	9.841192
003	CaOODSP
005	20221107152028
007	cr |||||||||||
008	170808s1966    onca    ob   f000 0 eng d
040	|aCaOODSP|beng
041	|aeng|bfre
043	|an-cn---
086	1 |aM34-20/78E-PDF|zM34-20/78
100	1 |aMogan, J. P.
245	10|aPilot plant for low and high pressure fluid catalyst bed reactions |h[electronic resource] / |cJ.P. Mogan, R.W. Taylor, and F.L. Booth, Fuels and Mining Practice Division.
260	|aOttawa : |bQueen's Printer, |c1966.
300	|aiv, 29 p. : |bill.
490	1 |aTechnical bulletin ; |vTB 78
500	|aCover title.
500	|a"November 1965."
500	|aDigitized edition from print [produced by Natural Resources Canada].
504	|aIncludes bibliographical references (p. 27).
520	3 |a“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.
546	|aIncludes abstract in French.
692	07|2gccst|aPetroleum
692	07|2gccst|aProcessing
692	07|2gccst|aEquipment
692	07|2gccst|aDesign
700	1 |aTaylor, R. W.
700	1 |aBooth, F. L.
710	1 |aCanada. |bNatural Resources Canada.
710	1 |aCanada. |bMines Branch.
830	#0|aTechnical bulletin (Canada. Dept. of Energy, Mines and Resources. Mines Branch)|vTB 78|w(CaOODSP)9.834857
856	40|qPDF|s5.98 MB|uhttps://publications.gc.ca/collections/collection_2017/rncan-nrcan/M34-20/M34-20-78-eng.pdf
986	|a299965