Encyclopedia of Environmental Science and Engineering, Volume I and II

(Ben Green) #1

424 FOSSIL FUEL CLEANING PROCESSES


nations in Asia and Latin America, nations are reviewing their
fuel alternatives. One such fuel is petroleum coke (PC), being
produced at a worldwide rate of over 50 tons per year in 2000.
PC is a byproduct of oil refi ning that can be burned along with
other fossil fuels. The cement industry is currently one of the
widest consumers of blended PC. When co-fi ring liquid or
gaseous fuel, PC will usually require additional control equip-
ment for particulate and sulfur oxides reduction. In boilers
cofi ring coal particulate controls may be adequate since PC ash

contents are low, however, the fl ue gas may require scrubbers
to reduce sulfur oxides, since PC sulfur contents are high. See
table for typical PC properties. The low ash content and low
grindability reduce solids handling costs. The high vanadium
content may, however, contribute to secondary plumes prob-
lems in the absence of sulfur removal equipment.

REFERENCES


  1. Myerboff, A.A., American Scientist 69, 624 (1981).

  2. Lynch, M.C., Chem. Eng. Prog. 84, 20–25 (Mar. 1988).

  3. Balzhiser, R.E., Chem. Eng. 74–96 (Jan. 11, 1982).
    3a. Hansen, Teresa, Electric Power and Light, November 1996, pp. 15–16.

  4. Finfer, E.Z., J. Air Poll. Control Asso. 15, 485–488 (1965).

  5. Harris, R.D. and R.G. Moses, “Coal Desulfurization” at MECAR Sym-
    posium, Feb. 24, 1966.

  6. Beckberger, L.H., E.H. Burk, J.H. Frankovich, J.O. Siemssen, and J.S.
    Yoo, EPRI Report #CS-3902, Feb. 1985, Elect. Pwr. Res. Inst., Palo
    Alto, CA 94304.

  7. Parkinson, J.W. and E.R. Torak, EPRI Report #CS-3808, Feb. 1985,
    Elec. Pwr. Research Inst., Palo Alto, CA 94304.

  8. Bartenope, D.P. and E.N. Ziegler, Enc. of Env. Sci. and Eng. 2,
    837 (1975), 1st Edition, Gordon and Breach Sci. Pub., New York
    (London).

  9. Hoog, H.J. Inst. Petrol. 36, 738 (1950).

  10. Trowbridge, T.F., Chem. Eng. Prog. 84, 26–33 (Mar. 1988).

  11. Bartok, W., R.K. Lyon, A.D. McIntyre, L.A. Ruth and R.E. Sommer-
    lad, Chem. Eng. Prog. 84, 54–71 (Mar. 1988).

  12. Bowling, K.M., H.W. Rottendofr and A.B. Waugh, J. Inst. of Energy
    155, 179–184 (1988).

  13. Genereux, R.P. and Doucette, B., Power, July/August 1996.


EDWARD N. ZIEGLER
Polytechnic University

Ultimate & Proximate Analyses and Ash Contend of
Delayed PC, Typical Weight %, As Received

Species Avg. Range

Carbon 80 75–86
Hydrogen 3.3 3.0–3.6
Nitrogen 1.6 1.3–1.9
Sulfur 4.5 3.4–5.3
Ash 0.27 0.0–0.6
Oxygen 0.1 0.0–0.1
Moisture 10.6 5.5–15.0
HHV, kBtu/ lb 13.5 12.6–14.5
Volatile Matter 10 8–6
Ash Analysis, ppm
Vanadium  2000 500–000
Nickel 336 250–50
Iron 84 50–50

FRESH WATER: see EUTROPHICATION, WATER—FRESH
GASEOUS POLLUTANT CONTROL:
see VAPOR AND GASEOUS POLLUTANT FUNDAMENTALS

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