User:Milton Beychok/Sandbox: Difference between revisions
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==Composition of petroleum coke== | ==Composition of petroleum coke== | ||
The table below illustrates the wide range of | The table below illustrates the wide range of specifications for raw petroleum coke (referred to as green coke<ref>[http://goldbook.iupac.org/P04522.html Petroleum coke] (from the [[IUPAC]] Compendium of Chemical Terminology</ref>) produced in a delayed coker and the corresponding compositions after the green coke has been calcined at in a [[rotary kiln]] at 1200 to 1400 °C: | ||
<center> | <center> | ||
{| class="wikitable" | {| class="wikitable" | ||
|+ ''' | |+ '''Typical Specifications for Sponge Coke Coker'''<ref>{{cite book|author=David S.J. Jones and Peter P.Pujado (Editors)|title=Handbook of Petroleum Processing|edition=First Edition|publisher=Springer|year=2006|id=ISBN 1-4020-2819-9}} (page 61)</ref> | ||
! Component!! Green coke<br>as produced!!Coke calcined<br>at 2375 °F | ! Component!! Green coke<br>as produced!!Coke calcined<br>at 2375 °F | ||
|- | |- | ||
|Fixed carbon, wt %||align="center"| | |Fixed carbon, wt %||align="center"|86 − 92 ||align="center"|99.5 | ||
|- | |- | ||
| | |Sulfur, wt %||align="center"|<2.5 ||align="center"|<2.5 | ||
|- | |- | ||
| | |Volatile matter, wt %||align="center"|8− 14||align="center"|0.5 | ||
|- | |- | ||
| | |Moisture, wt %||align="center"|6-14||align="center"|0.1 | ||
|- | |- | ||
| | |Ash, wt %||align="center"|0.25 ||align="center"|0.4 | ||
|- | |- | ||
| | ||Iron||align="center"|0.01||align="center"|0.02 | ||
|- | |- | ||
| | |Nickel||align="center"|0.02||align="center"|0.03 | ||
|- | |- | ||
| | |Silicon||align="center"|0.02||align="center"|0.02 | ||
|- | |- | ||
|Vanadium||align="center"|0.02||align="center"|0.03 | |||
| | |||
|} | |} | ||
</center> | </center> | ||
Revision as of 01:07, 14 February 2008
Delayed coking is one of the chemical engineering unit processes used in many petroleum refineries. In brief, the process heats the residual oil from the crude oil distillation unit in a petroleum refinery to its thermal cracking temperature in the heat transfer tubes of a furnace. This cracks the long chain hydrocarbon molecules of the residual oil into coker gas oil and petroleum coke.[1][2][3].
Some delayed coking units produce as much as 5,000 tons of coke per day.[4]
Flow diagram and process description
The diagram and description in this section are based on typical delayed coking unit with two coke drums. However, larger units have tandem pairs of drums, some with as many as 6 drums, each of which may have diameters of up to 10 meters and overall heights of up to 43 meters.[5]
Typical schematic flow diagram
Process description
Thermal cracking begins in the furnace line between the furnace and the coke drums and finishes in the coke drum that is on-stream.
As cracking continues in the drum, gas oil and lighter components are generated in vapor phase and separate from the liquid and solids. The drum effluent is vapor except for any liquid or solids entrainment, and is directed to a distillation column where it is separated into the desirable boiling point fractions. Solid coke is deposited in the drum in a porous structure that allows flow through the pores.
After the drum is full of the solidified coke, the hot mixture from the furnace is switched to the second drum. While the second drum is filling, the full drum is steamed out to further reduce the hydrocarbon content of the petroleum coke, and then quenched with water to cool it. The top and bottom heads of the full coke drum are removed, and the solid petroleum coke is then cut from the coke drum with a high pressure water nozzle, where it falls into a pit, pad, or sluiceway for reclamation to storage.
Composition of petroleum coke
The table below illustrates the wide range of specifications for raw petroleum coke (referred to as green coke[6]) produced in a delayed coker and the corresponding compositions after the green coke has been calcined at in a rotary kiln at 1200 to 1400 °C:
| Component | Green coke as produced |
Coke calcined at 2375 °F |
|---|---|---|
| Fixed carbon, wt % | 86 − 92 | 99.5 |
| Sulfur, wt % | <2.5 | <2.5 |
| Volatile matter, wt % | 8− 14 | 0.5 |
| Moisture, wt % | 6-14 | 0.1 |
| Ash, wt % | 0.25 | 0.4 |
| Iron | 0.01 | 0.02 |
| Nickel | 0.02 | 0.03 |
| Silicon | 0.02 | 0.02 |
| Vanadium | 0.02 | 0.03 |
History
References
- ↑ Gary, J.H. and Handwerk, G.E. (1984). Petroleum Refining Technology and Economics, 2nd Edition. Marcel Dekker, Inc. ISBN 0-8247-7150-8.
- ↑ Leffler, W.L. (1985). Petroleum refining for the nontechnical person, 2nd Edition. PennWell Books. ISBN 0-87814-280-0.
- ↑ Petroleum Coke Glossary
- ↑ Staff (November 2002). "2002 Refining Processes". Hydrocarbon Processing: pp. 85-147. ISSN 0887-0284.
- ↑ Delayed coking innovations and new design trends
- ↑ Petroleum coke (from the IUPAC Compendium of Chemical Terminology
- ↑ David S.J. Jones and Peter P.Pujado (Editors) (2006). Handbook of Petroleum Processing, First Edition. Springer. ISBN 1-4020-2819-9. (page 61)