ÇAĞRILI KONUŞMALAR / KEYNOTES Invited Speeches ... - TPJD
ÇAĞRILI KONUŞMALAR / KEYNOTES Invited Speeches ... - TPJD
ÇAĞRILI KONUŞMALAR / KEYNOTES Invited Speeches ... - TPJD
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
Hydrocarbon Production from Oil Shales (Himmetoğlu-Hatıldağ)<br />
Hüseyin Çalışgan, Erşan Alpay, Y. Haluk İztan<br />
Turkish Petroleum Corporation, Research Center, Ankara<br />
The known producible oil and gas reserves are assumed to be diminishing or declining in near future.<br />
Deposits of oil shale are in many parts of the world. The alternative to oil and gas energy resources should<br />
be investigated. The oil shale sources especially in Western Anatolia Region should be focused to search<br />
its energy potential and oil productivity feasibilities technically, economically and commercially. Energy<br />
development is getting more important each day, especially for developing countries like Turkey. In order<br />
to decrease the dependency on energy exporting countries, alternative fossil fuel resources of Turkey<br />
need to be further investigated. Oil shale resources are the second largest fossil fuel resources of Turkey<br />
especially in Beypazarı – Bolu Mudurnu Göynük Himmetoğlu and Hatıldağ field. The most effective way of<br />
processing oil shales is the retort technique which is converting kerogen into synthetic crude oil by pyrolysis,<br />
hydrogenation, or thermal dissolution. The retort technique can be applied as surface or in situ retorting.<br />
For the mineable part of an oil shale resource, surface retorting is the most appropriate method. It is mostly<br />
a continuous process in which the raw oil shale undergoes pyrolysis under the effect of heat, yielding oil and<br />
waste products. Since it is a continuous process, it demands applying heat for an extended time, requiring<br />
a significant amount of energy. To minimize the energy consumption in retort technique, electromagnetic<br />
heating can be employed as an alternative recovery method. Oil shale is a general expression usually<br />
used for a finegrained sedimentary rock, containing significant amounts of kerogen, from which liquid<br />
hydrocarbons can be obtained.<br />
Oil shale is commonly defined as a fine-grained sedimentary rock containing organic matter. The organic<br />
matter of oil shale, which is the source of liquid and gaseous hydrocarbons, typically has a higher hydrogen<br />
and lower oxygen content than that of lignite and bituminous coal. Most of the organic matter is insoluble<br />
in ordinary organic solvents; therefore, it must be decomposed by heating to release such materials. The<br />
oil shale is a great potential for the economic recovery of energy, including shale oil and combustible gas,<br />
as well as a number of byproducts. The most economic potential oil shale reservoirs are generally the ones<br />
that is at or near enough to the surface to be developed by open-pit or conventional underground mining<br />
or by in-situ methods. Oil shales were deposited in a variety of depositional environments, including freshwater<br />
to highly saline lakes, marine basins and shelves, and in coastal swamps, commonly in association<br />
with deposits of coal. Oil shales range widely in organic content and oil yield. Commercial grades of oil<br />
shale, as determined by their yield of shale oil, range from about 100 to 200 liters per metric ton (liter/ton)<br />
of rock. The U.S. Geological Survey has used a lower limit of about 40 liter/ton for classification of Federal<br />
oil-shale lands. Others have suggested a limit as low as 25 liter/ton.<br />
Optimum heating and soaking periods were selected according to the highest oil production. Because<br />
thermal cracking, which is also known as pyrolysis, takes place over 1200 o F to produce shale oil, heat and<br />
soak periods belonging to these experiment were selected as optimum periods. There are two different<br />
soaking periods determined as the optimal experimental operation period. The first one starts at 400 o F.<br />
This soaking period that is 40 minutes helps to vaporize water. The second soaking period begins at 1200<br />
o F (650 o C), which is the pyrolysis temperature required for the decomposition of the kerogen. To vaporize<br />
the water or decompose the kerogen needed, time is given with the help of soaking periods. Below the<br />
pyrolysis temperature, it is impossible to produce oil from oil shale samples.<br />
In this study, the recovery characteristics of Himmetoğlu and Hatıldağ oil shale samples were tested<br />
experimentally using the retort technique in the laboratory. Himmetoğlu and Hatıldağ oil shales showed<br />
different oil recovery results. Himmetoğlu Oil shale yielded remarkably higher produced oil recoveries<br />
compared to the Hatıldağ Oil Shale samples. The oil content of the samples were determined by atmosheric<br />
distillation of the oil from the sample. The oil distilled from a sample is collected in a calibrated receiving<br />
tube where its volume is measured. Temperatures up to 1200 o F (about 650 o C) were used to distill the oil<br />
from the sample. This causes some coking and cracking of the oil and loss of small portion of the oil.<br />
159