Page 24 - Synthetic Fuels Handbook
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12                         CHAPTER ONE

           or thermal decomposition. The pyrolysis reaction is endothermic in nature, requiring heat,
           and produces lighter molecules thereby increasing the pressure.
             In addition to the kerogen pyrolysis reaction, carbonate decomposition reactions are
           also included here as principal chemical reactions, due to their abundant existence and also
           to their reaction temperature ranges that overlap the kerogen pyrolysis temperature range.
           Other mineral matters of oil shale that are worthy of note are alumina, nahcolite, and daw-
           sonite. Some of the processes are designed to recover these mineral matters for economic
           benefit to the overall process. The pyrolysis reaction is quite active at a temperature above
           400°C, where most of the commercial retorting processes are operated. Most of the ex situ
           processes utilize the spent (processed) shale as a char source to supply the process heat, thus
           accomplishing higher energy efficiency for the process. The typical temperature required
           to carry out such pyrolysis reaction is in the range of 450 to 520°C. In order to make the
           efficiency of oil extraction higher, oil shale rocks need to be ground to finer particle sizes,
           thus alleviating mass transfer resistance and at the same time facilitating smoother flow for
           cracked hydrocarbons to escape out of the rock matrix. Due to the poor porosity or perme-
           ability of oil shale rock, the rock matrix often goes through stress fracture during pyrolysis
           operation, typically noticed as crackling.
             Major drawbacks of this type of process involve (a) “mining first” operation, which
           is costly, (b) transportation or conveying the mined shale to retorting facilities, (c) size
           reduction such as rubblizing, grinding, or milling, and (d) returning the spent shale back
           to the environment. In the current energy market of the globe, any major transportation of
           unprocessed (raw) shale would be economically unfavorable, unless the raw shale contain
           very high levels of oil contents or liquid fuel price from conventional petroleum source
           is substantially higher. In ex situ operations, heavy reliance on earth-moving equipment
           (EME) and rock-handling equipment, such as rock pump and heavy-duty hammer mill, is
           noticeable. Furthermore, it is likely to be constrained by the underlying market principle
           that the recoverable value including any tax credits or incentives from oil shale has to be
           favorable after considering all the cost factors including mining, transportation, and pro-
           cessing. Often, the mass percentage of oil content of oil shale or the volume of recoverable
           oil from unit mass of oil shale is used as a measuring parameter. The latter is called Fischer
           assay, which is based on the ASTM standard under a prescribed condition of retorting.
           However, this value should not be considered as the maximum recoverable oil content for
           the shale or the oil content itself in the shale.
             Several of the ex situ retorting processes have been commercially tested on large
           scales and also proven effective for designed objectives. Some of the successfully demon-
           strated processes include: (a) Gas Combustion retort process, (b) TOSCO (The Oil Shale
           Corporation) process, (c) Union Oil retorting process, (d) Lurgi-Ruhrgas (LR) process,
           (e) Superior Oil’s multi-mineral process, and (f) Petróleo Brasileiro (Petrobrás) process.
           Partial combustion of residual char provides the thermal energy for heating the shale via
           direct contact, thus achieving energy efficiency. TOSCO process uses heated ceramic balls
           to provide the thermal energy for heating the shale by direct contact, and also successfully
           implements multi-levels of heat recovery and energy integration strategy. The Union Oil
           retorting process is unique and innovative with utilizing well-designed rock pumps and
           adopting a number of designs for heating shale in the retort. The LR process produces
           hydrocarbons from oil shale by bringing raw shale in contact with hot fine-grained solid
           heat carrier, which can be just spent shale. The Petrobrás process was operated for about
           10 years in southern Brazil, treating over 3,500,000 tons of Irati (Permian age) oil shale to
           produce more than 1,500,000 bbl of shale oil and 20,000 tons of sulfur.
             In situ retorting of oil shale does not involve any mining operation, except starter holes
           and implementation digging. Therefore, in situ retorting does not require any transportation
           of shale out of the oil shale field. In situ retorting is often called subsurface retorting. The
           advantages of in situ retorting processes include: (a) no need for mining, (b) no need for
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