TOSCO II process

Last updated
TOSCO II process
Process typeChemical
Industrial sector(s) Chemical industry
oil industry
Feedstock oil shale
Product(s) shale oil
Main facilities Colony Shale Oil Project
Developer(s) Tosco Corporation

The TOSCO II process is an above ground retorting technology for shale oil extraction, which uses fine particles of oil shale that are heated in a rotating kiln. The particularity of this process is that it use hot ceramic balls for the heat transfer between the retort and a heater. The process was tested in a 40 tonnes per hour test facility near Parachute, Colorado.

Contents

History

TOSCO II process is a refinement of the Swedish Aspeco process. [1] The Tosco Corporation purchased its patent rights in 1952. [2] In 1956, the Denver Research Institute performed research and development of this technology, including testing of a 24  ton per day pilot plant, which operated until 1966. Later the technology development was continued under Tosco's own directions. [3] In 1964 Tosco, Standard Oil of Ohio, and Cleveland Cliffs Iron Company formed Colony Development, a joint venture company to develop the Colony Shale Oil Project and to commercialize the TOSCO II technology. The project was ended in April 1972. [2]

Technology

The TOSCO II process is classified as a hot recycled solids technology. [4] It employs a horizontal rotating kiln-type retort. In this process, oil shale is crushed smaller than 0.5 inches (13 mm) and enters the system through pneumatic lift pipes in which oil shale is elevated by hot gas streams and preheated to about 500  °F (260  °C ). [5] After entering into retort, oil shale is mixed with hot ceramic balls with temperature from 1,200  °F (650  °C ) to 1,600  °F (870  °C ). This increases the oil shale temperature to between 900  °F (480  °C ) and 1,100  °F (590  °C ), in which pyrolysis occurs. In the pyrolysis process, kerogen decomposes to oil shale gas and oil vapors, while the remainder of the oil shale forms spent shale. Vapors are transferred to a condensor (fractionator) for separation into various fractions. [2] At the kiln passage, the spent shale and the ceramic balls are separated in a perforated rotating separation drum (trommel). [5] The crushed spent shale falls through holes in the trommel, while ceramic balls are transferred to the ball heater. [6] Combustible shale gas is burned in the ball heater to reheat the ceramic balls. [2]

The overall thermal efficiency of TOSCO II process is low because the energy of spent shale is not recovered and much of the produced shale gas is consumed by the process itself. The efficiency could be increased by burning char (carbonaceous residue in the spent shale) instead of shale gas as a fuel of the ball heater. The process' other disadvantages are mechanical complexity and large number of moving parts. Also the lifetime of ceramic balls is limited. Disposal of spent shale includes environmental problems because it is very finely crushed and contains carbon residue. [2]

See also

Related Research Articles

Petrosix is the world's largest surface oil shale pyrolysis retort with an 11 metres (36 ft) diameter vertical shaft kiln, operational since 1992. It is located in São Mateus do Sul, Brazil, and it is owned and operated by the Brazil energy company Petrobras. Petrosix means also the Petrosix process, an externally generated hot gas technology of shale oil extraction. The technology is tailored to Irati oil shale formation, a Permian formation of the Paraná Basin.

<span class="mw-page-title-main">Shale oil extraction</span> Process for extracting oil from oil shale

Shale oil extraction is an industrial process for unconventional oil production. This process converts kerogen in oil shale into shale oil by pyrolysis, hydrogenation, or thermal dissolution. The resultant shale oil is used as fuel oil or upgraded to meet refinery feedstock specifications by adding hydrogen and removing sulfur and nitrogen impurities.

Oil shale gas is a synthetic non-condensable gas mixture (syngas) produced by oil shale thermal processing (pyrolysis). Although often referred to as shale gas, it differs from the natural gas produced from shale, which is also known as shale gas.

Chattanooga Corporation is an American developer of technology for unconventional oil, particularly for tar sands and shale oil extraction.

Combustion Resources, Inc. was a consulting company based in Provo, Utah, United States. It provided consulting services in the fields of fuel and combustion, such as testing of flow and mixing systems, reactor design, gas and particle sampling, gasification modeling, and shale oil extraction design and testing. The company was incorporated in 1995 as a spin-off from the Center for Advanced Combustion Engineering Research, joint collaboration between Brigham Young University and the University of Utah.

The Kiviter process is an above ground retorting technology for shale oil extraction.

<span class="mw-page-title-main">Galoter process</span> Shale oil extraction technology

The Galoter process is a shale oil extraction technology for the production of shale oil, a type of synthetic crude oil. In this process, the oil shale is decomposed into shale oil, oil shale gas, and spent residue. Decomposition is caused by mixing raw oil shale with hot oil shale ash generated by the combustion of carbonaceous residue (semi-coke) in the spent residue. The process was developed in the 1950s, and it is used commercially for shale oil production in Estonia. There are projects for further development of this technology and expansion of its usage, e.g., in Jordan and the USA.

The Alberta Taciuk process is an above-ground dry thermal retorting technology for extracting oil from oil sands, oil shale and other organics-bearing materials, including oil contaminated soils, sludges and wastes. The technology is named after its inventor William Taciuk and the Alberta Oil Sands Technology and Research Authority.

<span class="mw-page-title-main">Colony Shale Oil Project</span>

Colony Shale Oil Project was an oil shale development project at the Piceance Basin near Parachute Creek, Colorado. The project consisted of an oil shale mine and pilot-scale shale oil plant, which used the TOSCO II retorting technology, developed by Tosco Corporation. Over time the project was developed by a consortium of different companies until it was terminated by Exxon on 2 May 1982 a day which is known amongst locals as "Black Sunday".

The Fushun process is an above-ground retorting technology for shale oil extraction. It is named after the main production site of Fushun, Liaoning province in northeastern China.

The Paraho process is an above ground retorting technology for shale oil extraction. The name "Paraho" is delivered from the words "para homem", which means in Portuguese "for mankind".

The Lurgi–Ruhrgas process is an above-ground coal liquefaction and shale oil extraction technology. It is classified as a hot recycled solids technology.

The gas combustion retort process was an above-ground retorting technology for shale oil extraction. It was a predecessor of the Paraho and Petrosix processes, and modern directly heated oil shale retorting technologies in general.

The Nevada–Texas–Utah retort process was an above-ground shale oil extraction technology to produce shale oil, a type of synthetic crude oil. It heated oil shale in a sealed vessel (retort) causing its decomposition into shale oil, oil shale gas and spent residue. The process was developed in the 1920s and used for shale oil production in the United States and in Australia. The process was simple to operate; however, it was ceased from the operation because of a small capacity and labor extensiveness.

The Superior multimineral process is an above ground shale oil extraction technology designed for production of shale oil, a type of synthetic crude oil. The process heats oil shale in a sealed horizontal segmented vessel (retort) causing its decomposition into shale oil, oil shale gas and spent residue. The particularities of this process is a recovery of saline minerals from the oil shale, and a doughnut-shape of the retort. The process is suitable for processing of mineral-rich oil shales, such as in the Piceance Basin. It has a relatively high reliability and high oil yield. The technology was developed by the American oil company Superior Oil.

The Union process was an above ground shale oil extraction technology for production of shale oil, a type of synthetic crude oil. The process used a vertical retort where heating causes decomposition of oil shale into shale oil, oil shale gas and spent residue. The particularity of this process is that oil shale in the retort moves from the bottom upward to the top, countercurrent to the descending hot gases, by a mechanism known as a rock pump. The process technology was invented by the American oil company Unocal Corporation in late 1940s and was developed through several decades. The largest oil shale retort ever built was the Union B type retort.

The Chevron STB process is an above-ground shale oil extraction technology. It is classified as a hot recycled solids technology.

LLNL HRS process is an above-ground shale oil extraction technology. It is classified as a hot recycled solids technology.

KENTORT II is an above-ground shale oil extraction process developed by the Center for Applied Energy Research of the University of Kentucky. It is a hot recycled solids fluidized bed retorting process developed since 1982 for processing the eastern United States Devonian oil shales. The concept of this process was initiated in 1986 in the test unit.

The Shell Spher process is an above ground fluidization bed retorting technology for shale oil extraction. It is classified as a hot recycled solids technology.

References

  1. "The Trillion-Barrel Field". Time . 1957-06-03. Archived from the original on April 14, 2011. Retrieved 2008-11-29.
  2. 1 2 3 4 5 United States Office of Technology Assessment (June 1980). An Assessment of Oil Shale Technologies (PDF). DIANE Publishing. ISBN   978-1-4289-2463-5. NTIS order #PB80-210115. Retrieved 2008-11-29.
  3. Yen, Teh Fu; Chilingar, George V. (1976). Oil Shale. Amsterdam: Elsevier. p. 244. ISBN   978-0-444-41408-3 . Retrieved 2009-07-07.
  4. Burnham, Alan K.; McConaghy, James R. (2006-10-16). Comparison of the acceptability of various oil shale processes (PDF). 26th Oil shale symposium. Golden, Colorado: Lawrence Livermore National Laboratory. UCRL-CONF-226717. Retrieved 2008-11-29.
  5. 1 2 Johnson, Harry R.; Crawford, Peter M.; Bunger, James W. (2004). "Strategic significance of America's oil shale resource. Volume II: Oil shale resources, technology and economics" (PDF). Office of Deputy Assistant Secretary for Petroleum Reserves; Office of Naval Petroleum and Oil Shale Reserves; United States Department of Energy . Retrieved 2008-11-29.{{cite journal}}: Cite journal requires |journal= (help)
  6. Lee, Sunggyu (1990). Oil Shale Technology. CRC Press. p. 111. ISBN   0-8493-4615-0 . Retrieved 2008-11-29.