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Relevant bibliographies by topics / Oil processing

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Academic literature on the topic 'Oil processing'

Author: Grafiati

Published: 28 May 2022

Last updated: 31 May 2022

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Journal articles on the topic "Oil processing"

1

Muratova, A. K., I. A. Kyrgyzalina, B. R. Nussupbekov, A. Zh Satybaldin, and Z. K. Aitpaeva. "Innovative method of processing oil products." Bulletin of the Karaganda University. "Physics Series" 88, no. 4 (December 30, 2017): 53–58. http://dx.doi.org/10.31489/2017phys4/53-58.

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Mullakaev, M. S., G. B. Wexler, and R. M. Mullakaev. "Mobile sonochemical complex оf oil sludge processing." SOCAR Proceedings, no. 3 (September 30, 2019): 88–96. http://dx.doi.org/10.5510/ogp20190300402.

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Pysh’yev, Serhiy, Olexander Lazorko, and Michael Bratychak. "Oxidative Processing of Light Oil Fractions. A Review." Chemistry & Chemical Technology 3, no. 1 (March 15, 2009): 77–81. http://dx.doi.org/10.23939/chcht03.01.077.

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The review and analysis of oxidation processes necessary for quality improvement of oil fractions boiling to 623 K have been carried out. Different oxidative technologies for crude oil processing have been examined. Their advantages and disadvantages have been shown.

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Dung, Nguyen V., Arona J. Feltenstein, and Regano G. Benito. "Processing oil shales with heavy oil recycle." Fuel 71, no. 12 (December 1992): 1505–10. http://dx.doi.org/10.1016/0016-2361(92)90226-e.

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Livshits, Michael, and Alexander Sizikov. "Primary oil processing optimization." MATEC Web of Conferences 92 (December 21, 2016): 01022. http://dx.doi.org/10.1051/matecconf/20179201022.

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Huang, W. "Processing Lunpola Crude Oil." Petroleum Science and Technology 26, no. 13 (August 22, 2008): 1610–17. http://dx.doi.org/10.1080/10916460701287631.

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Timms, R. E. "Processing of Palm Kernel Oil." Fette, Seifen, Anstrichmittel 88, no. 8 (1986): 294–300. http://dx.doi.org/10.1002/lipi.19860880805.

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Dudkin, D. V., M. G. Kul’kov, E. N. Shestakova, A. A. Yakubenok, and A. A. Novikov. "Mechanochemical processing of oil residues." Chemistry and Technology of Fuels and Oils 48, no. 4 (September 2012): 302–7. http://dx.doi.org/10.1007/s10553-012-0372-x.

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Sato, Susumu. "Quality control in oil processing." Journal of the American Oil Chemists' Society 62, no. 2 (February 1985): 309–10. http://dx.doi.org/10.1007/bf02541396.

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Evdoshenko, Yu V. "Xinjiang oil and the "Dushantsi" oil processing plant. Oil production and processing in northwest China in 1938–1943." Neftyanoe khozyaystvo - Oil Industry 2 (2020): 108–12. http://dx.doi.org/10.24887/0028-2448-2020-2-108-112.

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Dissertations / Theses on the topic "Oil processing"

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Mardupenko, Aleksey, Andrey Grigorov, Irina Sinkevich, and Alena Tulskaya. "Technological processing of oil sludge." Thesis, ФОП Бондаренко М. О, 2017. http://repository.kpi.kharkov.ua/handle/KhPI-Press/48883.

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Lopez, Yadira. "Integrated processing for heavy crude oil." Thesis, University of Manchester, 2015. https://www.research.manchester.ac.uk/portal/en/theses/integrated-processing-for-heavy-crude-oil(ec191370-cb4a-417f-995e-33f9ff053c1d).html.

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Energy based on non-renewable resources such as gas, oil, coal and nuclear fission, even with their serious problems of pollution, contributes to 86% of the global energy consumption. Oil will remain the dominant transport fuel: about 87% of transport fuel in 2030 will still be petroleum-based. Discoveries of conventional sources of light easy-to-access crude oil are becoming less common and current oil production levels are struggling to match demand, it is necessary to develop new non-conventional sources of oil in order to supplement conventional oil supply, whose demand is increasing continuously. A possible clue to solve this situation could be to take advantage of the extensive reserves of heavy crude oils existing in different places around the world, which could be an excellent source of more valuable hydrocarbons. In this context, some facilities called upgraders are used to process theses heavy crude oils to both increase the hydrogen-carbon ratio and improve their quality, reducing their density and decreasing their viscosity, sulphur, nitrogen and metals. The main objective in this work is to study the heavy crude oil upgrading processes in order to identify new operation schemes which explore different opportunities of integration between the upgraders and other processes or new schemes for upgraders that can sustain on its own through the production of a wide range of products. Each design alternative has been modelled with state-of-the-art commercial software packages. The crude oil dilution process was evaluated using naphtha and a light crude oil as diluents. Sensitivity analyses were done with the purpose of selecting the type and flow rate of diluent. Once the best diluent was selected, the integration of an upgrader to a refinery was studied. Heavy ends from both the upgrader and the refinery were taken as feedstocks to an integrated gasification combined cycle (IGCC). The best operation schemes for IGCC, in order to achieve the requirements of power and hydrogen for the upgrader and the refinery was determined. Different schemes for heavy crude oil processing to produce transportation fuel instead of syncrude were proposed, too. Finally, economic evaluation of all the schemes was performed to find the best solution for heavy crude oils. The best results for the dilution process of heavy crude oils were obtained when naphtha was used as diluent. The configuration proposed for the upgrader allows producing a synthetic crude oil with 35.5 °API. The integration of the upgrader to a refinery allows the treatment of the heavy streams of the refinery and transforms them into products of higher qualities. The integration of the IGCC to the upgrader and the refinery permits a complete elimination of the heavy residues produced in these units and produces hydrogen and power to be used in the site or to export. Economic evaluation shows that all the proposed processing schemes studied are economically attractive. The proposed processing schemes chosen include the integration between upgrader refinery and IGCC unit with CCS.

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Yousef, Abdul Halek, and M. Zenkin. "Oil-processing pump units vibromonitoring system." Thesis, Київський національний університет технологій та дизайну, 2019. https://er.knutd.edu.ua/handle/123456789/14599.

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Pereira, Igor S. M. "Microwave processing of oil contaminated drill cuttings." Thesis, University of Nottingham, 2013. http://eprints.nottingham.ac.uk/28515/.

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Easily accessible oil reserves are currently decreasing, leading to an increase in more complex offshore deep-sea drilling programs, which require increasingly greater depths to be drilled. Such wells are commonly drilled using oil based muds, which leads to the production of drilled rock fragments, drill cuttings, which are contaminated with the base oil present in the mud. It is a legal requirement to reduce oil content to below 1 wt% in order to dispose of these drill cuttings in the North Sea and microwave processing is suggested as a feasible method of achieving the desired oil removal. However, there are currently gaps in our understanding of the mechanisms behind, and variables affecting, the microwave treatment of oil contaminated drill cuttings. The work described in this thesis seeks to address some of these gaps in knowledge. There were three main objectives for this thesis: (1) quantification, for the first time in the literature, of the main mechanisms driving oil and water removal during microwave processing of oil contaminated drill cuttings, (2) determination of key variables affecting performance during pilot scale continuous processing of oil contaminated drill cuttings and, for the first time, (3) treatment of drill cuttings with microwaves continuously at 896 MHz. Bench scale experiments carried out in a single mode applicator were used to quantify the mechanisms involved in oil and water removal from drill cuttings. It was found that both vaporisation and entrainment mechanisms play a role in oil and water removal. Vaporisation was the main mechanism of water and oil removal, and typically accounted for >80-90% of the water and oil removed. For oil removal, vaporisation of the oil phase accounted for 70-100% of the overall removal. The absolute amount of water entrained and vaporised was found to increase with increasing energy input and power density. However, as a percentage of the overall amount removed, entrainment was found to increase with increasing energy input. This was mainly due to higher heating rates at higher energy inputs, leading to pressurised, high velocity steam, which increased liquid carry-over (entrainment). Both the drill cuttings sample composition and applicator type were found to have an effect on the extent of entrainment/vaporisation. Samples consisting of a higher overall liquid content, tended to have a greater amount of surface liquid content. This led to a greater potential of carry over when steam generated internally left the sample. Increasing the power again led an increase in entrainment in this case. Different applicators were found to impact the electric field strength and power density within the water phase of the sample. Oil removal in multimode applicators progressed mainly through vaporisation (steam distillation) until the water content was sufficiently low to generate steam at a velocity high enough to entrain liquid droplets. When treatment was changed to single mode operation, entrainment occurred at an earlier stage, probably due to higher electric field strengths and power densities. It was also noted that the vaporisation mechanism of oil was more efficient at higher field strengths and powers, which could again be attributed to superheating and higher velocity steam, which enabled better mixing and heat transfer. Experiments were also run to determine the main variables affecting the performance of continuous processing of cuttings. Overall continuous processing showed a substantial improvement in the energy required, 150 kWh/t vs. >250 kWh/t, to reduce the oil content of a drill cuttings sample to 1 wt%. It was found that the initial water and oil content of the sample, as well as the sample particle size distribution, had the greatest effect on the efficiency of continuous processing. The effect of initial water and oil content on residual oil content was investigated methodically for the first time for continuous microwave processing of oil contaminated drill cuttings. An increase in initial oil content was found to have a significant impact on the energy input required to treat the sample to 1 wt% oil content. As the oil content increased, the energy input required increased exponentially, mainly as a result of the change in the physical structure of the sample. An increase in the water content led to an increase in energy input without any additional benefit to oil removal. However, as the water content was increased it was noticed that the theoretical energy input required to heat the entire sample approached the actual value measured for the energy input. This occurs as a result of the increasingly greater bulk dielectric properties of the sample as a result of higher levels of water content, which in turn leads to a higher efficiency in the conversion of microwave energy to heat in the sample. The effect of particle size on oil content distribution and removal was investigated. Oil content was found to be substantially higher in particles of size <1.0 mm, with removal also being significantly higher in this particle size range. However, as the majority of the samples tested, >80%, consisted of particles >1.0 mm, this improved removal is diluted by the performance of the coarser particles. The improved removal in finer particles is likely to be due to larger surface area, reduced path length within the particles and potentially higher electric field strength. Finally, samples processed continuously using a continuous microwave setup at 896 MHz showed improvements over both continuous microwave treatment at 2.45 GHz and bench scale setups. Increasing the f10wrate of the system at 896 MHz was also found to improve oil removal efficiency, which can be explained by the higher power requirements that would be required to maintain the energy inputs observed at the lower flowrate. Increasing the power leads to improved heating rates and thus increased removal rates through entrainment and vaporisation.

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Rahman, Ibrahim Haji Abdul. "The influence of processing on coconut oil." Thesis, University of Reading, 1990. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.278107.

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Warnock, Peter. "Identification of ancient olive oil processing methods based on olive remains /." free to MU campus, to others for purchase, 2004. http://wwwlib.umi.com/cr/mo/fullcit?p3144469.

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Kubanek, Gordon J. "Heavy oil processing in steam and hydrogen plasmas." Thesis, McGill University, 1985. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=63281.

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Voldsund, Mari. "Exergy analysis of offshore oil and gas processing." Doctoral thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for kjemi, 2014. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-25310.

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Oil and gas extraction have been responsible for 25—28% of the total greenhouse gas emissions in Norway the last 10 years. The part from offshore oil and gas processing, including power production, flaring, and cold ventilation on production platforms, accounted for 20—22%. Exergy analysis is a method for systematic assessment of potential to perform work. It gives the possibility to identify where in a process inefficiencies occur: both losses to the surroundings and internal irreversibilities, and can be used as a tool for pinpointing improvement potential and for evaluation of industrial processes. When used in the petroleum sector, this can motivate more efficient oil and gas extraction, leading to a better utilisation of the resources and less greenhouse gas emissions. The objectives of this thesis were to: (i) establish exergy analyses of the oil and gas processing plants on different types of North Sea platforms; (ii) identify and discuss improvement potentials for each case, compare them and draw general conclusions if possible; and (iii) define meaningful thermodynamic performance parameters for evaluation of the platforms. Four real platforms (Platforms A—D) and one generic platform of the North Sea type were simulated with the process simulators Aspen HYSYS and Aspen Plus. The real platforms were simulated using process data provided by the oil companies. The generic platform was simulated based on literature data, with six different feed compositions (Cases 1—6). These five platforms presented different process conditions; they differed for instance by their exported products, gas-to-oil ratios, reservoir characteristics and recovery strategies. Exergy analyses were carried out, and it was shown that for the cases studied in this work, the power consumption was in the range of 5.5—30 MW, or 20—660 MJ/Sm3 o.e. exported. The heat demand was very small and covered by electric heating for two of the platforms, and higher, but low enough to be covered by waste heat recovery from the power turbines and by heat integration between process streams, for the other three platforms. The main part of the power was consumed by compressors in the gas treatment section for all cases, except Platform B and Case 4 of the generic model. Platform B had lower pressures in the products than in the feeds, resulting in a low compression demand. Case 4 of the generic model had a high content of heavy hydrocarbons in the feed, resulting in large power demand in the oil export pumping section. The recompression and oil pumping sections appeared to be the other major power consumers, together with the seawater injection system, if installed. The total exergy destruction was in the range of 12—32 MW, or 43—517 MJ/Sm3 o.e. exported. Most exergy destruction was related to pressure increase or decrease. Exergy destruction in the gas treatment section made up 8—57% of the total amount, destruction in the recompression section accounted for 11—29%, while 10—28% took place in the production manifolds. Exergy losses due to flaring varied in the range of 0—13 MW. Platforms with high gas-to-oil ratios and high pressures required in the gas product presented the highest power consumption and exergy destruction. Several measures were proposed for reduction of exergy destruction and losses. Two alternatives included use of mature technologies with potential to increase efficiency significantly: (i) limit flaring by installation of gas recovery systems, and (ii) improve gas compression performance by updating/exchanging the compressors. Several thermodynamic performance indicators were discussed, with Platforms A—D as case studies. None of the indicators could at the same time evaluate (i) utilisation of technical achievable potential, (ii) utilisation of theoretical achievable potential and (iii) total use of energy resources. It was concluded that a set of indicators had to be used to evaluate the thermodynamic performance. The following indicators were suggested: BAT efficiency on exergy basis, exergy efficiency, and specific exergy destruction. The formulation of exergy efficiency for offshore processing plants is difficult because of (i) the high throughput of chemical exergy, (ii) the large variety of chemical components in the process streams and (iii) the differences in operating conditions. Approaches found in the literature for similar processes were applied to Platforms A—D. These approaches had several drawbacks when applied to offshore processing plants; they showed low sensitivity to performance improvements, gave inconsistent results, or favoured platforms operating under certain conditions. A new exergy efficiency, called the component-by-component efficiency, was proposed. This efficiency could successfully evaluate the theoretical improvement potential. Eksergianalyse av offshore olje- og gassprosessering Olje- og gassutvinning har vært kilde til 25—28% av de totale klimagassutslippene i Norge de siste 10 årene. Den delen som stammer fra offshore olje- og gassprosessering (kraftproduksjon, fakling og kaldventilering på produksjonsplattformer) stod for 20—22%. Eksergianalyse er en metode for systematisk bestemmelse av potensiale til å utføre arbeid. Det gir mulighet til å identifisere hvor i en prosess ineffektiviteter oppstår: både i form av tap til omgivelsene og i form av interne irreversibiliteter. Det kan brukes som et verktøy for å finne forbedringsmuligheter og for evaluering av industrielle prosesser. Ved bruk innen petroleumssektoren kan dette motivere for mer effektiv olje- og gassutvinning, noe som gir bedre utnyttelse av ressursene og mindre utslipp av klimagasser. Formålet med denne avhandlingen er å: (i) etablere eksergianalyser av olje- og gassprosessering på ulike typer Nordsjø-plattformer; (ii) identifisere og diskutere forbedringspotensialer for hvert tilfelle, sammenligne dem og trekke generelle konklusjoner om mulig; og (iii) definere meningsfulle termodynamiske ytelsesindikatorer for evaluering av plattformene. Fire virkelige plattformer (Plattform A—D) og en generisk Nordsjø-type plattform er simulert med prosessimulatorene Aspen HYSYS og Aspen Plus. De virkelige plattformene er simulert ved å bruke prosessdata stilt til rådighet av operatørene av plattformene. Den generiske plattformen er simulert basert på litteraturdata, med seks ulike fødesammensetninger (Case 1—6). Disse fem plattformene har ulike prosessbetingelser; de har for eksempel ulike eksporterte produkter, gass/olje-forhold, reservoaregenskaper og utvinningsstrategier. Eksergianalyser viser at for tilfellene studert i dette arbeidet er kraftforbruket i størrelsesorden 5,5—30 MW, eller 20—660 MJ/Sm3 o.e. eksportert. Varmebehovet er svært lite og blir dekket med elektrisitet for to av plattformene, og noe høyere men lavt nok til å bli dekket med varmegjenvinning fra kraftturbinene og ved varmeveksling mellom prosesstrømmer for de tre andre plattformene. Hoveddelen av kraften blir konsumert av kompressorene i gassbehandlingsseksjonen for alle tilfellene bortsett fra Plattform B og Case 4 i den generiske modellen. Plattform B har lavere trykk i produktstrømmene enn i fødestrømmene, noe som resulterer i lavt behov for kompresjon. Case 4 i den generiske modellen har et høyt innhold av tunge hydrokarboner i føden, noe som resulterer i høyt kraftbehov i seksjonen for eksportpumping. Seksjonene for rekompresjon og eksportpumping viser seg å være de andre viktigste kraftforbrukerene, sammen med systemet for sjøvannsinjeksjon hvis dette er installert. Den totale ekserginedbrytingen er 12—32 MW, eller 43—517 MJ/Sm3 o.e. eksportert. Mest ekserginedbryting er relatert til trykkøking eller trykkreduksjon. Ekserginedbryting i gassbehandlingsdelen utgjør 8—57% av den totale mengden, nedbryting i rekompresjonsseksjonen utgjør 11-29%, mens nedbryting i produksjonsmanifoldene utgjør 10—28%. Eksergitap på grunn av fakling varierer mellom 0—13 MW. Plattformene med høye gass/olje-forhold og behov for høyt trykk i gassproduktene har høyest kraftforbruk og ekserginedbryting. Ulike tiltak for reduksjon av ekserginedbryting og eksergitap er foreslått. To alternativer inkluderer bruk av modne teknologier og har potensiale til å øke effektiviteten betydelig: (i) begrensning av fakling av gass ved installasjon av gassgjenvinningssystemer, og (ii) forbedring av gasskompresjonen ved å oppdatere/bytte ut kompressorer. Flere termodynamiske ytelsesindikatorer er diskutert med utgangspunkt i Plattform A—D. Ingen av indikatorene kan på samme tid evaluere (i) utnyttelse av teknisk oppnåelig potensiale, (ii) utnyttelse av teoretisk potensiale og (iii) total bruk av energiressurser. Det konkluderes med at et sett med indikatorer må brukes for å evaluere termodynamisk ytelse. De følgende indikatorene foreslås: BAT (best tilgjengelig teknologi) effektivitet på eksergibasis, eksergieffektivitet og spesifikk ekserginedbryting. Formuleringen av eksergieffektivitet for offshore olje- og gassprosessering er utfordrende på grunn av (i) den høye gjennomgangen av kjemisk eksergi, (ii) den store variasjonen av kjemiske komponenter i prosesstrømmene og (iii) de store forskjellene i driftsbetingelser. En ny type eksergieffektivitet foreslås. Denne effektiviteten kan evaluere utnyttelsen av det teoretiske potensialet på tross av punktene nevnt ovenfor.

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Michel, de Arévalo Aymeé. "Phytosterol enrichment in vegetable oil by high pressure processing." Aachen Shaker, 2008. http://d-nb.info/994829892/04.

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Nantiyakul, Nantaprapa. "Processing rice bran to yield added-value oil based extracts." Thesis, University of Nottingham, 2012. http://eprints.nottingham.ac.uk/12669/.

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Rice bran, a by-product from rice milling, is an excellent source of natural antioxidants. Lipids in rice bran appear as small spherical droplets called oil bodies. This work attempted to recover the oil bodies from rice bran (fresh, stored and heat-treated) and to determine their chemical, biochemical and physical properties ex vivo. As revealed by transmission electron microscopy, oil bodies were observed mainly in the sub-aleurone and aleurone layer of brown rice. Oil bodies were successfully recovered from rice bran and were enriched in tocochromanols and oryzanol (656 - 1,006 mg/kg lipid and 8,880 - 9,692 mg/kg lipid respectively). Further washing to remove extraneous protein and non-associated compounds, effective lipid concentration increased while protein concentration decreased. The washed oil body preparation contained approximately 35 - 68 % tocochromanols and 60 - 62 % oryzanol of the parent rice bran oil. Therefore, the majority of tocochromanols and oryzanol molecules appeared to be intrinsically associated with rice bran oil bodies ex vivo. Fatty acid composition of rice bran oil bodies was similar to that of parent rice bran. SDS-PAGE of proteins present in differentially washed oil body preparations revealed similar protein profiles; however, there was a relative enrichment of the bands at 16 - 18 kDa (typical molecular weight of oleosins). Rice bran oil bodies possessed negatively charged surface (-30 mV) at neutral pH. As the pH of the oil body suspension was lowered to the pH near pI (about pH 4 - 5), zeta potential of the oil bodies approached zero and the suspension had the least physical stability; aggregation and the least relative turbidity. The biochemical instability of rice occurs immediately after milling, which leads to the limited use of rice bran for human consumption. Free fatty acids and lipid hydroperoxides in rice bran and corresponding oil bodies increased significantly (P<0.05) during storage. Oil bodies recovered from stored rice bran aggregated and coalesced. 41% of tocochromanols in the oil bodies had decomposed while the concentration of oryzanol was relatively stable during the storage. Rice bran heat treatments (pan roasting and extrusion) caused the coalescence of oil bodies in vivo and the instability of an oil body suspension ex vivo. The main findings of this study were that rice bran oil bodies were enriched in phytochemicals including tocochromanols and oryzanol and were resistant to oxidation providing that the oil bodies were still intact. The oil bodies could delay the onset of lipid oxidation of stored lipids inside the oil bodies. This may be explained by the physical barrier of surface membrane protein (oleosin) against pro-oxidants and the intrinsic association between the oil bodies and phytochemicals in rice bran.

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Books on the topic "Oil processing"

1

Edible oil processing. Chichester, West Sussex: John Wiley & Sons Inc., 2013.

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Hamm, Wolf, Richard J. Hamilton, and Gijs Calliauw, eds. Edible Oil Processing. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.

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Farr, Walter E. Green vegetable oil processing. Urbana, IL: AOCS Press, 2012.

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Green vegetable oil processing. Urbana, Illinois: AOCS Press, 2014.

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Unnikrishnan, G. Oil and Gas Processing Equipment. First edition. | Boca Raton : CRC Press, 2021.: CRC Press, 2020. http://dx.doi.org/10.1201/9780429287800.

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Lubricant base oil and wax processing. New York: M. Dekker, 1994.

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Practical guide for vegetable oil processing. Urbana, IL: AOCS Press, 2007.

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Small-scale palm oil processing in Africa. Rome: Food and Agriculture Organization of the United Nations, 2002.

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Lai, Oi-Ming. Palm oil: Production, processing, characterization, and uses. Urbana, IL: AOCS Press, 2012.

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World Conference on Lauric Oils (1994 Manila, Phiippines). Proceedings of the World Conference on Lauric Oils: Sources, processing, and applications. Edited by Applewhite Thomas H. Champaign, Ill: AOCS Press, 1994.

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Book chapters on the topic "Oil processing"

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UNIFEM. "Prelims - Oil Processing." In Oil Processing, i—x. Rugby, Warwickshire, United Kingdom: Practical Action Publishing, 1987. http://dx.doi.org/10.3362/9781780444192.000.

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UNIFEM. "1. Oil Processing." In Oil Processing, 1–38. Rugby, Warwickshire, United Kingdom: Practical Action Publishing, 1987. http://dx.doi.org/10.3362/9781780444192.001.

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Cowan, David. "Enzyme Processing." In Edible Oil Processing, 197–221. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch7.

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Hettinger, W. P., D. P. Wesley, and R. H. Wombles. "Residual Oil Processing." In ACS Symposium Series, 99–117. Washington, DC: American Chemical Society, 1986. http://dx.doi.org/10.1021/bk-1986-0303.ch006.

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Oja, Vahur, and Eric M. Suuberg. "Oil Shale oil shale Processing oil shale processing , Chemistry and Technology." In Encyclopedia of Sustainability Science and Technology, 7457–91. New York, NY: Springer New York, 2012. http://dx.doi.org/10.1007/978-1-4419-0851-3_102.

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van Duijn, Gerrit, and Gerrit den Dekker. "Oil Processing Design Basics." In Edible Oil Processing, 267–310. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch10.

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Kellens, Marc, and Gijs Calliauw. "Oil Modification Processes." In Edible Oil Processing, 153–96. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch6.

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Gunstone, Frank D. "Composition and Properties of Edible Oils." In Edible Oil Processing, 1–39. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch1.

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Hamm, Wolf. "Bulk Movement of Edible Oils." In Edible Oil Processing, 41–54. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch2.

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van Doosselaere, Philippe. "Production of Oils." In Edible Oil Processing, 55–96. Chichester, UK: John Wiley & Sons, Ltd, 2013. http://dx.doi.org/10.1002/9781118535202.ch3.

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Conference papers on the topic "Oil processing"

1

Georgie, Wally John, and Patrick Colin Smith. "The Challenges in Processing Heavy Oil." In SPE Heavy Oil Conference Canada. Society of Petroleum Engineers, 2012. http://dx.doi.org/10.2118/157894-ms.

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Sabins, F. F. "Digital Processing of Satellite Images of Saudi Arabia." In Middle East Oil Show. Society of Petroleum Engineers, 1991. http://dx.doi.org/10.2118/21357-ms.

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3

Bothamley, Mark. "Offshore Processing Options for Oil Platforms." In SPE Annual Technical Conference and Exhibition. Society of Petroleum Engineers, 2004. http://dx.doi.org/10.2118/90325-ms.

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4

Ray, Tapas, Faisal Ibrahim Alharam, Mohamed Abdulla Shayea, Ali Saleh Al Hammadi, Abdulla Humaid AL-Jarwan, Jumaan Mohamed Al-Breiki, Mohamed Ali Bani Hamoor, and Nagendra Rustagi. "Debottlenecking of Oil Processing Train Capacity." In Abu Dhabi International Petroleum Exhibition & Conference. Society of Petroleum Engineers, 2019. http://dx.doi.org/10.2118/197608-ms.

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Eriksson, Klas. "Subsea Processing : Oil/Water Quality Control." In Offshore Technology Conference-Asia. Offshore Technology Conference, 2014. http://dx.doi.org/10.4043/24689-ms.

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Li, Ning, Xiao Yu, Qingqiang Wu, and Maowen Wu. "Oil exploration data mining image processing." In 2012 7th International Conference on Computer Science & Education (ICCSE 2012). IEEE, 2012. http://dx.doi.org/10.1109/iccse.2012.6295261.

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AlRashoud, Anwar M. "Processing Heavy Crude." In SPE Kuwait Oil and Gas Show and Conference. Society of Petroleum Engineers, 2015. http://dx.doi.org/10.2118/175328-ms.

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Al-Azemi, Hamed. "Refining Technology and Processing Developments." In SPE International Heavy Oil Conference and Exhibition. Society of Petroleum Engineers, 2018. http://dx.doi.org/10.2118/193672-ms.

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Roos, Arnout, and Mika Tienhaara. "Compact Processing Solutions." In SPE Asia Pacific Oil and Gas Conference and Exhibition. Society of Petroleum Engineers, 2012. http://dx.doi.org/10.2118/158690-ms.

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Rasmussen, Andreas W. "Enhanced Oil Recovery by Retrofitting Subsea Processing." In SPE Offshore Europe Oil and Gas Exhibition and Conference. Society of Petroleum Engineers, 2003. http://dx.doi.org/10.2118/83976-ms.

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Reports on the topic "Oil processing"

1

Torvikey, Gertrude Dzifa, and Fred Mawunyo Dzanku. In the Shadow of Industrial Companies: Class and Spatial Dynamics of Artisanal Palm Oil Processing in Rural Ghana. Institute of Development Studies (IDS), March 2022. http://dx.doi.org/10.19088/apra.2022.010.

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Abstract:

This paper is concerned with the multiple opportunities and challenges of artisanal palm oil processing and the potential multiplier effects on local economies. It examines the effect of the presence of large oil palm plantations and their industrial processing mills on artisanal palm oil processing in two districts in the Western region of Ghana. Although artisanal and industrial processors have co-existed for a long time in the same catchment areas, little is known about the impact of this relationship on artisanal processing. Acknowledging the importance of rural diversity, complexity, and difference in agriculture-based off-farm activities, this paper also examines the effect of community and household level factors on palm oil processing incidence and intensity as well as the impact of processing on food (in)security.

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Johnson, L. R., and R. H. Riley. Beneficiation-hydroretort processing of US oil shales, engineering study. Office of Scientific and Technical Information (OSTI), December 1988. http://dx.doi.org/10.2172/5585032.

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Skone, Timothy J. Canadian Oil Sands Synthetic, Extraction and Post-processing, Operation. Office of Scientific and Technical Information (OSTI), June 2009. http://dx.doi.org/10.2172/1509003.

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Nock, Anthony. Silica Hydrogel and its Use in Edible Oil Processing. AOCS, November 2016. http://dx.doi.org/10.21748/lipidlibrary.40336.

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Elliott, Douglas C., Suh-Jane Lee, and Todd R. Hart. Stabilization of Fast Pyrolysis Oil: Post Processing Final Report. Office of Scientific and Technical Information (OSTI), March 2012. http://dx.doi.org/10.2172/1047417.

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Duddy, J. E., S. V. Panvelker, M. S. Pramanik, G. A. Popper, and R. J. Parker. Bench-scale development of coal/oil co-processing technology. Office of Scientific and Technical Information (OSTI), December 1991. http://dx.doi.org/10.2172/6782727.

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Author, Not Given. Beneficiation-hydroretort processing of US oil shales: Volume 2. Office of Scientific and Technical Information (OSTI), January 1989. http://dx.doi.org/10.2172/5533660.

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Burnham, A. K. Slow Radio-Frequency Processing of Large Oil Shale Volumes to Produce Petroleum-Like Shale Oil. Office of Scientific and Technical Information (OSTI), August 2003. http://dx.doi.org/10.2172/15004663.

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Schulman, B. L. A fundamental research program in coal/heavy oil coprocessing and heavy oil processing: Final report. Office of Scientific and Technical Information (OSTI), June 1989. http://dx.doi.org/10.2172/6088853.

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Duddy, J. E., S. V. Panvelker, M. S. Pramanik, G. A. Popper, and R. J. Parker. Bench-scale development of coal/oil co-processing technology. Final summary report. Office of Scientific and Technical Information (OSTI), December 1991. http://dx.doi.org/10.2172/10128643.

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