IN-SITU CATALYTIC UPGRADING OF HEAVY CRUDE AND BITUMEN: OPTIMISATION OF NOVEL CAPRI REACTOR
IN-SITU CATALYTIC UPGRADING OF HEAVY CRUDE AND BITUMEN: OPTIMISATION OF NOVEL CAPRI REACTOR
批准号:
EP/E057977/1
负责人:
Joseph Wood
金额:
$53.86万
依托单位:
依托单位国家:
英国
项目类别:
Research Grant
财政年份:
2007
资助国家:
英国
项目状态:
已结题
起止时间:
2007 至 --
中文摘要
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英文摘要
Heavy crude oil and bitumen are a vast, largely unexploited hydrocarbon resource, with barely 1% produced so far, compared with more than 50% of conventional light oil (like the North Sea). More than 80% of this heavy, unconventional oil, lies in the Western hemisphere, whereas more than 80% of conventional light oil lies in the Eastern hemisphere (mainly in the Middle East). Over the next 10-30 years, geopolitical factors, and also the emerging strength of Asian countries, especially India and China, will create increasing tensions and uncertainty, with regard to the availability and supply of crude oil. Alongside gas, nuclear and renewables, crude oil will continue to be an important part of the UK's 'energy mix' for decades to come. How will the crude oil we need for industry and transportation be obtained and will it be as secure as it was from the North Sea?The huge Athabasca Oil Sands deposits in Canada (1.5 trillion barrels) provides an opportunity for the UK to secure access to a long-term, stable supply. The first step towards this was the development of a new technology, THAI - 'Toe-to-Heel Air Injection', to produce Oil Sands bitumen and heavy oil. It was discovered by the Improved Oil Recovery group at the University Bath, in the 1990's, and is currently being field tested at Christina Lake, Alberta, Canada. In 1998, in collaboration with the Petroleum Recovery Institute (PRI), Calgary, Canada, the Bath group discovered another process, based on THAI, called CAPRI. The THAI-CAPRI processes have the potential to convert bitumen and heavy crude into virtually a light crude oil, of almost paraffin-like consistency, at a fraction of the cost of conventional surface processing. A surface upgrading plant has recently been proposed for the UK, at a cost of $2-3 billion.The advantage of CAPRI is that it creates a catalytic reactor in the petroleum reservoir, by 'sleeving' a layer of catalyst around the 500-100 m long horizontal production well, inside the reservoir. The high pressure and temperature of the reservoir enable the thermal cracking and hydroconversion reactions to take place, so that only light, converted oil is produced at the surface. Apart from the cost of the catalyst, which can be a standard refinery catalyst, the CAPRI reactor is virtually free! All that is needed is to inject compressed air, in order to propagate a combustion front in a 'toe-to-heel' manner along the horizontal production well.In collaboration with the University of Birmingham, the project will investigate the effectiveness of a range of catalyst for use in the CAPRI process. The University of Birmingham team, led by Dr. Joe Wood, will investigate the long-term survivability of the catalysts, which is critical to operation of CAPRI. Once the catalyst is emplaced around the horizontal well, it will be expensive to recover or replace it. Previous 3D combustion cell experiments conducted by the Bath team, only allowed catalyst operating periods of a few hours, whereas in practice, the catalyst will need to survive, remain active, for days, or weeks. The Bath team will undertake detailed studies to characterise the internal pore structure of the catalysts used in the experiments, to obtain fundamental information on catalyst deactivation, which can be related to the process conditions and oil composition. They will also develop a detailed numerical model of the CAPRI reactor. This will provide a tool to explore 'fine details' of the THAI-CAPRI process, which will aid in the selection/optimisation of the most suitable catalysts. The model will be incorporated into a larger model using the STARS reservoir simulator. Preliminary reservoir simulations will be made to explore the potential operating conditions for CAPRI.
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DOI:
10.1021/acs.iecr.5b02953
发表时间:
2015-11-04
期刊:
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
影响因子:
4.2
作者:
[Al-Marshed, Abdullah, Hart, Abarasi, Wood, Joseph]
通讯作者:
Wood, Joseph
Investigation of the problems with using gas adsorption to probe catalyst pore structure evolution during coking.
研究利用气体吸附探测焦化过程中催化剂孔结构演变的问题。
DOI:
10.1016/j.jcis.2012.10.025
发表时间:
2013
期刊:
Journal of colloid and interface science
影响因子:
9.9
作者:
[Gopinathan N]
通讯作者:
Gopinathan N
DOI:
10.3390/en11030636
发表时间:
2018-03-01
期刊:
ENERGIES
影响因子:
3.2
作者:
[Hart, Abarasi, Wood, Joseph]
通讯作者:
Wood, Joseph
DOI:
10.1016/j.fuproc.2015.07.016
发表时间:
2015-10-01
期刊:
FUEL PROCESSING TECHNOLOGY
影响因子:
7.5
作者:
[Hart, Abarasi, Lewis, Charlotte, Wood, Joseph]
通讯作者:
Wood, Joseph
DOI:
10.1021/acs.energyfuels.5b01451
发表时间:
2015-10-01
期刊:
ENERGY & FUELS
影响因子:
5.3
作者:
[Al-Marshed, Abdullah, Hart, Abarasi, Wood, Joseph]
通讯作者:
Wood, Joseph
共 9 条
Catalytic Microwave Process for Upgrading of Pyrolysis Liquids from Ubiquitous Plastic Wastes
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批准号:EP/Y001168/1
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项目类别:Research Grant
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资助金额:$67.97万
-
财政年份:2024
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负责人:Joseph Wood
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依托单位:
Thermally Responsive Supports for Enhanced Efficiency in PET Depolymerisation
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负责人:Joseph Wood
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依托单位:
A Scalable Process for the Chemical Recycling of PET using Ionic Organocatalysts
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资助金额:$119.95万
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财政年份:2022
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负责人:Joseph Wood
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Novel Membrane Catalytic Reactor for Waste Polylactic Acid Recycling and Valorisation
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批准号:EP/P016405/1
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项目类别:Research Grant
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资助金额:$94.29万
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财政年份:2017
-
负责人:Joseph Wood
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依托单位:
DIVA: Data Intensive Visual Analytics - Provenance and Uncertainty in Human Terrain Analysis
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批准号:EP/J020443/1
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项目类别:Research Grant
-
资助金额:$21.96万
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财政年份:2012
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负责人:Joseph Wood
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依托单位:
Towards Realisation of Untapped Oil Resources via Enhanced THAI-CAPRI Process Using Novel Catalysts
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批准号:EP/J008303/1
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项目类别:Research Grant
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资助金额:$64.21万
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财政年份:2012
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负责人:Joseph Wood
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依托单位:
The development of structure in coarse-grained river bed sediments: the key to predicting sediment flux
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批准号:NE/H021973/1
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项目类别:Research Grant
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资助金额:$2.19万
-
财政年份:2011
-
负责人:Joseph Wood
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依托单位:
Understanding Bio-induced Selectivity in Nanoparticle Catalyst Manufacture
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批准号:EP/I007806/1
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项目类别:Research Grant
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资助金额:$67.39万
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财政年份:2010
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负责人:Joseph Wood
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依托单位:
C-Cycle
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批准号:EP/E010601/1
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项目类别:Research Grant
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资助金额:$11.3万
-
财政年份:2006
-
负责人:Joseph Wood
-
依托单位:
Heterogeneous Catalysis in Supercritical Fluids: The Enhancement of Catalytic Stability to Coking
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批准号:EP/D503892/1
-
项目类别:Research Grant
-
资助金额:$24.91万
-
财政年份:2006
-
负责人:Joseph Wood
-
依托单位:
海外基金