Optimization of pipeline transport for CO2 sequestration
Optimization of pipeline transport for CO2 sequestration
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DOI:
10.1016/j.enconman.2005.06.001
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发表时间:
2006-04
影响因子:
10.4
通讯作者:
Zao-xiao Zhang;Geoff Wang;P. Massarotto;V. Rudolph
中科院分区:
文献类型:
--
作者:
Zao-xiao Zhang;Geoff Wang;P. Massarotto;V. Rudolph
Coal fired power generation will continue to provide energy to the world for the foreseeable future. However, this energy use is a significant contributor to increased atmospheric CO2concentration and, hence, global warming. Capture and disposal of CO2has received increased R&D attention in the last decade as the technology promises to be the most cost effective for large scale reductions in CO2emissions. This paper addresses CO2transport via pipeline from capture site to disposal site, in terms of system optimization, energy efficiency and overall economics. Technically, CO2can be transported through pipelines in the form of a gas, a supercritical fluid or in the subcooled liquid state. Operationally, most CO2pipelines used for enhanced oil recovery transport CO2as a supercritical fluid. In this paper, supercritical fluid and subcooled liquid transport are examined and compared, including their impacts on energy efficiency and cost. Using a commercially available process simulator, ASPEN PLUS 10.1, the results show that subcooled liquid transport maximizes the energy efficiency and minimizes the cost of CO2transport over long distances under both isothermal and adiabatic conditions. Pipeline transport of subcooled liquid CO2can be ideally used in areas of cold climate or by burying and insulating the pipeline. In very warm climates, periodic refrigeration to cool the CO2below its critical point of 31.1°C, may prove economical. Simulations have been used to determine the maximum safe pipeline distances to subsequent booster stations as a function of inlet pressure, environmental temperature and ground level heat flux conditions.