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Energy infrastructure modeling for the oil sands industry: Current situation

机译:油砂行业的能源基础设施建模:现状

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摘要

In this study, the total energy requirements associated with the production of bitumen from oil sands and its upgrading to synthetic crude oil (SCO) are modeled and quantified. The production scheme considered is based on the commercially applied steam assisted gravity drainage (SAGD) for bitumen extraction and delayed coking for bitumen upgrading. In addition, the model quantifies the greenhouse gas (GHG) emissions associated with the production of energy required for these operations from technologies utilized in the currently existing oil sands energy infrastructure. The model is based on fundamental engineering principles, and Aspen HYSYS and Aspen Plus simulations. The energy demand results are expressed in terms of heat, power, hydrogen, and process fuel consumption rates for SAGD extraction and bitumen upgrading. Based on the model's output, a range of overall energy and emission intensity factors are estimated for a bitumen production rate of 112,500 BPD (or 93,272 BPD of SCO), which were determined to be 262.5-368.5 MJ/GJ(SCO) and 14.17-19.84 gCO(2)/MJ(SCO), respectively. The results of the model indicate that the majority of GHG emissions are generated during SAGD extraction (up to 60% of total emissions) due to the combustion of natural gas for steam production, and the steam-to-oil ratio is a major parameter affecting total GHG emissions. The developed model can be utilized as a tool to predict the energy demand requirements for integrated SAGD/upgrading projects under different operating conditions, and provides guidance on the feasibility of lowering GHG emissions associated with their operation. (C) 2016 Elsevier Ltd. All rights reserved.
机译:在这项研究中,对从油砂生产沥青和将其升级为合成原油(SCO)的总能量需求进行了建模和量化。所考虑的生产方案基于用于沥青提取的商业应用蒸汽辅助重力排水(SAGD),以及用于沥青升级的延迟焦化。此外,该模型还通过使用现有油砂能源基础设施中使用的技术来量化与这些操作所需的能源生产相关的温室气体(GHG)排放。该模型基于基本工程原理以及Aspen HYSYS和Aspen Plus仿真。能源需求结果以热,功率,氢气和SAGD提取和沥青升级的过程燃料消耗率表示。根据模型的输出,估算出一系列总体能量和排放强度因子,得出沥青生产率为112,500 BPD(或SCO 93,272 BPD),确定为262.5-368.5 MJ / GJ(SCO)和14.17-分别为19.84 gCO(2)/ MJ(SCO)。该模型的结果表明,SAGD提取过程中产生的大部分GHG排放(占总排放量的60%)是由于用于生产蒸汽的天然气燃烧而产生的,而蒸汽/油比是影响其排放的主要参数。温室气体总排放量。所开发的模型可以用作预测在不同运行条件下集成SAGD /升级项目的能源需求需求的工具,并为降低与其运营相关的温室气体排放的可行性提供指导。 (C)2016 Elsevier Ltd.保留所有权利。

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