Process Simulation and Optimization of Heat Pump Assisted Distillation Based Condensate Stabilization Unit

Hilman Ali Hazmi, Tri Partono Adhi
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Abstract

The phenomena of global warming caused by excessive greenhouse gas emissions, particularly carbon dioxide gas, has seriously impacted many significant areas of human life. Over the last 30 years, the oil and gas sector has caused a gradual increased in terms of its carbon dioxide gas emission by a large portion. This research aims to conduct a conceptual study of techno-economic to compare heat pump-assisted distillation technologies against the conventional distillation method. This research has the objective of significantly reducing the utility consumption demand in the form of heating load and electrical power requirement, as well as minimizing the emission of carbon dioxide gas generated from gas turbine generator and steam boiler units. This research consists of a base case model that implements the conventional distillation method for the condensate stabilization process, while both optimized 1 and 2 implement heat pump-assisted distillation technologies, in the form of mechanical vapor recompression (in optimized model 1) and heat integrated distillation (in optimized model 2). All simulation models were prepared using process simulation software ASPEN HYSYS at steady state conditions with Peng-Robinson as a fluid package. The economic analysis conducted was based on a minimum feasibility estimate of class V with an accuracy of -30% / +50%. Optimized models 1 and 2 were able to reduce the total duty requirement by 23.68 % and 26.70 % compared to the base case model, thus causing a reduction in the OPEX by 51.11 % and 24.23 %. In line with the reduction of total duty requirement, the carbon dioxide gas emission rate for optimized models 1 and 2 has also decreased by 22.78 % and 36.18 % compared to the base case model. Furthermore, despite the slight increase in CAPEX, optimized models 1 and 2 still shows a positive trend in terms of their economic valuation, with a reduction in TAC compared to the base case model by 14.88 % and 4.86 % respectively.
基于热泵辅助蒸馏的冷凝水稳定装置的过程模拟与优化
过度排放温室气体,特别是二氧化碳气体造成的全球变暖现象已严重影响到人类生活的许多重要领域。在过去的 30 年中,石油和天然气行业的二氧化碳排放量逐渐增加了一大部分。本研究旨在开展一项技术经济概念研究,对热泵辅助蒸馏技术与传统蒸馏方法进行比较。这项研究的目标是大幅降低供热负荷和电力需求等公用事业消费需求,并最大限度地减少燃气涡轮发电机和蒸汽锅炉机组产生的二氧化碳气体排放。本研究包括一个基础模型,该模型在冷凝水稳定过程中采用传统蒸馏方法,而优化模型 1 和 2 均采用热泵辅助蒸馏技术,即机械蒸汽再压缩(在优化模型 1 中)和热集成蒸馏(在优化模型 2 中)。所有模拟模型均使用 ASPEN HYSYS 工艺模拟软件在稳态条件下制作,并将 Peng-Robinson 作为流体软件包。所进行的经济分析基于 V 级最低可行性估计,精确度为 -30% / +50%。与基础模型相比,优化模型 1 和 2 能够将总运行需求降低 23.68 % 和 26.70 %,从而使运营支出分别降低 51.11 % 和 24.23 %。随着总税率要求的降低,优化模型 1 和模型 2 的二氧化碳气体排放率也比基础模型降低了 22.78 % 和 36.18 %。此外,尽管资本支出(CAPEX)略有增加,但优化模型 1 和模型 2 的经济估值仍呈现出积极的趋势,与基础模型相比,总可变资本支出(TAC)分别减少了 14.88 % 和 4.86 %。
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