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Dynamic liquefied natural gas (LNG) processing with energy storage applications.

机译:具有储能应用的动态液化天然气(LNG)处理。

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摘要

The cryogenic carbon capture(TM) (CCC) process provides energy- and cost-efficient carbon capture and can be configured to provide an energy storage system using an open-loop natural gas (NG) refrigeration system, which is called energy storing cryogenic carbon capture (CCC-ES(TM)). This investigation focuses on the transient operation and especially on the dynamic response of this energy storage system and explores its efficiency, effectiveness, design, and operation. This investigation included four tasks. The first task explores the steady-state design of four different natural gas liquefaction processes simulated by Aspen HYSYS. These processes differ from traditional LNG process in that the CCC process vaporizes the LNG and the cold vapors return through the LNG heat exchangers, exchanging sensible heat with the incoming flows. The comparisons include costs and energy performance with individually optimized processes, each operating at three operating conditions: energy storage, energy recovery, and balanced operation. The second task examines steady-state and transient models and optimization of natural gas liquefaction using Aspen HYSYS. Steady-state exergy and heat exchanger efficiency analyses characterize the performance of several potential systems. Transient analyses of the optimal steady-state model produced most of the results discussed here. The third task explores transient Aspen HYSYS modeling and optimization of two natural gas liquefaction processes and identifies the rate-limiting process components during load variations. Novel flowrate variations included in this investigation drive transient responses of all units, especially compressors and heat exchangers. Model-predictive controls (MPC) effectively manages such heat exchangers and compares favorably with results using traditional controls. The last task shows how an unprocessed natural gas (NG) pretreatment system can remove more than 90% of the CO2 from NG with CCC technology using Aspen Plus simulations and experimental data. This task shows how CCC-based technology can treat NG streams to prepare them for LNG use. Data from an experimental bench-scale apparatus verify simulation results. Simulated results on carbon (CO2) capture qualitatively and quantitatively agree with experimental results as a function of feedstock properties.
机译:低温碳捕集(TM)(CCC)工艺提供了节能高效的碳捕集,可以配置为使用开环天然气(NG)制冷系统提供一种能量存储系统,称为储能低温碳捕获(CCC-ES(TM))。这项研究的重点是瞬态运行,尤其是该储能系统的动态响应,并探讨了其效率,有效性,设计和运行。这项调查包括四个任务。第一项任务是探索由Aspen HYSYS模拟的四种不同的天然气液化过程的稳态设计。这些过程与传统的LNG过程不同之处在于,CCC过程使LNG蒸发,而冷蒸汽通过LNG热交换器返回,从而与流入的气流交换显热。比较包括采用单独优化的过程的成本和能源性能,每个过程均在以下三种运行条件下运行:储能,能量回收和平衡运行。第二项任务是检查稳态和暂态模型以及使用Aspen HYSYS进行天然气液化的优化。稳态火用和热交换器效率分析表征了几种潜在系统的性能。最佳稳态模型的瞬态分析产生了此处讨论的大多数结果。第三个任务探讨了两个天然气液化过程的瞬时Aspen HYSYS建模和优化,并确定了负载变化过程中的限速过程组件。本研究中包括的新颖流量变化驱动了所有单元(尤其是压缩机和热交换器)的瞬态响应。模型预测控件(MPC)有效地管理了这些热交换器,并与使用传统控件的结果进行了比较。最后一项任务显示了使用Aspen Plus模拟和实验数据,使用CCC技术,未经处理的天然气(NG)预处理系统如何能够从NG中去除90%以上的CO2。该任务显示了基于CCC的技术如何处理NG流以准备将其用于LNG。实验台规模设备的数据验证了仿真结果。碳(CO2)捕集的模拟结果定性和定量地与实验结果一致,作为原料性能的函数。

著录项

  • 作者

    Fazlollahi, Farhad.;

  • 作者单位

    Brigham Young University.;

  • 授予单位 Brigham Young University.;
  • 学科 Chemical oceanography.;Climate change.
  • 学位 Ph.D.
  • 年度 2016
  • 页码 159 p.
  • 总页数 159
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-17 11:48:49

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