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Optimal Design and Operation of Heat Exchanger Network

机译:换热器网络的优化设计与运行

摘要

Heat exchanger networks (HENs) are the backbone of heat integration due totheir ability in energy and environmental managements. This thesis deals withtwo issues on HENs. The first concerns with designing of economically optimalHeat exchanger network (HEN) whereas the second focus on optimal operationof HEN in the presence of uncertainties and disturbances within the network. Inthe first issue, a pinch technology based optimal HEN design is firstlyimplemented on a 3–streams heat recovery case study to design a simple HENand then, a more complex HEN is designed for a coal-fired power plant retrofittedwith CO2 capture unit to achieve the objectives of minimising energy penalty onthe power plant due to its integration with the CO2 capture plant. The benchmarkin this case study is a stream data from (Khalilpour and Abbas, 2011).Improvement to their work includes: (1) the use of economic data to evaluateachievable trade-offs between energy, capital and utility cost for determination ofminimum temperature difference; (2) redesigning of the HEN based on the newminimum temperature difference and (3) its comparison with the base casedesign. The results shows that the energy burden imposed on the power plantwith CO2 capture is significantly reduced through HEN leading to utility costsaving maximisation. The cost of addition of HEN is recoverable within a shortpayback period of about 2.8 years. In the second issue, optimal HEN operationconsidering range of uncertainties and disturbances in flowrates and inlet streamtemperatures while minimizing utility consumption at constant targettemperatures based on self-optimizing control (SOC) strategy. The new SOCmethod developed in this thesis is a data-driven SOC method which uses processdata collected overtime during plant operation to select control variables (CVs).This is in contrast to the existing SOC strategies in which the CV selectionrequires process model to be linearized for nonlinear processes which leads tounaccounted losses due to linearization errors. The new approach selects CVsin which the necessary condition of optimality (NCO) is directly approximated bythe CV through a single regression step. This work was inspired by Ye et al.,(2013) regression based globally optimal CV selection with no model linearizationand Ye et al., (2012) two steps regression based data-driven CV selection but with poor optimal results due to regression errors in the two steps procedures.The advantage of this work is that it doesn’t require evaluation of derivativeshence CVs can be evaluated even with commercial simulators such as HYSYSand UNISIM from among others. The effectiveness of the proposed method isagain applied to the 3-streams HEN case study and also the HEN for coal-firedpower plant with CO2 capture unit. The case studies show that the proposedmethodology provides better optimal operation under uncertainties whencompared to the existing model-based SOC techniques.
机译:热交换器网络(HENs)由于其在能源和环境管理方面的能力而成为热集成的基础。本文涉及有关HENs的两个问题。第一个与经济上最佳的换热器网络(HEN)的设计有关,而第二个则关注在网络内部存在不确定性和干扰的情况下HEN的最佳运行。在第一个问题中,首先在三流热回收案例研究中实施了基于捏技术的最佳HEN设计,以设计一个简单的HEN,然后为装有CO2捕集单元的燃煤电厂设计了一个更复杂的HEN,以实现目标由于将其与CO2捕集装置集成在一起,可最大程度地减少发电厂的能源损失。本案例研究的基准是来自(Khalilpour和Abbas,2011)的流数据。对其工作的改进包括:(1)利用经济数据评估能源,资本和公用事业成本之间的可取取舍,以确定最小温差; (2)根据新的最小温差重新设计HEN,以及(3)与基本案例设计进行比较。结果表明,通过HEN可以显着减少带有CO2捕集的电厂的能源负担,从而最大程度地节省公用事业成本。添加HEN的成本可在约2.8年的短期内收回。在第二个问题中,基于自优化控制(SOC)策略,最佳HEN运行考虑了流量和入口流温度的不确定性和干扰范围,同时在恒定目标温度下将公用事业消耗降至最低。本文开发的新SOC方法是一种数据驱动的SOC方法,该方法使用工厂运行过程中超时收集的过程数据来选择控制变量(CV),这与现有SOC策略相反,在现有的SOC策略中,CV选择需要对过程模型进行线性化处理非线性过程,由于线性化误差导致无法估计的损失。新方法选择了CVsin,其中最优必要条件(NCO)由CV通过单个回归步骤直接近似。这项工作是受到Ye等人(2013年)基于回归的全局最优CV选择(没有模型线性化)和Ye等人(2012年)的两步基于数据驱动的CV选择的回归启发,但由于回归误差导致最优结果较差这两个步骤的过程。这项工作的优点在于它不需要评估衍生工具,因此即使使用商用模拟器(例如HYSYS和UNISIM等)也可以评估CV。所提出的方法的有效性再次应用于3股HEN案例研究以及具有CO2捕集单元的燃煤电厂的HEN。案例研究表明,与现有的基于模型的SOC技术相比,所提出的方法在不确定性下提供了更好的最优操作。

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    Salihu Adamu Girei;

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  • 年度 2015
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