M. Muharja, A. Widjaja, Rizki Fitria Darmayanti, B. Airlangga, R. P. Anugraha, M. Fauziyah, Eko Wijanarto, Mohammad Sholehuddin, Achri Isnan Khamil
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引用次数: 2
Abstract
Heat recovery is considered as the key to improve energy efficiency in the process design. An appropriate heat exchanger network (HEN) design is an effective tool to maximize heat recovery from the process streams and to minimize energy consumption. The objectives of this study were arranging optimum HEN based on the annual cost in the power industry. HEN in the Paiton Steam Power Plant, East Java, Indonesia, was designed using spreadsheet and Aspen Energy Analyzer with Peng-Robinson equation. Pinch analysis was conducted by comparing Tmin (10°C - 19°C) to obtain Maximum Energy Recovery (MER) and Heat Exchanger Area (HEA). The HEN design was optimized using grid diagram. Simulation in this study succeeded to reduce the annual cost the most effectively at ∆Tmin 16°C. This design optimized the process integration and contributed to the capital, operation, and total annual cost reduction of 14.3%. The maximum energy recovery was 286,706 kW and HEA 138.790 m2. This result is a solution for Steam Power Plant as an effort for enhancing energy efficiency and the company competitiveness.
在工艺设计中,热回收被认为是提高能源效率的关键。适当的热交换器网络(HEN)设计是最大限度地提高工艺流的热回收率和最大限度地降低能耗的有效工具。本研究的目的是根据电力行业的年度成本安排最佳HEN。印度尼西亚东爪哇派顿蒸汽发电厂的HEN是使用电子表格和Aspen Energy Analyzer和Peng-Robinson方程设计的。通过比较Tmin(10°C-19°C)进行夹点分析,以获得最大能量回收率(MER)和换热器面积(HEA)。使用网格图对HEN的设计进行了优化。本研究中的模拟成功地在∆Tmin 16°C下最有效地降低了年度成本。该设计优化了工艺集成,有助于资本、运营和年总成本降低14.3%。最大能量回收为286706千瓦,HEA为138.790平方米。这一结果为蒸汽发电厂提供了一个解决方案,以提高能源效率和公司竞争力。