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Shell and tube heat exchanger progression fouling and its mitigation using chemical cleaning process

机译:壳牌和管换热器进展污垢及其使用化学清洗过程缓解

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The heat exchanger calcium sulphate fouling in tube side is the deposition on the tube surfaces which affect the heat transfer. It's found that the oil refinery process plant having an issue of calcium sulphate fouling in heat exchangers due to the crude product which form by hydrous calcium with Sulphur trioxide developed calcium sulphate deposit. The crystalline form of aqueous solution in three forms: gypsum (CaSO_4·2H_2O), hemihydrate (CaSO_4·1/2H_2O), and anhydrate (CaSO_4), which is created by reacting Sulphur trioxide with calcium oxide in the presence of moisture in hydrous form (i.e. CaO+SO_3+2H_2O=CaSO_4·2H_2O and CaO+SO_3→CaSO_4) form. Calcium sulfate deposits as a crystalline mass which adheres tenaciously to the metal surface, builds up and tends to undesirably reduce the heat transfer characteristics as well as causes plugging. The heat exchanger fouling removal are difficult which is not remove by any normal online cleaning and flushing. The objective of this work is to provide essential understanding of calcium base fouling removal techniques by EDTA chemical cleaning methodology. The mechanical cleaning, needs major shutdown, bundle pulling and retro-jetting which associated with huge cost and additional integrity test. The results of an experimental study on fouling phenomena, environment of fouling, and mitigation of fouling in shell and tube heat exchanger have been clearly explained.
机译:管侧的热交换器硫酸钙污垢是在管表面上的沉积,其影响传热。目前发现,由于硫酸钙,具有硫酸钙沉积物,炼油厂工艺植物在热交换器中具有硫酸钙污垢,其具有含硫钙的硫酸钙。三种形式的水溶液的结晶形式:石膏(CasO_4·2H_2O),半水合物(CasO_4·1 / 2H_2O)和无水酸酐(CasO_4),其通过使三氧化硫与氧化钙在含水形式的水分存在下而产生(即CAO + SO_3 + 2H_2O = CASO_4·2H_2O和CAO + SO_3→CASO_4)表单。硫酸钙沉积物作为粗加工粘附在金属表面上的结晶物质,并倾向于不希望地降低传热特性以及导致堵塞。热交换器结垢去除难以通过任何正常的在线清洁和冲洗未去除。这项工作的目的是通过EDTA化学清洁方法提供对钙基污垢去除技术的基本理解。机械清洁,需要重大关机,捆绑拉动和复古喷射,与巨大的成本和额外的完整性测试相关。已经清楚地解释了对污垢现象,污垢环境的实验研究的结果,并在壳管和管热交换器中污染的缓解。

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