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利用Fluent内置的Mixture模型和Euler模型,对管内沸腾进行计算,条件基本一致,但模拟出的结果却相差很大,Mixture模型的管内壁换热系数在10的5次方级别,而Euler模型计算出的换热系数在10的3次方级别;有人对这方面有研究么,希望不惜赐教~~