热泵精馏分离D2O/H2O工艺过程节能分析

    Energy Saving Analysis of Heat Pump Distillation Separation Process of D2O/H2O

    • 摘要: D2O作为重水堆中的减速剂和冷却剂,广泛应用于核研究领域。采用水精馏工艺提浓D2O时,由于氘与氢的性质相近,需要较大的回流比(50~200),导致精馏塔能量消耗量(简称能耗)较高。本研究首先分析了D2O和H2O混合物分离体系的特点,通过ASPEN软件建立D2O提浓精馏工艺流程,并对其操作参数如塔板数、进料位置、回流比进行优化。模拟结果表明:常规精馏能耗较高,采用热泵精馏技术可以有效降低精馏系统的能耗,提出了一种用于D2O提浓的热泵精馏新工艺。通过分析热泵精馏的原理以及适用范围,对新工艺运行参数进行了优化设计,确定了循环工质流速为323.66 kg/h、压缩机压缩比为3.3的操作条件,以满足分离要求并降低能耗。通过对比常规精馏与热泵精馏的热力学参数和能耗分析,结果表明:热泵精馏在D2O提浓工艺中具有良好的应用前景,综合能耗比常规精馏降低了61.28%,节能效益达到66.66%。

       

      Abstract: D2O is widely used in nuclear research as a moderator and coolant in nuclear reactors. When using water distillation process to concentrate D2O, due to the similar properties of deuterium and hydrogen, a larger reflux ratio(50-200) is required, resulting in high energy consumption of the distillation tower. In this study, the characteristics of the mixture separation system of D2O and H2O were firstly analyzed, and the distillation process of D2O concentration was established by ASPEN software. Its operating parameters such as the number of tower plates, feed position, and reflux ratio were optimized. The simulation results show high energy consumption in conventional distillation. The use of heat pump distillation technology can effectively reduce the energy consumption of the distillation system. This paper proposes a new heat pump distillation process for D2O concentration. By analyzing the principle and applicable scope of heat pump distillation, the operating parameters of the new process were optimized and the operating conditions of the circulating working fluid flow rate of 323.66 kg/h and the compressor compression ratio of 3.3 were determined to meet the separation requirements and reduce energy consumption. By comparing the thermodynamic parameters and energy consumption analysis of conventional distillation and heat pump distillation, the results show that the heat pump distillation has good application prospect in the D2O concentration process. The comprehensive energy consumption than conventional distillation reduces by 61.28%, energy saving benefit of 66.66%.

       

    /

    返回文章
    返回