中国电力 ›› 2020, Vol. 53 ›› Issue (7): 184-188,196.DOI: 10.11930/j.issn.1004-9649.201910135

• 燃煤机组水分回收及处理关键技术专栏 • 上一篇    下一篇

燃煤电厂脱硫废水热法零排放技术热成本分析

赵舒然1,2, 韩小渠2, 张丹2, 刘继平1   

  1. 1. 西安交通大学 热流教育部重点实验室,陕西 西安 710049;
    2. 西安交通大学 动力工程多相流国家重点实验室,陕西 西安 710049
  • 收稿日期:2019-10-20 修回日期:2020-03-05 发布日期:2020-07-05
  • 作者简介:赵舒然(1995—),男,硕士研究生,从事热力系统经济性诊断理论、汽液两相流理论研究,E-mail: 1346587682@qq.com;刘继平(1971—),男,通信作者,教授,博导,从事热力系统经济性诊断理论、汽液两相流理论和热声理论研究,E-mail: liujp@mail.xjtu.edu.cn
  • 基金资助:
    国家重点研发计划资助项目(2018YFB0604303);国家自然科学基金资助项目(51806159)

Thermal Cost Analysis on Thermal Zero Discharge Technology for Flue Gas Desulfurization (FGD) Wastewater of Coal-Fired Units

ZHAO Shuran1,2, HAN Xiaoqu2, ZHANG Dan2, LIU Jiping1   

  1. 1. MOE Key Laboratory of Thermal Fluid Science and Engineering, Xi'an Jiaotong University, Xi'an 710049, China;
    2. State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China
  • Received:2019-10-20 Revised:2020-03-05 Published:2020-07-05
  • Supported by:
    This work is supported by the National Key Research and Development Program of China (No.2018YFB0604303) and National Natural Science Foundation of China (No.51806159)

摘要: 采用不同热源驱动多效蒸馏(MED)或多级闪蒸(MSF)系统,对燃煤电厂湿法脱硫工艺废水进行处理,有望实现废水的低成本零排放。针对“预处理—浓缩—蒸发脱盐”工艺中已经过预处理的脱硫废水,提出5种不同的集成方案以实现“浓缩—深度脱盐”。分别建立了各方案的热经济性分析模型,定量研究了造水比和热成本的变化规律。结果表明:从热源角度分析,厂用汽热源成本较高,烟气成本低廉而泵功成为主要成本;从提浓与脱盐工艺角度,采用MED-TVC(multi-effect distillation-thermal vapor compressor)方案可提高造水比10%~100%,降低热成本10%~50%,但是降膜蒸发结构的MED对废水盐浓度的波动比较敏感,且不适合处理高浓度废水,强制循环蒸发结构可改善该问题;MSF工艺对盐浓度具有更强的适应性,采用烟气供热的成本为0.3~1.2元/t。

关键词: 脱硫废水, 零排放, MED, MSF, 热成本, 经济性

Abstract: It is expected to achieve low-cost zero discharge of FGD wastewater by using MED or MSF technology driven by different heat sources of the power plant. In this paper, five different combinations of schemes are proposed for the desulfurization wastewater pretreated in the “pretreatment-concentration-evaporation desalination” process to achieve the target of "concentration-deep desalination". The thermal economic analysis model of each scheme was established respectively, and the change rules of gained output ratio (GOR) and heat cost was also quantitatively studied. The results show that as far as the heat source is concerned, the cost of auxiliary steam is higher, while the cost using the waste heat of the flue gas is cheaper with the pumping power becoming the major cost contributor. With the TVC device installed, the GOR of MED can be improved by 10%~100%, and the heat cost can be reduced by about 10%~50%. However, in addition to its high sensitivity to fluctuations in wastewater salt concentration, the structure of the MED structure is not suitable for treating high salt concentration wastewater. In contrast, the MSF structure demonstrates high adaptability to salt concentration. The heating cost of using flue gas heating is about 0.3~1.2 yuan/t.

Key words: desulfurization wastewater, zero discharge, MED, MSF, thermal cost, economic deposition