螺杆膨胀机双循环低温余热回收系统分析

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[1]曹滨斌,李惟毅.螺杆膨胀机双循环低温余热回收系统分析[J].天津大学学报(自然科学版),2010,04:309-314.
; \, ~. @6 |0 z! Z$ n, J/ p　CAO Bin-bin,LI Wei-yi.Analysis of Dual-Cycle Low-Temperature Waste Heat Recovery System with Screw Expander[J].Journal of Tianjin University,2010,04:309-314.
《天津大学学报（自然科学版）》[ISSN:0493—2137/CN:12—1127/N]期数: 2010年04 页码: 309-314 栏目: 机械工程 出版日期: 2010-04-15
1 }) O; g/ B4 I7 [# N文章信息/Info
" m) Q! F" ]- }# _1 ^; nTitle: Analysis of Dual-Cycle Low-Temperature Waste Heat Recovery System
( |( F) _4 g6 z1 Rwith Screw Expander
作者: 曹滨斌; 李惟毅
天津大学机械工程学院，天津 300072
Author(s): CAO Bin-bin; LI Wei-yi
; O& k! @! [" q( @+ n! oSchool of Mechanical Engineering, Tianjin University, Tianjin 300072,China
关键词: 螺杆膨胀机; 双循环; 低沸点工质; 余热回收
Keywords: screw expander; dual-cycle; low boiling point working fluid; waste heat recovery
分类号: TK11
% m$ w5 D/ l4 K0 Q" L" kDOI: -
文献标识码: A
摘要: 针对100.℃以下流体的余热回收，建立了采用低沸点工质的双循环螺杆膨胀机余热回收系统优化模型，根据工质在蒸发器出口的热力状态不同，对不同膨胀过程求解，并分析了影响系统性能的主要因素．结果表明：对于工质蒸发温度的选择，当可以忽略蒸发侧泵耗时，宜采用以机组效率最大为目标进行优化设计，当必须考虑蒸发侧泵耗时，宜采用以系统效率最大为目标进行优化设计；对于螺杆膨胀机膨胀比的选择，当余热温度＜100 ℃时，工质 R245fa 的最佳膨胀比为４，丁烷的最佳膨胀比为3，当余热温度＞100 ℃时，最佳膨胀比的值增大；对于循环工质的选择，应考虑单位质量做功能力强、蒸发压力低和最佳膨胀比小的有机物等．
4 B9 [, y- }0 k# b6 lAbstract: An optimizing model of dual-cycle low-temperature waste heat recovery system using screw expander was
* C$ O0 q1 i8 P" M! Pproposed in this paper. In this analysis，the working fluids were below boiling temperature，and the heat resource was waste thermal fluid below 100.℃. According to the thermal states of working fluids at the evaporator outlet，the factors affecting the system performance were analyzed through calculations in different expanding processes. The results show that as for the option of evaporate temperature，when power consumption of the pump at evaporator section can be neglected，the optimal design aims at the maximum of expander efficiency；when the power consumption can not be neglected，the optimal design aims at the maximum of the system efficiency；as for the option of expansion ratio，when waste heat source temperature is below 100.℃，the optimal expansion ratio of the working fluid R245fa is 4，that of the working fluid butane is 3；when waste heat source temperature is above 100.℃，the optimal expansion ratio increases；as for the option of working fluid，some organic matter with low evaporating pressure and low optimal expansion ratio while with strong working capability per unit mass needs to be considered to adopt. The conclusions provide references for the further engineering applications.
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