炭催化CH4-CO2重整反应系统压降分析与优化

ANALYSIS AND OPTIMIZATION OF PRESSURE LOSS IN THE SYSTEM OF CH_4-CO_2 REFORMING WITH CARBONACEOUS CATALYST

基于重整反应系统的设备和管道尺寸、空间布置和设计运行参数等基础数据，研究并建立了主要设备、管道摩擦阻力和局部阻力计算模型，采用该模型分析了系统内各设备、管道和管道元件的压降，并对压降较大的设备和管道进行了尺寸优化．研究和优化结果表明，重整反应系统中，氧气缓冲罐、加热炉、氧气管道OG101～OG104等设备压降较大．对设备和管道的尺寸进行优化后，系统总压降由8260．6Pa降低到3289．9Pa；当系统入口压强P1=40MPa时，系统出口压强P2=0．0367MPa．

Based on space arrangement, size and running parameters of equipments and pipes in CH4-CO2 reforming with carbonaceous catalyst, this paper estatmsnes calculation of frictional resistance and local resistance, analyzes pressure loss of equipments and pipes by model, and optimizes the size of some equipments and pipes. The result shows that O2 accumulator tank, reheating furnace and O2 pipes have much pressure loss. After optimization, total pressure loss of system reduced from 8 260.6 Pa to 3 289.9 Pa. When entrance pressure is 40 MPa, exit pressure was 0. 036 7 MPa.