Experiment and simulation of distillation process for dimethyl ether refining
|更新时间:2025-12-10
|
Experiment and simulation of distillation process for dimethyl ether refining
CIESC JournalIssue 5, Pages: 1184-1189(2008)
作者机构:
华东理工大学化学工程联合国家重点实验室,大型工业反应器工程教育部工程研究中心
作者简介:
基金信息:
DOI:
CLC:
Online First:05 May 2008,
Published:05 May 2008
稿件说明:
移动端阅览
HAN Yuanyuan, ZHANG Haitao, YING Weiyong, et al. Experiment and simulation of distillation process for dimethyl ether refining[J]. CIESC Journal, 2008, (5): 1184-1189.
DOI:
HAN Yuanyuan, ZHANG Haitao, YING Weiyong, et al. Experiment and simulation of distillation process for dimethyl ether refining[J]. CIESC Journal, 2008, (5): 1184-1189.DOI:
Experiment and simulation of distillation process for dimethyl ether refining
The distillation process is used for purifying dimethyl ether (DME)
when one-step synthesis of DME from syngas is adopted.Experimental flow of distillation for DME refining was built and the results were measured under operation conditions.A mathematical model was presented to research the distillation process on the basis of equilibrium stage theory.The cyclical nested-iteration method in sequential convergence was developed for solving the model equations
since the liquid phase was non-ideal and the components had a big difference in boiling point under normal conditions.The model yielded satisfactory results for laboratory data and the simulation results showed that for distillate DME product with concentration no less than 99%(mole)
the following operating conditions were recommended.The distillation process is at operating pressure 1.0 MPa
and the feed mass flow rate of less than 8.65 mol·m-2·s-1 is desirable.The distillation mixture is fed into the middle of the packing section and the reflux ratio is rigorously controlled in a certain range according to the DME concentration in feed.It is necessary to keep CO2 concentration in feed as low as possible in order to improve DME purity and yield.
Simulation of process for butanone-toluene solvent recovering in dewaxing of complex oil and/or wax mixtures replaced by a pseudo-single heavy component
Process simulation of methyl acetate hydrolysis via catalytic distillation
Numerical simulation on performances of rough-cut cyclone in FCC disengager
From multi-scale to meso-scale:new challenges for simulation of complex processes in chemical engineering