Coal gasification
and coking to methanol (GCtM) is a newly developed
and industrialized process in China. However, in the early stages,
the idea of integration hardly applied to this process. To improve
the degree of integration, this paper developed a coupling process
of coproducing methanol and ethylene glycol. The key idea was to find
an appropriate distribution of carbon and hydrogen components for
maximal resource utilization. The new process introduced additional
hydrogen and carbon sinks by adding a new ethylene glycol synthesis
unit. It separated excessive H2 or CO from different syngas
streams depending on their composition. This brought more hydrogen
and carbon sources. The new process conducted integration by matching
sinks and sources. A detailed process modeling and simulation were
conducted in Aspen Plus. The simulation results were verified with
reference and industrial data. The techno-economic performance was
analyzed and compared with the conventional process to find the advantages
of the new process. The results showed that the new process had a
much higher carbon utilization efficiency of 54% than that of the
GCtM process, 40%. The total greenhouse gas emissions of the new process
are 1.58 t CO2 equiv t–1, which is 26.2%
lower than that of the GCtM. It was also found that the exergy efficiency
was improved from 56.7% to 68.1%. As for economic benefits, the new
process decreased total product cost by 35.2% and increased internal
rate of return by 4.5%.