Methanol combustion in supercritical water was systematically investigated at iso-thermal iso-baric conditions using the Eastern Michigan University Supercritical Batch Reactor. The nominal mixture was 1.5% methanol by volume with an oxygen equivalence ratio of 0.22 and a total density of 193 mg/mL; reaction times were 8–30 min with temperatures from 375° to 475 °C. The experimental observations here provide new comprehensive benchmark data for methanol oxidation near the critical point, including an evaluation of wall effects on chemical kinetics. Excellent repeatability demonstrates the effective function of the new experimental facility. The system was modeled using a custom kinetics solver and an existing chemical kinetic mechanism, wit...
A detailed chemical kinetic model (DCKM) was compiled to investigate the chemistry of the supercriti...
Phenol and methanol were oxidized in supercritical water using two isothermal plug-flow reactors to ...
Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1998.Includes...
Methanol combustion in supercritical water was systematically investigated at iso-thermal iso-baric ...
We examined the feasibility of producing methanol from the partial oxidation of methane in near-crit...
Supercritical water oxidation (SCWO) is an emerging technology for the treatment of wastes in the pr...
© 2020 Elsevier B.V. A revised detailed chemical kinetic mechanism for the combustion of methanol in...
A kinetic model for the methanol reforming in supercritical water (SCW) at 600°C and 280 bar was dev...
Hydrothermal flame is a promising solution for problems in the preheating process of supercritical w...
The chemistry of oxidation in supercritical water is being investigated for development into a pract...
The effectiveness of multistage methanol injection in supercritical water oxidation (SCWO) of an amm...
A detailed chemical kinetics model comprising 148 reversible elementory reactions for the supercriti...
The decomposition of CH3OH and C2H5OH in supercritical water was studied in a flow reactor tube (Ni/...
This paper will present results on the investigation of different chemical reactions in supercritica...
Phenol and methanol were oxidized in supercritical water using two isothermal plug-flow reactors to ...
A detailed chemical kinetic model (DCKM) was compiled to investigate the chemistry of the supercriti...
Phenol and methanol were oxidized in supercritical water using two isothermal plug-flow reactors to ...
Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1998.Includes...
Methanol combustion in supercritical water was systematically investigated at iso-thermal iso-baric ...
We examined the feasibility of producing methanol from the partial oxidation of methane in near-crit...
Supercritical water oxidation (SCWO) is an emerging technology for the treatment of wastes in the pr...
© 2020 Elsevier B.V. A revised detailed chemical kinetic mechanism for the combustion of methanol in...
A kinetic model for the methanol reforming in supercritical water (SCW) at 600°C and 280 bar was dev...
Hydrothermal flame is a promising solution for problems in the preheating process of supercritical w...
The chemistry of oxidation in supercritical water is being investigated for development into a pract...
The effectiveness of multistage methanol injection in supercritical water oxidation (SCWO) of an amm...
A detailed chemical kinetics model comprising 148 reversible elementory reactions for the supercriti...
The decomposition of CH3OH and C2H5OH in supercritical water was studied in a flow reactor tube (Ni/...
This paper will present results on the investigation of different chemical reactions in supercritica...
Phenol and methanol were oxidized in supercritical water using two isothermal plug-flow reactors to ...
A detailed chemical kinetic model (DCKM) was compiled to investigate the chemistry of the supercriti...
Phenol and methanol were oxidized in supercritical water using two isothermal plug-flow reactors to ...
Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1998.Includes...