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CO2 hydrogenation to methanol and DME

Methanol is a common feedstock considered as a building block in the chemical industry because of its versatility in the synthesis of several important chemicals such as chloromethane, acetic acid, methyl ferf-butyl ether (MTBE), alkyl halides, and formaldehyde [202, 203]. Methanol can be converted into DME which is [Pg.278]

Methanol is currently produced from Syngas as feedstock. The first industrial plant for methanol production was commissioned by BASF in 1923 using Syngas and operated at a high pressure of 20 MPa and 573 K using zinc oxide/chromium oxide catalysts [208]. [Pg.279]

Thermodynamically, a decrease in reaction temperature or an increase in reaction pressure can favor the synthesis of methanol. A reaction temperature higher than 513 K facilitates CO2 activation and, consequently, methanol formation [4,5,197]. [Pg.279]

7 Carbon Dioxide Conversion in High Temperature Reactions [Pg.280]

Conventional 2-step synthesis based on CO (i) Methanol synthesis (eq. 7.107) CO + 2H, CROH [Pg.280]


See other pages where CO2 hydrogenation to methanol and DME is mentioned: [Pg.278]   
See also in sourсe #XX -- [ Pg.278 , Pg.279 ]




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