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  2. Methanol economy - Wikipedia

    en.wikipedia.org/wiki/Methanol_economy

    Efficiency for methanol synthesis of hydrogen and carbon dioxide currently is 79 to 80%. [19] Thus the efficiency for production of methanol from electricity and carbon dioxide is about 59 to 78%. If CO 2 is not directly available but is obtained by direct air capture then the efficiency amounts to 50-60 % for methanol production by use of ...

  3. CO2SYS - Wikipedia

    en.wikipedia.org/wiki/CO2SYS

    CO2SYS is a family of software programs that calculate chemical equilibria for aquatic inorganic carbon species and parameters. Their core function is to use any two of the four central inorganic carbon system parameters (pH, alkalinity, dissolved inorganic carbon, and partial pressure of carbon dioxide) to calculate various chemical properties of the system.

  4. Methanol reformer - Wikipedia

    en.wikipedia.org/wiki/Methanol_reformer

    A mixture of water and methanol with a molar concentration ratio (water:methanol) of 1.0 - 1.5 is pressurized to approximately 20 bar, vaporized and heated to a temperature of 250 - 360 °C. The hydrogen that is created is separated through the use of Pressure swing adsorption or a hydrogen-permeable membrane made of polymer or a palladium alloy.

  5. Methane reformer - Wikipedia

    en.wikipedia.org/wiki/Methane_reformer

    The reaction is exothermic due to the oxidation. When the ATR uses carbon dioxide the H 2:CO ratio produced is 1:1; when the ATR uses steam the H 2:CO ratio produced is 2.5:1 The reactions can be described in the following equations, using CO 2: 2 CH 4 + O 2 + CO 2 → 3 H 2 + 3 CO + H 2 O. And using steam: 4 CH 4 + O 2 + 2 H 2 O → 10 H 2 + 4 CO

  6. Electrochemical reduction of carbon dioxide - Wikipedia

    en.wikipedia.org/wiki/Electrochemical_reduction...

    The electrochemical reduction of carbon dioxide, also known as CO2RR, is the conversion of carbon dioxide (CO 2) to more reduced chemical species using electrical energy. It represents one potential step in the broad scheme of carbon capture and utilization .

  7. Non-random two-liquid model - Wikipedia

    en.wikipedia.org/wiki/Non-random_two-liquid_model

    VLE of the mixture of chloroform and methanol plus NRTL fit and extrapolation to different pressures. The non-random two-liquid model [1] (abbreviated NRTL model) is an activity coefficient model introduced by Renon and Prausnitz in 1968 that correlates the activity coefficients of a compound with its mole fractions in the liquid phase concerned.

  8. Alcohol fuel - Wikipedia

    en.wikipedia.org/wiki/Alcohol_fuel

    Methanol is a possible biofuel, however, when the syngas is derived from biomass. In theory, methanol can also be produced from sustainably sourced biomass and ultimately carbon dioxide, and by hydrogen electrolysis using nuclear power, geothermal power or some other renewable energy source (see Carbon Recycling International). Compared to ...

  9. Supercritical fluid extraction - Wikipedia

    en.wikipedia.org/wiki/Supercritical_fluid_extraction

    Carbon dioxide (CO 2) is the most used supercritical fluid, sometimes modified by co-solvents such as ethanol or methanol. Extraction conditions for supercritical carbon dioxide are above the critical temperature of 31 °C and critical pressure of 74 bar. Addition of modifiers may slightly alter this.