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  2. Partial oxidation - Wikipedia

    en.wikipedia.org/wiki/Partial_oxidation

    In CPOX (catalytic partial oxidation) the use of a catalyst reduces the required temperature to around 800°C – 900°C. [citation needed] The choice of reforming technique depends on the sulfur content of the fuel being used. CPOX can be employed if the sulfur content is below 50 ppm. A higher sulfur content can poison the catalyst, so the ...

  3. Syngas - Wikipedia

    en.wikipedia.org/wiki/Syngas

    Syngas is produced by steam reforming or partial oxidation of natural gas or liquid hydrocarbons, or coal gasification. [6] C + H 2 O → CO + H 2 [1] CO + H 2 O → CO 2 + H 2 [1] C + CO 2 → 2CO [1] Steam reforming of methane is an endothermic reaction requiring 206 kJ/mol of methane: CH 4 + H 2 O → CO + 3 H 2

  4. Methane reformer - Wikipedia

    en.wikipedia.org/wiki/Methane_reformer

    A methane reformer is a device based on steam reforming, autothermal reforming or partial oxidation and is a type of chemical synthesis which can produce pure hydrogen gas from methane using a catalyst. There are multiple types of reformers in development but the most common in industry are autothermal reforming (ATR) and steam methane ...

  5. Hydrogen production - Wikipedia

    en.wikipedia.org/wiki/Hydrogen_production

    Hydrogen production from natural gas and heavier hydrocarbons is achieved by partial oxidation. A fuel-air or fuel-oxygen mixture is partially combusted, resulting in a hydrogen- and carbon monoxide-rich syngas. More hydrogen and carbon dioxide are then obtained from carbon monoxide (and water) via the water-gas shift reaction. [35]

  6. Small stationary reformer - Wikipedia

    en.wikipedia.org/wiki/Small_stationary_reformer

    A membrane reactor is a device where oxygen separation, steam reforming and POX is combined in a single step. In 1997 Argonne National Laboratory and Amoco published a paper "Ceramic membrane reactor for converting methane to syngas" [3] which resulted in different small scale systems that combined an ATR based oxygen membrane with a water-gas shift reactor and a hydrogen membrane.

  7. Catalytic reforming - Wikipedia

    en.wikipedia.org/wiki/Catalytic_reforming

    The sensitivity of catalytic reforming to contamination by sulfur and nitrogen requires hydrotreating the naphtha before it enters the reformer, adding to the cost and complexity of the process. Dehydrogenation, an important component of reforming, is a strongly endothermic reaction, and as such, requires the reactor vessel to be externally heated.

  8. Chemical looping reforming and gasification - Wikipedia

    en.wikipedia.org/wiki/Chemical_looping_reforming...

    Chemical looping systems can directly be engaged as an effective means for syngas production. Compared to the conventional partial oxidation (POX) or autothermal reforming (ATR) processes, the key advantage of the chemical looping reforming (CLR) process is the elimination of the air separation unit (ASU) for oxygen production. The gaseous fuel ...

  9. Shilov system - Wikipedia

    en.wikipedia.org/wiki/Shilov_system

    Shilov cycle The overall charge is omitted from the complexes since the exact coordination sphere of the active species is unknown.. The Shilov system is a classic example of catalytic C-H bond activation and oxidation which preferentially activates stronger C-H bonds over weaker C-H bonds for an overall partial oxidation.