Autothermal schematic representation

Figure 3.3. Schematic representation of partial oxidation (POX), autothermal reforming (ATR), and catalytic partial oxidation (CPO) reformers followed by H2 purification steps. HEX, heat exchanger.

Figure 11.4 Schematic representation of the two fluidized membrane reactor concepts for autothermal methane reforming with integrated CO2 capture (a) Methane combustion configuration (b) Hydrogen combustion configuration, after Patil et al.

Figure 3.1 Schematic representation of autothermal reforming (ATR), and reformer followed by H2 separation steps. (HEX, heat exchanger, WGS, water gas shift reactor) (Liu et al., 2010). Reprinted with permission by Wiley.

Figure 4.1 Schematic representation of two novel multifunctional fluidized bed membrane reactors for the autothermal coproduction of ultrapure H2 and pure CO2 Kuipers et al., 1992 Van Sint Annaland et al., 2006). Reprinted from Gallucci et al. (2008).

FIGURE 9-28. Schematic representation of an autothermal reforming process. 

FIGURE 13.51 Schematic representation of an autothermal membrane reactor. (Reprinted from Int. J Hydrogen Energy, 35, S. Tosti, Overview of Pd-based membranes for producing pure hydrogen and state of art at ENEA laboratories, 12650-12659, Copyright 2010, with permission from Elsevier.)... 

---

See also in sourсe #XX -- [ ]

---