WebTOPSOE™’s SynCOR™ autothermal reforming technology (previously called ATR) is often the preferred technology in many of today’s world-scale projects because it enhances economy of scale by maximizing single-line capacity while significantly reducing capital and operating costs. Web28. aug 2014 · The dry methane reforming reaction is favored by low pressure, but high pressure synthesis gas is required in the downstream process. Higher reactor pressures reduce compression costs of the synthesis gas. However, higher pressures also require a higher reactor temperature to achieve high methane conversion.
SynCOR™ - Autothermal Reformer (ATR) Equipment - Topsoe
WebAnother type of steam-reforming reactor that is attracting increasing attention is known as gas heated reformers or heat exchange reformers. In such reformers, heat is transferred … Web19. júl 2012 · The industrial secondary reformer reactor plays an important role in the ammonia plant. The aim of the secondary reformer reactor is to produce and adjust the amount of hydrogen and nitrogen gases. A schematic diagram of the industrial-scale secondary reformer reactor is shown in Figure 1. romy victory photo
Heat Exchange Reforming - Global Syngas Technologies Council
WebHydrogen is produced by primary and secondary steam methane reforming reactors (SMR), followed by a two stage water–gas shift reactor, CO 2 removal and methanation. The first SMR reactor operates in allothermal conditions at around 850–900 °C and 25–35 bar and the energy required for the endothermic reaction is provided by external ... Web4. jún 2012 · The fuel processing unit includes a reformer (integrated with steam generation), two high and low temperature shift reactors, and a preferential oxidation reactor. The reformer integrated with steam generation is designed to produce hydrogen-rich syngas from natural gas and water. It can be operated under steam methane … Webreformer on pre-reformed gas – methanol: mixture of pre-reformed gas and natural gas “mild” conditions by: – high steam ratio – H2 at inlet ⇒low risk of soot formation Idea: use ATR as only reforming reactor, delete costly tubular primary reformer. Risk: soot formation in ATR with no pre-reformed gas romy vroman twitter