16 Sq Ft Vicarb Block Type Heat Exchanger

Complete GTL (Gas-To-Liquid) Plant for Operation in Place – Louisiana, USA Units available include SMR/Syngas, Fischer Tropsch Reactors, and Wax Upgrade Plants Gas-to-Liquids Facility – FT Wax – 1100 BPD with Property – Phoenix Plant # 530 Built in 2015, and never operated. Previous owners invested over $400 million in the plant. Originally designed to be the first commercial scale Fischer-Tropsch (“FT”) plant in North America, to convert cost advantaged and environmentally cleaner US natural gas into high quality FT waxes to address a structural supply shortage in the North American wax market (FT wax is a drop-in substitute for most applications with superior characteristics). Facility includes Syngas Plant, FT Reactors and Wax Upgrade Unit – can be operated together or available for individual operation in place. Site Highlights: 10.5 acres, easy access to highway and rail transportation. Access to natural gas pipeline and hydrogen.

Falling feedstock prices, greater efficiency, and an increased worldwide demand as more economies emerge all present lucrative opportunities for the conversion of natural gas to liquid synthetic crude oil. That’s because much of the world’s natural gas – up to one-third by many estimates – are located in remote deposits. Liquefaction of natural gas makes it more economical to transport via tanker or pipeline and to store for future refinement and use. Small, onsite gas-to-liquid (GTL) plants will make tapping these “stranded gas” deposits profitable. Natural gas has proven the best feedstock for creating crude oil alternatives through the industry standard Fischer-Tropsch process, topping coal in purity, handling, and ease in conversion to syngas, which is required for efficient conversion to synthetic crude. GTL Plant Benefits The synthetic oil GTL plants produce is virtually interchangeable with conventional oil, both as refined transport

In this article, we will show that a steam methane reformer (SMR) is critical in the production processes of hydrogen, ammonia, and methanol; as all three use the raw syngas produced by an SMR upstream in their synthesis. Syngas Production In what is called steam methane reforming, high-temperature steam (700°C–1,000°C) is used to produce raw syngas from a methane source, typically natural gas. Using a steam methane reformer (SMR), methane reacts with steam under 3–25 bar of pressure in the presence of a catalyst to produce hydrogen, carbon monoxide, and a relatively small amount of carbon dioxide. The resulting gas mixture is called synthesis gas, or syngas for short; and is the raw ingredient in hydrogen production, ammonia synthesis, and methanol synthesis. Hydrogen Production Subsequently, in what is called the "water-gas shift reaction," raw syngas and steam are reacted using a catalyst to produce carbon dioxide and more hydrogen. In