|
|||||||
![]() ![]() ![]() ![]() ![]() |
|||||||
![]() |
The GTL alternative energy market has significant need for fine particle filters (self cleaning and disposable), liquid/gas and liquid/liquid coalescers, and gas/gas separation membranes. GTL production units will range in size from 1000 bpd to 150,000 bpd of liquid fuels and chemical feedstocks, all having unique chemistries based on the source of the feed hydrocarbon gas, the plant location, and the GTL/BTL (biomass to liquid)/CTL (Coal to liquid) developer’s technology. Pall, as a total solution provider, can provide researchers needed technical assistance throughout the process demonstration phase to commercial scale production, to assure optimum selection of critical separation devices. Fischer Tropsch technology, the heart of the conversion process, is a 74-year-old process that had previously been limited to a few large scale commercial demonstrations. The process creates liquid fuel from syngas, either gasified from hydrocarbon sources or natural gas, but not crude oil. It has allowed South Africa to reduce their dependency on foreign crude after WWII. The global rebirth in GTL motor fuels is motivated by:
All GTL projects are scalable, allowing design optimization and application to smaller stranded gas deposits. The key influences on the competitiveness of each process are the cost of capital, operating costs of the plant, feedstock costs, scale, and ability to achieve high utilization rates in production. The first stage syngas step converts the natural gas to hydrogen and carbon monoxide by partial oxidation, steam reforming, or a combination of the two processes. Here, Pall has a long history of involvement with hot gas filtration. The heart of the GTL process is the Fischer Tropsch Reactor which can be a fixed bed or fluidized. FT reactors contain large volumes of iron or cobalt based catalyst composition. The fine sized catalyst can breakdown with time, and becomes deactivated if removed too far away from the reactor environment, making internal separations for the large flow applications more preferable, and less complex. The reformed syngas is sparged into the main GTL reactor(s) with up to 40%(wt) catalyst content. Internal separation mechanisms reduce the catalyst solids below 1-5 % wt. before the wax liquid products are drawn away. Pall's focus has been on effectively separating the fine size FT catalyst yielding a low TSS wax product. Cleanable filters in the reactor, and/or cross flow membranes outside the reactor on a product circuit, offer significant application for Pall products. The last stage of processing is hydrocracking, where hot liquid wax product is separated from the produced water and feed into fixed bed hydrocrackers where liquid fractions are produced, for various fuel and chemical feedstock uses. The hydrocracker catalyst must be protected from poisons and suspended solids to assure long on stream runtime. Pall filter/separator technologies are currently being demonstrated in all three phases of the GTL process. Read below for a sampling of our solutions by application. We're working hard to become the world’s foremost supplier of filtration and separation solutions to the GTL industry. We envision Pall will provide producers with not only the complete separation systems and the technical services to go with them, but also filter cartridges, supports, and porous substrates for various aspects of the GTL processes. Applications
Catalyst Separations - AccuSep® Inorganic Membranes - Membralox® Ceramic Membrane Products - Metal High Flow Filters - PSS® Filter Elements - Rigimesh® Filter Elements - ZHF Centrifugal Discharge Filter System Gasification Natural or Syngas Treatments Product Water Treatment Rotating Equipment Protection Spargers Total Fluid Management *Microza is a registered trademark of Asahi Kasei Corporation. Top |
||||||