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Process/catalyst development inventory

Aluminum Chloride-Based Alkylation. An improved aluminum chloride-based process was developed by Monsanto in the 1970s. Using a presynthesized aluminum chloride complex and operating the reactor at higher temperature and pressure, the catalyst inventory is reduced to below its solubility in the reaction mixture. The reactants and the catalyst complex are mixed in the reactor to form a homogeneous liquid. The transalkylation... [Pg.1555]

Basic process chemistry using less hazardous materials and chemical reactions offers the greatest potential for improving inherent safety in the chemical industry. Alternate chemistry may use less hazardous raw material or intermediates, reduced inventories of hazardous materials, or less severe processing conditions. Identification of catalysts to enhance reaction selectivity or to allow desired reactions to be carried out at a lower temperature or pressure is often a key to development of inherently safer chemical synthesis routes. Some specific examples of innovations in process chemistry which result in inherently safer processes include ... [Pg.36]

Over time the operating efficiency of hydrofluoric acid alkylation units has improved in order to minimize waste streams as well as minimize the actual hydrofluoric acid inventory. However, the only way to eliminate these issues completely is to develop a process based on a heterogeneous acid catalyst. Such a process would eliminate the hydrofluoric acid transportation and inventory, result in no waste polymer product, and would not require fluoride scrubbing and concomitant disposal of fluoride-containing solids. [Pg.440]

Technologically, the Alkylene process is a break-through. Several significant inventions were required to make it technically feasible. The development of a unique solid-acid catalyst and transport reactor by UOP allows for the potential elimination of hazardous liquid acid processes. About 1 MM gallons of hydrofluoric acid inventory could be eliminated, transport of 33 MM lbs (4 MM gallons) of hydrofluoric acid per year would be stopped, and ca. 20 MM lbs per year of other fluoride containing solids would not have to be land filled. [Pg.440]


See other pages where Process/catalyst development inventory is mentioned: [Pg.480]    [Pg.480]    [Pg.480]    [Pg.2423]    [Pg.72]    [Pg.97]    [Pg.94]    [Pg.281]    [Pg.413]    [Pg.226]    [Pg.21]    [Pg.9]    [Pg.137]    [Pg.72]    [Pg.97]   
See also in sourсe #XX -- [ Pg.173 , Pg.177 , Pg.178 , Pg.197 , Pg.198 , Pg.203 ]




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Process/catalyst development

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