Production control, hydrogen

Methods for the large-scale production of hydrogen must be evaluated in the context of environmental impact and cost. Synthesis gas generation is the principal area requiring environmental controls common to all syngas-based processes. The nature of the controls depends on the feedstock and method of processing. 

Controlled hydrogenation over Ni or the electrochemical reduction of o -nitrobenzo itriles produced 3-amino-2,l-benzisoxazoles either as the major product or by-product, depending in part on the reaction media and ratio of reactants (72BSF2365, 65CB1562). Reduction of o-nitrobenzonitrile gave either 3-amino-2,l-benzisoxazole or 2-aminobenzonitrile. The benzisoxazole is presumed to arise via an intermediate hydroxylamine. The electrochemical reduction of o-nitrobenzonitrile at acid pH produced the hydroxylamine as the primary product. Reduction at neutral pH gave the amino-2,1-benzisoxazole and the hydroxylamine (72BSF2365). 

In the feed preparation section, those materials are removed from the reactor feed which would either poison the catalyst or which would give rise to compounds detrimental to product quality. Hydrogen sulfide is removed in the DBA tower, and mercaptans are taken out in the caustic wash. The water wash removes traces of caustic and DBA, both of which are serious catalyst poisons. Also, the water wash is used to control the water content of the reactor feed (which has to be kept at a predetermined level to keep the polymerization catalyst properly hydrated) and remove NH3, which would poison the catalyst. Diolefins and oxygen should also be kept out of poly feed for good operation. 

Fluid catalytic cracking units present formidable emission control problems. Contaminants are present in both reactor product gas and regenerator flue gas. The reactor product contains hydrogen sulfide, ammonia, and cyanides, plus combined sulfur and nitrogen in the liquid products. Hydrogen sulfide, ammonia and cyanides are handled as part of the overall refinery waste water cleanup. The combined sulfur and nitrogen may be removed by hydrotreating. 

B. Precipitation and separation of hydroxides at controlled hydrogen ion concentration or pH. The underlying theory is very similar to that just given for sulphides. Precipitation will depend largely upon the solubility product of the metallic hydroxide and the hydroxide ion concentration, or since pH + pOH = pKw (Section 2.16), upon the hydrogen ion concentration of the solution. 

Reactor product gases were effectively treated in the two-stage scrubber system and product gas burner. However, Eco Logic concluded that process modifications might be necessary to control hydrogen sulfide and phosphine in the offgas from the reactor. Also, the liner in the product gas burner showed evidence of corrosion. 

The Reduction of the " Half-Hydrogenated State" is Product Controlling... 

The Adsorption of the Alkene is Product Controlling At high pressures of hydrogen, it is probable that and... 

The reduction of a-hydroxy ketones 43 to 1,2-diols 44 was achieved in good yield and high diastereoselectivity in favour of the anti product by using ClsSiH and photolytic conditions [56]. In the proposed mechanism of Scheme 5.8, the addition proceeded via the intermediate adduct 45, which participated in the stereo-controlled hydrogen donation, and via the a-silylether 46, affording 1,2-diols in a preferential anti conformation. 

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