Catalytic converter purification

Unavoidable loss of gas is compensated via a feed valve for supplying virgin nitrogen into the circulation pipe. The exhaust gas of the process has to be bypassed for purification. After the separation of dust by a filter, the gas is heated to 400 °C for the catalytic combustion of the side products. The gas is then cooled down, and the excess oxygen is catalytically converted to water by using hydrogen. For economic reasons, the gas flow will recover the heat via a heat exchanger and then be cooled down by a gas cooler. 

Reduction of nitric oxide by carbon monoxide is one of the reactions occurring in catalytic converters for the purification of the engine exhaust gases [489] ... 

The synthesis gas, after the customary shift conversion and purification, is delivered at synthesis gas specifications to the compressors for the methanol synthesis loop. This operates as a series of catalytic converters, which have advantages over the systems used conventionally both as to the fiow arrangement and catalyst used in the Wentworth process. Sulfur is removed in the elemental form but the crude methyl fuel retains the higher alcohols and other impurities produced in small amounts (2-3%). They contribute to its value as a fuel. 

The partial oxidation delivers the energy for the steam splitting. The resulting synthesis gas with a typical composition of 46 % H2, 46 % CO, 6 % CO2, 1 % CH4, 1 % N2 + At at 6 MPa can be either used for methanol synthesis or is further catalytically converted to increase the H2 yield. Purification is done in several steps. Maximum unit capacity is in the order of 80,000 Nm /h of H2 [55]. 

Favor catalytic conversion when impurities can be converted into desired product further purification and/or separation steps may be uimecessary. 

Intermediate 37 can be transformed into ( )-thienamycin [( )-1)] through a sequence of reactions nearly identical to that presented in Scheme 3 (see 22— 1). Thus, exposure of /(-keto ester 37 to tosyl azide and triethylamine results in the facile formation of pure, crystalline diazo keto ester 4 in 65 % yield from 36 (see Scheme 5). Rhodium(n) acetate catalyzed decomposition of 4, followed by intramolecular insertion of the resultant carbene 3 into the proximal N-H bond, affords [3.2.0] bicyclic keto ester 2. Without purification, 2 is converted into enol phosphate 42 and thence into vinyl sulfide 23 (76% yield from 4).18 Finally, catalytic hydrogenation of 23 proceeds smoothly (90%) to afford ( )-thienamycin... 

It was interesting that the cell-free extract had the capacity to support the biosynthesis all the way to FAc 1, an end product of one of the fluorometabolite pathways. This observation indicates that all of the enzymes and cofactors required to support FAc biosynthesis were present and active in the cell-free extract, even though the integrity of the cells had been destroyed. This experiment showed that organic fluoride production was achievable in vitro from the S. cattleya protein extract. Subsequent purification of the fluorinase (5 -fluoro-5 -deoxyadenosine synthase), using standard purification protocols revealed that the true substrate for the enzyme was SAM 8 and not ATP 7 [8]. It transpired that ATP 7 and L-methionine (L-Met) were converted to SAM 8 in the crude cell-free extract and that the resultant SAM 8 was then processed by the fluorinase with the release of L-Met. Thus, a catalytic cycle where L-Met was regenerated to drive these two reactions had been inadvertently established (Scheme 1). The fluorinase catalyses the conversion of SAM 8 and fluoride ion to make 5 -FDA 5 as shown in Scheme 1 [8]. 

Small reformers R D areas include compact and low cost reformers (1-5 kW) to convert fossil fuels (natural gas, gasoline) or biomass fuels (ethanol) to hydrogen via different processes (steam reforming, partial oxidation, auto-thermal, non catalytic hybrid steam reforming). Improvements in reformer efficiency, capacities and response times, and integration of purification unit are also being studied. Examples of projects include ... 

To purify a protein, it is essential to have a way of detecting and quantifying that protein in the presence of many other proteins at each stage of the procedure. Often, purification must proceed in the absence of any information about the size and physical properties of the protein or about the fraction of the total protein mass it represents in the extract. For proteins that are enzymes, the amount in a given solution or tissue extract can be measured, or assayed, in terms of the catalytic effect the enzyme produces—that is, the increase in the rate at which its substrate is converted to reaction products when the enzyme is present. For this purpose one must know (1) the overall equation of the reaction catalyzed, (2) an analytical procedure for determining the disappearance of the substrate or the appearance of a reaction product, (3) whether the enzyme requires cofactors such as metal ions or coenzymes, (4) the dependence of the enzyme activity on substrate concentration, (5) the optimum pH, and (6) a temperature zone in which the enzyme is stable and has high activity. Enzymes are usually assayed at their optimum pH and at some convenient temperature within the range... 

---