Nickel catalysts potassium effects

Next, a series of runs was conducted to determine the effect of various alkali metal hydroxide additions along with the sponge nickel catalyst. The 50 wt. % sodium hydroxide and 50 wt. % potassium hydroxide caustic solution used in the initial test was replaced with an aqueous solution of the alkali metal hydroxide at the level indicated in Table 2. After the reaction number of cycles indicated in Table 2, a sample was removed for analysis. The conditions and results are shown in Table 2. The results reported in Table 2 show the level of 2° Amine in the product from the final cycle. The level of NPA in all of the mns was comparable to the level observed in the initial test. No significant levels of other impurities were detected. 

In azide addition to quinones, the triazoline adducts are spontaneously oxidized to the triazoles.1-8 9,279-281,317,392 393 Potassium permanganate32,155,286,288 and nickel peroxide394 also effect triazoline oxidation. Permanganate oxidation of 1,5-substituted triazolines in a two-phase system using a phase-transfer catalyst provides a convenient route to the synthesis of 1,5-disubstituted triazoles (Scheme 118).395,396 Triazoline 4-carboxylic esters32,287,288 and a 4-carboxamide397 are converted to triazoles by potassium permanganate and nickel peroxide, respectively. 

Effects of Potassium on the Catalytic Behavior of Coked Nickel Catalysts in Hydrogenation and Hydrogenolysis Reactions... 

The effect of the addition of a potassium promoter to a nickel steam reforming catalyst has been probed in terms of the propensity of the catalyst to resist carbon formation. It has been found that potassium facilitates a reduced accumulation of carbon by decreasing the rate of hydrocarbon decomposition on the catalyst and by increasing the rate of steam gasification of filamentary carbon from the catalyst. The effect of the promoter on the carbon removal reaction is evident in an enhancement of the pre-exponential factor in the rate equation by promotion of water adsorption on the catalyst surface. 

EFFECTS OF POTASSIUM ON THE CATALYTIC BEHAVIOR OF COKED NICKEL CATALYSTS IN HYDROGENATION AND HYDROGENOLYSIS REACTIONS... 

MIBK is burned in a chemical incinerator equipped with an afterburner and scrubber. It can be destroyed by catalytic hydrogenation and molten salt treatment. The former process is applicable to wastewater. A nickel catalyst at 300°C (572°F) and 200-300 atm has been reported to be effective (Baker and Sealock 1988). In the laboratory, MIBK can be destroyed by oxidation with potassium permanganate (see Section 29.3). 

It has been observed2 that the dropwise addition of an aqueous solution of potassium ethyl xanthate to a cold (0°) aqueous solution of diazotized orthanilic acid results in the immediate loss of nitrogen when a trace of nickel ion is present in the stirred diazonium solution.3 The catalyst can be added as nickelous chloride or simply by using a nichrome wire stirrer. When no nickel ion is added and a glass stirrer is employed, the diazonium xanthate precipitates and requires heat (32°) to effect decomposition. 

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