The AFC had the capability to succeed fully in the application of market with the major breakthrough of CO_2 scrubbing technology and catalyst poisoning preventing technology.
It was found that the catalyst deactivation was not caused by the plugging of catalyst micropores, decrease in surface area, crystalline grain growth or catalyst poisoning. It was just because that excess Zn~ 2+ and Fe~ 2+ from the reaction slurry were adsorbed on the catalyst. After washing with acid, the activity and selectivity of the catalyst were almost completely recovered.
The cured polyphenylene sulfide(PPS) is well compatible with polysiloxane gel,but the uncured PPS made the Pt catalyst poisoning,it shows that poison contained materials are uncertain to make the Pt catalyst poisoning.
Phenomena in monolithic catalytic converters were analyzed in detail. Main physical and chemical processes include heat and mass transfer,flow distribution,chemical kinetics,oxygen storage release and catalyst deactivation.
Main physical and chemical processes including heat and mass transfer,flow distribution,chemical kinetics,oxygen storage and catalyst deactivation are discussed.
It was found that the catalyst deactivation was not caused by the plugging of catalyst micropores, decrease in surface area, crystalline grain growth or catalyst poisoning. It was just because that excess Zn~ 2+ and Fe~ 2+ from the reaction slurry were adsorbed on the catalyst. After washing with acid, the activity and selectivity of the catalyst were almost completely recovered.
The results showed that the Pb~(2+) has toxicity ,and Cu~(+ )、Mg~(2+) and Ba~(2+) have passivation,and Na~(+) 、Ni~(2+) 、Cu~(2+)和SO_(42) have no influence to zhe action of this catalyst .
The strong and irreversible chemisorption of substrate or (and) reaction products (?self-poisoning" of catalyst surface) has been found to account for an activity decrease and changes in catalytic selectivity in the reaction.
The implementation of the developed methodology for the quantification of VOSC as potential catalyst poison in a cleaning plant for groundwater contaminated with volatile haloorganics (VOX) is presented.
However it is not an irreversible catalyst poison, and oils containing relatively large amounts of trichloroethylene have been successfully hydrogenated in the laboratory and pilot plant.
An empirical catalyst deactivation function is incorporated into the model accounting for the loss in activity because of coke formation on the catalyst surface during the long-term operation.
This paper discusses the investigation on the effect of reactive activity of quadruply promoted ammonia synthesis catalyst A110 by using synthesis gas containing <5-~30ppm water vapor under high pressure. The experimental data were treated with the modified T- equation. We have found that the poisoning factor POIS=k/kTO is approximately in inverse proportion to VH2O and proportional to 6th power of absolute temperature, and minimal relation with pressure.
This report points out that chloride ion is a poison for iron catalyst of ammonia synthesis promoted by alkali metal. Results of the experiment on adding KC1 to the system Fe-AC (active carbon)-K showed a very marked decrease in catalytic activity (Fig. la), while the addition of KC1 to the system, Ru-AC-K, activity decreases much less (Fig. lb), indicating that chloride ion is a poison for iron catalyst but has little effect on ruthenum catalyst for ammonia synthesis.Gas chromotographic study on Fe3(C3O4) ...
The phase-transfer catalytic property of linear-chain polyoxyethylenes, the reactivity relationship between the structural of halohydrocarbons and esterification,and the effect of various solvents on yield of esters have been investiged by the reaction of halohydrocarbons with potassium acetate in L-S phase.Furthermore, the problem of catalystpoison by iodides and the solvable method have also been discussed.