Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Industrial, effluents lead concentrations

Fig. 3 A shows the effluent NH3 concentration observed for Ru/MgO as a function of reaction temperature for three different Pn, / Phj / Paf ratios at 20 bar total pressure. It is obvious that the reaction orders for N2 and H2 have opposite signs. Fig. 3B illustrates that the reaction orders for N2 and H2 partly compensate each other in the kineticaliy controlled temperature regime. Hence an increase in total pressure with a constant Pnj / Phj 1/3 ratio does not lead to a significant increase in conversion at lower temperatures. For the plication of alkali-promoted Ru catalysts under industrial synthesis conditions, it is necessary to find a compromise between kinetics and thermodynamics by increasing the Pn, / Phj ratio. The optimum observed for Cs-Ru/MgO prepared from CS2CO3 at 50 bar is at about Pnj / Phj 40 / 60 [15]. The high NH3 concentration of about 8 % obtained with 0.138 g catalyst using a total flow of 100 Nml/min clearly shows that Ru catalysts have indeed the potential to replace Fe-based catalysts in industrial synthesis [15]. Fig. 3 A shows the effluent NH3 concentration observed for Ru/MgO as a function of reaction temperature for three different Pn, / Phj / Paf ratios at 20 bar total pressure. It is obvious that the reaction orders for N2 and H2 have opposite signs. Fig. 3B illustrates that the reaction orders for N2 and H2 partly compensate each other in the kineticaliy controlled temperature regime. Hence an increase in total pressure with a constant Pnj / Phj 1/3 ratio does not lead to a significant increase in conversion at lower temperatures. For the plication of alkali-promoted Ru catalysts under industrial synthesis conditions, it is necessary to find a compromise between kinetics and thermodynamics by increasing the Pn, / Phj ratio. The optimum observed for Cs-Ru/MgO prepared from CS2CO3 at 50 bar is at about Pnj / Phj 40 / 60 [15]. The high NH3 concentration of about 8 % obtained with 0.138 g catalyst using a total flow of 100 Nml/min clearly shows that Ru catalysts have indeed the potential to replace Fe-based catalysts in industrial synthesis [15].
There are several such toxic agents that cause considerable medical, public and political concern. Two examples are discussed here the heavy metal ions (e.g. lead, mercury, copper, cadmium) and the fluorophosphonates. Heavy metal ions readily form complexes with organic compounds which are lipid soluble so that they readily enter cells, where the ions bind to amino acid groups in the active site of enzymes. These two types of inhibitors are discussed in Boxes 3.5 and 3.6. There is also concern that some chemicals in the environment, (e.g. those found in industrial effluents, rubbish tips and agricultural sprays), although present at very low levels, can react with enhanced reactivity groups in enzymes. Consequently, only minute amounts concentrations are effective inhibitors and therefore can be toxic. It is suggested that they are responsible for some non-specific or even specific diseases (e.g. breast tumours). [Pg.46]

Industrial effluents in the river Kalu at Ambivali, Madhya Pradesh, contain metals (mercury, lead, copper, and cadmium) chlorides, dyestuffs, organic acids from rayon, paper mills, dyestuff factories, and chemical plants at high concentrations [12]. [Pg.118]

Similarly, in the case of industrial effluents control maybe based on limitation of the discharge of another toxic metal, say copper or zinc, with a reduction in lead discharge occurring as an added bonus. In this chapter it is necessary, therefore, to consider both control methods specifically designed to limit the discharge of lead, as well as those more general methods which also affect concentrations of lead in effluents. [Pg.104]

The on-line monitoring of the concentrations of toxic metals such as lead, cadmium and mercury in industrial effluents, river water, drinking water, lake water and marine water has become an important aspect of environmental control. Ideally, in any on-line system for monitoring of industrial effluents which flow into the environment, the sampling, chemical treatment to remove interferences (if required), data manipulation, data reporting and all other necessary operations are completely automated. In the present era of chemical instrumentation, normally this means that all operations from the start of the experiment (sampling) to preparation of the final report are under microprocessor control. [Pg.167]

Cadmium is found in low concentrations in most soils and waters. It is produced as a by-product of zinc and lead mining and smeltering. Industrial use of cadmium has led to a dramatic increase in environmental problems caused by this element. Cadmium is used in semiconductors, nickel-cadmium batteries, electroplating, polyvinyl chloride (PVC) manufacturing, and control rods for nuclear reactors. The most important sources for aquatic contamination are active and inactive lead-zinc mines, land application of sewage sludge, zinc-cadmium smelters, effluents from plastic and steel production, and wastewaters from the production of nickel-cadmium batteries and electroplating (Zuiderveen, 1994). [Pg.485]


See other pages where Industrial, effluents lead concentrations is mentioned: [Pg.365]    [Pg.40]    [Pg.141]    [Pg.303]    [Pg.13]    [Pg.220]    [Pg.648]    [Pg.155]    [Pg.205]    [Pg.219]    [Pg.118]    [Pg.382]    [Pg.38]    [Pg.39]    [Pg.43]    [Pg.15]    [Pg.179]    [Pg.40]    [Pg.118]    [Pg.107]    [Pg.176]    [Pg.35]    [Pg.739]    [Pg.196]    [Pg.945]    [Pg.607]    [Pg.287]    [Pg.670]    [Pg.1395]    [Pg.1481]    [Pg.883]    [Pg.136]    [Pg.201]    [Pg.1395]    [Pg.1481]    [Pg.105]    [Pg.360]    [Pg.402]    [Pg.136]    [Pg.475]    [Pg.55]    [Pg.212]    [Pg.276]    [Pg.1085]   
See also in sourсe #XX -- [ Pg.40 ]




SEARCH



Effluent

Effluent concentrations

Industrial effluents

Industry concentrations

Lead concentration

© 2024 chempedia.info