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                  4.1 Basic Principles of Adsorption and Ion Exchange  245


                      nonaromatics (carbon tetrachloride, chloroalcyl ethers, and he utadiene), xachlorob
                      high molecular weight hydrocarbons (dyes, gasoline, amines, humics, and k erosene,
                      oil), and surfactants (alkyl benzene sulfonates).
                                            y
                                            ,
                  (b)  Inorganic compounds  : chlorine, bromine, iodine, fluoride, antimon arsenic, bis-
                        ,
                        ,
                      muth, chromium, tin, solv mercury cobalt, and zirconium.
                        er
                    In contrast, organic compounds like alcohols, lo acids and -weight k w-molecular etones,
                  aldehydes, sugars and starches, very high molecular weight or colloidal or lo ganics,  w-
                  molecular-weight aliphatics, and inorganic compounds such as nitrate, phosphate, chlo-
                      el,
                        anadium,
                  ride, bromide, iodide, lead, nick titanium, v iron, copper cadmium, zinc,
                          ,
                  barium, selenium, molybdenum, manganese, tungsten, and radium are poorly absorbed on
                  activated carbons.
                    There are a number of cases where carbon adsorption is preferably used in water treatment:
                  •  if compounds are not compliant for biode gradation,
                  •  if the molecule contains branched chairs, has a large molecular weight, and lo w polar-
                     ity,
                  •  in the case of removing solids for concentrations lower than 50 ppm,
                  •  in the case of removing oil for concentrations is lower than 10 ppm,
                  •  generally, in the case of removing organics and inorganic species, for concentrations
                     lower than 5000 and 1000 mg/L, respecti ely v .

                    Besides the applications of water treatment, acti ated carbon is called into action for the v
                    ents,
                  removal of volatile organic compounds such as solv toxic gases, and odors from
                  ide,
                  gaseous waste streams. Hydrogen sulf mercury and radon can also be remoed from v
                   ,
                  gas streams by means of chemically impregnated carbons. In f among the adsorbents, act,
                  it is the most attractive material because it is the only common nonpolar adsorbent (Noble
                  and Terry, 2004). The polarity of the adsorbent’ace plays a major role in the type of s surf
                  the compounds that can be adsorbed. Polar adsorbents will preferentially adsorb moisture
                  in gaseous waste streams, and as a result their usage in such applications is limited. In con-
                   v
                  trast, actiated carbon is an appropriate material in such cases, where the goal is the con-
                  trol of emissions of organic solv odors, toxic gases, acid v phenols, and
                     ents,
                         apors,
                  hydrocarbon vapors.
                    Some basic rules for carbon adsorption are the follo wing:
                  •  Larger molecules adsorb better than smaller molecules.
                  •  Nonpolar molecules adsorb better than polar molecules.
                  •  Nonsoluble or slightly soluble molecules adsorb better than highly soluble molecules.
                  •  On the basis of the polarity or solubility or both, of the molecule being adsorbed, the
                    ,
                     v pH may hae an influence on the extent of adsorption.
                  •  Temperature increases the rate of diffusion through the liquid to the adsorption sites;
                     but since the adsorption process is exothermic, increases in temperature may reduce the
                     degree of adsorption. This temperature effect is negligible in w-treatment applica- ater
                     tions and ambient v apor -phase applications.
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