Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev

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Computer Science Engineering (CSE) : Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev

The document Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev is a part of the Computer Science Engineering (CSE) Course Environmental Engineering - Notes, Videos, MCQs & PPTs.
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FACTORS CONTROLLING ADSORPTION 

The amount of adsorbate adsorbed by an adsorbent from adsorbate solution is influenced by a number of factors as discussed below: 


Nature of Adsorbent 

The physico-chemical nature of the adsorbent is important. Adsorbents differ in their specific surface area and affinity for adsorbate. Adsorption capacity is directly proportional to the exposed surface. For the non-porous adsorbents, the adsorption capacity is inversely proportional to the particle diameter whereas for porous material it is practically independent of particle size. However, for porous substances particle size affects the rate of adsorption. For substances like granular activated carbon, the breaking of large particles to form smaller ones open up previously sealed channels making more surface accessible to adsorbent. 

Pore sizes are classified in accordance with the classification adopted by the International Union of Pure and Applied Chemistry (IUPAC), that is, micro-pores (diameter (d) <20 Å), meso-pores (20 Å < d < 500 Å) and macro-pores (d > 500 Å). Micro-pores can be divided into ultra-micropores (d < 7 Å) and super micro-pores (7 Å < d < 20 Å). 


pH of Solution 

The surface charge as well as the degree of ionization is affected by the pH of the solution. Since the hydrogen and hydroxyl ions adsorbed readily on the adsorbent surface, the adsorption of other molecules and ions is affected by pH. It is a common observation that a surface adsorbs anions favorably at low pH and cations in high pH range.  


Contact Time  

In physical adsorption most of the adsorbate species are adsorbed within a short interval of contact time. However, strong chemical binding of adsorbate with adsorbent requires a longer contact time for the attainment of equilibrium. Available adsorption results reveal that the uptake of adsorbate species is fast at the initial stages of the contact period, and thereafter, it becomes slower near the equilibrium. In between these two stages of the uptake, the rate of adsorption is found to be nearly constant. This may be due to the fact that a large number of active surface sites are available for adsorption at initial stages and the rate of adsorption is a function of available vacant site. Concentration of available vacant sites decreases and there is repulsion between solute molecules thereby reducing the adsorption rate. 


Initial Concentration of Adsorbate 

A given mass of adsorbent can adsorb only a fixed amount of adsorbate. So the initial concentration of adsorbate solution is very important. The amount adsorbed decreases with increasing adsorbate concentration as the resistance to the uptake of solute from solution of adsorbate decreases with increasing solute concentration. The rate of adsorption is increased because of the increasing driving force . 


Temperature 

 Temperature dependence of adsorption is of complex nature. Adsorption processes are generally exothermic in nature and the extent and rate of adsorption in most cases decreases with increasing temperature. This trend may be explained on the basis of rapid increase in the rate of desorption or alternatively explained on the basis of Le-Chatelier's principle.  Some of the adsorption studies show increased adsorption with an increase in temperature. This increase in adsorption is mainly due to an increase in number of adsorption sites caused by breaking of some of the internal bonds near the edge of the active surface sites of the adsorbent. Also, if the adsorption process is controlled by the diffusion process (intraparticle transport-pore diffusion), than the sorption capacity increases with an increase in temperature due to endothermicity of the diffusion process. An increase in temperature results in an increased mobility of the metal ions and a decrease in the retarding forces acting on the diffusing ions. These result in the enhancement in the sorptive capacity of the adsorbents . 


ADSORPTION OPERATIONS 

Fixed bed adsorbers

  • These are used for the adsorption of dyes and colorants, refractory pollutants from wastewater.  
  • The size of the bed depends on the gas flow rate and the desired cycle time. 
  • The bed length usually varies from 0.3 to 1.3 m. 
  • The gas is fed downward through the adsorbent particles in the bed. 
  • Inside the bed, the adsorbent particles are placed on a screen, or performed plate. 
  • Upflow of feed is usually avoided because of the tendency of fluidization of the particles at high rates. When the adsorption reaches the desired value, the feed goes to the other bed through an automatic valve and the regeneration process starts. 

Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev
Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev
Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev
Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev
Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev
   Water Pollution Control by Adsorption (Part - 2) Computer Science Engineering (CSE) Notes | EduRev

 

Where, t is the service time of the bed, n is the linear flow rate of the solution, X is the depth of the bed, K is the rate constant, No is the adsorption capacity, Co is the concentration of the solute entering into the bed, CB is the allowable effective concentration. 

Stirred tank adsorbers 

  • Stirred tank adsorbers are generally used for the removing pollutants from the aqueous wastes.
  • Such an adsorber consists of a cylindrical tank fitted with a stirrer or air sparger. 
  • The stirrer or air-sparger keeps the particles in the tank in suspension. 
  • The spent adsorbate is removed by sedimentation or filtration.
  • The mode of operation may be batch or continuous. 


Continuous adsorbers 

  • The solid and the fluid move through the bed counter currently and come in contact with each other throughout the entire apparatus without periodic separation of the phrases. 
  • The solid particles are fed from the top and flow down through the adsorption and regeneration sections b gravity and are then returned to the top of the column by an air lift or mechanical conveyer. 
  • Multi-stage fluidized beds, in which the fluidized solids pass through down comers from stage to stage, may be used for fine particles. 
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