• Studies On The Treatment Of Coal And Brewery Wastewater Using Adsorption And Coagulation– Flocculation Techniques

  • CHAPTER TWO -- [Total Page(s) 8]

    Page 6 of 8

    Previous   2 3 4 5 6 7 8    Next
    • 2.7 ADSORPTION

      Adsorption is the binding of molecules or particles to a surface (Bungay,2000). The binding to the surface is usually weak and reversible. Just about anything including the fluid that dissolves or suspends the material of interest is bound, but compounds with color and those that have,taste or odor tend to bind strongly (Bungay,2000).

      2.7.1 TYPES OF ADSORPTION

      Adsorption can be classified into two categories as describes below (www.Trans tutors. Com/adsorption,2010).
      a). Depending upon the concentration: In adsorption, the concentration of one substance is different at the surface of the other substance as compared to adjoining bulk or interior phase.
      i). Positive adsorption: If the concentration of the adsorbate is more on the surface as compared to its concentration in the bulk phase then it is called positive adsorption. Example: When a concentrated solution of KCL is shaken with blood charcoal, it shows positive adsorption.
      ii). Negative adsorption: If the concentration of the adsorbate is less than its concentration in the bulk then it is called negative adsorption. Example: when a dilute solution of Kcl is shaken with blood charcoal, it shows negative adsorption.

      b).Depending upon the nature of force existing between adsorbate molecule and adsorbent:
      i). Physical adsorption: If the forces of attraction existing between adsorbate and adsorbent are vander waal’s forces, the adsorption is called physical adsorption is called physical adsorption. This type of adsorption is also known as physisorption or Vander Waal’s adsorption. It can be easily reversed by heating or decreasing the pressure.
      ii). Chemical adsorption: If the forces of attraction existing between adsorbate particles and adsorbent are almost of the same strength as chemicals bonds, the adsorption is called chemical adsorption. This type li of adsorption is also called chemisorption or Langmuir adsorption. This type of adsorption cannot be easily reversed.

      2.7.2 FACTORS WHICH AFFECT THE EXTENT OF ADSORPTION

      The following are the factors which affect the extent of adsorption (Transtutors.com,2010).

      a). Nature of the adsorbate (ga) and adsorbent (solid):
      i). In general, easily liquefiable gases e.g. C02, NH3, Cl2 and S02 etc are adsorbed to a greater extent than the elemental gases e.g. H2, 02, N2,He etc. (while chemisorption is specific in nature).
      ii). Porous and finely powdered solid e.g. charcoal, fullers earth, adsorb more as compared to the hard non-porous material. Due to this property powdered charcoal is used in gas masks.

      b).Surface area of the solid adsorbent:

      i). The extent of adsorption depends directly upon the surface area of the adsorbent, i.e the larger the surface area of the adsorbent, the greater is the extent of adsorption.
      ii). Surface area of a powdered solid adsorbent depends upon its particle size. The smaller the particle size, the greater is its surface area.

      c).Effect of pressure on the adsorbate gas:
      i). An increase in the pressure of the adsorbate gas increases the extent of adsorption.
      ii). At low temperature, the extent of adsorption increases rapidly with pressure.
      iii). At small range of pressure, the extent of adsorption is found to be directly proportional to the pressure.

      Fig 3: Effect of pressure on adsorbate gas

      d). Effect of temperature:
      i). As adsorption is accompanied by evolution of heat, so according to the Le-chatelier’s principle, the magnitude of adsorption should decrease with rise in temperature.
      ii). The relationship between the extent of adsorption and temperature at any constant pressure is called adsorption isobar.
      iii). A physical adsorption isobar shows a decrease in x/m (where ‘m’ is the mass of the adsorbent and ‘x’ that of adsorbate) as the temperature rises.

      iv). The isobar of chemisorption show an increase in the beginning and then decrease as the temperature rises.


  • CHAPTER TWO -- [Total Page(s) 8]

    Page 6 of 8

    Previous   2 3 4 5 6 7 8    Next
    • ABSRACT - [ Total Page(s): 1 ]ABSTACT This work is an experiment of the treatment of coal and brewery wastewater using coagulation-flocculation and adsorption techniques. Jar test method was applied as the coagulation-flocculation technique while batch adsorption method was implemented as the adsorption technique. The coagulants used were Alum and Mucuna pruriens (MUC). These were varied in terms of dosages, pH, time and was experimented on brewery effluent. The adsorbent used was the seed shell of pumpkin seeds. The adsorbe ... Continue reading---

         

      TABLE OF CONTENTS - [ Total Page(s): 1 ]TABLE OF CONTENT Title page - - - - - - - - i Certification - - - - - - - ii Dedication - - - - - - - - iii Acknowledgement - - - - - - iv Abstract - - - - - - - - v Table of content - - - - - - - vi CHAPTER ONE 1.0 INTRODUCTION 1.1 Background to the study - - - - - 1 1.2 Aims and Objectives - - - - - - 3 1.3 Significance of The work - - - - - 3 1.4 Scope of the research work. - - - - - 4 CHAPTER TWO 2.0 LITERATURE REVIEW 2.1 Coal - - - - - - - - 5 2.1.1 Coal Formation - -- - - - - 5 2.1.2 Testi ... Continue reading---

         

      CHAPTER ONE - [ Total Page(s): 1 ]CHAPTER ONE 1.0 INTRODUCTION 1.1 BACKGROUND TO THE STUDY Materials play a major role also in lowering pollution and contamination of the environment. For this reason there are intensive research activities in the areas of lowering toxicity of exhausts, confinement of contamination and recycling of materials of many kinds- including water. Effluent disposal is a major problem around the world. Growing along with the population growth, industries create environmental problems and health hazard for ... Continue reading---

         

      CHAPTER THREE - [ Total Page(s): 2 ]Freundlich Isotherm model is expressed as:qe = KCe1/n…….. (3.6)In linear form. It is written asIn qe = ln k + 1 In Ce …. (3.7)nWhereQe = amount of adsorbate (TSP) adsorbed per unit weight of adsorbent,mg/g.Ce =Equilibrium concentration of the adsorbate, mg/lIn k= a measure of adsorbent capacity1/n = Sorption intensityK and n are calculated from the intercept and slope of the plot of ln qe versus ln Ce respectively (Nath et al, 2006). The value 1/n indicates how favourable the a ... Continue reading---

         

      CHAPTER FOUR - [ Total Page(s): 2 ]CHAPTER FOUR 4.0 EQUIPMENT AND METHOD 4.1 EFFLUENT SAMPLE COLLECTION 4.1.1 BREWERY EFFLUENT COLLECTION Brewery effluent sample was collected from Nigeria Brewery in Enugu using a 25 liters Jerrican in July, 2009. The jerrican was filled to the brim with the brewery effluent in order to expel entrapped air within the jerrican. It was then corked and was left sealed until the commencement of the analysis (wright et al,1993). Preservatives were added before corking as required by the test method (A ... Continue reading---