• Modification And Testing Of Biomass Dryer

  • CHAPTER TWO -- [Total Page(s) 7]

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    • 2.4.2    Deep Bed Drying
      The deep-bed resent complex problems due to the multitude of interdependent and continuously changing temperature and moisture profiles generated in both air and grain masses as well as inside individual kernels.  In an attempt to characterize these phenomena, three distinct approaches have been used namely analytical, empirical and theoretical.   
      The drying air carries away moisture from the grain.  As the air-absorb moisture, its temperature fall and its ability to pick u more moisture decreases.  A batch type dryer can be considered t be made u if a group of thin layers of parboiled paddy stacked upon one another with the drying air flow up through the stacks.
      Thus, the moisture removed from one article affect the state of the air surrounding other adjacent articles in subsequent layers.  The mathematical simulation of such a dryer would lead to complex equation of momentum, heat and mass transfer since each is continuously exposed to continuously changing environmental condition.
      Three distinct layers exist within deep-bed drying proceeds as follows:

      The three distinct layer are:-  The drying zone, the dry zone and the wet or undried zone.  These zones progressively form the button of the bed to the top.  The rate of movement of the drying front will depend on factors such as grain depth, grain initial moisture, air flow, grain temperature and relative humidity.
      2.5    Factors affecting rate of drying
      Drying rate is the rate at which water is been removed from agricultural material per unit time
          Various important factors that affect drying can be classified into three general categories.
      i)    Crop parameters
      ii)    Air parameters
      iii)    Dryer parameters
      2.5.1    Crop Parameters
      i)    The initial moisture content of thee crop:-  If the initial moisture content of crop is high or low, this will affect the energy and period of drying of such crop.
      ii)    The final moisture content of the crop:-  This will also affect the rate of drying in terms of energy supplied for the period of drying etc.  
           iii)    The size of crop:-  This will also affect the rate of drying, small size dry faster than big sizes.
      iv)    Shape of the crop:-  This also affect the rate of drying which can either be a faster or slower rate depending on the shape.
      v)    The porosity of the crop:-  This also affect the rate of drying, a porous material will dry faster than a compact material because a porous material will allow easy evaporation than the compact ones.
      vi)    The solute concentration in the crop:-  if the solute concentration is high, the rate of drying is slow but if low, it means there are much water than the rate of evaporation/drying is high.
      vii)    The surface area:-  A crop that has a broad surface area will dry faster than a narrow surface area
      viii)    The extent of cracking of the kernel, a kernel that is prone to cracking will require a lower rate of drying than the one that is not prone to cracking.
      2.5.2    Air Parameters
      i)     Air Temperature:-  The higher the temperature, the faster the rate of drying and at a short length of time.  At high temperature, the air is dry and has less moisture content.  Hence, it will be able to absorb much water when ass into a stream of crop to be dried.  A lower temperature result in a slower rate of drying and a long period of drying because the air temperature is moist, it has little ability to absorb water.  Hence the rate and length of during is affected.
      ii)    Air relative humidity:-  The dryness of air is termed relative humidity, the lower the humidity, the dryer the air and such air have a high capacity to hold extra water vapor.  A lower humidity causes faster drying rate and a shorter period time but a high leads to a lower drying rate and longer period of time.
      iii)  Air Flow Rate:- The volume of air passing through the crop will cause even and higher or non-uniform and lower drying rate.  If the volume is high, it leads to faster, uniform drying and short time but when thee volume is small, then the drying rate quality of drying and time will be affected.
      2.5.3    Dryer Parameters
      i)   Type of dryer will also affect the drying, sun drying or natural method has a slower rate of drying and longer time when compared to mechanical method of drying.
      ii)   Feed rate of the crop:-  This is the thickness (depth) of crop in the dryer.  A thin layer dries faster than a deep layer.
      ii)   Heat losses in dryer by radiation and convection.  Dryer that is not well insulated to reverent heat losses will send much time and the drying rate will be slower than a well insulated dryer.  (Onipede, 2015).
      2.6    Review of Dryers
          The summary of researchers that have worked on dryers are reviewed below:
          Reyes et al(2014)developed hybrid solar dryer for dehydration of tomatoes.  In this dryer, the air temperature is increased to 118OC above the ambient temperature.  The various drying curves are obtained at different operation conditions and this curves exhibit good adjustment with empirical models of age such as modified are, the result obtained by this tomatoes is rehydrated into + 2% for all runs, in less than 20 minutes and the energy is save u to 6.6 – 12.5%
          Mohapatra et al (2013) developed a natural convection grain dryer for drying paddy and other cereals by use of thermal energy effectively.  Average drying temperature of paddy is between 500C to 580C.  For drying 100Kg of paddy the drying efficiency of the system is estimated as 50.4%.  A 20kg of paraffin wax grade II was used as a phase change material for constant rate of drying.  The moisture content of the product is reduced from 30.1% to 14.6%.
          Mursalim et al., (2002) developed natural convection solar dryer for drying cashew nut in shells (CNS).  The dryer could heat dry air up to 780C temperature and also high quality standard product was obtained through this process.

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    • ABSRACT - [ Total Page(s): 1 ]ABSTRACTDrying is out of the major problem in post harvest operation. The traditional method of  Drying (Sun drying) is weather dependent and unhygienic which affect food storage most especially in developing countries like India where more than 3300 to 3700 hours of bright sunshine per year available in North- West and West coastal region. The dryer consist of the following operating component parts: a cabinet, blower, trays, temperature controller, copper wire and light emitting Diode (LED) s ... Continue reading---

         

      APPENDIX A - [ Total Page(s): 1 ]Drying rate of turmeric at 500c 2kg= 2000g  of turmeric before peeling 1.572kg= 1572g of turmeric after peeling thickness= 3mm 2kg= 2000g of turmeric1.680kg= 168.0g of turmeric after peeling Thickness= 3mm     : 1572g÷6=310g 2kg= 2000g of turmeric 1.689kg= 1680g of turmeric after peeling Thickness= 6mm : 1680 ÷ 6= 280g2kg= 200g of turmeric 1.860kg= 1860g of turmeric after peeling Thickness= 9mm : 1860 ÷6= 310g ... Continue reading---

         

      APPENDIX C - [ Total Page(s): 1 ]Drying rate of turmeric at 700c 2kg= 2000g of turmeric before peeling 1.710kg= 1710g of turmeric after peeling Thickness= 3mm : 1.710 ÷ 6 = 285g 2kg= 2000g of turmeric before peeling 1.620kg= 1620g of turmeric after peeling Thickness= 6mm     : 1620g÷6=270g 2kg= 2000g of turmeric 1.740kg= 1740g of turmeric before peeling Thickness= 9mm: 1740 ÷ 6= 290g ... Continue reading---

         

      APPENDIX B - [ Total Page(s): 1 ]Drying rate of turmeric at 600c 2kg= 2000g of turmeric before peeling 1.620kg= 1620g of turmeric after peeling Thickness= 3mm : 1620 ÷ 6 = 260g 2kg= 2000g of turmeric before peeling 1.560kg= 1560g of turmeric after peeling Thickness= 6mm     : 1560g÷6=260g 2kg= 200g of turmeric 1.800kg= 1800g of turmeric before peeling Thickness= 9mm: 1800 ÷ 6= 300g ... Continue reading---

         

      LIST OF TABLES - [ Total Page(s): 1 ]LIST OF TABLESTable No   Table 3.1:      Bought out Components for the Production Table 3.2:      Cost of Materials for the Production Table 4.1     Drying Rate of Turmeric at 500C When Loaded with 2000g Table 4.2     Drying Rate of Turmeric at 600C When Loaded with 2000g  Table 4.3     Drying rate of Turmeric at 700C When Loaded with 2000g  Table 4.4     Analysis of Variance (ANOVA) Table for Sample 3mm, 6mm, and 9mm at Temperature 500C.  Table 4.5     Analysis of V ... Continue reading---

         

      LIST OF PLATES - [ Total Page(s): 1 ]LIST OF PLATESPlate No  Plate 3.1:     Charcoal  Plate 3.2:     Digital Weighing Scale Plate 3.3:     Temperature Controller  Plate 3.4:     Biomass Dryer  Plate 3.5:     Digital Venier Caliper Plate 4.1:     Sliced Tormeric Before Drying  ... Continue reading---

         

      LIST OF FIGURES - [ Total Page(s): 1 ]LIST OF FIGURESFigure No Figure 2.1:     The Period of drying  Figure 4.1:     Effect of Drying Rate of Turmeric at 500C of 3mm, 6mm and 9mm size of Turmeric Figure 4.2:     Effect of Drying Rate of Turmeric at 600C of 3mm, 6mm and 9mm size of Turmeric Figure 4.3:     Effect of Drying Rate of Turmeric at 700C of 3mm, 6mm and 9mm size of Turmeric ... Continue reading---

         

      APPENDIX D - [ Total Page(s): 1 ] ... Continue reading---

         

      TABLE OF CONTENTS - [ Total Page(s): 1 ]TABLE OF CONTENTSCover Page  Title Page  Certification Dedication  Acknowledgments Abstract Table of Contents List of Tables List of Figures  List of Plates  CHAPTER ONE: INTRODUCTION    1.1    Background to the Study 1.2    Problem  Statement  1.3    Aim and Objectives  1.4    Justification 1.5    Scope of the Project  CHAPTER TWO: LITERATURE REVIEW    2.1    Drying as an Element of Post Harvest  2.1.1    Types of Losses 2.1.1.1    Moisture Content 2.1.1. ... Continue reading---

         

      CHAPTER ONE - [ Total Page(s): 4 ]CHAPTER ONEINTRODUCTION1.1    Background to the StudyDrying is the dehydration process used to remove the moisture present in food products by the application of heat.  The heat may be supplied either by hot air or from the biomass energy.  Drying process is used to preserve the food products for future usage.  Drying prevents the growth of bacteria and yeast formation.  Drying can be achieved by using open air and biomass dryers. (Atul et al, 2014). Drying has a vital role in post harves ... Continue reading---

         

      CHAPTER THREE - [ Total Page(s): 7 ]Transport and logistic       =          N 20,000Total cost = A + B + C         N177,000 + N26,250 + N20,000        =    N223,250.003.10.1    Sourcing of Raw Material    The turmeric (Curcuma Longal) was bought at Ipata market in Ilorin, Kwara State. This material was confirmed fresh and tender and matured so as to get best quality and nutritious product at the end of the experiment. The initial moisture content of the turmeric was 43% moisture content.3.10.2   ... Continue reading---

         

      CHAPTER FOUR - [ Total Page(s): 5 ]The initial moisture content of Turmeric after harvest was 43% fresh weight basis. As drying temperature increases, moisture percentage decrease and as drying time increases, moisture content decreases as will.Hence, analysis of variance (ANOVA) shows that the cutting and drying temperature is significant at 5%. This work is related to the research conducted by Phagu, (2015) who reported that the best drying rate of turmeric is 60oC at 3mm. ... Continue reading---

         

      CHAPTER FIVE - [ Total Page(s): 1 ]CHAPTER FIVE CONCLUSIONS AND RECOMMENDATIONS 5.1    Conclusions     A biomass dryer was modified and tested in the department of Agricultural and Bio-environmental engineering, Kwara State Polytechnic, Ilorin. Based on the results obtained from the experiment, the following conclusions were drawn. 1.    The temperature considered was 500C, 600C and 700Cat 3mm, 6mm and 9mm respectively. 2.    The average weight loss at 500C of 1572g of turmeric was found to be 272.8g, at 600C of 2000g ... Continue reading---

         

      REFRENCES - [ Total Page(s): 2 ]REFERENCEAggarwal, B.B., Sundaram, C., Malani, N. and Ichikawa, H. (2007). Curcumin: The India Solid Gold. Advances in Experimental Medicine and Biology, 595: 1-75.Ajayi C., Orsunil K. S. and Depak D. P. (2009):  Design of solar dryer with Turbo ventilator and fireplace.  www.solarfood.org/solarfood/--/solarfood.Atul Petal AND Gaurav Petal (2004):  “Operation22..al Augmentation of forced circulation type solar Dryer System using CFD Analysis”.  Int. 10 Journal of Engineering Rese ... Continue reading---