<?xml version="1.0" encoding="UTF-8"?>
<record
    xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance"
    xsi:schemaLocation="http://www.loc.gov/MARC21/slim http://www.loc.gov/standards/marcxml/schema/MARC21slim.xsd"
    xmlns="http://www.loc.gov/MARC21/slim">

  <leader>02841nam a2200265 a 4500</leader>
  <controlfield tag="001">vtls000045113</controlfield>
  <controlfield tag="003">KUKTEM</controlfield>
  <controlfield tag="005">20251114204455.0</controlfield>
  <controlfield tag="008">100209t2009    my a   f m    000 0 eng|d</controlfield>
  <datafield tag="020" ind1=" " ind2=" ">
    <subfield code="a">THE0004525(Local)</subfield>
  </datafield>
  <datafield tag="039" ind1=" " ind2="9">
    <subfield code="a">201905131532</subfield>
    <subfield code="b">azhar</subfield>
    <subfield code="c">201112291324</subfield>
    <subfield code="d">ida</subfield>
    <subfield code="c">201108030933</subfield>
    <subfield code="d">Fida</subfield>
    <subfield code="c">201107132307</subfield>
    <subfield code="d">VLOAD</subfield>
    <subfield code="y">201002091355</subfield>
    <subfield code="z">ida</subfield>
  </datafield>
  <datafield tag="040" ind1=" " ind2=" ">
    <subfield code="a">UMP</subfield>
  </datafield>
  <datafield tag="090" ind1=" " ind2=" ">
    <subfield code="a">TP248.65.P76 F37 2009 rs Bc.</subfield>
  </datafield>
  <datafield tag="100" ind1="0" ind2=" ">
    <subfield code="a">Farhani Faisal</subfield>
  </datafield>
  <datafield tag="245" ind1="1" ind2="0">
    <subfield code="a">Protein purification using zeolite adsorbent /</subfield>
    <subfield code="c">Farhani Faisal</subfield>
  </datafield>
  <datafield tag="246" ind1="3" ind2=" ">
    <subfield code="a">Protein purification using zeolite adsorbent</subfield>
    <subfield code="h">[electronic resource]</subfield>
  </datafield>
  <datafield tag="260" ind1=" " ind2=" ">
    <subfield code="a">Kuantan, Pahang :</subfield>
    <subfield code="b">UMP,</subfield>
    <subfield code="c">2009</subfield>
  </datafield>
  <datafield tag="300" ind1=" " ind2=" ">
    <subfield code="a">80 p. :</subfield>
    <subfield code="b">ill. (some col.) ;</subfield>
    <subfield code="c">30 cm. +</subfield>
    <subfield code="e">1 computer disc</subfield>
  </datafield>
  <datafield tag="502" ind1=" " ind2=" ">
    <subfield code="a">Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2009</subfield>
  </datafield>
  <datafield tag="504" ind1=" " ind2=" ">
    <subfield code="a">Bibliography : p. 69-70</subfield>
  </datafield>
  <datafield tag="520" ind1="3" ind2=" ">
    <subfield code="a">There  has  been  much  interest  generated  in  the  development  of  protein purification  since  many  of  modern  biotechnology  products  can  be  produce  from purified protein such as insulin, vaccines and food additives. The aim of this research is  to study  the most optimum condition  to purify protein  in order  to produce a high purity  protein  with  low  cost  by  applying  the  principle  adsorption  process  using zeolite adsorbent. Adsorption of Bovine Serum Albumin used as protein  sample on Y,  Beta  and  ZSM-5  zeolites  at  various  pH  values was  carried  out  in  sequence  to   investigate  the  effect  of  different  pH  value  and  different  types  of  adsorbent  on protein purification. Batch  adsorption  experiment was  carried out by  contacting  the same  amount  of  different  zeolites  synthesized  with  the  Bovine  Serum  Albumin solution.  Outcome  of  the experiment  shows  that  maximum  adsorption  capacity occurred when Y zeolite was used as the adsorbent at pH 5 that is close to isoelectric point  (pI)  of  Bovine  Serum  Albumin  which  is  4.7.  This  proves  that  adsorption capacity depends on  the physicochemical properties of  the zeolite as well as  the pH of protein  solution. The maximum  adsorption on  the  zeolites  tended  to occur when   the pH was  at or  just below  the pI of  the protein. At  this pH,  the protein  sample  is positively  charged.  Adsorption  isotherms  obtained  on  effect  of  different  type  of adsorbent at pH5 and effect of different pH on Y zeolite were found to be confirmed well  to  the  ideal Langmuir model  equation.  In  order  to  improve  in  the  next  study, other parameters such as protein size, temperature of the protein solution and protein concentration need to be considered as well.</subfield>
  </datafield>
  <datafield tag="650" ind1=" " ind2="0">
    <subfield code="a">Protein</subfield>
    <subfield code="x">Purification</subfield>
  </datafield>
  <datafield tag="650" ind1=" " ind2="0">
    <subfield code="a">Zeolites</subfield>
  </datafield>
  <datafield tag="952" ind1=" " ind2=" ">
    <subfield code="0">0</subfield>
    <subfield code="1">0</subfield>
    <subfield code="4">0</subfield>
    <subfield code="7">1</subfield>
    <subfield code="a">10000</subfield>
    <subfield code="b">10000</subfield>
    <subfield code="d">2019-09-04</subfield>
    <subfield code="l">0</subfield>
    <subfield code="o">TP248.65.P76 F37 2009 rs Bc.</subfield>
    <subfield code="p">0000043003</subfield>
    <subfield code="r">2019-09-04 00:00:00</subfield>
    <subfield code="t">1</subfield>
    <subfield code="w">2019-09-04</subfield>
    <subfield code="y">PSM</subfield>
  </datafield>
  <datafield tag="952" ind1=" " ind2=" ">
    <subfield code="0">0</subfield>
    <subfield code="1">0</subfield>
    <subfield code="4">0</subfield>
    <subfield code="7">1</subfield>
    <subfield code="a">10000</subfield>
    <subfield code="b">10000</subfield>
    <subfield code="d">2019-09-04</subfield>
    <subfield code="l">0</subfield>
    <subfield code="o">CD 4033 | TP248.65.P76 F37 2009 rs Bc.</subfield>
    <subfield code="p">0000043004</subfield>
    <subfield code="r">2019-09-04 00:00:00</subfield>
    <subfield code="t">1</subfield>
    <subfield code="w">2019-09-04</subfield>
    <subfield code="y">PSM</subfield>
  </datafield>
  <datafield tag="999" ind1=" " ind2=" ">
    <subfield code="a">VIRTUA40</subfield>
    <subfield code="c">2654</subfield>
    <subfield code="d">2660</subfield>
  </datafield>
  <datafield tag="999" ind1=" " ind2=" ">
    <subfield code="a">VTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5040*5200*6500*6501*9992</subfield>
  </datafield>
</record>
