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Chapter 1 NATURAL PRODUCTS Edible and Essen;al oils Soaps and Detergents; Glycerin Starch and its Deriva;ves 1 2 Overview of topics Balaubramanian S 1 3
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Page 1: Chapter(1 (NATURAL(PRODUCTS(( …balasubramanian.yolasite.com/resources/Lecture 3 Soaps and... · Michel&Eugène&Chevreul&(31(August1786(–9(April ... (animal(fatand(salt.(1. History

Chapter  1  NATURAL  PRODUCTS    

       Edible  and  Essen;al  oils  

       Soaps  and  Detergents;  Glycerin  

       Starch  and  its  Deriva;ves    

1

2

Overview of topics

Balaubramanian  S     1  

3

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Soaps and Detergents 1.  History  of  Soap  2.  History  of  glycerin  3.  What  are  Soaps    and  Detergents  ?  4.  What  is  glycerin?  5.  Cleaning  ac;on  of  soaps  6.  What  are  the  process  methods  available  to  produce  soaps?    7.  Difference  between  batch  and  Con;nuous  process  8.  Con;nuous  Produc;on  process  -­‐  soap  9.  Process  descrip;on  10.  What  are  the  process  methods  available  to  produce  detergents?  11.   What  are  the  process  methods  available  to  produce  Glycerin?  12.   End  uses  of  soaps  and  detergents;  glycerin  13.   Conclusions  

Balaubramanian  S     2  

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Pliny  and  Elder  (23  AD  –  August  25,  79  AD)    A  Roman  author,  naturalist  and  natural  philosopher.    He  described  the  manufacture  of  hard  soap  and  so[  soap  in  the  first  century.  

Michel  Eugène  Chevreul  (31  August  1786  –  9  April  1889)    A   French   chemist   whose  work  with   fa_y   acids   led   to   early  applica;ons   in   the   fields   of   art   and   science   He   is   credited  with   the   discovery   of  margaric   acid   and   designing   an   early  form  of  soap  made  from  animal  fat  and  salt.  

1. History of soap and detergents

Balaubramanian  S     3  

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Nicolas  Leblanc  (December  6,  1742  –  January  16,  1806)    A  French  chemist  and  surgeon  who  discovered  how  to  manufacture  soda  from  common  salt.      He  showed  that  soap  forma;on  was  actually  a  chemical  reac;on.  

Domeier  completed  his  research  on  the  recovery  of  glycerin  from  saponifica;on  mixtures  in  this  period    

The  raw  material  shortages  of  World  War  I  led  the  Germans  to  develop  “Synthe;c  soaps”  or  “Detergents”  

1. History of soap

Balaubramanian  S     4  

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Ascanio  Sobrero(October  12,  1812  –  May  26,  1888)    An  Italian  chemist  who  had  produced  the  explosive    nitrogylcerin  for  the  first.  

Alfred  Nobel  (October  21,  1833  –  December  10,  1896)    A  Swedish  chemist,  engineer,  innovator,  and  armaments  manufacturer.  !n  1868  Alfred  Nobel  invented  dynamite.      

2. History of Glycerin

Balaubramanian  S     5  

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3. Soaps and Detergents

If  an  oil  is  hydrolyzed  and  or  saponified  with  alkali  soaps  are  obtained.    Any  metallic  salts  of  fa_y  acid  is  soap,  but  the  term  soap  is  applied  to  water  soluble  salts.    Soaps  comprises  of  the  sodium  or  potassium  salts  of  various  fa_y  acids  but  chiefly  of  oleic,  stearic,  palmi;c,  lauric  and  mys;ric  acids.    The  saturated  fat  gives  hard  soaps,  whereas  unsaturated  fat  gives  so[  soaps  on  saponifica;on         Balaubramanian  S     6  

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Balaubramanian  S     7  

Soaps  comprises  of  the  sodium  or  potassium  salts  of  various  fa_y  acids  but  chiefly  of  oleic,  stearic,  palmi;c,  lauric  and  mys;ric  acids.  It  also  comprises  of  salts  of  sodium  and  zinc  oxide  catalyst.      

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3. Soaps and Detergents Detergents  differ  from  soap  in  their  ac;on  in  hard  water.  

 

Detergents  may  react  with  hard  water  ions,  but  the  resul;ng  

products  are  either  soluble  or  remain  colloidally  dispersed  in  

water.  

 

Scien;fically,  the  term  detergent  covers  both  soap  and  

synthe;c  detergents  or  “Syndents”  but  it  is  widely  used  to  

indicate  synthe;c  cleaning  compound.    

Balaubramanian  S     8  

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3. Soaps and Detergents S.  No     Soaps     Detergents    

01.   Soaps  from  insoluble  compounds  with  the  calcium  and  magnesium  ions  present  in  hard  water  

Detergents  may  react  with  hard  water  ions,  but  the  resul;ng  products  are  either  soluble  or  remain  colloidally  dispersed  in  water.  

Synthe;c  cleaning  compound    

02.   To  make  soap      Tallow  /or  rice  bran  oil  +  Hydrolysis  (Splikng  fats)  Tallow  fa_y  acid  or  fa  

   Alkylbenzene  sulfonate  +  oleum    Disulfonate  and  Sulfuric  acid  

03.   Tallow  /or  rice  bran  oil  +  NaOH  (Saponifica;on)  Sodium  salt  

Tallow  fa_y  alcohol  +  oleum  Fa_y  alcohol  sulfate  

04.   Salt  of  fa_y  acid  +  builders,  etc    Soap  

Sulfonate  +  Sulfate  +  NaOH    Sodium  salts    

Sodium  salt  +  Builders    detergents  

9  

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4. Glycerin

Glycerin  is  a  clear,  nearly  colorless  liquid  having  a  sweet  taste  

but  no  odor.    

 

The  term  glycerin  is  chosen  for  the  technical  product  containing  

the  pure  trihydroxy  alcohol  “glycerol”.  

 

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5. Cleaning action of soaps

Balaubramanian  S    

The   success   of   an   cleaning   agent   is   to   supply   compounds  with   hydrophobic   (water  

ha;ng)   and   hydrophilic   (water   loving)   groups   which   will   also   appreciably   decrease  

surface  tension  and  increase  we_ability.   i.e.  surface  tension  is   inversely  propor;onal  

to  the  we_ability.    

 

In  wash  water,  soaps  or  detergents  increase  the  wekng  ability  of  water  so  that  it  can  

more  easily  penetrate  into  the  fabrics  and  reach  the  soil.  

 

Each  molecule  of   the  cleaning   solu;on  may  be  considered  a   long  chain.  One  end  of  

the  chain   is  hydrophilic(Water   loving)  and  the  other  end  of  the  chain   is  hydrophobic  

(Water   ha;ng  or   soil   loving).   The   soil   loving   end   are   a_racted   to   a   soil   par;cle   and  

surround  it.  

   11  

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5. Cleaning action of soaps

Balaubramanian  S    

 

At  the  same  ;me  the  water  loving  end  pulls  molecules  and  the  soil  par;cles  

away  from  the  fabric  and  into  the  wash  water.  

 

This  is  the  ac;on  which,  when  combined  with  the  mechanical  agita;on  of  the  

washing  machine,   enables   a   soap   or   detergents   to   remove   soil,   suspend   it,  

and  keep  it  from  redeposi;ng  on  clothes.    

12  

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6. Methods of production - Soap

Balaubramanian  S     13  

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7. Difference between batch and Continuous process

Balaubramanian  S     14  

Batch  (Twitchell)  Process     ConEnuous  process    

Temperature,  deg.  C     150  –  175     230  -­‐  250    

Pressure,  mPa  (g)     5.2  –  10     4.1  –  4.9    40  –  45  atm    

Catalyst     Alkyl  aryl  sulfonic  acids,  Oxides  of  calcium,  zinc  and  magnesium  i.e.  CaO,  ZnO,  MgO.  

Same  catalyst  or  op;onal    

Acid  used     Sulfuric  acid     __________  

Time,  h     12  –  48     2  –  3    

Opera;on  equipment     Batch     Con;nuous    

Hydrolysis     85  –  98  %     97  –  99%    

Glycerol  obtained     5  –  15%   10  –  25%    

Advantages     Low  temperature,  adaptable  to  small  scale  

Small  floor  space,  uniform  product  quality,  high  yield  of  acids,  high  glycerin  concentra;on,  automa;c  control    

Disadvantages     Catalyst  handling;  ling  reac;on  ;me,  need  more  than  one  stage  for  good  yield    

High  temperature  and  pressure,  High  cost  and  greater  opera;ng  skill  

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8. Production Process – Soap

Balaubramanian  S     15  

ConEnuous  hydrolysis  and  SaponificaEon    

Process  

Fat  or  Oil    

Catalyst  

Water    

Steam    

Soap    

Caus;c   Glycerin-­‐  by  product    

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Balaubramanian  S     16  

Hydrolysis  (Fat  –  SpliJng)      (R  .  COO)3  .  C3H5  +  3H20        3R  .  COO  .  H  +  C3H5(OH)3  (Triglyceride)              +  (Water)      Fa_y  acid  +  Glycerin    (C17H35C00)3  C3H5      +  3H2O      3C17H35COOH  +  H2O  Glyceryl  stearate    +  Water      Fa_y  acid  (Stearic  Acid)  +  Glycerin    SaponificaEon  (CausEc  AddiEon)      R  .  COOH  +      M  .  OH        R  .  COO  .  M  +  H2O    C17H35COOH    +      NaOH        C17H35COONa      +  H20  (Stearic  acid)  +      (Caus;c)        Sodium  stearate  +  water    

8. Production Process – Unit process

Fa_y  acid  radical  represen;ng  oleic,  stearic,  palmi;c,  lauric  and  mystric  acids  

Alkali  element  such  as  Na  or  K  

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8. Production Process – Block diagram

Balaubramanian  S    

ConEnuous    Hydrolysis  and    SaponificaEon    

Holding  tank  (or)    

Dis;llate  receiver  

Mixer  (Neutraliza;on)    

Blender  (Saponifica;on)    

Ion  exchanger  

Mul;ple  effect  evaporator    

S;ll    

Cooling    

Holding    Tank    

Adsorber    

Filter    

Blend  tank     Hydrolyzer  (Fat  splikng)    

Steam  flash  tank  

Vacuum    Dis;lla;on     Condenser    

Waste  

   Oil  or  Fat  +  Catalyst   Hot  Water     Steam  out      

99%  White  Glycerin    

98%  Yellow  Glycerin    

Ac;vated    Carbon  

Caus;c  (NaOH)    

Steam    in    

Fa_y  Acids  

Steam    Out      

Steam    in    

Steam    Out      

Soap  to  final  product  

Bar  Stock    Press  Chipping  rolls    

Spray  drier  to  soap  powder  

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8. Production Process–process diagram

Mixer  

Hydrolyser    

Fat  or  Oil  and  Catalyst  

Hot  water  

Steam  Flash  Tank    

Vacuum

 Dis;

lla;o

n  Rejects  or  trace  impuri;es   Steam    

Ion  exchange    

Triple    Effect    Evaporator    

FaLy  acid  product  

Holding  

tank  

Blender  

NaOH  

Air   Water  

Holding    Tank  

S;ll  

Steam  

Heater  

Soap  to  final  products  

Bar  stock    press  

Chipping  rolls   Spray  drier    for  soap    powder  

Filte

r  

99%  Glycerin  99%  Yellow  Glycerin  

Ac;vated  Carbon  

Adsorp;o

n  Blending  Tank    

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Balaubramanian  S     19  

S.  No    

Process     Equipment     Unit  operaEons     Unit  process   ObjecEve     OperaEng  condiEons  

1.   Con;nuous  Hydrolysis  and  Saponifica;on  (Con;nuous  Process)        

(a)  Blend  tank     Physical  blending    

__________  

Blending  of  fat  or  oil  and  catalyst  

__________  

(b)  Hydrolyzer    __________  

 

Hydrolysis   Splikng  of  fats     230  -­‐  250  deg.  C  40  –  45  atm    

(c)  Ion  exchanger     Ion  exchange  

__________    

Separa;on  of  dissolved  salts  and  glycerides  collected  from  the  hydrolyzer  as  the  bo_om  product  

__________    

(d)  Evaporator     Evapora;on    

__________    

Separa;on  of  water  and  glycerides  (or)  Concentra;on  of  glycerides      

__________    

9. Process description

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Balaubramanian  S     20  

S.  No    

Process     Equipment     Unit  operaEons     Unit  process   ObjecEve     OperaEng  condiEons  

(e)  Dis;lla;on  s;ll    

Dis;lla;on    

__________    

Glycerides  obtained  from  the  evaporator  is  purified  to  produce  99%  Yellow  Glycerin    

__________    

(f)  Cooler  (or)  Heat  exchanger    

Cooling  or  Heat  transfer     __________  

 

Cool  the  glycerides  obtained  from  the  s;ll  

__________    

(g)  Holding  tank     Storage    __________  

 

Cooled  glycerides    Stored     __________  

 

(h)  Adsorber     Adsorp;on    

__________    

Removal  of  color  cons;tuents  using  ac;vated  carbon  as  the  adsorbent    

__________    

9. Process description

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Balaubramanian  S     21  

S.  No    

Process     Equipment     Unit  operaEons     Unit  process   ObjecEve     OperaEng  condiEons  

(i)  Filter     Filtra;on    

__________    

Final  separa;on  of  glycerides    

__________    

(j)  Steam  flash  tank    

Steam  separa;on    __________  

 

Separa;on  of  steam  from  fa_y  acid  

__________    

(k)  Vacuum  dis;lla;on  column  

Dis;lla;on    __________  

 

Separa;on  of  fa_y  acids  and  trace  impuri;es    

__________    

(l)  Condenser     Condensa;on     __________    

Vapors  of  fa_y  acids  converted  to  liquid    

__________    

(m)  Holding  tank  (or)  Dis;llate  receiver      

Storage    __________  

 

The  dis;llate  from  the  condenser  is  stored    

__________    

9. Process description

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Balaubramanian  S     22  

S.  No    

Process     Equipment     Unit  operaEons     Unit  process   ObjecEve     OperaEng  condiEons  

(n)  Mixer     Mixing    

__________    

Neutraliza;on  of  fa_y  acids    

__________    

(o)  Blender     Blending     Saponifica;on     Saponifica;on  of  neutralized  fa_y  acids  

__________    

(p)  Spray  drier     Drying    __________    

Drying  of  soaps  into  powder  a[er  saponifica;on.  

__________    

9. Process description

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Balaubramanian  S     23  

10. Methods of production-Detergents

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Two  of  the  most  prominent  detergents  used  today  are    

1.  Sulfated  fa_y  alcohols      

2.  Alkyl-­‐Aryl  sulfonates    

Manufacturing  method    

             1.  Sulfated  fa_y  alcohols  

   Deriving  higher  molecular  weight  of  alcohols  from  oils  of  plant  origin  by    

   sodium  reduc;on  or  hydrogena;on  followed  by  sulfona;on.  The  steps    

   involved  in  the  manufacture    of  sulfated  fa_y  alcohols  are  as  follows,  

a)  Cataly;c  hydrogena;on  of  coconut  oil    

b)  Sodium  reduc;on    

c)  Sulfa;on  of  fa_y  acids  

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10. Methods of production-Detergents

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Manufacturing  method    

             1.  Alkyl-­‐Aryl  sulfonates  

   The  steps  involved  in  the  manufacture    of  Alkyl-­‐Aryl  sulfonates  are  as  follows  

   (a)  Conversion  of  hydrocarbon  (paraffin)  to  alkyl  chloride  

   (b)  Alkyla;on  of  Alkylchloride  yields  Aryl-­‐Benzene  compounds  

   (c)  Aryl-­‐Benzene  compound  on  sulfona;on  in  presence  of  oleum  yields    

     detergents  (Aryl-­‐Benzene  sulfonate)  

     

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10. Methods of production-Detergents

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Manufacturing  method    

             1.  Alkyl-­‐Aryl  sulfonates  

   The  steps  involved  in  the  manufacture    of  Alkyl-­‐Aryl  sulfonates  are  as  follows  

   (a)  Conversion  of  hydrocarbon  (paraffin)  to  alkyl  chloride  

   (b)  Alkyla;on  of  Alkylchloride  yields  Aryl-­‐Benzene  compounds  

   (c)  Aryl-­‐Benzene  compound  on  sulfona;on  in  presence  of  oleum  yields    

     detergents  (Aryl-­‐Benzene  sulfonate)  

     

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10. Methods of production-Detergents

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11. Methods of production-Glycerin

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12. End Uses – Soaps and Detergents; Glycerin A  par;al  list  of  soaps  and  detergents;  glycerin  is  given  to  show  the  diversity  of  applica;on  

Glycerin    Alkyl  resin  and  Plas;cs    Tobacco  humidifica;on  Cellulose  Plas;cizer  Explosives  Food  and  Pharmaceu;cals    

Soaps  and  detergents    Tex;le  manufacture    Sanita;on    Food  processing    Shaving  soaps    Synthe;c  rubber  and  plas;cs  emulsion  polymeriza;on    Paints  -­‐  water  emulsion  formula;ons    Paper  -­‐  Applica;on  of  sizing    

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Starch Manufacture – Manufacture

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General  process    

Balasubramanian  S  

Process  

Maize  

Sulfur  dioxide  

Air    

Water    

Steam  

Starch    

Germ  to  maize  oil  processing      

Steep  water    

Gluten  (Water  insoluble)  

Byproducts  

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Starch Manufacture

30  Balasubramanian  S  

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Starch Manufacture-Process description

31  Balasubramanian  S  

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14. References

1.  Dryden  C.  E,  Outlines  of  Chemical  technoloy  –  for  the  21st  Century,  3rd  edi;on,  East-­‐West  Press  (2004)  

2.  Aus;n  G.  T,  Shreve’s  Chemical  Process  Industries,  5th  edi;on,  Mc  Graw  Hill  Interna;onal  edi;ons  (1984)    

3.  United  States  Department  of  Agriculture,  Oil  seeds:  World  markets  and  trade  report.  

4.  h_p://www.mapsofindia.com/indiaagriculture/oil-­‐seeds/soyabean-­‐growing-­‐states.html  

5.  h_p://www.mapsofindia.com/indiaagriculture/oil-­‐seeds/soyabean-­‐growing-­‐states.html  

6.  h_p://www.wishh.org/aboutsoy/composi;on.html  7.  h_p://en.wikipedia.org/wiki/Pliny_the_Elder  8.  h_p://en.wikipedia.org/wiki/Michel_Eugène_Chevreul  9.  h_p://en.wikipedia.org/wiki/Nicolas_Leblanc  10. h_p://en.wikipedia.org/wiki/Ascanio_Sobrero  11. h_p://en.wikipedia.org/wiki/Alfred_Nobel  


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