Moving on to two other strategy that will be used in safety which are Active and Procedural.
These  strategies  will  encompass  of  several  layers  of  protection  (LOPA).  Before  proceeding  to  the 
factors and solution to the disaster, we shall see the consequence of the Bhopal incident brought to 
the surrounding people.  
Bhopal  gas  tragedy  as  called  by  many  is  a  gas  leak  incident  that  occurred  in  India.  It  is 
currently  classified  as  the  worst  industrial  disaster  in  human  kind.  It  happened  on  the  night  of  2
nd
 
and  3
rd
  of  December  1984  in  the  pesticide  plant  of  Union  carbide  India  limited  (UCIL)  in  Bhopal, 
Madhya  Pradesh,  India.  This  extremely  dangerous  event  happened  as  it  released  40    45  tons  of 
extremely  toxic  Methyl  Isocyanate  (MIC)  and  other  gases  in  the  villages  around  the  plant.  It  was 
estimated that the affected area was about 40 sq km. 
In  this  section  it  will  divided  into  two  strategies  where  we  will  discuss  the  incident  if  there 
are  Active  and  Procedural  strategy  applied  in  operating  this  plant.  Starting  with  the  factors  of  the 
incident and next to discuss solution based on Layer of Protection (LOPA) module. 
Active  is  a  mainly  about  control,  safety  interlock,  automatic  shutdown  systems.  It  can  also 
be  defined  that  preventing  accidents  by  using  detector  or  sensor  that  can  identify  the  problem  to 
mitigate the consequences of accident and of course preventing accident itself. 
For  Bhopal  causes  one  of  them  is  the  failure  of  after  tank  safety  process  (leak  mitigation 
process).    There  are  possibilities  that  the  water  enters  the  storage  tank  and  run    away  reaction 
occurs, refrigeration system fails to keep low temperature inside the vessel, for preventing explosion 
to occur a safety valve  will be  opened. This valve  is a type  of rapture disc to allow  the gas to go to 
the next mitigation step. Next will be the vent gas scrubber. This scrubber will work as the gas will be 
entered from its lower part and it will be sprayed by caustic soda solution which can neutralize the 
MIC and convert it to harmless material. If it is not enough, then the residual will need to be sent to 
the  flare  which  will  burn  any  MIC  and  convert  it  to  be  CO
2
  gas.  For  this  type  of  solution  it  can  be 
classified as the manual intervention that need to operate when failure happen. 
However  for  as  the maintenance  for  this  safety  operation was  not  close  to  good  condition. 
MIC storage tank alarms did not work for 4 years and there was only one feedback system while in a 
similar  plant  in  US  there  were  4  feedback  systems.  Plus,  there  were  not  storage  tank  prepared 
between  the  large  storage  container  and  the  MIC  production  unit to  check  its purity.  On  the other 
hand reserve tank built was full with MIC whilst it should be emptied to allow evacuation of some of 
the MIC from the other tank to reduce the pressure. 
For  the  sake  of  minimizing  operating  cost,  the  refrigeration  unit  was  shut  down  by  setting 
the  temperature  set  point  to  20
o
C  instead  of  the  4.5
o
C  as  recommended  in  the  operating  manual. 
The  Freon  liquids  that  need  to  be  used  for  MIC  cooling  was  drained  and  used  within  the  plant. 
Therefore,  MIC  was  stored  without  cooling,  and  if  a  run-away  reaction  event  should  occur,  no 
cooling was available. 
In  addition  to  that,  there  should  be  slip  blind  plates  that  could  be  one  of  the  preventing 
measures  for  cleaning  water  in  the  pipes  from  entering  MIC  tank.  However  these  plates  were  not 
installed  and  their  installation  was  ignored  from  the  maintenance  checklist.    As  for  the  scrubbers  
were  not  well  maintained,  moreover  they  were  not  even  working,  during  the  disaster  it  was  in 
standby mode. MIC gas could not be neutralized it with caustic soda. Even it was activated, it could 
not  neutralize  a  huge  volume  of  MIC  gas  released  by  the  tank.  Compared  to  plant  in  USA  it  had  4 
times the number of vent gas scrubbers in the Bhopal plant. 
For the flare tower was out of service for five months before the disaster because a length of 
piping  was  corroded  and  was  not  replaced  in  contrast  similar  plant  in  USA  has  two  flares.  Material 
used for safety valves  and pipes  in the factory were corrodible when exposed to acid. This was the 
main  reason  for  the  safety  devices  malfunction.    Other  than  that  the  existence  of  Iron  Oxides  with 
water which entered the MIC tank acts as a catalyst accelerates its chemical reaction with water. 
These are  the  problems that  can be  found in the controls system and safety measures  that 
can be very important in plant safety. The lack of critical alarms and operator supervision which are 
part of the layer in LOPA was being omitted by the plant management. 
In Procedural strategy it mainly consists of standard operating procedures (SOP), safety rules 
and  standard  procedures,  emergency  response  procedures  and  training.  Base  on  the  paragraph 
above  we  can  conclude  that  plant  management  failed  to  follow  the  standard operating  procedures 
of certain processes which cause the plant to explode. 
In  Bhopal  incident  there  were  different  numbers  victims  estimated.  The  official  number  of 
immediate  deaths  was  2259.  Also  some  stated  that  other  8000  died  after  two  weeks  and  another 
8000  died  as  a  result  of  diseases  related  to  exposure  to  the  gas.  This  shows  that  the  lack  of  plant 
emergency  response  and  also  community  emergency  response  are  almost  not  existed  which  cause 
this huge number of deaths.  
At time when this event occurred there are about 40 to 45 tons of MIC released out of the 
vent gas scrubber. The gas is heavier than the air settled down and pushed by a gentle wind towards 
Bhopal  city.  It  was  too  late  for  the  people  in  the  city  to  react  as  the  gas  arrived  and  they  were 
suffocated. There was no warning or any emergency plan to evacuate the people as soon as possible. 
The  lack  of  community  response  was  poorly  shown  by  the  developer  of  the  plant  as  it  has  not 
calculated  the  risk  for  the  surrounding  community  that  live  near  the  plant.  Bad  turn  to  be  worst 
when victims arrived to the hospitals, the doctors didnt know how to deal with this poisonous gas. 
The  plant  should  have  been  providing  the  medical  manual  to  the  nearby  hospitals  in  case  that  the 
gas was released. There are none provided.  
Workers  in  that  plant  were  not  given  any  rewards  which  turn  them  to  behave  in  bad 
manners and cause some the good employees to quit. In addition the manual given were in English 
even  some  of  them  hardly  understand  it.  Training  should  be  given  to  the  workers  and  also  the 
proper safety procedure should be followed in order this plant to comply the LOPA. 
Conclusion that  can  be  made  from  this  accident, clearly  it  was  from the  poor management 
systems.  The  safety  process  designs  were  omitted  as  they  were  try  to  imitate  the  plant  in  West 
Virgina  but  made  it  in  wrong  ways.  They  ignored  process  and  personnel  safety  regulations.  Lastly, 
Both Indian government and Union Carbide Corporation gave the priority to the profit. They did not 
wary a lot about the life of indian citizens.