Page 6 - LSR on Servocyclotherm G
P. 6

I n t r o d u c t i o n   o f   S e r v o c y c l o t h e r m   G   a t   D i g b o i   R e f i n e r y   An Import Substitution
                  Introduction of Servocyclotherm G at Digboi Refinery – An Import Substitution








               INTRODUCTION


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                                                                               processes
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               I In petroleum refining world, waxing (or de-oiling) and dewaxing processes are two sides of the

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               same coin. When we manufacture paraffin wax or lube base stock, we normally adopt the process
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               s same coin. When we manufacture paraffin wax or lube base stock, we normally adopt the process
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               on scraped surface heat exchangers (chillers).  All lube stocks, except those from a few highly
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                                                                                cept those from a few highly
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               n naphthenic crude oils, must be dewaxed or they will not flow properly at ambient temperatures.

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               naphthenic crude oils, must be dewaxed or they will not flow properly at ambient temperatures.


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               T h e r e   a r e   t w o   t y p e s   o f   p r o c e s s e s   i n   u s e   t o d a y .   O n e    selective hydrocracking process to crack
               There are two types of processes in use today. One uses selective hydrocracking process to crack
                                               c bons. The other uses refrigeration to crystallize the wax and
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               the wax molecules to light hydrocarrbons. The other uses refrigeration to crystallize the wax and
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                           s solvent to dilute the oil portion sufficiently to permit rapid filtration to separate the
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               mixing with solvent to dilute the oil portion sufficiently to permit rapid filtration to separate the
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                                  D Digboi  Refinery  uses  the  second  method  for  production  of  Praffin  Wax.

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               wax  from  the  oil.  Digboi  Refinery  uses  the  second  method  for  production  of  Praffin  Wax.  An
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                         i is given here to explain the working of Feed Scraper Chiller (FSC):

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               animation is given here to explain the working of Feed Scraper Chiller (FSC)::
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              In  Solvent  Dewaxing  Unit  (SDU)  of  Digboi
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              R   Refinery,  Inhibited  Ethylene  Glycol  based efinery,  Inhibited  Ethylene  Glycol  based
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              product  is  the  coolant  for  feed  chilling  in
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              the  2   and  3   feed  scraper  chiller.  This
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              Glycol  based  product  is  also  used  for
              G   l y c o l    b a s e d    p r o d u c t    i s    a l s o    u s e d    f o r
              cooling  of  the  solvent  i.e.  Methyl  Isobutyl
              c o o l i n g   o f    t h e   s o l v e n t   i . e .   M e t h y l   I s o b u t y l
              K   Ketone (MIBK) and Blow Gas chilling. etone (MIBK) and Blow Gas chilling. This
              c o o l i n g    a g e n t    i s    c o o l e d    i n    r e f r i g e r a t i o n
              cooling  agent  is  cooled  in  refrigeration

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              system  by  propylene  from  3  Deg  C  to  -6
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              Deg  C.  Thus  the  coolant  takes  away  heat
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                 f   from  processes  in  Feed  Scrapper  Chiller rom  processes  in  Feed  Scrapper  Chiller
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              ( (FSC),  MIBK  cooler  and  Blow  Gas  chiller.
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              The principal steps for deoiling at SDU are
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              shown in the flow diagram on the side:
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