Page 193 - CTB_Engilsh_Web_Version1
P. 193

Panipat Refinery, Technology with Ecology at Heart






 Growth Timeline  2010                                                                                   2013


              Þ The Naphtha Cracker Complex which is one of                                             Butadiene
                 the largest of its kind in India comprising                                            extraction unit
 1998  1999      Naphtha Cracker Unit (NCU), NCU associated                                             (BDEU) was

                 units, High Density Polyethylene (HDPE) Unit, Swing                                    commissioned in
 Panipat Renery is   The major secondary processing units of   (LLDPE/HDPE) Unit, Mono Ethylene Glycol (MEG)   October 13 for
 IndianOil's seventh and the   the Renery include Catalytic Reforming
 technically most advanced   Unit (CCRU), Once through Hydrocracker   Plant, Polypropylene (PP) line 1& Line 2 Units and Utilities   extracting 1,3-Butadiene
                 including Captive Power Plant was commissioned between                                 from cracked C4s. 1, 3
 public sector renery complex   unit (OHCU), Resid Fluidised Catalytic
 of India. Renery was set up on   Cracking unit(RFCC), Visbreaker unit (VBU),   March 2010 to May 2010. The world-class Panipat Naphtha Cracker   Butadiene is used for
 July 12, 1998 with the   Bitumen blowing unit (BBU), Sulphur block and   was built at a cost of INR 14, 439 crore. The project is a cornerstone for   production of Styrene Butadiene
                                                                                                        rubber by neighboring M/s ISRPL.
                 IndianOil's entry into petrochemicals and forms a new business line for
 commissioning of rst 6.0 MMTPA   associated Auxiliary facilities. In order to improve
 Crude Distillation Unit on October 2,   diesel quality, a Diesel Hydro Desulphurisation Unit   growth  Butadiene is also sold to domestic
 1998 and 3.3 MMTPA Vaccum Distillation Unit   (DHDS) was subsequently commissioned on July 12, 1999. The   Þ Further, to meet the potential demand renery capacity again augmented   customers
 on October 11, 1998. It has a capacity to   process of desulphurisation through the DHDS enables the   to 15.0 MMTPA in December, 2010
 process a wide range of both indigenous and   reduction of sulphur content in diesel, resulting in positive
 imported grades of crude oil.  It has grown up   environmental protection results in the control of automotive
 using world-class technology from Axens,   emissions. When the commissioning was formalised, the
 Haldor-Topsoe, UNOCAL/UOP, Stone &   renery became the fastest commissioned DHDS plant in the
 Webster, Lummus Global and Technip  country  2014                                    2017


              Butene-1 Unit was commissioned                                          Sale of surplus Butene-1 was
              in May 2014. Butene-1 is                                                started
 2006  2009   produced in the unit by
              dimerization of ethylene. After
 With a view to meet the growing decit of   Motor Spirit   commission of Butene-1 unit, import
 petroleum products, especially in the Northern   Quality   was stopped
 region of the country, the capacity of Panipat   Upgradation
 Renery was expanded to 12 MMTPA in June, 2006   project with
 under Panipat Renery Expansion Project (PREP).  In   Naphtha
 expansion project 6.0 MMTPA Crude Distillation Unit-II   Hydrotreating unit
 and a full conversion hydrocracker as the secondary   (NHDT), Isomerization
 processing unit, Delayed Coker unit for bottom processing   (ISOM), FCC Gasoline   2018  2019
 and associated Auxiliary facilities commissioned. IndianOil stepped into   Desulphurization unit
 the Petrochemical venture by setting up a Linear Alkyl Benzene (LAB)   (Prime G) was   Naphtha Cracker Unit (NCU)   PNC has achieved highest ever
 plant at Gujurat Renery in 2004. Subsequently in the year 2006, a   commissioned in   Expansion project was approved   Naphtha processing (3027 TMT)
 facility for manufacturing Puried Terephthalic Acid (PTA) at Panipat   Deember 2009 for   by Board in August. The project   and highest ever polymers
 Renery was setup. A Para-xylene complex was setup to make the feed   production of BS-IV   includes NCU Ethylene capacity   production (1357 TMT)
 for the PTA plant. The plant is licensed by M/s UOP, USA. PX-PTA block   quality compliant MS  enhancement from 857 kTA to 970 kTA
 comprised of Naphtha hydrotreating unit (NHT), continuous catalytic   by integration of Panipat renery off
 reformer, Benzene toluene fractionation unit (BTF), sulfolane unit, Trans   gasses from FCCU & DCU. The project
 alkylation disproportionation (TATORAY) and Paraxylene recovery unit   includes Ethylene Recovery Unit (ERU), NCU Expansion,
 (PAREX) commissioned during May-November 2006  BEU Expansion and MEG Expansion




 190 IndianOil Reneries                                                                                                      IndianOil Reneries  191
   188   189   190   191   192   193   194   195   196   197   198