| Scope |
The company invites all prospective suppliers and contractors for Supply of Hydrogenation Catalyst.
CATALYST LIFE 20MONTHS MINIMUM (WITHOUT REGENERATION) PALLADIUM CONTENT : 0.3 WT% PACKING TYPE : STEEL DRUMS PACKING SIZE : 113 KG NET WEIGHT OR 140 KG NET WEIGHT OR NEARBY SIZE IN STEEL DRUMS FOR OLEFINIC LPG SERVICE MAX FEED OLEFIN : 10% MOL PROD TOTAL OLEFIN: 200PPM MAX FOR REACTOR - 4407-D FEED RATE THE LPG HYDROGENATION SECTION IS DESIGNED TO PROCESS 3740 BPSD (24.77 M3/H) OF AN OLEFINIC C3/C4 STREAM PRODUCED IN THE CATALYTIC POLYMERISATION SECTION PRODUCT QULAITY:- TOTAL OLEFINS CONTENT, PPMW < 200 H2S, PPMW (B) < 1 MERCAPTAN SULPHUR, PPMW (B) < 5 TOTAL SULPHUR, PPMW (B) < 5 COPPER STRIP CORROSION TEST 1A REACTOR CONDITIONS-EXISTING/DESIGN:- CURRENT OPERATING TEMPERATURE (RIT) 145-155 DEG C (SOR OPERATING TEMPERATURE (RIT) 190 DEG C (EOR)-MAX DESIGN TEMPERATURE 300 DEG C DESIGN OPERATING PRESSURE 18.5 BARG DESIGN PRESSURE 28 BARG / FV DESIGN HYDROGEN FLOW 631 NM3/H HYDROGEN FLOW MAX 1100NM3/H NO. OF REACTORS 01 VOLUME OF CATALYST ~9.0M3 FOLLOWING IS REQUIRED TO BE ADDRESSED BY VENDOR: CURRENT OPERATING TEMPERATURE (RIT) SOR/EOR OPERATING TEMPERATURE (RIT) EOR DESIGN OPERATING PRESSURE SOR/EOR DESIGN HYDROGEN FLOW/ACTUAL HYDROGEN FLOW HYDROGEN CONSUMPTION NM3/M3 OF FEED AND TO BE INCLUDED IN PERFORMANCE GUARANTEE DEGREE OF EXPECTED EXOTHERM CATALYST LIFE (WITHOUT REGENERATION) POISONS FOR CATALYST
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