Propane-Propane-97% Butane 2%

Iso Butane-Propane up to 1% Butane 97%

N-Butane-

Commercial Propane

Commercial Butane

LPG

31410m3 water capacity x 2 Nos refrigerated storage tanks

710m3 water capacity x 2 Nos Moundaed bullet

800 MT per Lne x 2 Lines

20000 MT average total cargo(Propane 9500 MT @ -37 Deg.C & Butane10500 MT @ 2Deg.C.

8 Nos Present + 8 Nos Future

168 MT /Hr. Present + 168 MT/Hr Future

2 Shifts / 300 Days /Year (3 Shifts to be considered fo rdesign)

1 Hr (45 Minutes for filling 21 MT & 15 minutes for preperation)

Above ground Insulated (~3KM), Piggable. for future usere a branch have provided on landfall after trestle with two isolation valve os branch connection can be done in future.

By marine Loading /Unloadiong arms

700 M3 /Hr in ships

2500 MT averge cargosize x 52 Vessels/Year

11 Hours Cycle time (including 7.5 Hrs. Loading)

130000 MT /Annum re export fascility

1.4 Million MT / Annum with 2 shift operation

Typical C forms ships shall be used for design

Fire fighting & statutory approval by Port

Marine Loading arm for Ship Loading & Unloading

ESD systym at Jetty. The communiaction of Jetty to Terminal will be by Walky talky( Wireless set -FLP)

Common line for receipt & re export

Vapour balanceing shall be considered for product re export through ships & barges

All storage Refrigerated & Pressure vessels are propane rated.

Fire fighting shall be by fresh water & Storage shall be planned for 4 hours

GC for quality control for incoming, Storage & final product testing

System designed based on

100% back up Dg shall be provided. 1 additional smaller back up DG shall be provided to take care of emergancy loads required only fo rmaintaining safe storage condition in refregerated tanks. i.e. electrical load required to maintain refregararated tank pressure with all other operations stopped will have 200% back up.

Plant have full Automated control & ESD (Emergancy shut down.

Coldflare shall be provided for overpressure relief

Above ground diesel storage of 15 KL

safety valve relief shall be directly vented to amosphere. Emergancy vent shall be by remote operated On off valve which will routed to cold flare

Oil water seperator planned. ETP not envisaged

Nitrogen generator(PSA) planned with utility points at criticfal locations and also to vent stack.

Boil Off gas & Displaced gas recovery

Heating for tanker Unloading

Cryogenic tank unloading Pump

Cross country Line sizing