GAIL is the first company in India to own and operate pipelines for LPG transmission. It has 2040 km LPG pipeline network 1,427 km of which connects the western and northern parts of India and 610 km of networks is in the southern part of the country connecting Eastern Coast. GAIL has dedicated LPG pipelines from GPU, Gandhar (1 Km length) and GPU Vijaipur to OMC Bottling plants (2 Km length). The LPG transmission system has a capacity to transport 4.58 MMTPA of LPG.
GAIL is augmenting Jamnagar-Loni Pipeline capacity from 3.25 MMTPA to 6.5 MMTPA. GAIL is also executing Uran-Usar Propane pipeline and Vijaipur-Pata C2/C3 pipeline.
| S.No | LPG Pipeline Network | Length (KM)* |
|---|---|---|
| 1 | JAMNAGAR - LONI LPG PIPELINE | 1427 |
| 2 | VIZAG - SECUNDERABAD LPG PIPELINE | 610 |
| 3 | GPU VIJAIPUR - IOCL BP LPG PIPELINE | 2 |
| 4 | GPU GANDHAR - IOCL BP LPG P/L | 1 |
| Total Length | 2040 | |
| Start Point | RIL Jamnagar, EOL Vadinar and Import terminal at IOCL Kandla |
| End Point | Loni near Ghaziabad, UP |
| En-route TOPs' | Ajmer & Jaipur in Rajasthan, Piyala & Gurgaon in Haryana, M' Khadar in Delhi & Loni in Ghaziabad (U.P) |
| Length of P/L | 1427 KM including spur pipelines |
| Throughput Capacity | 3.25 MMTPA |
| Start Point | Vizag-HPC Refinery/EIPL Import facility/Cavern storage facilities |
| End Point | Secunderabad, Near Hyderabad |
| En-route TOPs' | Rajahmundry & Vijayawada and Cherlapally (Secunderabad) |
| Length of P/L | 610 KM |
| Throughput Capacity | 1.33 MMTPA |
For use in household
For use in hotels, bakeries, canteens, etc
For use as fuel in automobiles
For use in production process
| Sr. No. | Property | Data |
|---|---|---|
| 1 | Chemical Formula | Mix of mainly C4H10& C3H8 |
| 2 | Boiling Point | (-) 20 0C to (-) 27 0C |
| 3 | Explosive Limit | 1.5 - 9.0% |
| 4 | Vapour Density(Air=1) | 1.8 |
| 5 | Specific Gravity(Liquid) | 0.53 - 0.54 |
| 6 | Appearance | Colourless |
| 7 | Odour | Odourless** |
| 8 | Physical State | Compressed Liquid |
| 9 | Vapour Pressure at 40 0C | 1050 KPa(Max) |
| 10 | Calorific value ( gross) in Kcal/kg | 11900-11950 |
| Sr. No. | Chemical Composition | Unit | Specification (As per IS 4576) |
|---|---|---|---|
| 1 | Composition, liquid mol percentage C2 Hydrocarbons C3 Hydrocarbons C4 Hydrocarbons C5 Hydrocarbons Unsaturated Hydrocarbons OR Volatility : evaporation temperature in deg. C, for 95 percent by volume at 760 mm Hg pressure, Max |
Vol. % | Report ( 0.2 to 1 % max) Report ( 35 % to 65% ) Report (35% to 50%) 2.5 Max Report 2.0 |
| 2 | Hydrogen Sulphide (H2S) | ppm | < 5 ppm ( Pass) |
| 3 | Total Sulphur after odorizing | ppm | 150 max |
| 4 | Moisture | Free water content - none | |
| 5 | Copper strip corrosion | Not worse than No. 1 |