Library / GUIDE FOR THE ESTABLISHMENT AND OPERATIONS OF DOWNSTREAM GAS FACILITIES IN NIGERIA (LPG, CNG, LNG) ISSUED BY
GUIDE FOR THE ESTABLISHMENT AND OPERATIONS OF DOWNSTREAM GAS FACILITIES IN NIGERIA (LPG, CNG, LNG) ISSUED BY
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Applicable to all Oil & Gas Operators GUIDELINES FOR THE ESTABLISHMENT AND OPERATIONS OF A GAS RETICULATION FACILITY IN NIGERIA Code: DPR Guide 0028 - 2020 Revision Date: 1st September 2020 This is a property of the Department of Petroleum Resources. All rights reserved 10 ii. Hazardous areas are protected from sources of ignition. iii. There is safe access, routing, parking and exit for service vehicles and road tankers. 3. The facility’s dangerous areas shall be open air ventilated and clear of other buildings or obstructions that might otherwise adversely affect the ventilation. 4. Pipework, tanks to offset fill points, and vent pipes shall be routed and located to ensure protection from external effects or interference and to allow access if required. 5. The stand for delivering fuels into storage tanks shall be in the open, away from the facility buildings, and emergency escape routes, and be large enough to allow a road tanker to be positioned wholly within it during delivery. 6. Electrical connections shall be made in accordance with the manufacturer's instructions and shall maintain the integrity of the explosion protection. 7. The minimum separation distance in case of closeness to public and residential properties are as follows: Table 3.1 Minimum Separation Distances for Above Ground LPG Storage Tanks Capacity (Metric Tonnes) Separation Distance (Meters) from tanks to the line of Adjoining Properties, Control buildings, or fixed source of ignition. Of any single tank Of any group of tanks From Adjoining Property that May be Developed/Non- Public & Non- Residential From Public and Residential Boundaries Between tanks A: No fire wall B: With Fire wall A: No fire wall B: With Fire wall 0.1 – 5 0.1– 5 5 5 30 15 1.0 5.1 - 10 5.1 - 10 7.5 5 30 20 1.0 10.1 – 60 10.1 – 60 15 7.5 50 30 1.5 60.1 - 150 60.1 – 150 22.5 11 50 30 ¼ of sum of the diameter of 2 adjacent vessels 150.1 – 300 150.1 – 300 30 15 50 30
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