Library / © 2019 Department of Petroleum Resources. All rights reserved Department of Petroleum Resources (DPR) PROCEDURE GUIDE
© 2019 Department of Petroleum Resources. All rights reserved Department of Petroleum Resources (DPR) PROCEDURE GUIDE
Page 92 of 114
91 | P a g e 4 Dimensions Length: Upstream diameter: Downstream diameter: First pipe connection: Second pipe connection: Upstream pressure tap: Downstream pressure tap: D PRESSURE TAPS 1 Orientation 2 Location of static pressure transducer (upstream/downstream) 3 No. of pressure taps 4 Pressure tap size 5 Condition of tap hole edge 6 Temperature probe type E METER PARAMETERS 1 Minimum flow rate 2 Maximum flow rate 3 Meter factor 1.16 LNG OPERATIONS The LNG loaded at the loading points shall be measured in cubic meters by gauging LNG loaded in tanks of the LNG tanker vessel in accordance with ISO 10976:2015. 1. Each tanker should be equipped with level measuring device of different types capable of determining the LNG level to within accuracy equal to or better than ±7.5mm. The level of the liquid in the tank shall be determined by main primary capacitance measuring devices which give automatic readouts in the cargo control room, but if there is a failure, the level of liquid shall be determined by using the Auxiliary liquid level gauging device for the relevant cargo tank(s). For volume calculations, the gauging table shall convert the level of the liquid in tanks to the volume of that cargo tank using one (1) millimeter as the smallest unit of dimension. 1.16.1 QUALITY OF LNG FOR TRUCKING IN NIGERIA Quality of LNG loaded should: i. have a Gross calorific value (Volumetric) between 39.90 and 42.70 MJ/SCF on a dry basis ii. Not contain more than 1 (one) mol% of nitrogen Hydrogen Sulphide 5.0 mg/SCF Mercaptan sulphur 2.3 mg per standard cubic feet Mercury 50 mg per standard cubic feet Carbon Dioxide 0.1 mol per cent Carbonyl Sulphide plus Hydrogen 15.0 mg per standard cubic metre
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