Layout of the oil tank area
Thread Content
What are the considerations for the layout of oil tank areas?2. The total capacity of floating-roof storage tank groups should not exceed 200,000 m3.
3. The storage tanks within a storage tank group should be arranged in no more than two rows, and the number of tanks should not exceed 12. When the capacity of a single tank is 500,000 m3 or more, it should be arranged in a single row. Article 5.3.2 The fire separation distance between atmospheric-pressure storage tanks for Class A and Class B liquids shall not be less than the requirements specified in Table 5.3.2. Fire separation distance between atmospheric pressure storage tanks for Class A and Class B liquids Table 5.3.2 Note: ① In the table, D represents the diameter of the larger of the adjacent tanks; if the calculated fire separation distance is greater than 20 m, it may be set at 20 m. ②When the capacity of a single tank is less than or equal to 200 m3 and the total capacity is no more than 1000 m3, the fire separation distance for the storage tanks can be determined based on the requirements of production operations. Article 5.3.3 Fire dikes shall be constructed around Class A and Class B liquid storage tank groups. When the total capacity of the tank group is 20,000 m3 and there are more than two tanks, partition dikes shall be installed between the tanks within the fire dike, with a height that is 0.2 m lower than that of the fire dike. Article 5.3.4 The installation of fire dikes for Class A and Class B liquid storage tank groups shall comply with the following provisions: 1. The fire dike shall be closed ; II. The fire dike is a soil dike; when it is difficult to obtain soil, non-combustible materials such as bricks, stones, or reinforced concrete can be used, but soil should be piled up on the inner side ; III. The actual height of the fire dike should be 0.2 m higher than the calculated height; the recommended height for the fire dike is 1.0–2.0 m ; IV. The fire dike and separation dike shall be capable of withstanding the design hydrostatic column pressure of the liquid they contain ; V. The areas where pipelines pass through fire dikes should be filled and sealed with non-combustible materials ; VI. There shall be no less than two pedestrian stairs installed at different positions along the perimeter of the fire dike ; VII. No fewer than two pedestrian stairs shall be provided at different positions along the inner side of the fire dike ; 8. Rainwater discharge outlets located at the lower part of the fire dike should be equipped with adjustable shut-off devices. Article 5.3.5 The clear distance between the outer footline of the fire dike of adjacent tank groups shall not be less than 7 m. Article 5.3.6 A separate sludge tank with a capacity of 200 m3 or less may be exempt from having a fire dike. Article 5.3.7 The determination of the effective capacity within the fire dike shall meet the following requirements. 1. For fixed-roof storage tank groups, it shall be no less than the effective capacity of the largest tank within the group ; II. For floating roof tank groups, it shall be not less than half of the effective capacity of the largest tank within the tank group ; III. When fixed-roof storage tanks and floating-roof storage tanks are arranged in the same tank farm, the effective capacity within the fire dike shall be the larger of the values specified in the preceding two paragraphs. Article 5.3.8 The inlet pipe of the storage tank shall be connected to the bottom of the tank. Article 5.3.9 Liquefied petroleum gas and natural gas condensate storage tanks shall not be arranged in the same group as storage tanks for Class A and Class B liquids; the fire separation distance between them shall be determined in accordance with the provisions regarding liquefied petroleum gas tanks in the current **standard, the Code for Fire Protection Design of Buildings. LPG cylinders can be arranged in the same group as pressure-stored stable light hydrocarbon storage tanks, and the fire separation distance between them should not be less than the diameter of the larger tank among them. Article 5.3.10 A combustible gas concentration alarm device shall be installed within the protective wall of LPG tanks or natural gas liquefied gas storage tanks. Article 5.3.11 LPG or natural gas liquid storage tanks shall be equipped with safety valves, thermometers, pressure gauges, level gauges, and high-level alarms. Article 5.3.12 When the volume of a liquefied petroleum gas or natural gas condensate storage tank is 50 m3 or more, a remotely operated valve and an automatic shut-off valve should be installed on the liquid-phase outlet pipeline, and check valves should be installed on the liquid-phase inlet and outlet pipelines. Space at the bottom of the tank should be reserved for water pipe connections. Article 5.3.13: For all gaskets of the liquid inlet and outlet valves in liquefied petroleum gas and natural gas condensate storage tanks, spiral wound metal gaskets or metal-encased slate gaskets shall be used. Article 5.3.14 When cooling spray water is used for liquefied petroleum gas and natural gas liquid storage tanks, it shall be installed in conjunction with the fire protection cooling water system.