SY 5737-1995 Safety regulations for crude oil pipeline transportation
Some standard content:
Petroleum and Natural Gas Industry Standard of the People's Republic of China SY 57371995
Safety Regulations for Crude Oil Pipeline Transportation
1995-11-18 Issued
China National Petroleum Corporation
1996-05-15 Implementation
Cited Standards
Oil Pipeline Station
Oil Pipeline Pump
Heating Furnace
Oil Storage Tank
Crude Oil Loading and Unloading Trestle
Oil Pipeline
Instrument Maintenance and Repair
Fire Protection Facilities
Safety Management of Scientific Experiments and New Technology Promotion Objectives
Crude oil pipeline transportation is the middle link in the process of oil production and sales. It is also an important energy transportation artery of the country. At present, crude oil pipeline transportation has become an important part of the five major transportation industries in my country, but there is no systematic safety management regulation. In order to strengthen the safety production of crude oil pipeline transportation, this standard is specially formulated.
This standard is proposed and managed by Shixiu Industrial Safety Professional Standardization Technical Committee. Drafting unit of this standard: Safety Supervision Department of China Petroleum and Natural Gas Pipeline Bureau, main drafters of this standard Shen Jiren Chen Yanzeng Lu Shengqiu Scope
Petroleum and Natural Gas Industry Standard of the People's Republic of China Crude Oil Pipeline Transportation Safety Regulations
This standard specifies the safety technical requirements for onshore crude oil pipeline transportation. This standard applies to the entire process of commissioning and operation of onshore crude oil pipeline transportation. 2 Referenced standards
SY 5737--1995
The provisions contained in the following standards constitute the provisions of this standard through reference in this standard. The versions shown are valid at the time of publication of this standard: All standards will be revised, and parties using this standard should explore the possibility of using the latest version of the following standards. GBJ74-84 Oil depot design specification
GBJ140-90 Building fire extinguisher configuration design specification GB50151-92 Low-multiple foam fire extinguishing system design specification GB50183-93 Crude oil and natural gas engineering design fire protection specification SY/T0060-92 Oilfield anti-static grounding design regulations SY 0075-93 Fire dike design specification for oil tank area SYU031-95 Safety regulations for heating furnaces for oil industry SY5858--93 Safety regulations for industrial fires in oil enterprises SY5225-1994 Fire and explosion prevention and production safety management regulations for drilling, production, storage and transportation of oil and natural gas SY/T5920-94 Operation management specifications for crude oil depots SY/T5918-94 Technical regulations for major repairs of asphalt anti-corrosion layers of buried steel pipelines Regulations on the protection of petroleum and natural gas pipelines Order No. 33 of the State Council on March 12, 1989 3 Oil transportation stations
3.1 General safety regulations
3.1.1 The modification and expansion projects of oil pipelines and oil transportation stations shall comply with GB50183, and fire prevention and explosion prevention shall comply with SY5225. 3.1.2 The production area and living area of the oil transportation station shall be separated and have obvious safety signs. 3.1.3 The oil station should establish and improve the following safety management system: a) Three-level safety education system:
b) Personnel and motor vehicle station management system: c) Safety management system for external construction personnel: d) Job responsibility system:
e) Safety contract responsibility system for leading cadres
3.1.4 Gasoline, banana water and other organic solvents should not be used to clean equipment, clothes and the ground at the post, and flammable materials should not be placed on heat-carrying objects.
3.1.5 Fixed flammable gas alarms should be installed in the oil and gas area and checked regularly. 3.1.6 The oil product laboratory should have good ventilation facilities. 3.1.7 Fire in the production area shall comply with SY5858. 3.2 Trial operation and commissioning
Approved by China National Petroleum Corporation on November 18, 1995, implemented on May 15, 1996
SY 5737-1995
Before trial operation and commissioning, a trial operation and commissioning plan shall be formulated: it can only be implemented after approval by the superior competent department. 3.3 Process start-up, shutdown and switching
3.3.1 The operation and operation of the oil transportation process shall comply with SY/T59203.3.2 The operating parameters of the oil transportation process shall be controlled within the specified range. 3.3.3 In case of fire, explosion, oil leakage and other emergencies, timely measures shall be taken, and the communication between the upper and lower stations shall be strengthened, and dispatchers shall be dispatched to report to the superiors.
3.3.4 When the bypass oil tank process is running, it is necessary to prevent the bypass oil tank from being emptied or overflowing. 3.3.5 The temperature, flow rate and total output of the pipeline and reverse oil for positive and reverse alternating transmission should meet the safety requirements to avoid condensation. 3.3,6 The high and low pressure relief valves installed at the oil transfer station should be used for a long time and inspected regularly as required. 3.3.7 For pipelines and valves that have not been put into operation for a long time, in order to prevent the pipelines and valves from being pressurized and frozen, the lines should be swept or the pipelines and valves should be "activated" at regular intervals.
3.3.8 When the process is reversed, the control and display instruments should be sensitive and accurate, and should not be operated without protection and indication. 3.3.9 When the communication between the oil transfer station and the superior dispatch is interrupted, the station dispatcher should take the initiative to contact the upper and lower stations in reverse, maintain the source operation process production, closely monitor the changes in the operation parameters, and take emergency measures when abnormalities are found. If the upper and lower stations lose contact, the station pressure and the liquid level of the bypass oil tank should be closely monitored, and measures should be taken to prevent pressure and tank accidents. 4 Oil pump
4.1 Matters to be observed in the operation of the pump
4.1.1 Before starting the pump, the operator should make all preparations according to the operating procedures. 4.1.2 The turning, starting and stopping of the pump should be supervised. 4.1.3 The operator should strictly follow the dispatching order: when adjusting the operating parameters, the connection between the positions should be strengthened to prevent pressure holding and emptying.
4.2 Inspection and supervision of normal operation
The operator should check the operating and standby pumps one by one, item by item, and point by point in accordance with the regulations: if any problems are found, they should be dealt with in time, and relevant records should be kept.
4.3 Matters to be noted in the maintenance of the oil pump
4.3.1 The power supply of the motor should be cut off, and a warning sign of "strictly prohibited from holding the gate" should be hung on the corresponding switch cabinet. 4.3.2 The power supply of the inlet and outlet electric valves should be cut off, the valves should be in the closed state, the handles should be placed in the neutral position and fixed. 5 Heating furnace
1 General safety requirements
The use, management, inspection and scrapping of heating furnaces should comply with SY0031. 5.2 Inspection before opening the furnace
5.2.1 All parts of the furnace body, such as manholes, fire holes, explosion-proof doors, air regulators and emergency vent valves, should be complete and intact. 5.2.2 The heating furnace should be equipped with safety protection devices such as burner fire extinguishing, over-temperature alarm, and fuel oil high and low pressure alarms. 5.2.3 Crude oil, fuel oil, and heat medium systems should be unobstructed. 5.2.4 The new furnace is put into use according to 3.2
5.2.5 When adding heat medium to the heat medium furnace, the added heat medium should be dehydrated to ensure qualified quality. 5.2.6 Various instruments, automatic adjustments and protection devices should be complete and intact. 5.3 Safety requirements for shutdown and furnace shutdown
5.3.1 The operator shall execute the oil dispatching order and operate according to the start-stop steps of the operating procedures. 5.3.2 When starting the furnace, the communication between posts shall be strengthened, and the operation status of each system shall be closely watched: and the adjustment shall be made according to the specified process parameters. 5.3.3 When the fuel oil system is replaced with other fuels, in order to avoid sudden extinguishing due to operation fluctuations, inspection and monitoring shall be strengthened, and adjustments shall be made until the combustion is completely positive.
5.4 Inspection and monitoring during operation
SY 57371995
5.4.1 Daily inspections shall be carried out carefully, and attention shall be paid to the changes in various process parameters and operation status, and the operation parts shall be adjusted in time. And records shall be kept. 5.4.2 The temperature out of the furnace and the pressure difference between the inlet and outlet shall not be higher than the design specified value. 5.4.3 The temperature difference of the crude oil out of the parallel furnace tubes shall not be greater than the specified value to avoid bias flow. 5.4.4 The flame should not lick the furnace tube.
5.4.5 If a sudden fire is extinguished, the fuel oil valve of the burner should be closed immediately, and the source of the fire should be found and the fault should be eliminated. Before re-igniting the furnace, the furnace should be purged as required.
5.5 Emergency shutdown
When emergency shutdown is required due to an accident, different types of heating furnaces should be executed according to their respective operating procedures. 5.6 Treatment of oil leakage and rupture of furnace tubes
When oil leakage is found in the heating furnace, the oil transportation operation mode should be changed in time: and the following measures should be taken: a) Close the fuel oil valve:
b) Close the inlet and outlet valves of the accident furnace tube
Open the emergency vent valve:
d) Carry out furnace tube sweeping;
e) Cut off the power supply of the fan, close the burner nozzle, the secondary air door f) Use steam or fire extinguisher to extinguish the fire
6 Oil storage tank
6.1 Operation of oil storage tank
6.1.1 After the completion of the oil tank, it should be accepted by the safety, fire protection and other relevant departments before it can be put into operation. 6,1.2 Operators should be familiar with the process flow of the tank area and the purpose of each valve, 6.2 Safety accessories of oil storage tank
6.2.1 The safety accessories of the arched roof oil tank (including breathing valve, safety valve, flame arrester, light transmission hole, anti-soft connecting pipe, cooling spray and fire foam pipeline, air foam generator) and the safety accessories of the floating roof oil tank (including central drain pipe, cooling spray and fire foam pipeline air foam generator) should be complete and in good performance. 6.2.2 The accessories of the oil tank should be inspected regularly and any problems found should be rectified immediately. 6.3 Lightning protection and antistatic facilities
6.3.1 The lightning protection facilities for oil tanks shall comply with GBJ74, and the antistatic grounding shall comply with SY/T00606.3.2: The lightning protection and antistatic facilities for oil tanks (including lightning arresters, eliminators, antistatic grounding, antistatic soft connections of buoys and oil baffles) shall be inspected every quarter. The grounding resistance should be measured once in spring and autumn respectively. The resistance value should not exceed the design requirements. 6.3.3 The weight of the oil dipstick should be made of copper metal and the measuring port should be equipped with a non-ferrous metal bushing. 6.4: Firebreaks and fire roads in oil storage areas 6.4.1 The firebreaks of oil tanks or oil tank areas shall comply with SY00756, 4.2 The fire roads in the tank areas shall be kept unobstructed. 6.5 Oil tank operation inspection
6.5.1 To prevent the oil tank from overflowing and pumping out cancer, the liquid level should be controlled at the prescribed safety height. 6.5.2 The base oil hole and light hole of the oil tank should always be covered. 6.5.3 The operating oil should be checked every 2 hours. 6.5.4 The L tank should comply!
a) Use explosion-proof flashlights when loading tanks at night;
b) The number of people loading tanks at a time should not exceed 5;
SY 57371995
c) Do not load tanks when there is a thunderstorm or a strong wind of level 5 or above; d) Do not wear shoes with nails when loading tanks.
6.5.5 When draining water from the oil tank, a designated person should be responsible. 6.5.6 The oil storage tank should be maintained at the specified temperature. 6.5.7
The breathing valve should be checked at least twice a month in winter, and the ignition coil should be checked at least once a season. 6.5.8 The oil tank should be kept free of snow, water and oil. 6.6 Oil tank maintenance
6.6.1 A maintenance plan should be formulated when the tank is overhauled. The plan must include clear safety measures and must be submitted to the relevant departments for approval. 6.6.2 Fire in the oil tank area shall be carried out in accordance with SY5858.
7 Crude oil loading and unloading trestle
7.1 General safety regulations
7.1.1 The two sides (from the outer rail) and the two ends (from the first support) of the loading and unloading trestle are within 20m as "no fireworks" areas. At the main entrances and exits of the trestle, eye-catching "no fireworks" signs should be set up. 7.1.2 The locomotive head of the tank truck should not enter the "no fireworks" area. Smoking area". When picking up or dropping off tank trucks, the locomotive head should tow an isolation vehicle as required. 7.1.3 Flammable materials should not be stored in the "No Smoking Area" of the trestle, the roads should be kept clear, there should be sufficient lighting when loading and unloading oil products at night, and the locomotive entry and exit signals should be kept intact.
7.1.4 When loading and unloading crude oil, no motor vehicle should enter the "No Smoking Area" of the trestle. 7.1.5 Loading and unloading should be suspended in case of rain and wind speed of level 5 or above. 7.1.6 All electrical equipment on the pier must comply with explosion-proof regulations. Electrical equipment maintenance and light bulb replacement should not be performed while power is on. Explosion-proof flashlights should be used on trestles and tank trucks.
7.2 Connection, grounding and testing of anti-static equipment 7.2.1 Metal spanning connections should be used at each rail connection and crane pipe flange of the trestle, and a grounding point should be set up every 200ml. 7.2.2 The oil loading and unloading crane pipe should use a special filter hose with a copper end inside to conduct away static electricity. Anti-static facilities should be in accordance with SY/T00607.2.3. The grounding resistance of the grounding point should be measured once every quarter, and the resistance value should not be greater than 102. 7.2.4 When loading and unloading oil on the trestle, high positive steam should not be used to blow on the oil tanker and the trestle. Remove oil stains and prevent static electricity from causing fire.
7.3 Inspection before oil filling
7.3.1 The crane pipe should always be kept in a safe position. There should be no obstacles on the track. 7.3.2 Before loading and unloading, the tank car's roof, iron ladder, pedal, car cover gasket and bottom valve should be inspected and confirmed to be qualified before oil can be loaded. 7.4 Oil loading operation
Oil loading operation shall be in accordance with SY/T5920
7.5 Pier fire-fighting roads and fire-fighting facilities
Pier fire-fighting roads and fire-fighting facilities shall be in accordance with GB50183. 8 Valves
8.1 Inspection and operation of electric shelves
8.1.1 The lubricating oil of the oil cup shall meet the requirements. 8.1.2 The limit switch, valves and parts of the electric valve should be intact. 8.1.3 The operation of the electric valve should be carried out according to the operating procedures. 8.2 Safe operation of hydraulic ball valves and flat gate valves. Hydraulic ball valves and half-plate gate valves should be fully opened or closed during operation (excluding regulating valves). After the manual valve is opened, the handwheel should be returned half a turn to one turn.
9 Oil pipeline
9.1 Inspection and maintenance of pipeline
SY 5737—1995
9.1.1 The oil pipeline (including underground pipelines, rivers, railways, highway crossing sections and line valve rooms) should be implemented in accordance with the requirements of the State Council's "Regulations on the Protection of Petroleum and Natural Gas Pipelines": 9.1.2 Guards should be posted at key crossing sections 9.1.3 The inspection of pipelines includes the following: a) Whether there are trenching, earth excavation, mountain quarrying, mining, house building, threshing grounds, feeding grounds, pig hunting pens, hotbeds and other structures within the pipeline safety protection zone: | |tt||b) Are there any fruit trees (forests and other deep-rooted crops) planted in the pipeline safety protection zone, any piles, stones or bricks piled, or other materials that may affect the pipeline line and pipeline maintenance? c) Are there any stones or bricks removed, doors and windows damaged, or pipeline signs and notice boards damaged in the pipeline ancillary projects, facilities (such as various retaining walls, water-passing pavements, slope protection, etc.) and line valve rooms? d) Are there any blasting operations or planning of human-shaped engineering facilities within 200m on both sides of the pipeline centerline? e) Are there any pipes along the pipeline?
9.1.4 Inspection and examination of pipeline crossing and spanning sections Contents a) Inspection and examination of the integrity of pipeline crossing and its ancillary facilities. If any damage is found, it should be repaired in time. If it cannot be restored, it should be reported to the superior immediately.
b) For major pipeline crossing river sections, water level should be regularly observed during flood seasons, flow rate, velocity and other data should be collected, and flood situation should be reported at any time.
c) Regular inspection and monitoring of pipeline burial depth, exposed pipes, stability of pipeline crossing protection projects and river channel changes should be carried out. d) "No passage" signs should be set up on both sides of the crossing pipeline section to prevent pedestrians from passing directly on the upper part of the pipeline. Regular inspection of crossing and spanning sections Corrosion of pipeline supports, fixed piers, hangers, traction elements and steel casings; whether there are any docks, anchoring, blasting, dredging, sand panning, stone and dredging and deepening operations in the underwater pipeline safety protection zone.
9.1.5 The oil pipeline trunk line should be inspected regularly. 9.1.6 When inspections reveal pipeline leaks, man-made damage or other incidents that threaten pipeline safety, the site should be protected, timely measures should be taken, and reports should be made to superiors. Oil leaks across large rivers should be notified to relevant departments in a timely manner. 9.2 Trunk Pipeline Cleaning
9.2.1 A scientific and reasonable cleaning schedule should be formulated for pipeline cleaning 9.2.2 For pipelines that are not cleaned for a long time, a cleaning plan should be formulated before cleaning, and it should be implemented after approval by the superior competent department. 9.2.3 The cleaning operation procedures should be strictly followed during cleaning. 9.3 Preventing pipeline condensation
9.3,1 The oil flow rate and inlet temperature of the oil pipeline shall not be lower than the prescribed minimum flow rate and minimum inlet temperature. 9.3,2 When the pipeline needs to be stopped for planned maintenance, the stop time shall not exceed the allowed stop time for oil transportation. 9.3.3 For pipelines with small flow and low oil temperature, if signs of initial condensation are found during operation, the operating parameters should be adjusted immediately to prevent condensation. 9.3.4 For the pipe section where initial condensation occurs, Immediately take measures to increase pressure and increase temperature, and continue to squeeze at the maximum outlet pressure and temperature allowed at the accident station. If it is ineffective, further formulate squeezing or replacement measures and report to the relevant superior departments for approval and implementation. 9.3.5 When the hot oil pipeline that uses heat treatment, chemical repellent treatment and other cooling methods needs to change the oil transportation process, it should be implemented in accordance with relevant process regulations. And try to maintain a smooth transition during the pipeline transportation process. 9.4 Pipeline maintenance and emergency repair
9.4.1 Trench excavation
9.4.1.1 When excavating the trench, SY/T5918-94 shall be followed in accordance with 9.4.1.1 5737:-1995
9.4.1.2 When digging at the edge of a narrow passage or traffic path, fences and safety warning signs should be set up, and red lights should be set up at night. 9.4.1.3 When unexpected and unrecognizable facilities or objects are found in the excavation area, the operation should be stopped immediately. Report to the relevant superior departments for handling.
9.4.1.4 When it is found during excavation that the soil may collapse, large rocks may slide or cracks may occur, the operators should evacuate immediately and take safety measures before continuing the construction.
9.4.1.5 When working near towers, electric poles, railways, underground buried objects, communication and power lines, or other buildings, the pipeline technical files should be consulted in advance, and the relevant departments should be contacted to follow the safety instructions before construction. 9.4.2 Repair of pipeline anti-corrosion coating
9.4.2.1 When boiling and applying asphalt anti-corrosion coatings, masks and protective clothing should be worn to prevent burns and poisoning. During boiling operations, operators should stand on the upwind side.
9.4.2.2 During the repair process of other anti-corrosion coatings, corresponding safety measures should be taken according to the different properties of the coatings to ensure the safety of the operators.
9.4.3 Pipeline emergency repair
9.4.3.1 Pipeline emergency repair machinery and equipment should be complete and in good condition ready for use at any time. 9.4.3.2 Oil transportation enterprises should set up full-time emergency repair teams and conduct technical training regularly. 9.4.3.3 At the accident site, protective measures should be formulated to prevent idle personnel from entering the accident area, and security and fire prevention measures should be formulated. 9.4.3.4 The on-site leader should review the safety measures and issue a fire permit for on-site fire. 9.4.3.5 Before the emergency repair work of the non-stop pipeline F., the elevation of the pipeline, the dynamic pressure and flow rate of the pipeline and the wall thickness of the pipeline at the station where the accident point is located should be found out. Www.bzxZ.net
9.4.3.6 Before welding, the concentration of combustible gas around the welding point should be measured and protective measures should be formulated. During the welding operation, the welding point and possible leakage should be tracked and monitored. 9.4.3.7 For sudden pipeline rupture accidents, emergency measures should be taken immediately to reduce the leakage of pipeline crude oil and prevent the main condensate pipe. 10 Instrument maintenance and repair
10.1 Instrument maintenance and commissioning
10.1.1 Before work, the operating status of the process and equipment should be understood. 10.1.2 When disassembling and installing a primary instrument or component, the measured medium passage and the instrument power source should be cut off. On-site operation should be supervised by someone to prevent the breakage of pipe threads or welds.
10.1.3 Before setting the instrument parameters in the monitoring system or the regulating system, the instrument should be separated from the monitored equipment.10.2 Instrument maintenance in flammable and explosive places
10.2.1 The instrument cover should not be opened for maintenance or adjustment when it is powered on.10.2.2 Explosion-proof tools should be used when maintaining the instrument10.3 Inspection of instrument wires, power supplies and cables10.3.1 The instrument panel (table, box) and junction box should be grounded and sealed10.3.2 The fuses used for instruments and auxiliary equipment should meet the technical requirements.10.3.3 The signal pressure pipes and wires should have terminal numbers, and the cables should be labeled. The nameplate of the power supply device should be complete and clear.10.4 Monitoring, interlocking and alarm system instruments10.4.1 The alarm system instruments and switches used for monitoring and interlocking should not be removed or short-circuited at will.10.4.2 The test, reset, silencing, memory and tone distinction functions of the alarm instrument should be intact. 10.4.3 Instrument actuators such as solenoid valves, safety valves, regulating valves and speed regulating devices belonging to the instrument system should be calibrated and positioned regularly. 11 Firefighting facilities
11.1 Equipment of mobile firefighting equipment
SY 57371995
11.1,1 Oil pumping stations and other flammable and explosive places should be equipped with portable or cart-type fire extinguishers. 11.1.2 The equipment standard of firefighting equipment shall be in accordance with GB140. Low-multiple foam fire extinguishing system shall be in accordance with GB50151.11.2 Fixed fire pump room
11.2.1 The on-duty personnel of the fire pump room shall be familiar with the performance of all equipment in this position, the fire extinguishing process, the fire extinguishing combat plan, and conduct regular drills.
11.2.2 The fire pump room should be manned 24 hours a day and should not leave the post without permission. 11.2.3 The communication of the fire pump room should be unobstructed, and the fire pump should be able to start at any time. 11.2.4 The fire pump should be turned once per shift, and the pump should be turned on and drained once a week. Each operation should be no less than 301in, and records should be kept. 11.2.5 Check the valves and fire hydrant boxes of the fire pipelines in each shift, and deal with any problems in a timely manner. 11.2.6 Test spraying of the oil tank fire water system once in May and June every year, and foam test once every 2 to 3 years. 11.3 Management of fire water tanks (pools) and storage of foam liquid 11.3.1 Requirements for fire water tanks (pools):
a) Fire water tanks (pools) are special facilities for fire fighting, and no unit or individual should use them without authorization; b) Fire water tanks (pools) should always maintain the highest water level, and the water tanks (pools) should be kept clean; c) The location of the fire water tanks (culverts) should be marked and kept intact. 11.3.2 Storage of foam liquid:
a) Foam liquid should not be placed in the open air. The temperature of the storage environment is: 0-40℃ for plant protein foam liquid, -5-40℃ for animal protein foam liquid and fluoroprotein foam liquid;
The storage volume of foam liquid should be able to meet the sum of the amount of foam liquid required for one fire extinguishing and the amount of foam liquid contained in the foam mixture filling the pipeline;
c) The foam liquid stored in the foam liquid tank should be replenished in time after use;) The foam liquid should be checked monthly for foaming condition, and a comprehensive chemical inspection should be carried out on the foam liquid every year. If it does not meet the requirements, it should be replaced in time.
11.4 Fire extinguishing and cooling after oil tank fire
11.4.1 If an oil tank catches fire, fire extinguishing should be carried out under unified command, and the fire scene should be guarded and protected. 11.4.2 After the fire pump room attendant receives the fire alarm: the process should be quickly reversed, and the cooling water pump and foam pump should be started within 3 minutes. 11.4.3 After the fire pump is started, the cooling water should be immediately delivered to the burning oil tank and the adjacent oil tanks that need to be cooled. The foam mixture should be delivered to the burning tank within Snmin after the pump is started.
11.4.4 After receiving the alarm, the station's own fire truck should arrive at the fire scene within 5 minutes. 11.4.5 According to the tank position, estimate the possible spraying and boiling time, and take safety measures to prevent casualties. 11.4.6 After the oil tank fire is extinguished, the following measures should be taken: a) Continue to cool the tank wall uninterruptedly until the tank temperature is reduced to the temperature before the fire; continue to supply a certain amount of foam liquid to increase the thickness of the foam coverage to prevent the crude oil from re-igniting c) Strengthen on-site monitoring to prevent the burning again. 11.4.7 Cooling of the burning oil tank and adjacent tanks: a) The water for cooling the oil tank should be sprayed on the upper part of the tank wall; b) The cooling water should be continuous and evenly cool the tank wall to prevent the tank wall from being deformed and damaged by cooling; c) Cooling water should not be injected into the oil
12 Safety management of scientific experiments and promotion of new technologies 12.1 New technologies can only be applied for testing on oil production pipelines and equipment after repeated simulation tests confirm that they are safe and feasible. 12.2 Before the test, the test unit should submit a test application report and a plan of safety measures during the test to the superior, and the test can only be carried out after approval.
SY 5737-1995
12.3 During the test, the person in charge of the new technology test should be identified and the test should be conducted under the unified leadership and command. 12.4 The test and operating personnel should understand the entire process of the test, the performance and source of the test equipment, safety operation precautions and emergency measures.
After the test, the oil production unit should be notified in a timely manner to resume the normal oil transportation procedure.3 Signal pressure pipes and wires should have terminal numbers, and cables should be labeled. The nameplate of the power supply device should be complete and clear. 10.4 Monitoring, interlocking and alarm system instruments 10.4.1 The alarm system instruments and switches used for monitoring and interlocking should not be removed or short-circuited at will. 10.4.2 The test, reset, silencer, memory and tone distinction functions of the alarm instrument should be intact. 10.4.3 The instrument actuators such as solenoid valves, safety valves, regulating valves and speed regulating devices belonging to the instrument system should be regularly calibrated and positioned. 11 Fire-fighting facilities
11.1 The configuration of mobile fire-fighting equipment
SY 57371995
11.1,1 Oil pumping stations and other flammable and explosive places should be equipped with portable or cart-type fire extinguishers. 11.1.2 The configuration standard of fire-fighting equipment shall be in accordance with GB140. Low-multiple foam fire extinguishing system is in accordance with GB50151.11.2 Fixed fire pump room
11.2.1 The on-duty personnel of the fire pump room should be familiar with the performance of all equipment in this position, the fire extinguishing process, the fire extinguishing combat plan, and conduct drills regularly.
11.2.2 The fire pump room should be manned 24 hours a day and should not leave their posts without permission. 11.2.3 The communication of the fire pump room should be unobstructed and the fire pump should be able to start at any time. 11.2.4 The fire pump should be turned once per shift, and the pump should be opened and drained once a week. Each operation should not be less than 301in, and records should be kept. 11.2.5 Check the valves and fire hydrant boxes of the fire pipelines every shift, and deal with any problems in time. 11.2.6 Test spraying of the oil tank fire water system in May and June every year, and test foam once every 2 to 3 years. 11.3 Management of fire water tanks (pools) and storage of foam liquid 11.3.1 Requirements for fire water tanks (pools):
a) Fire water tanks (pools) are special facilities for fire fighting and no unit or individual should use them without authorization: b) Fire water tanks (pools) should always maintain the highest water level and the water tanks (pools) should be kept clean: c) The location of the fire water tank (culvert) should be marked and kept in good condition. 11.3.2 Storage of foam liquid:
a) Foam liquid should not be placed in the open air. The temperature of the storage environment is: 0-40℃ for plant protein foam liquid, -5-40℃ for animal protein foam liquid and fluoroprotein foam liquid;
The storage volume of foam liquid should be able to meet the sum of the amount of foam liquid required for one fire extinguishing and the amount of foam liquid contained in the foam mixture filling the pipeline;
c) The foam liquid stored in the foam liquid tank should be replenished in time after use;) The foam liquid should be checked monthly for foaming condition, and a comprehensive chemical inspection should be carried out on the foam liquid every year. If it does not meet the requirements, it should be replaced in time.
11.4 Fire extinguishing and cooling after oil tank fire
11.4.1 If an oil tank catches fire, fire extinguishing should be carried out under unified command, and the fire scene should be guarded and protected. 11.4.2 After the fire pump room attendant receives the fire alarm: the process should be quickly reversed, and the cooling water pump and foam pump should be started within 3 minutes. 11.4.3 After the fire pump is started, the cooling water should be immediately delivered to the burning oil tank and the adjacent oil tanks that need to be cooled. The foam mixture should be delivered to the burning tank within Snmin after the pump is started.
11.4.4 After receiving the alarm, the station's own fire truck should arrive at the fire scene within 5 minutes. 11.4.5 According to the tank position, estimate the possible spraying and boiling time, and take safety measures to prevent casualties. 11.4.6 After the oil tank fire is extinguished, the following measures should be taken: a) Continue to cool the tank wall uninterruptedly until the tank temperature is reduced to the temperature before the fire; continue to supply a certain amount of foam liquid to increase the thickness of the foam coverage to prevent the crude oil from re-igniting c) Strengthen on-site monitoring to prevent the burning again. 11.4.7 Cooling of the burning oil tank and adjacent tanks: a) The water for cooling the oil tank should be sprayed on the upper part of the tank wall; b) The cooling water should be continuous and evenly cool the tank wall to prevent the tank wall from being deformed and damaged by cooling; c) Cooling water should not be injected into the oil
12 Safety management of scientific experiments and promotion of new technologies 12.1 New technologies can only be applied for testing on oil production pipelines and equipment after repeated simulation tests confirm that they are safe and feasible. 12.2 Before the test, the test unit should submit a test application report and a plan of safety measures during the test to the superior, and the test can only be carried out after approval.
SY 5737-1995
12.3 During the test, the person in charge of the new technology test should be identified and the test should be conducted under the unified leadership and command. 12.4 The test and operating personnel should understand the entire process of the test, the performance and source of the test equipment, safety operation precautions and emergency measures.
After the test, the oil production unit should be notified in a timely manner to resume the normal oil transportation procedure.3 Signal pressure pipes and wires should have terminal numbers, and cables should be labeled. The nameplate of the power supply device should be complete and clear. 10.4 Monitoring, interlocking and alarm system instruments 10.4.1 The alarm system instruments and switches used for monitoring and interlocking should not be removed or short-circuited at will. 10.4.2 The test, reset, silencer, memory and tone distinction functions of the alarm instrument should be intact. 10.4.3 The instrument actuators such as solenoid valves, safety valves, regulating valves and speed regulating devices belonging to the instrument system should be regularly calibrated and positioned. 11 Fire-fighting facilities
11.1 The configuration of mobile fire-fighting equipment
SY 57371995
11.1,1 Oil pumping stations and other flammable and explosive places should be equipped with portable or cart-type fire extinguishers. 11.1.2 The configuration standard of fire-fighting equipment shall be in accordance with GB140. Low-multiple foam fire extinguishing system is in accordance with GB50151.11.2 Fixed fire pump room
11.2.1 The on-duty personnel of the fire pump room should be familiar with the performance of all equipment in this position, the fire extinguishing process, the fire extinguishing combat plan, and conduct drills regularly.
11.2.2 The fire pump room should be manned 24 hours a day and should not leave their posts without permission. 11.2.3 The communication of the fire pump room should be unobstructed and the fire pump should be able to start at any time. 11.2.4 The fire pump should be turned once per shift, and the pump should be opened and drained once a week. Each operation should not be less than 301in, and records should be kept. 11.2.5 Check the valves and fire hydrant boxes of the fire pipelines every shift, and deal with any problems in time. 11.2.6 Test spraying of the oil tank fire water system in May and June every year, and test foam once every 2 to 3 years. 11.3 Management of fire water tanks (pools) and storage of foam liquid 11.3.1 Requirements for fire water tanks (pools):
a) Fire water tanks (pools) are special facilities for fire fighting and no unit or individual should use them without authorization: b) Fire water tanks (pools) should always maintain the highest water level and the water tanks (pools) should be kept clean: c) The location of the fire water tank (culvert) should be marked and kept in good condition. 11.3.2 Storage of foam liquid:
a) Foam liquid should not be placed in the open air. The temperature of the storage environment is: 0-40℃ for plant protein foam liquid, -5-40℃ for animal protein foam liquid and fluoroprotein foam liquid;
The storage volume of foam liquid should be able to meet the sum of the amount of foam liquid required for one fire extinguishing and the amount of foam liquid contained in the foam mixture filling the pipeline;
c) The foam liquid stored in the foam liquid tank should be replenished in time after use;) The foam liquid should be checked monthly for foaming condition, and a comprehensive chemical inspection should be carried out on the foam liquid every year. If it does not meet the requirements, it should be replaced in time.
11.4 Fire extinguishing and cooling after oil tank fire
11.4.1 If an oil tank catches fire, fire extinguishing should be carried out under unified command, and the fire scene should be guarded and protected. 11.4.2 After the fire pump room attendant receives the fire alarm: the process should be quickly reversed, and the cooling water pump and foam pump should be started within 3 minutes. 11.4.3 After the fire pump is started, the cooling water should be immediately delivered to the burning oil tank and the adjacent oil tanks that need to be cooled. The foam mixture should be delivered to the burning tank within Snmin after the pump is started.
11.4.4 After receiving the alarm, the station's own fire truck should arrive at the fire scene within 5 minutes. 11.4.5 According to the tank position, estimate the possible spraying and boiling time, and take safety measures to prevent casualties. 11.4.6 After the oil tank fire is extinguished, the following measures should be taken: a) Continue to cool the tank wall uninterruptedly until the tank temperature is reduced to the temperature before the fire; continue to supply a certain amount of foam liquid to increase the thickness of the foam coverage to prevent the crude oil from re-igniting c) Strengthen on-site monitoring to prevent the burning again. 11.4.7 Cooling of the burning oil tank and adjacent tanks: a) The water for cooling the oil tank should be sprayed on the upper part of the tank wall; b) The cooling water should be continuous and evenly cool the tank wall to prevent the tank wall from being deformed and damaged by cooling; c) Cooling water should not be injected into the oil
12 Safety management of scientific experiments and promotion of new technologies 12.1 New technologies can only be applied for testing on oil production pipelines and equipment after repeated simulation tests confirm that they are safe and feasible. 12.2 Before the test, the test unit should submit a test application report and a plan of safety measures during the test to the superior, and the test can only be carried out after approval.
SY 5737-1995
12.3 During the test, the person in charge of the new technology test should be identified and the test should be conducted under the unified leadership and command. 12.4 The test and operating personnel should understand the entire process of the test, the performance and source of the test equipment, safety operation precautions and emergency measures.
After the test, the oil production unit should be notified in a timely manner to resume the normal oil transportation procedure.4 The test and operating personnel should understand the whole process of the test, the performance and source of the test equipment, safety operation precautions and emergency measures.
After the test, the oil production unit should be notified in time to resume the normal oil transportation procedures.4 The test and operating personnel should understand the whole process of the test, the performance and source of the test equipment, safety operation precautions and emergency measures.
After the test, the oil production unit should be notified in time to resume the normal oil transportation procedures.
Tip: This standard content only shows part of the intercepted content of the complete standard. If you need the complete standard, please go to the top to download the complete standard document for free.