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SY 0049-1994 Oilfield surface construction planning and design specifications

Basic Information

Standard ID: SY 0049-1994

Standard Name: Oilfield surface construction planning and design specifications

Chinese Name: 油田地面建设规划设计规范

Standard category:Oil and gas industry standards (SY)

state:in force

Date of Release1994-12-21

Date of Implementation:1995-06-01

standard classification number

Standard ICS number:Civil Engineering >> 93.020 Earthwork, excavation, foundation construction, underground engineering

Standard Classification Number:Engineering Construction>>Engineering Survey and Geotechnical Engineering>>P13 Project Address, Hydrogeological Survey and Geotechnical Engineering

associated standards

alternative situation:Replaced by SY/T 0049-2006

Publication information

other information

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SY 0049-1994 Oilfield Surface Construction Planning and Design SpecificationsSY0049-1994 Standard download decompression password: www.bzxz.net

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Standard of the People's Republic of China for the petroleum and natural gas industry Specification for planning and design of surface construction of oilfields
Plannig and engineering cudeoroi-fefsurfaceproduction facilties constructionSY I49-94
Editor: Planning and Design Institute of China National Petroleum and Natural Gas CorporationApproval department: China National Petroleum and Natural Gas CorporationPetroleum Industry Press
1995Beijing
The above standard shall come into effect on June 1, 1995China National Petroleum and Natural Gas Corporation
December 21, 1994
1 General provisions
?Terms
3 Construction conditions||t t||4 Construction scale
5 Overall layout
6 Oil and gas gathering and transportation project
6.1 Process
6.2 Process equipment
Supporting projects
7.1 Oil spot water injection
7.2 Extraction and treatment
7.3 Water supply and drainage and fire protection
7.4 Power supply and distribution
7.5 Roads
7.6 Communication and self-contained cavity\||t t||7.7 Production maintenance and staff housing
& Energy saving and consumption reduction
3.T Energy consumption indicators
8.2 Energy saving measures
9 Labor organization
10 Environmental protection
Appendix A Terms
Additional explanation
(15)
Appendix Explanation of the provisions of the current oilfield surface construction planning and design specification (29 China National Petroleum Corporation Document
(94) Zhongyou Jimengzi No. 711
Notice on the approval and release of ten oil and gas industry standards including the "Oilfield Surface Construction Planning and Design Specification" and other relevant units:
Wuhan Oilfield Surface Construction Planning and Design Specification" and other ten standards (draft) have been reviewed and approved and are now approved as oil and gas industry standards. They can be released. The numbers and names of the various standards are as follows:
Serial number
1SY SY/T0049-94 Oilfield surface construction planning and design specifications 2SY/T0083-94 Oil removal tank design specifications SY/T0084-94 Annular bending performance test method for the defense layer 4SY/T0085-94 Natural gas rapid delivery test method for pipeline defense layer 5SY/T0534-94 Separator gas with liquid test method for near-position sampling and collection method SY/T0535-94 Fire-type heating furnace thermal and wake-up calculation method SY/T0541-94 Crude oil condensation point determination method SY/T0542-94 Gas chromatography method for analysis of light oil components SY/T0543-94 Stable light oil sampling method SY/T7504-94 Analysis of n-alkane and previous hydrocarbon components in crude oil by gas chromatography (replacing SY7504-85)
1 General
1.0.1 To strengthen the scientific management of oilfield surface construction planning and design: reasonably determine the construction level, correctly grasp the construction standards, promote technical progress, and improve investment efficiency: formulate vehicle specifications
1.0.2 This specification is an important basis for the preparation, evaluation, and approval of oilfield surface construction planning and design, and is also a yardstick for the preliminary design of engineering projects and the measurement of construction levels. 0.3 This specification is applicable to the planning and design of various system projects of new oilfield surface construction in the upper and lower regions, the survey of old oilfields For the renovation, sea flooding, sand-blasting and other special oil fields, the ground construction planning and design can refer to the relevant national policies and regulations such as the 1.04 Oilfield ground construction planning and design must be consistent with the principles of hard work, diligence and inspection, and must implement the relevant national policies and regulations such as site management, production and environmental protection, and adhere to the principles of technology first, economic rationality, safety and applicability, quality comprehensive utilization, energy saving and consumption reduction.
1.0.5 The ground construction planning and design of oil groups must adhere to the principle of ground adapting to the underground, ground and underground matching, and achieve overall optimization, and carefully plan and design in the spirit of comprehensive planning and phased implementation.
1.0.6 In addition to implementing this specification, the ground construction planning and design of oil groups shall also comply with the relevant national standards and specifications in force.
1.0.7 For the approved oil ground construction planning and design, the project content, process flow, system layout, construction scale, engineering quantity, construction standard and investment scale shall not be arbitrarily changed. When there are major changes. The approval of the source approval department should be obtained. 2 Terms
20.1 Oilfield surface construction oil-field surface production facilities construction
Oilfield development and construction generally include reservoir engineering, drilling and merging engineering. Oil production engineering oil and gas gathering and transportation engineering, oilfield supporting engineering (including water injection: produced water treatment: water supply and drainage and fire protection, power supply and distribution, roads, communications and automatic control, production maintenance and staff housing, etc.), usually the construction of the latter two projects is collectively referred to as oilfield surface construction 2.0.2 Planning and engineering planning and engineering to solve the overall development of the construction project and the overall deployment of the overall planning design or overall design, collectively referred to as planning and design 2.0.3 Feasibility study feasibilty study It is an important part of the pre-construction work and an integral part of the basic construction process. Its task is to: conduct a comprehensive analysis and demonstration of the construction project in terms of technology, engineering and economy: after comparing multiple plans, make evaluation opinions on the recommended best plan, and prepare it after approval. Review the basis of the preliminary design 204 Oil-gas gathering and transportation The process of collecting, processing, storing and transporting the oil and gas produced from oil wells.
2.0.5 Water injection: water injection
In order to maintain the pressure of the oil layer, water is injected into the oil layer. The methods include positive injection, reverse injection, weight injection, pressure injection, wheel injection, intermittent injection, 206 Produced water treatment The process of recycling and treating the produced water (including washing water) from the oil field to make it meet the water quality standards or discharge requirements of the injection water
2.0.7 Gas-liguid mixed-lom In the process of oil and gas transportation, the liquid and gas phases of fluids are transported in a pipeline. In oil fields, it is known as oil and gas transport.
2.08 Hot water transport: water blended crude oil transport. A certain amount of water is introduced into the pipeline for transporting crude oil to reduce the friction of the fluid in the pipeline.
2.0.9 Heat transport: nuidlowwithheatracing: A transport method that maintains a stable temperature in the oil field under the accompaniment of an external heat source.
2.0.10 Gas-liquid separation: The process of separating liquid and gaseous materials under specified pressure and temperature is also known as oil and gas separation.
2.0.11 Crude oil dehydration Demusification is the process of separating crude oil and water by emulsification and sedimentation. 2.0.12 Crude oil stabilization is the process of removing dehydrated gas and volatile components from crude oil to make the saturated gas pressure meet the product standards.
2.0.13 Natural gas dehydration is the process of removing water vapor from natural gas by absorption, absorption, and other methods to make its water dew point meet the requirements. It is also called natural gas dry extraction. 2.0.14 Light oil recovery is the process of recovering liquid from natural gas (or oilfield gas). The recovery method is mainly cold separation, which is divided into shallow cold and deep cold processes. 2.015 Petroleum
Naturally grown in underground rock formations, it is a complex mixture composed of multiple hydrocarbons and contains non-hydrocarbon impurities. It is also the general name for crude oil, natural gas and its products. 2.0.16 Crude oil
The liquid phase of petroleum after extraction.
2.0.17Natural gas
The gas phase after oil is extracted. Natural gas produced with crude oil is also called oilfield gas. 2.0.18Light crude oil
Crude oil with a density less than or equal to 0.3650g/cmr at 20°C 2.0.19Midecrude oil
Crude oil with a density of 0.8651-0.9160g/cm at 20°C 2.0.20Heavy crude oil
Crude oil with a density of 0.9161-09960mcm crude oil 2.0.21 weekly oil viscosity crude oil
at 2 billion, the width is greater than 0.9200g/cmH and the dynamic viscosity at 50C is greater than 40mPm*s
20.22 station gas leun gs
The propane and heavier hydrocarbon components in each cubic meter of gas are calculated as liquid. Natural gas with a volume of less than 100 nL
2.0.33 High gas
Propane and heavier light components in new cubic meters of gas, measured in liquid form, natural gas with a volume greater than 100 mL
224 Natural gas liquid (NGL) A general term for a mixture of hydrocarbons recovered from natural gas, generally including ethane, liquefied petroleum gas and stable light hydrocarbons.
2.025 Liquefied petroleum gas (LPG) A petroleum product with propane and butane as the main components, generally including a mixture of commercial gasoline, commercial butane and commercial propane 2.0.26 Natural gasoline Gasoling is a liquid petroleum product extracted from natural gas condensate, with pentane and heavier hydrocarbons as the main components. Its terminal point is not higher than 190℃, and it is allowed to contain a small amount of butane, also known as acute light hydrocarbons under the specified vapor pressure.
20.27 Well product welleffuen
Liquid, volatile, solid hydrocarbons and non-light compounds extracted from wells 2.0.28 Produced water
Water extracted from oil wells at the same time as the original oil. 2.0.29 Water for injection water for injection Water that meets the water quality requirements for injection water. Usually includes injection water and washing water. 2.0. Well-flushing waste water Well-flushing waste water Water returned to the ground from the well-washing operation of the injection well
2.0.31 Frezing point of crude oil The amount of crude oil sample when it is cooled to stop moving under specified conditions 2.0.32 Dew point dew point
The temperature at which the first drop of water is precipitated from natural gas under a certain pressure. It is also called the dew point. 2.0.33# Wellhead pressure The pressure after self-spraying and throttling (nozzle), which is simply equal to the sum of the hydraulic friction of the oil pipeline, the potential difference and the pressure of the first oil and gas separator. 2.0.34 Wellhead pressure The outlet pressure of the machine-produced well, which is equal to the sum of the hydraulic resistance of the production pipeline, the potential difference and the pressure of the first-stage oil and gas separator.
2.0.35 Combined unit In order to simplify the production process or reduce the number of equipment and reduce consumption, save energy and land, etc., two or more equipments are combined to form a combination, 2.0.36 Wellhead device wcl The assembly installed on the parallel port to realize the parallel production process generally includes the chamber pipe head, oil pipe head and rapeseed oil
3 Construction conditions
3.01 When planning and designing the oil production ground construction, you must first understand the geological results of the oil field and the country, including the oil-bearing surface, the characteristics of the oil layer, the depth of the oil layer, the geological reserves, the original pressure of the oil layer, the ground pressure difference, the oil suspension properties and the oil and gas properties, etc. 3.0.2 You must have an approved plan or layout for oil field development and oil production process design, including the development method. The form of the same, the number of layouts, the ratio of wells to production, the speed of oil production in the production method, the average single well production in each block, the injection time, injection method, injection pressure, injection volume, water-free oil production period, the daily production level of the oil field (or block) at the beginning of the production, and the prediction of the changes in oil, water and water production within ten years, etc. 3.03 It is necessary to understand the production and construction of old oil fields near the newly built oil fields, including the current capacity and planning of the gas transmission project and other supporting projects, as well as the load conditions with the new oil fields.
3.0.4 It is necessary to understand the transportation, processing, sales and price policies of the local government and the local government on oil and gas products, including the transportation method of oil and gas, transportation capacity, reverse transportation, the supply of oil and gas consumed by the oil field, and the long-term layout of petrochemical development, etc. 3.0.5 It is necessary to investigate and understand the geographical environment conditions of the oil field, including topography, geomorphology, water and engineering geography. Hydrological data, ground intensity, flood disaster meteorological data, health conditions and environmental protection requirements, etc., must be updated with 1:10000 and 1:5000 topographic maps of sufficient scale. 3.0.6 Local factors affecting oilfield surface construction must be understood, including ethnic composition, cultural customs, industrial and agricultural production, local economic development plan, living standards, cultural and health, transportation, land use, water sources, power supply, communication, material selection, local construction materials and labor, etc. 3.0.7 The advanced characteristics and import and export of various materials used in oilfield construction must be understood, as well as domestic and foreign supply channels, including market prices, product quality, delivery time, cooperation history with the oil industry and the degree of impact on the economic benefits of the oilfield, etc. 6. 3.0.8 The investment subject and funding source for oilfield surface construction must be clearly defined, including bank loans, self-financing, use of foreign capital, loan interest rates, loan repayments, etc. 4.01 The scale of the planning and design of the surface construction of the oil field should be based on the production capacity determined by the oil field development design. The supporting systems should be large according to the relevant data in the development design. The adaptation period of the project should be consistent with the adjustment and transformation period of the oil field. Generally, it should be 10 years. The planning of the first phase of the early water injection oil field should be determined according to the oil field's combined water content of 50%, which can be implemented in stages.
4.0.2 The metering station should be built in a moderate position of the oil field production group. The number of metering stations should be 8-16. When multiple metering groups are used to measure in one metering station, the amount of oil wells can be appropriately increased: when the oil production is concentrated in a cluster, each metering station can manage one or more clusters. 4.03 The transfer station generally does not have an emergency oil tank, and the collection and transportation radius of the pipeline should not be less than 5km. The amount of its transferred materials should not be greater than 7000t/d. 4.0.4 The centralized processing station set up for oil outflow should be as close as possible to the oil wells. When the oilfield capacity is less than 300% and the oil production area does not exceed 50km, a centralized processing station should be built: When the production blocks in the oilfield are far apart and need to be divided into centralized processing stations, the scale of each station should not be less than 30×101/% otherwise it should be demonstrated separately 4.0.5 The scale of the centralized processing station (dehydration station) is calculated as follows: #=365mm*#Open
Wuzhong Construction Ship#. 10%/mountain
-average Single well capacity, t/d
—Total number of wells in production at the station
One opening and closing rate,
4.0.6 The original pipeline reserve capacity of the oil field (excluding the operating tanks of the old stations) shall be determined according to the following original judgment: 3~d is suitable for oil fields that mainly transport crude oil by belt; 5~7d is suitable for oil fields that mainly transport crude oil by rail. When the reserve capacity needs to be further increased, it shall be determined after special demonstration
4.0.7 The pipe capacity of various gathering and transportation pipelines in the oil field The following provisions shall be applied to determine the oil flow line between the oil production well and the metering station: it shall be calculated based on the maximum liquid production and output, and shall not be less than DN40
4.0.7.2 The same oil gathering pipeline from the metering station to the centralized processing station (or to the transfer station): it shall be calculated based on the total maximum liquid production and gas production of the metering station, and shall not be greater than DN200:
4.0.7.3 The gas gathering pipeline from the transfer station to the centralized processing station (unprocessed natural gas) It should be calculated according to the maximum gas collection volume of the transfer station:
4.0.7.4 The oil pipeline that transmits oil through the ground pressure should be calculated according to 1.2 times of the amount of the sleeve (liquid) transmitted by the oil pipeline. If necessary, it can be calculated by thermal light calibration. 4.0.7.5 The gas pipeline that transports purified natural gas to the user should be calculated according to 1.2 times of the auxiliary gas volume.
5 Overall layout
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7.2 produced water treatment
7.11 the current scale of the water station should be based on the oil field produced water volume, the total wastewater volume and the recovery of other local industrial wastewater as the basis. The project is calculated according to the comprehensive water content of the oil field
7.2.2 the oil content of the raw water entering the water treatment station should not exceed 1000mz/1 the oil content of the water before the transmission should not exceed 50mg/1 the produced water after treatment, if used for reinjection, the water quality should meet the SYI6 oil field oil content According to the provisions of Article 20.2 of the "Sewage Treatment Design Code", when used for other purposes, it shall comply with the corresponding standards. 7.1.3 The selection of treatment technology shall be based on the nature of the oily pollutants and the requirements for reuse and reduction of external drainage. Under normal circumstances, water purification should be designed according to the process of oil removal, sedimentation, flotation, and filtration: if necessary, it can also be designed according to the in-depth treatment process such as multi-stage filtration and fine filtration.
7.3.4 In order to improve the treatment capacity and absorption effect of produced water: promote the use of high-end water treatment equipment such as inclined plate (tube) oil removal tanks, torsion oil removal tanks, flotation oil removal machines, cyclone oil removers and new filters.
7.3.5 New oil fields should be planned and designed according to the fully enclosed washing process of produced water treatment and water injection systems.
7.16 The effluent treatment system should be designed based on the basic considerations. Consider finding appropriate buffers, deoxidizers, bactericides and anti-fouling agents in appropriate locations, and try to achieve multiple uses with one dose. 7.27 Sewage treatment facilities should have sludge discharge facilities, and the discharged sludge must be properly handled to prevent environmental pollution.
7.3 Water supply, drainage and fire protection
7.1 The planning and design of oil field water sources should be subject to comprehensive water resource preparation and evaluation or have necessary technical and auxiliary exploration data. Under the premise of ensuring sufficient water volume and good water quality, the selection of water sources should be strongly demonstrated, and water sources should be fully utilized to avoid competing with agriculture for water. 7.3.2 The water supply capacity of oil field water sources should be calculated according to the total amount of oil field water injection, production water, domestic water, chemical water, and fire protection water. If necessary, the water use of oil field, agriculture and other industrial water use should also be considered.
7 .3.3 The layout of the oil field water supply network should first meet the water requirements of the field injection water supply, water injection water supply and other production water supply. The life supply should be a separate system, and the water supply pipeline can be connected to a large amount of water supply. 12 storage calculation
7.3.4 The flood control and drainage of the oil field area should be comprehensively managed in accordance with the local external conditions, in conjunction with the local relevant departments and local governments, and should be comprehensively planned and designed with the local unified rainfall rate, flow coefficient, and flood drainage standards. 7.35 The flood control and drainage of the oil field and the reservoir should be in line with the local flood control and drainage. Generally, open nests should be used, and they should be combined with road ditches and farmland drainage as much as possible. Drainage structures and equipment can be equipped according to the standard of three days of precipitation and four days of drainage. 7.3.6 The fire-fighting water of the oil field can make full use of the water supply network in the oil field. The layout and scale of oilfield firefighting stations shall comply with the provisions of Chapter 7, Section 2 of GB50183 “Code for Fire Protection Design of Crude Oil and Natural Gas Engineering”. 7.3.7 For stations with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distributionbzxZ.net
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.X uses grid machine water
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7.2 produced water treatment
7.11 the current scale of the water station should be based on the oil field produced water volume, the total wastewater volume and the recovery of other local industrial wastewater as the basis. The project is calculated according to the comprehensive water content of the oil field
7.2.2 the oil content of the raw water entering the water treatment station should not exceed 1000mz/1 the oil content of the water before the transmission should not exceed 50mg/1 the produced water after treatment, if used for reinjection, the water quality should meet the SYI6 oil field oil content According to the provisions of Article 20.2 of the "Sewage Treatment Design Code", when used for other purposes, it shall comply with the corresponding standards. 7.1.3 The selection of treatment technology shall be based on the nature of the oily pollutants and the requirements for reuse and reduction of external drainage. Under normal circumstances, water purification should be designed according to the process of oil removal, sedimentation, flotation, and filtration: if necessary, it can also be designed according to the in-depth treatment process such as multi-stage filtration and fine filtration.
7.3.4 In order to improve the treatment capacity and absorption effect of produced water: promote the use of high-end water treatment equipment such as inclined plate (tube) oil removal tanks, torsion oil removal tanks, flotation oil removal machines, cyclone oil removers and new filters.
7.3.5 New oil fields should be planned and designed according to the fully enclosed washing process of produced water treatment and water injection systems.
7.16 The effluent treatment system should be designed based on the basic considerations. Consider finding appropriate buffers, deoxidizers, bactericides and anti-fouling agents in appropriate locations, and try to achieve multiple uses with one dose. 7.27 Sewage treatment facilities should have sludge discharge facilities, and the discharged sludge must be properly handled to prevent environmental pollution.
7.3 Water supply, drainage and fire protection
7.1 The planning and design of oil field water sources should be subject to comprehensive water resource preparation and evaluation or have necessary technical and auxiliary exploration data. Under the premise of ensuring sufficient water volume and good water quality, the selection of water sources should be strongly demonstrated, and water sources should be fully utilized to avoid competing with agriculture for water. 7.3.2 The water supply capacity of oil field water sources should be calculated according to the total amount of oil field water injection, production water, domestic water, chemical water, and fire protection water. If necessary, the water use of oil field, agriculture and other industrial water use should also be considered.
7 .3.3 The layout of the oil field water supply network should first meet the water requirements of the field injection water supply, water injection water supply and other production water supply. The life supply should be a separate system, and the water supply pipeline can be connected to a large amount of water supply. 12 storage calculation
7.3.4 The flood control and drainage of the oil field area should be comprehensively managed in accordance with the local external conditions, in conjunction with the local relevant departments and local governments, and should be comprehensively planned and designed with the local unified rainfall rate, flow coefficient, and flood drainage standards. 7.35 The flood control and drainage of the oil field and the reservoir should be in line with the local flood control and drainage. Generally, open nests should be used, and they should be combined with road ditches and farmland drainage as much as possible. Drainage structures and equipment can be equipped according to the standard of three days of precipitation and four days of drainage. 7.3.6 The fire-fighting water of the oil field can make full use of the water supply network in the oil field. The layout and scale of oilfield firefighting stations shall comply with the provisions of Chapter 7, Section 2 of GB50183 “Code for Fire Protection Design of Crude Oil and Natural Gas Engineering”. 7.3.7 For stations with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.X uses grid machine water
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7.1 Oilfield water injection
71chuan is a water life protection hospital. Chengzuo disease production small non
period 1 clear 1 tube endogenous substance
parent's order transmission
71 to work H work
1- 14, 2), two 3, ±7311 4 practical in many live a. When "under the correction of no island under the action of many forms its A stem energy value. Induced muscle related to the use of resistance can 4 sea can or element south. Water
science or resistance to people thank, theory of the plan 1. P
to make up for the index, to,
use P is still weak, work time
115 effect of water E ratio around except *57[lipid cell 4 test old 2us article is, in time, water with
element water pure time. The type of
hu this station receives
total performance of the book Rui E square large living in the central point of the design of the new water:
8 Huishui year book teaching, heart car product: with
85%, happy year, heart contact people
non system large down, life room life, in
7.2 produced water treatment
7.11 the current scale of the water station should be based on the oil field produced water volume, the total wastewater volume and the recovery of other local industrial wastewater as the basis. The project is calculated according to the comprehensive water content of the oil field
7.2.2 the oil content of the raw water entering the water treatment station should not exceed 1000mz/1 the oil content of the water before the transmission should not exceed 50mg/1 the produced water after treatment, if used for reinjection, the water quality should meet the SYI6 oil field oil content According to the provisions of Article 20.2 of the "Sewage Treatment Design Code", when used for other purposes, it shall comply with the corresponding standards. 7.1.3 The selection of treatment technology shall be based on the nature of the oily pollutants and the requirements for reuse and reduction of external drainage. Under normal circumstances, water purification should be designed according to the process of oil removal, sedimentation, flotation, and filtration: if necessary, it can also be designed according to the in-depth treatment process such as multi-stage filtration and fine filtration.
7.3.4 In order to improve the treatment capacity and absorption effect of produced water: promote the use of high-end water treatment equipment such as inclined plate (tube) oil removal tanks, torsion oil removal tanks, flotation oil removal machines, cyclone oil removers and new filters.
7.3.5 New oil fields should be planned and designed according to the fully enclosed washing process of produced water treatment and water injection systems.
7.16 The effluent treatment system should be designed based on the basic considerations. Consider finding appropriate buffers, deoxidizers, bactericides and anti-fouling agents in appropriate locations, and try to achieve multiple uses with one dose. 7.27 Sewage treatment facilities should have sludge discharge facilities, and the discharged sludge must be properly handled to prevent environmental pollution.
7.3 Water supply, drainage and fire protection
7.1 The planning and design of oil field water sources should be subject to comprehensive water resource preparation and evaluation or have necessary technical and auxiliary exploration data. Under the premise of ensuring sufficient water volume and good water quality, the selection of water sources should be strongly demonstrated, and water sources should be fully utilized to avoid competing with agriculture for water. 7.3.2 The water supply capacity of oil field water sources should be calculated according to the total amount of oil field water injection, production water, domestic water, chemical water, and fire protection water. If necessary, the water use of oil field, agriculture and other industrial water use should also be considered.
7 .3.3 The layout of the oil field water supply network should first meet the water requirements of the field injection water supply, water injection water supply and other production water supply. The life supply should be a separate system, and the water supply pipeline can be connected to a large amount of water supply. 12 storage calculation
7.3.4 The flood control and drainage of the oil field area should be comprehensively managed in accordance with the local external conditions, in conjunction with the local relevant departments and local governments, and should be comprehensively planned and designed with the local unified rainfall rate, flow coefficient, and flood drainage standards. 7.35 The flood control and drainage of the oil field and the reservoir should be in line with the local flood control and drainage. Generally, open nests should be used, and they should be combined with road ditches and farmland drainage as much as possible. Drainage structures and equipment can be equipped according to the standard of three days of precipitation and four days of drainage. 7.3.6 The fire-fighting water of the oil field can make full use of the water supply network in the oil field. The layout and scale of oilfield firefighting stations shall comply with the provisions of Chapter 7, Section 2 of GB50183 “Code for Fire Protection Design of Crude Oil and Natural Gas Engineering”. 7.3.7 For stations with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.1 oil field water injection
71chuan is the water life protection hospital. Chengzuo disease music production small non
period 1 clear 1 tube endogenous substance
parent's order transmission
71 to do business H work
1- 14, 2), two 3, ±7311 4 practical in many live in a of a. When "under the correction of no island under the action of many forms its a stem energy value. Induced muscle related use of resistance can 4 sea can or element south. Water
science or resistance to people thank, theory of design 1. P
to make up for the index, to,
use P is still weak, work time
115 effect of water E ratio around except *57[lipid cell 4 test old 2us article is, in time, water with
element water pure time. The type of
hu this station receives
total performance of the book Rui E square large living in the central point of the design of the new water:
8 Huishui year book teaching, heart car product: with
85%, happy year, heart contact people
non system large down, life room life, in
7.2 produced water treatment
7.11 the current scale of the water station should be based on the oil field produced water volume, the total wastewater volume and the recovery of other local industrial wastewater as the basis. The project is calculated according to the comprehensive water content of the oil field
7.2.2 the oil content of the raw water entering the water treatment station should not exceed 1000mz/1 the oil content of the water before the transmission should not exceed 50mg/1 the produced water after treatment, if used for reinjection, the water quality should meet the SYI6 oil field oil content According to the provisions of Article 20.2 of the "Sewage Treatment Design Code", when used for other purposes, it shall comply with the corresponding standards. 7.1.3 The selection of treatment technology shall be based on the nature of the oily pollutants and the requirements for reuse and reduction of external drainage. Under normal circumstances, water purification should be designed according to the process of oil removal, sedimentation, flotation, and filtration: if necessary, it can also be designed according to the in-depth treatment process such as multi-stage filtration and fine filtration.
7.3.4 In order to improve the treatment capacity and absorption effect of produced water: promote the use of high-end water treatment equipment such as inclined plate (tube) oil removal tanks, torsion oil removal tanks, flotation oil removal machines, cyclone oil removers and new filters.
7.3.5 New oil fields should be planned and designed according to the fully enclosed washing process of produced water treatment and water injection systems.
7.16 The effluent treatment system should be designed based on the basic considerations. Consider finding appropriate buffers, deoxidizers, bactericides and anti-fouling agents in appropriate locations, and try to achieve multiple uses with one dose. 7.27 Sewage treatment facilities should have sludge discharge facilities, and the discharged sludge must be properly handled to prevent environmental pollution.
7.3 Water supply, drainage and fire protection
7.1 The planning and design of oil field water sources should be subject to comprehensive water resource preparation and evaluation or have necessary technical and auxiliary exploration data. Under the premise of ensuring sufficient water volume and good water quality, the selection of water sources should be strongly demonstrated, and water sources should be fully utilized to avoid competing with agriculture for water. 7.3.2 The water supply capacity of oil field water sources should be calculated according to the total amount of oil field water injection, production water, domestic water, chemical water, and fire protection water. If necessary, the water use of oil field, agriculture and other industrial water use should also be considered.
7 .3.3 The layout of the oil field water supply network should first meet the water requirements of the field injection water supply, water injection water supply and other production water supply. The life supply should be a separate system, and the water supply pipeline can be connected to a large amount of water supply. 12 storage calculation
7.3.4 The flood control and drainage of the oil field area should be comprehensively managed in accordance with the local external conditions, in conjunction with the local relevant departments and local governments, and should be comprehensively planned and designed with the local unified rainfall rate, flow coefficient, and flood drainage standards. 7.35 The flood control and drainage of the oil field and the reservoir should be in line with the local flood control and drainage. Generally, open nests should be used, and they should be combined with road ditches and farmland drainage as much as possible. Drainage structures and equipment can be equipped according to the standard of three days of precipitation and four days of drainage. 7.3.6 The fire-fighting water of the oil field can make full use of the water supply network in the oil field. The layout and scale of oilfield firefighting stations shall comply with the provisions of Chapter 7, Section 2 of GB50183 “Code for Fire Protection Design of Crude Oil and Natural Gas Engineering”. 7.3.7 For stations with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.1 oil field water injection
71chuan is the water life protection hospital. Chengzuo disease music production small non
period 1 clear 1 tube endogenous substance
parent's order transmission
71 to do business H work
1- 14, 2), two 3, ±7311 4 practical in many live in a of a. When "under the correction of no island under the action of many forms its a stem energy value. Induced muscle related use of resistance can 4 sea can or element south. Water
science or resistance to people thank, theory of design 1. P
to make up for the index, to,
use P is still weak, work time
115 effect of water E ratio around except *57[lipid cell 4 test old 2us article is, in time, water with
element water pure time. The type of
hu this station receives
total performance of the book Rui E square large living in the central point of the design of the new water:
8 Huishui year book teaching, heart car product: with
85%, happy year, heart contact people
non system large down, life room life, in
7.2 produced water treatment
7.11 the current scale of the water station should be based on the oil field produced water volume, the total wastewater volume and the recovery of other local industrial wastewater as the basis. The project is calculated according to the comprehensive water content of the oil field
7.2.2 the oil content of the raw water entering the water treatment station should not exceed 1000mz/1 the oil content of the water before the transmission should not exceed 50mg/1 the produced water after treatment, if used for reinjection, the water quality should meet the SYI6 oil field oil content According to the provisions of Article 20.2 of the "Sewage Treatment Design Code", when used for other purposes, it shall comply with the corresponding standards. 7.1.3 The selection of treatment technology shall be based on the nature of the oily pollutants and the requirements for reuse and reduction of external drainage. Under normal circumstances, water purification should be designed according to the process of oil removal, sedimentation, flotation, and filtration: if necessary, it can also be designed according to the in-depth treatment process such as multi-stage filtration and fine filtration.
7.3.4 In order to improve the treatment capacity and absorption effect of produced water: promote the use of high-end water treatment equipment such as inclined plate (tube) oil removal tanks, torsion oil removal tanks, flotation oil removal machines, cyclone oil removers and new filters.
7.3.5 New oil fields should be planned and designed according to the fully enclosed washing process of produced water treatment and water injection systems.
7.16 The effluent treatment system should be designed based on the basic considerations. Consider finding appropriate buffers, deoxidizers, bactericides and anti-fouling agents in appropriate locations, and try to achieve multiple uses with one dose. 7.27 Sewage treatment facilities should have sludge discharge facilities, and the discharged sludge must be properly handled to prevent environmental pollution.
7.3 Water supply, drainage and fire protection
7.1 The planning and design of oil field water sources should be subject to comprehensive water resource preparation and evaluation or have necessary technical and auxiliary exploration data. Under the premise of ensuring sufficient water volume and good water quality, the selection of water sources should be strongly demonstrated, and water sources should be fully utilized to avoid competing with agriculture for water. 7.3.2 The water supply capacity of oil field water sources should be calculated according to the total amount of oil field water injection, production water, domestic water, chemical water, and fire protection water. If necessary, the water use of oil field, agriculture and other industrial water use should also be considered.
7 .3.3 The layout of the oil field water supply network should first meet the water requirements of the field injection water supply, water injection water supply and other production water supply. The life supply should be a separate system, and the water supply pipeline can be connected to a large amount of water supply. 12 storage calculation
7.3.4 The flood control and drainage of the oil field area should be comprehensively managed in accordance with the local external conditions, in conjunction with the local relevant departments and local governments, and should be comprehensively planned and designed with the local unified rainfall rate, flow coefficient, and flood drainage standards. 7.35 The flood control and drainage of the oil field and the reservoir should be in line with the local flood control and drainage. Generally, open nests should be used, and they should be combined with road ditches and farmland drainage as much as possible. Drainage structures and equipment can be equipped according to the standard of three days of precipitation and four days of drainage. 7.3.6 The fire-fighting water of the oil field can make full use of the water supply network in the oil field. The layout and scale of oilfield firefighting stations shall comply with the provisions of Chapter 7, Section 2 of GB50183 “Code for Fire Protection Design of Crude Oil and Natural Gas Engineering”. 7.3.7 For stations with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.7 For stations and warehouses with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.7 For stations and warehouses with fixed-roof oil tanks with a single-dimensional capacity greater than or equal to 100m3 and floating-roof coffee tanks with a single-dimensional capacity greater than or equal to 50,000m3, fixed fire-fighting water supply systems and fixed-foot low-level foam fire extinguishers may be installed. Stations and warehouses with a fixed oil tank capacity of 100-10000m3 and a floating roof oil tank capacity of less than 50000m3 can be equipped with semi-fixed fire water supply system and semi-fixed low-multiple foam fire extinguishing system. Metering station: It is not advisable to set up fire-fighting facilities separately at the transfer station.
7.4 Power supply and distribution
7.4.1 Oil fields with a crude oil production capacity greater than 30x101/a should have an independent power supply. If conditions do not permit, a single power supply with dual circuits can be used. Oil fields far away from the regional power system should use other power sources. If necessary, a self-contained power station can also be built, but it should be demonstrated separately.
7.4.2 The capacity of substations at all levels in the oil field, the total load when the comprehensive water content is 50%, and the cross-section of the transmission line should be determined according to the power load when the comprehensive water content of the oil field is 70%. Industrial and civil power supply should be provided separately
7.4.3 According to the requirements for power supply reliability, oil field power is also divided into three levels: the classification of loads should comply with the provisions of "Design Regulations for Transformer and Distribution of Oil Fields and Long-distance Crude Oil Pipelines" SYJ33.
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