E04 基础标准与通用方法 标准查询与下载

GPA STD 2145-2009 天然气工业感兴趣的碳氢化合物和其它合成物物理性质表

Table of Physical Properties for Hydrocarbons and Other Compounds of Interest to the Natural Gas Industry

Table of Physical Properties for Hydrocarbons and Other Compounds of Interest to the Natural Gas Industry

KS M ISO 1998-2:2008 石油工业.术语.第2部分:特性和试验

이 표준은 석유산업의 석유제품 특성과 시험방법에서 사용되는 용어 정의 리스트로 이루어져 있

Petroleum industry－Terminology－Part 2：Properties and tests

KS M ISO 1998-1:2008 石油工业.术语.第1部分:原材料和产品

KS M ISO 1998은 원유와 석유 제품을 취급하는 석유 산업부터, 생산 현장에서 최종

Petroleum industry－Terminology－Part 1：Raw materials and products

KS M ISO 1998-3:2008 石油工业.术语.第3部分:勘探和生产

KS M ISO 1998은 원유와 석유 제품을 취급하는 석유 산업부터, 생산 현장에서 최종

Petroleum industry－Terminology－Part 3：Exploration and production

SY/T 0030-2008 油气田及管道腐蚀与防护工程基本词汇

本标准规定了油气田及管道腐蚀与防护工程的基本词汇，并统一其含义。 本标准适用于油气田及管道腐蚀与防护工程的设计、施工和管理。

Vocabulary of corrosion protection-engineering for oil and gas field and pipeline

ISO/TS 29041:2008 气体混合物.重量分析准备.控制成分的相关性

In this Technical Specification, the gravimetric mixture preparation as given in ISO 6142 is investigated for influences of a priori existing, as well as correlations introduced by data processing. All calculations refer to an example which consists in the preparation of a synthetic natural gas of a target composition as follows: 1,4 mol % N2, 1,8 mol % CO2, 9,4 mol % ethane, 3,4 mol % propane, 1 mol % nbutane, and 83 mol % methane. All considerations given for this example concerning mixture feasibility, choice of preparation procedure, and weighing steps and sequences are the same as given in ISO 6142. This also applies to all estimates for basic uncertainty sources and the purity tables of the gases used for preparation. All calculations follow the principles, and use the tools and algorithms laid down in Annex A. For the sake of simplicity, procedural steps such as matrix transformation, inversion or matrix calculus are not detailed each time they are used in the calculations.

Gas mixtures - Gravimetric preparation - Mastering correlations in composition

ASTM D1250-08 石油测量表使用的标准指南

The expanded limits of API MPMS Chapter 11.1–2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250–04 (ADJD1250CD) are defined in a mixture of terms of customary and metric units. Table 1 shows the defining limits and their associated units in bold italics. Also shown in Table 1 are the limits converted to their equivalent units (and, in the case of the densities, other base temperatures). Note that only the precision levels of the defining values shown in Table 1 are correct. The other values showing converted units have been rounded to the significant digits shown; as rounded values, they may numerically fall just outside of the actual limits established by the defining values. Table 2 provides a cross-reference between the historical table designations and the corresponding section in API MPMS Chapter 11.1–2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250–04 (ADJD1250CD). Note that procedure paragraphs 11.1.6.3 (U.S. customary units) and 11.1.7.3 (metric units) provide methods for correcting on-line density measurements from live conditions to base conditions and then to compute CTPL factors for continuous volume corrections to base conditions. 4.4 When a glass hydrometer is used to measure the density of a liquid, special corrections must be made to account for the thermal expansion of the glass when the temperature is different from that at which the hydrometer was calibrated. The 1980 CTL Tables had generalized equations to correct glass hydrometer readings, and these corrections were part of the printed odd-numbered tables. However, detailed procedures to correct a glass hydrometer reading are beyond the scope of API MPMS Chapter 11.1–2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250–04 (ADJD1250CD). The user should refer to the appropriate sections of API MPMS Chapter 9 or other appropriate density/hydrometer standards for guidance. 4.5 The set of correlations given in API MPMS Chapter 11.1–2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250–04 (ADJD1250CD) is intended for use with petroleum fluids comprising either crude oils, refined products, or lubricating oils that are single-phase liquids under normal operating conditions. The liquid classifications listed here are typical terms used in the industry, but local nomenclature may vary. The list is illustrative and is not meant to be all-inclusive. 4.6 Crude Oils8212;A crude oil is considered to conform to the commodity group Generalized Crude Oils if its density falls in the range between approximately –10°API to 100°API. Crude oils that have been stabilized for transportation or storage purposes and whose API gravities lie within that range are considered to be part of the Crude Oil group. Also, aviation jet B (JP-4) is best represented by the Crude Oil correlation. 4.7 Refined Products8212;A refined product is considered to conform to the commodity group of Generalized Refined Products if the fluid falls within one of the refined product groups. Note the product descriptors are generalizations. The commercial specification ranges of some products may place their densities partly within an adjacent class (for example, a low density diesel may lie in the jet fuel class). In such cases, the product shoul......

Standard Guide for Use of the Petroleum Measurement Tables

ASTM D6300-08 用于石油产品和润滑油的试验方法中的精密性和偏差数据测定的标准实施规程

ASTM test methods are frequently intended for use in the manufacture, selling, and buying of materials in accordance with specifications and therefore should provide such precision that when the test is properly performed by a competent operator, the results will be found satisfactory for judging the compliance of the material with the specification. Statements addressing precision and bias are required in ASTM test methods. These then give the user an idea of the precision of the resulting data and its relationship to an accepted reference material or source (if available). Statements addressing determinability are sometimes required as part of the test method procedure in order to provide early warning of a significant degradation of testing quality while processing any series of samples. Repeatability and reproducibility are defined in the precision section of every Committee D02 test method. Determinability is defined above in Section 3. The relationship among the three measures of precision can be tabulated in terms of their different sources of variation (see Table 1). When used, determinability is a mandatory part of the Procedure section. It will allow operators to check their technique for the sequence of operations specified. It also ensures that a result based on the set of determined values is not subject to excessive variability from that source. A bias statement furnishes guidelines on the relationship between a set of test results and a related set of accepted reference values. When the bias of a test method is known, a compensating adjustment can be incorporated in the test method. This practice is intended for use by D02 subcommittees in determining precision estimates and bias statements to be used in D02 test methods. Its procedures correspond with ISO 4259 and are the basis for the Committee D02 computer software, Calculation if Precision Data: Petroleum Test Methods. The use of this practice replaces that of Research Report RR:D02–1007. Standard practices for the calculation of precision have been written by many committees with emphasis on their particular product area. One developed by Committee E11 on Statistics is Practice E 691. Practice E 691 and this practice differ as outlined in Table 2. TABLE 1 Sources of Variation MethodApparatusOperatorLaboratoryTime ReproducibilityCompleteDifferentDifferentDifferentSpecified (Result) RepeatabilityCompleteSameSame SameAlmost same (Result) Dete.......

Standard Practice for Determination of Precision and Bias Data for Use in Test Methods for Petroleum Products and Lubricants

NFPA 58-2007 液化石油气规则.2008版

This code applies to the storage, handling, transportation, and use of LP-Gas.

Liquefied Petroleum Gas Code 2008 Edition

ASTM F2152-07 溢出油就地燃烧的标准指南:耐火臂

1.1 This guide covers a set of criteria to evaluate the performance, material characteristics, and essential features of fire-resistant oil spill containment boom.1.2 This guide covers two types of fire-resistant oil containment boom: those that are intrinsically fire-resistant through the use of fire-resistant materials, and those that provide fire-resistance through the use of coolants. This guide may not be fully applicable to other types of fire-resistant boom.1.3 This guide is one of four related to in-situ burning of oil spills. Guide F 1788 addresses environmental and operational considerations, Guide F 1990 addresses ignition devices, and Guide F 2230 addresses burning in ice conditions.1.4 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory requirements prior to use.

Standard Guide for In-Situ Burning of Spilled Oil: Fire-Resistant Boom

ASTM D3244-07 利用试验数据测定规范符合性的标准实施规程

1.1 This practice covers guidelines and statistical methodologies with which two parties, usually a supplier and a receiver, can compare and combine independently obtained test results to obtain an Assigned Test Value (ATV) for the purpose of resolving a product quality dispute.1.2 This practice defines a technique for comparing an assigned test value with a specification limit.1.3 This practice applies only to those test methods which specifically state that the repeatability and reproducibility values conform to the definitions herein.

Standard Practice for Utilization of Test Data to Determine Conformance with Specifications

ASTM D3244-07a 利用试验数据测定规范符合性的标准实施规程

1.1 This practice covers guidelines and statistical methodologies with which two parties, usually a supplier and a receiver, can compare and combine independently obtained test results to obtain an Assigned Test Value (ATV) for the purpose of resolving a product quality dispute.1.2 This practice defines a technique for comparing an assigned test value with a specification limit.1.3 This practice applies only to those test methods which specifically state that the repeatability and reproducibility values conform to the definitions herein.

Standard Practice for Utilization of Test Data to Determine Conformance with Specifications

ASTM D1250-07 石油测量表使用标准指南

1.1 The API MPMS Chapter 11.1-2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250-04 (ADJD1250CD) for temperature and pressure volume correction factors for generalized crude oils, refined products, and lubricating oils, provides the algorithm and implementation procedure for the correction of temperature and pressure effects on density and volume of liquid hydrocarbons. Natural gas liquids (NGLs) and liquefied petroleum gases (LPGs) are excluded from consideration. The combination of density and volume correction factors for both temperature and pressure is collectively referred to in the standard/adjunct(s) as a Correction for Temperature and Pressure of a Liquid (CTPL). The temperature portion of this correction is termed the Correction for the effect of Temperature on Liquid (CTL), also historically known as VCF (Volume Correction Factor). The pressure portion is termed the Correction for the effect of Pressure on Liquid (CPL). As this standard will be applied to a variety of applications, the output parameters specified in this standard/adjunct(s) (CTL, Fp, CPL, and CTPL) may be used as specified in other standards.1.2 Including the pressure correction in API MPMS Chapter 11.1-2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250-04 (ADJD1250CD) represents an important change from the "temperature only" correction factors given in the 1980 Petroleum Measurement Tables. However, if the pressure is one atmosphere (the standard pressure) then there is no pressure correction and the standard/adjunct(s) will give CTL values consistent with the 1980 Petroleum Measurement Tables.1.3 API MPMS Chapter 11.1-2004/Adjunct to IP 200/04/Adjunct to ASTM D 1250-04 (ADJD1250CD) covers general procedures for the conversion of input data to generate CTL, Fp, CPL, and CTPL values at the user specified base temperature and pressure ( Tb, Pb). Two sets of procedures are included for computing volume correction factor: one set for data expressed in customary units (temperature in F, pressure in psig); the other for the metric system of units (temperature in C, pressure in kPa or bar). In contrast to the 1980 Petroleum Measurement Tables, the metric procedures require the procedure for customary units be used first to compute density at 60176;F. This value is then further corrected to give the metric output. The metric procedures now incorporate the base temperature of 20176;C in addition to 15176;C.1.4 The procedures recognize three distinct commodity groups: crude oil, refined products, and lubricating oils. A procedure is also provided for determining volume correction for special applications where the generalized commodity groups' parameters may not adequately represent the thermal expansion properties of the liquid and a precise thermal expansion coefficient has been determined by experiment.

Standard Guide for Use of the Petroleum Measurement Tables

ASTM F1990-07 溢出油原地燃烧的标准指南:点火装置

This guide describes the requirements for igniting oil for the purpose of in-situ burning. It is intended to aid decision-makers and spill-responders in contingency planning, spill response, and training, and to aid manufacturers in developing effective ignition devices. This guide describes criteria for the design and selection of ignition devices for in-situ burning applications. This guide is not intended as a detailed operational manual for the ignition and burning of spilled oil.1.1 This guide relates to the use of in-situ burning of spilled oil. The focus of the guide is in-situ burning of oil on water, but the ignition techniques and devices described in the guide are generally applicable to in-situ burning of oil spilled on land as well.1.2 The purpose of this guide is to provide information that will enable oil-spill responders to select the appropriate techniques and devices to successfully ignite oil spilled on water.1.3 This guide is one of four related to in-situ burning of oil spills. Guide F 1788 addresses environmental and operational considerations. Guide F 2152 addresses fire-resistant booms, and Guide F 2230 addresses burning in ice conditions.1.4 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and to determine the applicability of regulatory limitations prior to use. In particular, the storage, transport, and use of ignition devices may be subject to regulations that will vary according to the jurisdiction. While guidance of a general nature is provided herein, users of this guide should determine regulations that apply to their situation.

Standard Guide for In-Situ Burning of Spilled Oil: Ignition Devices

ASTM F2533-07 海船或其他船舶中油I现场燃烧的标准指南

This guide is primarily intended to aid decision-makers and spill-responders in contingency planning, spill response, and training. This guide is general and site conditions can change the situation considerably.1.1 This guide covers the use of in-situ burning directly in ships and other vessels. This guide is not applicable to in-situ burning of oil on sea or land.1.2 This guide is applicable to situations in which the vessel and cargo are not salvageable. After the burn, the vessel will never be salvageable. It is intended that the in-situ burning of oil spills in ships be a last resort option.1.3 The purpose of this guide is to provide information that will enable spill responders to decide if burning will be used to remove oil from stranded ships or other vessels.1.4 This is a general guide only. It is assumed that conditions at the spill site have been assessed and that these conditions are suitable for the burning of oil. It is also assumed that permissions to burn the oil have been obtained. Variations in the behavior of different oil types are not dealt with and may change some of the parameters noted in this guide.1.5 This guide is one of several related to in-situ burning.1.6 There are many safety concerns associated with in-situ burning of oil in ships. These include the unsafe nature of the wrecked vessel and the use of explosives.1.7 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use.

Standard Guide for In-Situ Burning of Oil in Ships or Other Vessels

SY/T 0043-2006 油气田地面管线和设备涂色规范

本标准规定了油气田和管道工程中的地面管线、设备和钢结构的涂色，便于生产操作、管理检修，减少误操作，有利于安全生产。 本标准适用于油气田地面工程和管道工程新建或改扩建项目的地面管线、设备以及钢结构的表面涂色和标志。 本标准不适用于炼油厂、化工厂。

Code for painting colors of pipelines and equipments in oil-gas field

SY/T 0082.3-2006 石油天然气工程初步设计内容规范 第3部分:天然气处理厂工程

SY/T 0082的本部分规定了天然气处理厂工程项目初步设计文件的组成、工程设计及概算的具体内容和深度要求。 本部分适用于新建陆上天然气处理厂的初步设计。扩建、改建天然气处理厂和新建单独的工艺装置、天然气脱硫站、天然气脱水站、LNG工程的初步设计可参照执行。 天然气处理厂初步设计的内容除应符合本规范外，尚应符合国家现行的有关强制性标准的规定。

Code for preliminary design of petroleum & natural gas engineering. Part 3: Natural gas treating plant engineering

ASTM G170-06(2012) 实验室中对油田和精炼厂腐蚀抑制剂评测的评价指南

5. Significance and UseTop Bottom 5.1 Corrosion inhibitors continue to play a key role in controlling internal corrosion associated with oil and gas production and transportation. This results primarily from the industry's extensive use of carbon and low alloy steels, which, for many applications, are economic materials of construction that generally exhibit poor corrosion resistance. As a consequence, there is a strong reliance on inhibitor deployment for achieving cost-effective corrosion control, especially for treating long flowlines and main export pipelines (1).6 5.2 For multiphase flow, the aqueous-oil-gas interphases can take any of an infinite number of possible forms. These forms are delineated into certain classes of interfacial distribution called flow regimes. The flow regimes depend on the inclination of the pipe (that is, vertical or horizontal), flow rate (based on production rate), and flow direction (that is, upward or downward). The common flow regimes in vertical upward flow, vertical downward flow, and horizontal flow are presented in Figs. 1-3 respectively (2, 3). Note 1?????G and ??L are gas and liquid densities and UL and UG are superficial velocities or the volume of flow rates of the liquid and gas per unit cross-sectional area of the channel (2).FIG. 1 Flow Regimes for Vertical Upward Multiphase Flow FIG. 2 Flow Regimes for Vertical Downward Flow (2) Note 1???Boundary conditions given by two studies are presented.(2) FIG. 3 Flow Regimes for Horizontal Flow

Standard Guide for Evaluating and Qualifying Oilfield and Refinery Corrosion Inhibitors in the Laboratory

ASTM F2465-05 漏油分散剂应用设备标准指南:单点喷射系统

1.1 This guide covers performance criteria, requirements, material characteristics, and essential features for oil spill dispersant application systems. This guide is not intended to be restrictive to a specific configuration.1.2 This guide covers vessel-based spray systems employing single-point spray nozzles, including designs that have been based on or evolved from "fire-monitor" systems, and is not fully applicable to other systems such as spray boom/nozzle or aircraft systems.1.3 This guide is one of five related to dispersant application systems. The other four guides cover the design of boom and nozzle systems, spray system calibration, spray deposition measurements, and use of the systems. Familiarity with all five guides (listed in ) is recommended.1.4 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use.

Standard Guide for Oil Spill Dispersant Application Equipment: Single-point Spray Systems

ASTM D5765-05(2010) 用封闭式容器微波加热法从土壤和沉积物中溶剂萃取全部石油烃物质的标准操作规程

Solvent extraction of soils and sediments can provide information on the availability of petroleum hydrocarbons to leaching, water quality changes, or other site conditions. Rapid heating, in combination with temperatures in excess of the atmospheric boiling point of acetone/hexane, reduces sample preparation or extraction times. Reduced amounts of solvents are required and solvent loss due to boiling and evaporation are eliminated by use of closed extraction vessels.1.1 This practice covers the solvent extraction of total petroleum hydrocarbon (TPH) from soils and sediments, using closed vessel microwave heating, for subsequent determination by gravimetric or gas chromatographic techniques. 1.2 This practice is recommended only for solid samples that can pass through a ten mesh screen (approximately 2 mm openings). 1.3 The solvent extract obtained by this practice may be analyzed for total or specific nonvolatile and semivolatile petroleum hydrocarbons but may require sample clean-up procedures prior to specific compound analysis. 1.4 This practice is limited to solvents that are recommended for use in microwave solvent extraction systems. 1.5 The values stated in pounds per square inch (psi) are to be regarded as the standard. The SI units given in parentheses are for information only. 1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use. Specific hazard statements are given in Section 8.

Standard Practice for Solvent Extraction of Total Petroleum Hydrocarbons from Soils and Sediments Using Closed Vessel Microwave Heating