75.180.99 其他石油和天然气工业设备 标准查询与下载



共找到 89 条与 其他石油和天然气工业设备 相关的标准,共 6

Guidelines for Safety Assessment of Main Structures of Aging Offshore Stationary Production Facilities

ICS
75.180.99
CCS
E 94
发布
2020-11-10
实施
2021-05-01

Technical requirements for charging facilities of refueling and refueling stations

ICS
75.180.99
CCS
E 90
发布
2019-10-29
实施
2019-11-29

1.1 This practice covers the evaluation of the degree of rusting on painted steel surfaces. The visual examples which depict the percentage of rusting given in the written specifications form part of the standard. In the event of a dispute, the written definition prevails. These visual examples were developed in cooperation with SSPC: The Society for Protective Coatings to further standardization of methods. The photographs can be used to estimate the percentage of other coating defects on various substrates. This standard does not include evaluation of rust propagation around an initially prepared scribe, score, or holiday. 1.2 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.3 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

Standard Practice for Determining the Performance of Oil/Water Separators Subjected to Surface Run-Off

ICS
75.180.99
CCS
发布
2019
实施
0000-00-00

1.1 This practice describes the testing procedure, any necessary related apparatus, and the sampling technique to be used in determining the performance characteristics of an oil/water separator subjected to the sudden release of a relatively large quantity of hydrocarbons that may appear in its influent in pure form or at high concentration. 1.2 This practice does not address the determination of the performance characteristics of an oil/water separator subjected to surface run-off resulting from rain water draining from improved or unimproved land. In this case, refer to Practice D6104. 1.3 This practice does not address the determination of the performance characteristics of an oil/water separator subjected to a mechanically emulsified influent such as provided by a pump. 1.4 This practice does not investigate the ability of the separator to handle debris or suspended solids, that is, grit or tree leaves. 1.5 While the effluent may meet code requirements for total oil and grease content, this practice does not address the presence of soluble organics, that is, benzene, toluene, ethylbenzene, and xylene (BTEXs) that may be detected in the effluent. It also does not make any provisions for the effects of detergents, surfactants, soaps or any water soluble matter (that is, salts) or any portion of an essentially insoluble matter that may be found in solution on separation. (Effects of certain water soluble chemicals or solids may be investigated by adding them to the water at predetermined constant concentrations.) 1.6 In order to estimate the effect of water temperature on the performance of the separator, the tests described in this practice must be performed at two water temperatures. The selected temperatures must be at least 10°C (18°F) apart, with the temperature ranging from a minimum of 0°C (32°F) to a maximum of 50°C (122°F). 1.7 This practice does not make any provisions for the variation of pH or temperature during a test run. Refer to Appendix X1 for further detail. 1.8 This practice can be used with a variety of hydrocarbons. It adopts No. 2 fuel oil with a density2 of 845 kg/ m3 (52.73 lbm/ft3 ) and a viscosity2 of 1.9 to 4.1 centistokes at 40°C (104°F) and SAE 90 lubricating oil with a density (See SAE J313) of 930 kg/m3 (58 lbm/ft3 ) at 15.5°C (60°F) and a viscosity (see SAE J306) of 13.5 to

Standard Practice for Determining the Performance of Oil/Water Separators Subjected to a Sudden Release

ICS
75.180.99
CCS
发布
2017-12-15
实施

1.1 This practice covers the procedure, any necessary related apparatus, and the sampling technique to be used in determining the performance characteristics of oil/water separators subjected to contaminated run-off. 1.2 This practice does not address the determination of the performance characteristics of an oil/water separator subjected to the sudden release of a relatively large quantity of hydrocarbons that may appear, in pure form or at high concentration, in the influent to the separator. In this case, refer to Practice D6157. 1.3 This practice does not address the determination of the performance characteristics of an oil/water separator subjected to a mechanically emulsified influent such as provided by a pump. 1.4 This practice does not investigate the ability of the separator to handle debris or suspended solids, that is, grit or tree leaves. 1.5 While the effluent may meet code requirements for total oil and grease content, this practice does not address the presence of soluble organics, that is, benzene, toluene, ethylbenzene, and zylene (BTEXs) which may be detected in the effluent. It also does not make any provisions for the effects of detergents, surfactants, soaps, or any water soluble matter (that is, salts), or any portion of an essentially insoluble matter that may be found in solution on separation. (Effects of certain water soluble chemicals or solids may be investigated by adding them to the water at predetermined constant concentrations.) 1.6 In order to estimate the effect of water temperature on the performance of the separator, the tests described in this practice must be performed at two water temperatures. The selected temperatures must be at least 10°C (18°F) apart, with the temperature ranging from a minimum of 0°C (32°F) to a maximum of 50°C (122°F). 1.7 This practice does not make any provisions for the variation of pH or temperature during a test run. Refer to Appendix X1 for further detail. 1.8 This practice can be used with a variety of hydrocarbons. It adopts No. 2 fuel oil with a density2 of 845 kg/m3 (52.73 lbm/ft3 ) and a viscosity2 of 1.9 to 4.1 centistokes at 40°C (104°F) and SAE 90 lubricating oil with a density2 of 930 kg/m3 (58 lbm/ft3 ) at 15.5°C (60°F) and a viscosity (see SAE J313) of 13.5 to < 24 centistokes at 100°C (212°F) as the comparative testing media. It is understood that the results obtained from this practice are only directly applicable to No. 2 fuel oil and SAE 90 lubricating oil for the tested concentrations and only careful interpolation or extrapolation, or both, is allowed to other hydrocarbons. Low viscosity or high density hydrocarbons or hydrocarbons that contain a larger fraction of highly soluble compounds may need to be tested separately. NOTE 1—No extrapolation outside the range of the tested influent or effluent oil concentrations is allowed as performance may not be linear. Hence, to establish performance at a higher or lower concentration, the separator shall be tested for that specific condition. In addition, linearity must be established prior to using linear interpolation. 1.9 Since regulations are based on effluent total hydrocarbon content, this practice does not set forth any lower limits on oil particle size for the evaluation of separator efficiency. However, a standardized means for mixing oil and water shall be specified to ensure repeatability. It must be noted however that smaller particles, having a greater surface area to volume ratio, rise at a slower rate than their larger counterparts. (Guide F933 requires that 20 % of all oil particles be smaller than or equal to 50 µm and IMO MEPC 60 (30) does not mention any particle size requirements but asks the user to avoid emulsion causing chemicals.) 1.10 Although the tests described in this practice intend to simulate contaminated storm water run-off separation 1 This practice is under the jurisdiction of ASTM Committee D19 on Water and is the direct responsibility of D19.06 on Methods for Analysis for Organic Substances in Water Current edition approved Dec. 15, 2017. Published January 2018. Originally approved in 1997. Last previous edition approved in 2011 as D6104 – 97 (2011). DOI: 10.1520/D6104-97R17E01. 2 Bolz, R. E., and Tuve, G. L., CRC Handbook of tables for Applied Engineering Science, 2nd Edition, CRC Press, 1981. Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee. 1 requirements, they do not cover all possible applications. It is the end user’s responsibility to determine whether his separation requirements are within the scope of this practice. 1.11 A product different from the general description herein may be tested and found to be in compliance with the performance criteria set forth. 1.12 The values stated in SI units are to be regarded as standard. The values given in parentheses are mathematical conversions to inch-pound units that are provided for information only and are not considered standard. 1.13 This practice does not purport to address all the environmental hazards, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate environmentally responsible practices and to determine the applicability of regulatory limitations prior to use. 1.14 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.15 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

Standard Practice for Determining the Performance of Oil/Water Separators Subjected to Surface Run-Off

ICS
75.180.99
CCS
发布
2017-12-15
实施

Casing, tubing, line pipe and drill pipe thread protectors

ICS
75.180.99
CCS
E98
发布
2016-12-05
实施
2017-05-01

Gas distribution systems. Block gas delivery stations. Cabinet gas delivery stations. General technical requirements

ICS
75.180.99
CCS
发布
2016
实施
2017-09-01

Pipes for use as casing or tubing and couplings for them. Basic parameters and inspection of thread connections. General technical requirements

ICS
75.180.99
CCS
发布
2016
实施
2017-09-01

Thread connections for casing, tubing, line pipe and thread gauges for them. General technical requirements

ICS
75.180.99
CCS
N11
发布
2015
实施
2015-11-01

本规范适用于DN150~DN1500各种规格的钢质管道现场焊接接头内表面液体涂料补口机补口施工。公称直径小于150的钢质管道可参照执行。

Procedure specification of inner coating for welded joint with liquid paint by special machine for steel pipeline

ICS
75.180.99
CCS
E98
发布
2014-10-15
实施
2015-03-01

本规范规定了石油化工装置隔热耐磨衬里设备和管道到货检验、现场组焊、安装、施工检验等过程控制的质量标准和检验方法,明确了交工技术文件的要求。本规范适用于石油化工建设工程新建、扩建和改建项目催化裂化、甲醇制烯烃等装置隔热耐磨衬里设备和管道的施工质量验收。

Acceptance specification for construction quality of equipment and piping with thermal insulating and abrasion resistant refractory lining in petrochemical industry

ICS
75.180.99
CCS
P72
发布
2014-07-09
实施
2014-11-01

Gas distribution systems. Gas pressure regulating stations. Functional requirements

ICS
75.180.99
CCS
发布
2014
实施
2015-01-01

本标准适用于新建石油天然气站场的埋地钢质管道、金属设施的阴极保护设计、施工、验收及运行管理。已建的石油天然气站场的阴极保护可参照本标准执行。本标准不适用于大型罐区、油气田井场和LNG厂的阴极保护。

Specification of cathodic protection for petroleum & gas station

ICS
75.180.99
CCS
E98
发布
2013-11-28
实施
2014-04-01

本规范适用于天然气中硫化氢体积分数大于或等于5%的高含硫化氢气田地面集输系统的以下部分:--集输管道系统;--站场设施;--净化厂。本规范适用于失重挂片法、测试短节、电阻法、线性极化法、电化学噪声法、电感探针、电子指纹测量技术、渗氢法和环对腐蚀监测等腐蚀监测方法。

Technical code of on-line corrosion monitoring in gathering system for highly hydrogen sulfide gas field

ICS
75.180.99
CCS
E98
发布
2013-11-28
实施
2014-04-01

本规范规定了石油化工给水排水管道工程施工要求及质量标准。本规范适用于石油化工企业及以煤为原料制取燃料和化工产品企业工程建设的新建、改建、扩建工程的给水排水埋地和地上管道,以及装置区内消防系统地下管道的施工及验收。

Specification for construction and acceptance of water and sewerage pipeline in petrochemical industry

ICS
75.180.99
CCS
P71
发布
2013-10-17
实施
2014-03-01

本标准规定了撬装式CNG增压装置的结构、基本参数及型号、要求、试验方法、检验规则、出厂文件、标志、包装、运输及贮存。本标准适用于入口压力0~20MPa,工作环境温度-20℃~50℃,介质为压缩天然气的撬装式CNG增压装置(以下简称产品)。

Skid-mounted CNG booster

ICS
75.180.99
CCS
E98
发布
2013/01/15
实施
2013/01/15

本标准规定了天然气田气井、气田水回注井井史编制内容和要求。本标准适用于天然气田气井、气田水回注井的井史编制。

The compilation specification of well history of natural gas field

ICS
75.180.99
CCS
E12
发布
2012-08-23
实施
2012-12-01

本标准规定了天然气开发规划编制的原则、内容、方法和技术要求。本标准适用于气田气(含凝析气)的开发规划编制,油田伴生气、煤层气、页岩气参照执行。

Technical requirement for establishment of natural gas development plan

ICS
75.180.99
CCS
E12
发布
2012-08-23
实施
2012-12-01

本标准规定了双侧向测井仪、邻近侧向测井仪、微电极测井仪、微球形聚焦测井仪、双感应一八侧向测井仪、高分辨率感应—球形数字聚焦测井仪、高分辨率阵列感应测井仪和高频等参数感应测井仪(以下简称电法测井仪)的校准方法。本标准适用于新投产、使用中和维修后的电法测井仪的校准。

Calibration methods for electric log tools

ICS
75.180.99
CCS
E92
发布
2012-08-23
实施
2012-12-01

本标准规定了火烧油层实验过程中门槛温度、燃料消耗量、火烧油层驱油效率等基础参数的测定及计算方法。本标准适用于稠油油藏火烧油层基础参数测定。

Experimental testing method of in - situ combustion parameters

ICS
75.180.99
CCS
E11
发布
2012-08-23
实施
2012-12-01



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