API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf

上传人:towelfact221 文档编号:399868 上传时间:2018-10-23 格式:PDF 页数:86 大小:605.47KB
下载 相关 举报
API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf_第1页
第1页 / 共86页
API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf_第2页
第2页 / 共86页
API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf_第3页
第3页 / 共86页
API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf_第4页
第4页 / 共86页
API PUBL 4702-2001 Technologies to Reduce Oil and Grease Content of Well Treatment Well Completion and Workover Fluids for Overboard Disposal《减少对石油和油脂的含量.修井液为过火处置技术》.pdf_第5页
第5页 / 共86页
亲,该文档总共86页,到这儿已超出免费预览范围,如果喜欢就下载吧!
资源描述

1、 TECHNOLOGIESTOREDUCEOILANDGREASECONTENTOFWELLTREATMENT, WELLCOMPLETION, ANDWORKOVERFLUIDSFOROVERBOARDDISPOSALRegulatory and Scientific AffairsPublication Number 4702March 2001American Petroleum InstituteEnvironmental, Health and Safety Missionand Guiding PrinciplesMISSIONThe members of the American

2、 Petroleum Institute are dedicated to continuousefforts to improve the compatibility of our operations with the environment whileeconomically developing energy resources and supplying high quality products andservices to consumers. We recognize our responsibility to work with the public, thegovernme

3、nt, and others to develop and to use natural resources in an environmen-tally sound manner while protecting the health and safety of our employees and thepublic. To meet these responsibilities, API members pledge to manage our busi-nesses according to the following principles using sound science to

4、prioritize risksand to implement cost-effective management practices:PRINCIPLES To recognize and to respond to community concerns about our raw materials,products and operations. To operate our plants and facilities, and to handle our raw materials and products in a manner that protects the environm

5、ent, and the safety and health of our employees and the public. To make safety, health and environmental considerations a priority in our plan-ning, and our development of new products and processes. To advise promptly, appropriate ofcials, employees, customers and the public of information on signi

6、cant industry-related safety, health and environmental haz-ards, and to recommend protective measures. To counsel customers, transporters and others in the safe use, transportation and disposal of our raw materials, products and waste materials. To economically develop and produce natural resources

7、and to conserve those resources by using energy efciently. To extend knowledge by conducting or supporting research on the safety, health and environmental effects of our raw materials, products, processes and waste materials. To commit to reduce overall emission and waste generation. To work with o

8、thers to resolve problems created by handling and disposal of haz-ardous substances from our operations. To participate with government and others in creating responsible laws, regula-tions and standards to safeguard the community, workplace and environment. To promote these principles and practices

9、 by sharing experiences and offering assistance to others who produce, handle, use, transport or dispose of similar raw materials, petroleum products and wastes.Technologies to Reduce Oil and GreaseContent of Well Treatment, WellCompletion, and Workover Fluidsfor Overboard DisposalRegulatory and Sci

10、entific Affairs DepartmentAPI Publication Number 4702PREPARED UNDER CONTRACT BY:Marc Halevy, ing.Conor Pacific Environmental Technologies, Inc.Mississauga, OntarioCanadaJULY 2000FOREWORDAPI publications necessarily address problems of a general nature. With respect to particular circum-stances, loca

11、l, state, and federal laws and regulations should be reviewed.API is not undertaking to meet the duties of employers, manufacturers, or suppliers to warn and prop-erly train and equip their employees, and others exposed, concerning health and safety risks and precau-tions, nor undertaking their obli

12、gations under local, state, or federal laws.Nothing contained in any API publication is to be construed as granting any right, by implication orotherwise, for the manufacture, sale, or use of any method, apparatus, or product covered by letterspatent. Neither should anything contained in the publica

13、tion be construed as insuring anyone against lia-bility for infringement of letters patent.All rights reserved. No part of this work may be reproduced, stored in a retrieval system, or transmitted by any means, electronic, mechanical, photocopying, recording, or otherwise, without prior written per-

14、mission from the publisher. Contact the Publisher, API Publishing Services, 1220 L Street, N.W., Washington, D.C. 20005.Copyright 2001 American Petroleum InstituteACKNOWLEDGMENTSTHE FOLLOWING PEOPLE ARE RECOGNIZED FOR THEIR CONTRIBUTIONS OF TIMEAND EXPERTISE DURING THIS STUDY AND IN THE PREPARATION

15、OF THISREPORT:API STAFF CONTACTRoger E. Claff, Regulatory and Scientific Affairs DepartmentMEMBERS OF THE PRODUCED WATER OIL AND GREASE WORKGROUPSyed Ali, Chevron Petroleum Technology CompanyKris Bansal, Conoco Inc.Larry Henry, Chevron USA, Inc.Sung-I Johnson, Phillips Petroleum CompanyZara Khatib,

16、Shell Development CompanyDavid LeBlanc, Texaco Exploration and Production, Inc.James Ray, Equilon Enterprises LLCJoseph Smith, Exxon Production Research CompanyDonna Stevison, Marathon Oil CompanySteve Tink, VASTAR Resources, Inc.The following colleagues were an essential part of this project and th

17、eir contributions weregreatly appreciated: Abbas Zaidi, Dan Caudle, Samira Nawar, Nadine Toscani, and FanjianMeng.ABSTRACTThe flowback of non-produced fluids to surface de-oiling facilities on offshore platforms cancreate severe process upsets. Consequently, meeting oil and grease (O technology revi

18、ew and screening at laboratory scale; and bench scaletechnology development of the most promising technology.To properly simulate NPF flowback, the first phase targeted the collection and review ofchemical use procedures. A reduced-scale sand pack column simulated a downhole sandstoneformation. Form

19、ulation and fluid preparation procedures were established for produced water,well stimulation solutions, and non-produced fluids. A nitrogen gas flotation process was usedto simulate produced water de-oiling operations. Experimental protocols and O Polymer-modified clay adsorption; Iron-catalyzed hy

20、drogen peroxide advanced oxidation; Liquid-liquid extraction; Electro-coagulation; and Membrane filtration.Based on laboratory scale treatability data, two processes were initially retained: granularactivated carbon (GAC) adsorption and iron-catalyzed hydrogen peroxide oxidation. Althoughboth techno

21、logies demonstrated similar performance at laboratory scale, chemical oxidation wasabandoned in favor of adsorption. This decision was based on technical and logistic scale-upconsiderations, safety requirements, process flexibility, process control needs, and capital costs.Bench scale technology dev

22、elopment activities were pursued on GAC adsorption. A polymer-modified clay adsorbent (PCA) was also included in the bench scale experimental work since ithas recently been introduced to offshore operations for the treatment of non-produced fluidsfrom acidizing operations. The performance of PCA ads

23、orption was evaluated both as analternative to the GAC process and as a pretreatment step.Two discharge options for the treated NPF were investigated: 1) direct overboard discharge, and2) indirect overboard discharge entailing controlled blending of treated NPF with produced waterprior to final de-o

24、iling treatment by flotation. Adsorption performance was investigated on rawNPF (R-NPF), characterized by high dissolved O and on produced waterspiked NPF (PW-NPF), characterized byhigh dissolved and emulsified O Ali, 1997; Caudle, 1996): Acidizing additives, such as mutual solvents, surfactants, an

25、d corrosion inhibitors; Precipitates formed during acidizing, including colloidal ferric hydroxides; Iron (III) interactions with asphaltenes; Oil-wetted solids, including corrosion and scale compounds and formation fines; and Acidity of return non-produced fluids.Although the industry is engineerin

26、g well stimulation formulations and procedures forsatisfactory formation acidizing while reducing the impact of fluid returns on de-oiling facilities,these measures alone are not capable of eliminating operational problems (Bansal, 1993; Ali andHill, 1997; Hebert and Khatib, 1996). As part of the de

27、velopment of these integrated systemapproaches, effective point-source treatment processes, designed to selectively removecontaminants responsible for stabilizing emulsions and inducing process upsets, need to bedeveloped.Based on current industry needs, the American Petroleum Institute (API) initia

28、ted thisindependent study to identify effective technologies for the point-source treatment of non-produced fluids. The study was structured into four phases: Phase I consisted of collecting and reviewing current chemical use and procedures. Phase II targeted the laboratory simulation of produced wa

29、ter (PW), non-produced fluids(NPF), and a blend of PW and NPF (termed “combined fluids,” CF). It also included the set-up of a sand pack column simulating a sandstone formation, and the set-up of an induced gasflotation process for produced water de-oiling. Oil and grease (O 2) produced water, follo

30、wing treatment inthe flotation cell; 3) well stimulation solutions and fluids; and 4) non-produced fluids.Table 6 presents Freon-extractable O&G data for the 0.5% solutions of each wellstimulation chemical formulation in a 100 g/L salt solution (35 g/L sea salt and 65 g/Lsodium chloride). Table 6 il

31、lustrates that even at 0.5% concentration, high O&Gconcentrations (193-721 mg/L) were measured for the corrosion inhibitor, anti-sludge, andsurfactant formulations. Significantly lower O&G concentrations (1246 mg/L) weremeasured for the clay and iron stabilizer formulations.Table 7 presents Freon-ex

32、tractable O&G data for each of the four well stimulation solutionsprior to contacting the sand pack. High O&G concentrations (1166-4648 mg/L) were measuredfor each well stimulation stock solution. These high O&G concentrations primarily reflect thehigh concentrations of organic solvents and surfacta

33、nts present in well stimulation formulations.These measurements were made on raw stock solutions prior to downflow contacting of the sandpack.The stock solutions were pumped downflow through the sand pack. Each well stimulation fluidwas collected in a separate container following downflow contacting. An aliquot of each fluid,

展开阅读全文
相关资源
  • API SALES OF NGL & LRG-2018 2016 Sales of Natural Gas Liquids and Liquefied Refinery Gas.pdfAPI SALES OF NGL & LRG-2018 2016 Sales of Natural Gas Liquids and Liquefied Refinery Gas.pdf
  • API MPMS 9 4-2018 Manual of Petroleum Measurement Standards Chapter 9 4-Continuous Density Measurement Under Dynamic (Flowing) Conditions (FIRST EDITION).pdfAPI MPMS 9 4-2018 Manual of Petroleum Measurement Standards Chapter 9 4-Continuous Density Measurement Under Dynamic (Flowing) Conditions (FIRST EDITION).pdf
  • API MPMS 9 3-2012 Manual of Petroleum Measurement Standards Chapter 9 3 Standard Test Method for Density Relative Density and API Gravity of Crude Petroleum and.pdfAPI MPMS 9 3-2012 Manual of Petroleum Measurement Standards Chapter 9 3 Standard Test Method for Density Relative Density and API Gravity of Crude Petroleum and.pdf
  • API MPMS 9 2-2012 Manual of Petroleum Measurement Standards Chapter 9 2 Standard Test Method for Density or Relative Density of Light Hydrocarbons by Pressure H.pdfAPI MPMS 9 2-2012 Manual of Petroleum Measurement Standards Chapter 9 2 Standard Test Method for Density or Relative Density of Light Hydrocarbons by Pressure H.pdf
  • API MPMS 9 1-2012 Manual of Petroleum Measurement Standards Chapter 9 1 Standard Test Method for Density Relative Density or API Gravity of Crude Petroleum and .pdfAPI MPMS 9 1-2012 Manual of Petroleum Measurement Standards Chapter 9 1 Standard Test Method for Density Relative Density or API Gravity of Crude Petroleum and .pdf
  • API MPMS 8 5-2015 Manual of Petroleum Measurement Standards Chapter 8 5 Standard Practice for Manual Piston Cylinder Sampling for Volatile Crude Oils Condensate.pdfAPI MPMS 8 5-2015 Manual of Petroleum Measurement Standards Chapter 8 5 Standard Practice for Manual Piston Cylinder Sampling for Volatile Crude Oils Condensate.pdf
  • API MPMS 8 5 SPANISH-2015 Manual of Petroleum Measurement Standards Chapter 8 5 - Standard Practice for Manual Piston Cylinder Sampling for Volatile Crude Oils .pdfAPI MPMS 8 5 SPANISH-2015 Manual of Petroleum Measurement Standards Chapter 8 5 - Standard Practice for Manual Piston Cylinder Sampling for Volatile Crude Oils .pdf
  • API MPMS 8 4-2017 Manual of Petroleum Measurement Standards Chapter 8 4 Standard Practice for Sampling and Handling of Fuels for Volatility Measurement (FOURTH .pdfAPI MPMS 8 4-2017 Manual of Petroleum Measurement Standards Chapter 8 4 Standard Practice for Sampling and Handling of Fuels for Volatility Measurement (FOURTH .pdf
  • API MPMS 8 4-2014 Manual of Petroleum Measurement Standards Chapter 8 4 Standard Practice for Sampling and Handling of Fuels for Volatility Measurement (THIRD E.pdfAPI MPMS 8 4-2014 Manual of Petroleum Measurement Standards Chapter 8 4 Standard Practice for Sampling and Handling of Fuels for Volatility Measurement (THIRD E.pdf
  • API MPMS 8 3-1995 Manual of Petroleum Measurement Standards Chapter 8 - Sampling Section 3 - Standard Practice for Mixing and Handling of Liquid Samples of Petr.pdfAPI MPMS 8 3-1995 Manual of Petroleum Measurement Standards Chapter 8 - Sampling Section 3 - Standard Practice for Mixing and Handling of Liquid Samples of Petr.pdf
  • 猜你喜欢
    相关搜索

    当前位置:首页 > 标准规范 > 国际标准 > API

    copyright@ 2008-2019 麦多课文库(www.mydoc123.com)网站版权所有
    备案/许可证编号:苏ICP备17064731号-1