API TR 6J1-2000 Elastomer Life Estimation Testing Procedures (First Edition)《弹性寿命估计测定过程.第1版》.pdf

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1、Elastomer Life Estimation Test i ng Procedu res API TR 6J1 FIRST EDITION, AUGUST 2000 American Petroleum Institute Helping You Get The Job Done Right.“ Elastomer Life Estimation Testing Procedures Upstream Segment API TR 6J1 FIRST EDITION, AUGUST 2000 American Petroleum Institute Helping You Get The

2、 Job Done Right2 SPECIAL NOTES API publications necessarily address problems of a general nature. With respect to partic- ular circumstances, local, state, and federal laws and regulations should be reviewed. API is not undertaking to meet the duties of employers, manufacturers, or suppliers to warn

3、 and properly train and equip their employees, and others exposed, concerning health and safety risks and precautions, nor undertaking their obligations under local, state, or fed- eral laws. Information concerning safety and health risks and proper precautions with respect to par- ticular materials

4、 and conditions should be obtained from the employer, the manufacturer or supplier of that material, or the material safety data sheet. Nothing contained in any API publication is to be construed as granting any right, by implication or otherwise, for the manufacture, sale, or use of any method, app

5、aratus, or prod- uct covered by letters patent. Neither should anything contained in the publication be con- strued as insuring anyone against liability for infringement of letters patent. Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. Sometime

6、s a one-time extension of up to two years will be added to this review cycle. This publication will no longer be in effect five years after its publication date as an operative API standard or, where an extension has been granted, upon republication. Status of the publication can be ascertained from

7、 the API Upstream Segment telephone (202) 682- 80001. A catalog of API publications and materials is published annually and updated quar- terly by API, 1220 L Street, N.W., Washington, D.C. 20005. This document was produced under API standardization procedures that ensure appropri- ate notification

8、and participation in the developmental process and is designated as an API standard. Questions concerning the interpretation of the content of this standard or com- ments and questions Concerning the procedures under which this standard was developed should be directed in writing to the general mana

9、ger of the Upstream Segment, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C. 20005. Requests for permission to reproduce or translate all or any part of the material published herein should also be addressed to the general manager. API standards are published to facilitate the br

10、oad availability of proven, sound engineer- ing and operating practices. These standards are not intended to obviate the need for apply- ing sound engineering judgment regarding when and where these standards should be utilized. The formulation and publication of API standards is not intended in any

11、 way to inhibit anyone from using any other practices. Any manufacturer marking equipment or materials in conformance with the marking requirements of an API standard is solely responsible for complying with all the applicable requirements of that standard. API does not represent, warrant, or guaran

12、tee that such prod- ucts do in fact conform to the applicable API standard. All rights reserved. No part of this work my be reproduced, stored in a retrieval system, or transmitted by any meuns, electronic, mechanical, photocopying, recording, or otherwise, without prior written permission from the

13、publisher. Contact the Publisher, API Publishing Services, 1220 L Street, N.W., Washington, D.C. 20005. Copyright O 2000 American Petroleum institute FOREWORD API publications may be used by anyone desiring to do so. Every effort has been made by the Institute to assure the accuracy and reliability

14、of the data contained in them; however, the Institute makes no representation, warranty, or guarantee in connection with this publication and hereby expressly disclaims any liability or responsibility for loss or damage resulting from its use or for the violation of any federal, state, or municipal

15、regulation with which this publication may conflict. Suggested revisions are invited and should be submitied to the general manager of the Upstream Segment, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C. 20005. iii CONTENTS Page 1 SCOPE . 1 2 REFERENCES 1 3 PROBLEMSTATEMENT . 1

16、4 LIFE ESTIMATION TECHNIQUE-OVERVIEW . 1 5 PROCEDURE FOR LIFE ESTIMATION TESTING OF ELASTOMERS . 2 6 SUMMARY . 4 Figures 1-Typical Life Estimation Plot 3 3-TypicaiTestCycle 5 2-0-RingTestFixture . 4 V Elastomer Life Estimation Testing Procedures 1 Scope Estimating the service life of elastomeric sea

17、ling elements used in severe environments, such as encountered in energy exploration and oil/gas production industries, has been extremely difficult. Elastomeric sealing elements are fre- quently exposed to methane, hydrogen sulfide, and carbon dioxide gases, along with crude oil, water and corrosio

18、n inhibiting chemicals. The proposed procedure outlines a tech- nique based on the Arrhenius principle of chemical reaction rates, which permits the life of an elastomeric material to be estimated when exposed to a severe service environment. The actual test procedure must be coordinated and agreed

19、upon between the supplier of the equipment that incorporates the elastomer sealing elements and the end user. The procedure should be based upon a definition of the service conditions and requirements such as: a. Temperature-steady state or a high and low range of service. b. Fluids and gases-stagna

20、nt or flowing. c. Pressure-continuous or a low and high range. d. Chemicals and additives-inhibitors, descalers, acidiz- ing, etc. e. Mechanical requirements-dynamic or static, torque, set- ting force. f. Failure criteria-pressure leakage, loss of mechanical function, inability to set or retrieve. 2

21、 References The following references are recommended as sources of additional information on the life prediction technique dis- cussed above: 1. Vicic, J.C., Testing of Polymers for Oil and Gas Appli- cations, American Chemical Society, Energy Rubber Group, 1984. 2. Abrams, P.I., Kennelley, K.J., Jo

22、hnson, D.V., A User?s Approach to Qualification of Dynamic Seals for Sour Gas Environments, American Chemical Society, Rubber Divi- sion, 1988. 3. Brady, J.E., Humiston, G.E., General Chemistry Prin- ciples and Structure, Third Edition, John Wiley the mini- mum internal volume should be equal to or

23、exceed 100 cc. The main body and end closures contain O-ring glands that are fabricated from an appropriate alloy. Typically, a corro- sion resistant alloy is used to fabricate the test fixture. Since thermo-chemical degradation of the elastomeric sealing ele- ment is of interest, thermo-mechanical

24、effects should be min- imized. Therefore, clearances between the end closure and the test vessel bore are minimized to eliminate extrusion (thermo-mechanicai type failure) of the candidate elastomer. If additional mechanical protection is required for the 0- ring seal, an anti-extrusion ring (back-u

25、p ring) of suitable material can be used. In life estimation testing, only the thermo-chemical effects of a severe environment on a candi- date elastomer are evaluated. Actual geometry and thermo- mechanical effects are bestevaluated using full scale testing. ELASTOMER LIFE ESTIMATION TESTING PROCED

26、URES 3 Log time to failure 1 07 1 06 105 1 04 103 1 o2 Temperature (OK) Figure 1-Typical Life Estimation Plot 5.2 The severe service environment is introduced into the test chamber formed by the two end closures. The test vessel is pressurized and heated to a predetermined temperature dur- ing each

27、test cycle. The length of the test cycle is established by the testing protocol, i.e., steady state temperature for downhole components or alternating low and high tempera- ture cycles for surface wellhead equipment. In this example for a surface wellhead application, a 72-hour (3-day) test cycle is

28、 used. Figure 3 shows how the 3-day test cycle is con- ducted. The objective of the test sequence is to establish the rate of chemical degradation as a function of temperature. 5.3 The selection of a starting temperature for a life estima- tion experiment is somewhat arbitrary. A good starting point

29、 is an elevated temperature that will consistently give a failure in one or two test cycles. Some experimentation may be required to establish this maximum test temperature. Once the maximurn test temperature is determined, lower test tem- peratures can be selected, usually in 10C (1 8F) increments.

30、 For example, if 450F is determined to be the maximum test temperature where only one test cycle can be consistently completed, the next lower test temperature would be 432F. If the experiment follows the Arrhenius relation, two or more test cycles should be completed at 432F. If two or more test cy

31、cles are not achieved at 432“F, the test temperature would be lowered by another 18F until at least two or more test cycles are achieved consistently. At each subsequent test tem- perature, sufficient test runs should be done to obtain test data that are statistically significant. A minimum of three

32、 different test temperatures should be used, but preferably, five tests or more should be done with some replicates. 5.4 Use of the Arrhenius principle in estimating the life of an elastomeric component requires that the chemical process that controls degradation remains constant. If test tempera- t

33、ures are excessive, other reactions may occur and data obtained may lead to erroneous life estimation. Once suffi- cient data have been accumulated, a least squares regression analysis is done and the data plotted to look for any non-lin- earity in the life estimation curve. If a single degradation

34、reaction occurred during testing, the best-fit line should approximate a straight line. For a valid life estimation, the least squares regression analysis on the test data should indi- cate a correlation coefficient greater than 0.90. Once satisfac- tory test data have been generated, the life estim

35、ation line (best fit to data) may be extended to the specified maximum service temperature. An estimate of service life can be read from the vertical scale of the life estimation plot or it can be calculated from the appropriate mathematical formula. 5.5 Proper simulation of the chemical reactions t

36、hat occur between candidate elastomers and the severe service envi- ronment requires a sufficient volume of chemicals must be present to prevent depletion of the reactants. A three (3) day 4 API TR6J1 Full rated pressure at low temperature extreme for 1 hour A test cycle is used so that the candidat

37、e elastomeric material is regularly exposed to fresh chemicals. In service, the elas- tomer may be constantly exposed to a steady stream of fresh chemicals and/or produced fluids/gases or it may only be exposed to stagnant conditions. At the end of the 3-day test cycle, the test vessel is typically

38、rapidly depressurized and purged of the liquid and gas phases. Other decompression cycles can be used with agreement of all concerned parties. Fresh liquid and gas are added and the candidate sealing ele- ments are pressure tested at ambient temperature. For spe- cific applications, other temperatur

39、es below ambient can be used. If the seals hold pressure for one hour without leakage, the test vessel is heated up to the test temperature for another 3-day test cycle. This is repeated until failure is observed. Full rated pressure at low temperature extreme for 1 hour Pressurized service environm

40、ent Test port P 5.6 Some examples of typical failure modes observed for elastomers in life estimation testing are excessive compres- sion set, hardening, cracking and chemical softening. 6 Summary The life estimation procedure outlined above provides a cost effective technique to evaluate the long t

41、erm effects of a chemical environment on a elastomer component. Use of the Arrhenius principle of chemical reaction rates allows an accelerated estimation of the thermochemical degradation of the elastomer in a severe service environment. This evalua- tion technique for studying the long-term effect

42、s of an envi- ronment on an elastomer compound is an alternative to fuii scale, long term testing in the field. I Test - API Member (Check $Ya) Invoice To - U Check here if same as “Ship To” Company: Company: Nammept.: Nammept.: Ship To - (UPS will not deliver to a PO. Box) I Address: StaWrovince: c

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