ASTM G96-1990(2008) Standard Guide for Online Monitoring of Corrosion in Plant Equipment (Electrical and Electrochemical Methods)《工厂设备中腐蚀性的在监视的标准指南(电化学方法)》.pdf
《ASTM G96-1990(2008) Standard Guide for Online Monitoring of Corrosion in Plant Equipment (Electrical and Electrochemical Methods)《工厂设备中腐蚀性的在监视的标准指南(电化学方法)》.pdf》由会员分享,可在线阅读,更多相关《ASTM G96-1990(2008) Standard Guide for Online Monitoring of Corrosion in Plant Equipment (Electrical and Electrochemical Methods)《工厂设备中腐蚀性的在监视的标准指南(电化学方法)》.pdf(10页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: G 96 90 (Reapproved 2008)Standard Guide forOnline Monitoring of Corrosion in Plant Equipment(Electrical and Electrochemical Methods)1This standard is issued under the fixed designation G 96; the number immediately following the designation indicates the year of originaladoption or, in t
2、he case of revision, the year of last revision.Anumber in parentheses indicates the year of last reapproval.Asuperscriptepsilon () indicates an editorial change since the last revision or reapproval.1. Scope1.1 This guide covers the procedure for conducting onlinecorrosion monitoring of metals in pl
3、ant equipment underoperating conditions by the use of electrical or electrochemicalmethods. Within the limitations described, these test methodscan be used to determine cumulative metal loss or instanta-neous corrosion rate, intermittently or on a continuous basis,without removal of the monitoring p
4、robes from the plant.1.2 The following test methods are included: Test MethodAfor electrical resistance, and Test Method B for polarizationresistance.1.2.1 Test Method A provides information on cumulativemetal loss, and corrosion rate is inferred. This test methodresponds to the remaining metal thic
5、kness except as describedin Section 5.1.2.2 Test Method B is based on electrochemical measure-ments for determination of instantaneous corrosion rate butmay require calibration with other techniques to obtain truecorrosion rates. Its primary value is the rapid detection ofchanges in the corrosion ra
6、te that may be indicative ofundesirable changes in the process environment.1.3 The values stated in SI units are to be consideredstandard. The values in parentheses are for information only.1.4 This standard does not purport to address all of thesafety concerns, if any, associated with its use. It i
7、s theresponsibility of the user of this standard to establish appro-priate safety and health practices and determine the applica-bility of regulatory limitations prior to use. Specific precau-tionary statements are given in 5.6.2. Referenced Documents2.1 ASTM Standards:2D 1125 Test Methods for Elect
8、rical Conductivity and Re-sistivity of WaterG1 Practice for Preparing, Cleaning, and Evaluating Cor-rosion Test SpecimensG3 Practice for ConventionsApplicable to ElectrochemicalMeasurements in Corrosion TestingG4 Guide for Conducting Corrosion Tests in Field Appli-cationsG15 Terminology Relating to
9、Corrosion and CorrosionTestingG59 Test Method for Conducting Potentiodynamic Polar-ization Resistance MeasurementsG 102 Practice for Calculation of Corrosion Rates andRelated Information from Electrochemical Measurements3. Terminology3.1 DefinitionsSee Terminology G15 for definitions ofterms used in
10、 this guide.4. Summary of Guide4.1 Test Method AElectrical ResistanceThe electricalresistance test method operates on the principle that theelectrical resistance of a measuring element (wire, strip, or tubeof metal) increases as its cross-sectional area decreases:R 5slA(1)where:R = resistance,s = re
11、sistivity of metal (temperature dependent),l = length, andA = cross-section area.In practice, the resistance ratio between the measuringelement exposed to corrosion and the resistance of a similarreference element protected from corrosion is measured, tocompensate for resistivity changes due to temp
12、erature. Basedon the initial cross-sectional area of the measurement element,the cumulative metal loss at the time of reading is determined.Metal loss measurements are taken periodically and manuallyor automatically recorded against a time base. The slope of thecurve of metal loss against time at an
13、y point is the correctionrate at that point. The more frequently measurements are taken,1This guide is under the jurisdiction of ASTM Committee G01 on Corrosion ofMetals and is the direct responsibility of ASTM Subcommittee G01.11 onElectrochemical Measurements in Corrosion Testing.Current edition a
14、pproved Aug. 15, 2008. Published September 2008. Originallyapproved in 1990. Last previous edition approved in 2001 as G 9690(2001)1.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStandards volume infor
15、mation, refer to the standards Document Summary page onthe ASTM website.1Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.the better is the resolution of the curve from which thecorrosion rate is derived.4.1.1 The electrical resistance
16、 of the metal elements beingmeasured is very low (typically 2 to 10 mV). Consequently,special measurement techniques and cables are required tominimize the effect of cable resistance and electrical noise.4.1.2 Various probe element cross-sectional areas are nec-essary so that a wide range of corrosi
17、on rates can be monitoredwith acceptable resolution.4.2 Test Method BPolarization Resistance:4.2.1 The polarization resistance test method involves inter-action with the electrochemical corrosion mechanism of metalsin electrolytes in order to measure the instantaneous corrosionrate. Its particular a
18、dvantage is its speed of response tocorrosion rate upsets. On a corroding electrode subject tocertain qualifications (see 12.1), it has been shown that thecurrent density associated with a small polarization of theelectrode is directly proportional to the corrosion rate of theelectrode.4.2.2 The pol
19、arization resistance equation is derived in TestMethod G59. See Practice G3for applicable conventions. Forsmall polarization of the electrode (typically DE up to 20 mV),the corrosion current density is defined as:icorr5BRp(2)where:B = a combination of the anodic and cathodic Tafel slopes( ba,bc), an
20、dRp= the polarization resistance with dimensions ohmcm2.B 5babc2.303 ba1 bc!(3)4.2.3 The corrosion current density, icorr, can be convertedto corrosion rate of the electrode by Faradays law if theequivalent weight (EW) and density, r, of the corroding metalare known (see Practice G 102):corrosion ra
21、te 5 K1icorrrEW (4)where:K1= a constant.4.2.4 Equivalent weight of an element is the molecularweight divided by the valency of the reaction (that is, thenumber of electrons involved in the electrochemical reaction).4.2.5 In order to obtain an alloy equivalent weight that is inproportion with the mas
22、s fraction of the elements present andtheir valence, it must be assumed that the oxidation process isuniform and does not occur selectively; that is, each element ofthe alloy corrodes as it would if it were the only elementpresent. In some situations these assumptions are not valid.4.2.6 Effective e
23、quivalent weight of an alloy is as follows:1(lmnifiWi(5)where:fi= mass fraction of ithelement in the alloy,Wi= atomic weight of the ithelement in the alloy,ni= exhibited valence of the ithelement under the condi-tions of the corrosion process, andm = number of component elements in the alloy (normal
24、lyonly elements above 1 mass % in the alloy areconsidered).Alloy equivalent weights have been calculated for manyengineering metals and alloys and are tabulated in PracticeG 102.4.2.7 Fig. 1 represents an equivalent circuit of polarizationresistance probe electrodes in a corroding environment. Theva
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