1、 Reference number ISO/TR 12148:2009(E) ISO 2009TECHNICAL REPORT ISO/TR 12148 First edition 2009-02-15 Natural gas Calibration of chilled mirror type instruments for hydrocarbon dewpoint (liquid formation) Gaz naturel talonnage des instruments du type miroir refroidi pour points de rose hydrocarbures
2、 (formation de liquide) ISO/TR 12148:2009(E) PDF disclaimer This PDF file may contain embedded typefaces. In accordance with Adobes licensing policy, this file may be printed or viewed but shall not be edited unless the typefaces which are embedded are licensed to and installed on the computer perfo
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7、12148:2009(E) ISO 2009 All rights reserved iii Contents Page Foreword iv Introduction v 1 Scope . 1 2 Normative references . 1 3 Terms and definitions. 1 4 Symbols . 2 5 Performance characteristics of automatic weighing method in accordance with ISO 6570:2001 2 5.1 Working principle 2 5.2 Functional
8、 requirements 4 5.3 Measurement uncertainty 5 6 Performance requirements for a chilled-mirror-type instrument for hydrocarbon-dew- point determination 6 6.1 Working principle 6 6.2 Precision 7 7 Requirements/Points of interest to carry out a calibration 8 7.1 Process gas. 8 7.2 Sampling system 8 7.3
9、 Selection of the PHLC reference value. 9 7.4 Compositional range of gases covered by the calibration procedure 10 7.5 Calibration interval . 10 8 Execution of calibration procedure 10 8.1 General. 10 8.2 Method A Change in trip point value 11 8.3 Method B Direct change of dew point value . 12 8.4 W
10、hich method should be used? . 12 Annex A (informative) Condensation behaviour of natural gas 13 Annex B (informative) Example of a hydrocarbon-dew-point analysis 16 Annex C (informative) Examples of a calibration 19 Annex D (informative) Performance of different types of chilled-mirror instruments f
11、or hydrocarbon dew point determination .29 Bibliography . 31 ISO/TR 12148:2009(E) iv ISO 2009 All rights reservedForeword ISO (the International Organization for Standardization) is a worldwide federation of national standards bodies (ISO member bodies). The work of preparing International Standards
12、 is normally carried out through ISO technical committees. Each member body interested in a subject for which a technical committee has been established has the right to be represented on that committee. International organizations, governmental and non-governmental, in liaison with ISO, also take p
13、art in the work. ISO collaborates closely with the International Electrotechnical Commission (IEC) on all matters of electrotechnical standardization. International Standards are drafted in accordance with the rules given in the ISO/IEC Directives, Part 2. The main task of technical committees is to
14、 prepare International Standards. Draft International Standards adopted by the technical committees are circulated to the member bodies for voting. Publication as an International Standard requires approval by at least 75 % of the member bodies casting a vote. In exceptional circumstances, when a te
15、chnical committee has collected data of a different kind from that which is normally published as an International Standard (“state of the art”, for example), it may decide by a simple majority vote of its participating members to publish a Technical Report. A Technical Report is entirely informativ
16、e in nature and does not have to be reviewed until the data it provides are considered to be no longer valid or useful. Attention is drawn to the possibility that some of the elements of this document may be the subject of patent rights. ISO shall not be held responsible for identifying any or all s
17、uch patent rights. ISO/TR 12148 was prepared by Technical Committee ISO/TC 193, Natural gas, Subcommittee SC 1, Analysis of natural gas. ISO/TR 12148:2009(E) ISO 2009 All rights reserved v Introduction Under certain conditions, higher hydrocarbons present in natural gas or similar gases can condense
18、 and the hydrocarbon liquids formed can cause difficulties in the operation of gas transport and distribution systems. Hydrocarbon dew-point measurements, by condensation on a mirror, can give an indication of the conditions under which condensation starts. Theoretically, the hydrocarbon dew point i
19、s the temperature at which the first small droplets of liquid are formed at a fixed pressure. In practice, all dew-point-measurement methods are based on the observation of the formation of a film of hydrocarbon liquids on the surface of an illuminated, cooled mirror. The observation can be done vis
20、ually (manual mirror) or by an electronic sensor (automatic chilled mirror). The cooling can be achieved in two ways: expansion of natural gas, compressed air or carbon dioxide or by applying a Peltier-cooling device. Either manual or automatic chilled mirrors can be applied to measure the hydrocarb
21、on dew point of natural gas. It is not possible to calibrate commercially available hydrocarbon dew point analysers in a traceable way, because no hydrocarbon dew-point reference material or reference instrument is available. Because of differences in working principles, analysers from different man
22、ufacturers can give different values for the hydrocarbon dew point for a given gas. In practice, the dew point of an automatic dew point monitor is often “tuned” to match the value measured by a manual chilled mirror, or “tuned” to the value calculated from a known gas composition using a thermodyna
23、mic model. Modern automatic hydrocarbon-dew-point chilled-mirror instruments have the possibility of adjusting the value of the presented hydrocarbon dew point. Sometimes this adjustment is carried out by changing a physical setting in the instrument itself; in other cases the setting can be changed
24、 by entering a new value into the instruments controller. The availability of such an adjustable parameter is a prerequisite for using the calibration procedure described in this Technical Report. NOTE 1 Changing the setting of such a parameter can result in a major change in the presented hydrocarb
25、on-dew- point value. For example, a study carried out under the auspices of the National Physical Laboratory2shows from real measurements that the hydrocarbon dew point for a natural gas measured at the same pressure varies between 6,28 C and 8,54 C Gas B, with pressure equal to 3,5 MPa (35 bars), d
26、etector sensitivity varying between 110 mV and 275 mV. In 2007, the results of a comprehensive study2of the measurement of the hydrocarbon dew point of real and synthetic natural gases was published. In this study, six analytical methods were examined: one automatic chilled-mirror instrument, one ma
27、nual chilled-mirror instrument, two laboratory gas chromatographs and two process gas chromatographs. In this study, it is concluded that the role of accurate synthetic gas mixtures in the calibration of chilled-mirror instruments is limited. Furthermore, it is stated that a standard composed of n-
28、butane in nitrogen is indeed a straightforward and inexpensive way to calibrate a chilled-mirror instrument, yet forms an atypical, rapidly condensing hydrocarbon film. Therefore, such a calibration gas has limited use in calibrating a hydrocarbon-dew-point instrument. NOTE 2 Several studies showed
29、the importance of not only the component concentration in a calibration mixture but also knowledge of the nature of the components used. For example, a GERG study4shows that adding aromatic and/or cyclic hydrocarbons has a significant influence on the hydrocarbon dew point. Based on the working prin
30、ciple of chilled-mirror devices, there are five major sources that can be responsible for significant systematic errors in the measured hydrocarbon dew point and for which no adjustment can be made because no proper calibration method exists. These five sources are a) the often significant amount of
31、 liquid that it is necessary to form before the instrument is able to detect the dew point temperature; b) the cooling rate, which is often too fast to ensure that the temperature measured by a temperature sensor somewhere in the mirror equals the temperature of the mirror surface and the temperatur
32、e of the gas in the measuring cell; ISO/TR 12148:2009(E) vi ISO 2009 All rights reservedc) the way the gas flow passes through the measurement cell during the actual measuring phase (continuous versus stop-flow principle); d) the measurement of the mirror temperature, which doesnt take place at the
33、mirror surface itself but near the mirror surface; e) the hydrocarbon dew point that, when measured at a certain pressure setting, doesnt necessarily corresponds to the cricondentherm pressure valid for the actual gas composition. In this Technical Report, a calibration procedure is presented which
34、allows the adjustment and even the calibration of a hydrocarbon-dew-point chilled-mirror analyser against the indirect automatic weighing method according to ISO 6570. By using this procedure, the measured hydrocarbon dew point corresponds unambiguously to a given value for the potential hydrocarbon
35、 liquid content (PHLC) at this measured dew- point temperature. In this way, a traceable and much more objective measurement of the hydrocarbon dew point is possible. By doing an on-site comparison/calibration against the indirect automatic weighing method, it is even possible to correct for the gas
36、-dependent performance of the hydrocarbon-dew-point analyser, which exists to some extent for different natural gases. Measurements carried out according to ISO 6570 consist of cooling down a well defined gas flow to a specified and accurately measured temperature. The gas has enough time to form li
37、quid and to establish a gas-liquid equilibrium at a certain pressure and temperature. This process is similar to the process that occurs in practice, when in a pipeline the pressure and/or temperature are reduced, the complete gas flow is cooled down and depending on the gas quality in the worst cas
38、e can result in hydrocarbon liquid drop out. By calibrating a dew point analyser against ISO 6570, it is made sure that a dew point is obtained, which is related to the process which actually occurs in the pipeline upon pressure reduction, although the measurement technique is quite different to the
39、 process in the pipeline. According to ISO 6570, the detection limit of the automatic weighing method is 5 mg/Nm 3 . Theoretically it can be argued that the temperature corresponding to a potential hydrocarbon liquid content of 5 mg/m 3is not a correct estimate for the hydrocarbon-dew-point temperat
40、ure. However, taking into account the measuring capabilities of the existing hydrocarbon-dew-point measurement devices, this effect can be neglected. Based on the geometry of the measurement cell of a chilled mirror instrument, it is estimated by Cowper 3that it is necessary to condense approximatel
41、y 70 mg/Nm 3onto a mirror surface to register a hydrocarbon- dew-point temperature. Depending on the gas composition, this effect results in a bias of up to 1,5 C in the measured hydrocarbon dew point value. NOTE 3 EASEE-gas (European Association for the Streamlining of Energy Exchange) recently agr
42、eed upon harmonized values of the hydrocarbon dew point throughout Europe (Common Business Practice 2005-001/01)1 . The required harmonized measuring method, which it is still necessary to identify, can clearly benefit from the proposed traceable calibration procedure presented in this Technical Rep
43、ort. TECHNICAL REPORT ISO/TR 12148:2009(E) ISO 2009 All rights reserved 1 Natural gas Calibration of chilled mirror type instruments for hydrocarbon dewpoint (liquid formation) WARNING The use of this Technical Report can involve hazardous materials, operations and equipment. This Technical Report d
44、oes not purport to address all of the safety problems associated with its use. It is the responsibility of the user of this Technical Report to establish appropriate safety and health practices and to determine the applicability or regulatory limitations prior to use. 1 Scope This Technical Report d
45、escribes the principles of, and general requirements for, the traceable calibration of automatic hydrocarbon-dew-point chilled-mirror instruments using the indirect automatic weighing method (method B) described in ISO 6570:2001 to determine the potential hydrocarbon liquid content of natural gas, o
46、r similar gas. The calibration procedure is intended for use by chilled-mirror instruments in downstream applications transferring processed natural gas. If the gas composition is constant, the manual weighing method (method A) described in ISO 6570:2001 is also applicable. NOTE 1 Whether or not a g
47、as composition is constant is difficult to establish. A process gas chromatograph (GC) measuring calorific values within 0,1 % is absolutely no guarantee for a constant hydrocarbon liquid drop-out content. Information up to C 12is required to verify that the gas composition is constant. NOTE 2 The a
48、pplication of this calibration procedure in the upstream area is not excluded a priori, however, currently there is no experience using this procedure in an upstream environment. The usability of data on the potential hydrocarbon liquid content of natural gas for verification, adjustment or calibrat
49、ion of hydrocarbon-dew-point chilled-mirror instruments is based on the condensation behaviour of natural gases. Information on the condensation behaviour of natural gases and the various measuring techniques to determine properties, like hydrocarbon dew point and potential hydrocarbon liquid content, related to the condensation behaviour of natural gases are given in Annex A. NOTE 3 Unless otherwise specified, gas volumes are in cubic metres at 273,15 K and 101,325 kPa. 2 Normative references The following referenced documen
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