{"id":396,"date":"2010-08-01T21:03:31","date_gmt":"2010-08-01T21:03:31","guid":{"rendered":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/?p=396"},"modified":"2011-06-02T14:23:07","modified_gmt":"2011-06-02T19:23:07","slug":"important-aspects-of-centrifugal-compressor-testing-part-1","status":"publish","type":"post","link":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/2010\/08\/important-aspects-of-centrifugal-compressor-testing-part-1\/","title":{"rendered":"Important Aspects of Centrifugal Compressor Testing-Part 1"},"content":{"rendered":"<p>Every centrifugal compressor, whether it is new or has been in service for many years will most likely be tested to verify its thermodynamic performance.\u00a0 For a new machine the testing may be conducted in the manufacturer\u2019s facility under strict controlled conditions or in the field at actual operating conditions.\u00a0 Older compressors that have been placed in service after maintenance or have been operating for an extended period of time may require testing to verify the efficiency and normal operation.\u00a0 This TOTM will review ASME PTC-10 (also referred to as the Code) testing procedure and other topics that contribute to an accurate centrifugal compressor test results.<\/p>\n<p>This two-part series will review the salient aspects of a performance test.\u00a0 Part 1 will review the thermodynamic performance test objectives established in the Code as well as other factors to consider in a testing procedure.\u00a0 While this code is primarily applicable to shop testing it can also apply to field testing.\u00a0 Part 2 will review the Code assumptions and basic performance relationships.\u00a0 It will also examine the three important principles that influence the operating conditions and ultimately influence the accuracy of the performance test.\u00a0 They are volume ratio, Machine Mach Number and Machine Reynolds Number.<\/p>\n<p><strong>Introduction<\/strong><\/p>\n<p>The purpose of a performance test is to verify that a centrifugal compressor will perform in accordance with the manufacturer\u2019s design at the operating conditions given in the specifications.\u00a0 It also provides a method of confirming the shape of the compressor head-flow curve, efficiency, and the maximum and minimum flow limits at various speeds.\u00a0 Frequently a performance test is conducted under field conditions with the specified gas and operating conditions.\u00a0 However, if the performance test is conducted in the shop it may not be possible to test the compressor with the specified gas because of safety concerns or testing facility limitations.\u00a0 Whether the test is conducted in the field or in the shop, proof of the compressor design is recommended and often necessary to demonstrate contractual obligations and mechanical integrity.<\/p>\n<p>Frequently the gas composition used to confirm a compressor performance differs from the specified gas.\u00a0 This is often the case regardless if the test is conducted in the field or in the shop.\u00a0 For field tests, where the gas composition and operating conditions are set by the process, adjustments must be made in the calculations to confirm the compressor design specifications.\u00a0 Typically, a shop test is conducted with a carefully selected mixture of gases blended together to form a gas that has physical properties that closely resemble the specified gas.\u00a0 Even with a substitute gas, differences remain which influence the test results.<\/p>\n<p>The original compressor design places limits on the thermodynamic performance.\u00a0 The most important of these limits include flow rate, power, temperature, pressure and speed.\u00a0 There are other design restraints which are not as commonly known but will also influence the compressor performance.\u00a0 Such factors are volume ratio, Mach number and Reynolds number.\u00a0 These limits were incorporated in the compressor design and are influenced by gas properties, operating conditions and the mechanical design.\u00a0 To verify the design and operating limits for a compressor, it is necessary to test the machine.\u00a0 For new machines, these tests are commonly performed in the manufacturer\u2019s facility; however, the testing is sometimes performed in the field.\u00a0 It may also be helpful to periodically test a compressor to trend the machine performance.\u00a0 Testing conducted during commissioning will establish a baseline of performance.\u00a0 Periodic field tests are often conducted to verify the overall performance and signal changes that may predict mechanical damage, internal fouling, or other deteriorating conditions.<\/p>\n<p><strong>Summary of ASME PTC-10 \u2013 Performance Test Code <\/strong><br \/>\nThe procedure presented in the Code provides a method of verifying the thermodynamic performance of centrifugal and axial compressors.\u00a0 This code offers two types of tests which are based on the deviation between test and specified conditions.\u00a0 A detail procedure is given for calculating and correcting results for differences in gas properties and test conditions.\u00a0 The following briefly describes the guiding principles of the Code.<\/p>\n<ul>\n<li>Type 1 test is conducted with the specified gas at or very near to the specified operating conditions. \u00a0While the actual and test operating conditions may differ, the permissible deviations are limited.\u00a0 See Table 1, 2 and 3 for deviation limits of testing variables of a Type 1 test.<\/li>\n<li>Type 2 test is conducted with either the specified gas or a substitute gas.\u00a0 The test operating conditions will often differ significantly from the specified conditions.\u00a0 The operating conditions are subject to limitations based on the compressor aerodynamic design.\u00a0 See Table 2 and 3 for permissible deviations of operating conditions and test gas properties.<\/li>\n<li>The calculation method of a Type 1 and Type 2 test may conform to either Ideal or Real Gas laws.\u00a0 Physical property limitations are given in Table 3 if Ideal Gas Law methodology is used.<\/li>\n<\/ul>\n<p><strong><\/strong><br \/>\n<strong><a href=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/114.png\"><img data-recalc-dims=\"1\" decoding=\"async\" loading=\"lazy\" class=\"aligncenter size-full wp-image-397\" title=\"1\" src=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/114.png?resize=479%2C589\" alt=\"Tables 1 and 2\" width=\"479\" height=\"589\" srcset=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/114.png?w=479 479w, https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/114.png?resize=243%2C300 243w\" sizes=\"auto, (max-width: 479px) 100vw, 479px\" \/><\/a><br \/>\n<a href=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/210.png\"><img data-recalc-dims=\"1\" decoding=\"async\" loading=\"lazy\" class=\"aligncenter size-full wp-image-398\" title=\"2\" src=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/210.png?resize=480%2C299\" alt=\"Table 3\" width=\"480\" height=\"299\" srcset=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/210.png?w=480 480w, https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/210.png?resize=300%2C186 300w\" sizes=\"auto, (max-width: 480px) 100vw, 480px\" \/><\/a><br \/>\n<\/strong><\/p>\n<p>The Code also gives procedures for calculating and correcting test results for difference between the test conditions and specified conditions.\u00a0 It also gives recommendations for accurate testing including compressor testing schemes, instrumentation, piping configuration and test value uncertainties.\u00a0 The following summarizes each topic.<\/p>\n<ul>\n<li>Thermodynamic calculations may utilize either enthalpy, isentropic or polytropic methods.\u00a0 The Code provides equations and examples for determining compressor work (also referred to as head), gas and overall efficiencies, gas and shaft power, and parasitic losses.<\/li>\n<li>The Code gives a correction procedure for test gases and test operating conditions that deviated from the specified operating conditions.<\/li>\n<li>Compressor testing may be open-loop or closed-loop; however, the test results are subject to limits that may give preference to the test arrangement.<\/li>\n<li>Instrumentation methods and measurement uncertainties (refer to PTC-19 series of standards) used to test compressors are given.<\/li>\n<li>Recommendations for piping layout are also included.<strong><\/strong><\/li>\n<\/ul>\n<p><strong>Test Gas Selection<\/strong> <strong><\/strong><br \/>\nThere are many gases commonly used to test compressors.\u00a0 They are selected based on physical properties, toxicity, flammability and environmental concerns.\u00a0 See Table 4 for a list of the most frequently used gases.\u00a0 The manufacturers will sometimes blend the various gases to match the equivalency criteria and the test facilities limitations.\u00a0 Following are recommendations to consider when selecting a test gas.<\/p>\n<ul>\n<li>The compressor mechanical design may impose constraints on the test.\u00a0 Consider the machine rotor dynamics, overspeed, maximum temperature and power limitations when selecting a test gas.<\/li>\n<li>Avoid flow rate mismatch of impellers.\u00a0 The volume ratio equivalency is the most important parameter in selecting a test gas.\u00a0 This may also place limitations on the operating conditions. \u00a0More on this subject in Part 2. of this series.<\/li>\n<li>The test gas molecular weight should closely match the molecular weight of the specified gas.<\/li>\n<li>The test gas k-value should closely match the specified gas to duplicate the Machine Mach Number.\u00a0 If this is not practical then the test k-value should be slightly greater to avoid possible stonewall limitations.<\/li>\n<li>Select a test gas with minimum Reynolds Number deviation from the specified gas.\u00a0 This will minimize the efficiency and head correction factors.\u00a0 This is especially important for machines with a low Machine Reynolds Number.<\/li>\n<\/ul>\n<p><strong>Table 4 <\/strong><br \/>\n<strong>Typical Test Gas Mediums (1)<\/strong><\/p>\n<div>\n<table border=\"1\" cellspacing=\"0\" cellpadding=\"0\" width=\"483\">\n<tbody>\n<tr>\n<td valign=\"top\"><strong>Test Gas<\/strong><\/td>\n<td valign=\"top\"><strong>Molecular Weight<\/strong><\/td>\n<td valign=\"top\"><strong>k-Value (2)<\/strong><\/td>\n<td valign=\"top\"><strong>Absolute Viscosity-cP (2)<\/strong><\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Helium<\/td>\n<td valign=\"top\">4.003<\/td>\n<td valign=\"top\">1.667<\/td>\n<td valign=\"top\">0.0194<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Nitrogen<\/td>\n<td valign=\"top\">28.014<\/td>\n<td valign=\"top\">1.401<\/td>\n<td valign=\"top\">0.0174<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Air (dry)<\/td>\n<td valign=\"top\">28.959<\/td>\n<td valign=\"top\">1.401<\/td>\n<td valign=\"top\">0.0175<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Carbon Dioxide<\/td>\n<td valign=\"top\">44.010<\/td>\n<td valign=\"top\">1.299<\/td>\n<td valign=\"top\">0.0145<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">R134a<\/td>\n<td valign=\"top\">102.0<\/td>\n<td valign=\"top\">1.124<\/td>\n<td valign=\"top\">0.0114<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Natural Gas (4)<\/td>\n<td valign=\"top\">17.1\u00a0 (3)<\/td>\n<td valign=\"top\">1.26\u00a0 (3)<\/td>\n<td valign=\"top\">0.010\u00a0 (3)<\/td>\n<\/tr>\n<tr>\n<td valign=\"top\">Propane<\/td>\n<td valign=\"top\">44.096<\/td>\n<td valign=\"top\">1.141<\/td>\n<td valign=\"top\">0.00789<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n<p>Note:<\/p>\n<ol>\n<li>From \u201cCompressors 201\u201d course at Turbomachinery Conference, 2009<\/li>\n<li>Values from National Institute of Standards and Technology and Gas Processors Suppliers Association<\/li>\n<li>Values at 60 0F (15.6 C) and 14.696 psia (101.3 kPa)<\/li>\n<li>Gas composition and physical properties varies with local utility<\/li>\n<\/ol>\n<p><strong>Test Objectives<\/strong><br \/>\nThe following are some factors to consider as part of the performance test procedure.<\/p>\n<ul>\n<li>API 617 requires a minimum of five test points to be taken at the operating speed to demonstrate the surge point, stonewall, required operating point and two alternate points.\u00a0 The user may optionally request additional test points to verify compressor performance at alternate speeds.\u00a0 For example, extra data points may be needed to verify the surge line or critical process operating conditions for variable speed machines.<\/li>\n<li>The test may be performed as a Type 1 or Type 2 test.\u00a0 Type 1 is normally more accurate and is typically reserved when test conditions can be made to closely match the specified operating conditions.\u00a0 A Type 2 test is typically a shop test utilizing a substitute gas.<\/li>\n<li>If a Type 2 test is recommended, the test gas may be a pure gas such as those listed in Table 4, or a mixture of gases.\u00a0 The composition of the test gas should be agreed upon before testing.\u00a0 In addition, the composition of the test gas should be sampled before, during and after the test.\u00a0 Some gas mixtures tend to stratify and give erroneous results.<\/li>\n<li>The physical properties of the test gas are critical to the outcome especially if it is a mixture of selected gases.\u00a0 An agreement on the physical properties is recommended.<\/li>\n<li>Normally an agreement is made as to the \u201cequation of state\u201d used to calculate the results of the test.\u00a0 Not all EOS programs give the same results, nor is there industry agreement as to which method is best.<\/li>\n<li>Discuss the specific driver used in the test.\u00a0 Will a shop driver or the specified driver be used?\u00a0 Will the driver be fixed or variable speed?\u00a0 If it is variable speed, will it be motor, gas turbine or steam turbine?<\/li>\n<li>If a gear is part of the test, will it be manufacturer or user supplied?\u00a0 Is the efficiency of the gear known?\u00a0 Tests can be performed to verify gear efficiency.<\/li>\n<li>Will the gas be cooled with a water-cooled or air-cooled exchanger?\u00a0 Is there temperature limitations on the coolant used in the test?<\/li>\n<li>Is the allowable working pressure of equipment and piping systems adequate for the test?\u00a0 Will a pressure safety valve be needed to protect the system and is it properly sized?<\/li>\n<li>An agreement on how the input power will be measured is important.\u00a0 Options include, heat balance, calibrated driver, dynamometer, and torque meter.\u00a0 Review the specific method of measuring input power with the manufacturer.<\/li>\n<li>A piping and instrument schematic is recommended.\u00a0 The drawing should show details of the test loop including the placement of major equipment, number and location of instruments, and piping size. \u00a0This is especially important for compressors with multiple sections, inlet sidestream, or back-to-back configuration.<\/li>\n<li>Before proceeding with a performance test a written procedure is recommended that outlines how the test will be conducted.\u00a0 The procedure should clearly convey the scope of the test, the responsibilities of each party, test piping and instrument arrangement, measurement methods, uncertainty limits, calibration, taking of test data and how to interpret results, and acceptance criteria.<\/li>\n<\/ul>\n<p><em>By Joe Honeywell<\/em><\/p>\n<p><strong>References<\/strong><\/p>\n<ol>\n<li>ASME PTC-10, \u201c<em>Performance test Code on Compressors and Exhausters<\/em>\u201d, 1997.<\/li>\n<li>API Standard 617, \u201c<em>Centrifugal compressors for Petroleum, Chemical, and Gas Services Industries<\/em>\u201d, 1995.<\/li>\n<li>Kurz, R., Brun, K, &amp; Legrand, D.D., \u201c<em>Field Performance Testing of Gas Turbine Driven Compressor Sets<\/em>\u201d, Proceeding of the 28th Turbomachinery Symposium, 1999.<\/li>\n<li>Short Course \u201c<em>Centrifugal Compressors 201<\/em>\u201d, Colby, G.M., et al. 38th Turbomachinery Symposium, 2009.<\/li>\n<li>National Institute of Standards and Technology, Web Site for Properties of Fluids.<\/li>\n<\/ol>\n","protected":false},"excerpt":{"rendered":"<p>Every centrifugal compressor, whether it is new or has been in service for many years will most likely be tested to verify its thermodynamic performance.\u00a0 For a new machine the testing may be conducted in the manufacturer\u2019s facility under strict controlled conditions or in the field at actual operating conditions.\u00a0 Older compressors that have been [&hellip;]<\/p>\n","protected":false},"author":28,"featured_media":0,"comment_status":"open","ping_status":"open","sticky":false,"template":"","format":"standard","meta":{"nf_dc_page":"","_monsterinsights_skip_tracking":false,"_monsterinsights_sitenote_active":false,"_monsterinsights_sitenote_note":"","_monsterinsights_sitenote_category":0,"_jetpack_newsletter_access":"","_jetpack_dont_email_post_to_subs":false,"_jetpack_newsletter_tier_id":0,"_jetpack_memberships_contains_paywalled_content":false,"_jetpack_feature_clip_id":0,"_jetpack_memberships_contains_paid_content":false,"footnotes":"","jetpack_publicize_message":"","jetpack_publicize_feature_enabled":true,"jetpack_social_post_already_shared":false,"jetpack_social_options":{"image_generator_settings":{"template":"highway","default_image_id":0,"font":"","enabled":false},"version":2},"jetpack_post_was_ever_published":false},"categories":[5],"tags":[],"coauthors":[],"class_list":["post-396","post","type-post","status-publish","format-standard","hentry","category-mechanical"],"jetpack_publicize_connections":[],"jetpack_featured_media_url":"","jetpack_shortlink":"https:\/\/wp.me\/p1pQc4-6o","jetpack_sharing_enabled":true,"_links":{"self":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/396","targetHints":{"allow":["GET"]}}],"collection":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts"}],"about":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/types\/post"}],"author":[{"embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/users\/28"}],"replies":[{"embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/comments?post=396"}],"version-history":[{"count":5,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/396\/revisions"}],"predecessor-version":[{"id":1064,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/396\/revisions\/1064"}],"wp:attachment":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/media?parent=396"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/categories?post=396"},{"taxonomy":"post_tag","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/tags?post=396"},{"taxonomy":"author","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/coauthors?post=396"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}