{"id":100,"date":"2007-06-01T21:59:46","date_gmt":"2007-06-01T21:59:46","guid":{"rendered":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/?p=100"},"modified":"2011-06-13T13:31:22","modified_gmt":"2011-06-13T18:31:22","slug":"why-do-i-care-about-phase-diagrams","status":"publish","type":"post","link":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/2007\/06\/why-do-i-care-about-phase-diagrams\/","title":{"rendered":"Why do I care about phase diagrams?"},"content":{"rendered":"<p>In facilities operations the understanding of where the process is on a phase diagram can often help the engineer and operator avoid extremely embarrassing design and operating mistakes. The oil and gas industry is full of many \u201cwar stories\u201d about \u201cphase diagram disasters.\u201d Most instances are never related back to the phase diagram misunderstanding. In one well-documented but poorly published case a \u201cdry gas\u201d pipeline that was pigged flooded miles of sandy beach. In another case thousands of kilowatts of compression power were installed to maintain the pressure of a reservoir above the dew point when in fact the reservoir was at a temperature above the cricondentherm. In many cases equipment manufacturers and purchasers of gas have specifications of \u201csuperheat\u201d or dew point that have not been met and led to upset customers and\/or millions of dollars of lawsuits.<\/p>\n<p>One of the first issues to be resolved by a facilities engineer working in a gas plant or gas production facility is where is the process operating with respect to the phase diagram. A general knowledge, if not a detailed knowledge, will allow the design engineer and the facilities operator to make intelligent decisions that have significant impact on the profitability of a gas production facility.<\/p>\n<p>The following figure is a \u201cgeneric hydrocarbon mixture\u201d phase diagram for a lean gas. The area to the left of the\u00a0<strong>Bubble Point<\/strong> line is the sub-cooled liquid region.<\/p>\n<div><a href=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph14.gif\"><img data-recalc-dims=\"1\" decoding=\"async\" loading=\"lazy\" class=\"aligncenter size-full wp-image-101\" title=\"graph1\" src=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph14.gif?resize=460%2C358\" alt=\"Graph 1\" width=\"460\" height=\"358\" srcset=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph14.gif?w=460 460w, https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph14.gif?resize=300%2C233 300w\" sizes=\"auto, (max-width: 460px) 100vw, 460px\" \/><\/a><\/div>\n<p>The area to the right of the Dew Point line is the super-heated gas region. Between these two lines the mixture is two-phase. Other areas of interest are the retrograde region and the supercritical region. Each of these regions provides advantages and disadvantages for operations.<\/p>\n<p>This month we will start to define the points of interest so that we may choose proper operating points for various types of processes. The first point to define is the\u00a0<strong>cricondentherm<\/strong>. The definition of this point is the highest temperature at which twophases (liquid and vapor for most processes) can coexist. In Figure 1, this is point M. Point M has considerable theoretical and practical importance. For example, if the cricondentherm for a sales gas (point M) is 0 \u00baC (32 \u00baF) cooling the gas to 4 \u00baC (40 \u00baF) at any pressure will not result in condensation of liquids. This type of operation is typically the type used for cross-country transportation of gas in pipelines. Operation with this type of system will not require \u201cslug catchers\u201d at the end of the pipeline and will significantly decrease pressure drop in the pipeline.<\/p>\n<p>If the gas were processed in a cold separator such that point B (a dew point) was 0 \u00baC (32 \u00baF) problems could occur in the same conditions as the pipeline mentioned above. If the pressure of the pipeline was between the pressure of point B and F and the pipeline cooled to 4 \u00baC (40 \u00baF) there could be significant quantities of liquid in the pipeline. If the operations people were not familiar with the phase diagram they might increase the operating pressure of the cold separator and still keep the temperature at 0 \u00baC (32 \u00baF). This action would result in\u00a0<strong>increased<\/strong> liquids in the pipeline, not decreased. However, if the cold separator was operated at the pressure of point M, at a temperature of 0 \u00baC (32 \u00baF),\u00a0<strong>in theory<\/strong> there would be no liquids in the pipeline again. (More about the difference between theory and practice in future tips).<\/p>\n<div><a href=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph22.gif\"><img data-recalc-dims=\"1\" decoding=\"async\" loading=\"lazy\" class=\"aligncenter size-full wp-image-102\" title=\"graph2\" src=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph22.gif?resize=460%2C377\" alt=\"Graph 2\" width=\"460\" height=\"377\" srcset=\"https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph22.gif?w=460 460w, https:\/\/i0.wp.com\/www.jmcampbell.com\/tip-of-the-month\/wp-content\/uploads\/2011\/03\/graph22.gif?resize=300%2C245 300w\" sizes=\"auto, (max-width: 460px) 100vw, 460px\" \/><\/a><\/div>\n<p>To learn more about similar cases and how to minimize operational problems, we suggest attending our\u00a0<a href=\"http:\/\/www.jmcampbell.com\/gas-conditioning-and-processing-g4.php\">G4 (Gas Conditioning and Processing)<\/a> and <a href=\"http:\/\/www.jmcampbell.com\/gas-conditioning-and-processing-special.php\">G5 (Gas Conditioning and Processing &#8211; Special)<\/a> courses.<\/p>\n<p><em>Dr. Larry L. Lilly<\/em><\/p>\n","protected":false},"excerpt":{"rendered":"<p>In facilities operations the understanding of where the process is on a phase diagram can often help the engineer and operator avoid extremely embarrassing design and operating mistakes. The oil and gas industry is full of many \u201cwar stories\u201d about \u201cphase diagram disasters.\u201d Most instances are never related back to the phase diagram misunderstanding. In [&hellip;]<\/p>\n","protected":false},"author":29,"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":[3],"tags":[],"coauthors":[],"class_list":["post-100","post","type-post","status-publish","format-standard","hentry","category-gas-processing"],"jetpack_publicize_connections":[],"jetpack_featured_media_url":"","jetpack_shortlink":"https:\/\/wp.me\/p1pQc4-1C","jetpack_sharing_enabled":true,"_links":{"self":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/100","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\/29"}],"replies":[{"embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/comments?post=100"}],"version-history":[{"count":3,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/100\/revisions"}],"predecessor-version":[{"id":1119,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/posts\/100\/revisions\/1119"}],"wp:attachment":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/media?parent=100"}],"wp:term":[{"taxonomy":"category","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/categories?post=100"},{"taxonomy":"post_tag","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/tags?post=100"},{"taxonomy":"author","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/coauthors?post=100"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}