{"id":9233,"date":"2022-07-19T04:21:51","date_gmt":"2022-07-19T04:21:51","guid":{"rendered":"https:\/\/file.currentschoolnews.com\/?post_type=product&p=9233"},"modified":"2022-07-19T08:26:46","modified_gmt":"2022-07-19T08:26:46","slug":"analysis-of-horizontal-air-silicone-oil-plug-to-slug-transition-flow","status":"publish","type":"product","link":"https:\/\/pastexamquestions.com\/product\/analysis-of-horizontal-air-silicone-oil-plug-to-slug-transition-flow\/","title":{"rendered":"Analysis of Horizontal Air-Silicone Oil Plug-To-Slug Transition Flow"},"content":{"rendered":"

– Analysis of Horizontal Air-Silicone Oil Plug-To-Slug Transition Flow –<\/strong><\/span><\/p>\n

Download Analysis of Horizontal Air-Silicone Oil Plug-To-Slug Transition Flow<\/strong><\/span>. Petroleum Engineering students who are writing their projects can get this material to aid their research work.<\/span><\/span><\/p>\n

Abstract<\/b><\/span><\/h2>\n

The analysis of the experimental data for the air-silicone oil plug-slug transition in a 67mm id and 6m long horizontal pipe was carried out in this work.<\/p>\n

The superficial gas and liquid velocity ranged from (0.05 \u2013 4.73) m\/s and (0.05 \u2013 0.473) m\/s respectively. The transition from plug to slug flow was investigated by increasing the superficial gas velocity at fixed superficial liquid velocity.<\/p>\n

For the investigated experimental data set, the intermittent flow was observed at the superficial liquid velocity of 0.142m\/s. The transition from plug to slug flow for the experimental data was observed at the superficial velocity of between 0.7 \u2013 1.2m\/s.<\/p>\n

To characterize the plug \u2013 slug transition, the effect of liquid and gas superficial velocity on void fraction, bubble velocity, bubble length and slug frequency were obtained.<\/p>\n

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Introduction<\/span><\/span><\/strong><\/span><\/h2>\n

Two-phase flow occurs when two different fluids move concurrently through a pipe. The exact form of two-phase flow is determined according to the phases appearing in the mixture, namely solid-liquid, gas-solid (e.g. particles in a gas or liquid) and gas-liquid (droplets in gas and gas bubbles in a liquid)(Gschnaidtner, 2015).<\/p>\n

The study of two-phase flows is of great importance for several technological applications.<\/p>\n

Particularly, gas-liquid two-phase flows are often encountered in a wide range of industrial applications, such as condensers, evaporators, distillation towers, nuclear power plants, boilers, crude oil transportation and chemical plants among others.<\/p>\n

Gas-liquid flow is not only the most common of the two-phase flows; it is also the most complex since it combines the characteristics of a deformable interface with those of a compressible phase (Carpintero, 2009).<\/p>\n

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