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David Mason - Academia.edu
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<div id="Pill-react-component-3959ad98-0d9c-4c96-aff6-656f709f93bb"></div> </a></div></div></div></div><div class="right-panel-container"><div class="user-content-wrapper"><div class="uploads-container" id="social-redesign-work-container"><div class="upload-header"><h2 class="ds2-5-heading-sans-serif-xs">Uploads</h2></div><div class="documents-container backbone-social-profile-documents" style="width: 100%;"><div class="u-taCenter"></div><div class="profile--tab_content_container js-tab-pane tab-pane active" id="all"><div class="profile--tab_heading_container js-section-heading" data-section="Papers" id="Papers"><h3 class="profile--tab_heading_container">Papers by David Mason</h3></div><div class="js-work-strip profile--work_container" data-work-id="34238882"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238882/Transient_heating_of_semitransparent_droplet"><img 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class="js-work-strip profile--work_container" data-work-id="34238881"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238881/The_effect_of_a_bend_on_the_particle_cross_section_concentration_and_segregation_in_pneumatic_conveying_systems"><img alt="Research paper thumbnail of The effect of a bend on the particle cross-section concentration and segregation in pneumatic conveying systems" class="work-thumbnail" src="https://attachments.academia-assets.com/54152916/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238881/The_effect_of_a_bend_on_the_particle_cross_section_concentration_and_segregation_in_pneumatic_conveying_systems">The effect of a bend on the particle cross-section concentration and segregation in pneumatic conveying systems</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1998</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="465b6472902f59d4c651519fdcef65ba" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54152916,"asset_id":34238881,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54152916/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238881"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa 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class="wp-workCard_item"><span>International Journal of Multiphase Flow</span><span>, 2001</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="2079d1350f1094c4ae0e737f5db01f39" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54152919,"asset_id":34238880,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238880"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span 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WowProfile.WorkStripView({ el: this, workJSON: {"id":34238880,"title":"A model for non-suspension gas–solids flow of fine powders in pipes","translated_title":"","metadata":{"grobid_abstract":"The two-layer concept developed previously for a liquid±solids¯ow has been adapted to model dense phase transport of powders in pneumatic conveying systems. Many bulk materials of this type are capable of¯owing in a non-suspension moving-bed type of¯ow. A new model for this type of¯ow in a horizontal pipe has been developed where the¯ow is modelled as two layers: a dilute gas±solids mixturē owing above a dense gas±solids mixture. For each layer, the conservation equations for mass, momentum and energy were solved for both the gas and solids phases. In addition, mass, momentum and energy transfers between the two layers were modelled. A single pressure was shared between the two layers. The paper describes the sub-models used to describe phenomena, such as the momentum transfer between the gas and solids in a layer. Transfer of mass, momentum and energy between the two layers results in a model that behaves in a similar manner to experimental observations. For example, as the mean¯ow velocity increases, the depth of the dense layer decreases. The predicted pressure pro®le for fully developed¯ow was compared with experimental data. In general, the prediction of pressure pro®le, and the predicted depth of the dense layer show reasonable agreement with the experimental observations. A parametric study was conducted to assess the relative signi®cance of the initial conditions on the overall behaviour of the model. Variation of the initial conditions for the same total gas and solids mass¯ow rates was found to have only a small eect on the prediction of fully developed ow. 7","publication_date":{"day":null,"month":null,"year":2001,"errors":{}},"publication_name":"International Journal of Multiphase Flow","grobid_abstract_attachment_id":54152919},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238880/A_model_for_non_suspension_gas_solids_flow_of_fine_powders_in_pipes","translated_internal_url":"","created_at":"2017-08-16T02:14:38.004-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021512,"work_id":34238880,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":3188978,"email":"a***y@gcal.ac.uk","display_order":1,"name":"Avi Levy","title":"A model for non-suspension gas–solids flow of fine powders in pipes"}],"downloadable_attachments":[{"id":54152919,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152919/thumbnails/1.jpg","file_name":"s0301-9322_2800_2900033-120170816-24899-yw1g44.pdf","download_url":"https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_model_for_non_suspension_gas_solids_fl.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152919/s0301-9322_2800_2900033-120170816-24899-yw1g44-libre.pdf?1502875702=\u0026response-content-disposition=attachment%3B+filename%3DA_model_for_non_suspension_gas_solids_fl.pdf\u0026Expires=1732701372\u0026Signature=KmE-f-UkiHiGk522kx5M3sbaTV0EDrgdl-i~izhWSj-7zT-oZhVPXLcGPHdGhOGzo71dxW9TV8nAsJB2z5pqn5NoxWvQweT8r5mL1DcJPpOud2pCzNlWoWwsdEcBG8XcrfaQgKQviANFJJxUeAWlPMa3~BCYoJEb3PCILvieE08gUEyYvCIBM8G3I5Crnk4GLeYw7RF3n0DEnEphmOM6mPtz80ge9nKMKjT~c8s6WRi0XJqMRE~xP2nFGjRK2S7rdDeFQ6kaoZWG6qz-FYUW3DwDtDqTXy1D2Xqzh5GUm4S2Q8IZ5XJlfVKW8zgq-y4fey2T~qmXh-CA6Vb6M9niRA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"A_model_for_non_suspension_gas_solids_flow_of_fine_powders_in_pipes","translated_slug":"","page_count":21,"language":"en","content_type":"Work","owner":{"id":66921411,"first_name":"David","middle_initials":null,"last_name":"Mason","page_name":"DavidMason51","domain_name":"independent","created_at":"2017-08-02T02:46:31.327-07:00","display_name":"David Mason","url":"https://independent.academia.edu/DavidMason51"},"attachments":[{"id":54152919,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152919/thumbnails/1.jpg","file_name":"s0301-9322_2800_2900033-120170816-24899-yw1g44.pdf","download_url":"https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_model_for_non_suspension_gas_solids_fl.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152919/s0301-9322_2800_2900033-120170816-24899-yw1g44-libre.pdf?1502875702=\u0026response-content-disposition=attachment%3B+filename%3DA_model_for_non_suspension_gas_solids_fl.pdf\u0026Expires=1732701372\u0026Signature=KmE-f-UkiHiGk522kx5M3sbaTV0EDrgdl-i~izhWSj-7zT-oZhVPXLcGPHdGhOGzo71dxW9TV8nAsJB2z5pqn5NoxWvQweT8r5mL1DcJPpOud2pCzNlWoWwsdEcBG8XcrfaQgKQviANFJJxUeAWlPMa3~BCYoJEb3PCILvieE08gUEyYvCIBM8G3I5Crnk4GLeYw7RF3n0DEnEphmOM6mPtz80ge9nKMKjT~c8s6WRi0XJqMRE~xP2nFGjRK2S7rdDeFQ6kaoZWG6qz-FYUW3DwDtDqTXy1D2Xqzh5GUm4S2Q8IZ5XJlfVKW8zgq-y4fey2T~qmXh-CA6Vb6M9niRA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":7114,"name":"Multiphase Flow","url":"https://www.academia.edu/Documents/in/Multiphase_Flow"},{"id":717129,"name":"Energy Transfer","url":"https://www.academia.edu/Documents/in/Energy_Transfer"},{"id":898062,"name":"Flow Rate","url":"https://www.academia.edu/Documents/in/Flow_Rate"},{"id":1119718,"name":"Initial Condition","url":"https://www.academia.edu/Documents/in/Initial_Condition"},{"id":1120502,"name":"Experimental Data","url":"https://www.academia.edu/Documents/in/Experimental_Data"},{"id":1712648,"name":"Momentum Transfer","url":"https://www.academia.edu/Documents/in/Momentum_Transfer"},{"id":2003399,"name":"Parametric Study","url":"https://www.academia.edu/Documents/in/Parametric_Study"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34238879"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe"><img alt="Research paper thumbnail of An investigation of the flow structure through abrupt enlargement of circular pipe" class="work-thumbnail" src="https://attachments.academia-assets.com/54152918/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe">An investigation of the flow structure through abrupt enlargement of circular pipe</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1999</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="da8d287df0ccf2c6e686330bf1f4f13e" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54152918,"asset_id":34238879,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54152918/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238879"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34238879"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34238879; 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dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "da8d287df0ccf2c6e686330bf1f4f13e" } } $('.js-work-strip[data-work-id=34238879]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238879,"title":"An investigation of the flow structure through abrupt enlargement of circular pipe","translated_title":"","metadata":{"grobid_abstract":"There are many examples of flow of gas, with or without solids, where an abrupt change of cross-sectional area has to be implemented. A typical example is long distance pneumatic conveying where single bore pipeline normally requires high pressure drop which consequently results in high gas and solids velocities towards the end of pipeline. In those cases, stepped pipeline is used in order to reduce both gas and solids velocity whenever they reach unacceptable level. The flow structure through an abrupt enlargement of a conduit can be very complex, specially in the case of gas-solids flow. Both velocity and pressure fields are very important for the analysis and design of the overall flow characteristics. The compressible flow of gas through an abrupt enlargement was modelled using both a 1-D analytical model and 3-D numerical model. A summary of the analytical 1-D model of compressible flow through an abrupt Ž . enlargement and the results obtained for the flow through stepped pipe 81 to 105 mm for several flow conditions are presented in this paper. Those results have been compared with the 3-D numerical model which solves basic conservation equations and very good agreement was found. Finally the same 3-D numerical model was applied to several regimes of gas-solids flow in order to investigate the structure of gas and solids velocity field, as well as pressure distribution along the pipe. Special attention has been paid to the pressure recovery downstream from the enlargement due to its important role in the design of stepped pipeline pneumatic conveying system. q 1999 Elsevier Science S.A. All rights reserved.","publication_date":{"day":null,"month":null,"year":1999,"errors":{}},"publication_name":"Powder Technology","grobid_abstract_attachment_id":54152918},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe","translated_internal_url":"","created_at":"2017-08-16T02:14:37.730-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021529,"work_id":34238879,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":6479836,"email":"p***c@gcal.ac.uk","display_order":0,"name":"Predrag Marjanovic","title":"An investigation of the flow structure through abrupt enlargement of circular pipe"},{"id":30021530,"work_id":34238879,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":3188978,"email":"a***y@gcal.ac.uk","display_order":4194304,"name":"Avi Levy","title":"An investigation of the flow structure through abrupt enlargement of circular 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Field","url":"https://www.academia.edu/Documents/in/Velocity_Field"},{"id":1144265,"name":"Pressure Distribution","url":"https://www.academia.edu/Documents/in/Pressure_Distribution"},{"id":1714028,"name":"Long Distance","url":"https://www.academia.edu/Documents/in/Long_Distance"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34238878"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238878/A_comparison_of_analytical_and_numerical_models_with_experimental_data_for_gas_solid_flow_through_a_straight_pipe_at_different_inclinations"><img alt="Research paper thumbnail of A comparison of analytical and numerical models with experimental data for gas-solid flow through a straight pipe at different inclinations" class="work-thumbnail" src="https://attachments.academia-assets.com/54152921/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238878/A_comparison_of_analytical_and_numerical_models_with_experimental_data_for_gas_solid_flow_through_a_straight_pipe_at_different_inclinations">A comparison of analytical and numerical models with experimental data for gas-solid flow through a straight pipe at different inclinations</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1997</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="dc8723685dc7aee792b06634b1d022ac" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" 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developed. This model predicts the ratio of the total pressure drop in an inclined pipe to that of a horizontal pipe. The model has been used to predict the critical pipe angle, which is defined as the angle at which the maximum pressure drop for a given solids flow rate is achieved. This angle differs from 90 ° (found in a single-phase flow) and is directly proportional to the ratio between the gas superficial velocity and the particle terminal velocity. The three-dimensional conservation equations for steady-state two-phase flow in an inclined pipe were solved numerically for constant solids and gas flow rates at different pipe inclinations. This model was based on the continuum theory for describing the mass and momentum balance equations for the fluid and solid phases. A packing model, describing the shear stress of the solid phase as a function of its volume fraction, is suggested in order to limit the maximum value of the solid volume fraction. A new model for particle-wall interaction was developed taking into account the angle of inclination of the pipe. The prediction of the numerical model was compared with experimental data obtained in a specially designed test rig. In general, the agreement between the experimental data and the models was satisfactory. The results of the numerical simulation also confirmed that the critical pipe angle for gas-solid flow is lower than 90 ° . The assumptions made during the development of the models were assessed in order to explain the differences between the predicted and measured values of the flow parameters for different flow regimes. © 1997 Elsevier Science S.A.","publication_date":{"day":null,"month":null,"year":1997,"errors":{}},"publication_name":"Powder 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data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems"><img alt="Research paper thumbnail of A simulation system for pneumatic conveying systems" class="work-thumbnail" src="https://attachments.academia-assets.com/54152917/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems">A simulation system for pneumatic conveying systems</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1998</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="58cac44dade2bd73929a7a9082ff5a13" class="wp-workCard--action" rel="nofollow" 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window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=34238877]").text(description); $(".js-view-count[data-work-id=34238877]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 34238877; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='34238877']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 34238877, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (true){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "58cac44dade2bd73929a7a9082ff5a13" } } $('.js-work-strip[data-work-id=34238877]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238877,"title":"A simulation system for pneumatic conveying systems","translated_title":"","metadata":{"grobid_abstract":"Pneurnai,ic conveying sysi,erns provide a highly flexible means of transporting dry hulk particuhite materials, The main prahlerri encountered when designing, optimising, or uprating these systems ix the deterrnination of tile air supply necessary to achieve a particular duty ( solids mass ttow rate ). Many correlations exist i,o predict the pressure drop llecessary to drive the flow, arid Ihe gas velocities necessary fi)r successful openltion. Unforturiately. i,l'ie design methods th:lt incorponite these correlatioris are limited in terms of their Ilexibilitv. The developnlent of this siiriulation resulted fi'orrl the desire to increase the Itexibilii,y of i,he design method, and the need to employ rnore than one pressure drop con'elai,ion. As a i'e~ult of Ihese i,~o requirerneni,s tile prohlen'i of simulating the Ol'~eration of a pneunlati¢ conveying system was re-evaluated. ~¢; \u003e I t)91.,l Elsevier Scielice S.A.","publication_date":{"day":null,"month":null,"year":1998,"errors":{}},"publication_name":"Powder Technology","grobid_abstract_attachment_id":54152917},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems","translated_internal_url":"","created_at":"2017-08-16T02:14:37.158-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021533,"work_id":34238877,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":6479836,"email":"p***c@gcal.ac.uk","display_order":1,"name":"Predrag Marjanovic","title":"A simulation system for pneumatic conveying systems"}],"downloadable_attachments":[{"id":54152917,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152917/thumbnails/1.jpg","file_name":"s0032-5910_2897_2903310-x20170816-24893-13chr6.pdf","download_url":"https://www.academia.edu/attachments/54152917/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_simulation_system_for_pneumatic_convey.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152917/s0032-5910_2897_2903310-x20170816-24893-13chr6-libre.pdf?1502875711=\u0026response-content-disposition=attachment%3B+filename%3DA_simulation_system_for_pneumatic_convey.pdf\u0026Expires=1732701372\u0026Signature=EzN23OEqC8sbTPUn1oYy-pbM9qSvjrnJU63JBTSwIrfF~p8PvLl-ExDn7XmXQW25XBzHTs002yRVMOGoua~CcDX-Q5fEf~SvEBm7F5zvftdobEdawv-H5J-7ICdLiKcAA~UnCbfUVhcVAgaBIb~62Vw8jahDEed1nuGa101CTLwfbfz2NfCSPJy8kKWBbDAFxQN9ZT-Mn0M2av7EKpoM~iK9XAaHyUdqj~HXfApe~4SHfiL9k9NdhCTLoYAQ71fYouKSmS4Pm~ZCDQddTdln78~aXbEWx9LvrApeZATYqyoU-pKS2AQqG8PHYYVhymM3saS5bly8FpdMmHPqUhxaEg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"A_simulation_system_for_pneumatic_conveying_systems","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":66921411,"first_name":"David","middle_initials":null,"last_name":"Mason","page_name":"DavidMason51","domain_name":"independent","created_at":"2017-08-02T02:46:31.327-07:00","display_name":"David Mason","url":"https://independent.academia.edu/DavidMason51"},"attachments":[{"id":54152917,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152917/thumbnails/1.jpg","file_name":"s0032-5910_2897_2903310-x20170816-24893-13chr6.pdf","download_url":"https://www.academia.edu/attachments/54152917/download_file?st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_simulation_system_for_pneumatic_convey.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152917/s0032-5910_2897_2903310-x20170816-24893-13chr6-libre.pdf?1502875711=\u0026response-content-disposition=attachment%3B+filename%3DA_simulation_system_for_pneumatic_convey.pdf\u0026Expires=1732701372\u0026Signature=EzN23OEqC8sbTPUn1oYy-pbM9qSvjrnJU63JBTSwIrfF~p8PvLl-ExDn7XmXQW25XBzHTs002yRVMOGoua~CcDX-Q5fEf~SvEBm7F5zvftdobEdawv-H5J-7ICdLiKcAA~UnCbfUVhcVAgaBIb~62Vw8jahDEed1nuGa101CTLwfbfz2NfCSPJy8kKWBbDAFxQN9ZT-Mn0M2av7EKpoM~iK9XAaHyUdqj~HXfApe~4SHfiL9k9NdhCTLoYAQ71fYouKSmS4Pm~ZCDQddTdln78~aXbEWx9LvrApeZATYqyoU-pKS2AQqG8PHYYVhymM3saS5bly8FpdMmHPqUhxaEg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":23020,"name":"Powder technology","url":"https://www.academia.edu/Documents/in/Powder_technology"},{"id":80596,"name":"Design method","url":"https://www.academia.edu/Documents/in/Design_method"},{"id":331203,"name":"Pressure Drop","url":"https://www.academia.edu/Documents/in/Pressure_Drop"},{"id":898062,"name":"Flow Rate","url":"https://www.academia.edu/Documents/in/Flow_Rate"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34238876"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238876/Pneumatic_Conveying_Systems_in_Dense_Phase"><img alt="Research paper thumbnail of Pneumatic Conveying Systems in Dense Phase" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238876/Pneumatic_Conveying_Systems_in_Dense_Phase">Pneumatic Conveying Systems in Dense Phase</a></div><div class="wp-workCard_item"><span>Nondestructive Testing and Evaluation</span><span>, 1998</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phas...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phase pneumatic pipelines. The instrument has six americium-241 gamma ray sources and thirty miniature sodium iodide detectors arranged symmetrically around a pipe section. The instrumentation system comprises a multi-channel preamplifier, a CAMAC crate containing multi-channel discriminators, scalers and a GPIB crate controller, and an IBM-compatible personal computer. The detector gains are individually controlled by analogue voltage outputs provided by multi-channel DAC interface cards. The detector count-rates are used with a filtered linear back-projection algorithm to estimate the distribution of solid material over the pipe cross-section at a rate of ten images per second in real time. Preliminary laboratory tests have been carried out on a fluidised bed formed inside a permeameter tube and a full-scale test pipeline and instrument room have been developed for conveying tests.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238876"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34238876"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34238876; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=34238876]").text(description); $(".js-view-count[data-work-id=34238876]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 34238876; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='34238876']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 34238876, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=34238876]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238876,"title":"Pneumatic Conveying Systems in Dense Phase","translated_title":"","metadata":{"abstract":"ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phase pneumatic pipelines. 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This model was applied to the drying process of wet coal particles in a gas flow. The coal particles were assumed to have a wet core and a dry oute crust. 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34075885"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34075885/Transient_heating_of_a_semitransparent_spherical_body"><img alt="Research paper thumbnail of Transient heating of a semitransparent spherical body" class="work-thumbnail" src="https://attachments.academia-assets.com/54010855/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34075885/Transient_heating_of_a_semitransparent_spherical_body">Transient heating of a semitransparent spherical body</a></div><div class="wp-workCard_item wp-workCard--coauthors"><span>by </span><span><a class="" data-click-track="profile-work-strip-authors" href="https://independent.academia.edu/SergeiSazhin">Sergei Sazhin</a> and <a class="" data-click-track="profile-work-strip-authors" href="https://independent.academia.edu/DavidMason51">David Mason</a></span></div><div class="wp-workCard_item"><span>International Journal of Thermal Sciences</span><span>, 2007</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="3f4e790dc5d58a0e5c902b70026a761e" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54010855,"asset_id":34075885,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54010855/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34075885"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34075885"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34075885; 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dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "3f4e790dc5d58a0e5c902b70026a761e" } } $('.js-work-strip[data-work-id=34075885]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34075885,"title":"Transient heating of a semitransparent spherical body","translated_title":"","metadata":{"grobid_abstract":"The problem of transient heating of a semitransparent spherical body immersed in a stationary hot gas is investigated, taking into account the effect of thermal radiation. The size of the domain occupied by the gas is assumed to be finite, and the outer boundary of this domain is kept at constant temperature. The initial radial distribution of temperature in the body is taken into account. A modification of Newton's law for body heating is introduced via a correction to either the gas temperature or convection heat transfer coefficient. Explicit expressions for these corrections are obtained for the case of homogeneous initial distribution of temperature and radiation absorption inside the body, and constant radiation temperature. For large Fourier numbers Fo, the correction to gas temperature is expected to be of limited practical importance, as both this correction and the difference between the initial gas temperature and the body surface temperature approach zero (heat transferred from gas to the body becomes negligible). The results are analysed using values of parameters relevant to diesel engines. The values of the corrections to the convection heat transfer coefficient vary from about 0.1 (large domain occupied by gas and Fo = 500) to 2.8 at Fo = 0.1. This means that ignoring these corrections is expected to lead to unacceptably large errors in computations. The total time for body heating is shown to be more than an order of magnitude longer when compared to the heating of this body in a perfectly stirred gas. The effect of thermal radiation on droplet heating is accounted for via the additional corrections of gas temperature or the convection heat transfer coefficient. 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class="wp-workCard_item"><span>International Journal of Multiphase Flow</span><span>, 2001</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="2079d1350f1094c4ae0e737f5db01f39" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54152919,"asset_id":34238880,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238880"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa 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$('.js-work-strip[data-work-id=34238880]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238880,"title":"A model for non-suspension gas–solids flow of fine powders in pipes","translated_title":"","metadata":{"grobid_abstract":"The two-layer concept developed previously for a liquid±solids¯ow has been adapted to model dense phase transport of powders in pneumatic conveying systems. Many bulk materials of this type are capable of¯owing in a non-suspension moving-bed type of¯ow. A new model for this type of¯ow in a horizontal pipe has been developed where the¯ow is modelled as two layers: a dilute gas±solids mixturē owing above a dense gas±solids mixture. For each layer, the conservation equations for mass, momentum and energy were solved for both the gas and solids phases. In addition, mass, momentum and energy transfers between the two layers were modelled. A single pressure was shared between the two layers. The paper describes the sub-models used to describe phenomena, such as the momentum transfer between the gas and solids in a layer. Transfer of mass, momentum and energy between the two layers results in a model that behaves in a similar manner to experimental observations. For example, as the mean¯ow velocity increases, the depth of the dense layer decreases. The predicted pressure pro®le for fully developed¯ow was compared with experimental data. In general, the prediction of pressure pro®le, and the predicted depth of the dense layer show reasonable agreement with the experimental observations. A parametric study was conducted to assess the relative signi®cance of the initial conditions on the overall behaviour of the model. Variation of the initial conditions for the same total gas and solids mass¯ow rates was found to have only a small eect on the prediction of fully developed ow. 7","publication_date":{"day":null,"month":null,"year":2001,"errors":{}},"publication_name":"International Journal of Multiphase Flow","grobid_abstract_attachment_id":54152919},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238880/A_model_for_non_suspension_gas_solids_flow_of_fine_powders_in_pipes","translated_internal_url":"","created_at":"2017-08-16T02:14:38.004-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021512,"work_id":34238880,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":3188978,"email":"a***y@gcal.ac.uk","display_order":1,"name":"Avi Levy","title":"A model for non-suspension gas–solids flow of fine powders in pipes"}],"downloadable_attachments":[{"id":54152919,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152919/thumbnails/1.jpg","file_name":"s0301-9322_2800_2900033-120170816-24899-yw1g44.pdf","download_url":"https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_model_for_non_suspension_gas_solids_fl.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152919/s0301-9322_2800_2900033-120170816-24899-yw1g44-libre.pdf?1502875702=\u0026response-content-disposition=attachment%3B+filename%3DA_model_for_non_suspension_gas_solids_fl.pdf\u0026Expires=1732701372\u0026Signature=KmE-f-UkiHiGk522kx5M3sbaTV0EDrgdl-i~izhWSj-7zT-oZhVPXLcGPHdGhOGzo71dxW9TV8nAsJB2z5pqn5NoxWvQweT8r5mL1DcJPpOud2pCzNlWoWwsdEcBG8XcrfaQgKQviANFJJxUeAWlPMa3~BCYoJEb3PCILvieE08gUEyYvCIBM8G3I5Crnk4GLeYw7RF3n0DEnEphmOM6mPtz80ge9nKMKjT~c8s6WRi0XJqMRE~xP2nFGjRK2S7rdDeFQ6kaoZWG6qz-FYUW3DwDtDqTXy1D2Xqzh5GUm4S2Q8IZ5XJlfVKW8zgq-y4fey2T~qmXh-CA6Vb6M9niRA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"A_model_for_non_suspension_gas_solids_flow_of_fine_powders_in_pipes","translated_slug":"","page_count":21,"language":"en","content_type":"Work","owner":{"id":66921411,"first_name":"David","middle_initials":null,"last_name":"Mason","page_name":"DavidMason51","domain_name":"independent","created_at":"2017-08-02T02:46:31.327-07:00","display_name":"David Mason","url":"https://independent.academia.edu/DavidMason51"},"attachments":[{"id":54152919,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152919/thumbnails/1.jpg","file_name":"s0301-9322_2800_2900033-120170816-24899-yw1g44.pdf","download_url":"https://www.academia.edu/attachments/54152919/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_model_for_non_suspension_gas_solids_fl.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152919/s0301-9322_2800_2900033-120170816-24899-yw1g44-libre.pdf?1502875702=\u0026response-content-disposition=attachment%3B+filename%3DA_model_for_non_suspension_gas_solids_fl.pdf\u0026Expires=1732701372\u0026Signature=KmE-f-UkiHiGk522kx5M3sbaTV0EDrgdl-i~izhWSj-7zT-oZhVPXLcGPHdGhOGzo71dxW9TV8nAsJB2z5pqn5NoxWvQweT8r5mL1DcJPpOud2pCzNlWoWwsdEcBG8XcrfaQgKQviANFJJxUeAWlPMa3~BCYoJEb3PCILvieE08gUEyYvCIBM8G3I5Crnk4GLeYw7RF3n0DEnEphmOM6mPtz80ge9nKMKjT~c8s6WRi0XJqMRE~xP2nFGjRK2S7rdDeFQ6kaoZWG6qz-FYUW3DwDtDqTXy1D2Xqzh5GUm4S2Q8IZ5XJlfVKW8zgq-y4fey2T~qmXh-CA6Vb6M9niRA__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":48,"name":"Engineering","url":"https://www.academia.edu/Documents/in/Engineering"},{"id":7114,"name":"Multiphase Flow","url":"https://www.academia.edu/Documents/in/Multiphase_Flow"},{"id":717129,"name":"Energy Transfer","url":"https://www.academia.edu/Documents/in/Energy_Transfer"},{"id":898062,"name":"Flow Rate","url":"https://www.academia.edu/Documents/in/Flow_Rate"},{"id":1119718,"name":"Initial Condition","url":"https://www.academia.edu/Documents/in/Initial_Condition"},{"id":1120502,"name":"Experimental Data","url":"https://www.academia.edu/Documents/in/Experimental_Data"},{"id":1712648,"name":"Momentum Transfer","url":"https://www.academia.edu/Documents/in/Momentum_Transfer"},{"id":2003399,"name":"Parametric Study","url":"https://www.academia.edu/Documents/in/Parametric_Study"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34238879"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe"><img alt="Research paper thumbnail of An investigation of the flow structure through abrupt enlargement of circular pipe" class="work-thumbnail" src="https://attachments.academia-assets.com/54152918/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe">An investigation of the flow structure through abrupt enlargement of circular pipe</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1999</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="da8d287df0ccf2c6e686330bf1f4f13e" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54152918,"asset_id":34238879,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54152918/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238879"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34238879"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34238879; 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dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "da8d287df0ccf2c6e686330bf1f4f13e" } } $('.js-work-strip[data-work-id=34238879]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238879,"title":"An investigation of the flow structure through abrupt enlargement of circular pipe","translated_title":"","metadata":{"grobid_abstract":"There are many examples of flow of gas, with or without solids, where an abrupt change of cross-sectional area has to be implemented. A typical example is long distance pneumatic conveying where single bore pipeline normally requires high pressure drop which consequently results in high gas and solids velocities towards the end of pipeline. In those cases, stepped pipeline is used in order to reduce both gas and solids velocity whenever they reach unacceptable level. The flow structure through an abrupt enlargement of a conduit can be very complex, specially in the case of gas-solids flow. Both velocity and pressure fields are very important for the analysis and design of the overall flow characteristics. The compressible flow of gas through an abrupt enlargement was modelled using both a 1-D analytical model and 3-D numerical model. A summary of the analytical 1-D model of compressible flow through an abrupt Ž . enlargement and the results obtained for the flow through stepped pipe 81 to 105 mm for several flow conditions are presented in this paper. Those results have been compared with the 3-D numerical model which solves basic conservation equations and very good agreement was found. Finally the same 3-D numerical model was applied to several regimes of gas-solids flow in order to investigate the structure of gas and solids velocity field, as well as pressure distribution along the pipe. Special attention has been paid to the pressure recovery downstream from the enlargement due to its important role in the design of stepped pipeline pneumatic conveying system. q 1999 Elsevier Science S.A. All rights reserved.","publication_date":{"day":null,"month":null,"year":1999,"errors":{}},"publication_name":"Powder Technology","grobid_abstract_attachment_id":54152918},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238879/An_investigation_of_the_flow_structure_through_abrupt_enlargement_of_circular_pipe","translated_internal_url":"","created_at":"2017-08-16T02:14:37.730-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021529,"work_id":34238879,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":6479836,"email":"p***c@gcal.ac.uk","display_order":0,"name":"Predrag Marjanovic","title":"An investigation of the flow structure through abrupt enlargement of circular 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different inclinations" class="work-thumbnail" src="https://attachments.academia-assets.com/54152921/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238878/A_comparison_of_analytical_and_numerical_models_with_experimental_data_for_gas_solid_flow_through_a_straight_pipe_at_different_inclinations">A comparison of analytical and numerical models with experimental data for gas-solid flow through a straight pipe at different inclinations</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1997</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="dc8723685dc7aee792b06634b1d022ac" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" 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analytical model for gas-solid suspension flow through an inclined section of pipe was developed. This model predicts the ratio of the total pressure drop in an inclined pipe to that of a horizontal pipe. The model has been used to predict the critical pipe angle, which is defined as the angle at which the maximum pressure drop for a given solids flow rate is achieved. This angle differs from 90 ° (found in a single-phase flow) and is directly proportional to the ratio between the gas superficial velocity and the particle terminal velocity. The three-dimensional conservation equations for steady-state two-phase flow in an inclined pipe were solved numerically for constant solids and gas flow rates at different pipe inclinations. This model was based on the continuum theory for describing the mass and momentum balance equations for the fluid and solid phases. A packing model, describing the shear stress of the solid phase as a function of its volume fraction, is suggested in order to limit the maximum value of the solid volume fraction. A new model for particle-wall interaction was developed taking into account the angle of inclination of the pipe. The prediction of the numerical model was compared with experimental data obtained in a specially designed test rig. In general, the agreement between the experimental data and the models was satisfactory. The results of the numerical simulation also confirmed that the critical pipe angle for gas-solid flow is lower than 90 ° . The assumptions made during the development of the models were assessed in order to explain the differences between the predicted and measured values of the flow parameters for different flow regimes. © 1997 Elsevier Science S.A.","publication_date":{"day":null,"month":null,"year":1997,"errors":{}},"publication_name":"Powder 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data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems"><img alt="Research paper thumbnail of A simulation system for pneumatic conveying systems" class="work-thumbnail" src="https://attachments.academia-assets.com/54152917/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems">A simulation system for pneumatic conveying systems</a></div><div class="wp-workCard_item"><span>Powder Technology</span><span>, 1998</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="58cac44dade2bd73929a7a9082ff5a13" class="wp-workCard--action" rel="nofollow" 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materials, The main prahlerri encountered when designing, optimising, or uprating these systems ix the deterrnination of tile air supply necessary to achieve a particular duty ( solids mass ttow rate ). Many correlations exist i,o predict the pressure drop llecessary to drive the flow, arid Ihe gas velocities necessary fi)r successful openltion. Unforturiately. i,l'ie design methods th:lt incorponite these correlatioris are limited in terms of their Ilexibilitv. The developnlent of this siiriulation resulted fi'orrl the desire to increase the Itexibilii,y of i,he design method, and the need to employ rnore than one pressure drop con'elai,ion. As a i'e~ult of Ihese i,~o requirerneni,s tile prohlen'i of simulating the Ol'~eration of a pneunlati¢ conveying system was re-evaluated. ~¢; \u003e I t)91.,l Elsevier Scielice S.A.","publication_date":{"day":null,"month":null,"year":1998,"errors":{}},"publication_name":"Powder Technology","grobid_abstract_attachment_id":54152917},"translated_abstract":null,"internal_url":"https://www.academia.edu/34238877/A_simulation_system_for_pneumatic_conveying_systems","translated_internal_url":"","created_at":"2017-08-16T02:14:37.158-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021533,"work_id":34238877,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":6479836,"email":"p***c@gcal.ac.uk","display_order":1,"name":"Predrag Marjanovic","title":"A simulation system for pneumatic conveying systems"}],"downloadable_attachments":[{"id":54152917,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152917/thumbnails/1.jpg","file_name":"s0032-5910_2897_2903310-x20170816-24893-13chr6.pdf","download_url":"https://www.academia.edu/attachments/54152917/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_simulation_system_for_pneumatic_convey.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152917/s0032-5910_2897_2903310-x20170816-24893-13chr6-libre.pdf?1502875711=\u0026response-content-disposition=attachment%3B+filename%3DA_simulation_system_for_pneumatic_convey.pdf\u0026Expires=1732701372\u0026Signature=EzN23OEqC8sbTPUn1oYy-pbM9qSvjrnJU63JBTSwIrfF~p8PvLl-ExDn7XmXQW25XBzHTs002yRVMOGoua~CcDX-Q5fEf~SvEBm7F5zvftdobEdawv-H5J-7ICdLiKcAA~UnCbfUVhcVAgaBIb~62Vw8jahDEed1nuGa101CTLwfbfz2NfCSPJy8kKWBbDAFxQN9ZT-Mn0M2av7EKpoM~iK9XAaHyUdqj~HXfApe~4SHfiL9k9NdhCTLoYAQ71fYouKSmS4Pm~ZCDQddTdln78~aXbEWx9LvrApeZATYqyoU-pKS2AQqG8PHYYVhymM3saS5bly8FpdMmHPqUhxaEg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"slug":"A_simulation_system_for_pneumatic_conveying_systems","translated_slug":"","page_count":8,"language":"en","content_type":"Work","owner":{"id":66921411,"first_name":"David","middle_initials":null,"last_name":"Mason","page_name":"DavidMason51","domain_name":"independent","created_at":"2017-08-02T02:46:31.327-07:00","display_name":"David Mason","url":"https://independent.academia.edu/DavidMason51"},"attachments":[{"id":54152917,"title":"","file_type":"pdf","scribd_thumbnail_url":"https://attachments.academia-assets.com/54152917/thumbnails/1.jpg","file_name":"s0032-5910_2897_2903310-x20170816-24893-13chr6.pdf","download_url":"https://www.academia.edu/attachments/54152917/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Miw4LjIyMi4yMDguMTQ2&","bulk_download_file_name":"A_simulation_system_for_pneumatic_convey.pdf","bulk_download_url":"https://d1wqtxts1xzle7.cloudfront.net/54152917/s0032-5910_2897_2903310-x20170816-24893-13chr6-libre.pdf?1502875711=\u0026response-content-disposition=attachment%3B+filename%3DA_simulation_system_for_pneumatic_convey.pdf\u0026Expires=1732701372\u0026Signature=EzN23OEqC8sbTPUn1oYy-pbM9qSvjrnJU63JBTSwIrfF~p8PvLl-ExDn7XmXQW25XBzHTs002yRVMOGoua~CcDX-Q5fEf~SvEBm7F5zvftdobEdawv-H5J-7ICdLiKcAA~UnCbfUVhcVAgaBIb~62Vw8jahDEed1nuGa101CTLwfbfz2NfCSPJy8kKWBbDAFxQN9ZT-Mn0M2av7EKpoM~iK9XAaHyUdqj~HXfApe~4SHfiL9k9NdhCTLoYAQ71fYouKSmS4Pm~ZCDQddTdln78~aXbEWx9LvrApeZATYqyoU-pKS2AQqG8PHYYVhymM3saS5bly8FpdMmHPqUhxaEg__\u0026Key-Pair-Id=APKAJLOHF5GGSLRBV4ZA"}],"research_interests":[{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":72,"name":"Chemical Engineering","url":"https://www.academia.edu/Documents/in/Chemical_Engineering"},{"id":23020,"name":"Powder technology","url":"https://www.academia.edu/Documents/in/Powder_technology"},{"id":80596,"name":"Design method","url":"https://www.academia.edu/Documents/in/Design_method"},{"id":331203,"name":"Pressure Drop","url":"https://www.academia.edu/Documents/in/Pressure_Drop"},{"id":898062,"name":"Flow Rate","url":"https://www.academia.edu/Documents/in/Flow_Rate"}],"urls":[]}, dispatcherData: dispatcherData }); $(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34238876"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34238876/Pneumatic_Conveying_Systems_in_Dense_Phase"><img alt="Research paper thumbnail of Pneumatic Conveying Systems in Dense Phase" class="work-thumbnail" src="https://a.academia-assets.com/images/blank-paper.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238876/Pneumatic_Conveying_Systems_in_Dense_Phase">Pneumatic Conveying Systems in Dense Phase</a></div><div class="wp-workCard_item"><span>Nondestructive Testing and Evaluation</span><span>, 1998</span></div><div class="wp-workCard_item"><span class="js-work-more-abstract-truncated">ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phas...</span><a class="js-work-more-abstract" data-broccoli-component="work_strip.more_abstract" data-click-track="profile-work-strip-more-abstract" href="javascript:;"><span> more </span><span><i class="fa fa-caret-down"></i></span></a><span class="js-work-more-abstract-untruncated hidden">ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phase pneumatic pipelines. The instrument has six americium-241 gamma ray sources and thirty miniature sodium iodide detectors arranged symmetrically around a pipe section. The instrumentation system comprises a multi-channel preamplifier, a CAMAC crate containing multi-channel discriminators, scalers and a GPIB crate controller, and an IBM-compatible personal computer. The detector gains are individually controlled by analogue voltage outputs provided by multi-channel DAC interface cards. The detector count-rates are used with a filtered linear back-projection algorithm to estimate the distribution of solid material over the pipe cross-section at a rate of ten images per second in real time. Preliminary laboratory tests have been carried out on a fluidised bed formed inside a permeameter tube and a full-scale test pipeline and instrument room have been developed for conveying tests.</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34238876"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34238876"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34238876; window.Academia.workViewCountsFetcher.queue(workId, function (count) { var description = window.$h.commaizeInt(count) + " " + window.$h.pluralize(count, 'View'); $(".js-view-count[data-work-id=34238876]").text(description); $(".js-view-count[data-work-id=34238876]").attr('title', description).tooltip(); }); });</script></span></span><span><span class="percentile-widget hidden"><span class="u-mr2x work-percentile"></span></span><script>$(function () { var workId = 34238876; window.Academia.workPercentilesFetcher.queue(workId, function (percentileText) { var container = $(".js-work-strip[data-work-id='34238876']"); container.find('.work-percentile').text(percentileText.charAt(0).toUpperCase() + percentileText.slice(1)); container.find('.percentile-widget').show(); container.find('.percentile-widget').removeClass('hidden'); }); });</script></span><span><script>$(function() { new Works.PaperRankView({ workId: 34238876, container: "", }); });</script></span></div><div id="work-strip-premium-row-container"></div></div></div><script> require.config({ waitSeconds: 90 })(["https://a.academia-assets.com/assets/wow_profile-f77ea15d77ce96025a6048a514272ad8becbad23c641fc2b3bd6e24ca6ff1932.js","https://a.academia-assets.com/assets/work_edit-ad038b8c047c1a8d4fa01b402d530ff93c45fee2137a149a4a5398bc8ad67560.js"], function() { // from javascript_helper.rb var dispatcherData = {} if (false){ window.WowProfile.dispatcher = window.WowProfile.dispatcher || _.clone(Backbone.Events); dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "-1" } } $('.js-work-strip[data-work-id=34238876]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34238876,"title":"Pneumatic Conveying Systems in Dense Phase","translated_title":"","metadata":{"abstract":"ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phase pneumatic pipelines. 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Preliminary laboratory tests have been carried out on a fluidised bed formed inside a permeameter tube and a full-scale test pipeline and instrument room have been developed for conveying tests.","publication_date":{"day":null,"month":null,"year":1998,"errors":{}},"publication_name":"Nondestructive Testing and Evaluation"},"translated_abstract":"ABSTRACT A gamma ray tomograph has been designed for the study of the modes of flow in dense phase pneumatic pipelines. The instrument has six americium-241 gamma ray sources and thirty miniature sodium iodide detectors arranged symmetrically around a pipe section. The instrumentation system comprises a multi-channel preamplifier, a CAMAC crate containing multi-channel discriminators, scalers and a GPIB crate controller, and an IBM-compatible personal computer. The detector gains are individually controlled by analogue voltage outputs provided by multi-channel DAC interface cards. The detector count-rates are used with a filtered linear back-projection algorithm to estimate the distribution of solid material over the pipe cross-section at a rate of ten images per second in real time. Preliminary laboratory tests have been carried out on a fluidised bed formed inside a permeameter tube and a full-scale test pipeline and instrument room have been developed for conveying tests.","internal_url":"https://www.academia.edu/34238876/Pneumatic_Conveying_Systems_in_Dense_Phase","translated_internal_url":"","created_at":"2017-08-16T02:14:36.899-07:00","preview_url":null,"current_user_can_edit":null,"current_user_is_owner":null,"owner_id":66921411,"coauthors_can_edit":true,"document_type":"paper","co_author_tags":[{"id":30021540,"work_id":34238876,"tagging_user_id":66921411,"tagged_user_id":null,"co_author_invite_id":6479839,"email":"j***r@gcal.ac.uk","display_order":0,"name":"John Crowther","title":"Pneumatic Conveying Systems in Dense Phase"}],"downloadable_attachments":[],"slug":"Pneumatic_Conveying_Systems_in_Dense_Phase","translated_slug":"","page_count":null,"language":"en","content_type":"Work","owner":{"id":66921411,"first_name":"David","middle_initials":null,"last_name":"Mason","page_name":"DavidMason51","domain_name":"independent","created_at":"2017-08-02T02:46:31.327-07:00","display_name":"David Mason","url":"https://independent.academia.edu/DavidMason51"},"attachments":[],"research_interests":[{"id":56,"name":"Materials Engineering","url":"https://www.academia.edu/Documents/in/Materials_Engineering"},{"id":60,"name":"Mechanical Engineering","url":"https://www.academia.edu/Documents/in/Mechanical_Engineering"},{"id":15912,"name":"Electromagnetic Nondestructive Testing and Evaluation","url":"https://www.academia.edu/Documents/in/Electromagnetic_Nondestructive_Testing_and_Evaluation"},{"id":24815,"name":"Process Tomography","url":"https://www.academia.edu/Documents/in/Process_Tomography"},{"id":229390,"name":"Real Time","url":"https://www.academia.edu/Documents/in/Real_Time"},{"id":404000,"name":"Cross Section","url":"https://www.academia.edu/Documents/in/Cross_Section"},{"id":912885,"name":"Gamma Ray","url":"https://www.academia.edu/Documents/in/Gamma_Ray"},{"id":1195987,"name":"Laboratory Tests","url":"https://www.academia.edu/Documents/in/Laboratory_Tests"}],"urls":[]}, dispatcherData: dispatcherData }); 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href="https://www.academia.edu/34238872/The_influence_of_bends_on_the_performance_of_pneumatic_conveying_systems"><img alt="Research paper thumbnail of The influence of bends on the performance of pneumatic conveying systems" class="work-thumbnail" src="https://attachments.academia-assets.com/54152915/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34238872/The_influence_of_bends_on_the_performance_of_pneumatic_conveying_systems">The influence of bends on the performance of pneumatic conveying systems</a></div><div class="wp-workCard_item"><span>Advanced Powder Technology</span><span>, 1998</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="850ee29ebb3e683692d6ec2ac92544be" class="wp-workCard--action" 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$(this).data('initialized', true); } }); $a.trackClickSource(".js-work-strip-work-link", "profile_work_strip") }); </script> <div class="js-work-strip profile--work_container" data-work-id="34075885"><div class="profile--work_thumbnail hidden-xs"><a class="js-work-strip-work-link" data-click-track="profile-work-strip-thumbnail" href="https://www.academia.edu/34075885/Transient_heating_of_a_semitransparent_spherical_body"><img alt="Research paper thumbnail of Transient heating of a semitransparent spherical body" class="work-thumbnail" src="https://attachments.academia-assets.com/54010855/thumbnails/1.jpg" /></a></div><div class="wp-workCard wp-workCard_itemContainer"><div class="wp-workCard_item wp-workCard--title"><a class="js-work-strip-work-link text-gray-darker" data-click-track="profile-work-strip-title" href="https://www.academia.edu/34075885/Transient_heating_of_a_semitransparent_spherical_body">Transient heating of a semitransparent spherical body</a></div><div class="wp-workCard_item wp-workCard--coauthors"><span>by </span><span><a class="" data-click-track="profile-work-strip-authors" href="https://independent.academia.edu/SergeiSazhin">Sergei Sazhin</a> and <a class="" data-click-track="profile-work-strip-authors" href="https://independent.academia.edu/DavidMason51">David Mason</a></span></div><div class="wp-workCard_item"><span>International Journal of Thermal Sciences</span><span>, 2007</span></div><div class="wp-workCard_item wp-workCard--actions"><span class="work-strip-bookmark-button-container"></span><a id="3f4e790dc5d58a0e5c902b70026a761e" class="wp-workCard--action" rel="nofollow" data-click-track="profile-work-strip-download" data-download="{"attachment_id":54010855,"asset_id":34075885,"asset_type":"Work","button_location":"profile"}" href="https://www.academia.edu/attachments/54010855/download_file?st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&st=MTczMjY5Nzc3Myw4LjIyMi4yMDguMTQ2&s=profile"><span><i class="fa fa-arrow-down"></i></span><span>Download</span></a><span class="wp-workCard--action visible-if-viewed-by-owner inline-block" style="display: none;"><span class="js-profile-work-strip-edit-button-wrapper profile-work-strip-edit-button-wrapper" data-work-id="34075885"><a class="js-profile-work-strip-edit-button" tabindex="0"><span><i class="fa fa-pencil"></i></span><span>Edit</span></a></span></span><span id="work-strip-rankings-button-container"></span></div><div class="wp-workCard_item wp-workCard--stats"><span><span><span class="js-view-count view-count u-mr2x" data-work-id="34075885"><i class="fa fa-spinner fa-spin"></i></span><script>$(function () { var workId = 34075885; 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dispatcherData = { dispatcher: window.WowProfile.dispatcher, downloadLinkId: "3f4e790dc5d58a0e5c902b70026a761e" } } $('.js-work-strip[data-work-id=34075885]').each(function() { if (!$(this).data('initialized')) { new WowProfile.WorkStripView({ el: this, workJSON: {"id":34075885,"title":"Transient heating of a semitransparent spherical body","translated_title":"","metadata":{"grobid_abstract":"The problem of transient heating of a semitransparent spherical body immersed in a stationary hot gas is investigated, taking into account the effect of thermal radiation. The size of the domain occupied by the gas is assumed to be finite, and the outer boundary of this domain is kept at constant temperature. The initial radial distribution of temperature in the body is taken into account. A modification of Newton's law for body heating is introduced via a correction to either the gas temperature or convection heat transfer coefficient. Explicit expressions for these corrections are obtained for the case of homogeneous initial distribution of temperature and radiation absorption inside the body, and constant radiation temperature. For large Fourier numbers Fo, the correction to gas temperature is expected to be of limited practical importance, as both this correction and the difference between the initial gas temperature and the body surface temperature approach zero (heat transferred from gas to the body becomes negligible). The results are analysed using values of parameters relevant to diesel engines. The values of the corrections to the convection heat transfer coefficient vary from about 0.1 (large domain occupied by gas and Fo = 500) to 2.8 at Fo = 0.1. This means that ignoring these corrections is expected to lead to unacceptably large errors in computations. The total time for body heating is shown to be more than an order of magnitude longer when compared to the heating of this body in a perfectly stirred gas. The effect of thermal radiation on droplet heating is accounted for via the additional corrections of gas temperature or the convection heat transfer coefficient. 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