{"id":31,"date":"2018-09-16T14:13:09","date_gmt":"2018-09-16T21:13:09","guid":{"rendered":"https:\/\/blogs.ubc.ca\/mzare\/?page_id=31"},"modified":"2022-06-28T20:05:27","modified_gmt":"2022-06-29T03:05:27","slug":"research","status":"publish","type":"page","link":"https:\/\/blogs.ubc.ca\/mzare\/research\/","title":{"rendered":"Research"},"content":{"rendered":"<p style=\"text-align: center;\"><em><strong>Mechanics and rheology of complex fluids<\/strong><\/em><\/p>\n<p>My research interests lie in fluid mechanics, with a focus on experimental studies of complex fluids in particular viscoplastic fluids (VPFs). A significant number of fluids that are categorized as VPFs: used in our daily life such as toothpaste, hand sanitizers, and peanut butter; in geophysical and industrial settings, such as magma, cement slurry, tailing fluids, and drilling mud. Studying the flow of complex fluids and non-colloidal suspensions have been the focus of my doctoral and current research activities.<\/p>\n<p>As the manager of the complex fluids lab at UBC, I also organize training sessions and advise students in performing rheological tests and using rheo-imaging and rheo-scattering techniques.<\/p>\n<p>My research studies are described as follows:<\/p>\n<p><em><em>(I) Mechanics of bubbles rise in complex fluids. <\/em><\/em><\/p>\n<p>The focus of this part of my research is on restoring polluted lakes. It is in collaboration\u00a0with Professor Greg Lawrence at the Department of Civil Engineering, UBC.<\/p>\n<p><img loading=\"lazy\" decoding=\"async\" class=\"size-medium wp-image-460 aligncenter\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-300x233.png\" alt=\"\" width=\"300\" height=\"233\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-300x233.png 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-1024x795.png 1024w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-768x597.png 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-1536x1193.png 1536w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4-624x485.png 624w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Fig4.png 1770w\" sizes=\"auto, (max-width: 300px) 100vw, 300px\" \/><\/p>\n<p>Spatiotemporal images of first bubble propagation through three layers of Densified Carbopol (DC), glycerol, and Carbopol. Pure glycerol is used in cases (a)-(e). Glycerol concentration in case (f) is 80%. The concentration of Carbopol solutions used in DC and C layers are: a) DC=0.15%, C=0.06%; b) DC=0.15%, C=0.1%; c) DC=0.15%, C=0.2%; d) DC=0.18%, C=0.15%; e) DC=0.18%, C=0.1%; f) DC=0.15%, C=0.1%. As DC concentration increases, bubbles tend to have a larger volume. As glycerol concentration decreases, bubbles tend to have a less spherical shape. The DC layer in case (e) was dyed to investigate whether bubbles entrain the DC fluid into the glycerol layer.<\/p>\n<p><img loading=\"lazy\" decoding=\"async\" class=\"alignnone wp-image-459\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001-300x105.jpeg\" alt=\"\" width=\"477\" height=\"167\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001-300x105.jpeg 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001-1024x358.jpeg 1024w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001-768x269.jpeg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001-624x218.jpeg 624w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/twitter.001.jpeg 1100w\" sizes=\"auto, (max-width: 477px) 100vw, 477px\" \/><img loading=\"lazy\" decoding=\"async\" class=\"alignnone wp-image-463\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-268x300.jpg\" alt=\"\" width=\"148\" height=\"165\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-268x300.jpg 268w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-916x1024.jpg 916w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-768x859.jpg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-1374x1536.jpg 1374w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-1832x2048.jpg 1832w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp-624x698.jpg 624w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/OffsetExp.jpg 1909w\" sizes=\"auto, (max-width: 148px) 100vw, 148px\" \/><\/p>\n<p class=\"p1\">The flow and trajectory of a rising bubble initially positioned within a yield stress fluid at a horizontal distance\u00a0to a Newtonian layer. The panel on the left shows the numerical results and the experimental results are shown in the panel on the right.<\/p>\n<p><img loading=\"lazy\" decoding=\"async\" class=\"alignnone wp-image-465\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled.001-300x179.jpeg\" alt=\"\" width=\"349\" height=\"208\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled.001-300x179.jpeg 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled.001-768x457.jpeg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled.001-624x372.jpeg 624w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled.001.jpeg 900w\" sizes=\"auto, (max-width: 349px) 100vw, 349px\" \/><img loading=\"lazy\" decoding=\"async\" class=\"alignnone wp-image-462\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-300x269.jpg\" alt=\"\" width=\"231\" height=\"207\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-300x269.jpg 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-1024x918.jpg 1024w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-768x689.jpg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-1536x1377.jpg 1536w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-2048x1837.jpg 2048w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/03\/Angled_EXP-624x560.jpg 624w\" sizes=\"auto, (max-width: 231px) 100vw, 231px\" \/><\/p>\n<p class=\"p1\">The flow and trajectory of a bubble rising bubble in a viscous layer crossing a yield stress fluid at <span class=\"Apple-converted-space\">\u00a0 $\\theta$<\/span>= 72.5 . The panel on the left shows the numerical results and the experimental results are shown in the panel on the right.<\/p>\n<p><em>(II) Multi-layer flows with yield stress fluids,\u00a0<\/em><\/p>\n<p>Evaluating the interface position and the shape of the interface between the fluids by solving the nonlinear wave equation obtained from the lubrication model:<\/p>\n<div id=\"attachment_457\" style=\"width: 2570px\" class=\"wp-caption alignnone\"><img loading=\"lazy\" decoding=\"async\" aria-describedby=\"caption-attachment-457\" class=\"wp-image-457 size-full\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-scaled.jpg\" alt=\"\" width=\"2560\" height=\"811\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-scaled.jpg 2560w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-300x95.jpg 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-1024x324.jpg 1024w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-768x243.jpg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-1536x486.jpg 1536w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-2048x649.jpg 2048w, https:\/\/blogs.ubc.ca\/mzare\/files\/2021\/02\/Lubrication-1-624x198.jpg 624w\" sizes=\"auto, (max-width: 2560px) 100vw, 2560px\" \/><p id=\"caption-attachment-457\" class=\"wp-caption-text\">Interface propagation obtained from two-layer model: (a) Frontal shock; (b) contact shock (spike). M. Zare, et al., J. non-Newton. Fluid Mech, (2017), https:\/\/doi.org\/10.1016\/j.jnnfm.2017.06.002.<\/p><\/div>\n<p>Computational results obtained for the density unstable displacement of a yield stress fluid from a channel:<\/p>\n<div id=\"attachment_391\" style=\"width: 7885px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" aria-describedby=\"caption-attachment-391\" class=\"wp-image-391 size-full\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3.jpg\" alt=\"\" width=\"7875\" height=\"3937\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3.jpg 7875w, https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3-300x150.jpg 300w, https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3-768x384.jpg 768w, https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3-1024x512.jpg 1024w, https:\/\/blogs.ubc.ca\/mzare\/files\/2019\/11\/B1m3-1200x600.jpg 1200w\" sizes=\"auto, (max-width: 7875px) 100vw, 7875px\" \/><p id=\"caption-attachment-391\" class=\"wp-caption-text\">Panorama of flow types observed for Bingham (B)=1, and viscosity ratio (m)=3. Markers indicate data position in (Re, Re\/Fr^2) plane with symbols indicating the corresponding flow regime [M. Zare, and I.A. Frigaard. J. non-Newton. Fluid Mech, (2018) https:\/\/doi.org\/10.1016\/j.jnnfm.2018.07.007].<\/p><\/div>\n<p><em>(III) Onset of invasion of viscous fluids to a yield stress fluid column and their propagation through the gelled column,\u00a0<\/em><\/p>\n<p>&nbsp;<\/p>\n<div id=\"attachment_173\" style=\"width: 454px\" class=\"wp-caption aligncenter\"><img loading=\"lazy\" decoding=\"async\" aria-describedby=\"caption-attachment-173\" class=\"wp-image-173 size-full\" src=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2018\/12\/Presentation1.jpg\" alt=\"\" width=\"444\" height=\"387\" srcset=\"https:\/\/blogs.ubc.ca\/mzare\/files\/2018\/12\/Presentation1.jpg 444w, https:\/\/blogs.ubc.ca\/mzare\/files\/2018\/12\/Presentation1-300x261.jpg 300w\" sizes=\"auto, (max-width: 444px) 100vw, 444px\" \/><p id=\"caption-attachment-173\" class=\"wp-caption-text\">This figure shows the invasion process of air, rhodorsil oil, glycein, and water respectively from top to bottom to our model yield stress fluid, i.e carbopol [M. Zare, I. A. Frigaard, Phys. Fluids, https:\/\/doi.org\/10.1063\/1.5024718].<\/p><\/div>\n<p>&nbsp;<\/p>\n<p>&nbsp;<\/p>\n","protected":false},"excerpt":{"rendered":"<p>Mechanics and rheology of complex fluids My research interests lie in fluid mechanics, with a focus on experimental studies of complex fluids in particular viscoplastic fluids (VPFs). A significant number of fluids that are categorized as VPFs: used in our daily life such as toothpaste, hand sanitizers, and peanut butter; in geophysical and industrial settings, [&hellip;]<\/p>\n","protected":false},"author":54983,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":{"footnotes":""},"class_list":["post-31","page","type-page","status-publish","hentry"],"_links":{"self":[{"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/pages\/31","targetHints":{"allow":["GET"]}}],"collection":[{"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/pages"}],"about":[{"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/types\/page"}],"author":[{"embeddable":true,"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/users\/54983"}],"replies":[{"embeddable":true,"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/comments?post=31"}],"version-history":[{"count":47,"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/pages\/31\/revisions"}],"predecessor-version":[{"id":488,"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/pages\/31\/revisions\/488"}],"wp:attachment":[{"href":"https:\/\/blogs.ubc.ca\/mzare\/wp-json\/wp\/v2\/media?parent=31"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}