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A major application of these devices is in the flue gas desulfurization (FGD) of coal burning power plants. Before the exhaust gas is released to the atmosphere, liquid droplets entrained in the gas must be removed. A chevron mist eliminator relies on droplet inertia to cause the droplets to impinge on a surface where they are collected and drained away. The droplet removal efficiency is the critical design parameter of the mist eliminator. Pressure drop and flow capacity is also of major importance.<\/jats:p>\n               <jats:p>The droplet removal efficiency, pressure drop, and flow capacity have been investigated experimentally by several investigators. The experimental results were obtained using an air-water system of gas and fluid droplets.<\/jats:p>\n               <jats:p>This paper presents the results of a study using computational fluid dynamics to model the two-phase flow through the mist eliminator. Droplet removal efficiency and pressure drop were determined and compared with the experimental results. Three-stage chevron mist eliminator with 45\u00b0 angle to flow was modeled.<\/jats:p>\n               <jats:p>Comparison of the model results with previous experimental results indicated that the model is reasonably accurate. The model predicts pressure drop and the diameter at which 95% of droplets are removed with reasonably good accuracy. However, calculated droplet removal efficiencies of droplets with diameters less than 20\u03bcm did not agree well with experiments. The main advantage of the proposed model is that it can be used to predict droplet removal efficiencies for gas streams whose properties differ appreciably from that of an air-water system. Actual gas streams properties are input to the computational model. 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This situation not only affects the quality of natural gas, but also causes corrosion and damage to gas equipment, and even seriously affects normal production. In order to solve these problems, we have carried out an innovative design for its structure. Based on the single\u2010stage baffle, vortex blades are added at the first straight plate section from the inlet and the second straight plate section in the middle to enhance the turbulent vortex degree and complexity of the flow field in this area and improve the probability of collision of small particles with the wall, thus achieving the purpose of improving the demisting efficiency. In this paper, performance of the new mist eliminator is analyzed and evaluated by means of experimental study and computational fluid dynamics (CFD) numerical simulation. The results show that when the flow rate is 3.5\u20135.5\u00a0m\/s, total separation efficiency of the new mist eliminator for fine particles with a particle size of 5\u201325\u2009\u03bcm is about 51.72%\u201386.13%, which is about 38.57%\u201355.76% higher than ordinary baffled mist eliminator. The separation efficiency of particles with a diameter of 5\u00a0\u03bcm is about 31.79%, increased about 26.15%. The separation efficiency of particles with a diameter of 10\u00a0\u03bcm is about 52.09%, increased about 37.21%. In addition, when the flow rate is 3.5\u20135.5\u00a0m\/s, the pressure drop is increased by about 41.68\u2013135.97\u2009Pa. It could be concluded that the new type of mist eliminator could effectively improve the demisting efficiency of fine droplets.<\/jats:p>","DOI":"10.1002\/apj.2757","type":"journal-article","created":{"date-parts":[[2022,3,1]],"date-time":"2022-03-01T07:39:01Z","timestamp":1646120341000},"update-policy":"https:\/\/doi.org\/10.1002\/crossmark_policy","source":"Crossref","is-referenced-by-count":7,"title":["Study on the performance of a vortex mist eliminator for improving the separation efficiency of fine particles"],"prefix":"10.1002","volume":"17","author":[{"ORCID":"https:\/\/orcid.org\/0000-0003-0752-618X","authenticated-orcid":false,"given":"Huizhen","family":"Liang","sequence":"first","affiliation":[{"name":"College of Mechanical and Electronic Engineering Shandong University of Science and Technology  Qingdao 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In this system, wire mesh mist eliminator is one of the key components and used to separate waste water containing tritium, and remove moisture after reactor accident. Base on the ideal fluid model and packing pad model developing by Carpenter, A calculation model is presented for separation efficiency of mist eliminator. The calculation program \u201cSEP-WMME\u201d is developed based on the model. The calculation results fit well with experiment results. Theoretic analysis is carried out for the mist eliminator of HTR-PM helium purification system engineering validation test loop. The analysis shows the inlet velocity is an important parameter for mist eliminator. When the inlet velocity is above 3.0m\/s, high separation efficiency will be obtained.<\/jats:p>","DOI":"10.1115\/icone21-15417","type":"proceedings-article","created":{"date-parts":[[2014,2,7]],"date-time":"2014-02-07T15:32:41Z","timestamp":1391787161000},"update-policy":"https:\/\/doi.org\/10.1115\/crossmarkpolicy-asme","source":"Crossref","is-referenced-by-count":0,"title":["Theoretic Analysis on Separation Efficiency of Wire Mesh Mist Eliminator of High-Temperature Gas-Cooled Reactor Helium Purification and Auxiliary System"],"prefix":"10.1115","author":[{"given":"Huaqiang","family":"Yin","sequence":"first","affiliation":[{"name":"Tsinghua University, Beijing, China"}],"role":[{"role":"author","vocabulary":"crossref"}]},{"given":"Lei","family":"Hao","sequence":"additional","affiliation":[{"name":"Tsinghua University, Beijing, China"}],"role":[{"role":"author","vocabulary":"crossref"}]},{"given":"Xingtuan","family":"Yang","sequence":"additional","affiliation":[{"name":"Tsinghua University, Beijing, China"}],"role":[{"role":"author","vocabulary":"crossref"}]},{"given":"Xuedong","family":"He","sequence":"additional","affiliation":[{"name":"Tsinghua University, Beijing, China"}],"role":[{"role":"author","vocabulary":"crossref"}]}],"member":"33","published-online":{"date-parts":[[2014,2,7]]},"event":{"name":"2013 21st International Conference on Nuclear Engineering","start":{"date-parts":[[2013,7,29]]},"sponsor":["Nuclear Engineering Division"],"location":"Chengdu, China","end":{"date-parts":[[2013,8,2]]},"acronym":"ICONE21"},"container-title":["Volume 2: Plant Systems, Construction, Structures and Components; Next Generation Reactors and Advanced Reactors"],"link":[{"URL":"http:\/\/asmedigitalcollection.asme.org\/ICONE\/proceedings-pdf\/doi\/10.1115\/ICONE21-15417\/4250646\/v002t03a015-icone21-15417.pdf","content-type":"unspecified","content-version":"vor","intended-application":"similarity-checking"}],"deposited":{"date-parts":[[2019,9,1]],"date-time":"2019-09-01T07:21:42Z","timestamp":1567322502000},"score":22.70645,"resource":{"primary":{"URL":"https:\/\/asmedigitalcollection.asme.org\/ICONE\/proceedings\/ICONE21\/55799\/Chengdu,%20China\/247055"}},"issued":{"date-parts":[[2013,7,29]]},"references-count":0,"URL":"https:\/\/doi.org\/10.1115\/icone21-15417","published":{"date-parts":[[2013,7,29]]},"article-number":"V002T03A015"},{"indexed":{"date-parts":[[2025,10,26]],"date-time":"2025-10-26T18:52:12Z","timestamp":1761504732953,"version":"build-2065373602"},"publisher-location":"Research Triangle Park, NC","edition-number":"5","reference-count":1,"publisher":"International Union of Pure and Applied Chemistry (IUPAC)","license":[{"start":{"date-parts":[[2025,10,26]],"date-time":"2025-10-26T00:00:00Z","timestamp":1761436800000},"content-version":"vor","delay-in-days":0,"URL":"https:\/\/creativecommons.org\/licenses\/by-sa\/4.0\/"}],"content-domain":{"domain":[],"crossmark-restriction":false},"published-print":{"date-parts":[[2025,10,26]]},"abstract":"<jats:p>Citation: 'eliminator' in the IUPAC Compendium of Chemical Terminology, 5th ed.; International Union of Pure and Applied Chemistry; 2025. Online version 5.0.0, 2025. 10.1351\/goldbook.15657 \u2022 License: The IUPAC Gold Book is licensed under Creative Commons Attribution-ShareAlike CC BY-SA 4.0 International for individual terms. Requests for commercial usage of the compendium should be directed to IUPAC.<\/jats:p>","DOI":"10.1351\/goldbook.15657","type":"book-section","created":{"date-parts":[[2025,1,2]],"date-time":"2025-01-02T16:58:49Z","timestamp":1735837129000},"source":"Crossref","is-referenced-by-count":0,"title":["eliminator"],"prefix":"10.1351","member":"113","reference":[{"key":"ref1","doi-asserted-by":"publisher","unstructured":"'Glossary of terms used in toxicology, 2nd edition (IUPAC Recommendations 2007)' Pure and Applied Chemistry, 2007, 79, 1153","DOI":"10.1351\/pac200779071153"}],"container-title":["The IUPAC Compendium of Chemical Terminology"],"language":"en","deposited":{"date-parts":[[2025,10,26]],"date-time":"2025-10-26T18:45:34Z","timestamp":1761504334000},"score":22.232578,"resource":{"primary":{"URL":"https:\/\/goldbook.iupac.org\/terms\/view\/15657"}},"issued":{"date-parts":[[2025,10,26]]},"references-count":1,"URL":"https:\/\/doi.org\/10.1351\/goldbook.15657","published":{"date-parts":[[2025,10,26]]}},{"indexed":{"date-parts":[[2023,4,6]],"date-time":"2023-04-06T10:13:34Z","timestamp":1680776014873},"reference-count":0,"publisher":"American Chemical Society (ACS)","issue":"9","content-domain":{"domain":[],"crossmark-restriction":false},"short-container-title":["Chem. 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A simplification method is used during the simulation process to solve the difficulty of model building during the simulation of the mist pad. A two-dimensional model is employed to acquire the resistance of mesh pad with different layer spacing. The flow field is calculated using 2D Reynolds-averaged Navier-Stokes equations.   turbulence model is used to simulate the Reynold stress. And pressure drop of wire mesh mist eliminator is expressed as a function of broad ranges of inlet velocity. After CFD simulation, model experiment study is carried on using a small scale wind-tunnel. 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This is a requirement specified in many process applications especially in gas treatment prior to atmospheric dispersion. In this paper a model is proposed, based on determining the trajectory of droplets through a knitted mesh mist eliminator, from which both the outlet gas concentration and drop size distribution in this gas stream can be specified. The model predicts the expected variations in performance, a decrease in the separation efficiency with decreasing both drop size in the feed mixture and gas velocity. A limiting velocity is predicted at which the drainage of liquid from the pad decreases. This corresponds to the flooding condition. Quantitative predictions of this limiting velocity compare well with the experimental results measured for air-water systems. The model offers the prospect of optimising the pad construction to maximise the separation efficiency at a target pressure drop or designing to a maximum pressure drop. For all designs, the conditions of the outlet gas steam can be defined.<\/jats:p>\n                  <jats:sec>\n                     <jats:title>Introduction<\/jats:title>\n                     <jats:p>The separation of liquid droplets from gases and vapours is a process common to many chemical engineering operations in both the production and processing of petroleum. Distillation, partial condensation of vapours, gas scrubbing and gas compression are all process where the entrainment of liquid drops in the fluid stream must be minimised. A range of separation devices are available for this duty, the selection is largely dependent on the quantity of liquid per unit volume of gas and the drop size distribution of the liquid dispersion. For relatively coarse dispersions in which mean drop,, is between 500-1000 m simple gravity settling drums are used. In gas-liquid systems the difference in the density between the two phases is usually high, typically from 400-1000 kg. m-3 the viscosity of gas phase is by contrast relatively low so that the settling velocity of drops in this range is high, Under these conditions adequate separation can normally be achieved in a simple drum providing that there is sufficient residence time of the gas in the drum. As the drop size of the dispersed phase is reduced, as for example is observed in the exhaust from gas scrubbers then gravity settling is no longer effective. Then some form of interceptor must be introduced in which a surface, as a baffle blade or louvre plate, is introduced into the gas stream and onto which the droplets are captured or retained and can then coalesce until such a time as they can settle out under gravity from the gas phase. Their effective range extends down to drop diameters of approximately 20 m. As the drop size decreases further then the dimensions of the capture surfaces must decrease if effective separation is to be achieved. Thus, for dispersions containing droplets down to approximately 2 m diameter, knitted mesh mist eliminators are used. Here the filaments making up the capture surfaces are normally in the range 0.15-0.4mm diameter (compared with vanes typically 30 \u00d7 3 mm in section).<\/jats:p>\n                     <jats:p>For sub micron droplets fibre bed 'coalescers' are used in which the fibre diameters are in the range 3-0.5 m. As one progresses from gravity separators to fibre coalescers, the superficial gas velocities decrease from around 10 ms-1 to 0.05 ms-1 (depending on the process conditions T, etc.) whilst the pressure differential across the separators will increase from 100 Pa to 1.5 \u00d7 104 Pa. Therefore, it is clear that the cross section of separators normal to the flow and the power costs increase substantially as the dispersion drop size decreases. It is therefore essential to have reliable and accurate design procedures for equipment particularly when dealing with fine dispersion.<\/jats:p>\n                     <jats:p>P. 735<\/jats:p>\n                  <\/jats:sec>\n               <\/jats:sec>","DOI":"10.2118\/36649-ms","type":"proceedings-article","created":{"date-parts":[[2007,12,20]],"date-time":"2007-12-20T22:53:23Z","timestamp":1198191203000},"source":"Crossref","is-referenced-by-count":0,"title":["A Stochastic Model To Describe The Design And Operation Of Knitted Mesh Mist Eliminator"],"prefix":"10.2118","author":[{"given":"S.E.","family":"Wilcock","sequence":"additional","affiliation":[{"name":"UMIST"}],"role":[{"role":"author","vocabulary":"crossref"}]},{"given":"G.A.","family":"Davies","sequence":"additional","affiliation":[{"name":"UMIST"}],"role":[{"role":"author","vocabulary":"crossref"}]}],"member":"861","published-online":{"date-parts":[[1996,10,6]]},"event":{"name":"SPE Annual Technical Conference and 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