Evaporation experiment and numerical simulation study of desulfurization wastewater in high-temperature raw gas

[Display omitted] •Optimization parameters of wastewater evaporation were obtained by CFD simulation.•An improved evaporation model of solution at high temperature was established.•The influence of gas flow on droplets dispersion was found.•The relationship between temperature and evaporation heat c...

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Veröffentlicht in:Chemical engineering research & design 2019-06, Vol.146, p.117-129
Hauptverfasser: Li, Chao, Deng, Tong, Wen, Zengguang, Tian, Taiqing, Li, Guoqiang, Zhang, Yongfa, Li, Zhenhua
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container_start_page 117
container_title Chemical engineering research & design
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creator Li, Chao
Deng, Tong
Wen, Zengguang
Tian, Taiqing
Li, Guoqiang
Zhang, Yongfa
Li, Zhenhua
description [Display omitted] •Optimization parameters of wastewater evaporation were obtained by CFD simulation.•An improved evaporation model of solution at high temperature was established.•The influence of gas flow on droplets dispersion was found.•The relationship between temperature and evaporation heat consumption was obtained.•The optimized injection system solved such problems as accumulated tar. This study adopts Fluent software to perform a numerical simulation on the evaporation of desulfurization wastewater, which is based on the experimental study of spraying desulfurization wastewater to the high-temperature raw gas (around 750 °C) inside the single riser of industrial coke oven. Regarding to the results, a further optimization was applied to the core-part nozzle structures of spraying wastewater in the experimental plant. The results indicated that the farthest distance of the droplets movement calculated by the modified formula We = f(T) was 0.051 m at 800 °C, which is more consistent with the experiment. When the flow rate of raw gas was increased from 0 m3/h to 700 m3/h, the dispersion degree of droplet particle trajectory was enlarged from range −0.181−0.174 m to −0.308−0.246 m on the x-axis, and the time that the droplet particles reached the gas flow rate accelerated from 0.007 s to 0.02 s. The relationship between the riser’s average temperatures before and after spraying desulfurization wastewater was T = 568.49In(T0) − 3151.9. It was consistent with the actual value. Within the coking time of 20 h, the average temperature of the riser after evaporation was 620.44 °C and the average evaporation time was 0.0025 s, when the desulfurization wastewater was sprayed at 3 m away from the water seal of the riser. The optimized injection system according to the simulation results has improved the treatment effect of the wastewater in the experimental plant.
doi_str_mv 10.1016/j.cherd.2019.03.043
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This study adopts Fluent software to perform a numerical simulation on the evaporation of desulfurization wastewater, which is based on the experimental study of spraying desulfurization wastewater to the high-temperature raw gas (around 750 °C) inside the single riser of industrial coke oven. Regarding to the results, a further optimization was applied to the core-part nozzle structures of spraying wastewater in the experimental plant. The results indicated that the farthest distance of the droplets movement calculated by the modified formula We = f(T) was 0.051 m at 800 °C, which is more consistent with the experiment. When the flow rate of raw gas was increased from 0 m3/h to 700 m3/h, the dispersion degree of droplet particle trajectory was enlarged from range −0.181−0.174 m to −0.308−0.246 m on the x-axis, and the time that the droplet particles reached the gas flow rate accelerated from 0.007 s to 0.02 s. The relationship between the riser’s average temperatures before and after spraying desulfurization wastewater was T = 568.49In(T0) − 3151.9. It was consistent with the actual value. Within the coking time of 20 h, the average temperature of the riser after evaporation was 620.44 °C and the average evaporation time was 0.0025 s, when the desulfurization wastewater was sprayed at 3 m away from the water seal of the riser. The optimized injection system according to the simulation results has improved the treatment effect of the wastewater in the experimental plant.</description><identifier>ISSN: 0263-8762</identifier><identifier>EISSN: 1744-3563</identifier><identifier>DOI: 10.1016/j.cherd.2019.03.043</identifier><language>eng</language><publisher>Rugby: Elsevier B.V</publisher><subject>CFD ; Coke ovens ; Coke-oven raw gas of high temperate in riser ; Coking ; Computer simulation ; Desulfurized wastewater ; Desulfurizing ; Droplets ; Evaporation ; Flow velocity ; Gas flow ; High temperature ; Nozzles ; Numerical simulation ; Optimization ; Particle trajectories ; Simulation ; Software ; Spray evaporation ; Spraying ; Wastewater</subject><ispartof>Chemical engineering research &amp; design, 2019-06, Vol.146, p.117-129</ispartof><rights>2019 Institution of Chemical Engineers</rights><rights>Copyright Elsevier Science Ltd. 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This study adopts Fluent software to perform a numerical simulation on the evaporation of desulfurization wastewater, which is based on the experimental study of spraying desulfurization wastewater to the high-temperature raw gas (around 750 °C) inside the single riser of industrial coke oven. Regarding to the results, a further optimization was applied to the core-part nozzle structures of spraying wastewater in the experimental plant. The results indicated that the farthest distance of the droplets movement calculated by the modified formula We = f(T) was 0.051 m at 800 °C, which is more consistent with the experiment. When the flow rate of raw gas was increased from 0 m3/h to 700 m3/h, the dispersion degree of droplet particle trajectory was enlarged from range −0.181−0.174 m to −0.308−0.246 m on the x-axis, and the time that the droplet particles reached the gas flow rate accelerated from 0.007 s to 0.02 s. The relationship between the riser’s average temperatures before and after spraying desulfurization wastewater was T = 568.49In(T0) − 3151.9. It was consistent with the actual value. Within the coking time of 20 h, the average temperature of the riser after evaporation was 620.44 °C and the average evaporation time was 0.0025 s, when the desulfurization wastewater was sprayed at 3 m away from the water seal of the riser. The optimized injection system according to the simulation results has improved the treatment effect of the wastewater in the experimental plant.</description><subject>CFD</subject><subject>Coke ovens</subject><subject>Coke-oven raw gas of high temperate in riser</subject><subject>Coking</subject><subject>Computer simulation</subject><subject>Desulfurized wastewater</subject><subject>Desulfurizing</subject><subject>Droplets</subject><subject>Evaporation</subject><subject>Flow velocity</subject><subject>Gas flow</subject><subject>High temperature</subject><subject>Nozzles</subject><subject>Numerical simulation</subject><subject>Optimization</subject><subject>Particle trajectories</subject><subject>Simulation</subject><subject>Software</subject><subject>Spray evaporation</subject><subject>Spraying</subject><subject>Wastewater</subject><issn>0263-8762</issn><issn>1744-3563</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9kEtPwzAQhC0EEqXwC7hY4pywjvOwDxxQxUuqxAXOlmtvWldtUmyHUn49LuHMabXamVnNR8g1g5wBq2_XuVmht3kBTObAcyj5CZmwpiwzXtX8lEygqHkmmro4JxchrAEgXcWE9A-fetd7HV3fUfzaoXdb7CLVnaXdsE2r0Rsa3HbYjJoQB3ugfUsthmHTDt59j4e9DhH3OqKnrqMrt1xlEbcpUMfBI_V6T5c6XJKzVm8CXv3NKXl_fHibPWfz16eX2f08M7wWMeOirUDKypasaFshy1oWldAWeFGZheFWVry2i6Y0kgngQhvOdKslNJWRNRo-JTdj7s73HwOGqNb94Lv0UhVFxRqAUoik4qPK-D4Ej63apf7aHxQDdSSr1uqXrDqSVcBVIptcd6MLU4FPh14F47AzaJ1HE5Xt3b_-H89QhQI</recordid><startdate>20190601</startdate><enddate>20190601</enddate><creator>Li, Chao</creator><creator>Deng, Tong</creator><creator>Wen, Zengguang</creator><creator>Tian, Taiqing</creator><creator>Li, Guoqiang</creator><creator>Zhang, Yongfa</creator><creator>Li, Zhenhua</creator><general>Elsevier B.V</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope><orcidid>https://orcid.org/0000-0002-4185-7030</orcidid><orcidid>https://orcid.org/0000-0003-1539-9854</orcidid></search><sort><creationdate>20190601</creationdate><title>Evaporation experiment and numerical simulation study of desulfurization wastewater in high-temperature raw gas</title><author>Li, Chao ; Deng, Tong ; Wen, Zengguang ; Tian, Taiqing ; Li, Guoqiang ; Zhang, Yongfa ; Li, Zhenhua</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c368t-38f50995d412ff89469258ad0325cbc3d9536db74c918038ac31afa9075c96ec3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>CFD</topic><topic>Coke ovens</topic><topic>Coke-oven raw gas of high temperate in riser</topic><topic>Coking</topic><topic>Computer simulation</topic><topic>Desulfurized wastewater</topic><topic>Desulfurizing</topic><topic>Droplets</topic><topic>Evaporation</topic><topic>Flow velocity</topic><topic>Gas flow</topic><topic>High temperature</topic><topic>Nozzles</topic><topic>Numerical simulation</topic><topic>Optimization</topic><topic>Particle trajectories</topic><topic>Simulation</topic><topic>Software</topic><topic>Spray evaporation</topic><topic>Spraying</topic><topic>Wastewater</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Li, Chao</creatorcontrib><creatorcontrib>Deng, Tong</creatorcontrib><creatorcontrib>Wen, Zengguang</creatorcontrib><creatorcontrib>Tian, Taiqing</creatorcontrib><creatorcontrib>Li, Guoqiang</creatorcontrib><creatorcontrib>Zhang, Yongfa</creatorcontrib><creatorcontrib>Li, Zhenhua</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Chemical engineering research &amp; design</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Li, Chao</au><au>Deng, Tong</au><au>Wen, Zengguang</au><au>Tian, Taiqing</au><au>Li, Guoqiang</au><au>Zhang, Yongfa</au><au>Li, Zhenhua</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaporation experiment and numerical simulation study of desulfurization wastewater in high-temperature raw gas</atitle><jtitle>Chemical engineering research &amp; design</jtitle><date>2019-06-01</date><risdate>2019</risdate><volume>146</volume><spage>117</spage><epage>129</epage><pages>117-129</pages><issn>0263-8762</issn><eissn>1744-3563</eissn><abstract>[Display omitted] •Optimization parameters of wastewater evaporation were obtained by CFD simulation.•An improved evaporation model of solution at high temperature was established.•The influence of gas flow on droplets dispersion was found.•The relationship between temperature and evaporation heat consumption was obtained.•The optimized injection system solved such problems as accumulated tar. This study adopts Fluent software to perform a numerical simulation on the evaporation of desulfurization wastewater, which is based on the experimental study of spraying desulfurization wastewater to the high-temperature raw gas (around 750 °C) inside the single riser of industrial coke oven. Regarding to the results, a further optimization was applied to the core-part nozzle structures of spraying wastewater in the experimental plant. The results indicated that the farthest distance of the droplets movement calculated by the modified formula We = f(T) was 0.051 m at 800 °C, which is more consistent with the experiment. When the flow rate of raw gas was increased from 0 m3/h to 700 m3/h, the dispersion degree of droplet particle trajectory was enlarged from range −0.181−0.174 m to −0.308−0.246 m on the x-axis, and the time that the droplet particles reached the gas flow rate accelerated from 0.007 s to 0.02 s. The relationship between the riser’s average temperatures before and after spraying desulfurization wastewater was T = 568.49In(T0) − 3151.9. It was consistent with the actual value. Within the coking time of 20 h, the average temperature of the riser after evaporation was 620.44 °C and the average evaporation time was 0.0025 s, when the desulfurization wastewater was sprayed at 3 m away from the water seal of the riser. The optimized injection system according to the simulation results has improved the treatment effect of the wastewater in the experimental plant.</abstract><cop>Rugby</cop><pub>Elsevier B.V</pub><doi>10.1016/j.cherd.2019.03.043</doi><tpages>13</tpages><orcidid>https://orcid.org/0000-0002-4185-7030</orcidid><orcidid>https://orcid.org/0000-0003-1539-9854</orcidid></addata></record>
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subjects CFD
Coke ovens
Coke-oven raw gas of high temperate in riser
Coking
Computer simulation
Desulfurized wastewater
Desulfurizing
Droplets
Evaporation
Flow velocity
Gas flow
High temperature
Nozzles
Numerical simulation
Optimization
Particle trajectories
Simulation
Software
Spray evaporation
Spraying
Wastewater
title Evaporation experiment and numerical simulation study of desulfurization wastewater in high-temperature raw gas
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