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Effective treatment of emulsified oil wastewater by the coagulation–flotation process

Ship emulsified oil wastewater was used as the research object in this study. The highly efficient coagulant demulsification degreasing mechanism and microbubble flotation technology were combined and the effects of coagulant type and dosage amount on the demulsification of emulsified oil wastewater...

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Autores principales: You, Zhaoyang, Xu, Haiyang, Sun, Yongjun, Zhang, Shujuan, Zhang, Li
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9091706/
https://www.ncbi.nlm.nih.gov/pubmed/35557887
http://dx.doi.org/10.1039/c8ra06565a
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author You, Zhaoyang
Xu, Haiyang
Sun, Yongjun
Zhang, Shujuan
Zhang, Li
author_facet You, Zhaoyang
Xu, Haiyang
Sun, Yongjun
Zhang, Shujuan
Zhang, Li
author_sort You, Zhaoyang
collection PubMed
description Ship emulsified oil wastewater was used as the research object in this study. The highly efficient coagulant demulsification degreasing mechanism and microbubble flotation technology were combined and the effects of coagulant type and dosage amount on the demulsification of emulsified oil wastewater were evaluated. The influence of the mixed coagulation effect of pH values, temperature, and hydraulic condition parameters were determined and water intake, air intake, and oil content were regulated. The coagulant for the demulsification of emulsified oil wastewater was screened; the dosage was 500 mg L(−1), and the removal capacity of the coagulant was in the following order: polyaluminum ferric chloride (PAFC) > polyaluminum chloride (PAC) > polysilicate aluminum ferric sulfate (PSAFS) > alum > Al(2)(SO(4))(3) > polyferric sulfate > FeCl(3). Polyacrylamide (PAM) with added water was used to further reduce the oil content. The PAFC, PAC, and PSAFS were selected as coagulation–air flotation dynamic test alternative agents. The investment quantities of PAFC, PSAFS and PAM were 300 mg L(−1), 300 mg L(−1) and 30 mg L(−1), respectively. The stirring time was 5 min, the pH value was 6.5–6.9, the flow rate was 0.25 m(3) h(−1), the oil content of the emulsified oil wastewater was 3000–5000 mg L(−1) and the effluent oil was stable below 15 ppm. The microbubble generation device using air flotation effluent was used in the two air flotation treatments to enhance the device efficiency. The air flotation device adopted the structural design of the upper part of the water inlet and the lower part of the micro-air bubble, which can increase the collision probability of the microbubble and improve the efficiency of oil removal.
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spelling pubmed-90917062022-05-11 Effective treatment of emulsified oil wastewater by the coagulation–flotation process You, Zhaoyang Xu, Haiyang Sun, Yongjun Zhang, Shujuan Zhang, Li RSC Adv Chemistry Ship emulsified oil wastewater was used as the research object in this study. The highly efficient coagulant demulsification degreasing mechanism and microbubble flotation technology were combined and the effects of coagulant type and dosage amount on the demulsification of emulsified oil wastewater were evaluated. The influence of the mixed coagulation effect of pH values, temperature, and hydraulic condition parameters were determined and water intake, air intake, and oil content were regulated. The coagulant for the demulsification of emulsified oil wastewater was screened; the dosage was 500 mg L(−1), and the removal capacity of the coagulant was in the following order: polyaluminum ferric chloride (PAFC) > polyaluminum chloride (PAC) > polysilicate aluminum ferric sulfate (PSAFS) > alum > Al(2)(SO(4))(3) > polyferric sulfate > FeCl(3). Polyacrylamide (PAM) with added water was used to further reduce the oil content. The PAFC, PAC, and PSAFS were selected as coagulation–air flotation dynamic test alternative agents. The investment quantities of PAFC, PSAFS and PAM were 300 mg L(−1), 300 mg L(−1) and 30 mg L(−1), respectively. The stirring time was 5 min, the pH value was 6.5–6.9, the flow rate was 0.25 m(3) h(−1), the oil content of the emulsified oil wastewater was 3000–5000 mg L(−1) and the effluent oil was stable below 15 ppm. The microbubble generation device using air flotation effluent was used in the two air flotation treatments to enhance the device efficiency. The air flotation device adopted the structural design of the upper part of the water inlet and the lower part of the micro-air bubble, which can increase the collision probability of the microbubble and improve the efficiency of oil removal. The Royal Society of Chemistry 2018-12-05 /pmc/articles/PMC9091706/ /pubmed/35557887 http://dx.doi.org/10.1039/c8ra06565a Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
You, Zhaoyang
Xu, Haiyang
Sun, Yongjun
Zhang, Shujuan
Zhang, Li
Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title_full Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title_fullStr Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title_full_unstemmed Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title_short Effective treatment of emulsified oil wastewater by the coagulation–flotation process
title_sort effective treatment of emulsified oil wastewater by the coagulation–flotation process
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9091706/
https://www.ncbi.nlm.nih.gov/pubmed/35557887
http://dx.doi.org/10.1039/c8ra06565a
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