Wastewater Treatment Plant Synthesis and Design
The most used process for biological nitrogen removal from municipal and industrial wastewaters is the activated sludge process. Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strate...
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Veröffentlicht in: | Industrial & engineering chemistry research 2007-11, Vol.46 (23), p.7497-7512 |
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description | The most used process for biological nitrogen removal from municipal and industrial wastewaters is the activated sludge process. Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strategies or improving the individual plant design. However, the systematic optimization of the process structure (process synthesis) and operation conditions based on rigorous process models has not been presented in the literature. The objective of this work is to address the simultaneous optimization of the process configuration and equipment dimensionsi.e., process synthesis and designand the operation conditions of activated sludge wastewater treatment plants for nitrogen removal based on a superstructure model. The model embeds up to five reactors and a secondary settler, and allows flow distribution of the main process streams, i.e., nitrate and sludge recycle streams and fresh feed, along the reaction zone. The objective function is to minimize the net present value formed by investment and operating costs, while verifying compliance with the effluent permitted limits. The investment cost computes the reaction tanks, aeration systems, secondary settler, influent pumping station, and sludge pump costs. The operation cost computes the cost for pumping, aeration, dosage of an external carbon source, excess sludge treatment for disposal, and fines according to pollution units discharged. Influent wastewater flowrate and composition are assumed to be known. The activated sludge model no. 3 and the Takács model are selected to describe the biochemical processes and the secondary settler, respectively. This results in a highly nonlinear system with nonsmooth functions. Because of the problem complexity, in this first approach, a nonlinear programming (NLP) problem (specifically a nonlinear programming with discontinuous derivatives (DNLP) problem) is proposed and solved to obtain some insights for future models. It was implemented and solved using general algebraic modeling system (GAMS). Results for case studies are presented and discussed. |
doi_str_mv | 10.1021/ie0704905 |
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Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strategies or improving the individual plant design. However, the systematic optimization of the process structure (process synthesis) and operation conditions based on rigorous process models has not been presented in the literature. The objective of this work is to address the simultaneous optimization of the process configuration and equipment dimensionsi.e., process synthesis and designand the operation conditions of activated sludge wastewater treatment plants for nitrogen removal based on a superstructure model. The model embeds up to five reactors and a secondary settler, and allows flow distribution of the main process streams, i.e., nitrate and sludge recycle streams and fresh feed, along the reaction zone. The objective function is to minimize the net present value formed by investment and operating costs, while verifying compliance with the effluent permitted limits. The investment cost computes the reaction tanks, aeration systems, secondary settler, influent pumping station, and sludge pump costs. The operation cost computes the cost for pumping, aeration, dosage of an external carbon source, excess sludge treatment for disposal, and fines according to pollution units discharged. Influent wastewater flowrate and composition are assumed to be known. The activated sludge model no. 3 and the Takács model are selected to describe the biochemical processes and the secondary settler, respectively. This results in a highly nonlinear system with nonsmooth functions. Because of the problem complexity, in this first approach, a nonlinear programming (NLP) problem (specifically a nonlinear programming with discontinuous derivatives (DNLP) problem) is proposed and solved to obtain some insights for future models. It was implemented and solved using general algebraic modeling system (GAMS). 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Eng. Chem. Res</addtitle><description>The most used process for biological nitrogen removal from municipal and industrial wastewaters is the activated sludge process. Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strategies or improving the individual plant design. However, the systematic optimization of the process structure (process synthesis) and operation conditions based on rigorous process models has not been presented in the literature. The objective of this work is to address the simultaneous optimization of the process configuration and equipment dimensionsi.e., process synthesis and designand the operation conditions of activated sludge wastewater treatment plants for nitrogen removal based on a superstructure model. The model embeds up to five reactors and a secondary settler, and allows flow distribution of the main process streams, i.e., nitrate and sludge recycle streams and fresh feed, along the reaction zone. The objective function is to minimize the net present value formed by investment and operating costs, while verifying compliance with the effluent permitted limits. The investment cost computes the reaction tanks, aeration systems, secondary settler, influent pumping station, and sludge pump costs. The operation cost computes the cost for pumping, aeration, dosage of an external carbon source, excess sludge treatment for disposal, and fines according to pollution units discharged. Influent wastewater flowrate and composition are assumed to be known. The activated sludge model no. 3 and the Takács model are selected to describe the biochemical processes and the secondary settler, respectively. This results in a highly nonlinear system with nonsmooth functions. Because of the problem complexity, in this first approach, a nonlinear programming (NLP) problem (specifically a nonlinear programming with discontinuous derivatives (DNLP) problem) is proposed and solved to obtain some insights for future models. It was implemented and solved using general algebraic modeling system (GAMS). Results for case studies are presented and discussed.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>General purification processes</subject><subject>Pollution</subject><subject>Sewerage works: sewers, sewage treatment plants, outfalls</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><recordid>eNptkMFKAzEQhoMoWKsH32AvIh7WJtnMJjlqtSpULLSieAmzu4lu3W5rskX79q60tBcvmcB888_wEXLK6CWjnPVKSyUVmsIe6TDgNAYqYJ90qFIqBqXgkByFMKWUAgjRIb0XDI39xsb6aOItNjNbN9GowvYdr-rmw4YyRFgX0U37e6-PyYHDKtiTTe2S58HtpH8fD5_uHvpXwxgTnTZxmrpC69xmicgS4IUunLI0SbWmGSDXDhiXiCJjTrFcMss5t8idSjImhSuSLjlf5y78_GtpQ2NmZcht1R5m58tgJAgQGoC35MWazP08BG-dWfhyhn5lGDV_TszWScuebVIx5Fg5j3Veht2A5gwSplouXnNlK-dn20f_aVKZSDCT0dg8vkmQ168DM9zlYh7MdL70devmn_2_L9d6Ww</recordid><startdate>20071107</startdate><enddate>20071107</enddate><creator>Alasino, Noelia</creator><creator>Mussati, Miguel C</creator><creator>Scenna, Nicolás</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope></search><sort><creationdate>20071107</creationdate><title>Wastewater Treatment Plant Synthesis and Design</title><author>Alasino, Noelia ; Mussati, Miguel C ; Scenna, Nicolás</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a396t-66fd99ceb34b352d9df8e036990b5a29f5127aa4b1f81c71e222ea2f83b174fd3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>General purification processes</topic><topic>Pollution</topic><topic>Sewerage works: sewers, sewage treatment plants, outfalls</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Alasino, Noelia</creatorcontrib><creatorcontrib>Mussati, Miguel C</creatorcontrib><creatorcontrib>Scenna, Nicolás</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Alasino, Noelia</au><au>Mussati, Miguel C</au><au>Scenna, Nicolás</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Wastewater Treatment Plant Synthesis and Design</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2007-11-07</date><risdate>2007</risdate><volume>46</volume><issue>23</issue><spage>7497</spage><epage>7512</epage><pages>7497-7512</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>The most used process for biological nitrogen removal from municipal and industrial wastewaters is the activated sludge process. Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strategies or improving the individual plant design. However, the systematic optimization of the process structure (process synthesis) and operation conditions based on rigorous process models has not been presented in the literature. The objective of this work is to address the simultaneous optimization of the process configuration and equipment dimensionsi.e., process synthesis and designand the operation conditions of activated sludge wastewater treatment plants for nitrogen removal based on a superstructure model. The model embeds up to five reactors and a secondary settler, and allows flow distribution of the main process streams, i.e., nitrate and sludge recycle streams and fresh feed, along the reaction zone. The objective function is to minimize the net present value formed by investment and operating costs, while verifying compliance with the effluent permitted limits. The investment cost computes the reaction tanks, aeration systems, secondary settler, influent pumping station, and sludge pump costs. The operation cost computes the cost for pumping, aeration, dosage of an external carbon source, excess sludge treatment for disposal, and fines according to pollution units discharged. Influent wastewater flowrate and composition are assumed to be known. The activated sludge model no. 3 and the Takács model are selected to describe the biochemical processes and the secondary settler, respectively. This results in a highly nonlinear system with nonsmooth functions. Because of the problem complexity, in this first approach, a nonlinear programming (NLP) problem (specifically a nonlinear programming with discontinuous derivatives (DNLP) problem) is proposed and solved to obtain some insights for future models. It was implemented and solved using general algebraic modeling system (GAMS). Results for case studies are presented and discussed.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie0704905</doi><tpages>16</tpages></addata></record> |
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subjects | Applied sciences Chemical engineering Exact sciences and technology General purification processes Pollution Sewerage works: sewers, sewage treatment plants, outfalls Wastewaters Water treatment and pollution |
title | Wastewater Treatment Plant Synthesis and Design |
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