On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation

Rafiqul Gani, Deenesh Kavi Babi

Research output: Chapter in Book/Report/Conference proceedingConference abstract in proceedingsResearchpeer-review

Abstract

Solvents (mass separating agents) play an important role in separation-based processes. For example, consider the separation of an azeotropic mixture. If the azeotrope is not pressure dependent, then a feasible separation technique that can be employed for separation of the azeotrope is usually extractive distillation. In extractive distillation the solvent affects the relative volatility of the two key compounds to be separated. In other words, for a two column distillation sequence configuration, the lighter boiling compound is obtained as the top product of the first distillation column and the heavier boiling compound is obtained as the top product of the second distillation column where the solvent is recovered (for re-use and recycle).
Therefore, the solvent design problem can be defined as follows, given an azeotropic mixture to be separated into two pure streams that utilizes a mass separating agent, find the best (optimal or near-optimal) solvent candidate (or mixture) that can perform the separation subject to economic, environmental and thermo-physical property constraints. This design problem inherently is a mixed integer non-linear programming problem because the property-process models used can be linear, non-linear or a combination of both and, numerous solvents (or solvent mixtures) can in principle be selected (Lei et al., 2015).
In this work, the generation, screening and verification of the solvent candidate follows a three stage approach, in order to, decompose the solvent design problem into manageable sub-problems. In the first stage, a number of solvent candidates are generated based on pre-defined structural constraints, for example, acyclic, cyclic and/or aromatic compounds, etc. In the second stage, the solvent candidates are screened using property constraints, for example, temperature/non-temperature dependent properties and environmental properties. In stage 3, the selected feasible solvent candidates are verified through simulation for selection of the best (optimal) solvent candidate (mixture). In stages 1-3, property models play an integration role, service plus advice role and service role respectively (Kontogeorgis and Gani, 2004).
Application of the method is highlighted for a typical azeotropic mixture separation. Di-methyl carbonate (DMC) is an important chemical because it can be used as a fuel additive and is therefore considered to be one of the better replacements for methyl tert-butyl ether. Methanol (MeOH) is used as a common raw material in the production of DMC, for example, using phosgene with hydrochloric acid as the by-product, using carbon monoxide and oxygen with water as the by-product, using a cyclic carbonate with a glycol as the by-product, etc. Therefore, recovery/separation of MeOH/DMC is an important separation sequence encountered in generating more sustainable process alternatives for the production of DMC (Babi et al., 2015, Holtbruegge et al., 2014) using MeOH as the raw material. The objective of this presentation is to present the best separation system, with the focus on solvent generation, screening and verification for extractive distillation for the separation of MeOH and DMC. The three stage approach will be presented and it will be shown that existing solvent candidates found in the literature are already generated in the ?'generation'' stage plus new solvent candidates. In the ?'screening'' and ?'verification'' stages, it will be shown that two solvent candidates (not previously reported) are selected that satisfy the structural, property and environmental constraints for the effective separation and recovery of MeOH and DMC. Finally, a design of experiments method will be presented in order to cover the design and pilot testing of the best solvent candidate.
Original languageEnglish
Title of host publicationProceedings of the 2015 AIChE Annual Meeting
Number of pages1
Publication date2015
Article number165a
ISBN (Electronic)978-0-8169-1094-6
Publication statusPublished - 2015
Event2015 AIChE Annual Meeting - Salt Palace Convention Center, Salt Lake City, United States
Duration: 8 Nov 201513 Nov 2015
http://www.aiche.org/conferences/aiche-annual-meeting/2015

Conference

Conference2015 AIChE Annual Meeting
LocationSalt Palace Convention Center
CountryUnited States
CitySalt Lake City
Period08/11/201513/11/2015
Internet address

Cite this

Gani, R., & Babi, D. K. (2015). On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation. In Proceedings of the 2015 AIChE Annual Meeting [165a]
Gani, Rafiqul ; Babi, Deenesh Kavi. / On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation. Proceedings of the 2015 AIChE Annual Meeting. 2015.
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Gani, R & Babi, DK 2015, On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation. in Proceedings of the 2015 AIChE Annual Meeting., 165a, 2015 AIChE Annual Meeting, Salt Lake City, United States, 08/11/2015.

On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation. / Gani, Rafiqul; Babi, Deenesh Kavi.

Proceedings of the 2015 AIChE Annual Meeting. 2015. 165a.

Research output: Chapter in Book/Report/Conference proceedingConference abstract in proceedingsResearchpeer-review

TY - ABST

T1 - On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation

AU - Gani, Rafiqul

AU - Babi, Deenesh Kavi

PY - 2015

Y1 - 2015

N2 - Solvents (mass separating agents) play an important role in separation-based processes. For example, consider the separation of an azeotropic mixture. If the azeotrope is not pressure dependent, then a feasible separation technique that can be employed for separation of the azeotrope is usually extractive distillation. In extractive distillation the solvent affects the relative volatility of the two key compounds to be separated. In other words, for a two column distillation sequence configuration, the lighter boiling compound is obtained as the top product of the first distillation column and the heavier boiling compound is obtained as the top product of the second distillation column where the solvent is recovered (for re-use and recycle).Therefore, the solvent design problem can be defined as follows, given an azeotropic mixture to be separated into two pure streams that utilizes a mass separating agent, find the best (optimal or near-optimal) solvent candidate (or mixture) that can perform the separation subject to economic, environmental and thermo-physical property constraints. This design problem inherently is a mixed integer non-linear programming problem because the property-process models used can be linear, non-linear or a combination of both and, numerous solvents (or solvent mixtures) can in principle be selected (Lei et al., 2015).In this work, the generation, screening and verification of the solvent candidate follows a three stage approach, in order to, decompose the solvent design problem into manageable sub-problems. In the first stage, a number of solvent candidates are generated based on pre-defined structural constraints, for example, acyclic, cyclic and/or aromatic compounds, etc. In the second stage, the solvent candidates are screened using property constraints, for example, temperature/non-temperature dependent properties and environmental properties. In stage 3, the selected feasible solvent candidates are verified through simulation for selection of the best (optimal) solvent candidate (mixture). In stages 1-3, property models play an integration role, service plus advice role and service role respectively (Kontogeorgis and Gani, 2004).Application of the method is highlighted for a typical azeotropic mixture separation. Di-methyl carbonate (DMC) is an important chemical because it can be used as a fuel additive and is therefore considered to be one of the better replacements for methyl tert-butyl ether. Methanol (MeOH) is used as a common raw material in the production of DMC, for example, using phosgene with hydrochloric acid as the by-product, using carbon monoxide and oxygen with water as the by-product, using a cyclic carbonate with a glycol as the by-product, etc. Therefore, recovery/separation of MeOH/DMC is an important separation sequence encountered in generating more sustainable process alternatives for the production of DMC (Babi et al., 2015, Holtbruegge et al., 2014) using MeOH as the raw material. The objective of this presentation is to present the best separation system, with the focus on solvent generation, screening and verification for extractive distillation for the separation of MeOH and DMC. The three stage approach will be presented and it will be shown that existing solvent candidates found in the literature are already generated in the ?'generation'' stage plus new solvent candidates. In the ?'screening'' and ?'verification'' stages, it will be shown that two solvent candidates (not previously reported) are selected that satisfy the structural, property and environmental constraints for the effective separation and recovery of MeOH and DMC. Finally, a design of experiments method will be presented in order to cover the design and pilot testing of the best solvent candidate.

AB - Solvents (mass separating agents) play an important role in separation-based processes. For example, consider the separation of an azeotropic mixture. If the azeotrope is not pressure dependent, then a feasible separation technique that can be employed for separation of the azeotrope is usually extractive distillation. In extractive distillation the solvent affects the relative volatility of the two key compounds to be separated. In other words, for a two column distillation sequence configuration, the lighter boiling compound is obtained as the top product of the first distillation column and the heavier boiling compound is obtained as the top product of the second distillation column where the solvent is recovered (for re-use and recycle).Therefore, the solvent design problem can be defined as follows, given an azeotropic mixture to be separated into two pure streams that utilizes a mass separating agent, find the best (optimal or near-optimal) solvent candidate (or mixture) that can perform the separation subject to economic, environmental and thermo-physical property constraints. This design problem inherently is a mixed integer non-linear programming problem because the property-process models used can be linear, non-linear or a combination of both and, numerous solvents (or solvent mixtures) can in principle be selected (Lei et al., 2015).In this work, the generation, screening and verification of the solvent candidate follows a three stage approach, in order to, decompose the solvent design problem into manageable sub-problems. In the first stage, a number of solvent candidates are generated based on pre-defined structural constraints, for example, acyclic, cyclic and/or aromatic compounds, etc. In the second stage, the solvent candidates are screened using property constraints, for example, temperature/non-temperature dependent properties and environmental properties. In stage 3, the selected feasible solvent candidates are verified through simulation for selection of the best (optimal) solvent candidate (mixture). In stages 1-3, property models play an integration role, service plus advice role and service role respectively (Kontogeorgis and Gani, 2004).Application of the method is highlighted for a typical azeotropic mixture separation. Di-methyl carbonate (DMC) is an important chemical because it can be used as a fuel additive and is therefore considered to be one of the better replacements for methyl tert-butyl ether. Methanol (MeOH) is used as a common raw material in the production of DMC, for example, using phosgene with hydrochloric acid as the by-product, using carbon monoxide and oxygen with water as the by-product, using a cyclic carbonate with a glycol as the by-product, etc. Therefore, recovery/separation of MeOH/DMC is an important separation sequence encountered in generating more sustainable process alternatives for the production of DMC (Babi et al., 2015, Holtbruegge et al., 2014) using MeOH as the raw material. The objective of this presentation is to present the best separation system, with the focus on solvent generation, screening and verification for extractive distillation for the separation of MeOH and DMC. The three stage approach will be presented and it will be shown that existing solvent candidates found in the literature are already generated in the ?'generation'' stage plus new solvent candidates. In the ?'screening'' and ?'verification'' stages, it will be shown that two solvent candidates (not previously reported) are selected that satisfy the structural, property and environmental constraints for the effective separation and recovery of MeOH and DMC. Finally, a design of experiments method will be presented in order to cover the design and pilot testing of the best solvent candidate.

M3 - Conference abstract in proceedings

BT - Proceedings of the 2015 AIChE Annual Meeting

ER -

Gani R, Babi DK. On the Integration Role of Solvents in Process Synthesis-Design-Intensification: Application to DMC/MeOH separation. In Proceedings of the 2015 AIChE Annual Meeting. 2015. 165a