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Estimation of chemical concentration due to fugitive emissions during chemical process design
Authors:Mimi H Hassim  Alberto L Pérez  Markku Hurme
Affiliation:1. Department of Biotechnology and Chemical Technology, School of Science and Technology, Aalto University, P.O. Box 6100, FIN-02015 HUT, Finland;2. Department of Chemical Engineering, University Teknologi Malaysia, 81310 UTM Skudai, Malaysia;1. Centre of Hydrogen Energy, Department of Chemical Engineering, Universiti Teknologi Malaysia, 81310, UTM, Johor Bahru, Malaysia;2. Institute of Chemical and Engineering Sciences, 1, Pesek Road, Jurong Island, Singapore 627833, Singapore;1. Department of Chemical and Biological Engineering, University of Wisconsin-Madison,1415 Engineering Drive, Madison, WI 53706, USA;2. Faculty of Chemical and Energy Engineering/Centre of Hydrogen Energy, Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia;3. Department of Biotechnology and Chemical Technology, Aalto University, P. O. Box 16100, FIN-00076 Aalto, Finland;1. AGH University of Science and Technology, Academic Centre for Materials and Nanotechnology, A. Mickiewicza 30 Ave., Krakow, 30-059, Poland;2. AGH University of Science and Technology, Faculty of Materials Science and Ceramics, A. Mickiewicza 30 Ave., Krakow, 30-059, Poland;3. AGH University of Science and Technology, Faculty of Foundry Engineering, A. Mickiewicza 30 Ave. Krakow, 30-059, Poland
Abstract:Fugitive emissions are not an environmental concern alone, but are also a health concern. From occupational health standpoint, fugitive emissions are the main sources of origin of the continuous exposure to workers. Operating plants regularly measure release and concentration levels through a plant-monitoring program. However, for processes which are still ‘on paper’, predictive estimation methods are required. Therefore, three methods for estimating concentration of the fugitive emissions are presented for the process development and design phases of petrochemical processes. The methods estimate the fugitive emission rates and plant plot dimensions resulting to fugitive emission concentrations. The methods were developed for the type and amount of information available in three process design stages; conceptual design, preliminary process design, and detailed process design. The methods are applied on a real benzene plant; the estimated benzene concentrations are compared to the actual concentration measured at the plant. The results show that as the information mounts up during design, the concentration estimate becomes more accurate. The results indicate that the methods presented provide simple estimates of fugitive emission-based concentrations during the design stages.
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