Validation of design and scaling heuristics integrating environmental externalities
Authorship
A.P.C.
Master in Chemical and Bioprocess Engineering
A.P.C.
Master in Chemical and Bioprocess Engineering
Defense date
02.19.2025 10:45
02.19.2025 10:45
Summary
Early stage evaluations are of interest in validating the current reliability of design heuristics in chemical engineering by anticipating the technical, economic and environmental viability of a project from a holistic perspective. Their development depends on the maturity of a technology, so this document addresses their application to two representative case studies. Initially, the suitability of the typical factor between the reflux ratio and its minimum value is tested in a distillation column with a double analysis in a large-scale azeotropic system in a tray unit, and packed contact in a typical production in the fine chemicals sector. In a second evaluation, the most suitable scale up methods are reviewed for a hypothetical industrial plant of polyhydroxyalkanoates with mixed microbial cultures and a residual organic substrate based on pilot experimental records. The results obtained in the mature technology demonstrated a favourable balance between separation efficiency and operating costs at lower reflux ratios, addressing a higher initial investment to prioritise a reduction in emissions and process costs. Regarding the case study of the emerging system, the process engineering scale up heuristics were found to be optimal in terms of applicability and uncertainty, while the economic and carbon footprint analysis pointed to acidification conversion, intracellular product extraction and raw material acquisition costs as the main limitations for its introduction into the market.
Early stage evaluations are of interest in validating the current reliability of design heuristics in chemical engineering by anticipating the technical, economic and environmental viability of a project from a holistic perspective. Their development depends on the maturity of a technology, so this document addresses their application to two representative case studies. Initially, the suitability of the typical factor between the reflux ratio and its minimum value is tested in a distillation column with a double analysis in a large-scale azeotropic system in a tray unit, and packed contact in a typical production in the fine chemicals sector. In a second evaluation, the most suitable scale up methods are reviewed for a hypothetical industrial plant of polyhydroxyalkanoates with mixed microbial cultures and a residual organic substrate based on pilot experimental records. The results obtained in the mature technology demonstrated a favourable balance between separation efficiency and operating costs at lower reflux ratios, addressing a higher initial investment to prioritise a reduction in emissions and process costs. Regarding the case study of the emerging system, the process engineering scale up heuristics were found to be optimal in terms of applicability and uncertainty, while the economic and carbon footprint analysis pointed to acidification conversion, intracellular product extraction and raw material acquisition costs as the main limitations for its introduction into the market.
Direction
HOSPIDO QUINTANA, ALMUDENA (Tutorships)
MAURICIO IGLESIAS, MIGUEL (Co-tutorships)
HOSPIDO QUINTANA, ALMUDENA (Tutorships)
MAURICIO IGLESIAS, MIGUEL (Co-tutorships)
Court
GONZALEZ ALVAREZ, JULIA (Chairman)
FRANCO RUIZ, DANIEL JOSE (Secretary)
GONZALEZ GARCIA, SARA (Member)
GONZALEZ ALVAREZ, JULIA (Chairman)
FRANCO RUIZ, DANIEL JOSE (Secretary)
GONZALEZ GARCIA, SARA (Member)