Scaled-up and economic assessment approach of the split-phase glycolysis process for the recycling of flexible polyurethane foam wastes

The economic viability of the split-phase glycolysis process for the recycling of any kind of flexible polyurethane foam waste employing crude glycerol as cleavage agent has been demonstrated. First, experiments at pilot plant scale were carried out to check that the process can be extrapolated to l...

Descripción completa

Detalles Bibliográficos
Autores: Amo León, Jesús del, Simón, D., Ramos Marcos, María Jesús, Rodríguez Romero, Juan Francisco, Lucas Martínez, Antonio de, Borreguero Simón, Ana María
Tipo de recurso: artículo
Fecha de publicación:2022
País:España
Institución:Universidad de Castilla-La Mancha
Repositorio:RUIdeRA. Repositorio Institucional de la UCLM
OAI Identifier:oai:ruidera.uclm.es:10578/29956
Acceso en línea:http://hdl.handle.net/10578/29956
Access Level:acceso abierto
Palabra clave:Glycolysis
Scale-up
Polyurethane wastes
Economic assessment
Circular economy
Crude glycerol
Glucólisis
Aumentar proporcionalmente
Residuos de poliuretano
Evaluación económica
Economía circular
Glicerol crudo
Descripción
Sumario:The economic viability of the split-phase glycolysis process for the recycling of any kind of flexible polyurethane foam waste employing crude glycerol as cleavage agent has been demonstrated. First, experiments at pilot plant scale were carried out to check that the process can be extrapolated to larger scales. With the goal of scaling-up the process from laboratory scale to pilot plant, geometric similarity criteria were applied together with dynamic similarity for laminar flow in agitated tank reactors. Hence, a pilot plant installation was designed with geometrically similar equipment to those used for lab scale, obtaining analogous results in terms of recovered polyol properties. Then, the basic design of a split-phase glycolysis industrial plant with a capacity for treating 270 Tm per year of flexible PU foams scraps was proposed. Finally, the economic feasibility of such recycling process was confirmed because of the obtention of a Net Present Value (NPV) of 1,464,555€, with an Internal Rate of Return (IRR) of 27.99%, and a payback time between 4 and 5 years.