TY - JOUR
T1 - Simulated moving bed technology
T2 - Old and new
AU - Sá Gomes, Pedro
AU - Minceva, Mirjana
AU - Rodrigues, Alírio E.
N1 - Funding Information:
Acknowledgment Pedro Sá Gomes acknowledges the financial support from FCT “Fundac¸ão para a Ciência e a Tecnologia” (Ph-D grant SFRH/BD/22103/2005), Ministry of Science and Technology of Portugal. Financial support through the project POCI/EQU/59296/2004 is gratefully acknowledged.
PY - 2006/9
Y1 - 2006/9
N2 - The Simulated Moving Bed (SMB) concept has been applied to the separation of different mixtures as a continuous counter current separation process, avoiding several problems related with solid motion. The aim of this work is to present some relevant examples of SMB separations corresponding to the two major ages in the use of the SMB concept, here named "old" and "new" applications. The "old" applications of SMB technology in the petrochemical industry are still important, with large and highly productive units; and the "new" applications of the second "age" of SMB concept are from the fine chemical, pharmaceutical and biochemistry areas, associated with the demand of high purity products during the last 10 years. Different examples are presented for different ages: a UOP Parex ® process for the "old", modelled with the equivalent True Moving Bed (TMB) approach; and a chiral resolution for the "new", modelled by the real SMB model. Some of the latest developments are also mentioned: the non conventional techniques as the Varicol ® process, PowerFeed, Modicon, M3C or Enriched Extract-SMB (EE-SMB), MultiFeed (MF), Outlet Streams Swing (OSS) or Pseudo-SMB, involving considerable changes in the SMB concept itself. The use of the last optimization/modelling packages for the development of design techniques, either at the conception stage as well as for performance improvements of existing units is emphasized.
AB - The Simulated Moving Bed (SMB) concept has been applied to the separation of different mixtures as a continuous counter current separation process, avoiding several problems related with solid motion. The aim of this work is to present some relevant examples of SMB separations corresponding to the two major ages in the use of the SMB concept, here named "old" and "new" applications. The "old" applications of SMB technology in the petrochemical industry are still important, with large and highly productive units; and the "new" applications of the second "age" of SMB concept are from the fine chemical, pharmaceutical and biochemistry areas, associated with the demand of high purity products during the last 10 years. Different examples are presented for different ages: a UOP Parex ® process for the "old", modelled with the equivalent True Moving Bed (TMB) approach; and a chiral resolution for the "new", modelled by the real SMB model. Some of the latest developments are also mentioned: the non conventional techniques as the Varicol ® process, PowerFeed, Modicon, M3C or Enriched Extract-SMB (EE-SMB), MultiFeed (MF), Outlet Streams Swing (OSS) or Pseudo-SMB, involving considerable changes in the SMB concept itself. The use of the last optimization/modelling packages for the development of design techniques, either at the conception stage as well as for performance improvements of existing units is emphasized.
KW - Chiral
KW - Chromatographic separations
KW - Modelling
KW - P-xylene
KW - Simulated moving bed
KW - Simulation and optimization
KW - True moving bed
UR - http://www.scopus.com/inward/record.url?scp=33845459699&partnerID=8YFLogxK
U2 - 10.1007/s10450-006-0566-9
DO - 10.1007/s10450-006-0566-9
M3 - Article
AN - SCOPUS:33845459699
SN - 0929-5607
VL - 12
SP - 375
EP - 392
JO - Adsorption
JF - Adsorption
IS - 5-6
ER -