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Massachusetts Institute of Technology

Scale-up of continuous chemical synthesis systems

Abstract

dc:description.abstract

Continuous flow systems for chemical synthesis have become increasingly important in the pharmaceutical and fine chemical industry in the past decade. Initially, this work was confined primarily to microfluidic systems, but recently there has been a growing demand for milliscale systems capable of making material for clinical trials and pilot plant testing. The objective of this thesis is to demonstrate a practical system to accomplish continuous chemical synthesis within the context of a fully integrated pilot plant. The plant provided a platform to test scaled-up membrane-based liquid-liquid separators which were studied in detail. Previous work demonstrated the use of microfiltration membranes to separate liquid-liquid systems by leveraging the dominance of interfacial tension over gravity at small scales. When scaling up, it was determined that pressure control was critical to the operation of the separators. A pressure control module was designed and integrated into the separator device to provide the appropriate conditions to guarantee separation. The separators required no outside control to accomplish separation when connected to various downstream conditions including pumps, backpressure controllers, and other separators. This allowed for easy design and operation of multistep processes such as solvent swaps and countercurrent extraction. The main accomplishment covered in this thesis is the building and operation of an integrated continuous manufacturing plant for a small molecule pharmaceutical product (aliskiren tablets). An advanced intermediate was continuously processed through two synthetic steps with workup which are detailed here. The remainder of the process purified and formulated the drug substance and formed the final tablet which met many key performance criteria. This work opens avenues to look at even more complex liquid-liquid and even gas-liquid separation processes. Improved processes for continuous manufacturing which make use of recycling, multistage extraction, and novel chemistries can build on the research performed here to further improve synthesis systems. These results demonstrate that continuous processes are possible even for complex, industrially-relevant products.

Degree

thesis:*
Department dc:contributor.department
Massachusetts Institute of Technology. Department of Chemical Engineering.
Grantor dc:publisher
Massachusetts Institute of Technology
Year dc:date.issued
2013

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Heider, Patrick Louis
Advisor dc:contributor.advisor
  • Klavs F. Jensen.

Subjects

dc:subject × 1

Rights

dc:rights
Statement dc:rights
  • M.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission.
Language dc:language.iso
eng

Identifiers

dc:identifier.*
Handle dc:identifier.uri
http://hdl.handle.net/1721.1/86870
OAI identifier oai:identifier
oai:dspace.mit.edu:1721.1/86870

Chain of custody

source
Harvested from
MIT
Base URL
dspace.mit.edu/oai/request
Last updated
2026-07-22
Source record
OAI-PMH GetRecord
citation

Heider, Patrick Louis. Scale-up of continuous chemical synthesis systems. Massachusetts Institute of Technology, 2013. http://hdl.handle.net/1721.1/86870