Acetonitrile Regeneration from Oligonucleotide Production Waste Streams

A distillation concept is described to process organic and aqueous waste streams from an oligonucleotide process to regenerate 85% of acetonitrile contained in the wastes, for reintroduction back into the oligonucleotide process. Careful selection of the streams to send to regeneration based on their acetonitrile content was shown to simplify the number of processing steps and minimize the size of the equipment required for regeneration. Availability of accurate vapor–liquid equilibrium data was shown to be key to designing the number of processing steps, the operating conditions, and calculating purification performance. A modified classical two-column distillation pressure swing dewatering system with an intermediate-pressure column for the separation of light boilers, was shown to effectively purify and dewater acetonitrile to the required specifications. Aspen Plus software was used to generate vapor–liquid equilibrium (VLE) data and simulate process alternatives.

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Publication Details

Journal
Organic Process Research & Development
Published
2024-08-30
DOI
https://doi.org/10.1021/acs.oprd.4c00188
Citations
2
Primary Topic
Innovative Microfluidic and Catalytic Techniques Innovation
Type
article
Field-Weighted Citation Impact
0.37
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article

Acetonitrile Regeneration from Oligonucleotide Production Waste Streams

Francesco Venturoni, Bertrand Guélat, Christian Fleury, Ruairí Ó Meadhra
2 citations
Organic Process Research & Development
Innovative Microfluidic and Catalytic Techniques Innovation
0.37
article

Acetonitrile Regeneration from Oligonucleotide Production Waste Streams

Francesco Venturoni, Bertrand Guélat, Christian Fleury, Ruairí Ó Meadhra
article en
2 citations

Abstract

A distillation concept is described to process organic and aqueous waste streams from an oligonucleotide process to regenerate 85% of acetonitrile contained in the wastes, for reintroduction back into the oligonucleotide process. Careful selection of the streams to send to regeneration based on their acetonitrile content was shown to simplify the number of processing steps and minimize the size of the equipment required for regeneration. Availability of accurate vapor–liquid equilibrium data was shown to be key to designing the number of processing steps, the operating conditions, and calculating purification performance. A modified classical two-column distillation pressure swing dewatering system with an intermediate-pressure column for the separation of light boilers, was shown to effectively purify and dewater acetonitrile to the required specifications. Aspen Plus software was used to generate vapor–liquid equilibrium (VLE) data and simulate process alternatives.

Organic Process Research & DevelopmentVol. 28(9)
Novartis (Switzerland) (CH)
Responsible consumption and production
Openalex Percentile: Top 44%
Innovative Microfluidic and Catalytic Techniques Innovation
0.37
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