Continuous separator bypass systems and methods of use thereof
The present disclosure provides for a continuous membrane separator bypass system and a continuous filtration separator system and methods of using the systems in the separation of liquid-liquid mixtures and filtration of process liquids. The methods and apparatus are useful for the production of fine chemicals and pharmaceuticals, particularly using Integrated Continuous Manufacturing (ICM), but can also be integrated with other manufacturing processes, such as batch and semi-continuous processes.
1. A filter separator bypass system for continuously separating fluid mixtures comprising:
a process stream ( 5 . 1 ) input path and a back flow wash stream ( 6 . 1 ) in fluid communication with a two position four way valve ( 2 . 1 ),
said valve ( 2 . 1 ) having a first position in fluid communication with
a first filtration path having a first differential pressure transducer ( 4 . 3 ), a first filter ( 3 . 4 ), a second differential pressure transducer ( 4 . 4 ), and a first three-way valve ( 2 . 4 ) in position one in fluid communication with a filtered stream ( 5 . 2 ) path, and
a first waste stream path in fluid communication said back flow wash stream ( 6 . 1 ) in fluid communication with a second three way valve ( 2 . 5 ) in position one, a third differential pressure transducer ( 4 . 6 ), a second filter ( 3 . 5 ), a fourth differential pressure transducer ( 4 . 5 ), and a waste stream path ( 5 . 8 ); and
said valve ( 2 . 1 ) having a second position in fluid communication with
a second filtration path having said fourth differential pressure transducer ( 4 . 5 ), said second filter ( 3 . 5 ), said third differential pressure transducer ( 4 . 6 ), and said three way valve ( 2 . 5 ) in position two in fluid communication with said filtered stream ( 5 . 2 ) path, and
a second waste stream path in fluid communication with said back flow wash stream ( 6 . 1 ) path in fluid communication with said first three-way valve ( 2 . 4 ) in position two, said second differential pressure transducer ( 4 . 4 ), said first filter ( 3 . 4 ), said first differential pressure transducer ( 4 . 3 ), and said waste stream path ( 5 . 8 ).
2. The filter separator bypass system of claim 1 , wherein said first filter ( 3 . 4 ) and said second filter ( 3 . 5 ) comprise a filter having a mean pore size of between 0.22 micrometers (μm) to 250 μm.
3. The filter separator bypass system of claim 1 , wherein said first filter ( 3 . 4 ) and said second filter ( 3 . 5 ) comprise a filter consisting of stainless steel, a metal alloy, hard anodized aluminum, or a polymer.
4. The filter separator bypass system of claim 3 , wherein said polymer comprises a fluorinated polymer selected from the group consisting of polytetrafluoroethylene, fluorinated ethylene propylene, perfluoroalkoxy, ethylene tetrafluoroethylene, and polyvinylidene fluoride.
5. The filter separator bypass system of claim 1 , further comprising one or more ultrasonic baths to facilitate the cleaning of said first filter ( 3 . 4 ) and said second filter ( 3 . 5 ).
6. The filter separator bypass system of claim 1 , further comprising an ultrasonic transducer configured to apply in-line ultrasonication to the housing of said system.
7. The filter separator bypass system of claim 1 , wherein said system is capable of running continuously for between 1 day and 1 year.