Multiphasic Microchannel Reactions
AssigneeBattelle Memorial Institute
InventorsJohn Brophy, Bruce Monzyk
Life of this patent
Estimating the term…
Abstract
Multiphasic reactions, especially those reactions using a phase transfer catalyst, are conducted in microchannel apparatus. Advantageously, these reactions can be conducted with two, planar microlayers of reactants in adjacent laminar flow streams. Microchannel apparatus and methods for conducting unit operations such as reactions and separations in microchannel apparatus is also described. Microchannel apparatus can provide advantages for controlling reactions and separating products, solvents or reactants in multiphase reactions.
Claims9
1-13. (canceled)
A phase transfer catalysis system, comprising:
- a first stream having a thickness of 1 mm or less and a length of more than 3 mm disposed in a reaction channel having a thickness of 2 mm or less and a length of more than 3 mm;
- providing a second stream adjacent the first stream and having a thickness of 1 mm or less and a length of more than 3 mm in the reaction channel;
- wherein the first stream and the second stream form a combined multiphase stream having a thickness of 2 mm or less and a length of more than 3 mm;
- wherein the first stream comprises a first reactant;
- wherein the second stream comprises a second reactant;
- and
- providing a phase transfer catalyst;
- wherein the phase transfer catalyst catalyzes the reaction of the first reactant and the second reactant to form a product.
A microchannel apparatus, comprising:
- a first channel inlet connected to a reaction channel having a thickness of 2 mm or less and a length of more than 3 mm;
- wherein the reaction channel comprises a ceiling and a floor and wherein the floor and the ceiling each define a border of an open area and wherein the thickness of the reaction channel is the distance between the ceiling and the floor;
- a second channel inlet connected to the reaction channel;
- a separator plate separating the first channel inlet from the second channel inlet;
- wherein an edge of the separator plate forms at least one border of the open area;
- wherein the open area has a length of at least 3 mm;
- and
- there being no membrane in the open area;
- a first channel outlet connected to the reaction channel;
- and
- a second channel outlet connected to the reaction channel;
- wherein the second channel outlet is separate from the first channel outlet.
Microchannel apparatus, comprising:
- a separation zone that comprises:
- at least one portion of an internal surface that is hydrophilic;
- at least one portion of an internal surface that is hydrophobic;
- and
- at least one separation assist feature selected from the group consisting of:
- an expansion zone in the separation zone that is connected to a reaction channel and has a larger internal cross-sectional area than the reaction channel, a phase coalescence agent, and a separator plate;
- and
- wherein the separation zone has at least one internal dimension of 2 mm or less.
A method of conducting at least one unit operation, comprising:
- passing a multiphasic fluid stream into a separation zone;
- wherein the multiphasic steam comprises a first non-solid phase and a second non-solid phase;
- wherein the separation zone comprises:
- at least one portion of an internal surface that is hydrophilic;
- at least one portion of an internal surface that is hydrophobic;
- and
- at least one separation assist feature selected from the group consisting of:
- an expansion zone in the separation zone that is connected to a reaction channel and has a larger internal cross-sectional area than the reaction channel, a phase coalescence agent, and a separator plate;
- wherein the multiphasic fluid stream passed into the separator zone has at least one dimension of 2 mm or less;
- and
- wherein at least two separate streams pass from the separator zone, comprising a first separated stream and a second separated stream;
- wherein the first separated stream contains a relatively higher ratio of the first non-solid phase to the second non-solid phase as compared to the multiphasic fluid stream entering the separator zone;
- and
- wherein the second separated stream contains a relatively lower ratio of the first non-solid phase to the second non-solid phase as compared to the multiphasic fluid stream entering the separator zone.
(canceled)
Dependencies are inferred from the claim text.