Reaction method using microreactor
View Patent ↗In a reaction caused by using a microreactor which provides a plurality of supply routes in communication with one reaction channel as a multicylindrical structure having a co-axis and causes a plurality of fluids L 1 , L 2 , L 3 to flow together in the reaction channel via the respective fluid supply routes, whereby these fluids L 1 , L 2 , L 3 are coaxially laminated and caused to flow as laminar flows whose sections orthogonal to the co-axis are annular and the fluids are diffused together in a normal direction of contact interfaces thereof to cause the reaction, among the plurality of laminated fluids L 1 , L 2 , L 3 , at least one fluid is constituted by a fluid not participating in the reaction of other fluids.
1. A reaction method comprising
flowing fluids through a microreactor,
coaxially laminating the fluids and causing the fluids to flow as laminar flows whose sections orthogonal to the co-axis are annular, and
reacting the fluids by diffusing the fluids in a normal direction of contact interfaces of the fluids,
wherein the microreactor has a plurality of fluid supply routes in communication with one reaction channel as a multicylindrical structure having a co-axis and causes a plurality of fluids to flow together in the reaction channel via the respective fluid supply routes,
wherein among said plurality of laminated fluids, at least one fluid is a fluid not participating in the reaction of other fluids and
wherein the cross-sectional thickness of said fluids participating in the reaction is varied by increasing or decreasing the flow rate of said fluid not participating in the reaction.
2. The reaction method according to claim 1 , wherein an opening width of said reaction channel is not less than 1 μm but not more than 1000 μm.
3. The reaction method according to claim 1 , wherein said laminated laminar flows are constituted by 3 or more kinds of fluids and, among these fluids, between the laminar flows formed by the fluids participating in the reaction is sandwiched a laminar flow of said fluid not participating in the reaction.
4. The reaction method to claim 1 , wherein said laminated laminar flows are constituted by 3 or more kinds of fluids and, among these fluids, said fluid not participating in the reaction is used as a fluid in contact with a wall surface of said reaction channel.
5. The reaction method according to claim 1 , wherein said laminated laminar flows are constituted by 3 or more kinds of fluids and, among these fluids, the fluids participating in the reaction form regular annular laminar flows.
6. The reaction method according to claim 1 , wherein said fluid not participating in the reaction is a solvent component of said fluids participating in the reaction.
7. The reaction method according claim 1 , wherein said laminated laminar flows are constituted by 3 or more kinds of fluids and, among these fluids, apart from layers formed by the fluids participating in the reaction, a layer for an extraction fluid for extracting and separating reaction products of the reaction is formed, and a desired reaction product formed by the reaction is extracted and separated by said extraction fluid.
8. The reaction method according to claim 1 , wherein in each of the fluid supply routes formed in the multicylindrical structure of said co-axis, a plurality of fluid supply ports are arranged at equal intervals in a circumferential direction of said multicylindrical structure.
9. The reaction method according to claim 1 , wherein the reaction temperature of fluids flowing in said reaction channel is controlled.