Continuous acoustic chemical microreactor
A continuous acoustic chemical microreactor system is disclosed. The system includes a continuous process vessel (CPV) and an acoustic agitator coupled to the CPV and configured to agitate the CPV along an oscillation axis. The CPV includes a reactant inlet configured to receive one or more reactants into the CPV, an elongated tube coupled at a first end to the reactant inlet and configured to receive the reactants from the reactant inlet, and a product outlet coupled to a second end of the elongated tube and configured to discharge a product of a chemical reaction among the reactants from the CPV. The acoustic agitator is configured to agitate the CPV along the oscillation axis such that the inner surface of the elongated tube accelerates the one or more reactants in alternating upward and downward directions along the oscillation axis.
1. A continuous acoustic chemical microreactor system comprising:
a continuous process vessel configured to oscillate along an oscillation axis, the continuous process vessel including:
a reactant inlet configured to receive one or more reactants into the continuous process vessel;
an elongated tube coupled at a first end to the reactant inlet and configured to receive the reactants from the reactant inlet, wherein the elongated tube has an inner surface having a hydraulic diameter of less than 2.5 cm; and
a product outlet coupled to a second end of the elongated tube and configured to discharge a product of a chemical reaction among the reactants from the continuous process vessel; and
an acoustic agitator coupled to the continuous process vessel and configured to agitate the continuous process vessel along the oscillation axis at a frequency greater than 10 Hz and less than 100 Hz such that the inner surface of the elongated tube accelerates the one or more reactants in alternating upward and downward directions along the oscillation axis.
2. The system of claim 1 , wherein the acoustic agitator is configured to agitate the continuous process vessel with an acceleration greater than 60 times the gravitational force equivalent (g).
3. The system of claim 1 , wherein the elongated tube is at least 10 cm long.
4. The system of claim 1 , wherein the elongated tube has an inner surface having a hydraulic diameter of less than 0.5 cm.
5. The system of claim 1 , wherein the continuous process vessel includes: a coolant inlet configured to receive a cooling fluid;
an interstitial region within the continuous process vessel and surrounding the elongated tube, the interstitial region configured to receive the cooling fluid and bring it into contact with an outer surface of the elongated tube; and
a coolant outlet for discharging the cooling fluid from the interstitial region.
6. The system of claim 1 , wherein the continuous process vessel includes: a heater inlet configured to receive a heating fluid;
an interstitial region within the continuous process vessel and surrounding the elongated tube, the interstitial region configured to receive the heating fluid and bring it into contact with an outer surface of the elongated tube; and
a heater outlet for discharging the heating fluid from the interstitial region.
7. The system of claim 1 , wherein the reactant inlet is configured to receive a transport gas.
8. The system of claim 1 , wherein the system is configured to operate at mechanical resonance.
9. The system of claim 1 , comprising:
a second reactant inlet coupled to the elongated tube at a point between the first end and the second end and configured to receive a midstream reactant and introduce it into the elongated tube.
10. The system of claim 1 , wherein the inner surface of the elongated tube has a cross section that is substantially circular.
11. The system of claim 1 , wherein the inner surface of the elongated tube has a cross section that is substantially ovular.
12. The system of claim 1 , wherein the inner surface of the elongated tube has a cross section that is substantially rectangular.
13. The system of claim 1 , wherein the inner surface of the elongated tube has a cross section that is substantially square.
14. The system of claim 1 , wherein the inner surface of the elongated tube has a cross section that is substantially triangular.
15. The system of claim 1 , wherein the inner surface of the elongated tube is smooth.
16. The system of claim 1 , wherein the inner surface of the elongated tube is rough.
17. The system of claim 1 , wherein the inner surface of the elongated tube is coated with a catalyst.