CROSS MIXERS FOR LIPID NANOPARTICLE PRODUCTION, AND METHODS OF OPERATING THE SAME
The present disclosure provides processes for controlled high-throughput preparation of lipid nanoparticle with defined parameters. A cross mixer can include a central region, a first inlet in fluidic communication with the central region, a second inlet in fluidic communication with the central region, a third inlet in fluidic communication with the central region, and an outlet in fluidic communication with the central region, the outlet oriented at an angle of between about 35° and about 120° from the first inlet and an angle of between about 35° and about 120° from the second inlet.
1 . A cross mixer, comprising:
a central region;
a first inlet in fluidic communication with the central region and coupled to a first side of the central region;
a second inlet in fluidic communication with the central region and coupled to a second side of the central region, the second side opposite the first side;
a third inlet in fluidic communication with the central region and coupled to a third side of the central region, the third side adjacent to the first side and the second side; and
an outlet in fluidic communication with the central region and coupled to a fourth side of the central region, the fourth side opposite the third side, the outlet oriented at an angle of between about 35° and about 120° from the first inlet and an angle of between about 35° and about 120° from the second inlet.
2 . The cross mixer of claim 1 , wherein the central region includes a first dimension approximately equal to a first dimension of a cross-sectional area of the first inlet, a second dimension approximately equal to a second dimension of the cross-sectional area of the first inlet, and a third dimension approximately equal to a first dimension of a cross-sectional area of the second inlet.
3 . The cross mixer of claim 1 , wherein the central region includes a convergence chamber.
4 . The cross mixer of claim 3 , wherein the convergence chamber has a cylindrical shape.
5 . The cross mixer of claim 4 , wherein the first inlet and the second inlet are offset, such that fluids flowing into the convergence chamber create a vertex.
6 . The cross mixer of claim 3 , wherein the convergence chamber has a cubic shape.
7 . The cross mixer of claim 3 , wherein the convergence chamber has a trapezoidal prism shape.
8 . The cross mixer of claim 3 , wherein the convergence chamber has a frustum shape.
9 . The cross mixer of claim 1 , wherein the first inlet has a square cross section.
10 . The cross mixer of claim 9 , wherein the square cross section has a cross-sectional dimension of about 1 mm to about 4 mm.
11 . The cross mixer of claim 1 , wherein the first inlet has a circular cross section.
12 . The cross mixer of claim 11 , wherein the circular cross section has a cross-sectional diameter of about 1 mm to about 4 mm.
13 . The cross mixer of claim 1 , wherein the outlet is oriented at an angle of about 90° from the first inlet.
14 . The cross mixer of claim 1 , wherein the outlet is oriented at an angle of about 35° to about 45° from the first inlet.
15 . The cross mixer of claim 1 , wherein the third inlet is oriented approximately in-line with the outlet.
16 . The cross mixer of claim 1 , wherein the first inlet includes a first section and a second section, the first section oriented approximately orthogonal to the second section.
17 . The cross mixer of claim 16 , wherein the first section is oriented vertically and the second section is oriented horizontally.
18 . The cross mixer of claim 1 , wherein the outlet is oriented within about 5° of parallel to the third inlet.
19 . The cross mixer of claim 1 , wherein the third inlet includes a bend having an angle between about 80° and about 100°.
20 . The cross mixer of claim 1 , wherein the outlet includes a narrow region and an expanded region, the expanded region further from the central region than the narrow region.
21 . The cross mixer of claim 20 , wherein the narrow region has a length between about 2 mm and about 10 mm.
22 . The cross mixer of claim 20 , wherein the narrow region has a length of at least about 40 mm.
23 . The cross mixer of claim 20 , wherein the expanded region has a diameter larger than the narrow region by a factor of between about 1.5:1 and about 5:1.
24 . The cross mixer of claim 20 , wherein the narrow region of the outlet has a length-to-diameter ratio between about 5:1 and about 15:1.
25 . The cross mixer of claim 20 , wherein the third inlet includes a narrow region and an expanded region, the expanded region further from the central region than the narrow region.
26 . The cross mixer of claim 25 , wherein the narrow region of the outlet has a first diameter and the narrow region of the third inlet has a second diameter, the ratio between the first diameter and the second diameter between about 0.5:1 and about 5:1.
27 . The cross mixer of claim 20 , wherein the narrow region has a length-to-diameter region of between about 2:1 and about 20:1.
28 . A method, comprising:
feeding a first fluid to a central region of a cross mixer via at least one of a first inlet or a second inlet, the first inlet coupled to a first side of the central region, the second inlet coupled to a second side of the central region, the first side opposite the second side;
feeding a second fluid to a third inlet of the cross mixer, the third inlet coupled to a third side of the central region, the third side adjacent to the first side and the second side;
mixing the first fluid and the second fluid to form a mixture in a central region fluidically coupled to the first inlet, the second inlet, and the third inlet; and
transferring the mixture out of the central region via an outlet of the cross mixer, the outlet coupled to a fourth side of the central region, the fourth side opposite the third side.
29 . The method of claim 28 , wherein the first fluid includes water.
30 . The method of claim 29 , wherein the second fluid includes LSS.
31 . The method of claim 30 , wherein the water reacts with the LSS to form nanoparticles via nucleation at a sufficient rate, such that the ethanol concentration in the first fluid reduces from at least about 99 wt % to less than about 30 wt % less than about 0.007 seconds after contacting the second fluid.
32 . The method of claim 31 , wherein the ethanol reacts with the LSS at a sufficient rate, such that the ethanol concentration in the first fluid reduces from at least about 99 wt % to less than about 30 wt % less than about 0.003 seconds after contacting the second fluid.
33 . The method of claim 28 , wherein the central region includes a first dimension approximately equal to a first dimension of a cross-sectional area of the first inlet, a second dimension approximately equal to a second dimension of the cross-sectional area of the first inlet, and a third dimension approximately equal to a first dimension of a cross-sectional area of the second inlet.
34 . The method of claim 28 , wherein the central region includes a convergence chamber.
35 . The method of claim 34 , wherein the convergence chamber has a cylindrical shape.
36 . The method of claim 35 , wherein the first inlet and the second inlet are offset, such that fluids flowing into the convergence chamber create a vortex.
37 . The method of claim 34 , wherein the convergence chamber has a cubic shape.
38 . The method of claim 34 , wherein the convergence chamber has a trapezoidal prism shape.
39 . The method of claim 34 , wherein the convergence chamber has a frustum shape.
40 . The method of claim 34 , wherein feeding the second fluid to the third inlet includes flowing the second fluid through a first flow path and flowing the second fluid through a second flow path, the second flow path oriented between about 80° and about 100° from the first flow path.
41 . A method for preparing LNPs, the method comprising:
mixing a lipid solution with an aqueous buffer solution in a C-Mixer, thereby forming a lipid nanoparticle solution (LNP solution) comprising LNPs, wherein:
the lipid solution is fed to an inlet (lipid inlet) of the C-Mixer;
the aqueous buffer solution is fed to an inlet (buffer inlet) of the C-Mixer; and/or
the LNP solution exits an outlet (LNP outlet) of the C-Mixer.
42 . The method of claim 41 , wherein the lipid solution is fed to an inlet that is within about 5° of parallel to the outlet.
43 . The method of claim 41 , wherein the aqueous buffer solution is fed to an inlet that forms an angle with the outlet between about 80° and about 120°.
44 . The method of claim 41 , wherein the aqueous buffer solution is fed to two inlets that each form an angle with the outlet between about 80° and about 120°.