High shear thin film machine for dispersion and simultaneous orientation-distribution of nanoparticles within polymer matrix
11173459 · 2021-11-16
Assignee
Inventors
Cpc classification
B01F27/2722
PERFORMING OPERATIONS; TRANSPORTING
B01F35/92
PERFORMING OPERATIONS; TRANSPORTING
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
C08J2300/00
CHEMISTRY; METALLURGY
B01F23/57
PERFORMING OPERATIONS; TRANSPORTING
B01F2101/2805
PERFORMING OPERATIONS; TRANSPORTING
C08J5/005
CHEMISTRY; METALLURGY
International classification
C08J3/20
CHEMISTRY; METALLURGY
C08J5/00
CHEMISTRY; METALLURGY
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
An improved a device and method for dispersion and simultaneous orientation of nanoparticles within a matrix is provided. A mixer having a shaft and a stator is provided. The shaft may have a rupture region and erosion region. Further, an orienter having an angled stationary plate and a moving plate are provided. The nanoparticles and the matrix are fed into the mixer. A rotational force is applied to the shaft to produce shearing forces. The shearing forces disperse and exfoliate the nanoparticles within the matrix. The dispersed mixture is outputted onto the moving plate. The moving plate is forced across the angled stationary plate to produce fully developed laminar shear flow. The fully developed laminar shear flow or the two-dimensional extensional drag flow orients the dispersed nanoparticles-matrix mixture.
Claims
1. A device to disperse particles within a matrix, the device comprising: a housing having a center axis, an outer surface, an inner diameter, and an inner surface; an inlet in fluid connection with the housing configured to receive a mixture of the particles and the matrix; a shaft within the housing, the shaft having a length defined between the inlet and an outlet of the housing, a substantially constant outer circumference and a center of rotation about the center axis; a rupture portion of the shaft having surface interruptions extending inwardly from the outer circumference; an erosion portion of the shaft between the rupture portion of the shaft and the outlet, the erosion portion of the shaft having a smooth outer surface along the substantially constant outer circumference, wherein the erosion portion of the shaft is greater than the rupture portion of the shaft; and a dispersion of the mixture between the inner diameter of the housing and along substantially an entirety of the length of the shaft between the inlet and the outlet.
2. The device of claim 1, further comprising: one or more cooling channels disposed within the housing between the outer surface and the inner surface.
3. The device of claim 2, wherein the one or more cooling channels is threaded.
4. The device of claim 1, further comprising: an elongated member removably installed into each of the one or more cooling channels.
5. The device of claim 1, further comprising: a screw groove portion of the shaft proximate to the inlet and having helical channels to force the particles and the matrix towards the rupture portion.
6. The device of claim 1, wherein the interior surface of the one or more cooling channels comprise surface irregularities to increase surface area of the interior surface to improve heat dissipation.
7. The device of claim 6, wherein the surface irregularities comprise surface undulations.
8. A device to disperse particles within a matrix, the device comprising: a housing having a central axis, an outer surface, an inner diameter, and an inner surface; an inlet connected in fluid communication with the housing configured to receive a mixture of the particles and the matrix; an outlet connected in fluid communication with the housing and the inlet; a shaft disposed within the housing between the inlet and the outlet, the shaft having a center of rotation about the central axis and an outer circumference; a rupture portion of the shaft having surface interruptions extending inwardly toward the center of rotation from the outer circumference, wherein the rupture portion of the shaft is disposed proximate the inlet; and an erosion portion of the shaft between the rupture portion of the shaft and the outlet, the erosion portion of the shaft having a smooth outer surface.
9. The device of claim 8, wherein the shaft comprises a substantially constant outer circumference.
10. The device of claim 9, wherein the erosion portion comprises a smooth outer surface along the substantially constant outer circumference.
11. The device of claim 9, wherein the one or more cooling channels is threaded.
12. The device of claim 11, further comprising: an elongated member removably installed into each of the one or more cooling channels.
13. The device of claim 11, wherein the interior surface of the one or more cooling channels comprise one or more surface irregularities to increase surface area of the interior surface to improve heat dissipation.
14. The device of claim 13, wherein the one or more surface irregularities comprise surface undulations.
15. The device of claim 8, wherein a dispersion of the mixture between the inner diameter of the housing and along substantially an entirety of a length of the shaft between the inlet and the outlet.
16. The device of claim 8, further comprising: one or more cooling channels disposed within the housing between the outer surface and the inner surface.
17. The device of claim 8, further comprising: a screw groove portion of the shaft proximate to the inlet and having helical channels to force the particles and the matrix towards the rupture portion.
18. A device to disperse particles within a matrix, the device comprising: a housing having a center axis, an outer surface an inner diameter, and an inner surface; an inlet in fluid connection with the housing configured to receive a mixture of the particles and the matrix; a shaft within the housing, the shaft having a length defined between the inlet and an outlet of the housing, one end of the length disposed at the inlet and an opposing end of the length disposed at the outlet, a substantially constant outer circumference and a center of rotation about the center axis; a rupture portion of the shaft having surface interruptions extending inwardly from the outer circumference, wherein the rupture portion of the shaft is disposed at the inlet of the housing; an erosion portion of the shaft extending along the length of the shaft between the rupture portion of the shaft and the opposing end at the outlet, the erosion portion of the shaft occupying and in communication with the outlet and having a smooth outer surface along the substantially constant outer circumference; one or more cooling channels disposed within the housing between the outer surface and the inner surface; an elongated member removably installed into each of the one or more cooling channels; one or more surface irregularities in the interior surface of the one or more cooling channels to increase surface area of the interior surface to improve heat dissipation; and a dispersion of the mixture between the inner diameter of the housing and along substantially an entirety of the length of the shaft between the inlet and the outlet.
19. The device of claim 18, wherein the one or more cooling channels is threaded.
20. The device of claim 18, further comprising: a screw groove portion of the shaft proximate to the inlet and having helical channels to force the particles and the matrix towards the rupture portion.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Illustrated embodiments of the disclosure are described in detail below with reference to the attached drawing figures, which are incorporated by reference herein, and where:
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
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(42) A motor 14 mounted on the frame 10 is operably connected to a mixer 16. A preferred embodiment includes a high horsepower electric motor, but the present disclosure contemplates the motor 14 may be powered by petrochemical, solar, stream, and the like. In the exemplary embodiment depicted in
(43) The mixer 16 may be secured to the frame 12 through any means commonly known in the art. For example, in the illustrated embodiment of
(44) Referring to
(45) The top portion 36, the middle portion 38, and the bottom portion 40 may be connected through a bolt 42 that extends through the three portions, as shown illustratively in
(46) The top portion 36 of the stator 26 is shown illustratively in
(47) With a top surface 50 of the top portion 36 of the stator 26 is a plurality of axial mounting holes 52. The plurality of axial mounting holes 52 are adapted to connect the coupler 30 shown illustratively in
(48) The top portion 36 of the stator 26 also has an inlet 54 for the polymer and/or nanoparticles. The location of the inlet 54 on the machine 10 is also shown illustratively in
(49) Referring to
(50) Furthermore, each of the cooling channels 56 may receive a cooling channel modifier 68, as shown illustratively in
(51) Referring to
(52) A lower portion 40 in accordance of an exemplary embodiment is illustrated in
(53) Referring back to
(54) The main portion 84 of the shaft 34 may contain a knurled region (or rupture region) 86 and a smooth region (or erosion region) 88. The knurled region 86 is disposed proximate to the inlet 54 relative to the smooth region 88. The knurled region 86 produces higher and more chaotic shearing forces to create aggressive mixing with higher flow rate. In a preferred embodiment, the knurled region 86 is approximately one-fourth the length of the main portion 84 of the shaft 34. The rupture region 86 was created shorter than the erosion region 88 because rupturing the agglomerations requires higher shear force and less time than erosion. In the erosion region, primary nanoparticle is continuously peeled apart from smaller aggregates in the erosion region, which requires more time and less energy. As mentioned above, the gap between the erosion region 88 and the stator 26 may be 0.1 millimeters. A gap between rupture region 86 and stator 26 may be a slightly smaller (e.g., approximately 0.02 millimeters smaller). In addition, the knurled region 86 assists in increasing the flow rate of the NPC within the mixer 16.
(55) The main portion 84 of the shaft 34 may include a screw groove region 90. The screw groove region 90 may be disposed adjacent to the knurled region 86 opposite the smooth region 88. The screw groove region 90 may further be disposed proximate to the inlet 54 relative to the knurled region 86. The screw groove region 90 assists in moving the polymer-nanoparticle mixture downwardly into the mixture (i.e., towards the knurled region 86). In an exemplary embodiment gap between shaft 34 and stator 26 in this screw groove region 90 may be a slightly smaller (e.g., approximately 0.03 millimeters smaller) than the rupture region.
(56) The middle portion 82 of the shaft 34 may be operable connected to a seal 92 and seal holder 94, as shown illustratively in
(57) An exemplary seal holder 94 is illustrated in
(58) In operation, a polymer nanoparticle (NPC) mixture (or separately) are fed into the inlet 54 of the stator 26. The motor 14 provides a rotational force to the shaft 34 via the interface at the axial ridge 114. The shaft 34 rotates at a high frequency. In an exemplary embodiment, the shaft 34 rotates at a frequency of 17,800 Hertz. The NPC mixture encounters the screw groove region 90 of the shaft 34, which forces the NPC mixture towards the knurled region 86. In the knurled region 86, the agglomerations within NPC mixture experience extraordinary shearing forces that rupture the same. Due to forces from NPC mixture present in the screw groove region 90 above, the NPC mixture is further forced down into the smooth region 88. The NPC mixture undergoes extremely efficient erosion, whereby the NPC mixture becomes highly exfoliated. Thereafter, the NPC mixture is discharged from the outlet 74 of the stator 26 and to the orienter, which is discussed in detail below.
(59) While in operation, fluid is pumped from a reservoir through couplers 64 and into the ports 58 of the top portion 36 of the stator 26. The fluid enters the cooling channels 56, wherein it encounters threading 66 and the cooling channel modifier 68. The fluid experiences heat transfer due to the increased surface area and turbulent now, thereby cooling the stator 26.
(60) The present disclosure also contemplate that the mixer 16 can used as a continuous heterogenic catalyst reactor, if shaft outside surface and the stator inside surface are coated with catalyst. In such an embodiment, the catalyst will not be fouled due to self-cleaning by the high shear stress.
(61) When the dispersed and exfoliated NPC mixture exits the outlet 74 of the stator 26, the mixture enters the orienter 120. Orientation does not require the high energy necessary for dispersion. In order to orient HARNPs within a polymer matrix requires fully developed steady laminar shear flow (FDSLSF). However, 10 get the FDSLSF is complicated due to surface roughness at the nanoscale. The orienter 120 of the present disclosure achieves FDSLSF by moving a moving plate 122 across a stationary plate 124 at a slight angle 121. In particular, the NPC mixture is disposed on a top surface 126 of the moving plate 122, after which the moving plate 122 travels at a slight angle 121 across the stationary plate 126 to orient the NPC based on the combination of shearing and extensional two-dimensional, drag-force-driven flow.
(62) An exemplary embodiment of the orienter 120 is illustrated in
(63) The stationary plate 124 is mounted on the frame 12. As illustrated in
(64) The inlet side distance between the moving plate 122 and stationary plate 124 may be 0.24 mm while the outlet side distance may be 0.1 mm. Further, the moving plate 122 may decline at approximately a three-degree angle 121 relative to horizontal, or may be parallel.
(65) The orienter 120 is in concurrent operation with the mixer 16 of the machine 10. In operation, the orienter 120 may receive a dispersed and exfoliated NPC mixture from mixer 16. The NPC mixture may descend onto the top surface 126 of the moving plate 122 through the force of gravity. The motor 130 drives the drive gear 132 that forces the moving plate 122 across the stationary plate 124, thereby exposing the NPC mixture to FDSLSF and/or to two-dimensional extending drag flow, thereby orienting the nanoparticles with the polymer mixture.
(66) In the illustrated embodiment, the cycling process of the moving plates 122 is not automated; i.e., an individual must manually remove the moving plate 122 from an end of the track 128 and replace it at a beginning of the track 128. The present disclosure envisions a fully automated system.
(67) Further, the moving plates lose heat during the continuous cycle. The moving plates need to cycle in closed area to prevent loose heat. The present disclosure envisions an enclosure that minimizes heat loss of the orienter 120.
(68) The resulting NPC is dispersed, exfoliated, and oriented. The examples of improved physical properties (and other testing results) are discussed in Appendix A, which is incorporated herein by reference in its entirety.
(69) The disclosure is not to be limited to the particular embodiments described herein. In particular, the disclosure contemplates numerous variations in the type of ways in which embodiments of the disclosure may be applied to disperse, exfoliate and orient high aspect nanoparticles with a polymer matrix. Further, the present disclosure contemplates that the mixer 16 and the orienter 120 of the HSTFM may be utilized separately as an independent mixer and orienter. The foregoing description has been presented for purposes of illustration and description. It is not intended to be an exhaustive list or limit any of the disclosure to the precise forms disclosed. It is contemplated that other alternatives or exemplary aspects that are considered included in the disclosure. The description is merely examples of embodiments, processes or methods of the disclosure. It is understood that any other modifications, substitutions, and/or additions may be made, which are within the intended spirit and scope of the disclosure. For the foregoing, it may be seen that the disclosure accomplishes at least all that is intended.
(70) The previous detailed description is of a small number of embodiments for implementing the disclosure and is not intended to be limiting in scope. The following to claims set forth a number of the embodiments of the disclosure with greater particularity.