Manifold designs, and flow control in multichannel microchannel devices
AssigneeVelocys, Inc.
InventorsSean Fitzgerald, Anna Tonkovich, Ravi Arora, Dongming Qiu, Thomas Yuschak, Laura Silva, Wm. Rogers, Kai Jarosch, Matthew Schmidt
Life of this patent
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Abstract
Novel manifolds and methods of flow through manifolds are described. Apparatus and techniques are described in which flow from a relatively large volume header is equally distributed to process channels. Methods of making laminated, microchannel devices are also described.
Claims35
Microchannel apparatus, comprising:
- a first channel extending in a first direction;
- a second channel extending in a second direction;
- and
- a third channel extending in the second direction;
- a fourth channel extending in the second direction;
- and
- a fifth channel extending in the second direction;
- wherein the first and second directions are substantially coplanar;
- wherein the second and third channels are adjacent and parallel;
- wherein the first channel is not parallel to either the second or third channels;
- wherein the first channel is connected to the second channel and the third channels via a first gate;
- wherein the third channel is positioned farther in the first direction than the second channel;
- wherein the third channel comprises a microchannel;
- wherein the second channel comprises a microchannel;
- wherein the second channel has an opening with a first cross-sectional area and the third channel has an opening with a second cross-sectional area;
- wherein the first gate has a cross-sectional area that is smaller than the sum of first and second cross-sectional areas and the wall cross-sectional area between them;
- wherein the fourth and fifth channels are adjacent and parallel;
- wherein the first channel is connected to the fourth channel and the fifth channels via a second gate;
- wherein the fourth and fifth channels are positioned farther in
- the first direction than the third channel;
- wherein the fourth channel comprises a microchannel;
- wherein the fifth channel comprises a microchannel;
- wherein the fourth channel has an opening with a third cross-sectional area and the fifth channel has an opening with a fourth cross-sectional area;
- wherein the second gate has a cross-sectional area that is smaller than the sum of third and fourth cross-sectional areas and the wall cross-sectional area between them;
- and
- wherein the cross-sectional area of the first gate differs from that of the cross-sectional area of the second gate.
A laminated device, comprising:
- a first layer comprising microchannels that end in a first crossbar;
- and
- a second layer comprising microchannels that end in a second crossbar;
- wherein the first crossbar defines at least a portion of one edge of an M2M manifold;
- wherein the second crossbar projects into the M2M manifold;
- wherein an interface between the microchannels in the second layer and the manifold is formed by an open gap between the first and second crossbars.
A method of distributing flow from a manifold through a connecting channel matrix, comprising:
- passing a fluid through a manifold inlet and into a manifold having the following characteristics:
- the height of the manifold (hM2M) is 2 mm or less;
- the length of the manifold (LM2M) is 7.5 cm or greater;
- the length of an optional straightening channel portion (L2) divided by LM2M is less than 6;
- passing the fluid into the manifold with a momentum (Mo) of at least 0.05
- maintaining the DPR2 ratio at 2 or greater or maintaining a DPR3 ratio of 0.9 or less;
- and
- distributing the fluid from the manifold into at least 2 channels which are connected to the manifold, with a quality index factor as a function of connecting channel areas of
- Q(Ra)=0.0008135Ra6−0.03114Ra5+0.4519Ra4−3.12Ra3+11.22Ra2−23.9Ra+39.09.
A method of distributing flow from a manifold through a connecting channel matrix, comprising:
- passing a fluid into a manifold having the following characteristics:
- the height of the manifold is 2 mm or less;
- the length of an optional straightening channel portion (L2) divided by LM2M is less than 6;
- with a FA value of less than 0.01
- FA
- =
- [
- 0.058
- +
- 0.0023
-
- (
- ln
-
-
- Re
- )
- 2
- ]
- 2
-
- D
- L
- M2M
- <
- 0.01
- maintaining the DPR2 ratio at 2 or greater or maintaining a DPR3 ratio of 0.9 or less;
- and
- distributing the fluid from the manifold into at least 2 channels, which are connected to the manifold, with a quality index factor as a function of connecting channel areas of Q2 equal to or less than 85% of the Qc function of connecting channel area ratio Ra and DPR1 of
- Qc(Ra,DPR1)=E1+E2+E4+E6+E8+E10+E12,
- where
- E1
- =
-
- 112.9
- +
- 1.261
-
- DPR
- 1
- 1
- +
- 0.3078
-
- DPR
- 1
- +
- 0.00353
-
- DPR
- 1
- 2
-
- [
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 10
- )
-
- (
- Ra
- -
- 12
- )
- (
- 1
- -
- 2
- )
-
- (
- 1
- -
- 4
- )
-
- (
- 1
- -
- 6
- )
-
- (
- 1
- -
- 8
- )
-
- (
- 1
- -
- 10
- )
-
- (
- 1
- -
- 12
- )
- ]
- E2
- =
-
- 91.73
- -
- 1.571
-
- DPR
- 1
- +
- 0.01701
-
- DPR
- 1
- 2
- 1
- +
- 0.2038
-
- DPR
- 1
- +
- 0.00193
-
- DPR
- 1
- 2
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 10
- )
-
- (
- Ra
- -
- 12
- )
- (
- 2
- -
- 1
- )
-
- (
- 2
- -
- 4
- )
-
- (
- 2
- -
- 6
- )
-
- (
- 2
- -
- 8
- )
-
- (
- 2
- -
- 10
- )
-
- (
- 2
- -
- 12
- )
- ]
- E4
- =
-
- 24.27
- -
- 4.943
-
- DPR
- 1
- +
- 0.3982
-
- DPR
- 1
- 2
- 1
- -
- 0.2395
-
- DPR
- 1
- +
- 0.03442
-
- DPR
- 1
- 2
- -
- 0.000006657
-
- DPR
- 1
- 3
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 10
- )
-
- (
- Ra
- -
- 12
- )
- (
- 4
- -
- 1
- )
-
- (
- 4
- -
- 2
- )
-
- (
- 4
- -
- 6
- )
-
- (
- 4
- -
- 8
- )
-
- (
- 4
- -
- 10
- )
-
- (
- 4
- -
- 12
- )
- ]
- E6
- =
-
- 29.23
- -
- 2.731
-
- DPR
- 1
- +
- 0.09734
-
- DPR
- 1
- 2
- 1
- -
- 0.1124
-
- DPR
- 1
- +
- 0.005045
-
- DPR
- 1
- 2
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 10
- )
-
- (
- Ra
- -
- 12
- )
- (
- 6
- -
- 1
- )
-
- (
- 6
- -
- 2
- )
-
- (
- 6
- -
- 4
- )
-
- (
- 6
- -
- 8
- )
-
- (
- 6
- -
- 10
- )
-
- (
- 6
- -
- 12
- )
- ]
- E8
- =
-
- 25.98
- +
- 11.26
-
- DPR
- 1
- +
- 0.02201
-
- DPR
- 1
- 2
- +
- 0.5231
-
- DPR
- 1
- 3
- 1
- -
- 0.8557
-
- DPR
- 1
- +
- 0.00887
-
- DPR
- 1
- 2
- +
- 0.02049
-
- DPR
- 1
- 3
- -
- 0.000002866
-
- DPR
- 1
- 4
- ×
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 10
- )
-
- (
- Ra
- -
- 12
- )
- (
- 8
- -
- 1
- )
-
- (
- 8
- -
- 2
- )
-
- (
- 8
- -
- 4
- )
-
- (
- 8
- -
- 6
- )
-
- (
- 8
- -
- 10
- )
-
- (
- 8
- -
- 12
- )
- ]
- E10
- =
-
- 20.75
- -
- 3.371
-
- DPR
- 1
- +
- 0.9026
-
- DPR
- 1
- 2
- +
- 0.01277
-
- DPR
- 1
- 3
- 1
- -
- 0.1514
-
- DPR
- 1
- +
- 0.03173
-
- DPR
- 1
- 2
- +
- 0.0003673
-
- DPR
- 1
- 3
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 12
- )
- (
- 10
- -
- 1
- )
-
- (
- 10
- -
- 2
- )
-
- (
- 10
- -
- 4
- )
-
- (
- 10
- -
- 6
- )
-
- (
- 10
- -
- 8
- )
-
- (
- 10
- -
- 12
- )
- ]
- E12
- =
-
- 51.67
- +
- 18.94
-
- DPR
- 1
- +
- 21.57
-
- DPR
- 1
- 2
- +
- 21.57
-
- DPR
- 1
- 3
- 1
- +
- 1.183
-
- DPR
- 1
- +
- 0.5513
-
- DPR
- 1
- 2
- -
- 0.00004359
-
- DPR
- 1
- 3
-
- [
- (
- Ra
- -
- 1
- )
-
- (
- Ra
- -
- 2
- )
-
- (
- Ra
- -
- 4
- )
-
- (
- Ra
- -
- 6
- )
-
- (
- Ra
- -
- 8
- )
-
- (
- Ra
- -
- 10
- )
- (
- 12
- -
- 1
- )
-
- (
- 12
- -
- 2
- )
-
- (
- 12
- -
- 4
- )
-
- (
- 12
- -
- 6
- )
-
- (
- 12
- -
- 8
- )
-
- (
- 12
- -
- 10
- )
- ]
- where Ra ranges from 1 to 12, and DPR1 is greater than 0 and less than 300.
A method of distributing flow from a manifold through a connecting channel matrix, comprising:
- passing a fluid through a manifold and into a connecting channel matrix,
- wherein the connecting channel matrix comprises repeating units of microchannels of differing cross-sectional areas, and wherein the manifold has an inlet disposed on one side of the connecting channel matrix so that fluid flow through the manifold is at a nonzero angle to flow in the connecting channel matrix;
- wherein the connecting channels in two or more repeating units do not change in cross-sectional area in the direction of length through the manifold;
- and wherein a fluid flows into the manifold with a momentum (Mo) of at least 0.05;
- and is distributed through the connecting channel matrix with a Q2 of less than 30%.
A method of distributing flow from a manifold through a connecting channel matrix, comprising:
- passing a fluid through a manifold inlet and into a manifold such that the fluid passes through a first portion of a manifold in a first flow regime and passes through a second portion of a manifold in a second flow regime
- wherein the manifold manifold has the following characteristics:
- the height of the manifold (hM2M) is 2 mm or less;
- the length of an optional straightening channel portion (L2) divided by LM2M is less than 6;
- maintaining the DPR2 ratio at 2 or greater or maintaining a DPR3 ratio of 0.9 or less;
- and
- distributing the fluid from the manifold into at least 2 channels, which are connected to the manifold, with a quality index factor as a function of connecting channel areas of
- Q(Ra)=0.0008135Ra6−0.03114Ra5+0.4519Ra4−3.12Ra3+11.22Ra2−23.9Ra+39.09.
A method of passing a fluid through a manifold of a microchannel device, comprising:
- flowing a first fluid stream into a manifold and then through a first channel in a first direction;
- flowing a portion of the first fluid stream to a second channel;
- and
- flowing a portion of the first fluid stream through the second channel;
- wherein the second channel extends at a nonzero angle relative to the first direction;
- wherein the second channel comprises a microchannel and comprises at least one dividing wall that separates the second channel into at least a first and a second subchannel;
- wherein the first layer and the manifold are each substantially planar;
- wherein the manifold is substantially contained within the first layer, and wherein the first layer and the manifold are substantially coplanar, and wherein the first channel is disposed in the first layer and flow through the first channel is substantially parallel to the plane of the first layer;
- wherein the first channel and the manifold are about the same height;
- wherein the second layer is substantially planar, and wherein the second channel is disposed in the second layer and flow through the second channel is substantially parallel to the plane of the second layer;
- and
- wherein the first layer and the second layer are substantially parallel and the nonzero angle refers to an angle within the second layer.
A fluid processing device comprising:
- an inlet to a chamber;
- a louver disposed within the chamber;
- and
- an outlet from the chamber.
Dependencies are inferred from the claim text.