The present disclosure relates to honeycomb structures used as reactors or heat exchangers, or “minireactors” formed into an array, and particularly to methods of joining the structures so as to form channels through the array in a direction perpendicular to the common direction of the honeycomb cells and to the resulting arrays.
In forming an array or honeycomb devices for use as a reactor or reactor array, channels may be machined into selected side faces of honeycomb substrates so that when the substrates are joined together one or more high aspect ratio channels are formed through the array in a direction perpendicular to the common direction of the honeycomb cells. Substrates may be joined together using a frit or a cement, or even a compression seal if desired, on selected side faces.
According to one embodiment, an array of honeycomb substrates comprises honeycomb substrates, a plurality of which have, for each substrate, substrate cells extending from a first end of the respective substrate to a second end and substrate sides extending from the first end to the second end. The substrates of the plurality are arranged in an array with sides of respective substrates facing one another and cells of respective substrates extending in a common direction. One or more channels are defined between facing substrate sides of two or more substrates of the plurality, and the one or more channels extend in a direction perpendicular to the common direction.
According to another embodiment, an array of honeycomb substrates comprises honeycomb substrates, a plurality of which have, for each substrate, substrate cells extending from a first end of the respective substrate to a second end and substrate sides extending from the first end to the second end. The substrates of the plurality are arranged in an array with sides of respective substrates facing one another and cells of respective substrates extending in a common direction. One or more channels are defined along the cells of two or more substrates of the plurality of substrates, and the channels extend from within a first substrate of the plurality through a substrate side thereof into a second substrate of the plurality through a substrate side thereof. The respective sides through which the one or more channels pass may be sealed to each other.
According to yet another embodiment of the invention, a method is provided of making an array of honeycomb substrates, the method including providing a plurality of honeycomb substrates having side faces and machining channels into selected ones of the side faces of the plurality of honeycomb substrates, in a direction generally perpendicular to a substrate cell direction, then sealing the channels by sealing the selected of the side faces to other side faces of the plurality of honeycomb substrates. The method may further include machining channels into one or more other side faces of the plurality of honeycomb substrates, in a direction perpendicular to the substrate cell direction, prior to the step of sealing.
Among other uses or applications of these embodiments of the present invention is the provision of a very flexible method for incorporating cross-flow heat exchange channels in a large array of substrates, with the cross-flow channels having low pressure drop and a large open frontal area, resulting in large honeycomb-based heat exchangers, or reactors with heat exchange.
A machined channel 12 may be formed on one side face of a rectangular honeycomb substrate 10 as shown in
Next the substrate is sintered (assuming green-substrate channel machining operations). As shown in
Frit may be applied via various processes, including doctor-blading, screen-printing, spray application, or by use of frit preforms. By orienting a number of substrates 10 in a row with either end faces or selected side faces touching one another (not shown), the frit may be applied in a continuous process. In general frit application is required on at most two adjacent substrate side faces 26, 28, simplifying the application process since each substrate 10 can rest on a non-frit coated side face 30, 32 (not directly visible in
End face cells 16, 18 directly over or beneath the machined channel are also be plugged, with frit 34, or with other suitable plug material 34 (shown in cells 18 only) for alternative embodiments. This prevents unintended mixing of fluid flowing in machined channels with fluid flowing in the substrate's open cells. A frit paste may be applied to plug the cells by first masking those cells which are to remain open, for example.
With reference to
After frit sintering a substrate array is formed that provides short straight channels in close proximity to a series of high aspect ratio cross-flow channels. The structure of such an array can be used as an efficient large area cross-flow heat exchanger. Overall heat transfer performance depends on thermal conductivity of the substrate material, the substrate channel layout and geometry, and the machined high aspect ratio channel geometry as well as working fluid properties.
In another aspect or alternative embodiment, the substrate channel machining operation can be performed on multiple side faces, as shown in
By selectively machining high aspect ratio channels into side faces of individual substrates, more complex channel routing configurations may be formed through the array. For example,
The substrate channel machining operation may also be performed on opposite substrate side faces 11a, 11c, as shown in
According to another embodiment of the present invention or according to another aspect which may optionally be applied to various of the embodiments disclosed herein, the substrates that make up the substrate array can have their end faces machined to form U-bend regions so as to form serpentine channels extending up and down along the direction of the cells of the substrate(s), traveling from cell to cell at or near the ends of the substrates and entering and exiting from the side of the substrate(s) or the side of the array, in the direction perpendicular to the open cells. An example of this is shown in
It is also possible to fabricate each substrate so only serpentine channels are provided.
As an alternative to drilling side face channel holes, the same end face U-bend region machining process illustrated in
Various combinations of side face machined high aspect ratio channels between substrates and end face machined serpentine U-bend channels may be combined together to form integrated manifold structures and channel layouts with optimized pressure drop and heat exchange performance. Other types of channels may also be formed in the substrate instead of U-bend serpentine channels, such as high aspect ratio channels formed by plunge machining operations, such as the high aspect ratio channel 124 depicted in cross-section in
As yet another embodiment of the present invention, high aspect ratio channels between substrates may be formed without machined channels or the need to machine substrates. Instead, the high aspect ratio channel regions may be formed by selective deposition of thick frit layers on one or more substrate sidewalls, or by use of shims, as represented in perspective view in
Within the various embodiments and variations thereof according to the present invention, proximity of high aspect ratio machined channels to short straight channels is easily adjusted by design to meet heat exchange requirements while maximizing open frontal area. Geometry of high aspect ratio channel and short straight channels can also be optimized to balance high heat transfer performance with low pressure drop. The various embodiments, particularly when frit seals are used, allow the short straight open cells of the substrates to operate at high pressures, with frit seals between substrates placed in compression or shear for maximum strength. The frit sealing area on substrate side faces can adjusted, increasing it as needed to increase mechanical strength at the fit-substrate interface.
Not as a limiting features, but as one potential benefits, the present invention can allow smaller substrates to be sintered individually in a short sintering cycle, relative to a long cycle required to sinter a single larger body. Even though a subsequent sintering cycle might be required if frit were used to join substrates together, this cycle would also be relatively short. Thus sintering time relative to device cross section may be reduced relative to large cross section honeycomb substrates. Flat side faces allow for simplified interfacing to other devices via bonded ports or O-ring seals. And substrate machining processes are relatively simple when only exterior channel forming operations are used. Such side face channel machining processes could be automated. Various high aspect ratio channels could also be laid out using a “mix and match” approach, where substrates with various side face machining patterns are joined together as needed to form the desired cross-flow heat exchange channel path.
Overall, the arrays of the present invention provide significant flexibility, since cross-flow heat exchange channels can be formed in relatively arbitrary sizes, both through side face channel machining as in some embodiments, and/or through internal substrate serpentine or high aspect ratio channels, as in other embodiments, and/or by the use of thick frit or shims and in the embodiment of
The arrays disclosed herein are generally useful in performing any process that involves mixing, separation, extraction, crystallization, precipitation, or otherwise processing fluids or mixtures of fluids, including multiphase mixtures of fluids—and including fluids or mixtures of fluids including multiphase mixtures of fluids that also contain solids—within a microstructure. The processing may include a physical process, a chemical reaction defined as a process that results in the interconversion of organic, inorganic, or both organic and inorganic species, a biochemical process, or any other form of processing. The following non-limiting list of reactions may be performed with the disclosed methods and/or devices: oxidation; reduction; substitution; elimination; addition; ligand exchange; metal exchange; and ion exchange. More specifically, reactions of any of the following non-limiting list may be performed with the disclosed methods and/or devices: polymerisation; alkylation; dealkylation; nitration; peroxidation; sulfoxidation; epoxidation; ammoxidation; hydrogenation; dehydrogenation; organometallic reactions; precious metal chemistry/homogeneous catalyst reactions; carbonylation; thiocarbonylation; alkoxylation; halogenation; dehydrohalogenation; dehalogenation; hydroformylation; carboxylation; decarboxylation; amination; arylation; peptide coupling; aldol condensation; cyclocondensation; dehydrocyclization; esterification; amidation; heterocyclic synthesis; dehydration; alcoholysis; hydrolysis; ammonolysis; etherification; enzymatic synthesis; ketalization; saponification; isomerisation; quaternization; formylation; phase transfer reactions; silylations; nitrile synthesis; phosphorylation; ozonolysis; azide chemistry; metathesis; hydrosilylation; coupling reactions; and enzymatic reactions.
Number | Date | Country | Kind |
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61174493 | Apr 2009 | US | national |
The present application claims priority to U.S. Provisional Patent Application No. 61174493, filed 30 Apr., 2009.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US10/33113 | 4/30/2010 | WO | 00 | 10/26/2011 |