1. Field of the Invention
Embodiments of the present invention relate to a tube and shell reactor design capable of being operated in an up flow or down flow configuration.
More particularly, embodiments of the present invention relate to a tube and shell reactor design capable of being operated in an up flow or down flow configuration, where the reactor includes a plurality of tubes arranged within a shell so that the tubes may be heated or cooled as required for the purpose of controlling the temperature of materials that are contained within the tubes; furthermore, the reactor components include a top and bottom screen capable of retaining a catalyst within the tubes while permitting reactants and products to flow through them.
2. Description of the Related Art
Various reactor systems for use in catalytic reactions, especially reactors using resin bead based catalysts have been proposed, built and used, but all have certain draw backs.
There remains a need in the art for reactors that are economical; simple to build, operate, and maintain; and that may be changed from up flow to down flow without having to modify the reactor or replace components.
Embodiments of this present invention relate to reactors for performing chemical reactions equally well in an up flow or a down flow orientation and are capable of routine flow reversals without modification, a capability which may have utility, for example, for the purpose of regenerating catalyst particles, or dislodging catalyst particles from filters thereby extending the service life of the filters. This design will avoid premature replacement of catalyst or replacement of filters avoiding untimely shutdown of the process.
Tube and Shell Core
The reactors include a tube and shell core having a top, a bottom, a plurality of tubes designed to contain a catalyst and a closed shell surrounding the tubes. The shell includes inlets and outlets for circulating a heat transfer fluid through the shell for either heating or cooling the tubes. The core end flanges each incorporate a recess between the sealing surface of the flange and the ends of the tubes, where the ends of the tubes terminate in a planar arrangement that either protrudes into the recess or simply ends flush with the bottom of the recesses. Each core end flange incorporates a lip that includes a plurality of fastener apertures.
Screens
The reactors also include screens that are assembled with screen flanges, where both screens and screen flanges are substantially the same for both ends of the reactor. The screens are comprised of geometrical elements having a narrow or pointed side and a polygonal flat side. The geometrical elements are arrayed so their flat sides describe a plane and gaps between adjacent elements are smaller than the smallest diameter of the catalyst particles. The screens are designed for assembly into the reactor so that the flat sides of the geometrical elements face the tube openings and thereby prevent passage of catalyst from the core into the head assemblies. In certain embodiments, the flat sides of the geometrical elements are installed flush or substantially flush with the ends of the tubes in the core. In other embodiments, the flat sides of the geometrical elements are spaced away from the tube ends to thereby create a lateral flow annular gap for reduced restriction entering or exiting the tubes.
Screen Flanges
The reactors also include screen flanges for holding the upper and lower screens, where the screen flanges are configured for each to be captured within recesses of either or both of the head flanges and reactor flanges during the process of assembling the respective head onto the core within the recesses of either or both of the head flanges and reactor flanges.
Head Assemblies
The reactor also includes head assemblies that are designed with head flange details that can be the same for both heads. Each head assembly also includes a flange that incorporates a lip having a plurality of fasteners apertures which register with the fastener apertures in the lip of a core flange so that the head assemblies may be mounted on the top and bottom of the reactor core. The head assemblies also include straight sections and domed sections. The domed section for each head assembly includes a port disposed substantially at the center, where a reactant stream can be fed into the port of the first head assembly and a product stream can then be withdrawn from the port of the second head assembly. The head assemblies also each include a baffle element for distributing the flow of the incoming reactant stream across the screen surface, the flow then passing through the screen and into the tubes. In certain embodiments, the baffle elements are designed to form a substantially uniform flow of reactants across the screen surface.
Gaskets
The reactors also include gaskets that are disposed between the core end flange sealing surface and the head assembly flange sealing surface so that when the head assemblies are mounted on the cores, the resulting couplings are fluid tight.
Catalyst Distribution with the Reactors
The reactor core of this invention is designed to operate with a catalyst retained therein by screens where the catalyst fills or substantially fills all tubes and all contiguous volumes bounded between the screens so that the resulting void volume is approximately equal to the void volume of close packed catalyst particles.
Operation
Flowing reactant is introduced to flow through the port of the first head, become distributed by the first baffle to flow across the first screen, flow through the first screen, flow through the catalyst behind the first screen, flow through the catalyst contained in the tubes, flow through the catalyst contained between the ends of the tubes and the second screen, flow through the second screen, and into the second head while leaving the catalyst behind, and then flow to exit through the port in the second head.
Embodiments of this invention relate to methods for assembling the reactor of this invention including the steps required for inserting the screen.
The methods also include disposing a bottom gasket on the bottom head assembly flange sealing surface, mounting the bottom head assembly onto the core bottom so the apertures in the lips register, inserting fasteners into the apertures, and securing the bottom assembly to the bottom of the core so that the bottom assembly flange sealing surface, the bottom gasket, and the bottom core flange sealing surface form a first fluid tight coupling and the bottom screen is captured in place.
The methods also include filling the reactor from the top with a catalyst, where the amount of catalyst is sufficient to fill the total volumetric capacity of the reactor contained between the catalyst retention faces of the two screens with a resulting void volume that is approximately equal to the void volume of close packed catalyst particles.
The methods also include inserting a screen and flange assembly into the top recess of the core flange (or resting the screen and flange assembly atop the core flange if such a recess is not present). The methods also include disposing a top gasket atop the top core flange sealing surface, mounting the top head assembly onto the core top flange so the apertures in the lips register, inserting fasteners into the apertures, and securing the top assembly to the top of the core so that the top core flange sealing surface, the top gasket, and the top head assembly flange sealing surface form a top fluid tight coupling and captures the top screen in place. The screens and assemblies are substantially identical so that a flow through the reactor may enter from either end (that is, up-flow or down-flow in the case of a vertically oriented reactor) without modifying the reactor and the flow may be reversed by switching the flow direction without modifying the reactor.
Embodiments of this present invention relate to a method for operating a reactor of this invention. The methods include the step of feeding a reactant stream into the inlet port of the top or bottom assembly. The methods also include intercepting the flow of the incoming reactant stream with a flow baffle element to disperse the reactant flow across the screen. In certain embodiments, the dispersed flow is uniform or substantially uniform across the screen so that each tube receives substantially the same reactant flow rate, where the term substantially here means that the flow rates through the tubes differ by no more that 20%; in some embodiments, no more than 15%; in other embodiments no more than 10%; and in yet other embodiments, no more that 5%. In certain embodiments, the flow rate of the reactant stream is sufficiently high so that the reactant flow through each tube is turbulent, thereby prompting or maximizing reactant and product mass transfer in or off the catalyst surfaces and/or into and out of the catalyst interior. In other embodiments, the flow rate may be adjusted so that the flow through the tube is laminar. In other embodiments, the flow rate may be variable. In all case, the flow of reactants through the tubes may be controlled by the reactant feed rate and the nature of the flow baffle element. The methods also include withdrawing a product stream from the outlet port of the other assembly. The methods may also include recycling a portion of the product stream. The methods may also periodically, semi-periodically, or intermittently reverse the flow of materials through the reactor in order to dislodge fugitive catalyst particles from the filters thereby possibly extending filter maintenance and/or filter replacement service intervals, regenerate catalyst, dislodge catalyst particles from the filters thereby potentially extending catalyst useable lifetimes and/or reduce catalyst regeneration cycle times. In certain embodiments, the flushing material may be the reactants used in the reaction or an inert stream. In other embodiments, periodic, semi-periodic, or intermittent flow reversal may be performed during normal operations by lowering the tube temperature below the reaction temperature and then reversing the flow again, raising the temperature of the tubes to reaction temperature and continuing the reaction.
The invention can be better understood with reference to the following detailed description together with the appended illustrative drawings in which like elements are numbered the same:
The inventors have found that a tube and shell reactor can be constructed that has top to bottom symmetry so that the reactor is capable of being operated in an up flow configuration or down flow configuration without having to modify the reactor or elements of the reactor. The inventors have found that the top to bottom symmetry allows the reactant flow through the reactor to be reversed allowing filters and/or screens clearing of fugitive catalyst particles without disassembly or other disruptive operations. Reversing the flow permits the dislodging of fugitive particles from filters possibly extending filter maintenance and/or replacement service intervals thereby reducing the need for downtime resulting from actual filter maintenance
Embodiments of this invention broadly relate to top to bottom symmetric reactors for carrying out catalytic reactions. The reactors include a reactor core including a plurality of tubes and a surrounding shell. The core also includes a top flange with lip, a bottom flange with lip, a top recess and a bottom recess. Alternately, the flanges may be configured with or without recesses depending upon the configuration of the top and bottom head flanges. The lips include fastener apertures. The reactors also include a top and bottom head assembly that is mounted to the top and bottom of the core. The two head assemblies can be identical so that the final assembled reactor can be symmetrical top to bottom. The shell includes ports for circulating a cooling fluid or heating fluid into the reactor core for heating or cooling the tubes. In certain embodiments, the coolant is circulated through the shell in order to control temperatures within the tubes. The symmetric top/bottom reactor designs permit reactor operation in either an up-flow or down-flow configuration with equal ease, without having to change any reactor components. This design feature permits the reactant flow through the reactor to be reversed and dislodge fugitive particles from filters with the reversed flow possibly extending filter maintenance and/or filter replacement service intervals reducing the need for downtime resulting from actual filter maintenance. The top/bottom symmetric designs also permits interchangeability of screens, heads, gaskets, etc. of the top and bottom assemblies thereby streamlining installation because parts can generally be harmlessly interchanged. The interchangeability of parts also simplifies ordering and inventory control.
The top and bottom head assemblies include a flange with sealing surface and bolting lip, a straight section, and a domed section. The lips include fastener apertures, designed to register with the fastener apertures of the core flange lips. The domed section for each head includes a port for supplying (or withdrawing) reactants (product) into (out of) the reactor. The assemblies also include screen flanges with catalyst retention screens, and sealing gaskets. The screen flanges with catalyst retention screens are designed to be disposed into the recesses of the core flanges. The gaskets are designed to be disposed between the sealing surfaces of the head assembly flanges and the core flanges to form a fluid tight seal when fasteners are inserted into the lip fastener apertures and tightened. Each screen is designed to permit reactants and products to flow into and out of the reactor core and tubes while retaining the catalyst within. The screens are disposed so that the faces of the screens comprised of the flat sides of the screen elements are flush with the tubes; but, in some designs there is a gap between the faces of the screens and the tubes openings that provides a transverse flow area leading to the tube entrances for ensuring unobstructed inflow from all points in the neighborhood of the tube opening. The screen and reactor designs are compatible with tube configurations that either project beyond the surface of the core flange or are flush with it.
In the embodiment of the screens, the screens are formed of a pattern of geometrical elements having a sharp side when examined from one direction, say when viewed from above for a top screen, and a flat side when examined from the opposite direction, say when viewed from below for a top screen, where the geometrical elements are arrayed so their flat sides describe a plane and the gaps between the elements (element gaps) are at least 10% smaller than a smallest dimension of the catalyst particles. In other embodiments, the gaps between the elements are at least 20% smaller than the smallest dimension of the catalyst. In other embodiments, the gaps between the elements are at least 30% smaller than the smallest dimension of the catalyst. In other embodiments, the gaps between the elements are at least 40% smaller than the smallest dimension of the catalyst. In other embodiments, the gaps between the elements are at least 50% smaller than the smallest dimension of the catalyst. Each screen is structured with all the elements oriented with the flat sides facing in the same direction. The screens are then oriented with the flat sides of the elements oriented toward the tubes. The geometrical elements may be conical elements (cones), polygonal pyramidal elements, or wedge profile linear elements. Suitable polygonal pyramidal elements include regular polygonal pyramids and star shaped polygonal pyramids. Suitable regular polygonal pyramids include tetrahedra or distorted tetrahedra, square pyramids and distorted square pyramids, pentagonal pyramids and distorted pentagonal pyramids, hexagonal pyramids and distorted hexagonal pyramids, octagonal pyramids and distorted octagonal pyramids, higher order polygonal pyramids and distorted higher order polygonal pyramids, and suitable combinations thereof. Suitable wedge shapes include convex side, flat side, and concave side wedge shapes. The screens are designed to require no additional gaskets or fasteners as a screen is designed to be held with the screen flange which during assembly becomes captured within a recess located in either or both of the top and bottom flange of the reactor core and the top and bottom head assembly flange.
The reactors also include reactor flanges that are designed in concert with screen flange design(s) in order that both the flange gasket and screen are secure and aligned during handling, assembly, and disassembly. The reactors also include at least one flow baffle disposed near the inlet to disperse the inlet flow more or less uniformly across the tubes in order to maximize catalyst utilization. In certain embodiments, the flow baffle includes a perforated disk attached via welded legs inside each head a distance 6 from the inlet port. The baffles are designed to disperse the flow of incoming reactants and then distribute it across the first screen for a more or less even flow and pressure distribution across all tubes. Both head assemblies include a flow baffle so that the reactor may be easily switched between up flow and down flow operation.
Embodiments of this invention relate also to screen assemblies including (a) screen flange and a screen, where the screen is adapted to be affixed to a screen shoulder of the flange. The affixing may be by, without limitation, welding such as spot welding, forge welding, TIG welding, MIG welding, etc., gluing, cold forging, hot forging, forging so that the screen and/or flange materials become deformed and the screen is retains due to the deformation, or any other similar method for affixing or secures the screen to the flange. In certain embodiments, the screen assembly may include a screen retaining member or ring that is placed on top of the screen after the screen is disposed on the flange and welded to the flange. In other embodiments, the screen assembly is of a unitary construction, where the circumference of the screen constitutes the flange. In other embodiments, the flange is molded or cast onto an outer edge of the screen to produce a unitary screen assembly.
Embodiments of this invention relate to reactors that include (a) a core, (b) two head assemblies, (c) two screen assemblies, and (d) a core flange recess and/or a head flange recess adapted to receive the screen assembly. The core includes: (1) a plurality of reactor tubes, each tube having a first tube end and a second tube end, (2) a first core end flange and a second core end flange, each end flange including a core sealing surface, (3) a pattern of tube apertures disposed in each flange for locating the reactor tubes, (4) a core flange lip having apertures there through, (5) a flange gasket, and (6) fasteners. Each head assembly includes: (1) a head flange including an assembly sealing surface, a head flange lip having a plurality of apertures therethrough, and an optional head flange recess, (2) a cap section including an inlet port and an outlet port for flowing a reactant into and out of the reactor, and (3) an interior. Each screen assembly includes: (1) a screen comprising a plurality of screen elements, and (2) a screen mounting flange characterized by an inside diameter, an outside diameter, a projected minor diameter, an overall thickness, and a shoulder height. The tubes are fixed in place within the tube apertures; the screen is or the screen elements are affixed to the screen flange to form the screen assembly; the gasket is interposed between the sealing surfaces; and the head assembly is seated on the core end flange so that the lip apertures of the core and the assembly are aligned and the fasteners are inserted through the lip apertures of the core and the assembly retains the gasket and screen assembly within and tightening the fasteners compresses the gasket creating a fluid tight seal between the core and the head assembly. The reactor design permits the reactor to be operated in a down flow arrangement or an up flow arrangement simply by changing a reactant flow direction due to a top to bottom symmetry of the reactor.
In certain embodiments, the reactor includes a core flange recess. In other embodiments, the reactor includes a head flange recess. In other embodiments, the screen flange outside diameter corresponds to and self locates within the screen flange recess of the core end flange, the screen flange projected minor diameter corresponds to and self locates within the screen flange recess of the head assembly. The gasket has an inside diameter that corresponds to and self locates on the screen flange projected diameter, a portion of the gasket material that extends inwardly beyond the sealing surface of the core end flange rests against the screen flange axial retention face, a shoulder created by the radial difference between the screen flange outside and projected diameter, and compresses when tightening the flange lip fasteners which presses the screen flange axially against the screen flange recess axial face thereby minimizing any gaps.
In other embodiments, the screen flange shoulder height corresponds to the depth of the screen flange recess of the core end flange. In other embodiments, the screen assembly is seated within the head assembly screen flange recess. In other embodiments, the gasket does not include a portion that extends past the sealing surface of core flange for pressing and holding the screen flange in axial contact, but includes a second compressible component for the purpose interposed between the screen flange and the core end flange. In other embodiments, the screen assembly further includes ribs for reinforcing, and/or for mounting, and unmounting the screen or screen assembly. In other embodiments, the ribs include holes, lugs, and/or flanges to assist screen handling. In other embodiments, the screen assembly is partially or wholly retained by a dowel assembly. In other embodiments, the reactor also further comprises top and bottom flow volumes are bounded between the screens and the tube ends and the ends of the core baffle, where the volumes are defined by a first gap height g between the screen flat ends and the tube ends and a second gap height r between the screen flat ends and the baffle tops, where the gaps g and r may be the same or different. In other embodiments, the reactor of claim further includes a catalyst loaded into the reactor in an amount sufficient to substantially fill the tubes and the flow volumes during normal reactor operation. In other embodiments, each head assembly further includes a flow baffle assembly mounted within the interior for distributing incoming reactant to the tubes of the reactor. In other embodiments, the flow baffles include flow pathways therethrough. In other embodiments, the reactor further includes a shell surrounding the tubes and including an interior, and shell ports for circulating a heating or cooling fluid through the interior of the shell.
In other embodiments, the tubes have a geometrical cross-section and are arranged in a tube pattern having a packing efficiency within an geometrical shell, where tube cross-section and the envelop cross-section geometrical shapes are selected from the group consisting of circular, elliptical, polygonal, and mixtures thereof.
Embodiments of this invention relate to method for using the reactor including the steps of providing a top to bottom reversible flow reactor of this invention. The methods also includes the steps of loading a catalyst into the reactor in an amount sufficient to substantially fill the tubes and the flow volumes and feeding a reactant stream into one of the ports of one of the head assemblies. The methods also include the steps of contacting the reactant with the catalyst in the tubes and the flow volumes, and withdrawing a product stream through one of the ports of the other head assembly. In other embodiments, the method further include the steps of stopping the reactant flow, and starting a flow of a reverse flow stream in an opposite flow direction to the reactant flow direction on an intermittent or periodic basis, where the reverse flow operates to clear the screens reducing maintenance In other embodiments, the methods further include the step of regenerating the catalyst during reverse flow, where the reverse flow stream is a catalyst regeneration stream and regeneration extends catalyst life. In other embodiments, the methods further includes the step of prior to the contacting step, distributing the reactant flow across the volumes and the tubes via a flow baffle to improve flow uniformity through the tubes.
Embodiments of this invention relate to a screen assembly including a screen comprising a plurality of screen elements, and a screen mounting flange characterized by an inside diameter, an outside diameter, a projected minor diameter, an overall thickness, and a shoulder height, and a core flange recess and/or a head flange recess adapted to receive the screen assembly, where the screen is or the screen elements are affixed to the screen flange to form the screen assembly.
Illustrative Embodiments Including Sacrificial Components and/or Coatings
In certain embodiments, where the reactants supplied to and/or products generated in the reactor may include corrosive components, the reactor may include additional components and/or coatings that act as sacrificial corrosion sites. Such sacrificial components may be used in reactor applications prone to crevice corrosion such as that induced within small openings (crevices) where two metal surfaces come into close proximity or actual contact, including where the two metal surfaces are of metal having the same or substantially the same galvanic potential. The sacrificial components and/or coatings are generally constructed out of materials having a lower galvanic potential than the materials that are to be protected by the sacrificial components and/or coating. For example, if the tubes, core flanges and head flanges are made of stainless steel, then the screen flange may be made of a lower galvanic potential iron alloy so that corrosion preferentially affects the aforementioned iron alloy flanges. Alternatively, surfaces of the core flanges and/or the head flanges may be coated with a sacrificial coating. In another alternative, surfaces of the screen flange may be coated with a sacrificial coating. In yet another embodiment, a sacrificial component may be interposed between contacting surfaces or simply placed in the flow volumes provided that the component does not interfere with reactant or product flow. In yet another embodiment, the flow baffle may be made of a sacrificial material.
Suitable materials out of which the core flanges and tube may be constructed include, without limitation, iron and iron alloys. Exemplary iron alloys include, without limitation, Elinvar (nickel, chromium); Fernico (nickel, cobalt); ferroalloys such as ferroboron, ferrochrome, ferromagnesium, ferromanganese, ferromolybdenum, ferronickel, ferrophosphorus, ferrosilicon, ferrotitanium, and ferrovanadium; Invar (nickel); cast iron (carbon); pig iron (carbon); wrought iron (carbon); Kovar (nickel; cobalt); Spiegeleisen (manganese; carbon; silicon); steel; bulat steel, Chromoly (chromium; molybdenum); crucible steel; Damascus steel; high speed steel; Mushet steel; HSLA steel; Maraging steel; Reynolds 531; silicon steel (silicon); spring steel; stainless steel (chromium, nickel) such as AL-6XN, Alloy 20, celestrium, marine grade stainless, martensitic stainless steel, surgical stainless steel (chromium, molybdenum; nickel), and Zeron 100 (chromium, nickel, molybdenum); tool steel (tungsten or manganese); silver steel (US:Drill rod) (manganese, chromium, silicon); Wootz steel; or mixtures and combinations thereof.
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The core 110 includes a first end flange 112, a second end flange 114, a plurality of reaction tubes 116, and a shell 118 surrounding the tubes 116. Each tube 116 includes a first end 120 and second end 122. The shell 118 includes a first port 124 and a second port 126 for circulating a heating fluid or cooling fluid through an interior 128 of the shell 118 for heating and/or cooling the tubes 116. The first end flange 112 and the second end flange 114 of the core 110. The flanges 112 and 114 include lips 130 and fastener apertures 132 therethrough. The tubes 116 are arranged in a pattern 134 as shown in
The reactor 100 also includes a first head assembly and a second head assembly, both designated 140. Each head assembly 140 includes a head assembly flange 142, which includes a lip 144 having fastener apertures 146 (shown in
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The tabulated dimensions are guidelines. Actual dimensions of h, w, l, ss, and r may be successfully varied within and beyond these ranges depending on the reactor design by a person skilled in the art.
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The tabulated dimensions are guidelines. Actual dimensions of h, w, l, ss, r, and sh may be successfully varied within and beyond these ranges depending on the reactor design by a person skilled in the art.
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The tabulated dimensions are guidelines. Actual dimensions of h, w, l, ss, r, sh, gb, and go may be successfully varied within and beyond these ranges depending on the reactor design by a person skilled in the art.
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In all the screen flange embodiments disclosed above, the screen flanges may be inverted so that the recesses in the core flange and the head assembly flange are inverted and the screen flanges are designed to register with the inverted screen flange.
All references cited herein are incorporated by reference. Although the invention has been disclosed with reference to its preferred embodiments, from reading this description those of skill in the art may appreciate changes and modification that may be made which do not depart from the scope and spirit of the invention as described above and claimed hereafter.