NZ612924B2 - Improved stackable structural reactors - Google Patents
Improved stackable structural reactors Download PDFInfo
- Publication number
- NZ612924B2 NZ612924B2 NZ612924A NZ61292412A NZ612924B2 NZ 612924 B2 NZ612924 B2 NZ 612924B2 NZ 612924 A NZ612924 A NZ 612924A NZ 61292412 A NZ61292412 A NZ 61292412A NZ 612924 B2 NZ612924 B2 NZ 612924B2
- Authority
- NZ
- New Zealand
- Prior art keywords
- fan
- reactor
- washer
- outer diameter
- helix
- Prior art date
Links
- 239000012530 fluid Substances 0.000 claims abstract description 90
- 210000001331 Nose Anatomy 0.000 claims description 33
- 239000011888 foil Substances 0.000 description 50
- 229910052751 metal Inorganic materials 0.000 description 36
- 239000002184 metal Substances 0.000 description 36
- 239000003054 catalyst Substances 0.000 description 9
- 210000000887 Face Anatomy 0.000 description 8
- 239000000919 ceramic Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 239000008188 pellet Substances 0.000 description 6
- 239000011800 void material Substances 0.000 description 5
- 238000003466 welding Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000037250 Clearance Effects 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 229940035295 Ting Drugs 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 230000035512 clearance Effects 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 230000003197 catalytic Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- LBFUKZWYPLNNJC-UHFFFAOYSA-N Cobalt(II,III) oxide Chemical compound [Co]=O.O=[Co]O[Co]=O LBFUKZWYPLNNJC-UHFFFAOYSA-N 0.000 description 1
- 235000012571 Ficus glomerata Nutrition 0.000 description 1
- 240000000365 Ficus racemosa Species 0.000 description 1
- 241000229754 Iva xanthiifolia Species 0.000 description 1
- 239000005092 Ruthenium Substances 0.000 description 1
- 235000015125 Sterculia urens Nutrition 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N al2o3 Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000024881 catalytic activity Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing Effects 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000001771 impaired Effects 0.000 description 1
- 229910001026 inconel Inorganic materials 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 150000002843 nonmetals Chemical class 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
- B01J19/249—Plate-type reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/19—Details relating to the geometry of the reactor
- B01J2219/194—Details relating to the geometry of the reactor round
- B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
- B01J2219/1944—Details relating to the geometry of the reactor round circular or disk-shaped spiral
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2451—Geometry of the reactor
- B01J2219/2453—Plates arranged in parallel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2451—Geometry of the reactor
- B01J2219/2456—Geometry of the plates
- B01J2219/2459—Corrugated plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2461—Heat exchange aspects
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2476—Construction materials
- B01J2219/2477—Construction materials of the catalysts
- B01J2219/2479—Catalysts coated on the surface of plates or inserts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2476—Construction materials
- B01J2219/2483—Construction materials of the plates
- B01J2219/2485—Metals or alloys
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2491—Other constructional details
- B01J2219/2492—Assembling means
- B01J2219/2493—Means for assembling plates together, e.g. sealing means, screws, bolts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2491—Other constructional details
- B01J2219/2492—Assembling means
- B01J2219/2496—Means for assembling modules together, e.g. casings, holders, fluidic connectors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/322—Basic shape of the elements
- B01J2219/32203—Sheets
- B01J2219/3221—Corrugated sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/322—Basic shape of the elements
- B01J2219/32203—Sheets
- B01J2219/32224—Sheets characterised by the orientation of the sheet
- B01J2219/32231—Horizontal orientation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/324—Composition or microstructure of the elements
- B01J2219/32408—Metal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/324—Composition or microstructure of the elements
- B01J2219/32466—Composition or microstructure of the elements comprising catalytically active material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0242—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly vertical
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1005—Arrangement or shape of catalyst
- C01B2203/1035—Catalyst coated on equipment surfaces, e.g. reactor walls
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/14—Details of the flowsheet
- C01B2203/142—At least two reforming, decomposition or partial oxidation steps in series
- C01B2203/143—Three or more reforming, decomposition or partial oxidation steps in series
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/382—Multi-step processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
Abstract
reactor comprises a stationary fan 3 arranged on a central rod 11 in a reactor tube. The fan 3 has radial fluid ducts 13a, 13b for directing fluid flow through the reactor. The fluid ducts 13b act to radially guide the fluid flow to contact the reactor tube and promote heat transfer along the reactor tube. The fan 3 has a top surface, a bottom surface and an outer diameter face such that the radial fluid ducts 13a, 13b terminate along the outer diameter face of the fan 3 to form fluid duct openings facing the reactor tube. tor tube. The fan 3 has a top surface, a bottom surface and an outer diameter face such that the radial fluid ducts 13a, 13b terminate along the outer diameter face of the fan 3 to form fluid duct openings facing the reactor tube.
Description
W0 2012/103432 PCT/U52012/022888
Improved Stackable ural Reactors
FILED
The present inventions relate to improved ble structural reactors having increased
efficiency and productivity, and in particular, ed stackable structural reactors
having component arrangements for increased heat transfer and reaction efficiency.
BACKGROUND
Reformers, such as those used to produce hydrogen, generally contain reactor tubes
exposed to a heat source, for example a furnace, to support endothermic reactions. Other
types of reactions, such an exothermic, can require exposure to a cooling source, such as a
cooling jacket. r tubes can be loaded with ceramic s impregnated with
catalyst or having a catalyst coating for carrying out a reaction. The ceramic pellets break
and become damaged over time and can form a powder in the r tubes, which can
undesirably clog gas flow in the reactor tubes and negatively affect heat transfer.
Moreover, the ceramic pellets are limited in the amount of heat that can be transferred
throughout the reactor tube core. Low heat transfer from the heat source located outside
the reactor tubes necessitates high e temperatures, increased energy costs, and
reactor tube walls that can lead to shortened or impaired reactor tube life. Mal-
distribution of ceramic pellets in the core can create zones with poor reaction
characteristics and hot spots on the tube, leading to poor mance and/or life. Reactor
efficiency and productivity can be significantly reduced from the limited heat transfer and
gas flow disruptions caused by the inherent ties and structural limitations of
ceramic pellets.
Attempts by manufacturers to improve the ceramic pellets used in the reactor tubes have
marginally improved heat transfer and deterioration and thus there remains a need for an
improved catalyst support that promotes heat er, provides high surface area, and
provides low pressure drop and can be easily ented at a reduced cost. Various
embodiments of foil-supported sts for use in tubular reactors are discussed below.
BRIEF SUMMARY
In an aspect of the present invention there is provided a reactor comprising:
a stationary fan arranged on a central rod in a reactor tube, the fan having radial
fluid ducts for directing fluid flow h the r, the fluid ducts being effective
to ly guide the fluid flow to contact the reactor tube and promote heat transfer
along the reactor tube;
the fan having a top e, a bottom surface and an outer diameter face such
that the radial fluid ducts terminate along the outer diameter face of the fan to form
fluid duct openings facing the reactor tube.
In particular, in one or more embodiments there is provided a r for
carrying out catalytic reactions and comprising a fan arranged on a central rod in a
r tube. The fan can have radial fluid ducts for directing fluid flow through the
reactor. The fluid ducts are effective for radially guiding fluid flow towards the reactor
tube to assist in heat transfer. The fan has a top surface, bottom surface and an outer
diameter face. The radial fluid ducts, formed by ations in the fan, terminate
along the outer diameter face of the fan to form fluid duct openings, for example
triangular openings, that face the reactor tube wall and thus promote heat er from
the reactor tube into the interior ofthe reactor.
In a related embodiment there is provided stackable structural reactor (SSR). The
SSR typically comprises a reactor component that has a top e, bottom surface and
a circular outer diameter face. The reactor component can be arranged in a reactor
tube, for example on a central rod disposed in the interior region of the reactor tube. A
washer having an inner diameter and an outer diameter can be in contact with the top
or bottom surface of the reactor component. The washer can extend radially outward
from the circular outer diameter face of the reactor component such that the outer er
ofthe washer does not contact the reactor tube, thus creating a annular gap between the
reactor tube and the circular outer er of the washer.
Throughout this specification, the word “comprise”, or variations thereof such as
“comprises” or “comprising”, will be understood to imply the inclusion of a stated element,
3O integer or step, or group of elements rs or steps, but not the exclusion of any other
element, integer or step, or group of elements, integers or steps.
Any discussion of documents, acts, materials, devices, articles or the like which has
been included in this specification is solely for the purpose ofproviding a context for the
t invention. It is not to be taken as an admission that any or all of these matters form
part of the prior art base or were common general knowledge in the field relevant to the
present invention as it existed in New d or elsewhere before the priority date of this
application.
BRIEF DESCRIPTION OF THE DRAWINGS
The following figures illustrate various aspects of one or more embodiments, but
are not intended to limit the present inventions to the embodiments shown.
shows a section View of a reactor having a loaded reactor sleeve of an
alternating ement of fans and cores.
shows a side View of a loaded reactor sleeve of an alternating arrangement of
fans and cores arranged on a central rod for use in a reactor tube.
shows a perspective view of a core arranged on a central rod for use in a
reactor tube.
shows a perspective view of stacked fans having washers positioned
between each reactor fan for use in a reactor tube.
PCTIU52012/0228'
shows a perspective View of a fan having a washer attached to the top surface of
the fan.
shows a perspective view of a fan having a washer with spacing tabs attached to
the top e ofthe fan.
shows a perspective view of a portion of a fan having a corrugated washer
attached to the bottom surface ofthe fan.
shows a top View of a n of a castellated washer for use with a reactor
component.
shows a top view of a castellated washer attached to the top surface of a reactor
component.
shows a perspective View ofa castellated washer having spacing tabs for use with
reactor component.
shows a top View of a portion of a reactor ent having a castellated washer
adjacent o.
shows a perspective view of a portion of reactor component having a castellated
washer with spacing tabs attached thereto.
shows a top view of a portion of a castellated blank base plate for forming a
castellated washer or reactor ent.
shows a portion of a castellated washer formed from the castellated blank base
plate of .
A shows a side view of a loaded reactor sleeve of fans arranged vertically on a
central rod, wherein each fan has a single notch around its circumference.
B shows a side view of a loaded reactor sleeve of fans arranged vertically on a
central rod, wherein each fan has multiple notches around its circumference.
shows a side view of a loaded reactor sleeve of fans arranged vertically on a
l rod, wherein each fan has a single notch around its circumference.
shows a side view of a loaded reactor sleeve of fans arranged ally on a
central rod, wherein each fan has a single notch around its circumference.
shows a side View of a loaded reactor sleeve of alternating fans and
cores
arranged vertically on central rods, one central rod having a cavity portion adapted for
fitting with r central rod directly below.
shows a side view of a loaded reactor sleeve of alternating fans and
cores arranged vertically on a central rod support and bushing assembly adapted for fitting
with another central rod directly below.
shows a side view of a helix fan ed on a central rod for use in
r tube.
shows a cross-section view of a helix fan arranged on a central rod for
use in a reactor tube.
ED DESCRIPTION OF EXEMPLARY EIVIBODIMENTS
OF THE INVENTION
As used herein, when a range such as 5-25 is given, this means at least or more
than 5 and, separately and independently less than, and not more than 25. Materials of
construction for all reactor components or parts thereof as discussed herein can include
any suitable material as known in the art, for example, metal, non-ferrous metal, metal
foil, steel, stainless steel, alloys, foils, non-metals such as plastics or glass, ceramic, or
combinations thereof.
The reactors as described herein, sometimes referred to as a stackable structural
reactors ("SSR"), can e multiple components arranged around a center t, such
as a central rod or mandrel, pipe, post or the like in order to form a monolith of l
annular cross section as viewed in the direction of flow of fluid through the reactor. As
described herein, various ations and ments of the reactors and associated
reactor components can be used.
An example ure of a reactor 1 is shown in The reactor tube 2
having an inner diameter wall face 2a and an outer diameter wall face 2b, such as a
reformer tube, houses reactor components, such as a fan 3 and/or core 4, arranged on
central rod 5. The reactor tube 2 is generally known in the art and is preferably made of
metal, such as steel, ess steel, aluminum or Inconel, or special spun-cast alloys such as
HPSO; alternatively (and preferably if the reaction is a low temperature reaction like CO to
C02) made ofpolymeric or plastic material. It is preferably a tube having a circular,
W0 2012/103432 PCT/US2012I022888
gular, oval, or other cross—section. The length of the reactor tube 2 can be at least
0.6, l, 2, 4, 6, 8, 10 or 12 m and preferably in the range of 0.6 to 2 m or 6 to 15 m. The
r tube 2 can have a circular cross section with an inner diameter of at least 25, 50,
75, 100, 125, 150, 175, 200, 225 or 250 mm and preferably in the range of 80 to 140 mm.
The diameter ofthe reactor tube 2 is preferably constant along its entire length.
Reactor components, such as fans 3 and cores 4, are constructed to have a central hole or
aperture for receiving the central rod 5 such that the components can slide on the central
rod 5 and be positioned in the reactor tube 2. The central rod 5 can have a length to
odate the length of the reactor tube 2. Alternatively, multiple rods, such as 2 to
10 rods, can be used, for example in a stacking manner, to accommodate tube 2 length,
which can mitigate thermal expansion of components. The rod 5 can have a circular cross
section diameter of at least 5, 10, 25, 50, 75, 100, 125 or 150 mm and preferably in the
range of 6 to 40 mm. For fitting purposes, the r components can have a central hole
or aperture the same as or slightly greater than the circular cross section er of the
rod 5. The central rod 5 can further e a bracket, bushing, base plate and the like for
providing a stop fitting so the components 3, 4 do not slide off of the l rod 5. The
l rod 5 can be preloaded with any number of reactor components 3, 4 or washers
before being inserted in the reactor tube 2. As shown, the fans 3 and cores 4 can be
stacked vertically, one on top of r, to form alternating layers ofreactor components
such that each fan 3 is in contact with and arranged between two cores 4 located below
and above the fan 3. Washers as described below can be inserted between one or more
reactor components as desired, for example, each fan and core can be separated by a
washer wherein the washer creates an open space between the components.
atively, in contrast to alternating layers, the reactor components 3, 4 can be
arranged in any desirable manner, for instance the rod 5 can be loaded with all fans 3
without one or more cores 4.
Generally, 24 to 400 or more reactor ents can be arranged or stacked inside a
reactor tube 2, for example in any alternating manner, wherein the stacked arrangement
accommodates fluid flow through each reactor component located in the reactor tube 2.
In an example, a reactor tube for a fuel cell can contain 24 to 72 vertically-stacked reactor
components. In another example, a r tube for a en reformer can contain 200
to 400 or more vertically-stacked reactor components. Although reactor components are
PCT/US20l2/022888
shown vertically stacked herein, the components can be arranged in alternative ways such
as horizontal to accommodate orientation of a reactor or certain logy requirements.
Fluid, such as gas or liquid, to be reacted generally flows vertically, either up flow or
down flow as desired, through the reactor tube 2 and through each ent 3, 4
arranged on the central rod 5. Reactor components 3, 4 direct fluid flow in other non-
vertical directions to increase heat transfer, for example fans 3 direct or guide fluid flow
ly (perpendicular to the overall vertical direction) towards the reactor tube wall. As
shown, fluid enters the reactor tube 2 at g or inlet 7a, flows through the vertically-
ed fans 3 and cores 4, and exits the reactor tube 2 at opening 7b. The fans 3 and
cores 4 preferably have lateral dimensions so that each component 3, 4 will entirely or
substantially fill the cross-sectional area of the r tube 2. The fans 3 and cores 4 can
be in contact with the inner wall surface 2a of the reactor tube 2, which effectively
ers heat from the exterior of the r to the reactor components 3, 4 and fluid
contained n. The cross-sectional diameter, if circular, of a fan 3 can be at least 20,
50, 100, 150, 200 or 250 mm and preferably in the range of 80 to 135 mm. The fan 3 can
have a height of at least 7, 15, 30, 45, 60 or 65 mm and preferably in the range of20 to 40
mm. The cross-sectional diameter, if circular, of a core 4 can be at least 20, 50, 100, 150,
200 or 230 mm and preferably in the range of 60 to 120 mm. The core 4 can have a
height of at least 6, 15, 30, 45, 60 or 80 mm and preferably in the range of 10 to 30 mm.
Preferably, the fans 3 located within the reactor tube 2 have a diameter less than the inner
diameter of the reactor tube 2 to create a gap 8 or free space between the outer diameter
edge or face 3a of the fans 3 and the inner wall surface 2a of the reactor tube 2. The gap
8 between the outer edge er face 3a of the fans 3 and the inner wall surface 2a of
the reactor tube 2 can be at least 1, 2, 3, 5, 10 or 15, mm and preferably in the range of l
to 8 mm. As discussed below, the gap 8 promotes heat transfer and forces fluid flow
traveling toward the inner wall e 2a of the reactor wall 2 to be directed back
towards the inner portion of the reactor. In other words, the gap 8 serves to redirect the
fluid flow such that flow is allowed to turn 180 degrees as it comes into contact with the
inner wall surface 2a of the reactor tube 2.
Fluid flow through the reactor tube 2 can be further altered by adding a seal 6 to the outer
edge of a reactor component, such as a core 4, so fluid does not flow n the outer
perimeter edge of each core 4 and the inner wall surface 2a of the reactor tube 2. Thus,
the seals 6 prevent the fluid flow from bypassing the cores 4 around the perimeter. The
W0 2012/103432 PCT/U82012l022888
seals 6 direct the fluid through each core 4 and into another ent such as a fan 3
located below of above the core 4 depending on the direction of fluid flow. Preferably,
the seals 6 are oned at the outer diameter edge of each core 4 and have a ring shape
to enclose the entire vertical outer diameter edge and a portion of the lateral top or bottom
surface near the outer diameter edge of the core 4. As shown, the fans 3 do not include a
seal for ting fluid from flowing between the outer diameter edge 3a of each fan 3
and the inner wall surface 2a of the reactor tube 2. Seals are not used with the fans so
fluid flow is directed to the reactor tube wall to promote heat transfer to the or
portion of the reactor. Examples of alternative structural components are described
below in separate embodiments.
The stacked arrangement of fans 3 and/or cores 4 is ed to promote heat transfer for
carrying out catalytic reactions. As such, reactor 1 components, such as fans 3 and/or
cores 4, or washers can be coated with a catalyst to effectively distribute catalyst contact
with most of the volume of fluid flowing through the reactor. Preferably, seals are not
coated with a catalyst. Catalytic material is known in the art and can include nickel,
palladium, platinum, zirconium, rhodium, ruthenium, iridium, cobalt and aluminum
oxide. The arrangement of stacked ents 3, 4 is not likely to form powder due to
expansion and contraction because there is no single mass of ceramic pellets forming a
packed bed. It is also ly, using the arrangements discussed herein, that the
expansion and contraction of the reactor tube 2 would have any effect on the catalyst.
For efficiency, different catalytic reactions and ses are d out at different
preferred temperatures in the reactor 1. Accordingly, the reactor tube 2, fans 3, cores 4
and the like are selected based upon what environment (temperature, pressure, ty,
gas or liquid composition) they will experience. le materials are preferably those
which perform effectively, or most effectively, or efficiently, or most efficiently at, and
can effectively tolerate, process temperatures of at least -20, -10, 0, 4, 10, 15, 20, 25, 30,
50, 80, 100, 150, 200, 250, 300 or 350° C and process temperatures not more than 1000,
900, 700, 500, 400, 350, 300, 250, 200, 150, 100, 80, 50, 30 or 27° C.
shows schematically a loaded reactor sleeve 10 having a plurality of fans 3 and
cores 4 arranged vertically in alternating order on a central rod 5 for insertion in a reactor
tube, for example as shown in The central rod 5 has a base plate 9 positioned near
its bottom portion for ting the series of fans 3 and cores 4 aligned vertically on the
rod 5. As shown, the base plate 9 can be ar, such as a disk or plate, with an opening
PCT/U820121022888
for fitting onto the l rod 5. As viewed from its top or bottom surface, the plate 9
can be a solid disk or have other openings for allowing fluid to flow through and enter the
center portions of a reactor component such as a fan. For example, the plate 9 can have
perforations, ls or triangular openings arranged to form a hub and spoke
configuration. The circular plate s laterally out from the central rod 5 such that a
bottom surface of a fan 3 or core 4 can rest directly on the top surface of the base plate 9.
The base plate 9 can have any diameter up to that of the inner diameter of the reactor
tube.
The base plate 9 can be secured or set in place by the use of a bushing 10 positioned
directly below the base plate 9. The bushing 10 acts as stop for the base plate 9 such that
once the base plate is slid onto the central rod 5 it stops upon contact with the fixed
bushing 10. The bushing 10 may be adjustable so that the desired base plate 9 location
can be altered depending on the number of reactor components being stacked on the
central rod 5. Preferably, base plate 9 can be permanently attached to the l rod 5 at
the desired location. For example, the base plate 9 can be welded onto the central rod 5
or be an integral part ofthe l rod 5 structure.
In one embodiment, shows an example spiral-wound core 4 positioned on a central
rod 5 for use in a reactor tube. The core 4 can be formed by spiraling metal foil, such as
flat, rippled or corrugated metal foil, around its center or a support tube 1] suitable for
fitting onto a central rod 5. For ce, metal foil can be d to the support tube 11,
such as by welding. The metal foil can then be wound around the support tube 11 until
the desired core 4 diameter is achieved. For fitting purposes, the optional support tube 11
can be used, either attached or unattached ) to the core, to fill any void space
between the inner diameter wall of the core 4 or fan and the outer diameter face ofthe rod
5. The spiral g of the core defines one or more annular flow channels so that fluid
can flow in one end 12a of the core 4, through the ls, and out the other end 12b of
the core 4.
The number and y of annular flow channels can be controlled as known in the art by
tightly or loosely winding the metal foil around its center or a support tube 11. The
thickness ofthe metal foil for forming the cores 4 can be selected to optimize the number
of channels, for example, a thin metal foil will provide more channels for accommodating
fluid flow than a thicker metal foil. The cores 4 preferably contain a high density of
surface area and thus enhance catalytic activity when coated with a catalyst. Any
W0 2012/103432 2012/022888
ble number of cores 4 can be stacked on a central rod 5, such as being alternated
with one or more fans 3.
In another embodiment, shows multiple fans 3 stacked vertically with one another
for use on a central rod (not shown). Each fan 3 has a top surface and a bottom surface
such that the bottom surface of one fan 3 is in either close proximity with, or directly in
contact with the top surface of another fan positioned directly below. That is, depending
on the topography of the top or bottom surface of a fan 3, which may be irregular or
generally flat, the entire top or bottom e of a fan, or at least a portion thereof if
irregular, directly contacts the top or bottom surface of another fan depending on its
position above or below. In the instances a washer separates fans, at least a portion of the
top or bottom e of a fan is in direct contact with the top or bottom surface of the
washer.
As arranged on a t tube 11, the fans 3 have multiple radial fluid ducts 13a and 13b
for directing fluid flow through the reactor. As shown, the radial fluid ducts are of
approximately triangular shape and extend outward from the support tube 11 to form a
circular cross n as viewed from the top of the fans 3. The radial fluid ducts
terminate along the outer diameter face of each fan to form triangular openings facing the
inner wall surface of the reactor tube. As viewed in the downward direction of fluid flow,
fluid flows in one end 14a of the stack of fans 3, radially through the triangular-shaped
ducts openly facing upward 13a towards the outer diameter face of the fans 3 for
contacting the reactor tube, around the outer diameter face of the fans 3 into the
triangular-shaped ducts openly facing downward 13b, radially s the center of the
fans 3 and onto the next fan and/or core in the same manner until the fluid exits the stack
of fans 3 at the other end 14b. In one ement, for e as shown in the
fans 3 can be stacked in an arrangement that vertically aligns the approximately
triangular-shaped ducts openly facing upward 13a of one fan with the approximately
triangular—shaped ducts openly facing downward 13b of the fan 3 positioned ly
above or below.
Flat washers 15 are preferably positioned between the top or bottom surfaces of each fan
3. For fitting and assembly purposes, as described herein, washers can be attached to the
fans or positioned loosely (unattached) between each fan. shows flat washers 15
attached to the bottom surface of the fans 3 whereas shows a flat washer 15
attached to the top surface of a fan 3. The flat washer 15 can provide additional structural
strength to the fans 3. The flat washers 15, like the various washers described below, can
be sized such that various ons along the top or bottom e of a reactor
component can be achieved. For example, the outer diameter of the washer 15 can be
inside, flush or extend beyond. the outer diameter face of a fan 3. As shown, the outer
diameter of the flat washer 15 is flush with the outer er face ofthe fan 3.
In operation, the stack of fans 3 having flat washers 15 is oned on a central rod and
the loaded reactor sleeve is inserted into a reactor tube. The flat washers 15 are
configured to have the same or slightly less diameter than the inner diameter of the
reactor tube as noted above. For example, the outer diameter of the flat washer 15 can be
at least 25, 50, 75, 100, 125, 150, 175, 200, 225 or 250 mm and preferably in the range of
80 to 140 mm. The flat washer 15 can have a ring width of at least 5, 10, 15, 20, 25, 30,
or 40 mm and preferably in the range of 6 to 12 mm. The inner diameter of the flat
washer 15 can be in the range of 20 to 245 mm or as necessary for the desired width and
outer diameter f as discussed above. As positioned on or near the top or bottom
surface of a fan, the outer diameter of the flat washer 15 can be at least 5, 10, 15, 20, 25,
, 35 or 40 mm less than the outer diameter of a fan to ensure that fluid flow around the
outer diameter face of a fan is not interrupted. Alternatively, the washer can extend
outward beyond the outer diameter face of a fan to create a gap between the outer
diameter of the washer 15 and the inner wall surface of the reactor tube. The gap can be
at least 1, 2, 3, 5, 10 or 15, mm and preferably in the range of l to 8 mm. Depending on
the size of gap created by the washer, re drop can be controlled and ed as
desired. The gap ensures that some fluid flowing through the reactor bypasses the washer
around its perimeter as it travels over the washer and through the gap. The bypass of
fluid around the washer generally does not promote heat transfer whereas fluid flow over
the outer diameter face of a fan promotes significant heat transfer because of turbulence
from the corrugations of the fan and the fluid flow being directed radially d from
the fluid ducts.
The flat washers 15 can be in close proximity but do not t the inner wall surface of
the reactor tube such that a significant portion of the overall fluid flow travels radially
though the upward facing triangular duct of a fan 3 and contacts the reactor tube wall and
is partially redirected either through the downward facing adjacent triangular duct of the
fan 3 or around the outer diameter of the . The flat washers 15 ensure that a
significant portion of the flow penetrates the center area of the fan. The flat washers 15,
W0 2012/103432 PCT/U82012/022888
preferably having a ntially open center as shown, allow the redirected portion of the
fluid to travel back into the ular ducts of the fan 3 located above or below
depending on direction of fluid flow through the r, which fills the center of the fan
with fluid. As fluid travels radially back towards the reactor tube, it is mixed with the
portion of fluid that traveled over the outer diameter of the washer. The fans 3 as shown
in FIGS. 4 and 5 can be prepared by initially selecting a corrugated (or finned) strip of
metal foil. The corrugations of the strip of metal foil can have substantially flat faces or,
alternatively, contain rippled or nonuniform faces as shown. The corrugated strip of
metal foil can be fanned out to form a ring or annular disk having an inner er
defining an opening for receiving a central rod. The inner diameter face of the fan can be
optionally attached to a support tube 11, for example by welding, to provide structural
support to the fan and accommodate receiving a central rod for mounting purposes. The
support tube can also be loosely positioned in the interior section of that fan 3 to fill any
void space that can be d as the fan is fitted onto a central rod. The fanned ring also
has an outer diameter face that defines triangular duct faces as described above as viewed
along the outer diameter surface ofthe fan.
shows another embodiment of a washer wherein spacing tabs 15a can be added to
the outer er of a . As shown, the spacing tabs 15a extend radially outward
from the outer diameter of the washer 15. Measured from the outer diameter of the
washer 15, the spacing tabs 15a can extend radially outward at least 1, 2, 3, 5, 10, 15, 20,
or 30 mm and preferably in the range of 1 to 8 mm. The width of the spacing tab 15a
can be adjusted as d. The spacing tabs 15a can be attached to the outer diameter of
the washer 15, for example by g, or alternatively the tabs can be an al part of
the washer.
A washer 15 can have one or more spacing tabs 15a, for instance a washer can have at
least 2, 3, 4, 5, 6, 7, 8, 9 or 10 or more spacing tabs 15a. The spacing tabs 15a prevent the
outer diameter face of a reactor component from contacting the inner wall surface of a
reactor tube. For example, if the outer diameter of a washer 15 is positioned flush with
the outer diameter face of a fan 3 as shown, the length of the spacing tabs 15a can
maintain a minimum distance that the outer diameter face of the fan is spaced from the
inner wall of a reactor tube. In another example, the , in on to a fan, can have
an outer diameter less than the fan. In such a case, the spacing tabs may need to be longer
to ensure a gap between the outer diameter face of the fan and the reactor tube. In both
W0 2012/103432 PCT/U52012/022888
examples the washer is attached to the fan to prevent the fan from sliding during
operation and ting the inner wall ofthe reactor tube.
shows a corrugated washer 16 attached to the bottom surface of a fan 3 for use in a
r tube. Alternatively, the corrugated washer 16 can be attached to the top surface of
a fan 3, for example by welding. As shown, the corrugated washer 16 extends radially
beyond the outer diameter of the fan 3. The preferred ions of the ated
washer 16 can be the same or substantially the same as those d with regard to the
flat washer 15. The corrugated washer 16, like the flat washer 15 of FIGS. 4-6, can be
positioned on the top or bottom surface of a fan to provide a predetermined gap between
the outer diameter face of the washer l6 and the inner wall surface of a reactor tube such
that fluid flow bypassing the washer and pressure drop can be lled as desired.
Although not shown, in another embodiment, a spacer can be attached to the corrugated
ring washer 16, for instance in a bottom peak or valley of a corrugation. A spacer can be
a wire, piece of metal, such as rectangular tab, or the like. For example, a piece of metal
wire can be welded to the washer 16 in an arrangement that the spacer extends outward or
radially from the outer diameter of the washer 16 and reactor component that the washer
may be attached to and s the inner wall surface of a reactor tube. The remaining
portion of the spacer not ing outward can be adjusted to any d length. and
preferably not greater than the ring width ofthe washer 16 so the spacer does not protrude
2O inward beyond the inner diameter of the washer 16. The length of the metal wire can be
adjusted to provide the desired length of wire extending outward from the washer 16
and/or reactor component so the gap between the washer 16 and reactor tube can be
controlled. Preferably, the spacer can extend at least 1, 2, 3, 5, 10 or 15 mm and
preferably in the range of l to 8 mm from the outer diameter face of the washer.
shows a n of a castellated washer 18 for use with a reactor component, such
as a fan 3. Preferably, the castellated washer 18 is configured to have the same or slightly
less of a diameter than the inner diameter of a reactor tube. For example, the outer
diameter of the lated washer 18 can be at least 25, 50, 75, 100, 125, 150, 175, 200,
225 or 250 mm and preferably in the range of 80 to 140 mm. The castellated washer 18
can have a ring width of at least 5, 10, 15, 20, 25, 30, 35 or 40 mm and preferably in the
range of 6 to 12 mm. The inner diameter of the castellated washer 18 can be in the range
of 20 to 245 mm or as necessary for the desired width and outer diameter thereof as
discussed above. The castellated washer 18 can have notches or grooves 19 in its outer
W0 2012/103432 PCT/U$2012/022888
diameter for permitting fluid to flow around the perimeter of the washer. The notches 19
can be any shape, such as square, triangular, curved or a combination thereof, and have
any dimensions, for example the width and depth of notches 19 can be adjusted as
desired. For instance, the depth of the notches 19 can be at least 1, 2, 3, 5, 10 or 15 mm
and preferably in the range of l to 8 mm. As shown in the notches 19 are
generally triangular in shape.
The castellated washer 18 is preferably positioned on a reactor component such that the
entire notch 19 or a portion thereof s radially beyond the outer diameter face of the
r component. For instance, the notches 19 can extend at least 1, 2, 5, 10 or 15 mm
beyond the outer diameter face of a fan 3. Attached to a fan, the depth of the notches 19
of a castellated washer 18 can provide a predetermined gap between the outer diameter
face of the fan 3 and the inner wall surface of a reactor tube such that fluid flow and
pressure drop can be controlled. The notches 19 also allow fluid to flow between the
grooves 19 and into fluid ducts of the fans above or below the washer 18 depending on
the direction of fluid flow. The depth and width of the notches 19 can be adjusted to
control pressure drop and the amount of fluid flowing over the outer diameter of the
washer. .
As shown, the castellated washer 18 can be corrugated to odate the peaks or
grooves defined by the fluid flow ducts, such as ular faced ducts, of a fan or reactor
2O component for fitting purposes. For example, shows a lated washer 18
attached to the top surface of a fan 3. The corrugations of the castellated washer 18 fit
and align with the rippled and corrugated top surface of the downward facing triangular
fluid ducts of the fan 3 to ensure a customized fit. To accommodate the shape of a fan 3
or fluid ducts of a reactor ent, the corrugations of the castellated washer 18 can be
at least 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12 or 13 mm and preferably in the range of2 to 7
In r embodiment, shows a portion of a castellated washer 20 for use with a
r component, ably a fan 3 for finned foil. For example, the castellated washer
can be attached to a fan 3 as shown in FIGS. 4-7 or be used with a spiral shaped finned
foil. The castellated washer 20 preferably has the same outer diameter, inner diameter
and ring width as the washer 18 shown in FIGS. 8 and 9 discussed above.
PCT/U82012/022888
The castellated washer 20 can have spacing tabs 22 for creating a predetermined gap
between the outer er face of a fan 3 and the inner wall surface of a r tube
such that the outer diameter end of the spacing tabs ly contacts the inner wall of the
reactor tube. The spacing tabs 22, as measured from the outer diameter face of the
triangular corrugations 24 of the castellated washer 20, can be at least at least 1, 2, 3, 5,
or 15 rmn and preferably in the range of 1 to 8 mm. The spacing tabs 22 can be
attached to the castellated washer 20, for example by welding, or be an integral portion of
the washer. As shown, the spacing tabs 22 are positioned on the flat sections 23 of the
washer 20. The flat sections 23 provide a contact surface for attaching the castellated
washer 20 to a reactor component such as a fan 3. For instance, one or more flat sections
23 can be welded to the top or bottom surfaces of a fan 3 in a similar arrangement as
shown in FIGS. 4-7.
Positioned in between the flat sections 23 of the lated washer 20 are corrugated
peaks 25. The corrugated peaks 25 provide flexibility to the castellated washer 20 such
that it can flex to accommodate arrangement with a particular reactor component. In
operation, the corrugated peaks 25 fit in the radial fluid ducts of a reactor component. As
shown in , the corrugated peaks 25 are positioned in fluid ducts of a finned foil 27
for use in a reactor tube.
shows a portion of a finned foil viewed from in the direction facing the inner wall
of a reactor tube. The finned foil 27 is corrugated to provide discrete fluid ducts 28, 29
for directing fluid flow through a reactor. The castellated washer 20 can be attached to a
finned foil by welding the flat sections 23 to the ends of the fluid ducts 28 or 29.
Preferably, the washer 20 is attached to the finned foil 27 in an arrangement where the
base of the spacing tab 22 begins at the outer diameter face of the finned foil 27 wherein
the spacing tab extends outward from the outer diameter face of the finned foil 27 to the
inner wall e of a reactor tube, and preferably ts the inner wall. For example,
shows a perspective View of a portion the finned foil 27 of having
g tabs 22 ing outward or radially from the outer er face of the finned
foil 27. As discussed below with respect to FIGS. 20 and 21, a reactor ent or
finned foil can be spiral wound with the castellated ring washer 20 for ion into a
reactor tube.
As discussed herein s embodiments of washers for use with reactor components are
described. A method for forming a castellated washer can include the step of selecting a
W0 2012/103432 PCT/U52012/022888
sheet of metal foil, such as a flat strip of metal foil having a length and width to
accommodate the dimensions of a castellated washer. In one e, the width of the
metal foil is at least twice that of the desired ring width of a single lated washer as
recited above. A series of holes can be punched in a straight line along the entire length
of the metal foil to form a punched metal foil 30. The holes 32 can be spaced apart or
immediately adjacent one another depending on the spacing and size of corrugations and
notches in the final red washer. The diameter of the holes 32 can be selected to
provide a predetermined gap that in operation equates to a spaced distance between the
outer diameter face of a reactor component and a reactor tube. The punched metal foil 30
can be split or cut into two notched metal foil strips 30a and 30b. Preferably the punched
metal foil 30 is split at the center diameter of the series of holes 32.
The d metal foil strips 30a and 30b can be corrugated as shown in . The
notched metal foil strips can be corrugated at varying degrees of corrugation density, for
example a corrugated peak can be positioned on each side of a single notch 36. As
shown, notched metal foil strip 30b has corrugated peaks at the center of each notch 36
and on each side of the notch, although such structured placement of corrugations is not
necessary since notches l9 and density thereof will determine what portion of fluid flows
over the outside of the washer. . The corrugated and d metal foil strips can be
further formed into rings to form a castellated washer for attaching to a reactor
component such as a fan or finned foil.
In another embodiment, a metal foil can be selected with a width of at least twice that of
the desired radius of a fan or finned foil. Similar to the method for g a washer, the
wider metal foil can be d with a series of holes along its center and entire length
before the foil is split into two notched strips. The notched strips can be corrugated and
fanned out into a ring to form a fan having a diameter of twice the width of the d
strip as ed ive of the notch depth or radius of center hole . Depending on the
depth of the notches, as detemrined by the diameter of holes punched in the metal foil, a
castellated fan can be formed wherein the outer diameter face of the fan contains notches
along the entire height of the outer diameter fan face creating a castellated, gap-
controlling edge. The castellated fan can be optionally fitted with a washer, however the
notches of the fan can be sufficient for creating a desired gap n the outer diameter
face thereofand the reactor tube.
Various embodiments relating to the stacking arrangement of reactor components in a
reactor tube, as shown in FIGS. 15-17, will now be described. As described herein, nose
and nose portions are used hangeably. A shows a series of fans 40 stacked
ally on a central rod 44 in a reactor tube 42. The outer diameter faces of the fans 40
have a single notch 45 extending uniformly around the perimeter of the fan. The notch 45
creates a gap between the outer diameter face of the fans 40 and the reactor tube 42. The
notch 45 can have a radial depth of at least 1, 2, 3, 5, 10 or 15 mm and preferably in the
range of l to 8 mm. The depth of the notch 45 also corresponds to the gap length created
between the outer diameter face of the fans 40 and the inner wall of the r tube 42.
The notch 45 can be any height and less than the overall height of the fans 40 and
preferably the height of the notch 45 can be at least 4, 10, 20, 30, 40 or 50 mm and
preferably in the range of 10 to 30 mm.
As viewed vertically, the fans 40 have an upper and lower nose, 46a and 46b,
respectively. The upper and lower noses 46a and 46b extend radially around the
perimeter of the fans 40 and define the height of the notches 45. Preferably, as shown,
the nose portions 46a, 46b of the fans 40 are in contact with the inner wall surface of the
reactor tube 42. In contact with the inner wall surface of the reactor tube 42, the nose
portions 46a, 46b of the fans 40 ensure a gap between the recessed portion of the fan or
notched portion 45 and reactor wall where fluid flowing h the reactor into each fan
40 can flow over the outer er face of the fan. Fluid flow is allowed to contact the
reactor tube 42 in the notched 45 portions for ing heat transfer before being
redirected back into the reactor core region. Alternatively, the nose portions can be
spaced away from the reactor tube 42. The upper and lower noses 46a, 46b can have a
height of at least 2, 4, 8, 10, 15, 20, 30 or 35 mm and preferably in the range of 5 to 20
mm.
In the stacked arrangement of A, washers 41 are positioned between each fan 40
such that either the top or bottom surface of each fan 40, or a portion thereof, contacts a
washer 41. As shown, the outer diameter of the washers 41 is flush with the innermost
diameter of each fan 40 or the innermost recessed portion of each notch 45.
Alternatively, the s 41 can be positioned such that the outer diameter of the
washers 41 s beyond the innermost recessed n of the notches 45 or inward
from the same.
W0 2012/103432 PCT/USZ012/022888
B shows a series of fans 40 stacked vertically on a central rod 44 in a r tube
42. The outer er faces of the fans 40 have four notches 45 extending uniformly
around the perimeter of the fan. Although the fans 40 are shown with four notches, any
number of notches can be included. depending on the height of the fan used and the
amount of pressure drop available across the total length of the reactor. For example, a
fan 40 can have at least 1, 2, 3, 3, 5, 6, 7, 8 or more notches. The notches 45 can have a
height and depth as bed with respect to the notches shown in A.
The fans 40 of 3 have upper, middle and lower noses 46a, 46c and 46b,
respectively. The nose portions 46a, 46b, 46c preferably contact the reactor tube 42 to
ensure a gap between recessed fan perimeter or notches 45 and reactor wall to allow fluid
to flow around the perimeter of each fan 40. The nose portions 46a, 46b, 46c can have a
height as described with respect to the nose portion shown in A. The nose
portions 46a, 46b, 46c extend radially around the perimeter of each fan 40 to define the
notches 45 wherein three middle noses 46c are located between the upper and lower noses
46a, 46b of each fan 40. FIG. ISB shows only fans 40 having 4 notches arranged
vertically however fans having greater or fewer notches can be included in the vertical
stack in any order as desired. Washers 41 separate each fan 40.
In another embodiment, shows fans 40 ted by washers 41 and stacked on a
central rod 44 in a reactor tube 42. The fans 40 have a single nose 48 positioned at the
top portion of each fan 40. The n of the outer diameter face of the fan 40 separate
from the nose 48 is recessed to form a notch 49 defining a radial gap around the perimeter
of each fan 40. Arranged vertically, the nose 48 of one fan 40 is adjacent the bottom
portion of the notch 49 of the fan 40 directly above. Thus, the nose 48 of one fan 40,
when d next to another fan 40 with a single nose 48, defines the height of a single
notch 49 as shown. The notch 49 and nose 48 of the fans 40 can have the same
dimensions as recited above with respect to A. Optionally, the fans 40 of
can be used with the notched fans . 15A and 15B to provide stacked arrangements
of different fans in any order.
In yet another embodiment, shows a series of fans 40 stacked on a central rod 44
in a r tube 42. The fans 40 have a single nose 50 positioned at the bottom portion
of each fan 40. The remaining portion of the outer diameter face of the fans 40 separate
from the nose 50 is recessed to for a notch 51 that defines a radial gap around the
perimeter of each fan 40. Attached to the bottom surface of each fan 40 is a washer 52.
PCT/U52012I022888
The washer 52 is recessed so it does not t the reactor tube 42 whereas the nose 50 is
in contact with the reactor tube 42 and directs fluid flow through the reactor. The washer
52, like the washers 41 of FIGS. 15-16, creates vertical gap 54 between the fans 40 that is
equal to the height of the washer, which can be in the range of 0.1 to 5 mm. As shown,
the washer 52 is a flat ring, however a corrugated washer can be used and, alternatively,
the washer 52 can be attached to the top e of each fan 40. The washer 52 can also
be loosely positioned between the fans 40 ifnot attached to a fan before assembly.
As ed, the bottom nose 50 of each fan 40 has a washer 52 attached thereto wherein
nose 50 of one fan defines the upper boundary of a notch 51 and the nose 50 of the fan 40
below defines the lower boundary of a notch 51. The notch 51 and nose 50 of the fans
40 can have the same ions as recited above with respect to A. Optionally,
the fans 40 of can be used with the notched fans of FIGS. 15A, 14b and 15 to
provide stacked arrangements of different fans in any order, with or without washers.
Various embodiments relating to the central rod and bushing configurations and
components, as shown in FIGS. 18-19, will now be described. shows two central
rods 60, 62 aligned in a vertical stacking arrangement for purposes of supporting cores 64
and fans 66 stacked in alternating order within a reactor tube 63. l rod 60 has a
cylindrical cavity 61 in its bottom portion for accommodating another central rod, such as
62, which fits inside of the cavity 61 as shown. The cylindrical cavity 61 can have an
inner diameter less than, the same or slightly greater than the outer diameter of another
central rod, 62, for fitting es. For example, the cylindrical cavity 6] can have a
diameter of at least 5, 10, 25, 50, 75, 100, 125 or 150 mm and preferably in the range of 6
to 40 mm. The inner diameter of the cavity 61 can be adjusted to permit a gap or
clearance between the top of rod 62 and the bottom face of the cavity. The clearance can
be at least 2, 4, 8, 10, 15, 20, 30 or 35 mm and ably in the range of 5 to 20 mm.
The height of the cylindrical cavity 61 can be adjusted as d, for example, the height
can be at least 100, 200, 300, 400 or 500 mm.
Extending radially d from ccntral rod 60 is a base plate 68 for supporting reactor
components 64, 66 in the reactor tube 63. The base plate 68 can be attached to the central
rod 60, for e by g, or be an integral portion of the rod 60. The base plate 68
can be located at the bottom end of the central rod 60 as shown or, alternatively, the plate
68 can be positioned above the bottom end anywhere along the length of the rod 60 as
desired. The base plate 68 can be have solid bottom and top faces for contacting reactor
PCT/U52012l022888
components or, alternatively, the plate 68 can be perforated for allowing fluid to flow
through the plate. The base plate 68 can have any diameter as desired that is greater than
the diameter of the cavity 61 but less than the inner diameter of the reactor tube 63. In
operation, a series of rods can be ed, all having the same structural features, such as
a bottom rical cavity, such that one or more rods are d and fit together for
arranging cores and fans in a reactor tube. Stacking rods vertically with protruding
portions of one rod inserted into the cavity of another rod eliminates or prevents excessive
gaps between reactor components. Disassembly of the reactor components can be
lished by pulling the central rods out of the r tube, for example engaging the
top of a central rod and pulling upward. The base plate of each central rod prevents the
reactor components from ng off the central rod during assembly and embly of
the reactor.
shows a central rod 70 vertically aligned above another central rod 72 in a reactor
tube 73. Central rod 70 has a base plate 78 located above the bottom end of the rod 70a
for supporting a fan 76 and core 74 stacked vertically on the rod. The base plate 78 can
be positioned at any location along the length of the rod 70 as desired, and ably the
base plate 78 can be at least 5, 10, 15, 20, 25, 30, 35 or 40 mm above the bottom 70a.
Similar to the base plate of , base plate 78 can be solid or perforated.
As shown, the bottom 70a of central rod 70 is spaced apart fi'om the top 72a of central rod
72 within a bushing 71 that circumferentially surrounds a n of both central rods.
The spacing can be the same as the clearance described above with regard to .
The g 71 can have a diameter of at least 10, 12, l4, 16, 18, 20, 22, 24 or 26 mm
and a height of at least 10, 20, 30, 40 or 50 um. The bushing 71 can be attached to the
bottom portion of central rod 70 or to the top of central rod 72 as desired. Alternatively,
the bushing 71 can be an integral part of a reactor component, for example the bushing
can be attached to the center re of a core 74 or fan 76. As shown, the g 71 is
positioned at the center of a core 74 located at the top of a reactor string aligned on
central rod 72. Positioned at the center of a core 74, the bushing 71 can be an integral
portion of the core 74 structure such that bushing and core assembly slides onto central
rod 72. Barbs 75 can be used directly below the bottom edge of the bushing 71 to hold it
in place and prevent the bushing from sliding down the central rod 72. The tapered
bottom of central rod 70 can be inserted into bushing 71 to create a stack of loaded
reactor sleeves.
W0 2012/103432 PCT/USZ012/022888
As described above, multiple reactor components can be stacked on rods for loading
reactor sleeves that can be further vertically aligned in a reactor. Various embodiments
relating to a single reactor component for use in a reactor tube, as shown in FIGS. 20 and
, will now be described. A spiral wound or helix reactor component, such as a fan or
finned foil, can reduce the use of multiple, stacked reactor components, for example, a
helix fan can be the sole reactor component positioned on a central rod for use in a r
tube. Optionally, one or more helix fans or finned foils can be stacked together or a
double helix assembly of a fan and core or finned foil and core can be used.
shows a helix fan 100 fitted on a central rod 102 for use in a reactor tube. The helix fan
100 can be formed by ating a strip of flat or rippled metal foil to create
substantially triangular corrugations for use as fluid flow ducts. The corrugated strip of
foil can be fanned out to create a ring wherein the corrugated strip is fiirther fanned out in
a spiral manner to obtain a helix structure as shown. The helix can be twisted in either
direction, clockwise or counterclockwise. The inner diameter of the helix can be
optionally attached to a support tube to provide structural strength to the helix structure
and for accommodating a central rod for mounting es. ably, the helix
structure has a constant outer diameter along its entire length. The outer diameter face of
the helix fan 100 can be spaced away from the inner wall of the reactor tube, for example
the spacing can be at least 1, 2, 3, 5, 10 or 15, mm and preferably in the range of 1 to 8
mm. The outer er face of the helix fan 100 can also have notches or be castellated
wherein the outermost diameter portions of the face, nose portions, are in contact with the
inner wall surface of the reactor tube. The helix fan 100 has an outer diameter face that
defines triangular fluid duct faces as described above for receiving and directing fluid
flow through the reactor.
The metal strip of foil used to form the helix fan can have s or cutouts on one edge
for arranging structural s or noses along the outer diameter face 100a of the helix
fan 100. For example, the outer diameter face 100a of the helix fan 100 can have notch
and gap arrangements as shown in FIGS. 8 and 15-17. ing on the arrangement of
notches and/or gaps in the outer diameter face of the helix fan 100, the entire face or a
portion thereof may be in contact with the inner wall surface of the reactor tube. As
described below, washers or spacers can be used to t the reactor tube and prevent
the helix fan 100 from contacting the tube.
W0 2012/103432 PCT/USZ012/022888
The helix fan 100 can have an outer diameter of at least 25, 50, 75, 100, 125, 150, 175,
200, 225 or 250 mm and preferably in the range of 80 to 140 mm. As used as a single
r component, the helix fan 100 can have a length of at least 0.6, 1, 2, 4, 6, 8, 10 or
m and ably in the range of 0.6 to 2 m or 6 to 12 m. The helix fan can be formed
with a twist or incline angle of at least 5, 10, 15, 20, 25, 30, 35 or 40 degrees and
preferably in the range of 5 to 40 degrees, and more preferably in the range of 10 to 35
degrees.
Depending on the length of the helix fan 100 and twist or incline angle, any number of
spirals can be used. A single spiral can be measured as a portion of the helix that
completes one complete circumference. The helix fan 100 can have at least 24, 48, 72,
96, 150, 200, 250, 300, 350 or 400 s and preferably in the range of 24 to 96 spirals.
The helix fan 100 can be coated with a catalyst as desired and preferably the entire
surface ofthe helix fan is coated.
The helix fan 100 can optionally have a helix washer 104 that can be flat, corrugated or
castellated. Due to the lity provided by corrugations, a corrugated helix washer is
preferred. In addition, the corrugations and/or peaks and valleys of the helix washer 104
can align with the corrugations of the helix fan 100. Flexibility of the helix washer 104 is
desirable for forming a continuous arc during installation of the helix fan 100. The helix
washer 104 can be attached to the top and/or bottom surface of the helix fan 100 and
able the helix washer 104 extends along the entire length of the helix fan 100. In a
similar arrangement as the washers described above, the helix washer 104 is a ring that is
preferably located at the outer circumference edge of the helix fan 100. The helix washer
104 can extend inward or outward from the outer er face 100a of the helix fan, or
be flush therewith. The helix washer 104, if extending outward fi'om the outer diameter
face 100a of the helix fan 100, is preferably not in contact with the inner wall surface of a
reactor tube wherein a gap is left between the outer diameter of the helix washer 104 and
the reactor tube. The gap created by the helix washer 104 can be the same as described
above, for example in FIGS. 5-7. Likewise, the inner diameter, outer diameter and ring
width dimensions of the helix washer 104 can be the same as recited above, for e
in FIGS. 5-7. In another aspect, the helix washer can be castellated and/or have spacers
or spacing tabs as described and shown in FIGS. 8-14.
In another embodiment, the helix fan 100 can be layered with other reactor components,
such as a core, to create a double helix reactor component. For example, a core can be
PCT/U52012/0228“
spiral wound or fanned out with the con'ugated foil used to make the helix fan 100 to
create a double helix that contains alternating layers, as viewed from the side, of fans and
cores. Optionally, a double helix arrangement can have one or more helix washers for
creating gaps between the outer diameter of the washer and the inner was surface of the
reactor tube. The outer diameter faces of the fan andlor core are ably spaced away
from the inner wall of the reactor tube as similarly discussed with regard to the helix fan
100.
shows a cross sectional view of the helix fan arrangement in a reactor tube.
Because the helix fan 110 has inner diameter associated with the center aperture of the
fan 110, a void space 116 is created. The center void 116 of the helix fan 110 can be
filled with loose aggregate of particles 118. The particles 118 can be made of c,
metal or combinations thereof as known in the art. The particles 118 are preferably
spherical or spheroidal or substantially spheroidal or y or somewhat spheroidal or
roundish or misshapen spheroids or elliptical, oval or nonuniform or shaped bodies like
s, granules, gravel, pebbles or stones, such as pebbles found on s or in
stream-beds. The les 118 can also be cylindrical or other shapes.
The particles 118 can function to maintain a minimal inner diameter of the helix fan 110
and thus secure the outer diameter face of the helix fan 110 or helix washer 112 against
the inner wall of the reactor tube 114. Maintaining contact with the inner wall surface of
2O the r tube 114 with a packed center space 116 prevents significant fluid from being
concentrated through the center of the helix fan 110. Prior to filing the void space 116 of
the helix fan 110, a seal tube 119 can be inserted to serve as a barrier between the inner
diameter face of the helix fan 110 and the loose aggregate. The seal tube 119 can be
attached or unattached to the helix fan 110 and preferably the seal tube 119 has a height
equal to that of the helix fan 110. The seal tube can be in direct contact with the inner
diameter face of the helix fan 110 or spaced away from the inner face as desired.
The single helix reactor component shown in FIGS. 20 and 21 provide distinct advantages
over reactor arrangements having multiple components. For example, only a single
component necessitates coating, which saves production time and cost. Moreover, using
a single r component, a fixed outer diameter is maintained which results in more
consistent flow as compared to multiple r ents ing diameters.
2012/022888
While various embodiments in accordance with the present invention have been shown
and described, it is understood the invention is not limited thereto, and is susceptible to
numerous changes and modifications as known to those skilled in the art. ore, this
invention is not limited to the details shown and described herein, and includes all such
changes and modification as encompassed by the scope of the appended claims.
Claims (14)
1. A reactor comprising: a stationary fan arranged on a central rod in a r tube, the fan having radial fluid ducts for directing fluid flow through the reactor, the fluid ducts being effective to radially guide the fluid flow to contact the reactor tube and promote heat transfer along the reactor tube; the fan having a top surface, a bottom surface and an outer diameter face such that the radial fluid ducts terminate along the outer er face of the fan to form fluid duct openings facing the reactor tube. 10
2. The reactor of claim 1, fiirther comprising a core arranged on the central rod.
3. The reactor of claim 1, the fan being a corrugated disk having a center aperture for ing the central rod.
4. The reactor ofclaim 1, further comprising a washer being in the shape of a ring having an inner diameter and an outer diameter, the washer being in t with the top surface or the bottom surface of the fan n the outer diameter ofthe washer s ly outward from the outer diameter face of the fan.
5. The reactor of claim 4, the washer further having spacing tabs extending d from the outer diameter of the washer.
6. The reactor according to any of claims 4 to 5, the washer or spacing tabs being in 20 contact with the reactor tube and the outer diameter face of the fan not being in contact with the reactor tube.
7. The reactor of claim 1, the central rod having a base plate for supporting the fan arranged on the central rod, the base plate extending radially outward from the central rod. 25
8. The reactor ofclaim 1, the central rod having a top end and a bottom end, the central rod having a cylindrical cavity at the top end or bottom end for receiving a portion of another central rod.
9. The reactor of claim 1, the fan being a helix fan.
10. The reactor of claim 9, the helix fan having an incline angle in the range of 5 to 40 30 degrees.
11. The reactor ofclaim 9, the helix fan further having a helix washer, the helix washer extending outward fiom the outer diameter face ofthe helix fan, a portion of the helix washer being in contact with the reactor tube.
12. The reactor of claim 11, the outer er face the helix fan being not in contact with the reactor tube wherein the helix washer creates a gap between the outer er face of the helix fan and the reactor tube, the gap being at least 1 mm.
13. The reactor m 1, the outer diameter face of the fan having a notch extending around the perimeter of the fan, the notch being an annular channel around the outer 10 diameter face of the fan.
14. The reactor of claim 13, the outer diameter face of the fan further having one or more nose portions, the one of one or more nose portions defining the notch and the one or more nose portions being in contact with the reactor tube. W0 20 20121022888
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201161437103P | 2011-01-28 | 2011-01-28 | |
US61/437,103 | 2011-01-28 | ||
PCT/US2012/022888 WO2012103432A2 (en) | 2011-01-28 | 2012-01-27 | Improved stackable structural reactors |
Publications (2)
Publication Number | Publication Date |
---|---|
NZ612924A NZ612924A (en) | 2014-10-31 |
NZ612924B2 true NZ612924B2 (en) | 2015-02-03 |
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US9751073B2 (en) | Stackable structural reactors | |
US7320778B2 (en) | High-performance catalyst support | |
US8257669B2 (en) | Multi-tube chemical reactor with tessellated heat transfer fins | |
EP2834586B1 (en) | Wire standoffs for stackable structural reactors | |
US7682580B2 (en) | Catalytic reactor having radial leaves | |
GB2103953A (en) | Catalyst devices | |
EP3099405B1 (en) | Seals for use with catalyst structures | |
NZ612924B2 (en) | Improved stackable structural reactors | |
SA111320881B1 (en) | New External Modular Grid For Radial Bed Reactors | |
JPS6219240A (en) | Catalytic reactor |