WO2024043908A1 - A method for converting an existing industrial unit to produce hydrogen from ammonia - Google Patents
A method for converting an existing industrial unit to produce hydrogen from ammonia Download PDFInfo
- Publication number
- WO2024043908A1 WO2024043908A1 PCT/US2022/041910 US2022041910W WO2024043908A1 WO 2024043908 A1 WO2024043908 A1 WO 2024043908A1 US 2022041910 W US2022041910 W US 2022041910W WO 2024043908 A1 WO2024043908 A1 WO 2024043908A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- layer
- aluminization
- equipment
- nitridation
- protective
- Prior art date
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000001257 hydrogen Substances 0.000 title claims abstract description 45
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 45
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims abstract description 37
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 27
- 239000003054 catalyst Substances 0.000 claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 claims abstract description 22
- 230000008569 process Effects 0.000 claims abstract description 17
- 239000011241 protective layer Substances 0.000 claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 9
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 7
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 7
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 5
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 4
- 239000010410 layer Substances 0.000 claims description 85
- 230000004888 barrier function Effects 0.000 claims description 39
- 238000009792 diffusion process Methods 0.000 claims description 35
- 230000001681 protective effect Effects 0.000 claims description 33
- 239000000463 material Substances 0.000 claims description 32
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 31
- 229910052759 nickel Inorganic materials 0.000 claims description 15
- 229910052782 aluminium Inorganic materials 0.000 claims description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 14
- 229910045601 alloy Inorganic materials 0.000 claims description 12
- 239000000956 alloy Substances 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 12
- 238000005336 cracking Methods 0.000 claims description 10
- 239000000843 powder Substances 0.000 claims description 10
- 239000010953 base metal Substances 0.000 claims description 8
- 239000002002 slurry Substances 0.000 claims description 8
- 229910000951 Aluminide Inorganic materials 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 229910052710 silicon Inorganic materials 0.000 claims description 5
- 239000010703 silicon Substances 0.000 claims description 5
- 238000003466 welding Methods 0.000 claims description 4
- 238000000151 deposition Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 13
- 229910000831 Steel Inorganic materials 0.000 description 10
- 239000010959 steel Substances 0.000 description 10
- 150000004767 nitrides Chemical class 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 238000000576 coating method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 229910001055 inconels 600 Inorganic materials 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- -1 FeAl Chemical compound 0.000 description 1
- 229910015372 FeAl Inorganic materials 0.000 description 1
- 229910000943 NiAl Inorganic materials 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- VNTLIPZTSJSULJ-UHFFFAOYSA-N chromium molybdenum Chemical compound [Cr].[Mo] VNTLIPZTSJSULJ-UHFFFAOYSA-N 0.000 description 1
- 238000005253 cladding Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910021326 iron aluminide Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 229910000907 nickel aluminide Inorganic materials 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000009420 retrofitting Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
Classifications
-
- 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
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/047—Decomposition of ammonia
-
- 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
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0811—Methods of heating the process for making hydrogen or synthesis gas by combustion of fuel
- C01B2203/0816—Heating by flames
Definitions
- the present invention relates to an apparatus and method for hydrogen production using existing industrial units. More specifically, embodiments of the present invention are related to avoiding embrittlement of steels caused by nitridation.
- Ammonia has raised some attention in the literature, since existing infrastructure can be used for storage and transportation (e.g., LPG infrastructure). As such, production of hydrogen using ammonia, instead of natural gas, to produce hydrogen is foreseen to be the future of the next generation of hydrogen production.
- new industrial facilities are quite costly to build and take many years to design and produce. Therefore, it will likely be at least a decade or more before any new dedicated ammonia cracking facilities can be operational. In the interim, it is still desirable to proceed with production of hydrogen in a more environmentally sensitive manner, which includes the cracking of ammonia gas by using existing hydrogen production facilities.
- Ammonia can be cracked into hydrogen and nitrogen at ambient pressure and moderate temperatures (450-600°C) by thermal cracking and/or in the presence of a catalyst.
- it can be advantageous to apply higher pressures for the NH3 cracking reaction (it is easier to compress ammonia gas compared to hydrogen gas due to hydrogen’s small molecular size).
- the cracking reaction is not favored according to Le Chatelier ’s principle, so higher temperatures are favored (around 700°C) in order to reach economic conversion rates.
- SMRs steam methane reformers
- hydrocarbon feedstock such as natural gas, LPG, naphtha, refinery off gas or the like
- natural gas typically contains nitrogen
- this molecular nitrogen does not lead to critical nitride formation in steels from the process (tube) side, as the partial pressure of nitrogen is not high enough and catalysts to split N2 into atomic nitrogen are not present.
- existing SMRs are not designed with this contingency in mind.
- a protective liner is applied in a common catalyst tube.
- the invention can include application of an aluminization layer on the inner tube surface.
- a diffusion barrier can be applied between the aluminization layer and the tube material to limit diffusion between the aluminization layer and the tube material. This diffusion barrier is preferably configured to block, or at least minimize, any interaction between the substrate (i.e., aluminization layer) and the environment.
- a weld-overlay can be applied to the inner surface of the catalyst tube.
- the method for converting an existing steam methane reformer (SMR) to produce hydrogen via ammonia cracking by adding a protective layer to an inner surface of equipment to be used in the existing SMR can include the steps of: providing the existing SMR, wherein the SMR was formerly used to produce hydrogen from a hydrocarbon feedstock; and improving the nitridation resistance of the inner surface of the equipment, wherein the equipment is selected from the group consisting of a catalyst tube, feed piping, a feed preheater, process gas heat exchangers, and combination thereof.
- the step of improving the nitridation resistance includes a process selected from the group consisting of applying a protective liner material that is mechanically coupled to the inner surface, applying an aluminization layer to the inner surface, applying a diffusion barrier layer in conjunction with the aluminization layer, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and applying a weld-overlay to the inner surface;
- the step of improving the nitridation resistance comprises applying an aluminization layer to the inner surface
- the step of applying the aluminization layer comprises the steps of: introducing an aluminization source powder into an internal space delimited by the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; transferring aluminum from the aluminization source powder to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide layer; and removing the aluminization source powder from the internal space;
- the step of applying the aluminization layer comprises the steps of: depositing an aluminization slurry layer on the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; drying the slurry layer; transferring aluminum from the aluminization slurry to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide layer; and removing the remains of the aluminization slurry from the internal space; • the step of improving the nitridation resistance comprises applying a diffusion barrier layer to the inner surface of the piece of equipment, and applying an aluminization layer to the diffusion barrier layer, such that the diffusion barrier layer is disposed between the inner surface of the piece of equipment and the aluminization layer;
- the diffusion barrier layer comprises a chrome-silicon barrier layer
- the step of improving the nitridation resistance comprises applying a protective liner that is mechanically coupled to the inner surface
- the protective liner material is selected from a group of alloys having a nickel content in excess of 60%;
- the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion
- the protective liner is coupled to the inner surface of the equipment via a flange or welding;
- the protective liner is configured to have a substantially similar thermal expansion coefficient to that of the piece of equipment
- the step of improving the nitridation resistance comprises applying a protective weld-overlay to the inner surface
- the protective weld-overlay is selected from a group of alloys having a nickel content in excess of 60%;
- the equipment that has improved nitridation resistance is a new piece of equipment or was previously used in the existing SMR.
- the method can include the steps of: providing the existing hydrogen industrial unit, wherein the hydrogen industrial unit was formerly used to produce hydrogen from a hydrocarbon feedstock; and improving the nitridation resistance of an inner surface of the equipment, wherein the equipment that has improved nitridation resistance is a new piece of equipment or was previously used in the existing hydrogen industrial unit.
- the equipment is selected from the group consisting of feed preheaters, feed piping, catalyst tubes, process gas heat exchangers, outlet system, process gas boiler, and combinations thereof; and/or
- the protective layer is applied to equipment that is configured to be in fluid communication with an ammonia feed gas at temperatures exceeding 400 °C.
- a hydrogen production facility can include: a reformer configured to catalytically convert a feed stream into a product stream comprising hydrogen, the reformer having a plurality of catalyst tubes and a plurality of burners configured to provide heat to the catalyst tubes; means for providing the feed stream to the reformer from an ammonia source, wherein the feed stream comprises at least 90% of ammonia, wherein the plurality of catalyst tubes comprise a nitridation protective layer on an inner surface of the catalyst tubes.
- the nitridation protective layer is selected from the group consisting of a protective liner material that is mechanically coupled to the inner surface, an aluminization layer applied to the inner surface, a diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and a weld-overlay applied to the inner surface; • the nitridation protective layer comprises the diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface;
- the diffusion barrier layer comprises a chrome-silicon barrier layer
- the nitridation protective layer comprises applying a protective liner that is mechanically coupled to the inner surface
- the protective liner material is selected from a group of alloys having a nickel content in excess of 60%;
- the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion
- the protective liner is coupled to the inner surface of the equipment via a flange or welding;
- the protective liner is configured to have a substantially similar thermal expansion coefficient to that of the piece of equipment
- the nitridation protective layer comprises a protective weld-overlay applied to the inner surface
- the protective weld-overlay is selected from a group of alloys having a nickel content in excess of 60%;
- the hydrogen production facility can also include additional equipment having the nitridation protective layer, wherein the additional equipment is selected from the group consisting of feed piping, a feed preheater, process gas heat exchangers, and combination thereof.
- FIG. 1 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a first embodiment of the present invention having a welded or flanged liner.
- FIG. 2 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a second embodiment of the present invention having an aluminization layer without a diffusion barrier layer.
- FIG. 3 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a third embodiment of the present invention having an aluminization layer with a diffusion barrier layer between the aluminization layer and the base material.
- FIG. 4 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a fourth embodiment of the present invention having a weld-overlay.
- aluminization layer is intended to cover a diffusion layer that includes a mixture of iron and nickel aluminides (e.g., FeAl, NiAl) with a preferred aluminum content of between 25-40 wt%.
- nitrides from elemental nickel is not documented in literature.
- the beneficial effects of reducing the nitridation susceptibility using nickel in steels include lower solubility of nitrogen and lower diffusion rates of nitrogen in alloys with nickel content up to 40 wt.%.
- some high content nickel base alloys are known to better withstand nitride formation and embrittlement as the aforementioned.
- One such candidate is Alloy 600.
- the currently used high-temperature, high-creep-strength catalyst tube material does not belong to these materials.
- the task is to optimize the material for the selection for the inner diameter surface of the catalyst tubes that are potentially affected by nitridation — either by replacing them with tubes made from another material or to coat/weld-overlay or line the inner diameter surface of the catalyst tube with a material having a lower nitridation embrittlement susceptibility.
- Catalyst tubes have to be resistant not only against the inner process conditions but also against the outer high temperature flue gas atmosphere while providing sufficient creep strength, which materials with high nitridation resistance typically do not possess. Therefore, certain embodiments of the present invention concentrate on improving the nitridation resistance on the inside of the common catalyst tubes by applying an appropriate selection of a resistant material.
- the resistant material can be a very thin layer applied on the material surface, a combination of layers, or a thicker lining or weld-overlay.
- the resistant material can also be chosen in combination with an oxidizing process medium in such a manner that, due to a more oxidizing atmosphere, the material forms a protective oxide layer upon exposure to the ammonia and oxidizing agent mixture.
- the liner material can be selected to be nickel or an alloy with a very high nickel content (Nickel content similar or higher than in alloy 600, i.e. Ni > 60% ).
- FIG. 1 provides a cross sectional view of a catalyst tube 1 having an outer wall 2 in accordance with these embodiments.
- the liner 10 can be flanged to the inlet or welded 12 to the inner wall 3 of the catalyst tube 1.
- either the protective liner 10 can be attached to the inner wall 3 of the catalyst tube only at one side (inlet), so that the different thermal expansion coefficients of the materials will not lead to damage of the liner 10 or the catalyst tube itself, or the material composition of the liner 10 is chosen such, that its thermal expansion coefficient is substantially similar to that of the catalyst tube 1.
- the latter solution would also allow the use of a material with non-optimal resistance against nitridation, but with the intention to replace it after reaching an appropriate lifetime.
- an expansion coefficient that is “substantially similar” means that the expansion coefficients are the same +/- 5%, or close enough that differences in thermal expansion do not cause problems in production or result in safety issues.
- FIG. 2 provides another embodiment of the invention, which can include application of an aluminization layer 15 on the inner wall 3 (e.g., inner surface).
- an aluminum-containing alloy with only some percent aluminum is known to be very susceptible to nitridation because aluminum is a strong nitride former, at very high aluminum content, as it is the case in such a coating, a protective oxide layer will form at the surface, even in atmospheres with low oxygen partial pressure.
- the coating process could be, but is not limited to, aluminization by pack cementation.
- the steps for providing the aluminization layer to an article having an internal cavity for protection against embrittlement can include introducing an aluminization source powder into the internal cavity through an inlet; heating the article with the aluminization source powder in the internal cavity to cause aluminum to transport from the aluminization source powder to the internal surface of the internal cavity; and thereafter removing the aluminization source powder from the internal cavity through the inlet.
- FIG. 3 provides a similar solution to that shown in FIG. 2; however, in this embodiment, very high temperatures (e.g. above about 700 °C) might introduce diffusion processes between the base material 17 of the catalyst tube 1 and the aluminization layer 15, which might affect the protective effect of the coating itself. Therefore, in addition to the aluminization layer 15, by modification of the aluminization process, another layer is disposed between the aluminization layer 15 and the tube material 17 and works as a diffusion barrier 20.
- This additional barrier layer can be, as a non-limiting example, a chrome-silicon barrier layer.
- one solution of the present invention is a catalyst tube 1 comprising: an external wall 2, an internal wall 3, an aluminization layer 15 mirroring at least a portion of the internal wall, a diffusion barrier 20 mirroring at least a portion of the internal wall, wherein the diffusion barrier 20 is between the internal wall 3 and the aluminization layer 15.
- the catalyst tube according to the present invention can exhibit one or more of the following characteristics: the diffusion barrier 20 matches the shape of the internal wall 3 and the shape of the aluminization layer 15; the diffusion barrier 20 can be a chrome-silicon barrier layer disposed between the tube material 17 and the aluminization layer 15. [0035] Preferably, the diffusion barrier fits the shape of the internal wall of the tube. The diffusion barrier must be selected as a function of its ability to withstand operating conditions at high temperature (700 to 1000° C.)
- FIG. 4 provides yet another embodiment, in which resistance to nitridation can be achieved by adding a resistant weld-overlay 25 to the inner wall 3 of components in contact with ammonia and ammonia-cracking products.
- a resistant weld-overlay 25 can include catalyst tubes, piping, heat coil, heat exchanger tube, etc. . .
- This resistant material can include a nickel-base alloy with a minimum 60% nickel, and forms a barrier between the tube side medium and the internal metallic tube wall.
- This weld-overlay is a type of cladding, where the high nickel metal is added to the surface of the inner tube wall by melting a weld consumable and depositing it in one or more welding passes. Contrary to a solid liner material, the final closed surface of a weld-overlay is built up by overlapping single weld beads into a closed, protective surface.
- Optional or optionally means that the subsequently described event or circumstances may or may not occur.
- the description includes instances where the event or circumstance occurs and instances where it does not occur.
- Ranges may be expressed herein as from about one particular value, and/or to about another particular value. When such a range is expressed, it is to be understood that another embodiment is from the one particular value and/or to the other particular value, along with all combinations within said range.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A method can include: providing the existing SMR, wherein the SMR was formerly used to produce hydrogen from a hydrocarbon; and improving the nitridation resistance of the inner surface of the equipment by adding a protective layer to an inner surface of equipment to be used in the existing SMR, wherein the equipment is selected from a catalyst tube, feed piping, a feed preheater, process gas heat exchangers, and combination thereof. The hydrogen production facility can include a reformer configured to catalytically convert a feed stream into a product stream comprising hydrogen, means for providing the feed stream to the reformer from an ammonia source, wherein the feed stream comprises at least 90% of ammonia, wherein the plurality of catalyst tubes comprise a nitridation protective layer on an inner surface of the catalyst tubes.
Description
A METHOD FOR CONVERTING AN EXISTING INDUSTRIAL UNIT TO PRODUCE HYDROGEN FROM AMMONIA
TECHNICAL FIELD OF THE INVENTION
[0001] The present invention relates to an apparatus and method for hydrogen production using existing industrial units. More specifically, embodiments of the present invention are related to avoiding embrittlement of steels caused by nitridation.
BACKGROUND OF THE INVENTION
[0002] In an effort to reduce the effects of carbon dioxide emissions, new energy carriers are becoming increasingly more important. One of the leading energy carriers is hydrogen; however, due to its small molecular size, high-pressure requirements, and very low boiling point, transportation of elemental hydrogen is difficult and costly.
[0003] Ammonia (NH3) has raised some attention in the literature, since existing infrastructure can be used for storage and transportation (e.g., LPG infrastructure). As such, production of hydrogen using ammonia, instead of natural gas, to produce hydrogen is foreseen to be the future of the next generation of hydrogen production. Unfortunately, new industrial facilities are quite costly to build and take many years to design and produce. Therefore, it will likely be at least a decade or more before any new dedicated ammonia cracking facilities can be operational. In the interim, it is still desirable to proceed with production of hydrogen in a more environmentally sensitive manner, which includes the cracking of ammonia gas by using existing hydrogen production facilities.
[0004] Ammonia can be cracked into hydrogen and nitrogen at ambient pressure and moderate temperatures (450-600°C) by thermal cracking and/or in the presence of a catalyst. In order to save
hydrogen compression energy on the backend, it can be advantageous to apply higher pressures for the NH3 cracking reaction (it is easier to compress ammonia gas compared to hydrogen gas due to hydrogen’s small molecular size). However, at higher pressures, the cracking reaction is not favored according to Le Chatelier ’s principle, so higher temperatures are favored (around 700°C) in order to reach economic conversion rates.
[0005] Unfortunately, ammonia is known to lead to nitride formation (nitridation) in steels during the process of NH3 cracking into H2 and N2, particularly so at elevated temperatures. This is because the ammonia cracking reaction at elevated temperature will lead to formation of atomic nitrogen, which diffuses into the metallic material to form nitrides, thereby causing the embrittlement of steels.
[0006] As some steels also act as catalysts for the NH3 cracking process, nitride formation of steel can occur already at its surface and at temperatures where only small ammonia conversion rates are observed. That means steels might already be at risk of embrittlement during heat up of ammonia to above 400°C.
[0007] Currently steam methane reformers (SMRs) are operated with hydrocarbon feedstock, such as natural gas, LPG, naphtha, refinery off gas or the like, at temperatures well above 700°C. Although natural gas typically contains nitrogen, this molecular nitrogen does not lead to critical nitride formation in steels from the process (tube) side, as the partial pressure of nitrogen is not high enough and catalysts to split N2 into atomic nitrogen are not present. As such, existing SMRs are not designed with this contingency in mind.
[0008] Current materials applied in the feed pretreatment and preheating section of an SMR plant are carbon steel (CS), chromium-molybdenum low alloy steels (CrMo), and stainless steel (SS).
In short, of the applied steels, especially iron, but also important alloying elements like chromium, can easily form nitrides. Furthermore, the majority of process equipment in a syngas generation unit is operated well above 400°C. Therefore, it is not feasible to simply switch the feedstock from hydrocarbons to ammonia for an existing hydrogen production facility.
[0009] As such, there is a need in the art to provide industrial facilities that can efficiently produce hydrogen from ammonia, particularly by retrofitting existing hydrogen production industrial facilities to produce hydrogen from an ammonia feed gas while preventing, delaying, or at least minimizing embrittlement issues during operation.
SUMMARY OF THE INVENTION
[0010] The present invention is directed to an apparatus and process that satisfies at least one of these needs. In certain embodiments of the invention, a protective liner is applied in a common catalyst tube. In a second embodiment, the invention can include application of an aluminization layer on the inner tube surface. In a third embodiment that addresses resistance against nitridation at very high temperatures (e.g., above about 700°C), a diffusion barrier can be applied between the aluminization layer and the tube material to limit diffusion between the aluminization layer and the tube material. This diffusion barrier is preferably configured to block, or at least minimize, any interaction between the substrate (i.e., aluminization layer) and the environment. In a fourth embodiment, a weld-overlay can be applied to the inner surface of the catalyst tube.
[0011] In one embodiment, the method for converting an existing steam methane reformer (SMR) to produce hydrogen via ammonia cracking by adding a protective layer to an inner surface of equipment to be used in the existing SMR can include the steps of: providing the existing SMR, wherein the SMR was formerly used to produce hydrogen from a hydrocarbon feedstock; and
improving the nitridation resistance of the inner surface of the equipment, wherein the equipment is selected from the group consisting of a catalyst tube, feed piping, a feed preheater, process gas heat exchangers, and combination thereof.
[0012] In optional embodiments of the method:
• the step of improving the nitridation resistance includes a process selected from the group consisting of applying a protective liner material that is mechanically coupled to the inner surface, applying an aluminization layer to the inner surface, applying a diffusion barrier layer in conjunction with the aluminization layer, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and applying a weld-overlay to the inner surface;
• the step of improving the nitridation resistance comprises applying an aluminization layer to the inner surface;
• the step of applying the aluminization layer comprises the steps of: introducing an aluminization source powder into an internal space delimited by the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; transferring aluminum from the aluminization source powder to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide layer; and removing the aluminization source powder from the internal space;
• the step of applying the aluminization layer comprises the steps of: depositing an aluminization slurry layer on the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; drying the slurry layer; transferring aluminum from the aluminization slurry to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide layer; and removing the remains of the aluminization slurry from the internal space;
• the step of improving the nitridation resistance comprises applying a diffusion barrier layer to the inner surface of the piece of equipment, and applying an aluminization layer to the diffusion barrier layer, such that the diffusion barrier layer is disposed between the inner surface of the piece of equipment and the aluminization layer;
• the diffusion barrier layer comprises a chrome-silicon barrier layer;
• the step of improving the nitridation resistance comprises applying a protective liner that is mechanically coupled to the inner surface;
• the protective liner material is selected from a group of alloys having a nickel content in excess of 60%;
• the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion;
• the protective liner is coupled to the inner surface of the equipment via a flange or welding;
• the protective liner is configured to have a substantially similar thermal expansion coefficient to that of the piece of equipment;
• the step of improving the nitridation resistance comprises applying a protective weld-overlay to the inner surface;
• the protective weld-overlay is selected from a group of alloys having a nickel content in excess of 60%; and/or
• the equipment that has improved nitridation resistance is a new piece of equipment or was previously used in the existing SMR.
[0013] In another embodiment, the method can include the steps of: providing the existing hydrogen industrial unit, wherein the hydrogen industrial unit was formerly used to produce
hydrogen from a hydrocarbon feedstock; and improving the nitridation resistance of an inner surface of the equipment, wherein the equipment that has improved nitridation resistance is a new piece of equipment or was previously used in the existing hydrogen industrial unit.
[0014] In optional embodiments of the method:
• the equipment is selected from the group consisting of feed preheaters, feed piping, catalyst tubes, process gas heat exchangers, outlet system, process gas boiler, and combinations thereof; and/or
• the protective layer is applied to equipment that is configured to be in fluid communication with an ammonia feed gas at temperatures exceeding 400 °C.
[0015] In another embodiment, a hydrogen production facility is provided and can include: a reformer configured to catalytically convert a feed stream into a product stream comprising hydrogen, the reformer having a plurality of catalyst tubes and a plurality of burners configured to provide heat to the catalyst tubes; means for providing the feed stream to the reformer from an ammonia source, wherein the feed stream comprises at least 90% of ammonia, wherein the plurality of catalyst tubes comprise a nitridation protective layer on an inner surface of the catalyst tubes.
[0016] In optional embodiments of the apparatus:
• the nitridation protective layer is selected from the group consisting of a protective liner material that is mechanically coupled to the inner surface, an aluminization layer applied to the inner surface, a diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and a weld-overlay applied to the inner surface;
• the nitridation protective layer comprises the diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface;
• the diffusion barrier layer comprises a chrome-silicon barrier layer;
• the nitridation protective layer comprises applying a protective liner that is mechanically coupled to the inner surface;
• the protective liner material is selected from a group of alloys having a nickel content in excess of 60%;
• the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion;
• the protective liner is coupled to the inner surface of the equipment via a flange or welding;
• the protective liner is configured to have a substantially similar thermal expansion coefficient to that of the piece of equipment;
• the nitridation protective layer comprises a protective weld-overlay applied to the inner surface;
• the protective weld-overlay is selected from a group of alloys having a nickel content in excess of 60%;
• the hydrogen production facility was formerly used to catalytically crack hydrocarbons in the presence of steam to produce hydrogen; and/or
• the hydrogen production facility can also include additional equipment having the nitridation protective layer, wherein the additional equipment is selected from the group consisting of feed piping, a feed preheater, process gas heat exchangers, and combination thereof.
[0017] The foregoing has outlined rather broadly the features and technical advantages of the present invention in order that the detailed description of the invention that follows may be better understood. Additional features and advantages of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and specific embodiment disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims. The novel features, which are believed to be characteristic of the invention, both as to its organization and method of operation, together with further objects and advantages, will be better understood from the following description when considered in connection with the accompanying figures. It is to be expressly understood, however, that the figures are provided for the purpose of illustration and description only and are not intended as a definition of the limits of the present invention.
BRIEF DESCRIPTION OF THE DRAWINGS
[0018] These and other features, aspects, and advantages of the present invention will become better understood with regard to the following description, claims, and accompanying drawings. It is to be noted, however, that the drawings illustrate only several embodiments of the invention and are therefore not to be considered limiting of the invention’s scope as it can admit to other equally effective embodiments.
[0019] FIG. 1 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a first embodiment of the present invention having a welded or flanged liner.
[0020] FIG. 2 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a second embodiment of the present invention having an aluminization layer without a diffusion barrier layer.
[0021] FIG. 3 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a third embodiment of the present invention having an aluminization layer with a diffusion barrier layer between the aluminization layer and the base material.
[0022] FIG. 4 shows an embodiment of a cross-sectional view of a catalyst tube in conformance with a fourth embodiment of the present invention having a weld-overlay.
DETAILED DESCRIPTION
[0023] While the invention will be described in connection with several embodiments, it will be understood that it is not intended to limit the invention to those embodiments. On the contrary, it is intended to cover all the alternatives, modifications and equivalence as may be included within the spirit and scope of the invention defined by the appended claims.
[0024] As used herein, “aluminization layer” is intended to cover a diffusion layer that includes a mixture of iron and nickel aluminides (e.g., FeAl, NiAl) with a preferred aluminum content of between 25-40 wt%.
[0025] While the current disclosure focuses on the protection of catalyst tubes, Applicants note that the inventive idea does not need to be restricted to its application in catalyst tubes only. It can also be used in some of the upstream equipment, if needed, for example in the feed superheating coils, heat exchangers, and connecting piping. This will be highly preferable, if the tie-in point is shifted further upstream in the process, for whatever reason, e.g., preheating of ammonia and heat
integration of the flue gas and splitting of NH3 starting prior to entering the catalyst tubes due to temperature and a certain catalytic effect of metallic surfaces.
[0026] Formation of nitrides from elemental nickel is not documented in literature. The beneficial effects of reducing the nitridation susceptibility using nickel in steels include lower solubility of nitrogen and lower diffusion rates of nitrogen in alloys with nickel content up to 40 wt.%. However, some high content nickel base alloys are known to better withstand nitride formation and embrittlement as the aforementioned. One such candidate is Alloy 600. The currently used high-temperature, high-creep-strength catalyst tube material does not belong to these materials. Hence, the task is to optimize the material for the selection for the inner diameter surface of the catalyst tubes that are potentially affected by nitridation — either by replacing them with tubes made from another material or to coat/weld-overlay or line the inner diameter surface of the catalyst tube with a material having a lower nitridation embrittlement susceptibility.
[0027] Catalyst tubes have to be resistant not only against the inner process conditions but also against the outer high temperature flue gas atmosphere while providing sufficient creep strength, which materials with high nitridation resistance typically do not possess. Therefore, certain embodiments of the present invention concentrate on improving the nitridation resistance on the inside of the common catalyst tubes by applying an appropriate selection of a resistant material. The resistant material can be a very thin layer applied on the material surface, a combination of layers, or a thicker lining or weld-overlay. The resistant material can also be chosen in combination with an oxidizing process medium in such a manner that, due to a more oxidizing atmosphere, the material forms a protective oxide layer upon exposure to the ammonia and oxidizing agent mixture.
[0028] In certain embodiments, the liner material can be selected to be nickel or an alloy with a very high nickel content (Nickel content similar or higher than in alloy 600, i.e. Ni > 60% ). FIG. 1 provides a cross sectional view of a catalyst tube 1 having an outer wall 2 in accordance with these embodiments. In the embodiment shown, the liner 10 can be flanged to the inlet or welded 12 to the inner wall 3 of the catalyst tube 1. In these embodiments, either the protective liner 10 can be attached to the inner wall 3 of the catalyst tube only at one side (inlet), so that the different thermal expansion coefficients of the materials will not lead to damage of the liner 10 or the catalyst tube itself, or the material composition of the liner 10 is chosen such, that its thermal expansion coefficient is substantially similar to that of the catalyst tube 1. The latter solution would also allow the use of a material with non-optimal resistance against nitridation, but with the intention to replace it after reaching an appropriate lifetime. As used herein, an expansion coefficient that is “substantially similar” means that the expansion coefficients are the same +/- 5%, or close enough that differences in thermal expansion do not cause problems in production or result in safety issues.
[0029] FIG. 2 provides another embodiment of the invention, which can include application of an aluminization layer 15 on the inner wall 3 (e.g., inner surface). Although an aluminum-containing alloy with only some percent aluminum is known to be very susceptible to nitridation because aluminum is a strong nitride former, at very high aluminum content, as it is the case in such a coating, a protective oxide layer will form at the surface, even in atmospheres with low oxygen partial pressure. The coating process could be, but is not limited to, aluminization by pack cementation.
[0030] In certain embodiments using pack cementation, a conversion layer with high aluminide
(e.g., NisAl) content with a controlled thickness can be achieved.
[0031] The steps for providing the aluminization layer to an article having an internal cavity for protection against embrittlement can include introducing an aluminization source powder into the internal cavity through an inlet; heating the article with the aluminization source powder in the internal cavity to cause aluminum to transport from the aluminization source powder to the internal surface of the internal cavity; and thereafter removing the aluminization source powder from the internal cavity through the inlet.
[0032] FIG. 3 provides a similar solution to that shown in FIG. 2; however, in this embodiment, very high temperatures (e.g. above about 700 °C) might introduce diffusion processes between the base material 17 of the catalyst tube 1 and the aluminization layer 15, which might affect the protective effect of the coating itself. Therefore, in addition to the aluminization layer 15, by modification of the aluminization process, another layer is disposed between the aluminization layer 15 and the tube material 17 and works as a diffusion barrier 20. This additional barrier layer can be, as a non-limiting example, a chrome-silicon barrier layer.
[0033] As illustrated in FIGS. 2 and 3, one solution of the present invention is a catalyst tube 1 comprising: an external wall 2, an internal wall 3, an aluminization layer 15 mirroring at least a portion of the internal wall, a diffusion barrier 20 mirroring at least a portion of the internal wall, wherein the diffusion barrier 20 is between the internal wall 3 and the aluminization layer 15.
[0034] As the case may be, the catalyst tube according to the present invention can exhibit one or more of the following characteristics: the diffusion barrier 20 matches the shape of the internal wall 3 and the shape of the aluminization layer 15; the diffusion barrier 20 can be a chrome-silicon barrier layer disposed between the tube material 17 and the aluminization layer 15.
[0035] Preferably, the diffusion barrier fits the shape of the internal wall of the tube. The diffusion barrier must be selected as a function of its ability to withstand operating conditions at high temperature (700 to 1000° C.)
[0036] FIG. 4 provides yet another embodiment, in which resistance to nitridation can be achieved by adding a resistant weld-overlay 25 to the inner wall 3 of components in contact with ammonia and ammonia-cracking products. A few non-limiting examples can include catalyst tubes, piping, heat coil, heat exchanger tube, etc. . . This resistant material can include a nickel-base alloy with a minimum 60% nickel, and forms a barrier between the tube side medium and the internal metallic tube wall. This weld-overlay is a type of cladding, where the high nickel metal is added to the surface of the inner tube wall by melting a weld consumable and depositing it in one or more welding passes. Contrary to a solid liner material, the final closed surface of a weld-overlay is built up by overlapping single weld beads into a closed, protective surface.
[0037] While the invention has been described in conjunction with specific embodiments thereof, it is evident that many alternatives, modifications, and variations will be apparent to those skilled in the art in light of the foregoing description. Accordingly, it is intended to embrace all such alternatives, modifications, and variations that fall within the spirit and broad scope of the appended claims. The present invention may suitably comprise, consist or consist essentially of the elements disclosed and may be practiced in the absence of an element not disclosed. Furthermore, language referring to order, such as first and second, should be understood in an exemplary sense and not in a limiting sense. For example, it can be recognized by those skilled in the art that certain steps or devices can be combined into a single step/device.
[0038] The singular forms "a", "an", and "the" include plural referents, unless the context clearly dictates otherwise. The terms about/approximately a particular value include that particular value plus or minus 10%, unless the context clearly dictates otherwise.
[0039] Optional or optionally means that the subsequently described event or circumstances may or may not occur. The description includes instances where the event or circumstance occurs and instances where it does not occur.
[0040] Ranges may be expressed herein as from about one particular value, and/or to about another particular value. When such a range is expressed, it is to be understood that another embodiment is from the one particular value and/or to the other particular value, along with all combinations within said range.
Claims
1. A method for converting an existing steam methane reformer (SMR) to produce hydrogen via ammonia cracking by adding a protective layer to an inner surface of equipment to be used in the existing SMR, the method comprising the steps of: providing the existing SMR, wherein the SMR was formerly used to produce hydrogen from a hydrocarbon feedstock; and improving the nitridation resistance of the inner surface of the equipment, wherein the equipment is selected from the group consisting of a catalyst tube, feed piping, a feed preheater, process gas heat exchangers, and combination thereof.
2. The method as claimed in Claim 1, wherein the step of improving the nitridation resistance includes a process selected from the group consisting of applying a protective liner material that is mechanically coupled to the inner surface, applying an aluminization layer to the inner surface, applying a diffusion barrier layer in conjunction with the aluminization layer, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and applying a weld-overlay to the inner surface.
3. The method as claimed in Claim 1 , wherein the step of improving the nitridation resistance comprises applying an aluminization layer to the inner surface.
4. The method as claimed in Claim 3, wherein the step of applying the aluminization layer comprises the steps of :
introducing an aluminization source powder into an internal space delimited by the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; transferring aluminum from the aluminization source powder to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide-rich layer; and removing the aluminization source powder from the internal space.
5. The method as claimed in Claim 3, wherein the step of applying the aluminization layer comprises the steps of depositing an aluminization slurry layer on the inner surface of the equipment through an inlet, the inner surface of the equipment comprising a base metal; drying the slurry layer; transferring aluminum from the aluminization slurry to the inner surface of the equipment by heating said equipment and allowing the aluminum to diffuse and react with elements in the base metal to form an aluminide-rich layer; and removing the remains of the aluminization slurry from the internal space.
6. The method as claimed in Claim 1, wherein the step of improving the nitridation resistance comprises applying a diffusion barrier layer to the inner surface of the piece of equipment, and applying an aluminization layer to the diffusion barrier layer, such that the diffusion barrier layer is disposed between the inner surface of the piece of equipment and the aluminization layer.
7. The method as claimed in Claim 6, wherein the diffusion barrier layer comprises a chromesilicon barrier layer.
8. The method as claimed in Claim 1, wherein the step of improving the nitridation resistance comprises applying a protective liner that is mechanically coupled to the inner surface.
9. The method as claimed in Claim 8, wherein the protective liner material is selected from a group of alloys having a nickel content in excess of 60%.
10. The method as claimed in Claim 8, wherein the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion.
11. A hydrogen production facility comprising: a reformer configured to catalytically convert a feed stream into a product stream comprising hydrogen, the reformer having a plurality of catalyst tubes and a plurality of burners configured to provide heat to the catalyst tubes; and means for providing the feed stream to the reformer from an ammonia source, wherein the feed stream comprises at least 90% of ammonia a reformer configured to catalytically convert a feed stream into a product stream comprising hydrogen, the reformer having a plurality of catalyst tubes and a plurality of burners configured to provide heat to the catalyst tubes; and means for providing the feed stream to the reformer from an ammonia source, wherein the feed stream comprises at least 90% of ammonia, wherein the plurality of catalyst tubes comprise a nitridation protective layer on an inner surface of the catalyst tubes.
12. The hydrogen production facility as claimed in Claim 11, wherein the nitridation protective layer is selected from the group consisting of a protective liner material that is mechanically
coupled to the inner surface, an aluminization layer applied to the inner surface, a diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface, wherein the diffusion barrier layer is disposed between the inner surface and the aluminization layer, and a weld-overlay applied to the inner surface.
13. The hydrogen production facility as claimed in Claim 11 , wherein the nitridation protective layer comprises the diffusion barrier layer in conjunction with the aluminization layer applied to the inner surface.
14. The hydrogen production facility as claimed in Claim 13, wherein the diffusion barrier layer comprises a chrome-silicon barrier layer.
15. The hydrogen production facility as claimed in Claim 11 , wherein the nitridation protective layer comprises applying a protective liner that is mechanically coupled to the inner surface.
16. The hydrogen production facility as claimed in Claim 15, wherein the protective liner material is selected from a group of alloys having a nickel content in excess of 60%.
17. The hydrogen production facility as claimed in Claim 15, wherein the protective liner is coupled to the inner surface via at only one end thereby reducing potential damage during thermal expansion.
18. The hydrogen production facility as claimed in Claim 15, wherein the protective liner is coupled to the inner surface of the equipment via a flange or welding.
19. The hydrogen production facility as claimed in Claim 15, wherein the protective liner is configured to have a substantially similar thermal expansion coefficient to that of the piece of equipment.
20. The hydrogen production facility as claimed in Claim 11 , wherein the nitridation protective layer comprises a protective weld-overlay applied to the inner surface
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US17/896,026 US20240068081A1 (en) | 2022-08-25 | 2022-08-25 | Method for converting an existing industrial unit to produce hydrogen from ammonia |
US17/896,029 | 2022-08-25 | ||
US17896026 | 2022-08-25 | ||
US17/896,029 US20240066493A1 (en) | 2022-08-25 | 2022-08-25 | Hydrogen production facility having equipment with a nitridation protective layer |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2024043908A1 true WO2024043908A1 (en) | 2024-02-29 |
Family
ID=90013761
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2022/041910 WO2024043908A1 (en) | 2022-08-25 | 2022-08-29 | A method for converting an existing industrial unit to produce hydrogen from ammonia |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2024043908A1 (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4401153A (en) * | 1980-06-14 | 1983-08-30 | Uhde Gmbh | Heat exchanger incorporating nitriding-resistant material |
US20050100693A1 (en) * | 2003-11-12 | 2005-05-12 | Mesofuel, Incorporated | Hydrogen generation reactor chamber with reduced coking |
US20050233599A1 (en) * | 2001-01-22 | 2005-10-20 | Tokyo Electron Limited | Method for producing material of electronic device |
US20080005965A1 (en) * | 2005-11-04 | 2008-01-10 | Speranza A J | System for providing high purity hydrogen and method thereof |
US20150099876A1 (en) * | 2013-10-04 | 2015-04-09 | Academia Sinica | Molecular Catalysts Capable of Catalyzing Oxidation of Hydrocarbons and Method for Oxidizing Hydrocarbons |
US20150211309A1 (en) * | 2012-01-31 | 2015-07-30 | Wagon Trail Ventures, Inc. | Lined downhole oilfield tubulars |
US20180178188A1 (en) * | 2016-12-22 | 2018-06-28 | Extiel Holdings, Llc | Sectionalized box style steam methane reformer |
US20190084831A1 (en) * | 2016-03-14 | 2019-03-21 | Equinor Energy As | Ammonia cracking |
-
2022
- 2022-08-29 WO PCT/US2022/041910 patent/WO2024043908A1/en unknown
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4401153A (en) * | 1980-06-14 | 1983-08-30 | Uhde Gmbh | Heat exchanger incorporating nitriding-resistant material |
US20050233599A1 (en) * | 2001-01-22 | 2005-10-20 | Tokyo Electron Limited | Method for producing material of electronic device |
US20050100693A1 (en) * | 2003-11-12 | 2005-05-12 | Mesofuel, Incorporated | Hydrogen generation reactor chamber with reduced coking |
US20080005965A1 (en) * | 2005-11-04 | 2008-01-10 | Speranza A J | System for providing high purity hydrogen and method thereof |
US20150211309A1 (en) * | 2012-01-31 | 2015-07-30 | Wagon Trail Ventures, Inc. | Lined downhole oilfield tubulars |
US20150099876A1 (en) * | 2013-10-04 | 2015-04-09 | Academia Sinica | Molecular Catalysts Capable of Catalyzing Oxidation of Hydrocarbons and Method for Oxidizing Hydrocarbons |
US20190084831A1 (en) * | 2016-03-14 | 2019-03-21 | Equinor Energy As | Ammonia cracking |
US20180178188A1 (en) * | 2016-12-22 | 2018-06-28 | Extiel Holdings, Llc | Sectionalized box style steam methane reformer |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EA011289B1 (en) | Composite tube | |
EP1322800B1 (en) | Surface on a stainless steel | |
US11213795B2 (en) | Corrosion-protected reformer tube with internal heat exchange | |
EP1325174B1 (en) | Process of treating stainless steel | |
CN105441112B (en) | Method for online treating of inner surface of hydrocarbon cracking furnace tube | |
US10207242B2 (en) | Alumina forming refinery process tubes with mixing element | |
CA3047160A1 (en) | Corrosion-protected reformer tube with internal heat exchange | |
WO2003072836A1 (en) | Copper based alloy resistant against metal dusting and its use | |
US20240068081A1 (en) | Method for converting an existing industrial unit to produce hydrogen from ammonia | |
US20240066493A1 (en) | Hydrogen production facility having equipment with a nitridation protective layer | |
WO2024043908A1 (en) | A method for converting an existing industrial unit to produce hydrogen from ammonia | |
US7543733B2 (en) | Method of protecting against corrosion at high temperature | |
CN106590724A (en) | Method for on-line repairing of manganese chromium spinel thin film of cracking furnace pipe | |
US20220119933A1 (en) | Anti-Coking Iron Spinel Surface | |
Lahiri et al. | Material Selection and Performance in Fertilizer Industry | |
US20210261790A1 (en) | Coated systems for hydrogen | |
JP2024074792A (en) | Process and apparatus for decomposing ammonia | |
JP2024074791A (en) | Process and apparatus for decomposing ammonia | |
EP1606050A1 (en) | Method of protecting equipment against corrosion at high temperature | |
CN118056780A (en) | Method and apparatus for cracking ammonia | |
Bayer | Surface engineered coatings for metal dusting | |
Evaluati0n | Problems, world records | |
TO et al. | INTERNATIONAL JOURNAL OF ADVANCED RESEARCH IN ENGINEERING AND TECHNOLOGY (IJARET) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 22956655 Country of ref document: EP Kind code of ref document: A1 |