Patent Application
20240068081
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.
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.
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.
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.
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.
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.
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.
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.
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.
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.
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.
In optional embodiments of the method:
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.
In optional embodiments of the method:
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.
In optional embodiments of the apparatus:
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.
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.
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.
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 %.
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.
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.
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.
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%).
In certain embodiments using pack cementation, a conversion layer with high aluminide (e.g., Ni3Al) content with a controlled thickness can be achieved.
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.
As illustrated in
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.
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.)
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.
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.
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.
