METHODS FOR SELF-ASSEMBLING MONOLAYERS TO MITIGATE HYDROGEN PERMEATION
20240342753 ยท 2024-10-17
Inventors
Cpc classification
International classification
B05D3/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The presently disclosed methods provide for preparing a stable hydrophobic self-assembled monolayer (SAM) coating, that includes preparing a SAM solution by combining a SAM compound with an initial solvent and an additional solvent and mixing, in a sealed container, the SAM solution at a first fixed temperature at a constant rotational speed for a first fixed time interval. The SAM coating is then prepared by treating a substrate to achieve pristine state, and heating the substrate at a second fixed temperature for a second fixed time interval. Then within a sealed container, immersing the substrate in the SAM solution for a third fixed time interval. Following the completion of the third fixed time interval, the substrate is removed from the sealed container and treated with the initial solvent and the additional solvent to remove excess SAM material, and heated at a third fixed temperature.
Claims
1. A method for preparing a stable hydrophobic self-assembled monolayer (SAM) coating, preparing a SAM solution, wherein the preparation of the SAM solution comprises: combining a first quantity of a SAM compound to a second quantity of an initial solvent and a third quantity of an additional solvent to form the SAM solution; and mixing, in a first sealed container, the SAM solution at a first fixed temperature at a constant rotational speed for a first fixed time interval; preparing the SAM coating, wherein the preparation of the SAM coating comprises: treating a substrate to achieve pristine state; heating the substrate at a second fixed temperature for a second fixed time interval; within a second sealed container, immersing the substrate in the SAM solution for a third fixed time interval; and following the completion of the third fixed time interval: removing the substrate from the sealed container; treating the substrate with the initial solvent and the additional solvent to remove excess SAM material; and heating the substrate at a third fixed temperature for a fourth fixed time interval.
2. The method of claim 1, wherein the SAM compound is C10 fluoroalkylphosphonic acid.
3. The method of claim 1, wherein the substrate is steel.
4. The method of claim 3, wherein the substrate is selected from at least one of: API 5L X70 steel and stainless steel 430.
5. The method of claim 1, wherein mixing the SAM solution comprises at least one of: implementation of a magnetic stir bar, and sonication via tip sonicator.
6. The method of claim 1, wherein heating the substrate at a second fixed temperature or heating the substrate at a third fixed temperature comprises at least one of: heating the substrate on a hot plate, and heating the substrate in an oven.
7. The method of claim 1, wherein the treating the substrate to achieve pristine state comprises at least one of the following: treating the substrate with one or more solvents, heating the substrate to 5000 for a specific time interval, and implementation of plasma cleaning to the substrate.
8. The method of claim 1, wherein the initial solvent and the additional solvent are methanol and isopropanol respectively.
9. The method of claim 1, wherein the SAM compound, initial solvent, and additional solvent are provided in a weight ratio of 1/124.5/124.5 respectively.
10. The method of claim 1, wherein mixing the SAM solution at a first fixed temperature at a constant rotational speed for a first fixed time interval comprises 30? C., 100 rpm, and 48 hours respectively.
11. The method of claim 1, wherein the third fixed time interval is 48 hours.
12. The method of claim 1, wherein heating the substrate at a third fixed temperature for a fourth fixed time interval comprises 100? C. for 30 minutes respectively.
13. A method for preparing a stable hydrophobic self-assembled monolayer (SAM) coating, comprising: preparing a SAM solution, wherein the preparation of the SAM solution comprises: combining C10 fluoroalkylphosphonic acid to methanol of isopropanol to form the SAM solution; and mixing, in a first sealed container, the SAM solution at 30? C. at 100 rpm for a 48 hour interval; preparing the SAM coating, wherein the preparation of the SAM coating comprises: treating a steel to achieve pristine state; heating the steel at 100? C. for 30 minutes; within a second sealed container, immersing the steel in a sealed container for 48 hours; and following the completion of the 48 hours: removing the steel from the sealed container; treating the steel to remove excess SAM material; and heating the steel at 100? C. for 30 minutes.
14. The method of claim 13 wherein the C10 fluoroalkylphosphonic acid, methanol, and isopropanol are provided in a weight ratio of 1/124.5/124.5 respectively.
15. The method of claim 13 wherein the steel is selected from at least one of API 5L X70 steel and stainless steel 430.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] The below and other objects and advantages of the disclosure will be apparent upon consideration of the following detailed description, taken in conjunction with the accompanying drawings, in which the reference characters refer to like parts throughout, and in which:
[0008]
[0009]
[0010]
[0011]
[0012]
[0013]
[0014]
[0015]
[0016]
[0017]
[0018]
DETAILED DESCRIPTION
[0019] The disclosed methods herein provide for self-assembled monolayer coatings that disrupted hydrogen permeation and consequently reduced hydrogen embrittlement. In some embodiments, the coating may be fluoroalkyl (C10) phosphonic acid (FAPA).
[0020] For lab testing, the FAPA used in this research was procured from Specific Polymers in France. Two types of steel were tested in this research under identical controlled environmentsstainless steel 430 (430SS) and API 5L X70 steel (X70). In lab testing, both samples of steel were cut into squares and rectangles with a thickness of 300 micrometers.
[0021] The disclosed methods provide for preparing a SAM solution by combining a first quantity of a SAM compound to a second quantity of an initial solvent and a third quantity of an additional solvent to form the SAM solution.
[0022] The disclosed methods provide that the SAM solution is mixed, in a sealed container, at a first fixed temperature at a constant rotational speed for a first fixed time interval. In some embodiments, the temperature is set to 30? C. to enhance the dissolution of the SAM in the solvents. In some embodiments, the temperature may be adjusted to a set temperature that is lower than the boiling point of the solvent. As an example, methanol has a boiling point of 64? C. Thus, the temperature may be adjusted to any temperature less than 64? C. In some embodiments, to increase the temperature, a hot plate may be implemented, and/or the solution may be inserted into an oven. The mixing is performed within a sealed container. As shown in FIG. 9, step 906, a SAM solution is being heated on a hotplate 907 and has a seal 910 on the container of SAM solution 909. In some embodiments, the sealed container is a bottle, a sealed glassware, and/or any container which prevents evaporation loss of solvent. The rotational speed that was found to be optimal was 100-200RPM. The rotational speed cannot be increased to a rate where the solvent mixing is overly turbulent. Turbulence may result in ineffective mixing of the SAM to the solvents. In some embodiments, mixing the SAM solution may implement a magnetic stir bar, and/or sonication via tip sonicator.
[0023] The disclosed methods include preparing the SAM coating. To prepare the coating, the substrate may be treated to achieve pristine state. A pristine state may be defined as the surface organic contamination is below a threshold of 15% by atomic percentage. In some embodiments, the treatment process may implement a solvent bath utilizing solvents, heating the substrate to 500? C. for a specific time interval, and/or implementation of plasma cleaning to the substrate.
[0024] The disclosed methods provide for heating the substrate at a second fixed temperature for a second fixed time interval. As mentioned previously, this is done to ensure there is minimal surface contamination of the substrate. In some embodiments, the second fixed temperature is configured at 100? C. for 30 minutes.
[0025] The disclosed methods provide, within a sealed container, immersing the substrate in the SAM solution for a third fixed time interval. This step allows the SAM solution to self assemble on the substrate. From lab results, optimal configuration suggests 48 hours time interval to allow for self-assembly. In some embodiments, a 24 hours interval may be sufficient for self-assembly depending on the SAM variant used.
[0026] The disclosed methods provide, following the completion of the third fixed time interval, the substrate is removed from the sealed container and treated with the initial solvent and the additional solvent to remove excess SAM material. Occasionally, excess SAM material may be deposited on the substrate and requires removal. Removal is achieved by treating the coated substrate with the initial solvent and the additional solvent (e.g., methanol and isopropanol).
[0027] The disclosed methods provide that the final step of preparing the SAM coating involves heating the substrate at a third fixed temperature for a fourth fixed time interval to strengthen the adhesion to the substrate. In some embodiments, the substrate (e.g. API 5L X70 steel) may be heated at 100? C. for 30 minutes.
[0028] After performing the above technique, laboratory results provided empirical proof of the efficacy of the coating.
[0029]
[0030]
[0031] As the hydrogen passed through the steel sample, it was oxidized in the exit cell to protons, releasing electrons in the process. This electrical current associated with hydrogen oxidation was detected by a potentiostat in the exit cell. A constant potential of 300 mV with respect to an alkaline Hg/HgO electrode (CH instruments) was applied in the exit cell. From this current, we used well-established time-lag based diffusion models.sup.4,11 to determine the hydrogen diffusion coefficient (measure of hydrogen permeability of a material) as well as the hydrogen flux.
[0032] Key metrics for determining hydrogen permeation are the hydrogen diffusion coefficient and flux. Flux quantifies the moles of hydrogen passing through a m.sup.2 of area of steel per second and hydrogen diffusion coefficient is a direct measure of the ability of the material to conduct hydrogen. These parameters are minimized using the FAPA monolayer, thus reducing the risk of hydrogen embrittlement in pipelines.
TABLE-US-00001 Value 430SS 430SS with Monolayer Hydrogen Diffusion (m.sup.2/s) .sup.3.98 ? 10.sup.?12 1.77 ? 10.sup.?12 Hydrogen Flux (mol/s/m.sup.2) 18.72 ? 10.sup.?8 7.24 ? 10.sup.?8 Value X70 X70 with Monolayer Hydrogen Diffusion (m.sup.2/s) 4.68 ? 10.sup.?12 0.51 ? 10.sup.?12 Hydrogen Flux (mol/s/m.sup.2) 8.02 ? 10.sup.?8 1.45 ? 10.sup.?8
[0033] As seen in the table above, there is a two-fold reduction in the hydrogen diffusion coefficient in 430 stainless steels. In the case of X70 steel we see a ten-fold reduction in the hydrogen diffusion coefficient.
[0034] Many pipelines are typically made using X70 and X80 steels..sup.12 The illustrated reduction in the diffusion of hydrogen through these steels is a promising step towards bringing the pipelines up to standard for safely transporting hydrogen gas. Hydrogen embrittlement is caused by the flux of hydrogen atoms through steel, and thus a reduction in the hydrogen flux through steel coated with the FAPA monolayer reduces the risk caused by hydrogen embrittlement. These results demonstrate that the FAPA monolayer coating reduces hydrogen permeation even at a bare-minimum thickness of a few molecules. Realistically, the applied coating can be much thicker than a few molecules thereby providing more protection by increasing resistance to hydrogen diffusion.
[0035] Many pipelines are typically made using X70 and X80 steels..sup.12 The illustrated reduction in the diffusion of hydrogen through these steels is a promising step towards mitigating hydrogen embrittlement.
[0036]
[0037] At 1102, a SAM solution is prepared that includes the following sub-steps. At step 1104, a first quantity of a SAM compound is combined to a second quantity of an initial solvent and a third quantity of an additional solvent to form the SAM solution. At step 1106, in a first sealed container, the SAM solution is mixed at a first fixed temperature at a constant rotational speed for a first fixed time interval.
[0038] At 1108, the SAM coating is prepared that includes the following sub-steps. At step 1110, the substrate is treated to achieve pristine state. At step 1112, the substrate is heated at a second fixed temperature for a second fixed time interval. At step 1114, within a second sealed container, the substrate is immersed in a sealed container for a third fixed time interval. At step 1116, the substrate is removed from the sealed container. At step 1118, the substrate is treated to remove excess SAM material. At step 1120, the substrate is heated at a third fixed temperature for a fourth fixed time interval.
[0039] It is contemplated that the steps or descriptions of
[0040] The processes discussed above are intended to be illustrative and not limiting. One skilled in the art would appreciate that the steps of the processes discussed herein may be omitted, modified, combined, and/or rearranged, and any additional steps may be performed without departing from the scope of the invention. More generally, the above disclosure is meant to be exemplary and not limiting. Only the claims that follow are meant to set bounds as to what the present invention includes. Furthermore, it should be noted that the features and limitations described in any one embodiment may be applied to any other embodiment herein, and flowcharts or examples relating to one embodiment may be combined with any other embodiment in a suitable manner, done in different orders, or done in parallel. In addition, the systems and methods described herein may be performed in real time. It should also be noted that the systems and/or methods described above may be applied to, or used in accordance with, other systems and/or methods.
Interpretation of Terms
[0041] Unless the context clearly requires otherwise, throughout the description and any accompanying claims (where present), the words comprise, comprising, and the like are to be construed in an inclusive sense, that is, in the sense of including, but not limited to. As used herein, the terms connected, coupled, or any variant thereof, means any connection or coupling, either direct or indirect, between two or more elements; the coupling or connection between the elements can be physical, logical, or a combination thereof. Additionally, the words herein, above, below, and words of similar import, shall refer to this document as a whole and not to any particular portions. Where the context permits, words using the singular or plural number may also include the plural or singular number respectively. The word or, in reference to a list of two or more items, covers all of the following interpretations of the word: any of the items in the list, all of the items in the list, and any combination of the items in the list.
[0042] Various features are described herein as being present in some embodiments. Such features are not mandatory and may not be present in all embodiments. Embodiments of the invention may include zero, any one or any combination of two or more of such features. This is limited only to the extent that certain ones of such features are incompatible with other ones of such features in the sense that it would be impossible for a person of ordinary skill in the art to construct a practical embodiment that combines such incompatible features. Consequently, the description that some embodiments possess feature A and some embodiments possess feature B should be interpreted as an express indication that the inventors also contemplate embodiments which combine features A and B (unless the description states otherwise or features A and B are fundamentally incompatible).
[0043] Specific examples of systems, methods and apparatus have been described herein for purposes of illustration. These are only examples. The technology provided herein can be applied to systems other than the example systems described above. Many alterations, modifications, additions, omissions, and permutations are possible within the practice of this invention. This invention includes variations on described embodiments that would be apparent to the skilled addressee, including variations obtained by: replacing features, elements and/or acts with equivalent features, elements and/or acts; mixing and matching of features, elements and/or acts from different embodiments; combining features, elements and/or acts from embodiments as described herein with features, elements and/or acts of other technology; and/or omitting combining features, elements and/or acts from described embodiments.
[0044] While a number of exemplary aspects and embodiments have been discussed above, those of skill in the art will recognize certain modifications, permutations, additions and sub-combinations thereof. It is therefore intended that the following appended claims and claims hereafter introduced are interpreted to include all such modifications, permutations, additions and sub-combinations as are consistent with the broadest interpretation of the specification as a whole.
REFERENCES
[0045] 1. Yue, M. et al. Hydrogen energy systems: A critical review of technologies, applications, trends and challenges. Renewable and Sustainable Energy Reviews 146, 111180 (2021). [0046] 2. The Hydrogen Strategy for Canada. Clean50 https://clean50.com/projects/lofty-ambitions-for-hydrogen-development-and-implementation-of-the-hydrogen-strategy-for-canada % e2%80% af/(2021). [0047] 3. CER-Canada's Pipeline System 2021-Crude Oil Pipeline Transportation System. https://www.cer-rec.gc.ca/en/data-analysis/facilities-we-regulate/canadas-pipeline-system/2021/crude-oil-pipeline-transportation-system.html. [0048] 4. Nagumo, M. Fundamentals of Hydrogen Embrittlement. (Springer Singapore, 2016). doi:10.1007/978-981-10-0161-1. [0049] 5. Nam, T.-H., Lee, J.-H., Choi, S.-R., Yoo, J.-B. & Kim, J.-G. Graphene coating as a protective barrier against hydrogen embrittlement. International Journal of Hydrogen Energy 39, 11810-11817 (2014). [0050] 6. Nemani?, V. Hydrogen permeation barriers: Basic requirements, materials selection, deposition methods, and quality evaluation. Nuclear Materials and Energy 19, 451-457 (2019). [0051] 7. Voloshchuk, I. & Zakroczymski, T. Hydrogen entry and absorption in ZrO2 coated iron studied by electrochemical permeation and desorption techniques. International Journal of Hydrogen Energy 37, 1826-1835 (2012). [0052] 8. Zajec, B. Hydrogen permeation barrierRecognition of defective barrier film from transient permeation rate. International Journal of Hydrogen Energy 36, 7353-7361 (2011). [0053] 9. Gharbi, K. et al. Alkyl phosphonic acid-based ligands as tools for converting hydrophobic iron nanoparticles into water soluble iron-iron oxide core-shell nanoparticles. New Journal of Chemistry 41, 11898-11905 (2017). [0054] 10. Devanathan M. A. V., Stachurski Z., & Tompkins Frederick Clifford. The adsorption and diffusion of electrolytic hydrogen in palladium. Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences 270, 90-102 (1962). [0055] 11. Crank, J. The mathematics of diffusion. (Clarendon Press, 1975). [0056] 12. Mohammadijoo, M., Collins, L., Henein, H. & Ivey, D. G. Canadian HSLA steel pipelinesHistory and technology developments. ERA https://era.library.ualberta.ca/items/a379aa08-e6dd-4dbf-9ba1-1fedfa601762 (2018) doi:10.7939/r3-wvqv-qg18.