ACS Engineering Au最新文献

{"title":"Quantifying the Impact of Intraparticle Convection within Fixed Beds Formed by Catalytic Particles with Low Macro-Porosities","authors":"Stylianos Kyrimis,&nbsp;Matthew E. Potter,&nbsp;Robert Raja and Lindsay-Marie Armstrong*,&nbsp;","doi":"10.1021/acsengineeringau.3c00015","DOIUrl":"10.1021/acsengineeringau.3c00015","url":null,"abstract":"<p >Computational fluid dynamics (CFD) modeling plays a pivotal role in optimizing fixed bed catalytic chemical reactors to enhance performance but must accurately capture the various length- and time-scales that underpin the complex particle–fluid interactions. Within catalytic particles, a range of pore sizes exist, with micro-pore scales enhancing the active surface area for increased reactivity and macro-pore scales enhancing intraparticle heat and mass transfer through intraparticle convection. Existing particle-resolved CFD models primarily approach such dual-scale particles with low intraparticle macro-porosities as purely solid. Consequently, intraparticle phenomena associated with intraparticle convection are neglected, and their impact in the full bed scale is not understood. This study presents a porous particle CFD model, whereby individual particles are defined through two distinct porosity terms, a macro-porosity term responsible for the particle’s hydrodynamic profile and a micro-porosity term responsible for diffusion and reaction. By comparing the flow profiles through full beds formed by porous and solid particles, the impact of intraparticle convection on mass and heat transfer, as well as on diffusion and reaction, was investigated.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 5","pages":"335–351"},"PeriodicalIF":0.0,"publicationDate":"2023-09-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00015","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"45222039","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Controlled Pretreatment and Reconstruction of a Bimetallic Pt–Ir/Al2O3/ZSM-5 Catalyst for Increased Stability during Butane Hydrogenolysis","authors":"Emily K. Schroeder,&nbsp;Prasanna Dasari,&nbsp;Muhammad Amtiaz Nadeem,&nbsp;Dustin Fickel and Phillip Christopher*,&nbsp;","doi":"10.1021/acsengineeringau.3c00012","DOIUrl":"10.1021/acsengineeringau.3c00012","url":null,"abstract":"<p >The activity and stability of bimetallic Pt–Ir nanoparticles supported on an Al₂O₃/ZSM-5 mixture were investigated as a function of pretreatment and regeneration conditions for butane hydrogenolysis to ethane. Catalyst characterization by scanning transmission electron microscopy and energy-dispersive X-ray spectroscopy before and after aging under butane hydrogenolysis conditions for 12 weeks confirmed that the bimetallic nanoparticles were resistant to sintering, coking, and bulk metal segregation. However, for catalysts that were pretreated through an initial H₂ reduction, <i>n</i>-butane conversion decreased from 68 to 34% after 12 days on stream while maintaining ∼76% selectivity to ethane. A specific regeneration (or pretreatment) protocol was identified, involving the exposure of the oxidized catalyst to a butane and hydrogen mixture followed by post-reduction, which recovered the catalyst activity and enhanced catalyst stability such that <i>n</i>-butane conversion decreased &lt;5% after 6 days on stream. The influence of various treatments on the structure and surface composition of the bimetallic nanoparticles was hypothesized based on analysis of in situ and cryogenic CO probe-molecule diffuse reflectance infrared Fourier transform spectroscopy measurements. Based on this analysis, it was inferred that high-temperature H₂ treatment of oxidized catalysts resulted in intraparticle segregation into a Pt shell and Ir core that was detrimental to long-term catalyst performance. The core–shell structure was reversible upon catalyst oxidation in O₂, forming an oxidized Ir (IrO_<i>x</i>) shell and Pt core. Treatment of the oxidized catalyst with a butane and H₂ mixture deposited CO and hydrocarbon adsorbates on the IrO_<i>x</i> shell, which stabilized Ir on the nanoparticle surface, even under reductive conditions. Post-reduction in H₂ restored the initial <i>n</i>-butane conversion with improved catalyst stability due to the adsorbate-stabilized, Ir-enriched surface. Therefore, carefully designed pretreatment protocols that deposit stable spectator adsorbates are presented as a valuable tool for controlling the surface composition of bimetallic nanoparticles under reaction conditions to improve their catalytic performance.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 5","pages":"301–315"},"PeriodicalIF":0.0,"publicationDate":"2023-07-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00012","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"41299772","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Transition Metal-Based Chalcogenides as Electrocatalysts for Overall Water Splitting","authors":"Kartick Chandra Majhi*,&nbsp; and ,&nbsp;Mahendra Yadav,&nbsp;","doi":"10.1021/acsengineeringau.3c00014","DOIUrl":"10.1021/acsengineeringau.3c00014","url":null,"abstract":"<p >Hydrogen is the key component in terms of energy economy, and electrochemical water splitting is one of the most important strategies to replace the widely used fossil fuels. The search for efficient electrocatalysts toward water splitting for hydrogen generation is very important. Transition metal-based chalcogenides have great attraction as efficient electrocatalysts due to their high conductivity, distinct valence electron configuration, and different surface morphological nano/microstructures. In this Review, recently developed transition metal-based chalcogenides (S, Se, and Te) as electrocatalysts toward hydrogen evolution reaction, oxygen evolution reaction, and overall water splitting have been discussed.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 5","pages":"278–284"},"PeriodicalIF":0.0,"publicationDate":"2023-07-25","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00014","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"44416558","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Low-Temperature Ammonia Synthesis with an In Situ Adsorber under Regenerative Reaction Cycles Surpassing Thermodynamic Equilibrium","authors":"William J. Movick,&nbsp;Yuuka Kubo,&nbsp;Fuminao Kishimoto and Kazuhiro Takanabe*,&nbsp;","doi":"10.1021/acsengineeringau.3c00009","DOIUrl":"10.1021/acsengineeringau.3c00009","url":null,"abstract":"<p >Catalytic NH₃ synthesis is a well-studied reaction, but its use in renewable energy storage is difficult due to the need for small-scale production, requiring greatly reduced operating temperatures and pressures. NH₃ inhibition on supported Ru catalysts becomes more prevalent at low temperatures, decreasing the reaction rates. In addition, promoter species are prone to oxidation at lower temperatures, further depressing the reaction rate. In situ NH₃ removal techniques have the potential to enhance NH₃ synthesis under milder conditions to combat both NH₃ inhibition and thermodynamic limitations, while the regeneration of the adsorber can potentially reactivate promoter species. The deactivation event of 5 wt % Ru/CeO₂ (3.9 nm average Ru particle size) was first explored in detail, and it was found that slight oxidation of Ce³⁺ promoter species is the major cause of deactivation at lower temperatures, which is easily restored by high-temperature H₂ treatment. Ru/CeO₂ was then mixed with zeolite 4A, a substance showing favorable NH₃ capacity under mild reaction conditions. In situ adsorption of NH₃ significantly increased the reaction rate of Ru/CeO₂ at 200 °C with 5 kPa H₂ and 75 kPa N₂, where the reaction rate increased from 128 to 565 μmol g^–1 h^–1 even at low H₂ conversions of 0.25% (average NH₃ yield of 0.01%). The temperature swings that were utilized to measure NH₃ uptake on zeolite 4A were also found to provide a reactivation event for Ru/CeO₂. In situ NH₃ removal went beyond equilibrium limitations, achieving H₂ conversions up to 98%. This study sheds light on the kinetics of the use of in situ NH₃ removal techniques and provides insight into future designs utilizing similar techniques.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 5","pages":"292–300"},"PeriodicalIF":0.0,"publicationDate":"2023-07-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00009","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"43142796","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Selective Partial Oxidation of Methane with CO2 Using Mobile Lattice Oxygens of LSF","authors":"Hen Ohayon Dahan,&nbsp;Gal Sror,&nbsp;Miron V. Landau,&nbsp;Eran Edri and Moti Herskowitz*,&nbsp;","doi":"10.1021/acsengineeringau.3c00008","DOIUrl":"10.1021/acsengineeringau.3c00008","url":null,"abstract":"<p >The effects of co-feeding CO₂ and methane on the performance of La_0.8Sr_0.2FeO₃ (LSF) were studied with different CO₂ concentrations. The reaction was conducted in chemical looping mode at 900 °C and a weight hourly space velocity (WHSV; g methane/g catalyst/h) of 3 h^–1 during 15 min reduction (10 mol % methane with 0–1.8% CO₂ in nitrogen) and 10 min oxidation (10 mol % oxygen in nitrogen) cycles. Analyses of X-ray diffraction and X-ray photoelectron spectroscopy data of spent materials indicated that CO₂ reacts with the oxygen vacancies on the LSF surface during methane reduction, increasing CO selectivity in POM. As the CO₂ feed concentration increased to an optimal value (1.6% CO₂), the CO selectivity increased to 94%. Under those conditions, the EOR (extent of reduction) of LSF, defined as the amount of oxygen depleted from the lattice, was 0.18–0.15 mmol/min·g_cat. Reducing the EOR to 0.09–0.08 mmol/min·g_cat (1.8% CO₂) led to partial methane combustion. These results were confirmed by altering the operating conditions (WHSV = 2 and 1 h^–1, <i>T</i> = 950 °C) and CO₂ feed concentrations while extending the reduction time. Operation in an optimal EOR range (0.17–0.10 mmol/min·gcat) that enabled optimal CO selectivity (&gt;90%) was obtained without oxidative regeneration for the 18 h reduction time.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 4","pages":"265–277"},"PeriodicalIF":0.0,"publicationDate":"2023-06-08","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00008","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"49177154","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Breakage of a Single Particle in an Air Jet Mill","authors":"Mahesh M. Dhakate,&nbsp;Aditya Venkatraman and Devang V. Khakhar*,&nbsp;","doi":"10.1021/acsengineeringau.3c00004","DOIUrl":"10.1021/acsengineeringau.3c00004","url":null,"abstract":"<p >An experimental study of the impact breakage of a single tapioca grain using an air jet mill is carried out. High-velocity jets at the circumference of the cylindrical grinding chamber propel the grain tangentially, resulting in numerous collisions with the cylinder walls prior to breakage. Videography and image analysis are used to obtain the trajectory of the particle and the sizes of the fragments. Each experiment is repeated 25 times at three different grinding jet pressures (1, 1.5, and 2 bar). The average collision rate and the average breakage times are nearly constant for the higher pressures at 1000 1/s and 0.18 s, respectively. The size distribution at the end of the experiment, obtained using a laser particle size analyzer, is trimodal. The probability of first breakage versus the cumulative specific kinetic energy of impacts is shown to follow the Vogel–Peukert equation (<i>Powder Technology</i> <b>2003</b>, <i>129</i>, 101–110).</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 4","pages":"257–264"},"PeriodicalIF":0.0,"publicationDate":"2023-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00004","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"47174575","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Facile and Robust Production of Ultrastable Micrometer-Sized Foams","authors":"Mariana Rodríguez-Hakim,&nbsp;Luka Oblak and Jan Vermant*,&nbsp;","doi":"10.1021/acsengineeringau.3c00005","DOIUrl":"10.1021/acsengineeringau.3c00005","url":null,"abstract":"<p >Stable foams that can resist disproportionation for extended periods of time have important applications in a wide range of technological and consumer materials. Yet, legislative initiatives limit the range of surface active materials that can be used for environmental impact reasons. There is a need for technologies to efficiently produce multiphase materials using more eco-friendly components, such as particles, and for which traditional thermodynamics-based processing routes are not necessarily efficient enough. This work describes an innovative foaming technology that can produce ultrastable Pickering-Ramsden foams, with bubbles of micrometer-sized dimensions, through pressure-induced particle densification. Specifically, aqueous nanosilica-stabilized foams are produced by foaming a suspension at subatmospheric pressures, allowing for adsorption of the particles onto large bubbles. This is followed by an increase back to atmospheric pressure, which induces bubble shrinkage and compresses the adsorbed particle interface, forming a strong elastoplastic network that provides mechanical resistance against disproportionation. The foam’s interfacial mechanical properties are quantified to predict the range of processing conditions needed to produce permanently stable foams, and a general stability criterion is derived by considering the interfacial rheological properties under slow, unidirectional compression. Foams that are stable against disproportionation are characterized by interfaces whose mechanical resistance to compressive deformations can withstand their tendency to minimize the interfacial stress by reducing their surface area. Our ultrastable nanosilica foams are tested in real-life applications by introducing them into concrete. In comparison to other commercial air entrainers, our microfoam improves concrete’s freeze–thaw resistance while supplying higher material strength, providing an economically attractive, industrially scalable, and durable alternative for use in real-life applications involving cementitious materials. The applicability of our stability criterion to other rheologically complex interfaces and the versatile nature of our foaming technology enables usage for a broad class of materials, beyond the construction industry.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 4","pages":"235–248"},"PeriodicalIF":0.0,"publicationDate":"2023-05-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00005","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"45707007","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Strategic CO2 Storage Material toward a Selective Control of Calcium Carbonate Polymorphs as Additives in Ester Oil Reinforcement","authors":"Benoit Rugabirwa*,&nbsp;Jean Népo Hakizimana,&nbsp;Abdul-Rauf Ibrahim,&nbsp;Yanzhen Hong,&nbsp;Yuzhong Su,&nbsp;Hongtao Wang and Jun Li*,&nbsp;","doi":"10.1021/acsengineeringau.3c00003","DOIUrl":"10.1021/acsengineeringau.3c00003","url":null,"abstract":"<p >In the efforts to corroborate safer environmental CO₂ mitigation strategies, herein, we elucidate engineered practices that convert the absorbed CO₂ in a solid material and its utilization in the path of product synthesis. In this way, the cheaper lime material, the primary calcium resource, when exposed to CO₂ capture, and the storage material (CO₂CSM) prepared by using 1,2-ethylenediamine and 1, 4-butanediol resulted in the formation of controlled vaterite and aragonite CaCO₃ polymorphs in their respective pure forms mediated by the functionalized CO₂CSM. The investigation studies demonstrated that the obtained CO₂CSM under the supercritical CO₂ state has a higher uptake and release efficiency of CO₂ equivalent to 3.730 and 3.17 mmol/g, respectively. Therefore, the conversion of raw materials depended on the amount of CO₂CSM availed in the reaction and would be complete at the expense of supercritical CO₂CSM in the solid-type reaction. The mechanism study explains the fundamental formation of products correlating to the amount of CO₂CSM supplied in the reaction which would initiate the reaction, while the amine functional group of the material could stabilize and effectively control the transition of vaterite to aragonite phases of CaCO₃. The so-obtained CaCO₃ phases were tested for their antiwear and friction stability of the lubricant 500SN; vaterite and aragonite demonstrated good reinforcement of the mechanical properties of lubricants compared to the calcite type. Therefore, this system proposes a validation platform of using sequestrated CO₂ to generate products with industrial commercialization benefits in the reinforcement of organic-based lubricants.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 4","pages":"249–256"},"PeriodicalIF":0.0,"publicationDate":"2023-05-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00003","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"43539895","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Heat Recuperation from Internal Combustion Engines by Fuel Reforming: Kinetics-Based Analysis","authors":"Moshe Sheintuch*,&nbsp;Olga Nekhamkina and Leonid Tartakovsky,&nbsp;","doi":"10.1021/acsengineeringau.3c00007","DOIUrl":"10.1021/acsengineeringau.3c00007","url":null,"abstract":"<p >In an effort to estimate the feasibility of heat recuperation from an internal combustion engine (ICE) by steam reforming (SR) or by decomposition of the fuel, we study here the required size of a reformer heat exchanger in order to power a 3.7 kW engine. To that end, we experimentally test the heat transfer in a structured commercial reactor with ∼0.39 m² of heat transfer area in an ∼1 L unit. We then simulate the required length for evaporation and reforming of several fuels, using published kinetics with a highly active catalyst, under a fixed exhaust temperature of 973 K, and study the effect of pressure and steam-to-fuel ratio. Both co- and counter-current schemes are considered. Methanol decomposition is probably the best solution from the energy point of view. However, it is known to lead to deactivation. Methanol SR (with S/M = 1) requires about 2 L of reformer-HE and seems to be a reasonable solution, yielding a chemical energy gain of ∼16%, a value close to the asymptotic thermodynamic value. Moreover, the presence of CO₂ in the reformate is known to mitigate to NO<i>_x</i> emissions down to zero-impact levels. Ethanol SR (with S/E = 1 or 3) yields poor results since CH₄ is an intermediate, which requires high temperatures for reforming; operating ESR requires exhaust temperatures of ∼1250 °K or higher. While such high temperatures may be attained and may yield an energetic gain of more than 20%, it will require modification of the process. Methylal SR (S/MA = 1) yields good results as well.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 3","pages":"210–223"},"PeriodicalIF":0.0,"publicationDate":"2023-05-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00007","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"43816557","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"Design, Construction, and Concept Validation of a Laboratory-Scale Two-phase Reactor to Valorize Whiskey Distillery By-products","authors":"Anga Hackula,&nbsp;Richard O’Shea,&nbsp;Jerry D. Murphy and David M. Wall*,&nbsp;","doi":"10.1021/acsengineeringau.3c00006","DOIUrl":"10.1021/acsengineeringau.3c00006","url":null,"abstract":"<p >The by-products generated from the whiskey distillation process consist of organic liquids with a high chemical oxygen demand (COD) and residues with a high solid content. Low-carbon strategies that repurpose and valorize such by-products are now imperative to reduce the carbon footprint of the food and beverage industries. The operation of a two-phase anaerobic digester to produce volatile fatty acids (VFAs) and biogas may enable distilleries to transition toward a low-carbon bioeconomy. An example of such a system is a leach bed reactor connected to an expanded granular sludge bed (LBR-EGSB) which was designed, commissioned, and conceptually validated in this paper. Several design improvements progress the LBR-EGSB beyond previous reactor designs. An external gas–liquid–solid separator in the EGSB was used to capture any residual gases produced by the effluent and may reduce the amount of methane slippage and biomass washout. The implementation of a siphon-actuated leachate cup is a low-cost alternative that is less prone to actuation malfunction as compared to electrically actuated solenoid valves in previous reactor designs. Furthermore, replacing fresh water with distillery’s liquid by-products as leachate promotes a circular repurpose and reuse philosophy. The system proved to be effective in generating VFAs (10.3 g VFAs L^–1_Leachate), in EGSB COD removal (96%), and in producing methane-rich biogas (75%_vol), which is higher than the values achieved by traditional anaerobic digestion systems. The LBR-EGSB could ultimately provide more by-product valorization and decarbonization opportunities than traditional anaerobic digestion systems for a whiskey distillery.</p>","PeriodicalId":29804,"journal":{"name":"ACS Engineering Au","volume":"3 4","pages":"224–234"},"PeriodicalIF":0.0,"publicationDate":"2023-05-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/acsengineeringau.3c00006","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"10040334","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}