Process Intensification Approach Using Microreactors For

Process Intensification Approach Using Microreactors For

nanomaterials Review Process Intensification Approach Using Microreactors for Synthesizing Nanomaterials—A Critical Review Vikas Hakke 1, Shirish Sonawane 1,* , Sambandam Anandan 2,* , Shriram Sonawane 3 and Muthupandian Ashokkumar 4,* 1 Chemical Engineering Department, National Institute of Technology, Warangal 506004, India; [email protected] 2 Department of Chemistry, National Institute Technology, Trichy 620015, India 3 Nano Research Project Laboratory, Department of Chemical Engineering, Visvesvaraya National Institute of Technology, Nagpur 440010, India; [email protected] 4 School of Chemistry, University of Melbourne, Melbourne, VIC 3010, Australia * Correspondence: [email protected] (S.S.); [email protected] (S.A.); [email protected] (M.A.) Abstract: Nanomaterials have found many applications due to their unique properties such as high surface-to-volume ratio, density, strength, and many more. This review focuses on the recent developments on the synthesis of nanomaterials using process intensification. The review covers the designing of microreactors, design principles, and fundamental mechanisms involved in process intensification using microreactors for synthesizing nanomaterials. The microfluidics technology operates in continuous mode as well as the segmented flow of gas–liquid combinations. Various examples from the literature are discussed in detail highlighting the advantages and disadvantages of microfluidics technology for nanomaterial synthesis. Keywords: microreactors; nanoparticles; continuous flow; segmented flow; process intensification Citation: Hakke, V.; Sonawane, S.; Anandan, S.; Sonawane, S.; Ashokkumar, M. Process 1. Introduction Intensification Approach Using 1.1. Microfluidics Technology for Process Intensification Microreactors for Synthesizing Conventional reactors have many bottleneck problems such as energy losses (mass Nanomaterials—A Critical Review. as well as heat), high wastages, poor reaction control, and high operational risk. The Nanomaterials 2021, 11, 98. https:// conversion of reagents depends upon space–time in the reactor and the mixing kinetics doi.org/10.3390/nano11010098 inside the reactor. Due to the large quantity, it is difficult to achieve a uniform mixing inside conventional batch reactors leading to dead zones. Many solutions have been proposed Received: 9 December 2020 after a decade of research such as the modification of the reactor internal surface with Accepted: 29 December 2020 Published: 4 January 2021 baffles but still, the problem of mixing kinetics remains unresolved with batch reactors. All these issues ultimately reduce the yield and quality of the product [1,2]. Publisher’s Note: MDPI stays neu- In recent decades, process intensification has gained importance due to its effec- tral with regard to jurisdictional clai- tiveness in the utilization of resources available. Maximum conversion, high safety and ms in published maps and institutio- minimal or optimal energy losses are the primary focus in the intensified design approach. nal affiliations. Microfluidics is one of the smart solutions generated by the intensification design approach. A new generation of micro dimension reactors are developed to reduce the overall fabrica- tion cost, size, optimal utilization of space and enhanced safety [3]. The compact size of the reactors induces good mixing conditions which improve the reaction kinetics. In the Copyright: © 2021 by the authors. Li- intensified reactor design approach, one of the dimensions is in the submillimeter range. censee MDPI, Basel, Switzerland. These new generation reactors are referred to as microstructured devices/reactors, or This article is an open access article microreactors [3,4]. The major advantage of microreactor technology is the higher surface- distributed under the terms and con- to-volume ratio which can be as high as 100,000 m2/m3 [5]. The heat and mass transfer ditions of the Creative Commons At- rates are synergistically improved due to the small volume and high surface area, which tribution (CC BY) license (https:// may reduce the reaction time to a few seconds from several hours. The safety associated creativecommons.org/licenses/by/ 4.0/). with the process is enhanced due to the small volume of the reactor. Nanomaterials 2021, 11, 98. https://doi.org/10.3390/nano11010098 https://www.mdpi.com/journal/nanomaterials Nanomaterials 2021, 11, 98 2 of 21 1.2. Nanostructures and Need for Microfluidics Technique in Their Synthesis Nanomaterials have been used for many centuries, however, the intense interest ar- rived only in recent decades. A large number of synthetic approaches have been developed; examples include chemical vapor deposition, sputtering, spray pyrolysis and electrochemi- cal methods [6]. Nanoparticles are widely applied in the areas of paint, coatings, electronics, textiles, bioimaging, medicine, and many more [7]. Most of these methodologies have some limitations such as poor control over particle size, size distribution, shape, poor reproducibility, and time-intensive synthetic processes. The main challenge is the produc- tion of nanomaterials on a commercial scale with control over particle size, shape and polydispersity. Microreactors offer control over these properties of nanomaterials. In this review, the fundamental aspects of microreactors and a comparative study of different modes of operation are discussed. The critical review also covers the advantages and disadvantages of microreactor technology for the synthesis of nanoparticles. 2. Microstructure Reactors Design Principles 2.1. Design Consideration for Nanoparticle Synthesis in Microstructured Reactors The microstructure reactors, which were initially introduced in processing as capillary- type reactors, have now been extended to small volume reactors such as Corning® Advanced- Flow™ Reactors (AFR), New Delhi, India. The synthesis of nanoparticles can be achieved through many physical as well as chemical processes. The commercially available processes select a top-down approach as it is easier for scale-up. Microfluidics uses a bottom-up method, where the chemical synthesis of the nanoparticles is achieved through the sol–gel or chemical reduction methods. The microreactors provide a controlled environment as Reynolds number is very low in the range of 100 to 500 so solute transport is uniform lead- ing to the generation of the desired size and shape of nanoparticles. Before understanding the design principles of the microreactor, one must understand the synthetic mechanism of nanoparticles from their constituents. Chemical Synthesis of Nanoparticles: Bottom-Up Approach In this section, an overview of the theories of formation and growth of nanoparticles is provided. The chemical synthesis of nanoparticles can be defined by four approaches: (i) LaMer approach, (ii) Ostwald ripening, (iii) Finke–Watzky mechanism and (iv) coalescence (Figure1). The LaMer model suggests that the diffusion rate of monomers in the solution is responsible for the nanoparticle formation through nucleation and its propagation. This model depends on the concentration gradient-based mechanism. Ostwald ripening is based on the solubility of particles in the solution. The smaller particles, due to their high solubility and surface charges, show higher mobility towards each other. This induces the growth of particles through the re-deposition of smaller nanoparticles. This process is exactly the opposite of digestive ripping. The Finke–Watzky model explains the mechanism in two stages: first is nucleation followed by particle growth. Whereas the theory of coalescence and oriented attachment explains the effect of coalescence on orientation effects in the growth of particles [8]. Nanomaterials 2021, 10, x FOR PEER REVIEW 3 of 22 Nanomaterials 2021, 11, 98 3 of 21 FigureFigure 1. 1.Nuclei Nuclei growth growth mechanisms mechanisms representationrepresentation ((AA)) LaMer LaMer approach,approach, ((BB)) Ostwald Ostwald ripening,ripening, ((CC)) Finke–Watzky Finke–Watzky and and (D(D)) coalescence coalescence and and oriented oriented connections connections mechanism. mechanism. The The Figure Figure was was conceptualized conceptualized based based on on the the information information provided provided inin Ref. Ref. [ [8].8]. 2.2.2.2. MicroreactorsMicroreactors One-dimensionalOne‐dimensional microscale reactors reactors have have their their benefits benefits and and drawbacks. drawbacks. The The nucle nu-‐ cleationation followed followed by bythe thegrowth growth of particles of particles within within a constrained a constrained environment environment is the gener is the‐ generalizedalized approach approach for the for synthesis the synthesis of nanoparticles of nanoparticles using usingmicroreactors. microreactors. Chemical Chemical reactions re- actionssuch as such oxidation as oxidation and reduction and reduction of precursors of precursors are the are themost most widely widely used used approaches approaches in inmicroreactors. microreactors. Two Two or or more more reactants reactants are are brought brought together together in in microreactors microreactors to to achieve achieve a amaximum maximum conversion conversion during during the the reaction. reaction. The Theproduct product with witha lower a lower solubility solubility and higher and highersurface surface energy energyleads to leads the formation to the formation of nanoparticles, of nanoparticles, through through nucleation nucleation and crystal and crystalgrowth. growth. All the Allprocesses the processes

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