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",isbn:"978-1-83969-642-8",printIsbn:"978-1-83969-641-1",pdfIsbn:"978-1-83969-643-5",doi:null,price:0,priceEur:0,priceUsd:0,slug:null,numberOfPages:0,isOpenForSubmission:!0,hash:"5d7f2aa74874444bc6986e613ccebd7c",bookSignature:"Prof. Antonio Morata, Dr. Iris Loira and Prof. Carmen González",publishedDate:null,coverURL:"https://cdn.intechopen.com/books/images_new/10901.jpg",keywords:"Grape, Wine, Vine Biotechnology, Plant Disease, Vine Physiology, Wine Technology, Winemaking, Fungal Disease, Biological Control, Vigor Management, Aroma Compound, Polysaccharide",numberOfDownloads:null,numberOfWosCitations:0,numberOfCrossrefCitations:null,numberOfDimensionsCitations:null,numberOfTotalCitations:null,isAvailableForWebshopOrdering:!0,dateEndFirstStepPublish:"March 4th 2021",dateEndSecondStepPublish:"April 1st 2021",dateEndThirdStepPublish:"May 31st 2021",dateEndFourthStepPublish:"August 19th 2021",dateEndFifthStepPublish:"October 18th 2021",remainingDaysToSecondStep:"20 days",secondStepPassed:!0,currentStepOfPublishingProcess:3,editedByType:null,kuFlag:!1,biosketch:"Prof. Morata is the Spanish delegate at the group of experts in wine microbiology and wine technology of the International Organisation of Vine and Wine (OIV). His team won the international Enoforum award 2019 by the application of UHPH in wines and was among the 5 finalists in 2020 by using PL.",coeditorOneBiosketch:null,coeditorTwoBiosketch:null,coeditorThreeBiosketch:null,coeditorFourBiosketch:null,coeditorFiveBiosketch:null,editors:[{id:"180952",title:"Prof.",name:"Antonio",middleName:null,surname:"Morata",slug:"antonio-morata",fullName:"Antonio Morata",profilePictureURL:"https://mts.intechopen.com/storage/users/180952/images/system/180952.jpg",biography:"Antonio Morata is a professor of Food Science and Technology at the Universidad Politécnica de Madrid (UPM), Spain, specializing in wine technology. He is the coordinator of the Master in Food Engineering Program at UPM, and a professor of enology and wine technology in the European Master of Viticulture and Enology, Euromaster Vinifera-Erasmus+. He is the Spanish delegate at the group of experts in wine microbiology and wine technology of the International Organisation of Vine and Wine (OIV). He is the author of more than 70 research articles, 3 books, 4 edited books, 6 special issues and 16 book chapters.",institutionString:"Technical University of Madrid",position:null,outsideEditionCount:0,totalCites:0,totalAuthoredChapters:"6",totalChapterViews:"0",totalEditedBooks:"3",institution:{name:"Technical University of Madrid",institutionURL:null,country:{name:"Spain"}}}],coeditorOne:{id:"186423",title:"Dr.",name:"Iris",middleName:null,surname:"Loira",slug:"iris-loira",fullName:"Iris Loira",profilePictureURL:"https://mts.intechopen.com/storage/users/186423/images/system/186423.jpg",biography:"Iris Loira is an assistant professor of Food Science and Technology at the Universidad Politécnica de Madrid (UPM), Spain. She is the author of 46 research articles, 3 books and 11 book chapters.",institutionString:"Technical University of Madrid",position:null,outsideEditionCount:0,totalCites:0,totalAuthoredChapters:"4",totalChapterViews:"0",totalEditedBooks:"0",institution:{name:"Technical University of Madrid",institutionURL:null,country:{name:"Spain"}}},coeditorTwo:{id:"201384",title:"Prof.",name:"Carmen",middleName:null,surname:"González",slug:"carmen-gonzalez",fullName:"Carmen González",profilePictureURL:"https://mts.intechopen.com/storage/users/201384/images/system/201384.jpg",biography:"Dr González-Chamorro has worked as a professor at the UPM since 1993. She has dedicated her teaching work to food technology and applications in the fruit and vegetable industries and fermented meat products. From 2004 until 2016 she held management positions in the university (Ombudsman and Deputy Director of University extension and International Relations). Her research activity has focused on the field of oenological biotechnology and on the selection of microorganisms (yeasts and BAL) that are of special interest in wine making processes. She has extensive experience in the use of instrumental and sensory tests to assess the quality of alcoholic beverages (wine and beer) and meat products. She has participated in different educational innovation projects and coordinated three of them. These projects have made it possible to coordinate working groups for the implementation of degrees in the EEES, and apply new teaching methodologies that allow the acquisition of horizontal competences by students. She has also evaluated research projects and national and international degrees (different Quality Agencies).",institutionString:"Technical University of Madrid",position:null,outsideEditionCount:0,totalCites:0,totalAuthoredChapters:"4",totalChapterViews:"0",totalEditedBooks:"0",institution:{name:"Technical University of Madrid",institutionURL:null,country:{name:"Spain"}}},coeditorThree:null,coeditorFour:null,coeditorFive:null,topics:[{id:"5",title:"Agricultural and Biological Sciences",slug:"agricultural-and-biological-sciences"}],chapters:null,productType:{id:"1",title:"Edited Volume",chapterContentType:"chapter",authoredCaption:"Edited by"},personalPublishingAssistant:{id:"347258",firstName:"Marica",lastName:"Novakovic",middleName:null,title:"Ms.",imageUrl:"//cdnintech.com/web/frontend/www/assets/author.svg",email:"marica@intechopen.com",biography:null}},relatedBooks:[{type:"book",id:"5253",title:"Grape and Wine Biotechnology",subtitle:null,isOpenForSubmission:!1,hash:"5626f83050894f6dfc5640fa908dc920",slug:"grape-and-wine-biotechnology",bookSignature:"Antonio Morata and Iris Loira",coverURL:"https://cdn.intechopen.com/books/images_new/5253.jpg",editedByType:"Edited by",editors:[{id:"180952",title:"Prof.",name:"Antonio",surname:"Morata",slug:"antonio-morata",fullName:"Antonio Morata"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"6293",title:"Yeast",subtitle:"Industrial Applications",isOpenForSubmission:!1,hash:"46632cf5c744c601f5c36175e8dc8dc4",slug:"yeast-industrial-applications",bookSignature:"Antonio Morata and Iris Loira",coverURL:"//cdnintech.com/web/frontend/www/assets/cover.jpg",editedByType:"Edited by",editors:[{id:"180952",title:"Prof.",name:"Antonio",surname:"Morata",slug:"antonio-morata",fullName:"Antonio Morata"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"8054",title:"Advances in Grape and Wine Biotechnology",subtitle:null,isOpenForSubmission:!1,hash:"f6b9b3b3d887ed9e7c0ad09cb07edf2b",slug:"advances-in-grape-and-wine-biotechnology",bookSignature:"Antonio Morata and Iris Loira",coverURL:"https://cdn.intechopen.com/books/images_new/8054.jpg",editedByType:"Edited by",editors:[{id:"180952",title:"Prof.",name:"Antonio",surname:"Morata",slug:"antonio-morata",fullName:"Antonio Morata"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"6418",title:"Hyperspectral Imaging in Agriculture, Food and Environment",subtitle:null,isOpenForSubmission:!1,hash:"9005c36534a5dc065577a011aea13d4d",slug:"hyperspectral-imaging-in-agriculture-food-and-environment",bookSignature:"Alejandro Isabel Luna Maldonado, Humberto Rodríguez Fuentes and Juan Antonio Vidales Contreras",coverURL:"https://cdn.intechopen.com/books/images_new/6418.jpg",editedByType:"Edited by",editors:[{id:"105774",title:"Prof.",name:"Alejandro Isabel",surname:"Luna Maldonado",slug:"alejandro-isabel-luna-maldonado",fullName:"Alejandro Isabel Luna Maldonado"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"1591",title:"Infrared Spectroscopy",subtitle:"Materials Science, Engineering and Technology",isOpenForSubmission:!1,hash:"99b4b7b71a8caeb693ed762b40b017f4",slug:"infrared-spectroscopy-materials-science-engineering-and-technology",bookSignature:"Theophile Theophanides",coverURL:"https://cdn.intechopen.com/books/images_new/1591.jpg",editedByType:"Edited by",editors:[{id:"37194",title:"Dr.",name:"Theophanides",surname:"Theophile",slug:"theophanides-theophile",fullName:"Theophanides Theophile"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"3161",title:"Frontiers in Guided Wave Optics and Optoelectronics",subtitle:null,isOpenForSubmission:!1,hash:"deb44e9c99f82bbce1083abea743146c",slug:"frontiers-in-guided-wave-optics-and-optoelectronics",bookSignature:"Bishnu Pal",coverURL:"https://cdn.intechopen.com/books/images_new/3161.jpg",editedByType:"Edited by",editors:[{id:"4782",title:"Prof.",name:"Bishnu",surname:"Pal",slug:"bishnu-pal",fullName:"Bishnu Pal"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"3092",title:"Anopheles mosquitoes",subtitle:"New insights into malaria vectors",isOpenForSubmission:!1,hash:"c9e622485316d5e296288bf24d2b0d64",slug:"anopheles-mosquitoes-new-insights-into-malaria-vectors",bookSignature:"Sylvie Manguin",coverURL:"https://cdn.intechopen.com/books/images_new/3092.jpg",editedByType:"Edited by",editors:[{id:"50017",title:"Prof.",name:"Sylvie",surname:"Manguin",slug:"sylvie-manguin",fullName:"Sylvie Manguin"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"371",title:"Abiotic Stress in Plants",subtitle:"Mechanisms and Adaptations",isOpenForSubmission:!1,hash:"588466f487e307619849d72389178a74",slug:"abiotic-stress-in-plants-mechanisms-and-adaptations",bookSignature:"Arun Shanker and B. Venkateswarlu",coverURL:"https://cdn.intechopen.com/books/images_new/371.jpg",editedByType:"Edited by",editors:[{id:"58592",title:"Dr.",name:"Arun",surname:"Shanker",slug:"arun-shanker",fullName:"Arun Shanker"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"72",title:"Ionic Liquids",subtitle:"Theory, Properties, New Approaches",isOpenForSubmission:!1,hash:"d94ffa3cfa10505e3b1d676d46fcd3f5",slug:"ionic-liquids-theory-properties-new-approaches",bookSignature:"Alexander Kokorin",coverURL:"https://cdn.intechopen.com/books/images_new/72.jpg",editedByType:"Edited by",editors:[{id:"19816",title:"Prof.",name:"Alexander",surname:"Kokorin",slug:"alexander-kokorin",fullName:"Alexander Kokorin"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"314",title:"Regenerative Medicine and Tissue Engineering",subtitle:"Cells and Biomaterials",isOpenForSubmission:!1,hash:"bb67e80e480c86bb8315458012d65686",slug:"regenerative-medicine-and-tissue-engineering-cells-and-biomaterials",bookSignature:"Daniel Eberli",coverURL:"https://cdn.intechopen.com/books/images_new/314.jpg",editedByType:"Edited by",editors:[{id:"6495",title:"Dr.",name:"Daniel",surname:"Eberli",slug:"daniel-eberli",fullName:"Daniel Eberli"}],productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}}]},chapter:{item:{type:"chapter",id:"57432",title:"Perspective Non-Fluorinated and Partially Fluorinated Polymers for Low-Temperature PEM FC",doi:"10.5772/intechopen.71250",slug:"perspective-non-fluorinated-and-partially-fluorinated-polymers-for-low-temperature-pem-fc",body:'\nFuel cells (FC) are chemical sources of current. They perform direct conversion of fuel energy into electricity, avoiding combustion processes and conversion of thermal energy into electrical energy. In an ideal fuel cell, electrolyte and electrodes are not consumed and do not undergo any changes during the operation process – the chemical energy of fuel is converted directly into electricity.
\nThe FC device is similar to the device of the galvanic cell. The main part of any fuel cell is the membrane-electrode assembly (MEA), which is a solid electrolyte layer with the applied electrodes. One side of the membrane (similar to liquid electrolyte in the galvanic element) is applied to the cathode and the other anode catalytic layers. Most often, the catalyst of the anode, molecular hydrogen dissociates and loses electrons. Cations of hydrogen are conducted through the membrane to the cathode, but the electrons are given to the external circuit because the membrane does not pass electrons. On the catalyst of the cathode, the oxygen molecule joins with an electron supplied from an external communications and with arrived proton to form water, which is the only product of the reaction. The current collecting at the cathode and anode sides, a supply source of reagents and withdrawal of the reaction products is carried through the porous gas diffusion layers (GDL), is usually made of carbon materials.
\nThere are several different types of fuel cells classified according to the type of electrolyte. The type of the electrolyte depends on the most parameters of the FC, such as operating temperature, size, energy output, etc.
\nFuel cells based on polymer electrolyte (proton-exchange) membrane (PEM) is designed to become compact sources of energy and replace petrol and diesel engines. These systems operate at relatively low temperatures up to 100°C. They quickly go on working power, and are compact, which is advantageous for use in transport. The main, and still not overcome the disadvantage of this type of FC is a weak resistance of the membrane to constantly changing environment in which operate PEM.
\nMembrane PEM FC works in conditions of constantly changing temperatures, high humidity, organic reagent and the formation of peroxides. The main requirement to the materials used to make membranes is the combination of high proton conductivity and resistance to the conditions of the FC. An important criterion is also the low cost of their production.
\nThe first electrolytic membrane, which was developed by General Electric in the USA in the late 1960s to FC used in spacecraft of the Gemini, was sulfonated copolymer poly-(styrene-divinylbenzene). This polymer was not sufficiently resistant to oxidation under operating conditions of FC. A major breakthrough in technology proton-conducting membranes for fuel cells was the emergence of perfluorosulfonate acid (PFSA) Nafion – DuPont product obtained in the 1970s and Nafion counterparts from other firms, for example, Flemion® (Asahi Glass), DowMembrane® (Dow Chemical) and Aciplex® (Asahi Chemical).
\nHowever, the own proton conductivity of such membranes is extremely small, and effectivity proton transfer is determined by the presence of adsorbed atmospheric moisture. Moreover, the market value of the Nafion membranes is 700–800$/m2.
\nDespite the fact that PFSA are still excellent materials for membrane fuel cells, yet they have several significant shortcomings that limit their widespread application. These factors stimulate the interest of researchers to finding cheap and high-performance alternative materials for use as membranes, fuel cells. Such polymers, as polyetherketone, polyetheretherketone, polysulfone, polyether sulfones and polyimides are particularly attractive for researchers. Due to the large diversity of possible chemical structures, including partially fluorinated, they have a high mechanical strength, chemical and thermal stability.
\nOne of the most promising materials for the fabrication of membranes FC are the aromatic polyimides. Polyimides have high heat resistance, the most heat-resistant polyimides based on dianhydride pyromellitic and 1,4,5,8-naphthalenemethanol acids.
\nThese polyimide films are hydrophilic and do not have proton conductivity. Therefore, to ensure high proton conductivity in polyimide chain introduce acidic groups (most often sulfonic – SO3H, sometimes phosphoric). The membranes based on sulfonated polyimides (SPIs) (containing the main chain and/or branches of the group SO3H), gas permeability for hydrogen is about three times lower than that of Nafion.
\nOne of the advantages of fuel cells with polymer electrolyte membrane (PEM FC) indicate a high efficiency of conversion of fuel energy into useful energy, compared with current alternative systems, based on heat engines, whose efficiency is limited by Carnot cycle. It is believed that efficiencies can be over 80%. In practice, however, the efficiency of fuel cells with a polymer membrane is about 50%.
\nThe main difference between fuel cells from other chemical current sources is the possibility of continuous fuel injection and continuous weaning current for potentially unlimited period of time. In practice, however, there is a severe degradation of all components of the MEA, which leads to a monotonous decrease of the voltage on the plates of FC (hence reduced efficiency) when fixing the subtracted current [1].
\nThe “heart” of the MEA is a polymer electrolyte (proton-exchange) membrane (PEM). Typically, the proton-exchange membrane is a film of polymer with a hydrophobic main chain and the acid groups in the side chains. Water in contact with polymer is clustered close to the acid groups, forming nano-sized hydrated cluster. In this area, in addition to water contain various hydrated forms of the movable proton. Thus, the hydrophilic part of the polymer provides efficient proton transport, while the hydrophobic part stabilizes the morphology of the membranes and ensures their mechanical strength [2].
\nThe hydrophobic part of the polymer usually contains aliphatic, aromatic, fluorinated or non-fluorinated fragments. As acid groups generating protons, sulfonates are most often used, more rarely acid residues of phosphoric acid. It is believed that the sulfonated polymers are more efficient in the presence of water vapor, while the more phosphorylated heat-resistant polymers and their conductivity is less dependent on humidity.
\nTo improve the conductivity, the hydrophilic portion of the proton-exchange membrane is often injected with a water-soluble proton-generating additives (usually strong acid), nanoscale oxides or solid electrolytes. Sometimes the proton-generating additive is injected into a non-conductive polymer matrix. In this case, the hydrophilic part is formed by the coordination of water around the introduced additives with subsequent separation of phases.
\nThe main function of proton-exchange membrane is to transfer the cathode area of a proton, resulting in ionization of hydrogen at the anode. Therefore, the membrane should have a maximum conductivity. The conductivity at the level of 10−1–10−3 s/cm is considered adequate for use in FC. Because ideally, the work of FC need to carry in conditions of significant fluctuations of temperature and humidity as fuel and oxidizer, it is desirable that an efficient proton transfer occurred under these conditions. In order to avoid electrical losses, the electronic component of conductivity should be minimal (at least 2–3 orders of magnitude lower than the ionic component) [3].
\nIn addition, the proton-exchange membrane plays a role of gas separation: it cuts off the anode side of the MEA, which contains hydrogen, from the cathode, where air or oxygen is blown. The low gas permeability when using hydrogen under high pressure is especially important. The permeability of the membranes of less than 10–2 ml/(min cm2) is considered sufficient for long-term operation of the fuel cell.
\nThe proton-exchange membrane is subject to a number of requirements. For the efficient operation of the fuel cell, ohmic losses in the membrane should be minimal, and the proton conductivity of the membrane is high. The membrane must have mechanical strength sufficient to pressing on the electrodes to the membrane and operation at elevated pressures of the reactants.
\nSince the formation of extremely reactive hydrogen peroxide on the cathode is possible, in addition to water, the membrane should possess high chemical stability to oxidation and hydrolysis. The water released at the cathode during the fuel cell works is partially absorbed by the membrane, leading to its swelling. This process is most noticeable when using the humidified air. Excessive swelling of the membrane with subsequent drying, after repeated enabling/disabling of the fuel cell, is extremely undesirable process that leads to destruction and exfoliation of the thin active layer and deterioration of the characteristics of the fuel cell. To prevent direct chemical (not electrochemical) reaction of the reactants on one of the electrodes is necessary that the membrane was gas-tight. Penetration of hydrogen on the cathode side equivalent leakage current and should be minimized in order to increase the efficiency of the fuel cell [4].
\nIn order for the materials to be used in PEM fuel cells, they must have a number of conflicting requirements such as in Ref. [5]:
Low cost.
Good film forming ability.
Sufficient proton conductivity (≥100 MS/cm), weakly dependent on relative humidity.
The ability to retain moisture at high temperature.
Thermal, oxidative and hydrolytic stability.
Low permeability to fuel, for example, methanol <10–6 mol (min cm)−1.
Preservation of the strength properties at operation temperatures of FC (80–200°C) within the required time.
The possibility of disposal of spent membranes by standard methods.
It should be noted that the functional characteristics of membranes need to be optimized in the complex, because they are fundamentally interrelated. Indeed, it would not be quite correct to improve, for example, the proton conductivity of the membrane material, without regard to the mechanical properties and the stability of the membrane as a whole. A simple way to increase proton conductivity of the polymer sulfonic acid is, for example, to increase the number of sulfonate groups per unit volume (i.e., decreasing equivalent weight), but this path inevitably leads to obtaining material with poor mechanical properties, excessive swelling or even dissolving in water, which is the product of the reaction. Similarly, the phosphorylation or the increase of doping of polybenzimidazole by phosphoric acid leads to soft gel consistence, incapable of effective separation of reactants between cathode and anode.
\nOn the other hand, losses in the membrane are determined by not specific but general resistance. This means that the transition to more durable membranes that could efficiently separate the reagents, being more delicate, with a mild deterioration in its conductivity could be an advantageous. In practice, however, the general principle is that an increase in mechanical stability of the membrane and reducing its permeability toward reactants, for example, by chemical linkage, always leads to the inevitable drop in conductivity.
\nThe first electrolytic membrane, which was developed by General Electric in the USA in the late 1960s to FC used in spacecraft of the Gemini, was sulfonated copolymer poly-(styrene-divinylbenzene). This polymer was not sufficiently resistant to oxidation under operating conditions of fuel cells [6]. A major breakthrough in technology proton-conducting membranes for fuel cells was the emergence of perfluorosulfonate acid (PFSA) Nafion – DuPont product [7, 8].
\nCurrently the most common membrane is a perfluorinated ion-exchange membrane Nafion developed by DuPont in the 1970s, there were also a number of analogous Nafion – products companies Asahi Glass (Flemion), Asahi Chemical (Aciplex), Dow Chemical, 3 M, FuMA-Tech (Fumapem), etc., wherein minor variations in the structure of side chain polymer molecules (Figure 1).
\nStructure of the Nafion membranes [
Membrane Nafion is a copolymer of tetrafluoroethylene and a possible co-monomer having a side chain of perfluorinated vinyl ether with end sulforaphanes.
\nMaterials based on such polymers are high-tech, and able to get a pretty high-performance at operating temperatures up to 90°C. However, the own proton conductivity of the membranes is extremely small, and effective the proton transfer in them is determined by the presence of adsorbed atmospheric moisture, Therefore, these membranes are FC only work under conditions of constant wetting and hydrostatic, which requires the introduction of additional devices and increase rates of electrochemical generators [2, 9].
\nIt is known that platinum catalysts are very sensitive to the purity of fuel. Negative impact on the catalyst may be present in such hydrogen as impurities hydrogen sulfide. Therefore, the preparation of fuel for low-temperature FC must include expensive phase removal of sulfur compounds and CO [9]. Increasing the operating temperature can in principle improve the efficiency of platinum catalysts. So, the permissible content of CO increases from 10 to 20 ppm at 80°C to 1000 ppm at 130°C. This significantly reduces the cost of the fuel. In addition, increasing the operating temperature allows for more effective heat dissipation and disposal of heat (the latter increases the total fuel efficiency).
\nTemperature rise of FC is also significantly accelerates the electrode reaction, therefore, can be expected to reduce necessary for the efficient operation, of the quantities of the noble metal in the electrodes. However, the proton conductivity of Nafion-type membranes at temperatures above 90°C is drastically reduced (Figure 2a), making their use impossible at elevated temperatures. Obtaining membranes themselves are extremely time-consuming and the cost of quality of membranes of this type are large.
\nDependence of proton conductivity for the membranes Nafion-117 (a) and on the basis of polybenzimidazole (PBI), doped with phosphoric acid (b), the temperature [
Another commercially available system that may be used at temperatures up to 200°C, are membrane based on PBI, doped with phosphoric acid (Figure 3).
\nThe structure of polybenzimidazole.
Phosphoric acid forms an acid-base complex with a polymer matrix (membrane brand the company PEMEAS Celtec Division) [10]. The significant superiority of such membranes in comparison with the Nafion membranes is their high proton conductivity in the absence of moisture (Figure 2b) and high thermal stability (up to 600°C). The working temperature range for the MEA on the basis of such membranes is 160–180°C. The fuel cell in this temperature region enables the use of hydrogen with high co content.
\nThe main problem with membranes is that they are “afraid” of liquid water, in contact with which is destroyed in an acid-base complex and the phosphoric acid is washed out in the area of catalytic and diffusion layers, leading to partial blockage of the gas pores, degradation of bipolar plates and the gas-feed system. The removal of phosphoric acid from the polymer matrix reduces the proton conductivity of the membrane. To avoid condensation of water vapor in the cathode area using relatively time-consuming procedure for stopping the fuel cell, which consists of the removal of loading, purging dry argon to remove water vapor, sealing and cooling. Of course, such a laborious procedure requires additional equipment, which significantly increases the cost of electrochemical generators of the MEA on the basis of the membranes of PBI/phosphoric acid.
\nDue to the high cost of perfluorinated polymer sulfonic acids and also because of their high permeability toward methanol, great attention to various hydrocarbon polymer sulfonic acid was given in recent years. At a lower cost of production, those acids could be a substitute Nafion [5].
\nTypical examples of hydrocarbon polymers used as membranes, fuel cells are sulfonated polyetheretherketone, polyarylene, polysulfone and polyimides.
\nIn general, in comparison with National, hydrocarbon polymers are characterized by both advantages and disadvantages. Typically, the synthesis of carbohydrate polymers of the least costly than the synthesis of fluorine-containing polymers. The permeability of the hydrocarbon polymers on oxygen and methanol is lower than polyfluorinated polymers. Because of lower hydrophobicity of the macromolecules of hydrocarbon polymers in General, the sensitivity of their proton conductivity to the degree of hydration of the reactants supplied to the fuel cells is not as pronounced as perfluorinated sulfonic acids. This simplifies the control of water balance in the MEA during the work. The less pronounced hydrophobic properties of hydrocarbon polymers molecules are also allowing to retain water at high temperatures, which increases the possible working temperature range of the FC – in comparison with FC-based membranes Nafion and its analogs. However, the balance of conductivity and mechanical properties of hydrocarbon polymers is worse, in general, than for the perfluorinated polymeric sulfonic acid.
\nThe first real working generator on fuel elements, was the generator of General Electric power of 1 KW, which was used as a source of electricity and drinking water for astronauts participating in the Gemini project in the mid-1960s. However, the working life of this installation was limited due to the chemical degradation of the membranes based on sulfonated polystyrene under the action of peroxides, formed at the cathode. For such membranes the company Ballard Power Systems has developed a new series of sulfonated copolymers of α,β,β-trifluorostyrene and substituted α,β,β-trifluorostyrene.
\nSuch polymers are known under the brand name Ballard Advanced third generation Membrane (BAM3G) and have a chemical structure shown in Figure 4.
\nStructural unit of sulfonated polystyrene.
Alternative and relatively cheap way of obtaining proton-exchange membranes is the method of grafting of ionogenic groups in the fluorinated polymer matrix. The method of radiation grafting is well known as a method of modification of polymers to modify their physical-chemical properties [11–16]. Radiation-grafted membranes get based on existing commercially available films in three stages. In the first stage, a polymer film is irradiated with an electron beam or gamma radiation for the formation of free radicals in the polymer material. Next, to the polymer backbone sutured to the lateral pendants, which are then sulfonated. It is argued that the process of obtaining such membranes more economical than the manufacture of Nafion. Using this method you can modify the fluorine-containing materials in [17–20], but comparison of these materials with each other is difficult due to different sample conditions and different degree of grafting.
\nMost radiation-grafted membranes contain polystyrenesulfonic acid in side chains (Figure 5).
\nStructure of the polymer with sulfonated styrene in the side chain. The main chain is hydrophobic.
As a polymer backbone, a variety of fluoro-substituted polymers include polyvinylidene fluoride, a vinylidene fluoride copolymer with hexafluoropropylene with a different molar ratio of comonomers, a copolymer of tetrafluoroethylene with hexafluoropropylene, etc. [20, 21, 22].
\nThe values of proton conductivity of the obtained membranes at high degrees of grafting are compared with Nafion up to 0.11 s/Cm under 100% humidity and room temperature. The same can be said about the permeability of hydrogen [22]. The value of proton conductivity is directly related to the ability of the membrane to absorb water, which in turn substantially depends on the properties of the polymer matrix. Usually, a significant disadvantage of these membranes is their high degree of swelling, greatly exceeding the values for Nafion [20, 21].
\nBallard Advanced Materials has been researching this group of polymers over the past 10 years. The first series of polymers based on polyphenylquinoxalines (PPQ), named BAM1G, was obtained by direct sulfonation of the PPQ (Figure 6).
\nThe structural unit of sulfonated polyphenylquinoxaline.
BAM1G membrane different thickness (40–120 μm) has good mechanical properties in dry and wet conditions. The characteristics of these membranes with equivalent weight of 390–420 is comparable to Nafion-117, however, the duration of work in the fuel cell before the onset of degradation is low, averaging 350 h [23]. It is obvious that they are not able to make real competition perfluorinated membranes.
\nThe basis of polyarylethersulfones is phenyl rings, separated alternately by ether and sulfonic groups. The most researched commercially available Udel polyarylethersulfones (PAES) (Figure 7) и and Victrex polyethersulfones (PES). PAES can be partially fluorinated, like Ballard Advanced Materials BAM2G membranes.
\nVarious polyarylethersulfones: PAES, sulfonated to the ortho position to the ether bridge of bisphenol-A (a); PAES, sulfonated to the diarylsulfonic part (b); polymer BAM2G (c); sulfonated PES (d) [
The processes of sulfonation of PAES have been studied in detail in [24, 25] and it is shown that for the case of PAES it is impossible to obtain a polymer containing more than one sulfogroup per monomer unit. The use of a softer sulfonating agent (methylsilylchlorosulfonate), in contrast to a rigid sulfurating agent (chlorosulfonic acid), avoids the destruction or cross-linking of the polymer. A disadvantage of sulfonation under mild conditions is the limited degree of sulfonation [26].
\nDirect sulfonation of PAES, depending on the conditions, leads to two different variants of the arrangement of the sulfogroups in the ortho position to the ether bridge of bisphenol-A (Figure 7a) see [27] or to the diarylsulfonic part (Figure 7b) see [28], which is most resistant to hydrolysis. In the first case, membranes based on sulfonated PAES are water-soluble at sulfonation degrees of more than 30%, which does not allow their use in fuel cells.
\nWhen sulfonated in the diarylsulfonic part, the membranes become water-soluble only at degrees of sulfonation greater than 65% [28]. Attempts have been made to cross-link such membranes in order to reduce solubility in water [29]. However, the cross-linked membranes become brittle at low humidity and show unsatisfactory results when tested in a fuel cell.
\nMembranes based on sulfonated PES (Figure 7d) are insoluble in water. In the case of PES, proton conductivity at the Nafion level is reached at degrees of sulfonation of the order of 90%, however, such membranes have a high degree of swelling (three times greater than Nafion at room temperature), which increases significantly with increasing temperature to 80°C and impairs the mechanical properties. To overcome this problem, the membranes were cross-linked with diamines, which reduced not only the degree of their swelling, but also the conductivity [27].
\nMembranes based on sulfonated fluorinated PAES that are insoluble in water show better performance when tested in a fuel cell compared to Nafion-117 and Dow membranes see [28], but their service life is limited to about 500 h.
\nPEEK is a class of aromatic semicrystalline polymers based on phenyl rings separated by ether and carbonyl (−CO-) groups (Figure 8).
\nStructural units of PEEK: Basic PEEK (a) and sulfonated (S-PEEK) (b).
These polymers have a high thermal stability, chemical resistance and have limited solubility in organic solvents. With the introduction of sulfogroups into the main chain of polymers, their crystallinity decreases and the solubility increases [30, 31].
\nThese non-sulfonated polymers are stable up to 500°C, and sulfonated polymers are stable up to 240°C. There are various procedures for sulfonation of PEEK [32, 33]. Since the sulfonation reaction proceeds by the electrophilic mechanism, in the case of PEEK, the sulfogroup is successfully introduced only into the aromatic nucleus between the two ether bonds because of the high electron density in this nucleus. It is possible to add only one sulfogroup to the monomer unit. In the case of PEEK, the use of chlorosulfonic acid as a sulfurizing agent destroys the polymer see [34], therefore concentrated sulfuric acid is used for this purpose [35, 36]. It is possible to achieve a degree of sulfonation of 30–100% without cross-linking and polymer degradation. However, in the sulfonation of PEEK by sulfuric acid under heterogeneous conditions, it is impossible to achieve a random sequence of sulfonated and non-sulfonated polymer units with a sulfonation degree of less than 30% [37]. Successful control of the arrangement of the sulfogroups in the polymer chain can be achieved by using a precursor polymer obtained by copolymerization of amenable and non-sulfonated monomers, followed by sulfonation of the resulting random copolymer [38]. Similar methods of directed design of molecular structure prevent additional and sometimes unpredictable macromolecular reactions in the process of sulfonation.
\nThe solubility of these polymers directly depends on the degree of sulfonation. Thus, with a degree of sulfonation of more than 30%, the polymers are soluble in DMSO, DMF, N-methylpyrrolidone. With an increase in the degree of sulfonation up to 70%, the polymer dissolves in methanol, and at a degree of sulfonation more than 70% – in water. The absorption of water by membranes based on S-PEEK at a degree of sulfonation of 65% and humidity of 100% is 8%. With the same degree of sulfonation and humidity, the conductivity of S-PEEK is small – about 10−5 S/cm [39]. At high degrees of sulfonation, membranes based on S-PEEK have high degrees of swelling. To reduce swelling, chemical cross-linking of macromolecules or the addition of agents forming strong hydrogen bonds are used [40]. For example, in Ref. [41] membranes based on mixtures of S-PEEK with amine derivatives of polyarylester sulfone, polyamides and poly-facets were obtained. The degree of swelling of such membranes can be reduced by strong hydrogen bonds between the polymer molecules or the formation of polysols, which, however, results in partial blocking of the sulfogroups and a decrease in the proton conductivity of the membranes.
\nPolyphosphazenes (Figure 9 in Ref. [42]) are a new class of polymers that are promising for use in FCs due to their thermal and chemical stability and the ability to easily vary the chemical structure of the polymer over a wide range by introducing various side chains into the main chain.
\nThe structural link of polyphosphazene basic (a), sulfonated (b) [
Proton-exchange membranes based on sulfonated polyphosphazenes may well act as an alternative to perfluorinated membranes. However, there are only a limited number of papers devoted to obtaining and investigating the properties of such membranes. Difficulties are associated with obtaining water-insoluble polymers and matching their hydrophilic/hydrophobic properties [44]. One of the main methods for the synthesis of these polymers is the reaction of polydichlorophosphazene with various nucleophilic agents to form organic polymeric derivatives with a high molecular weight, the properties of which depend to a large extent on the nature of the side substituents. The sulfonation of aryloxy- and arylaminophosphazenes with concentrated sulfuric acid was carried out in Ref. [45]. It is also possible to use 1,3-propanesulfone as a sulfurizing agent, however, the degree of sulfonation is low enough. Aryloxypolyphosphazenes can also be sulfonated with sulfur trioxide in dichloromethane. It is also possible to use 1,3-propanesulfone as a sulfurizing agent, but the degree of sulfonation is low enough [46]. Aryloxypolyphosphazenes can also be sulfonated with sulfur trioxide in dichloromethane. It was shown in Ref. [47] that at the molar ratio of SO3 to the amount of monomeric units, only C-sulfonation is observed and the polymer chains attack with the formation of the ≡N → SO3 complex, while increasing the amount of SO3 there is not only C-sulfonation.
\nOne of the promising materials for the manufacture of membranes TE are aromatic polyimides (PI). Polyimides are characterized by high heat resistance, and the most heat-resistant polyimides based on pyromellitic dianhydride and 1,4,5,8-naphthalenetetracarboxylic acids, which practically do not soften before the beginning of thermal decomposition, and their thermal decomposition temperature is more than 500°C (Figure 10).
\nGeneral scheme for the preparation of polyimides. For the preparation, one dianhydride and one or more diamines are used, therefore Q, most often aromatic, and X, Y, Z may be different or identical, both aromatic and aliphatic.
However, the heat resistance of polyimides is well regulated by varying the nature of the monomers and is usually 300–430°C [48]. Most aromatic polyimides are insoluble in most organic solvents, are inert to the action of oils, and also hardly change under the action of dilute acids.
\nWith the introduction into the side chain of various substituents, especially card groups (phthalide, phthalimidine, fluorene and anthrone), the solubility of polyimides is substantially improved. Thus, poly (pyromellitimide) of dianylinophthalein (I) dissolves in DMF, m-cresol, sim-tetrachloroethane, hexafluoro-2-propanol, polyimides 3,3′, 4,4′-benzophenone tetracarboxylic (II) or 3,3′, 4, 4′-diphenyloxydetracarboxylic acid (III) and dianilinfluorene are also dissolved in methylene chloride, chloroform [49].
\nBy themselves, polyimide films have very low proton conductivity. Therefore, to ensure high proton conductivity, acid groups are introduced into the polyimide chain (most often sulfonic acid – SO3H). In membranes based on sulfonated polyimides (containing in the main chain and/or in the branches of the group SO3H), the gas permeability for hydrogen is approximately three times lower than for Nafion-117 [50].
\nThe use of polyimides for the manufacture of membranes is hampered by their extremely poor solubility. Fortunately, this problem can be solved, as shown above, by the chemical structure of the polymer, for example, when a 2,2′-diamino-3,4′-diphenyl ether is used as the unsulfonated diamine, a polymer soluble in m-cresol can be obtained.
\nPolyimides exhibit different resistance to the action of water vapor in different ways. Since polyimide chains in membrane materials will be responsible for mechanical strength and resistance to fuel cell (FC) conditions, it is necessary to choose such structures of monomers (aromatic tetracarboxylic acid dianhydrides and aromatic diamines) that will yield polyimide matrices that are stable under the action of water vapor.
\nIt is necessary to consider what determines the stability of polyimides in water environment. Pure water under normal conditions for polyimide films does not work, however, when boiling in water, the films gradually lose their high mechanical properties [51]. In strongly alkaline (pH > 12) or strongly acidic (pH < 2) media, hydrolysis accelerates sharply, and the film is completely destroyed. This phenomenon is associated with the destruction of imidic bonds. Resistance to hydrolysis depends most strongly on the chemical structure of the dianhydride component of the unit. In particular, polypyromellitimides are among the least resistant to hydrolysis of polyimides [52]. The authors suggest that the hydrolysis of polyimides in neutral environment proceeds through tetrahedral compounds according to the scheme (Figure 11).
\nScheme of the first and second stage of hydrolysis of polyimides in a neutral environment.
Further, an amide bond is broken. The limiting stage is the first, namely, the breaking of the imide cycle. The mechanism of alkaline hydrolysis in the example of polypyromellitimides was considered in Ref. [53]. A polyimide film when immersed in a 4 M water solution of KOH at 20°C swells, turns pale, and after few hours becomes colorless while retaining strength and flexibility. After treatment with hydrochloric acid and heating for 30 min at 140°C, this film, according to the results of IR spectroscopy and its physical properties, becomes similar to the original one. In the described conditions, the polyimide regenerates.
\nTo study hydrolytic stability, the authors in Ref. [54] synthesized and studied less stable phthalic (I) polyimides, compared to naphthalic (II) polyimides (Figure 12). The resistance of polyimides to hydrolysis was investigated by IR spectroscopy. Thermal stability, proton conductivity, water absorption and ion-exchange capacity of polyimides were also measured.
\nPhthalic (I) and naphthalic (II) series of sulfonated polyimides (where X: –O– or –CH2–).
Comparing the IR spectra of both series of polyimides after aging in water at 80°C for 4 h, the intensity of 1784 cm−1 peaks characteristic for the C = O bond in the case of a series of naphthalic polyimides was higher than in the case of phthalic polyimides. In addition, in the case of naphthalic polyimides, the peaks characteristic of the S = O bond did not decrease or disappear. Similarly, naphthalic polyimide films retained their mechanical integrity even after 3 days of soaking. Phthalic polyimides disintegrated after 52 h.
\nThe presence in the polymer structure of a binaphthalic dianhydride fragment and benzophenone groups in the meta-position toward the imide ring should additionally increase the hydrolytic stability of the polyimide [55–58].
\nThe best hydrolytic stability of naphthalic polyimides appears to be due to steric hindrance, which hinders the approach of water to attack the carbonyl carbon atom of the imide ring (see Figure 11).
\nThe influence on the hydrolytic stability can also be exerted by diamine, by increasing (decreasing) the electron density (decrease (increase) in the electrophilicity) of the carbonyl carbon of the imide cycle, for example:
The introduction of a voluminous aliphatic fragment into the diamine structure both into the main chain and as side branches [59, 60].
The introduction of bridging electron-donor sulfur atoms or phenoxy groups into the main polyimide chain, in addition to substantially reducing the electrophilicity of carbonyl carbon, significantly increase the hydrolytic stability [61–64].
Membranes that are made from polyimides, with sulfonated side branches are more stable than similar membranes, where sulfogroups are in the main chain [65].
In contrast, the introduction of trifluoromethyl groups, which have a strong electron-withdrawing effect, would threaten the stability of the imide group [66].
The hydrolysis reaction of imide rings is reversible, this assumption was confirmed by the fact that cross-linked SPI, with a different chain length of cross-linker, is much more resistant to hydrolysis than non-cross-linked and resistance to hydrolysis increased in proportion to the reduction of the length of the chain of the cross-linking agent [67]. Thus, the main chain of polyimide can be restored provided that the fragments are closely spaced [68].
It was recently discovered that membranes based on porous spongy, non-sulfonated polyimides (matrices), the pores of which were filled with different SPIs, showed higher hydrolytic stability than membranes obtained from the same SPI, but not in the PI matrix [69].
The solubility of polyimides strongly depends on the chemical structure of the polymer. Two key factors in the development of soluble polyimides are the decrease in the regularity (repeatability of the links) of the main chain and the minimization of the density of imide rings along the main chain. Progress in solving these problems was achieved using fluorine-containing dianhydrides, such as 4,4-(hexafluoroisopropylidene) diphthalic anhydride, or by including oxygen atoms in the diamine (e.g., oxydianiline). In addition, aliphatic side chains were included in diamines to reduce the interaction between polyimide chains and increase solubility. In the previous decades, a large number of structural changes were undertaken, including the inclusion of thermally stable, flexible or asymmetric bonds in the main chain and the introduction of bulky substitutes. Polyimides containing bulky triphenylamine units along the polymer backbone are amorphous and have good solubility in many solvents, excellent film formation and high thermal stability [49].
\nIt is shown [50] that the sulfonated naphthalic (six-membered imide cycles in the circuit) polyimides when working in the fuel cell demonstrate results comparable to Nafion, at least when working up to 3000 h. At the same time, the characteristics of the membranes based on sulfonated phthalic (five-membered imide cycles in the circuit) of the polyimides is significantly deteriorated after 70 h of operation. It has been suggested that in the process of hydrolysis of phthalic imide structure, there is a rupture of the polymer chains and the membrane becomes brittle. Since six-membered cycles of naphthalic polyimide are much more stable to hydrolysis, their chemical structure meets the requirements for FC membranes. The permeability of methanol through the membrane SPI is much lower than for PFSA membranes [70].
\nThe use of SPI as proton-conductive membranes was first demonstrated in Ref. [71]. The main driving force for the development of SPI research was the search of cheaper alternatives to commercially available Nafion developed by DuPont. Very soon it was discovered that, although SPI swell in high humidity conditions needed to operate fuel cells, however, they showed high values of proton conductivity comparable to Nafion. The water absorption and the coefficient of osmotic pressure are not significantly changed in a wide range of temperatures in contrast to Nafion. Such features make SPI preferred for use in fuel cells operating at medium-temperature range, also SPI less membranes degrade when enabling/disabling FC and also better retain water on the anode side of the MEA.
\nWhile the first generation of the SPI electrolytes showed values of conductivity of 2·10−3 s/cm, up to 4·10−2 Sm/cm in [72, 73] which were significantly lower than the conductivity of Nafion, the next generation SPI electrolytes gave satisfactory values of conductivity to 1.67 Cm/cm at 120°C in Ref. [74] and 1201 Cm/cm at 80°C for SPI/graphene composite material.
\nThese materials are currently considered promising candidates for the use as FC with PEM, working in the temperature range from 40 to 100°C. In addition, SPI membranes exhibit a permeability to methanol is several times lower than in Nafion, particularly at elevated temperatures [75, 76].
\nTests made on FC based on the membranes from variety of SPI showed that the operating time of FC is strongly dependent on the temperature regime of its work. FC on the basis of SPI with sulforaphane in the side chains, in general, worked longer than FC based on SPI with sulfonate groups in the main chain, but still inferior to Nafion. Although testing of SPI membranes was carried out in a real working environment, working time of FC is depended not only on the stability of the membrane, but also on the quality of the connection of electrodes to the membrane [77, 78].
\nAccording to Ref. [5] there are not so much easily synthesized structures of dianhydride aromatic tetracarboxylic acids giving during polymerization of imide cycle naphthalic type. It should be noted that obtaining of the diamines is much easier than dianhydrides and almost all the variety of polyimide structures is achieved through various diamines. However, not all structures of aromatic diamines are easily synthesized and allow you to obtain a sulfonated polyimide with satisfactory hydrolytic stability [79, 80].
\nCopolymerization is one of the most common and successful ways of preparing new materials with the necessary properties arising from the presence of several structures with different chemical or physical properties in one polymer chain. In order to increase the efficiency of FC operation, it is necessary to develop polymeric electrolyte membranes of block structure (block copolymers) that each repeating polymer block will perform a certain function and to give the final materials unique properties that are inaccessible to conventional polymers.
\nThe most common type and appropriate type of units for inclusion in the PI circuit are polysiloxane, see [81], its characteristics of linear organosilicon polysiloxane meet the requirements of the PEM FC. One of the most common polysiloxane – polydimethylsiloxane (PDMS) among all synthetic polymers has the very high flexibility of the polymer chain. Another important advantage of polysiloxanes is their heat resistance and oxidation resistance.
\nFigure 13 shows the process of obtaining such block polymers [82].
\nSynthesis of sulfonated poly(imide-siloxane).
Polyimide chains of block copolymer are sufficiently rigid formations, sulfonate groups 3,3′-benzylisothiocyanate provide high proton conductivity. Experimental fuel cells, constructed with the use of such membranes showed output current, comparable to the FC based on Nafion [83]. Siloxane blocks are in them as a fragment, which increases the mobility and hydrophobicity of the chain, which ensured the formation of a large number of proton-conducting channels in the membrane [84]. Stitching also gives the membrane additional mechanical strength.
\nModification of polyimide chains of inclusions of crown ethers, may also improve mechanical properties and increase the solubility, reducing the rigidity and the regularity of polyimide chains. In addition, the size of the cavity of some crown ethers correspond to the diameters of the channels, these inclusions can provide additional ion conductivity, provided they are aligned properly for the formation of conducting channels [85].
\nEmerging market of FC is the main driving force pushing the scientific community for the development of inexpensive and high-performance membrane materials. That is, the cost of manufacturing proton-conducting membranes contributes most to the value of FC and, as a consequence, the cost of the produced energy. FC running on methanol are the most promising for transportation and portable electronic applications because of the serious problems associated with the storage and use of hydrogen.
\nDespite the fact that PFSA are still excellent materials for membrane fuel cells, their prices are still consistently high and they do not fully satisfy all of the requirements of PEM, in particular on the permeability of methanol. These factors stimulate the interest of researchers to finding cheap and high-performance alternative materials for use as membranes, fuel cells.
\nPolymers such as polyimides, despite their poor solubility and hydrolytic stability, are attractive to researchers due to the wide variety of possible chemical structures. Polyimides, including partially fluorinated, have high mechanical strength, chemical and thermal stability. In addition, naphthalic polyimides, when operating in a fuel cell, exhibit results comparable to Nafion, at least when operating up to 3000 h.
\nOne of the solutions to overcome the shortcomings of the PI, would be the development of PEM block structure (block copolymers), polyimide-based, where each repeating polymer unit performs a specific function, which together lead to the satisfaction of all conflicting requirements of PEM. However, development of such PEM is complicated by the fact that improving one characteristic (e.g., increasing the number of groups-proton acceptors in polymer chains), thereby deteriorating the other parameters (in this example, the deterioration of the mechanical stability, swelling and the formation of a non-conductive gel). On the other hand, improving the mechanical parameters of the PEM (e.g., cross-linking of the polymer) often leads to a deterioration of proton conductivity. Therefore, modeling of the PEM design must be complex. It is necessary to select the block structure of the copolymer a way to find the optimum implementation of the requirements of PEM FC. In view of the extremely high thermal stability of the polyimide base, the potential for the use of materials should not be limited to low-temperature FC only. Due to the possibility of introducing imidazole-containing blocks, and phosphoric acid groups, it is also possible to develop materials for medium-temperature phosphoric acid FC.
\nOur group has developed laboratory techniques for the preparation of monomers for the production of membranes based on SPI, as well as inclusion blocks, to improve their properties. According to the developed methods, experimental samples of monomers and inclusions were made. The properties of the experimental samples are investigated and characterized. A laboratory procedure for the production of SPI films and block copolymers based on them has been developed. According to the developed methods, experimental membrane samples were prepared. Research and adjustment of the properties of experimental samples are being carried out.
\nApplied researches are carried out with state financial support represented by the Ministry of Education of Russia under the Agreement on granting subsidies No. 14.625.21.0036 of October 27, 2015. Unique identifier for Applied Scientific Researches (project) RFMEFI62515X0036.
\nAn umbilical hernia is defined as a midline hernia located at or near the umbilicus [1]. Umbilicus is a frequent site of hernia because it represents a natural weak spot of the abdominal wall, being the attachment site of the umbilical cord during the fetal period.
The literature on umbilical hernias in adults remains less extensive compared to other types of hernias. In fact, in adults, groin hernias are more frequent, since umbilical hernias are more studied in children.
The risk of strangulation is important, estimated at up to 17% in umbilical hernias, up to three times higher than in femoral hernia [2]. To avoid these complications, a surgical treatment is required. Despite the recent advances in terms of mesh varieties and minimally invasive surgery (laparoscopic and robotic surgery), there is still no consensus on the optimal method for repair of umbilical hernia.
It is estimated that every year, 20 million abdominal wall hernias surgeries are performed worldwide [3]. Umbilical hernia is the second most frequent type of hernia and accounts for 6–14% of all abdominal wall hernias in adults, after inguinal hernias [1].
It is a very common condition in children, occurring in one of every six children [4]. It represents an important part in the practice of pediatric surgeons, especially in sub-Saharan Africa [5]. However, in adults, nearly 90% of umbilical hernias are acquired with no indication of hernia in childhood [6]. The risk factors are the same as for other abdominal wall hernias and are caused predominantly by intra-abdominal hyper pressure and/or parietal weakness. The repetitive action on the abdominal wall due to increased intraabdominal pressure favor microscopic tears of tissue. This will lead in time to hernia formation.
The risk factors are physical labor, obesity, ascites, constipation, pregnancies, excessive coughing, or dysuria. A female predominance is however noted with a sex ratio of 3:1 [7]. This is explained by the different distribution of risk factors according to sex. Indeed, obesity is more common in women and pregnancy is a factor noted exclusively in women. This female predominance is also due to the distension of the umbilicus associated with childbirth.
Umbilical hernias occur more often above or below the umbilicus rather than directly through the umbilicus [8]. This is why, according to the classification of the European Hernia Society, hernias whose rings are located between 3 cm on either side of the umbilicus on the linea alba, are considered as umbilical hernias (Figure 1) [9].
Localization of umbilical hernias according to the classification of the European hernia society [
Adult umbilical hernias are frequently asymptomatic. The most frequent reasons for consultation are intermittent pain and esthetic discomfort when the size is important [2].
Palpation helps assess the size of the neck and the reducibility of the hernia. When there is a complication, the abdominal pain is constant. The main complication is strangulation (occurrence of ischemia due to a compromised blood supply). In most cases, patients with a strangulated hernia have previously experienced incarceration seizures with spontaneous reduction.
On physical examination, palpation reveals an irreducible and painful umbilical swelling. Figure 2 shows a strangulated umbilical hernia with irreducible swelling. When the small intestines are in the hernia sac, signs of intestinal obstruction appear (vomiting, lack of gas or stool).
Non-reducible umbilical tumefaction (image of the Department of Surgery, Gaston Berger University, Saint-Louis, Senegal).
Another complication that can occur is loss of domain. It represents a chronic large irreducible hernia reducing the volume of the abdominal cavity and creating a “second abdomen” [10].
The diagnosis of umbilical hernia is most often evident on physical examination of the abdomen with tumefaction in the umbilicus.
However, the clinical presentation depends mainly on the size of the hernia (neck and sac) and the patient’s BMI. In fact, hernias with a small neck or occurring in obese subjects can go unnoticed, especially in an emergency context. In these cases, performing imaging tests is important for an accurate diagnosis.
Imaging has an important role in the definitive diagnosis. In fact, clinical examination alone cannot exclude the diagnosis of hernia [11].
Indeed, many hernias are only detectable on imaging (ultrasound or computed tomography) especially when the defect is small or the abdominal fat tissue is important. Besides, imaging can also look for other abdominal wall hernias and more accurately determine the size of the wall defect for an optimization of the treatment.
Imaging also allows to make the differential diagnosis with other, more rare conditions such as abscesses, hematomas or tumors.
Ultrasound is cost effective and efficient. A study has shown that up to 25% of the general population present umbilical hernia when ultrasound is used for diagnosis [12]. This confirms the fact that ultrasound has a much greater sensitivity in detecting umbilical hernias than clinical examination alone. On the other hand, ultrasounds are dependent on the skills of the operator and have a limited contribution when the hernias are large or even with loss of domain. In these cases, the CT scan is of great help. With sagittal and axial reconstructions, CT scan gives more precise information on umbilical hernias (Figures 3 and 4).
Axial contrast-enhanced reformatted CT image of an uncomplicated umbilical hernia with small bowel as contents (arrowhead) during Valsalva maneuver [
Axial contrast-enhanced reformatted CT image of an incarcerated umbilical hernia with omental fat as contents (arrow) [
More recently, some studies have shown that MRI has the best sensitivity and specificity of 92% and 95%, respectively, in the definitive diagnosis of abdominal wall hernias. Indeed, CT and ultrasound cannot completely rule out the presence of a hernia [14]. However, the main drawback of MRI remains the cost-effectiveness and its unavailability in resource limited context.
The treatment of umbilical hernia in adult is surgical. The preparation of the patient is very useful to decrease complications after elective umbilical hernia surgery. In fact, it is recommended smoking cessation for 4–6 weeks and weight loss to a BMI below 35 kg/m2 before surgery [15]. In fact, controlling these factors can reduce the rate of post-operative complications and improve the recovery.
All types of anesthesia are possible in umbilical hernia surgery (local, spinal or general anesthesia).
Local anesthesia is feasible in selected patients. Its main advantages lie in the reduction of complications associated with general anesthesia, the reduction of the length of hospital stay (ambulatory surgery) and its cost effectiveness [16, 17]. However, in large hernias or in obese subjects, its use can be difficult.
Rachi-anesthesia is also feasible but often requires a high block which is often incomplete [2].
Thus, general anesthesia is preferred because it allows surgery under better conditions. However, the best technique should be the one based on shared decision-making [15].
Recently, in developed countries there is an increased interest in “watchful waiting” due to the small risk of strangulation, less than 1% per year [18]. However, a study comparing watchful waiting to surgery showed that, despite no significant difference in terms of mortality in readmission, 19% of non-operated patients will require surgery in the follow up [19]. Due to the risk of complications (strangulation), a watchful waiting approach is not recommended in umbilical hernia and this approach cannot be generalized and depends on the context of care. There is a lack of evidence on the safety of this approach, especially since an adequate follow up is not always possible in resource limited context. Even if watchful waiting is chosen, only asymptomatic umbilical hernia with no esthetic compromise should be non-operatively treated [15].
Open approach is realized with different surgical techniques.
These surgical techniques depend mainly on the use or not of prosthetic material (suture repair or mesh repair).
The suture repairs most performed are simple primary closure and the technique of overlapping the fascia. This second technique was first described by William Mayo and was commonly used [8]. It consists of a plasty of the abdominal wall fascia in “vest-over-pants” (Paletot). However, with a high incidence of recurrence, this approach is less used now.
According to the Guidelines from the European Hernia Society and Americas Hernia Society, it is strongly recommended to use a mesh. In fact, it significantly decreases the rate of recurrence [15]. A randomized clinical trial showed that this rate can be reduced to 1% when mesh is used when compared to suture repair (11%) [20].
Mesh repair is now considered the “gold standard” for umbilical hernia in adults with no associated morbidity factors [21, 22]. In a selected group of patients, suture repair can be performed if the umbilical hernia defect is less than 1 cm.
The laparoscopic approach makes it possible to reduce esthetic damage by maintaining the appearance of the umbilicus and avoiding extensive dissections.
In addition, laparoscopy can diagnose other missed hernia during pre-operative procedures, evaluating all of the abdominal wall. Another advantage is the precise evaluation of the umbilical defect in order to use a mesh with the adequate size and overlap of the borders of the defect [23].
The technique consists in the placement of a mesh with a sufficient overlap (3 cm). The recommended site of the mesh placement is pre peritoneal or retro muscular due to the risk of adhesion with intra peritoneal mesh [15].
The prior primary closure of the umbilical defect is not mandatory but its realization may reduce the recurrence rate [24].
The most used mesh is polypropylene because it is cost effective and more available than others. However other types of mesh can also be used (light weight macroporous, composite or dual sides) [8].
Laparoscopic surgery is mainly suggested if the umbilical hernia is large (over 4 cm) [15]. This can decrease the risk of wound infections, post-operative pain, length of hospital stay, and other complications, mostly in patients at risk (obesity, smoking).
The use of robotic surgery can improve the results of conventional laparoscopy. Indeed, it allows additional degrees of movement, 3D visualization and better ergonomics for the surgeon. Besides, the attachment of the prosthesis to the anterior abdominal wall, which can be tedious in laparoscopy, is made even easier with the robotic approach [25]. However, longer learning curve, prolonged operative time and cost may be the main limitations of its use.
Hence, in low resource settings, open mesh repair is more feasible. This explains why “tailored surgery” should be the best approach according to the type of patient, the type of hernia, and the context of practice [26].
The additional morbidity and mortality in emergency surgery require elective surgery whenever it is possible [27]. Evaluation of the contents is mandatory to assess its viability. When there is only ischemia and recoloration after reduction, a simple reduction and parietal repair are done (Figure 5). Bowel resection is performed when there is necrosis.
Per operative image of open approach for a strangulated umbilical hernia: (A) Aspect of the unopened sac; (B) Contents of the hernia with small bowel with ischemia (yellow arrow) and omental fat (white arrow); (C) and (D) Resolution of the small bowel ischemia with recoloration (yellow arrows) (images of the Department of Surgery, Gaston Berger University, Saint-Louis, Senegal).
Both open or laparoscopic approaches are feasible but the open approach is recommended due to the possible necessity of bowel resection and the relative contra-indication of mesh use.
Considering the World Society of Emergency Surgery (WSES) guidelines, the use of mesh will depend on the contamination of the surgical field according to the Centers for Disease Control (CDC) classification. For clean (Class I) or clean-contaminated (Class II) procedures, a mesh can be used. However, for contaminated or infected wounds (Class III and Class IV), suture repair is preferred [28].
The most common post-operative complications regardless of the surgical technique are recurrence, superficial surgical site infection and chronic pain or discomfort [29].
Recurrence rate is now low (less than 1%) since the widespread use of mesh. However, mesh related complications are possible and not infrequent (seroma, adhesion, infection, migration or rejection). The removal of the mesh, if possible, should always be considered when mesh related complications occur.
The frequency of these complications is mainly related to co-morbidities, the kind of mesh, the surgical technique and the strategy used to prevent infections [30]. Hence, these complications can be prevented by patient optimization. In fact, obesity, excessive weight and smoking are the mains risk factor for the occurrence of complications [31]. Controlling these factors help reduce the rate of complications.
Umbilical hernia remains a relatively common disease in adults. Its diagnosis is clinical and imaging can be used for small defects or in patients with excessive weight. Mesh repair should be preferred for uncomplicated hernia with a defect of more than 1 cm.
Minimally invasive surgery (laparoscopy and robotic) presents important advantages in terms of cosmetic outcome, wound infections, post-operative pain and length of hospital stay.
According to the emergency, the patient characteristics, or the context, “tailored and optimized surgery” should always be used to have the best short and long terms outcomes.
“The authors declare no conflict of interest.”
As an Open Access publisher, IntechOpen is dedicated to maintaining the highest ethical standards and principles in publishing. In addition, IntechOpen promotes the highest standards of integrity and ethical behavior in scientific research and peer-review. To maintain these principles IntechOpen has developed basic guidelines to facilitate the avoidance of Conflicts of Interest.
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\n\nCONFLICT OF INTEREST - REVIEWER
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