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Glycerol Hydrogenolysis By In Situ Generated Hydrogen Development Of Novel Catalytic Reactive System
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Book Synopsis Glycerol Hydrogenolysis by in Situ Generated Hydrogen : Development of Novel Catalytic Reactive System by : Iñaki Gandarias Goikoetxea
Download or read book Glycerol Hydrogenolysis by in Situ Generated Hydrogen : Development of Novel Catalytic Reactive System written by Iñaki Gandarias Goikoetxea and published by . This book was released on 2012 with total page 206 pages. Available in PDF, EPUB and Kindle. Book excerpt:
Book Synopsis Catalytic Glycerol Hydrogenolysis to Produce 1,2-propanediol with Molecular Hydrogen and in Situ Hydrogen Produced from Steam Reforming by : Yuanqing Liu
Download or read book Catalytic Glycerol Hydrogenolysis to Produce 1,2-propanediol with Molecular Hydrogen and in Situ Hydrogen Produced from Steam Reforming written by Yuanqing Liu and published by . This book was released on 2014 with total page 282 pages. Available in PDF, EPUB and Kindle. Book excerpt: Biodiesel has shown great promise to supplement the fossil diesel since it is a renewable energy resource and is environmentally friendly. However, the major obstacle to biodiesel large scale commercialization is the high production cost; so converting glycerol, the by-product of a biodiesel process, into value-added products is an efficient way to promote biodiesel production. 1,2-propanediol (1,2PD), also known as propylene glycol, is an important commodity chemical used for many applications such as polyester resins, liquid detergents and anti-freeze. It can be produced via dehydration of glycerol into acetol followed by hydrogenation of acetol into 1,2PD using a bi-functional catalyst. Currently high pressure gaseous hydrogen added for hydrogenation causes safety issues as well as additional costs of hydrogen purchasing, transportation and storage. Therefore, the utilization of the in situ hydrogen produced by steam reforming of a hydrogen carrier could be a novel route for this process. In this work, processes of glycerol hydrogenolysis to produce 1,2PD have been developed using different hydrogen sources, i.e. molecular hydrogen and in situ hydrogen produced by steam reforming. Three different preparation methods were attempted to prepare a Cu/ZnO/Al2O3 catalyst in a glycerol hydrogenolysis process, which were oxalate gel-coprecipitation, Na2CO3 coprecipitation and impregnation. The catalyst prepared by oxalate gel-coprecipitation showed the highest activity for production of 1,2PD. It was also found that the addition of alumina did not only improve the activity but also enhanced the stability of the Cu/ZnO catalyst as shown by the catalyst recycling experiments. The morphological and chemical properties of the catalysts were characterized via XRD, NH3 TPD, TGA and TEM. Compared with other preparation methods, the Cu/ZnO/Al2O3 catalyst prepared by oxalate gel-coprecipitation exhibited a well-mixed form for all the metals as suggested by the XRD and TGA results; the particle size of the Cu/ZnO/Al2O3 catalyst was smaller as shown in the XRD and TEM results, and also based on NH3 TPD analysis the Cu/ZnO/Al2O3 catalyst showed stronger acidic sites. When Ni was loaded onto the Cu/ZnO/Al2O3 catalyst by oxalate gel-coprecipitation, it was found that the activity for acetol hydrogenation was improved but the overall glycerol hydrogenolysis reaction was slower. This was mainly due to the reduced amount of strong acidic sites caused by the addition of Ni as observed from the NH3 TPD results. 2wt% Pd supported on a Cu/MgO/Al2O3 catalyst was used in this process. Higher reaction rate and higher 1,2PD selectivity could be obtained compared with a Cu/ZnO/Al2O3 catalyst. However, a significant deactivation was observed when the spent catalyst was used. The catalyst deactivation was mainly due to catalyst sintering during the reaction resulting in a larger particle size as suggested by XRD results. The activation energies for the glycerol hydrogenolysis reaction using Cu/ZnO/Al2O3 and Pd supported on Cu/MgO/Al2O3 catalysts have been calculated. The activation energy was calculated to be 69.39kJ/mole using a Cu/ZnO/Al2O3 catalyst and 113.62kJ/mol using a Pd supported on Cu/MgO/Al2O3 catalyst. It is suggested that the reaction was chemically kinetically controlled using both catalysts and the reaction using the Pd supported on Cu/MgO/Al2O3 catalyst was more temperature dependent. It was found that the 1,2PD selectivity was strongly dependent on hydrogen pressure. The low 1,2PD selectivity at lower hydrogen pressure was due to the formation of by-products caused by side reactions with acetol. The kinetic data of acetol hydrogenation suggested that the acetol hydrogenation step was significantly faster than the overall reaction and hence the glycerol dehydration step was the rate-determining-step. In the glycerol hydrogenolysis process using in situ hydrogen, the activities of the Cu/ZnO/Al2O3 catalysts prepared by different methods were determined and the experimental results show that the catalyst prepared by oxalate gel-coprecipitation has the best catalytic activity for glycerol conversion and 1,2PD selectivity. With Ni loaded onto a Cu/ZnO/Al2O3 catalyst, the 1,2PD selectivity was improved and the glycerol conversion was lower. It might be because Ni could improve the steam reforming activity to produce more hydrogen, but due to the reduced strong acidic sites based on the NH3 TPD results glycerol conversion was decreased. Cu/MgO/Al2O3 catalysts prepared by oxalate gel-coprecipitation were used in this process and the activity was found to be higher, i.e. higher glycerol conversion and 1,2PD selectivity, compared with the Cu/ZnO/Al2O3 catalyst due to a higher amount of acidic sites based on the NH3 TPD results; the Cu/Mg/Al composition was optimized. When Ni was added into a Cu/MgO/Al2O3 catalyst, it was found that with only 1mole% Ni loaded, the glycerol conversion was lower than that without Ni loaded and the 1,2PD selectivity was slightly improved; when the Ni loading was increased to 5mole%, the catalyst was almost completely inactive, since when 5mole% Ni was loaded, the acidic sites were almost completely eliminated as observed from the NH3 TPD results. When Pd was added onto a Cu/MgO/Al2O3 catalyst the 1,2PD selectivity was significantly improved. When Pd was loaded, more surface hydrogen atoms were provided as observed from the H2 TPD results. Cu/ZnO/Al2O3 and Cu/MgO/Al2O3 catalysts have been recycled and reused to investigate the stability of the catalysts. All the catalysts were deactivated after they were recycled and reused, since it was apparent that catalyst sintering occurred during the reaction resulting in a larger particle size based on the XRD results. The deactivation of the spent catalyst was also possibly due to the formation of carbonate when the metals were contacted with CO2 which was formed via steam reforming.
Book Synopsis Catalytic Hydrogenolysis of Glycerol to 1-propanol Using Bifunctional Catalysts in an Aqueous Media by : Chau Thi Quynh Mai
Download or read book Catalytic Hydrogenolysis of Glycerol to 1-propanol Using Bifunctional Catalysts in an Aqueous Media written by Chau Thi Quynh Mai and published by . This book was released on 2016 with total page 208 pages. Available in PDF, EPUB and Kindle. Book excerpt: Biodiesel is an attractive alternative fuel obtained from renewable resources and glycerol is produced as a major byproduct in the biodiesel industry. Upgrading glycerol to other valuable chemicals will contribute to an economic sustainability of the biodiesel industry. Valuable commodity chemicals such as 1,2-propanediol (1,2-PD), 1,3-Propanediol (1,3-PD) and 1-Propanol (1-PO) could be produced by catalytic hydrogenolysis. Although much work has been done towards the conversion of glycerol to 1,2-PD and 1,3-PD, the direct conversion of glycerol to 1-PO has not received much attention. From an industry point of view, the production of 1-PO is very interesting. 1-PO has potential applications as a solvent, organic intermediate and can be dehydrated to produce “green“ propylene for the production of polypropylene. Therefore, the development of a new process for the efficient conversion of glycerol to 1-PO will contribute to new “green” chemicals which will benefit the environment and make biodiesel processes more profitable as 1 kg of glycerol is produced for every 10 kg of biodiesel. In this research, heterogeneous hydrogenolysis of glycerol to 1-PO was carried out in a batch reactor using a bi-functional catalyst (prepared by a sequential impregnation method) in water, a green and inexpensive liquid medium. It was found that a bi-functional solid catalyst consists of a non-noble metal Ni for hydrogenation and an acidic function of silicotungstic acid (HSiW) supported on alumina (Al2O3) to be an active catalyst for the one-pot synthesis of 1-PO from glycerol and H2 in a liquid phase reaction. A systematic study has been carried out to assess the effects of operating conditions on the glycerol conversion. The catalysts were characterized using BET, XRD, NH3-TPD, TPR, TGA and FTIR techniques. The effect of different metals (Cu, Ni, Pd, Pt and Cs) supported 30HSiW/Al2O3 catalyst, heteroatom substitution (HSiW, HPW and HPMo) on NiHPA/Al2O3 catalysts and 10Ni/30HSiW supported on different supports (Al2O3, TiO2 and MCM-41) were studied to determine to what extent these components affect the catalytic activity of the NiHPAs/Al2O3 catalysts for the hydrogenolysis of glycerol. The effect of the preparation process on the catalytic activity and the structure of the catalyst was also studied. It was found that 1%Pt is the best promoter for the production of 1-PO in a stainless steel batch reactor (the selectivity to 1-PO was 59.2% at 45.3% conversion of glycerol). 1%Ni, a much cheaper metal, has fairly comparable reactivity to 1%Pt (the selectivity to 1-PO was 54.7% at 39.2% converison of glycerol). It was reported that the catalytic activity and thermal stability towards decomposition of the catalyst dependends on heteroatom substitution. Using NH3-TPD, XRD and FTIR it was found that while the Keggin-structure of HSiW and HPW supported catalyst is stable up to a treatment temperature of 450oC, the Keggin-structure of a HPMo supported catalyst was decomposed even at a treatment temperature of 350oC; the decomposition of HPMo into MoO3 is likely to be responsible for the inactivity of the NiHPMo catalyst for glycerol conversion. HPW and HPMo lost their acidity much more readily than HSiW, and a HSiW supported catalyst was the best candidate for 1-PO production. The catalytic activity and the acidity of 10Ni/30HSiW supported catalyst are influenced strongly by supporting 10Ni/30HSiW on different supports. Using XRD and FTIR it was found that the thermal treatment during the preparation process indeed affected the structure and the activity of the catalyst to some extent. The loss in activity of the catalyst, the decomposition in Keggin-structure of HPAs occur if the treatment temperature is higher than 450oC. It is important to note that this is the first report on a 10Ni/30HSiW suported catalyst developed for the one-pot hydrogenolysis of glycerol in a water media with high conversion of glycerol (90.1%) and high selectivity to 1-PO (92.9%) at 240oC and 580PSI hydrogen using a Hastelloy batch reactor. The activation energy Ea of this reaction is 124.1kJ/mol. Reaction pathways for the hydrogenolysis of glycerol using a bifunctional catalyst 10Ni/30HSiW/Al2O3 is proposed. It is believed that acidity plays an important role for the dehydration and Ni plays an important role for the hydrogenation. It is suggested that with acidic catalysts, the main route for the formation of 1-PO from glycerol is via either the hydrogenation of acrolein or further hydrogenolysis of 1,2-PD (and 1,3PD) where 1,2-PD (and 1,3-PD) and acrolein are the intermediate species in the formation of 1-PO from glycerol. The formation of 1,2-PD and 1,3-PD takes place through an initial dehydration of the primary or secondary hydroxyl groups on glycerol to give acetol or 3- hydroxylpropanaldehyde (3-HPA). The hydrogen activated on the metal facilitates the hydrogenation of acetol or 3-HPA to release 1,2-PD or 1,3-PD respectively. However, dehydration of 3-HPA on the acid sites forms acrolein. Further hydrogenolysis of diols or hydrogenation of acrolein produces 1-PO. 1,3-PD that is a very high value-added chemical can also be obtained from hydrogenolysis of glycerol using a Ni-HSiW supported catalyst. To improve the selectivity of 1,3-PD it is suggested that the catalyst should have high hydrogenation activity for the intermediate 3-HPA. The equilibrium between acrolein and 3-HPA in the hydration-dehydration step is important, so it is essential to tune the bi-functional catalyst and the conditions of the reaction to form 1,3-PD from 3-HPA. A study of promoter effects for the activity of catalyst to form 1,3-PD is recommended.
Book Synopsis Sustainable Hydrogen Production Via Glycerol Steam Reforming with and Without In-situ CO2 Removal by : Marziehossadat Shokrollahi Yancheshmeh
Download or read book Sustainable Hydrogen Production Via Glycerol Steam Reforming with and Without In-situ CO2 Removal written by Marziehossadat Shokrollahi Yancheshmeh and published by . This book was released on 2019 with total page 251 pages. Available in PDF, EPUB and Kindle. Book excerpt: Over the past few decades, hydrogen has attracted a great deal of attention as a green energy carrier. Currently, more than 95 % of hydrogen is produced from fossil fuels, which has been questioned by the depletion of resources andincrease of greenhouse gas emissions. Therefore, renewable, carbon-neutral resources such as biomass and biomass-derived chemicals has been receiving a growing interest as an option to produce hydrogen. As a main by product in the biodiesel manufacturing process, glycerol has emerged as a promising source for hydrogen production. Although steam reforming (SR) is being recognized as a promising approach for converting glycerol to hydrogen, this process faces a number of challenges including the presence of equilibrium-limited reactions and the need of an expensive downstream purification system. To alleviate these problems, a promising alternative is sorption enhanced steam reforming (SESR) process, in which steam reforming, water gas shift (WGS), and CO2 capture reactions occur simultaneously using areforming catalyst and a CO2solid sorbent. In this process, CO2 removal occurs simultaneously with the reforming reaction, shifting the WGS reaction towards hydrogen production and producing a hydrogen-enriched gas stream in a single step. The key factors in the successful application of this technology are mainly: (i) reforming catalysts and CO2 sorbents that can work efficiently under the harsh conditions of SESR process and (ii) mixing pattern of catalyst and sorbent. This thesis focuses on the development of efficient catalyst and catalyst-sorbent bifunctional materials for sustainable hydrogen production by SR and SESR of glycerol (SRG and SESRG). More specifically, four main objectives of our workare: (i) investigating the influence of steam addition during either carbonation or calcination on the CO2 capture performance of Ca9Al6O18-CaO sorbent, (ii) developing Ca9Al6O18−CaO/xNiO (x = 15, 20, and 25 wt.%) and Ca9Al6O18−CaO/20NiO−yCeO2(y = 5, 10, and 15 wt %) catalyst-sorbent bifunctional materials and studying the influence of CeO2 on the material stability incyclic SESRG/regeneration operation, (iii) proposing a new method for the synthesis of a more readily reducible NiAl2O4 spinel and studying the influence of CeO2 addition on its catalytic performance, and (iv) novel synthesis of two Ni-CaO-based catalyst-sorbent bifunctional materials with highlyuniform distribution of catalytic active sites. (i) CO2 capture performance of Ca9Al6O18-CaO sorbent was investigated in the presence of two concentrations of steam, 2.3 and 9.5 vol. %.The obtained results revealed that the sorbent reactivity was remarkably enhanced for both concentrations of steam injected during carbonation step. In the case of steam addition during calcination, the CO2 capture performance was influenced negatively or positively depending on the concentration of steam. For 2.3 vol.% steam, the sorbent reactivity was worsened, while the presence of 9.5 vol.% steam led to an increase in the CO2capture capacity during 9 initial cycles.(ii) Two series of catalyst-sorbent bifunctional materials were developed for the sustainable production of high-purity hydrogen by SESRG. Using Ca9Al6O18−CaO/xNiO (x = 15,20, and 25 wt.%) materials during five SESRG/regeneration cycles revealed that their reactivity was rapidly deteriorated mainly due to CaO sintering and coke deposition. As a result, the pre-breakthrough time and hydrogen yield decreased notably over five cycles. Interestingly, the addition of CeO2 to the most efficient catalyst (Ca9Al6O18−CaO/20NiO) led to a significant enhancement in material stability during cyclic operation. The bifunctional material promoted with 10 wt.% of CeO2 demonstrated the best performance, with a stable H2purity of ∼98% and H2yield of ∼91% over 20SESRG/regeneration cycles. (iii) A novel method, involving one-or two-step calcination of Ni-Al mixed-metal alkoxide((Ni-Al)-Glycerate), was developed for the synthesis of NiAl2O4 spinel. For comparison purposes, the NiAl2O4 spinel was also synthesized throughthe conventional co-precipitation method followed by two-step calcination technique. The characterization results revealed that the synthesis of NiAl2O4 spinel through two-step calcination of (Ni-Al)-Glycerateresulted in the formation of a more easily reducible catalyst and a more developed porous structure. This sample showed the highest H2yield (76.38 %) and glycerol conversion into gaseous products (95.42 %) when compared to other two samples. In order to avoid or reduce coke formation, 10 wt.% of CeO2 was incorporated into the sample prepared by two-step calcination of (Ni-Al)-Glycerate. The thermogravimetric analysis of the CeO2-promoted catalyst after SRG reaction revealed that the coke formation was almost completely suppressed. The method developed for the synthesis of NiAl2O4 spinel in the previous work was combined with the ethanol/water treatment of CaO-based sorbents to synthesistwo new NiCaO-based catalyst-sorbent bifunctional materials for hydrogen production via SESRG. Cyclic SESRG/regeneration experiments showed that the Ca3Al2O6-CaO/NiO-CeO2 bifunctional material possessed higher activity and stability when compared to NiAl2O4-CaO/NiAl2O4-CeO2. The former one exhibited a high constant H2 purity of around 96% over 10 cycles, while the latter showed a H2 purity of approximately 90% over the first 6 cycles, followed by the further decrease to 86 % over the last 4 cycles. In conclusion, the results presented in this thesis show that SESRG can be a very promising approach for high-purity hydrogen production in a single step, providing that the employed catalyst-sorbent bifunctional materials possess uniform distribution of catalytic and sorption active sites on nanoscale and high resistance against CaO sintering and coke formation. To prepare catalyst-sorbent bifunctional materials with these characteristics, two main approaches were employed in this work: (i) developing new synthesis methods that provide a homogeneous distribution of targeted elements (Ca, Ni, Al, and Ce in this study) and (ii) using CeO2 as a promising promoter to reduce or suppress coke formation and enhance the cyclic stability of CaO particles.
Book Synopsis Biodiesel Science and Technology by : Jan C.J. Bart
Download or read book Biodiesel Science and Technology written by Jan C.J. Bart and published by Elsevier. This book was released on 2010-02-19 with total page 859 pages. Available in PDF, EPUB and Kindle. Book excerpt: Biodiesel production is a rapidly advancing field worldwide, with biodiesel fuel increasingly being used in compression ignition (diesel) engines. Biodiesel has been extensively studied and utilised in developed countries, and it is increasingly being introduced in developing countries, especially in regions with high potential for sustainable biodiesel production. Initial sections systematically review feedstock resources and vegetable oil formulations, including the economics of vegetable oil conversion to diesel fuel, with additional coverage of emerging energy crops for biodiesel production. Further sections review the transesterification process, including chemical (catalysis) and biochemical (biocatalysis) processes, with extended coverage of industrial process technology and control methods, and standards for biodiesel fuel quality assurance. Final chapters cover the sustainability, performance and environmental issues of biodiesel production, as well as routes to improve glycerol by-product usage and the development of next-generation products. Biodiesel science and technology: From soil to oil provides a comprehensive reference to fuel engineers, researchers and academics on the technological developments involved in improving biodiesel quality and production capacity that are crucial to the future of the industry. Evaluates biodiesel as a renewable energy source and documents global biodiesel development The outlook for biodiesel science and technology is presented exploring the challenges faced by the global diesel industry Reviews feedstock resources and vegetable oil formation including emerging crops and the agronomic potential of underexploited oil crops
Book Synopsis Sustainable Catalysis for Biorefineries by : Francesco Frusteri
Download or read book Sustainable Catalysis for Biorefineries written by Francesco Frusteri and published by Royal Society of Chemistry. This book was released on 2018-07-04 with total page 386 pages. Available in PDF, EPUB and Kindle. Book excerpt: Biorefineries are becoming increasingly important in providing sustainable routes for chemical industry processes. The establishment of bio-economic models, based on biorefineries for the creation of innovative products with high added value, such as biochemicals and bioplastics, allows the development of “green chemistry” methods in synergy with traditional chemistry. This reduces the heavy dependence on imports and assists the development of economically and environmentally sustainable production processes, that accommodate the huge investments, research and innovation efforts. This book explores the most effective or promising catalytic processes for the conversion of biobased components into high added value products, as platform chemicals and intermediates. With a focus on heterogeneous catalysis, this book is ideal for researchers working in catalysis and in green chemistry.
Book Synopsis Guaiacol Hydrogenation with In-situ Generated Hydrogen Through Aqueous Phase Glycerol Reforming by : Ziyin Chen
Download or read book Guaiacol Hydrogenation with In-situ Generated Hydrogen Through Aqueous Phase Glycerol Reforming written by Ziyin Chen and published by . This book was released on 2020 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:
Book Synopsis Synthesis, Characterization and Reactivity of Bimetallic PtRe Catalysts for Hydrogenolysis of Glycerol to Propanediols by : Oliver Mills Daniel
Download or read book Synthesis, Characterization and Reactivity of Bimetallic PtRe Catalysts for Hydrogenolysis of Glycerol to Propanediols written by Oliver Mills Daniel and published by . This book was released on 2010 with total page 116 pages. Available in PDF, EPUB and Kindle. Book excerpt:
Book Synopsis The Hydrogenation of Oils by : Carleton Ellis
Download or read book The Hydrogenation of Oils written by Carleton Ellis and published by . This book was released on 1915 with total page 340 pages. Available in PDF, EPUB and Kindle. Book excerpt:
Book Synopsis Development of Novel Pt-Ni-based G-alumina Catalysts for Hydrogen Production by Catalytic Reforming of Bioethanol-bioglycerol by :
Download or read book Development of Novel Pt-Ni-based G-alumina Catalysts for Hydrogen Production by Catalytic Reforming of Bioethanol-bioglycerol written by and published by . This book was released on 2012 with total page 249 pages. Available in PDF, EPUB and Kindle. Book excerpt:
Book Synopsis Hydrogenolysis of Glycerol by : Guanhua Liu
Download or read book Hydrogenolysis of Glycerol written by Guanhua Liu and published by . This book was released on 2010 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt: The purpose of this research was to achieved selective hydrogenolysis of glycerol to 1,2-PDO (1,2-propanediol). Hydrogenolysis of glycerol was investigated in batch and trickle flow fixed bed continuous reactors. Raney catalysts and carbon supported precious catalysts were tested in the batch reactor. Ru/C and oxide-supported catalysts were tested in a continuous reactor. Parametric studies were performed and kinetics parameters were estimated with Raney copper catalyst in a batch reactor and with Cu/Al2O3 in a continuous reactor. The network of glycerol hydrogenolysis was studied on Cu/Al2O3. Cu/Al2O3 was investigated in the continuous reactor. Preparation methods, Cu loading and Cu catalyst support effects were studied. Catalyst characterization was performed to find out the factors that affected catalyst performance. Cu/Al2O3 catalyst was further modified by adding small amounts of Co and Ni to enhance the activity. The factors that affect the catalyst deactivation were also investigated. Raney Cu in the batch reactor and Cu/Al2O3 in the continuous reactor were the catalysts most selective to 1,2-PDO for glycerol hydrogenolysis. Cu catalyst on Al2O3 support of 18 wt % Cu loading prepared by co-precipitation method with ammonia is the most efficient catalyst for glycerol hydrogenolysis to 1,2-PDO. Catalyst characterization shows that the Cu/Al2O3 activity is related to the active Cu surface area on alumina support and the selectivity to 1,2-PDO is constant for the Cu/Al2O3 with different Cu surface area. Small amounts of Ni or Co improve the Cu/Al2O3 activity. The most effective deactivation factor for Cu/Al2O3 is coking or oxygenates on the spent catalyst.
Book Synopsis Advanced Inorganic Fluorides: Synthesis, Characterization and Applications by : T. Nakajima
Download or read book Advanced Inorganic Fluorides: Synthesis, Characterization and Applications written by T. Nakajima and published by Elsevier. This book was released on 2000-05-12 with total page 715 pages. Available in PDF, EPUB and Kindle. Book excerpt: This book summarizes recent progresses in inorganic fluorine chemistry. Highlights include new aspects of inorganic fluorine chemistry, such as new synthetic methods, structures of new fluorides and oxide fluorides, their physical and chemical properties, fluoride catalysts, surface modifications of inorganic materials by fluorination process, new energy conversion materials and industrial applications. Fluorine has quite unique properties (highest electronegativity; very small polarizability). In fact, fluorine is so reactive that it forms fluorides with all elements except with the lightest noble gases helium, neon and argon. Originally, due to its high reactivity, fluoride chemistry faced many technical difficulties and remained undeveloped for many years. Now, however, a large number of fluorine-containing materials are currently produced for practical uses on an industrial scale and their applications are rapidly extending to many fields. Syntheses and structure analyses of thermodynamically unstable high-oxidation-state fluorides have greatly contributed to inorganic chemistry in this decade. Fluoride catalysts and surface modifications using fluorine are developing a new field of fluorine chemistry and will enable new syntheses of various compounds. The research on inorganic fluorides is now contributing to many chemical energy conversion processes such as lithium batteries. Furthermore, new theoretical approaches to determining the electronic structures of fluorine compounds are also progressing. On the industrial front, the use of inorganic fluorine compounds is constantly increasing, for example, in semi-conductor industry. "Advanced Inorganic Fluorides: Synthesis, Characterization and Applications" focuses on these new features in inorganic fluorine chemistry and its industrial applications. The authors are outstanding experts in their fields, and the contents of the book should prove to be of valuable assistance to all chemists, graduates, students and researchers in the field of fluorine chemistry.
Book Synopsis Chemoselective Catalytic Hydrogenolysis of Glycerol Into 1,2-Propanediol Over Supported Ruthenium Catalysts by : Tendai Terence Manjoro
Download or read book Chemoselective Catalytic Hydrogenolysis of Glycerol Into 1,2-Propanediol Over Supported Ruthenium Catalysts written by Tendai Terence Manjoro and published by . This book was released on 2017 with total page 274 pages. Available in PDF, EPUB and Kindle. Book excerpt: Discusses the project at hand, as a part of a technology package for biodiesel, aimed at catalytically converting the crude glycerol into value added chemicals that can be sold as raw materials or intermediates to other chemical industries, thereby significantly improving the profitability of the overall process and thus recouping some of the capital used in the biodiesel production. The main objectives of the project were: 1. To propose suitable heterogeneous catalyst which would transform the glycerol obtained from a biodiesel production system to value-added products mainly 1,2 Propane diol. 2. For this purpose ruthenium catalysts supported on zirconium oxide, aluminium oxide and silicon oxide were synthesized and tested in the conversion of glycerol. This was followed by evaluating the catalyst with the most promising catalytic properties amongst those tested. 3. To determine the optimum operating (temperature, pressure and catalysts weight) parameters of the best catalyst based on the conversion yield and the quality of the products.
Download or read book Coal Science written by Martin L. Gorbaty and published by Academic Press. This book was released on 2013-10-22 with total page 365 pages. Available in PDF, EPUB and Kindle. Book excerpt: Coal Science, Volume 3 presents and evaluates selected fundamental scientific areas on coal structure, reactivity, and utilization. This book describes the organic geochemistry of coal, role of oxygen functionality in coal and coal liquids reactivity, chemistry of hydrocarbon syntheses from carbon monoxide and hydrogen, and chemistry of coal in carbon monoxide/water systems. Other topics discussed include intermediates and mechanisms of the FTS of hydrocarbons; synthesis of oxygenates; and structural features of vitrinite macerals. The molecular weight determination for coal derivatives; thermal reactions of oxygen compounds; and alternative methods for removing oxygen compounds from coal-derived liquids are also elaborated. This publication likewise covers the aqueous coal conversions and conversion mechanism. This volume serves as a valuable source of information and guide to scientists and researchers interested in the coal literature.
Book Synopsis Metal Oxide Catalysis, 2 Volume Set by : S. David Jackson
Download or read book Metal Oxide Catalysis, 2 Volume Set written by S. David Jackson and published by John Wiley & Sons. This book was released on 2008-11-24 with total page 916 pages. Available in PDF, EPUB and Kindle. Book excerpt: With its two-volume structure, this handbook and ready reference allows for comprehensive coverage of both characterization and applications, while uniform editing throughout ensures that the structure remains consistent. The result is an up-to-date review of metal oxides in catalysis. The first volume covers a range of techniques that are used to characterize oxides, with each chapter written by an expert in the field. Volume 2 goes on to cover the use of metal oxides in catalytic reactions. For all chemists and engineers working in the field of heterogeneous catalysis.
Book Synopsis The Future of Glycerol by : Mario Pagliaro
Download or read book The Future of Glycerol written by Mario Pagliaro and published by Royal Society of Chemistry. This book was released on 2008 with total page 145 pages. Available in PDF, EPUB and Kindle. Book excerpt: By-products of global biodiesel manufacturing are a modern day global fact responsible for igniting a number of year's worldwide intense research activity into human chemical ingenuity. This highly anticipated 2nd Edition depicts how practical limitations posed by glycerol chemistry are solved based on the understanding of the fundamental chemistry of glycerol and by application of catalysis science and technology. The authors report and comment on employable, practical avenues applicable to convert glycerol into value added products of mass consumption. The best-selling reference book in the.
Book Synopsis Lignin Valorization by : Gregg T. Beckham
Download or read book Lignin Valorization written by Gregg T. Beckham and published by Royal Society of Chemistry. This book was released on 2018-03-29 with total page 544 pages. Available in PDF, EPUB and Kindle. Book excerpt: "Chapters will specifically focus on the production of fuels and chemicals from lignin."--Page [4] of cover.
