“…6 Apart from its utilization in fuel cells, hydrogen has a wide range of industrial importance due to its application as a feedstock in the synthesis of ammonia, methanol, and other high-value chemicals. 7,8 Currently, the majority of commercial H 2 is produced via conventional steam methane reforming (SMR), owing to the plentiful methane reserves in the earth's crust, while nonconventional methods such as solar water splitting and photobiological routes are still in their early stages of development. 9,10 However, SMR approximately accounts for 830 million tonnes of CO x emissions annually, making a serious contribution to global warming.…”
Section: Introductionmentioning
confidence: 99%
“…The rapid depletion of the accessible deposits of fossil fuels which contribute to the majority of the current energy sources and their effect on climate change have increasingly prompted research and development for environmentally friendly and sustainable alternate energy resources. , Hydrogen is regarded as a versatile, environmentally friendly, and clean energy carrier (heating value = 142 MJ/kg), which upon combustion releases only heat and water. − Having three times the energy storage capacity (per unit weight) of other liquid fuels, hydrogen has the potential to completely replace fossil fuels in the future . Apart from its utilization in fuel cells, hydrogen has a wide range of industrial importance due to its application as a feedstock in the synthesis of ammonia, methanol, and other high-value chemicals. , Currently, the majority of commercial H 2 is produced via conventional steam methane reforming (SMR), owing to the plentiful methane reserves in the earth’s crust, while nonconventional methods such as solar water splitting and photobiological routes are still in their early stages of development. , However, SMR approximately accounts for 830 million tonnes of CO x emissions annually, making a serious contribution to global warming. The reaction is also highly endothermic, commercially operated in the temperature range of 900–1000 °C, for breaking the strong C–H bonds of methane (bond energy = 415 kJ/mol). , The product is a mixture of CO x and hydrogen that demands further high- and low-temperature shift reactors to convert CO to CO 2 followed by separation and purification, rendering a high cost of manufacturing.…”
As a pathway to green hydrogen, the catalytic dehydrogenation of methane is an economical and CO x -free alternative to produce sufficient volumes of hydrogen to address energy sustainability. This work attempts to develop a catalyst to enhance conversion, stability, and favorable carbon nanostructures. Monometallic Fe catalysts were synthesized on a mesoporous carbon template to identify the best catalyst synthesis methodology covering incipient wetness, hydrothermal, and wet impregnation methods. As a logical step to enhance the conversion, stability, and ease of separation of the catalyst from the product carbon, a bimetallic Fe−Mo was synthesized on the same mesoporous carbon template for the first time, using the hydrothermal method, by varying the Mo loading from 2.5 to 15%. The optimal catalyst design had a composition of 30%Fe−5%Mo with a specific surface area of 606.9 g/m 2 , offering the highest conversion and stability, at a temperature of 950 °C. The highest conversion corresponded to the lowest space velocity, highest reaction temperature, and highest CH 4 concentration, with a maximum conversion of 90% and being stable until the end of 2 h of reaction time. X-ray diffraction analysis revealed the presence of Fe 2 O 3 and mixed oxides, Fe 2 (MoO 4 ) 3 and FeMoO 4 in the bimetallic catalyst. The initial H 2 yield was ∼61%, and it decreased during the reaction, reaching 48% after 4 h of reaction. Various structural, textural, and morphological characterizations of the catalyst pre-and postreaction were performed using advanced analytical techniques. Graphitic carbon, an Fe−Mo alloy, and FeMoO 4 phases were observed by XRD patterns of the spent catalyst. Carbon depositions with varying morphologies were observed under different reaction conditions ranging from carbon nanoparticles and carbon nanotubes to agglomerates of nanoparticles and nanoflowers. A well-defined network of carbon nanoflowers along with bamboo-shaped carbon nanotubes could be observed over the surface of the best catalyst under the optimized reaction conditions.
“…6 Apart from its utilization in fuel cells, hydrogen has a wide range of industrial importance due to its application as a feedstock in the synthesis of ammonia, methanol, and other high-value chemicals. 7,8 Currently, the majority of commercial H 2 is produced via conventional steam methane reforming (SMR), owing to the plentiful methane reserves in the earth's crust, while nonconventional methods such as solar water splitting and photobiological routes are still in their early stages of development. 9,10 However, SMR approximately accounts for 830 million tonnes of CO x emissions annually, making a serious contribution to global warming.…”
Section: Introductionmentioning
confidence: 99%
“…The rapid depletion of the accessible deposits of fossil fuels which contribute to the majority of the current energy sources and their effect on climate change have increasingly prompted research and development for environmentally friendly and sustainable alternate energy resources. , Hydrogen is regarded as a versatile, environmentally friendly, and clean energy carrier (heating value = 142 MJ/kg), which upon combustion releases only heat and water. − Having three times the energy storage capacity (per unit weight) of other liquid fuels, hydrogen has the potential to completely replace fossil fuels in the future . Apart from its utilization in fuel cells, hydrogen has a wide range of industrial importance due to its application as a feedstock in the synthesis of ammonia, methanol, and other high-value chemicals. , Currently, the majority of commercial H 2 is produced via conventional steam methane reforming (SMR), owing to the plentiful methane reserves in the earth’s crust, while nonconventional methods such as solar water splitting and photobiological routes are still in their early stages of development. , However, SMR approximately accounts for 830 million tonnes of CO x emissions annually, making a serious contribution to global warming. The reaction is also highly endothermic, commercially operated in the temperature range of 900–1000 °C, for breaking the strong C–H bonds of methane (bond energy = 415 kJ/mol). , The product is a mixture of CO x and hydrogen that demands further high- and low-temperature shift reactors to convert CO to CO 2 followed by separation and purification, rendering a high cost of manufacturing.…”
As a pathway to green hydrogen, the catalytic dehydrogenation of methane is an economical and CO x -free alternative to produce sufficient volumes of hydrogen to address energy sustainability. This work attempts to develop a catalyst to enhance conversion, stability, and favorable carbon nanostructures. Monometallic Fe catalysts were synthesized on a mesoporous carbon template to identify the best catalyst synthesis methodology covering incipient wetness, hydrothermal, and wet impregnation methods. As a logical step to enhance the conversion, stability, and ease of separation of the catalyst from the product carbon, a bimetallic Fe−Mo was synthesized on the same mesoporous carbon template for the first time, using the hydrothermal method, by varying the Mo loading from 2.5 to 15%. The optimal catalyst design had a composition of 30%Fe−5%Mo with a specific surface area of 606.9 g/m 2 , offering the highest conversion and stability, at a temperature of 950 °C. The highest conversion corresponded to the lowest space velocity, highest reaction temperature, and highest CH 4 concentration, with a maximum conversion of 90% and being stable until the end of 2 h of reaction time. X-ray diffraction analysis revealed the presence of Fe 2 O 3 and mixed oxides, Fe 2 (MoO 4 ) 3 and FeMoO 4 in the bimetallic catalyst. The initial H 2 yield was ∼61%, and it decreased during the reaction, reaching 48% after 4 h of reaction. Various structural, textural, and morphological characterizations of the catalyst pre-and postreaction were performed using advanced analytical techniques. Graphitic carbon, an Fe−Mo alloy, and FeMoO 4 phases were observed by XRD patterns of the spent catalyst. Carbon depositions with varying morphologies were observed under different reaction conditions ranging from carbon nanoparticles and carbon nanotubes to agglomerates of nanoparticles and nanoflowers. A well-defined network of carbon nanoflowers along with bamboo-shaped carbon nanotubes could be observed over the surface of the best catalyst under the optimized reaction conditions.
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