Understanding hydrogen redistribution and
designing a new hydrogen extraction method.
Presentation at 3rd UK-China Steel Research Forum
Rutherford Appleton Laboratory (UK)
10-11 July 2014
The document describes an efficient new process for removing hydrogen sulfide from gas mixtures using a dielectric barrier discharge plasma. A plasma device was constructed with a reservoir to hold sorbent powder within the plasma region. Plasma treatment of gas streams with high hydrogen sulfide concentrations in air removed over 98% of the hydrogen sulfide and deposited sulfur on the dielectric surface, while generating small amounts of sulfur dioxide. The presence of calcium carbonate powder in the plasma region resulted in over 99% removal of hydrogen sulfide and 98% removal of initial sulfur dioxide impurities from the gas mixture.
Slides of an invited talk, given at EuroCVD in 2007
R. L. Puurunen, Understanding the surface chemistry of atomic layer deposition: achievements and challenges, Sixteenth European Conference on Chemical Vapor Deposition, EuroCVD-16. Den Haag, The Netherlands, 16 - 21 Sept. 2007. Book of Extended Abstracts. Klein, C.R. (Ed.). Delft University of Technology (2007), 11. Invited talk.
Doran and Zander 2005 - An improved method for measuring soil microbial activ...Alek Zander
This document describes an improved method for measuring soil microbial activity by analyzing carbon dioxide (CO2) production using gas phase flow injection analysis (GPFIA). The traditional method involves trapping CO2 in an alkali solution and then determining concentration indirectly by titration, which is time-consuming and operator-dependent. The new GPFIA method allows CO2 trapped in alkali to be released into a sampling chamber and collected in a syringe for injection into the GPFIA system. A comparison of GPFIA and titration results found no significant difference, but GPFIA uses only a tenth of the sample volume and does not require expensive equipment. The GPFIA method was validated and then applied to analyze CO2
This document summarizes a dissertation submitted by Nur Fatin Dariah binti Mohamad Daud in partial fulfillment of the requirements for a Bachelor of Engineering (Hons) in Chemical Engineering at Universiti Teknologi PETRONAS in September 2015. The dissertation investigates the aqueous phase reforming of sorbitol over supported Ni/Alumina catalysts promoted with calcium. Various characterization techniques such as TGA, SEM, and H2-TPR were used to analyze the catalysts. The catalytic activity tests were carried out in a batch reactor to identify the value-added chemicals produced from sorbitol, which were analyzed using GCMS and HPLC. The addition of the cheap promoter calcium was studied
This document discusses combustion synthesized cobalt catalysts for converting syngas to liquid fuels via the Fischer-Tropsch reaction. It provides an introduction to the motivation and need for biomass to liquid fuel processes. It then reviews relevant literature on the Fischer-Tropsch process, catalysts used, and reactor types. The literature review establishes the desired properties for an effective Fischer-Tropsch catalyst and how synthesis parameters like metal loading, crystallite size, and degree of reduction impact activity and selectivity.
Enhanced fluidized bed methanation over a Ni Al2O3 catalyst for production of...Pengcheng Li
This document summarizes a study that investigated the fluidization behavior and CO methanation performance of a Ni/Al2O3 catalyst in a fluidized bed reactor for producing synthetic natural gas. The researchers found that the pure Ni/Al2O3 catalyst failed to properly fluidize on its own due to particle sizes between 10 and 100 μm, but fluidization was improved by adding larger Al2O3 particles. Methanation performance in the fluidized bed reactor increased substantially with the Al2O3 addition. Temperature was found to control the methanation reaction mechanism, with surface reactions dominating at lower temperatures and external diffusion controlling at higher temperatures. Stability tests showed the fluidized bed reactor had higher CO conversion, methane selectivity
This document provides a summary of Zhao Zhang's contact information, work experience, education, skills, and publications. Zhang has over 10 years of experience in CFD simulation working on projects related to chemical reactors, heat exchangers, furnaces, and separation devices. He has a Ph.D. in Chemical Engineering from Beijing University of Chemical Technology and is currently a researcher at Beijing Shenwu Environment & Energy Technology Co., Ltd. where he performs CFD simulations of chemical reactors. Zhang has published several papers in international journals on simulations of reactors for methane oxidation.
Presentation given by Mischa Werner of ETH Zurich on "Research on the direct mineralization of flue gas CO2 at ETH Zurich" at the Alternative CCS Pathways Workshop, Oxford Martin School, 27 June 2014
The document describes an efficient new process for removing hydrogen sulfide from gas mixtures using a dielectric barrier discharge plasma. A plasma device was constructed with a reservoir to hold sorbent powder within the plasma region. Plasma treatment of gas streams with high hydrogen sulfide concentrations in air removed over 98% of the hydrogen sulfide and deposited sulfur on the dielectric surface, while generating small amounts of sulfur dioxide. The presence of calcium carbonate powder in the plasma region resulted in over 99% removal of hydrogen sulfide and 98% removal of initial sulfur dioxide impurities from the gas mixture.
Slides of an invited talk, given at EuroCVD in 2007
R. L. Puurunen, Understanding the surface chemistry of atomic layer deposition: achievements and challenges, Sixteenth European Conference on Chemical Vapor Deposition, EuroCVD-16. Den Haag, The Netherlands, 16 - 21 Sept. 2007. Book of Extended Abstracts. Klein, C.R. (Ed.). Delft University of Technology (2007), 11. Invited talk.
Doran and Zander 2005 - An improved method for measuring soil microbial activ...Alek Zander
This document describes an improved method for measuring soil microbial activity by analyzing carbon dioxide (CO2) production using gas phase flow injection analysis (GPFIA). The traditional method involves trapping CO2 in an alkali solution and then determining concentration indirectly by titration, which is time-consuming and operator-dependent. The new GPFIA method allows CO2 trapped in alkali to be released into a sampling chamber and collected in a syringe for injection into the GPFIA system. A comparison of GPFIA and titration results found no significant difference, but GPFIA uses only a tenth of the sample volume and does not require expensive equipment. The GPFIA method was validated and then applied to analyze CO2
This document summarizes a dissertation submitted by Nur Fatin Dariah binti Mohamad Daud in partial fulfillment of the requirements for a Bachelor of Engineering (Hons) in Chemical Engineering at Universiti Teknologi PETRONAS in September 2015. The dissertation investigates the aqueous phase reforming of sorbitol over supported Ni/Alumina catalysts promoted with calcium. Various characterization techniques such as TGA, SEM, and H2-TPR were used to analyze the catalysts. The catalytic activity tests were carried out in a batch reactor to identify the value-added chemicals produced from sorbitol, which were analyzed using GCMS and HPLC. The addition of the cheap promoter calcium was studied
This document discusses combustion synthesized cobalt catalysts for converting syngas to liquid fuels via the Fischer-Tropsch reaction. It provides an introduction to the motivation and need for biomass to liquid fuel processes. It then reviews relevant literature on the Fischer-Tropsch process, catalysts used, and reactor types. The literature review establishes the desired properties for an effective Fischer-Tropsch catalyst and how synthesis parameters like metal loading, crystallite size, and degree of reduction impact activity and selectivity.
Enhanced fluidized bed methanation over a Ni Al2O3 catalyst for production of...Pengcheng Li
This document summarizes a study that investigated the fluidization behavior and CO methanation performance of a Ni/Al2O3 catalyst in a fluidized bed reactor for producing synthetic natural gas. The researchers found that the pure Ni/Al2O3 catalyst failed to properly fluidize on its own due to particle sizes between 10 and 100 μm, but fluidization was improved by adding larger Al2O3 particles. Methanation performance in the fluidized bed reactor increased substantially with the Al2O3 addition. Temperature was found to control the methanation reaction mechanism, with surface reactions dominating at lower temperatures and external diffusion controlling at higher temperatures. Stability tests showed the fluidized bed reactor had higher CO conversion, methane selectivity
This document provides a summary of Zhao Zhang's contact information, work experience, education, skills, and publications. Zhang has over 10 years of experience in CFD simulation working on projects related to chemical reactors, heat exchangers, furnaces, and separation devices. He has a Ph.D. in Chemical Engineering from Beijing University of Chemical Technology and is currently a researcher at Beijing Shenwu Environment & Energy Technology Co., Ltd. where he performs CFD simulations of chemical reactors. Zhang has published several papers in international journals on simulations of reactors for methane oxidation.
Presentation given by Mischa Werner of ETH Zurich on "Research on the direct mineralization of flue gas CO2 at ETH Zurich" at the Alternative CCS Pathways Workshop, Oxford Martin School, 27 June 2014
Absorption of CO2 gas from CO
2/Air mixture into aqueous sodium hydroxide solution has been
achieved using packed column in pilot scale at constant temperature (T) of 25±1℃.The aim of the present work
was to improve the Absorption rate of this process, to find the optimal operation conditions, and to contribute to
the using of this process in the chemical industry. Absorption rate (RA) was measured by using different
operating parameters: gas mixture flow rate (G) of 360 -540 m3/h, carbon dioxide inlet concentration (CCO
2) of
0.1-0.5 vol. %, NaOH solution concentration (CNaOH) of 1-2 M, and liquid holdup in the column (VL) of 0.022-0.028 m3 according to experimental design. The measured RA was in the range of RA = 3.235 – 22.340 k-mol/h.
Computer program (Statgraphics/Experimental Design) was used to estimate the fitted linear model of RA in
terms of (G, CCO2, CNaOH, and VL), and the economic aspects of the process. R -squared of RA model was
91.7659 percent, while the standard error of the estimate shows the standard deviation of the residuals to be
1.7619. The linear model of RA was adequate, the operating parameters were significant except the liquid holdup
was not significant, and the interactions were negligible.
1. This test report provides results for levels of lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers in a sample submitted for testing.
2. Testing found that the levels of lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers were all below their respective method detection limits.
3. The sample was tested according to various IEC test methods to determine the contents of the regulated substances.
This document describes the development of a novel Pt-Ru bimetallic nanoparticle catalyst supported on a wiregauze for use in passive autocatalytic recombiners to mitigate hydrogen accumulation during loss of coolant accidents in nuclear reactors. The catalyst is prepared via an electroless deposition method and exhibits high catalytic activity for hydrogen-oxygen recombination even in the presence of contaminants like CO2, CH4 and moisture, and shows enhanced activity in the presence of 400 ppm CO. Testing demonstrates the catalyst initiates recombination at room temperature and remains effective after multiple tests, making it suitable for use in nuclear power plant safety systems.
Computational Analysis of CuO Nano Coolant in a Car RadiatorIOSRJMCE
Nanofluids are basically nanoparticles in base fluids. Nanofluids have unique features different from conventional solid-liquid mixtures in which nano sized particles of metals and nonmetals are dispersed. Due to improvement of mechanical properties, nanofluids are widely used in heat transfer industries. The coolant is used water-based, with the addition of glycols to prevent freezing and other additives to limit corrosion, erosion and cavitations. In this study 50-50 mixture of Ethylene Glycol with water (EGW) is tested and compared with another mixture by adding 2 percent Copper oxide (CuO). The geometric model of radiator is uploaded in Autodesk CFD software for its computational analysis. It is analyzed up to 100 iterations. Both the results are compared to find the improved heat transfer rate due to the addition of 2% CuO with Ethylene Glycol and water
The document discusses aqueous phase reforming of sorbitol to produce value-added chemicals. It describes background studies on sorbitol and its potential for hydrogen production. The objectives are to identify value-added chemicals produced from reforming sorbitol over a Ni/Al2O3 catalyst promoted with Ca, and to synthesize and characterize the catalyst. The methodology involves preparing the catalyst using incipient wetness impregnation, characterizing it using TGA, SEM, and H2-TPR, and evaluating its performance in reforming sorbitol to identify products.
MANUFACTURE OF CHLORINE - CAUSTIC SODA USING ELECTROLYSIS PROCESS (MEMBRANE C...Ankush Gupta
This document summarizes the process of manufacturing chlorine and caustic soda using electrolysis. It includes:
- A process flow diagram of the membrane cell process used to separate NaCl into NaOH, H2, and Cl2 via electrolysis.
- Material and energy balances calculations for each unit operation including the membrane cell, evaporator, and dryer. These calculate chemical reactions, flows, heating needs and efficiencies.
- The process achieves 70.28% conversion of NaCl and 27.37% yield of NaOH from the reacted NaCl. Waste streams and energy requirements are also quantified.
Effective Adsorbents for Establishing Solids Looping as a Next Generation NG PCC Technology, Hao Liu, University of Nottingham - UKCCSRC Strathclyde Biannual 8-9 September 2015
The most difficult goal in the next few decades is the replacement of conventional petro-based fuels with more sustainable fuels that can be used in the existing infrastructure. By the use of Renewable energy or nuclear energy, CO2 and H2O can be recycled into liquid hydrocarbon fuels (the reverse of fuel combustion). Capture of CO2 from the atmosphere will form a close carbon-neutral fuel cycle loop. This article also reviews the aspects regarding thermodynamics involved, involved mechanisms and possible technological pathways for recycling CO2 into fuels using renewable energy. These pathways can be broken into three staged- CO2 capture from atmosphere, H2O and CO2 dissociation, and fuel synthesis.
The document summarizes experiments on upgrading combined froth using the water gas shift reaction (WGSR) with different reaction conditions. Key findings include:
1) Adding more water increased system pressure and product quality but did little for sulfur removal.
2) Hydrogen performed slightly better than carbon monoxide for sulfur removal and product quality due to its higher concentration.
3) Nickel promoted molybdenum catalyst the most for upgrading, while vanadium inhibited the WGSR when added to Mo/Ni catalyst.
4) Blank experiments without catalyst still showed WGSR and upgrading, confirming metals in the raw froth catalyzed the reactions.
1) Atmospheric CO2 levels have risen from 280 ppm pre-industrially to over 410 ppm currently due to emissions from fossil fuel combustion and respiration. Maximum safe levels are believed to be 450 ppm or less to avoid worst effects of global warming and ocean acidification.
2) The document discusses strategies for converting CO2 into useful products like dimethyl carbonate (DMC), formic acid and methanol. It outlines more sustainable routes for producing these chemicals directly from CO2 rather than traditional methods that rely on other carbon sources.
3) Specifically, it presents a method for continuously producing pure formic acid by hydrogenating supercritical CO2 with an immobilized catalyst and base, avoiding high
Separation of calcium carbonate and barium sulphate from a mixed sludge prduc...Timothy Rukuni
South Africa is one of the first countries to implement full-scale mine water reclamation to drinking water quality. Reverse osmosis is already being used on full scale for desalination of mine water. However, with increased recycling of mine water, the result has been the increased generation of sludge. The Council for Scientific and Industrial Research (CSIR) has developed the Alkali-Barium-Carbonate (CSIR-ABC) process that can be used for neutralization and desalination of sulphate-rich effluents while recovering valuable by-products from the mixed sludges produced. A mixture of BaSO4 and CaCO3 sludge is produced as one of the by-products, which preferably needs to be separated into its components prior to thermal treatment. The aim of this study was to separate CaCO3 and BaSO4 from a CaCO3-BaSO4 mixed sludge through dissolution of CaCO3 as Ca(HCO3)2 in contact with CO2. Measured quantities of a simulated CaCO3-BaSO4 mixed sludge from the CSIR-ABC process were fed into a reactor vessel containing deionized water and pressurized CO2 was introduced. The effects of temperature and pressure with time were investigated while monitoring alkalinity, pH and calcium concentration. The findings of this study were: (1) The dissolution rate of CaCO3 was rapid i.e. from 0 to 2000mg/L in the first 20 minutes; (2) Ca(HCO3)2 had a high solubility of about 2 600 mg/L when in contact with CO2 at 1 atm., while BaSO4 was almost completely insoluble; (3) The solubility of Ca(HCO3)2 increased with decreasing temperature and increasing pressure; (4) CaCO3, after conversion to Ca(HCO3)2, was separated from BaSO4 in a CaCO3-BaSO4 mixed sludge; (5) Visual MINTEQ model is a powerful tool that can be used to predict the solubilities of CaCO3 and BaSO4 when contacted with CO2.
Design of a High Pressure Catalytic Reactor Teststand-latest version by nightOdo B. Wang
The document describes the design of a high pressure catalytic reactor teststand to remove sulfur and nitrogen impurities from petrochemical feedstocks. The primary phase involved simulating, designing, and assembling the teststand. Simulation of a hydrodenitrogenation reaction helped determine operating parameters like temperature, pressure, and flow rates. The design included a 3D model of the frame and piping diagram. Assembly of the furnace, gas chromatography, pumps, and cylinders achieved the goals for the primary phase. Future phases will explore reaction pathways and catalyst structures. The teststand was designed and assembled to safely and effectively study hydrotreating processes for cleaning oil sands feedstocks.
Jonathan Lee (Newcastle University) - Intensification of Solvent Based Carbon Capture using Rotating Packed Beds - UKCCSRC Cranfield Biannual 21-22 April 2015
Presentation given by Dr Hao Liu from University of Nottingham on "CO2 capture from NGCC Flue Gas and Ambient Air Using PEI-Silica Adsorbent" in the Capture Technical Session on Solid Adsorption at the UKCCSRC Biannual Meeting - CCS in the Bigger Picture - held in Cambridge on 2-3 April 2014
Revised hydrolysis of complex hydrides for hydrogen generationDebesh Samanta
This document summarizes Debesh Samanta's research project on hydrolysis of complex hydrides for hydrogen generation. It discusses various solid-state hydrogen storage methods and their advantages. Complex hydrides like NaBH4, NH3BH3, and LiBH4 are promising due to their high gravimetric hydrogen densities. NaBH4 hydrolysis is exothermic and produces over 10 wt% hydrogen. Transition metals like cobalt are effective catalysts for this reaction. Further research aims to improve catalyst stability and recyclability while managing heat release during hydrolysis.
Presentation on "Study of process intensification of CO2 capture through modelling and simulation" given by Dr Meihong Wang from University of Hull in the Process Engineering Technical Session at the UKCCSRC Biannual Meeting in Cambridge on 2-3 April 2014
1) The document describes research into producing metal oxide aerogels for use as dual-purpose structural components in space exploration.
2) Rare earth metal oxide aerogels of various compositions were synthesized using a sol-gel process and characterized. Their properties included low density, high surface area, and variable conductivity and luminescence.
3) The aerogels were crosslinked using polyurethane chemistry to improve their mechanical properties for structural applications. Vanadium and silicon dioxide aerogels were successfully crosslinked as examples.
Robust Co3O4|α-Al2O3|cordierite structured catalyst for N2O abatement – Valid...CarmenMoncada10
Co3O4|α-Al2O3|cordierite structured catalysts were developed, optimizing washcoating procedure, active phase loading, and its deposition method via impregnation and solution combustion synthesis (SCS). The catalysts were thoroughly characterized by XRD, μRS, SEM/EDS, and BET, revealing that the catalyst layer deposited over cordierite carrier, consists of a washcoated micrometric α-Al2O3 (0.1–0.3 µm grains), where spinel nanocrystals (30–50 nm) were uniformly dispersed. It was found out that the SCS method to synthesize and finely disperse spinel nanoparticles results in significant better catalytic performance in low-temperature N2O decomposition than the classic impregnation method. The effectiveness factor evaluated, based on catalyst morphological features and deN2O catalytic results, was found to be ≈1. The determined mass transfer coefficients and type of the catalyst working regime (purely kinetic in the whole temperature range) provide the useful platform for rational design of a real deN2O catalyst.
Presentation given by Professor Joe Wood from University of Birmingham on "Studies of Hydrotalcite Clays for CO2 Adsorption " in the Capture Technical Session on Solid Adsorption at the UKCCSRC Biannual Meeting - CCS in the Bigger Picture - held in Cambridge on 2-3 April 2014
International Journal of Computational Engineering Research(IJCER)ijceronline
International Journal of Computational Engineering Research (IJCER) is dedicated to protecting personal information and will make every reasonable effort to handle collected information appropriately. All information collected, as well as related requests, will be handled as carefully and efficiently as possible in accordance with IJCER standards for integrity and objectivity.
This document discusses various types of liquid chromatography. It describes ion exchange chromatography and factors that influence retention such as ionic strength, pH, temperature, and buffer salt. It also discusses suppressed ion exchange. It explains partitioning chromatography and normal versus reverse phase, as well as factors that influence analyte interaction. Size exclusion chromatography is summarized, noting its advantages and limitations. Supercritical fluid chromatography is also covered, along with its instrumentation and properties of mobile phases used. Supercritical fluid extraction is defined as an alternative to soxhlet extraction.
Absorption of CO2 gas from CO
2/Air mixture into aqueous sodium hydroxide solution has been
achieved using packed column in pilot scale at constant temperature (T) of 25±1℃.The aim of the present work
was to improve the Absorption rate of this process, to find the optimal operation conditions, and to contribute to
the using of this process in the chemical industry. Absorption rate (RA) was measured by using different
operating parameters: gas mixture flow rate (G) of 360 -540 m3/h, carbon dioxide inlet concentration (CCO
2) of
0.1-0.5 vol. %, NaOH solution concentration (CNaOH) of 1-2 M, and liquid holdup in the column (VL) of 0.022-0.028 m3 according to experimental design. The measured RA was in the range of RA = 3.235 – 22.340 k-mol/h.
Computer program (Statgraphics/Experimental Design) was used to estimate the fitted linear model of RA in
terms of (G, CCO2, CNaOH, and VL), and the economic aspects of the process. R -squared of RA model was
91.7659 percent, while the standard error of the estimate shows the standard deviation of the residuals to be
1.7619. The linear model of RA was adequate, the operating parameters were significant except the liquid holdup
was not significant, and the interactions were negligible.
1. This test report provides results for levels of lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers in a sample submitted for testing.
2. Testing found that the levels of lead, cadmium, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers were all below their respective method detection limits.
3. The sample was tested according to various IEC test methods to determine the contents of the regulated substances.
This document describes the development of a novel Pt-Ru bimetallic nanoparticle catalyst supported on a wiregauze for use in passive autocatalytic recombiners to mitigate hydrogen accumulation during loss of coolant accidents in nuclear reactors. The catalyst is prepared via an electroless deposition method and exhibits high catalytic activity for hydrogen-oxygen recombination even in the presence of contaminants like CO2, CH4 and moisture, and shows enhanced activity in the presence of 400 ppm CO. Testing demonstrates the catalyst initiates recombination at room temperature and remains effective after multiple tests, making it suitable for use in nuclear power plant safety systems.
Computational Analysis of CuO Nano Coolant in a Car RadiatorIOSRJMCE
Nanofluids are basically nanoparticles in base fluids. Nanofluids have unique features different from conventional solid-liquid mixtures in which nano sized particles of metals and nonmetals are dispersed. Due to improvement of mechanical properties, nanofluids are widely used in heat transfer industries. The coolant is used water-based, with the addition of glycols to prevent freezing and other additives to limit corrosion, erosion and cavitations. In this study 50-50 mixture of Ethylene Glycol with water (EGW) is tested and compared with another mixture by adding 2 percent Copper oxide (CuO). The geometric model of radiator is uploaded in Autodesk CFD software for its computational analysis. It is analyzed up to 100 iterations. Both the results are compared to find the improved heat transfer rate due to the addition of 2% CuO with Ethylene Glycol and water
The document discusses aqueous phase reforming of sorbitol to produce value-added chemicals. It describes background studies on sorbitol and its potential for hydrogen production. The objectives are to identify value-added chemicals produced from reforming sorbitol over a Ni/Al2O3 catalyst promoted with Ca, and to synthesize and characterize the catalyst. The methodology involves preparing the catalyst using incipient wetness impregnation, characterizing it using TGA, SEM, and H2-TPR, and evaluating its performance in reforming sorbitol to identify products.
MANUFACTURE OF CHLORINE - CAUSTIC SODA USING ELECTROLYSIS PROCESS (MEMBRANE C...Ankush Gupta
This document summarizes the process of manufacturing chlorine and caustic soda using electrolysis. It includes:
- A process flow diagram of the membrane cell process used to separate NaCl into NaOH, H2, and Cl2 via electrolysis.
- Material and energy balances calculations for each unit operation including the membrane cell, evaporator, and dryer. These calculate chemical reactions, flows, heating needs and efficiencies.
- The process achieves 70.28% conversion of NaCl and 27.37% yield of NaOH from the reacted NaCl. Waste streams and energy requirements are also quantified.
Effective Adsorbents for Establishing Solids Looping as a Next Generation NG PCC Technology, Hao Liu, University of Nottingham - UKCCSRC Strathclyde Biannual 8-9 September 2015
The most difficult goal in the next few decades is the replacement of conventional petro-based fuels with more sustainable fuels that can be used in the existing infrastructure. By the use of Renewable energy or nuclear energy, CO2 and H2O can be recycled into liquid hydrocarbon fuels (the reverse of fuel combustion). Capture of CO2 from the atmosphere will form a close carbon-neutral fuel cycle loop. This article also reviews the aspects regarding thermodynamics involved, involved mechanisms and possible technological pathways for recycling CO2 into fuels using renewable energy. These pathways can be broken into three staged- CO2 capture from atmosphere, H2O and CO2 dissociation, and fuel synthesis.
The document summarizes experiments on upgrading combined froth using the water gas shift reaction (WGSR) with different reaction conditions. Key findings include:
1) Adding more water increased system pressure and product quality but did little for sulfur removal.
2) Hydrogen performed slightly better than carbon monoxide for sulfur removal and product quality due to its higher concentration.
3) Nickel promoted molybdenum catalyst the most for upgrading, while vanadium inhibited the WGSR when added to Mo/Ni catalyst.
4) Blank experiments without catalyst still showed WGSR and upgrading, confirming metals in the raw froth catalyzed the reactions.
1) Atmospheric CO2 levels have risen from 280 ppm pre-industrially to over 410 ppm currently due to emissions from fossil fuel combustion and respiration. Maximum safe levels are believed to be 450 ppm or less to avoid worst effects of global warming and ocean acidification.
2) The document discusses strategies for converting CO2 into useful products like dimethyl carbonate (DMC), formic acid and methanol. It outlines more sustainable routes for producing these chemicals directly from CO2 rather than traditional methods that rely on other carbon sources.
3) Specifically, it presents a method for continuously producing pure formic acid by hydrogenating supercritical CO2 with an immobilized catalyst and base, avoiding high
Separation of calcium carbonate and barium sulphate from a mixed sludge prduc...Timothy Rukuni
South Africa is one of the first countries to implement full-scale mine water reclamation to drinking water quality. Reverse osmosis is already being used on full scale for desalination of mine water. However, with increased recycling of mine water, the result has been the increased generation of sludge. The Council for Scientific and Industrial Research (CSIR) has developed the Alkali-Barium-Carbonate (CSIR-ABC) process that can be used for neutralization and desalination of sulphate-rich effluents while recovering valuable by-products from the mixed sludges produced. A mixture of BaSO4 and CaCO3 sludge is produced as one of the by-products, which preferably needs to be separated into its components prior to thermal treatment. The aim of this study was to separate CaCO3 and BaSO4 from a CaCO3-BaSO4 mixed sludge through dissolution of CaCO3 as Ca(HCO3)2 in contact with CO2. Measured quantities of a simulated CaCO3-BaSO4 mixed sludge from the CSIR-ABC process were fed into a reactor vessel containing deionized water and pressurized CO2 was introduced. The effects of temperature and pressure with time were investigated while monitoring alkalinity, pH and calcium concentration. The findings of this study were: (1) The dissolution rate of CaCO3 was rapid i.e. from 0 to 2000mg/L in the first 20 minutes; (2) Ca(HCO3)2 had a high solubility of about 2 600 mg/L when in contact with CO2 at 1 atm., while BaSO4 was almost completely insoluble; (3) The solubility of Ca(HCO3)2 increased with decreasing temperature and increasing pressure; (4) CaCO3, after conversion to Ca(HCO3)2, was separated from BaSO4 in a CaCO3-BaSO4 mixed sludge; (5) Visual MINTEQ model is a powerful tool that can be used to predict the solubilities of CaCO3 and BaSO4 when contacted with CO2.
Design of a High Pressure Catalytic Reactor Teststand-latest version by nightOdo B. Wang
The document describes the design of a high pressure catalytic reactor teststand to remove sulfur and nitrogen impurities from petrochemical feedstocks. The primary phase involved simulating, designing, and assembling the teststand. Simulation of a hydrodenitrogenation reaction helped determine operating parameters like temperature, pressure, and flow rates. The design included a 3D model of the frame and piping diagram. Assembly of the furnace, gas chromatography, pumps, and cylinders achieved the goals for the primary phase. Future phases will explore reaction pathways and catalyst structures. The teststand was designed and assembled to safely and effectively study hydrotreating processes for cleaning oil sands feedstocks.
Jonathan Lee (Newcastle University) - Intensification of Solvent Based Carbon Capture using Rotating Packed Beds - UKCCSRC Cranfield Biannual 21-22 April 2015
Presentation given by Dr Hao Liu from University of Nottingham on "CO2 capture from NGCC Flue Gas and Ambient Air Using PEI-Silica Adsorbent" in the Capture Technical Session on Solid Adsorption at the UKCCSRC Biannual Meeting - CCS in the Bigger Picture - held in Cambridge on 2-3 April 2014
Revised hydrolysis of complex hydrides for hydrogen generationDebesh Samanta
This document summarizes Debesh Samanta's research project on hydrolysis of complex hydrides for hydrogen generation. It discusses various solid-state hydrogen storage methods and their advantages. Complex hydrides like NaBH4, NH3BH3, and LiBH4 are promising due to their high gravimetric hydrogen densities. NaBH4 hydrolysis is exothermic and produces over 10 wt% hydrogen. Transition metals like cobalt are effective catalysts for this reaction. Further research aims to improve catalyst stability and recyclability while managing heat release during hydrolysis.
Presentation on "Study of process intensification of CO2 capture through modelling and simulation" given by Dr Meihong Wang from University of Hull in the Process Engineering Technical Session at the UKCCSRC Biannual Meeting in Cambridge on 2-3 April 2014
1) The document describes research into producing metal oxide aerogels for use as dual-purpose structural components in space exploration.
2) Rare earth metal oxide aerogels of various compositions were synthesized using a sol-gel process and characterized. Their properties included low density, high surface area, and variable conductivity and luminescence.
3) The aerogels were crosslinked using polyurethane chemistry to improve their mechanical properties for structural applications. Vanadium and silicon dioxide aerogels were successfully crosslinked as examples.
Robust Co3O4|α-Al2O3|cordierite structured catalyst for N2O abatement – Valid...CarmenMoncada10
Co3O4|α-Al2O3|cordierite structured catalysts were developed, optimizing washcoating procedure, active phase loading, and its deposition method via impregnation and solution combustion synthesis (SCS). The catalysts were thoroughly characterized by XRD, μRS, SEM/EDS, and BET, revealing that the catalyst layer deposited over cordierite carrier, consists of a washcoated micrometric α-Al2O3 (0.1–0.3 µm grains), where spinel nanocrystals (30–50 nm) were uniformly dispersed. It was found out that the SCS method to synthesize and finely disperse spinel nanoparticles results in significant better catalytic performance in low-temperature N2O decomposition than the classic impregnation method. The effectiveness factor evaluated, based on catalyst morphological features and deN2O catalytic results, was found to be ≈1. The determined mass transfer coefficients and type of the catalyst working regime (purely kinetic in the whole temperature range) provide the useful platform for rational design of a real deN2O catalyst.
Presentation given by Professor Joe Wood from University of Birmingham on "Studies of Hydrotalcite Clays for CO2 Adsorption " in the Capture Technical Session on Solid Adsorption at the UKCCSRC Biannual Meeting - CCS in the Bigger Picture - held in Cambridge on 2-3 April 2014
International Journal of Computational Engineering Research(IJCER)ijceronline
International Journal of Computational Engineering Research (IJCER) is dedicated to protecting personal information and will make every reasonable effort to handle collected information appropriately. All information collected, as well as related requests, will be handled as carefully and efficiently as possible in accordance with IJCER standards for integrity and objectivity.
This document discusses various types of liquid chromatography. It describes ion exchange chromatography and factors that influence retention such as ionic strength, pH, temperature, and buffer salt. It also discusses suppressed ion exchange. It explains partitioning chromatography and normal versus reverse phase, as well as factors that influence analyte interaction. Size exclusion chromatography is summarized, noting its advantages and limitations. Supercritical fluid chromatography is also covered, along with its instrumentation and properties of mobile phases used. Supercritical fluid extraction is defined as an alternative to soxhlet extraction.
Microwave Assited Extraction (MAE) techniques of herbal drugsAnurag Bhardwaj
Microwave-assisted extraction is an efficient method to extract compounds from plants using microwave energy. It provides faster extraction times, improved yields, and better accuracy compared to traditional techniques like Soxhlet extraction. The document discusses the principles and theory of microwave extraction, different instruments used, factors that affect the extraction process like solvent, temperature, and power. It concludes that microwave extraction is an effective technique for herbal drug extraction and more research is needed to improve industrial applications.
Galenicals are herbal medicines prepared according to ancient formulas. They are made by extracting active plant constituents using solvents like water or alcohol. Infusions and decoctions are two common types of galenicals. Infusions are used for plants with water-soluble compounds and soft tissues, prepared by steeping the plant in water. Decoctions are used for plants with hard, woody tissues, prepared by boiling the plant in water to extract water-soluble compounds. The document provides details on the preparation, storage, and examples of infusions and decoctions.
Solid phase extraction (SPE) is a sample preparation technique that selectively enriches analytes from a sample matrix. It involves passing a sample through a cartridge containing a solid stationary phase. Analytes selectively bind to the phase based on properties like polarity while interfering matrix components are removed. Bound analytes can then be eluted and analyzed. SPE offers advantages over liquid-liquid extraction like higher selectivity and cleaner extracts. It has various applications including impurity profiling, environmental analysis, food chemistry, and biological analysis. Solid phase microextraction (SPME) is a related technique that extracts analytes directly from vapors using a coated fiber for analysis by gas chromatography.
This document discusses various extraction methods for active components from medicinal plants. It defines extraction as separating medicinally active portions from inactive components using selective solvents. Extraction methods include decoction, infusion, maceration, fluid extracts, and tinctures. Decoction involves boiling plant material in water. Infusion uses cold or boiling water to make dilute solutions. Percolation is commonly used to make tinctures and fluid extracts using a percolator. Distillation isolates essential oils by boiling plant material in water or steam. Expression physically crushes plant peels to release oils. Standardizing extraction procedures is important to obtain the desired therapeutic portions and eliminate inert material.
This document discusses serial extraction, which is an interceptive orthodontic procedure used to correct hereditary tooth-size discrepancies. It describes when serial extraction should be considered, between ages 6-12, and the criteria for determining if a patient is a suitable candidate. Ideal candidates have a Class I malocclusion with a true tooth-size discrepancy of 10mm or more. Contraindications include Class III maloccusions. A thorough examination and diagnostic records including radiographs and models are required to properly diagnose if serial extraction is appropriate.
This document discusses potential complications that can arise from tooth extraction procedures. It outlines various local complications that can occur immediately, delayed, or late after an extraction. Immediate complications include failure of local anesthesia, inability to remove the tooth, fracture of tooth or surrounding bone, oro-antral communication, soft tissue displacement, hemorrhage, TMJ dislocation, and damage to nerves. Delayed complications involve pain, swelling, bleeding, dry socket, osteomyelitis, infection, oro-antral fistula, and failed socket healing. Late complications are chronic osteomyelitis, osteoradionecrosis, and nerve damage. The document provides details on causes and management of several specific complications.
This document discusses microwave-assisted extraction (MAE), an efficient method for deriving natural compounds from plants. MAE uses microwave energy to heat plant materials mixed with solvents, extracting compounds faster than conventional methods. It describes the principles of microwave heating, closed and open vessel extraction systems, factors affecting MAE like solvent, time, power and temperature, and its applications. MAE provides benefits of reduced extraction time, improved yields, and ability to extract thermolabile substances.
Essential oils are aromatic liquid substances extracted from plants through various methods. The most common extraction method is steam distillation, which involves using steam to separate the essential oils from plant material. Other methods include carbon dioxide extraction, cold press extraction, and using solvents to extract absolutes. Essential oils have various uses including aromatherapy, massage, room freshening, insect repellents, and beauty products due to their aromatic properties.
method to separate compounds based on their relative solubilities in two different immiscible liquids, usually water and an organic solvent. It is an extraction of a substance from one liquid into another liquid phase.
Liquid-liquid extraction is a technique used to separate components of a mixture based on differences in solubility. In this technique, a solvent is used to transfer a solute from one liquid phase to another immiscible liquid phase. For example, sugar can be extracted from a vegetable oil and water mixture by shaking the mixture, as the sugar is more soluble in water. The success of liquid-liquid extraction depends on choosing an extraction solvent that exploits differences in a compound's solubility between solvents. Additionally, compounds can be made more soluble in water by converting them to ionic salt forms using acid-base chemistry.
Essential oils are volatile (quickly evaporating) aromatic fluids extracted from plants through steam distillation, or in the case of citrus fruits through expression (or cold pressing) of the rind to obtain an oil that retains a juicy, fresh fruit scent.
Various extraction methods are used in the manufacture and extraction of essential oils, and the method used is normally dependant on what type of botanical material is being used.
This document discusses various methods for extracting volatile oils from plants. It describes distillation techniques like water distillation, steam distillation, and destructive distillation. It also covers solvent extraction methods and mechanical expression. The key extraction methods are distillation, solvent extraction using chemicals or supercritical fluids, and mechanical expression for certain plants. Distillation is a common traditional technique but requires more energy, while supercritical fluid extraction provides better oil yields in less time.
This document discusses the process of extraction, specifically maceration. It defines extraction as separating medicinally active portions of plants from inactive components using selective solvents. It then describes maceration as soaking crushed plant material in a solvent for a period of time to soften cells and dissolve soluble constituents. The key steps of maceration involve adding crushed plant material and solvent to a vessel, soaking for 7 days, straining and pressing the plant material, and filtering and concentrating the extracted liquid. Larger scale extraction processes like circulatory extraction and multiple stage extraction in an extraction battery are also summarized to improve efficiency.
This document defines extraction as the removal of soluble constituents from a solid or liquid with a suitable solvent. It discusses various types of extraction including solid-liquid extraction, liquid-liquid extraction, and expression. Key terms like menstruum, marc, and extractives are defined. Important solvents for extraction like water, alcohol, ether, and chloroform are described. The document also covers the theory of extraction and importance of extraction in quantitative control of drugs and producing more stable, palatable forms.
Production, Manufacturing and Extraction of Silver, Gold, Copper, Magnesium,...Ajjay Kumar Gupta
Electroplating involves passing an electric current through a solution called an electrolyte. This is done by dipping two terminals called electrodes into the electrolyte and connecting them into a circuit with a battery or other power supply. The electrodes and electrolyte are made from carefully chosen elements or compounds. When the electricity flows through the circuit they make, the electrolyte splits up and some of the metal atoms it contains are deposited in a thin layer on top of one of the electrodes—it becomes electroplated. All kinds of metals can be plated in this way, including gold, silver, tin, zinc, copper, cadmium, chromium, nickel, platinum, and lead.
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The document discusses various general methods used for the isolation and separation of plant constituents, including extraction processes, separation techniques, and analytical methods. Extraction methods covered include maceration, infusion, digestion, decoction, percolation, soxhlet extraction, ultrasound extraction, and supercritical fluid extraction. Separation techniques include fractional crystallization, fractional distillation, thin layer chromatography, column chromatography, and paper chromatography. Analytical methods for identification discussed are gas chromatography, high performance liquid chromatography, and qualitative chemical reactions.
CMEME2015 Conference: "Understanding hydrogen behaviour in steels" Daniel Gaude-Fugarolas
This document discusses understanding hydrogen behavior in steels, including diffusion, trapping, embrittlement risk and prevention. It covers several topics:
1. Studying hydrogen embrittlement and diffusion modeling.
2. Applications including analysis of casting processes, development of a new hydrogen extraction method during casting, analysis of baking treatments, and prediction of hydrogen damage.
3. Ongoing work on hydrogen desorption and permeation.
Understanding hydrogen redistribution during steel casting, and its effective extraction by thermally induced up-hill diffusion.
Presented at High Strength Low Alloy Steels International Conference 2011 in Beijing.
An Update on Gas CCS Project: Effective Adsorbents for Establishing Solids Looping as a Next Generation NG PCC Technology - presentation by Colin Snape in the Natural Gas CCS session at the UKCCSRC Cardiff Biannual Meeting, 10-11 September 2014
Balucan and Steel_2015_A regenerable precipitant-solvent system for CO2 mitig...Reydick D Balucan
This document describes a new process for CO2 mitigation and metals recovery using a regenerable solvent-precipitant system. The system uses a tertiary amine and acid that can undergo a pH swing via a change in temperature. Specifically, various tertiary amines and acids were tested to identify a combination that can adjust the pH between 10 and 2, which is suitable for metal hydroxide precipitation and metal leaching from magnesium solids. The researchers found that a triethylamine-sulfuric acid-water system could achieve a pH swing between 10.5 and 1.9 with temperature changes, meeting the criteria. This combination uses triethylamine to alkalize the solution to pH > 10.5 and uses sulfur
This presentation discusses carbon dioxide capture and sequestration using activated carbon adsorption. It begins with an introduction to climate change and carbon capture and storage technologies. It then presents the objective to model CO2 adsorption on activated carbon. A mathematical model is developed based on Dubinin's theory of micropore filling. Governing equations are presented and discretized. Results show the model validates experimentally. A parametric analysis examines the effects of bed thickness, cooling temperature, heat transfer coefficient and initial bed temperature on CO2 adsorption. It concludes lower bed radii and higher temperatures and heat transfer rates increase adsorption while noting temperature effects on materials. Future work could extend the model and realize challenges of practical implementation.
Hydrodynamic Behaviour of the Torbed® Reactor Operating in Fine Particle Mode.Grant Wellwood
This thesis investigates the hydrodynamic behaviour of the Torbed® reactor operating in fine particle mode. The Torbed reactor offers enhanced gas-solid contacting through increased transport and lower pressure drop compared to conventional systems. However, understanding of these process aspects was lacking, hindering development. The study aims to understand slip velocity characteristics and pressure drop to facilitate process development, optimization, and scale-up.
Qualitative experiments show the Torbed reactor exhibits particle streaming that increases effective particle velocities. Quantitative experiments investigate the relationship between slip velocity and operational parameters. The results support using a thermodynamic analogy to predict slip velocity as a function of inputs. Field trials applying the findings successfully achieved dry scrubbing goals.
- The document is a PhD thesis by Grant Ashley Wellwood investigating the hydrodynamic behaviour of the Torbed® reactor operating in fine particle mode.
- In fine particle mode, the Torbed reactor offers unique gas-solid contacting capabilities through enhanced transport and lower pressure drop than traditional systems. However, understanding of these processes was lacking, hindering development.
- The focus of the study was to understand slip velocities and pressure drop to facilitate process development, technology selection, optimization, and scale-up for the Torbed reactor operating in fine particle mode.
Abstracts of publications in ppc whilst affiliated with sask powerEmmanuel Quagraine
1) The document summarizes 5 journal publications by Emmanuel K. Quagraine related to power plant chemistry while affiliated with SaskPower.
2) The publications provide evidence that chlorinated compounds can ingress into power plant condensers in gaseous form through weak seals or porous brass tubesheets, causing chloride contamination issues. Regression models were able to confirm this hypothesis.
3) One publication evaluates using a biologically active carbon filter in series with a granular activated carbon filter for removing organics in boiler makeup water, finding over 80% removal with the two filters working synergistically.
1) Hydrogen embrittlement occurs when hydrogen degrades the mechanical properties of metals, which is important for assessing fatigue and fracture in pipeline steels exposed to gaseous hydrogen.
2) Testing shows gaseous hydrogen greatly accelerates the fatigue crack growth rate in pipeline steels by over 30 times and reduces their fracture resistance by over 50%.
3) There is no clear threshold for hydrogen effects - even small amounts of hydrogen in a gas mixture can have substantial impacts on fatigue and fracture behavior of pipeline steels.
Literature Review of Mineral Carbonations of steel slag.pptxsandeepsharma432939
This document presents a literature review and proposed research plan on utilizing mineral carbonation to sequester carbon dioxide using basic oxygen furnace (BOF) slag. The introduction discusses how CO2 concentration is increasing and various CO2 sequestration methods, including mineral carbonation. The literature review summarizes previous studies on BOF slag carbonation and identifies research gaps. The proposed research will investigate the effect of operational parameters on CO2 uptake and conversion, characterize carbonated slag, and analyze results to determine optimum conditions for maximum conversion. The methodology, work plan, and references are also outlined.
The document summarizes the Actinide and Brine Chemistry in a Salt Repository (ABC Salt V) workshop held in March 2017. It provides an overview of the workshop sessions which covered updates on the Waste Isolation Pilot Plant (WIPP) and international salt repositories, salt research project updates, microbial effects, corrosion and sorption studies, modeling and solubility studies, temperature effects, and actinide redox chemistry and solubility. Key discussions focused on data gaps in solubility models and understanding actinide redox processes under repository conditions. The workshop facilitated productive discussions between international researchers and showed continued progress is being made in salt repository research despite challenges.
Heat Transfer Characteristics of Nanofluid (Al2O3/water) in Cooling System of...Hussein S. Moghaieb
The document discusses the characteristics of heat transfer of nanofluids used for engine cooling. It provides background on using nanofluids to enhance heat transfer for applications like engine cooling where heat dissipation is important. The literature review summarizes previous studies that found heat transfer enhancement when using nanofluids like Al2O3 nanoparticles dispersed in water or ethylene glycol. The present work aims to investigate heat transfer enhancement under varying bulk temperatures, flow velocities, heat fluxes, and nanofluid concentrations to simulate engine operating conditions. It describes the proposed experimental test rig and setup that will be used to analyze the heat transfer performance of Al2O3/water nanofluids.
This document describes a project to develop a process intensification technique for post-combustion carbon capture using a rotating packed bed. The project aims to develop dynamic models of the intensified process and optimize the design through simulation and CFD studies. It will then scale up the optimized design and evaluate its technical, economic and environmental performance compared to conventional carbon capture processes. The rotating packed bed is expected to boost mass transfer and reduce the size of capture equipment compared to current absorption processes. The multi-institution consortium will work on experimental studies, modeling, simulation, design optimization and scale-up over a period of 4 years.
CFD investigation on heat transfer enhancement in shell and tube heat exchang...IRJET Journal
The document discusses a computational fluid dynamics (CFD) investigation of heat transfer enhancement in a shell and tube heat exchanger using graphene oxide (GO) nanofluid. A 3D model of a shell and tube heat exchanger is developed and GO nanofluid is introduced. Governing equations are solved numerically to analyze heat transfer performance. Results show that incorporating GO nanofluid leads to enhanced heat transfer compared to traditional fluids due to GO's higher thermal conductivity and its ability to disrupt thermal boundary layers and promote mixing. Heat transfer rate increased 42% and convective heat transfer coefficient increased 62% with GO nanofluid. This suggests GO nanofluid can significantly improve heat exchanger efficiency for applications like power plants and HVAC systems. Further
Development of an aqueous ammonia-based post-combustion capture technology fo...Global CCS Institute
To highlight the research and achievements of Australian researchers, the Global CCS Institute with ANLEC R&D will hold a series of webinars throughout 2016. Each webinar highlights a specific ANLEC R&D research project and the relevant report found on the Institute’s website. The fifth webinar of the series looked at the development of an aqueous ammonia-based post-combustion capture technology for Australian conditions.
CSIRO has been developing aqueous ammonia (NH3)-based post-combustion CO2 capture (PCC) technology for its application under Australian conditions since 2008. Previous pilot-plant trials at Delta Electricity’s Munmorah Power Station demonstrated the technical feasibility of the process and confirmed some of the expected benefits. With further support from the Australian Government and ANLEC R&D, CSIRO has worked closely with universities in Australia and China to develop an advanced aqueous NH3-based CO2 capture technology. The advanced technology incorporates a number of innovative features which significantly improve its economic feasibility. This webinar presented the advancements made from a recently completed project funded by ANLEC R&D, and was presented by Dr Hai Yu and Dr Kangkang Li from CSIRO Energy.
design optimization of a single-strand tundish based on CFDssusercf6d0e
This document summarizes a study that used computational fluid dynamics (CFD) modeling and Taguchi-Grey relational analysis to optimize the design of flow control devices in a single-strand tundish. The study aimed to maximize the inclusion removal rate and minimize the dead volume fraction by optimizing the positions of the weir and dam. A Taguchi orthogonal array was used to analyze the effects of design factors on the responses. Grey relational analysis and analysis of variance were then used to determine the optimum positions of the weir and dam based on the multiple design targets of high inclusion removal rate and low dead volume fraction.
Apec workshop 2 presentation 12 lh ci cinco presidentes-pemex-apec workshop 2Global CCS Institute
This document outlines a life cycle assessment of CO2 emissions from a CO2-EOR project in southern Mexico. It describes the goal of understanding environmental impacts from a life cycle perspective and estimating CO2 emissions associated with various steps of the project. The methodology estimates emissions using activity data and emission factors. Results found that CO2 emissions from the offshore platform to refinery via the EOR project were 5.41 tCO2eq per ton of CO2 injected, and the project reduced greenhouse gas emissions and environmental impacts compared to business as usual.
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Introduction- e - waste – definition - sources of e-waste– hazardous substances in e-waste - effects of e-waste on environment and human health- need for e-waste management– e-waste handling rules - waste minimization techniques for managing e-waste – recycling of e-waste - disposal treatment methods of e- waste – mechanism of extraction of precious metal from leaching solution-global Scenario of E-waste – E-waste in India- case studies.
Understanding Inductive Bias in Machine LearningSUTEJAS
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2. Operations Strategy in a Global Environment.ppt
Understanding hydrogen redistribution and designing a new hydrogen extraction method
1. Introduction
The Model
Application to real processes
Conclusion
Understanding hydrogen redistribution and
designing a new hydrogen extraction method
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net)
dgaude Prime Innovation SLU
Independent Research in Physical Metallurgy and Engineering
3rd UK-China Steel Research Forum
Rutherford Appleton Laboratory (UK)
10-11 July 2014
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
2. Introduction
The Model
Application to real processes
Conclusion
1 Introduction
2 The Model
3 Application to real processes
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
4 Conclusion
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
3. Introduction
The Model
Application to real processes
Conclusion
Embrittlement prevention methods
At the design stage (material & component
engineering)
Extraction from liquid metal during refining
(Vacuum, AOD, et c.)
Extraction from solid at high temperature (very
slow cooling & directional cooling:
METAL2010, HSLA2011, Euromat2011, Steel &
Hydrogen2014, et c. )
Extraction by treating after cooling (Baking
treatment: METAL2014)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
4. Introduction
The Model
Application to real processes
Conclusion
Embrittlement prevention methods
At the design stage (material & component
engineering)
Extraction from liquid metal during refining
(Vacuum, AOD, et c.)
Extraction from solid at high temperature (very
slow cooling & directional cooling:
METAL2010, HSLA2011, Euromat2011, Steel &
Hydrogen2014, et c. )
Extraction by treating after cooling (Baking
treatment: METAL2014)
Can we still do anything else to reduce the incidence
of hydrogen embrittlement in metals?
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
5. Introduction
The Model
Application to real processes
Conclusion
The Model
Let’s start at the beginning:
Let’s try and understand the redistribution of
interstitial elements
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
6. Introduction
The Model
Application to real processes
Conclusion
The Model
Let’s start at the beginning:
Let’s try and understand the redistribution of
interstitial elements
An interstitial diffusion model
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
7. Introduction
The Model
Application to real processes
Conclusion
Interstitial diffusion: Hydrogen
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
8. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel& Hydrogen2014, et c.)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
9. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel& Hydrogen2014, et c.)
Thermal evolution and T gradients (Heat Equation)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
10. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel& Hydrogen2014, et c.)
Thermal evolution and T gradients (Heat Equation)
Phase transitions from Liquid to BCC (Thermodynamic Model)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
11. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel Hydrogen2014, et c.)
Thermal evolution and T gradients (Heat Equation)
Phase transitions from Liquid to BCC (Thermodynamic Model)
Hydrogen diffusion as random walk, driven by chemical activation
gradient
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
12. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel Hydrogen2014, et c.)
Thermal evolution and T gradients (Heat Equation)
Phase transitions from Liquid to BCC (Thermodynamic Model)
Hydrogen diffusion as random walk, driven by chemical activation
gradient (... think of it as following a partial saturation gradient)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
13. Introduction
The Model
Application to real processes
Conclusion
Model: Diffusion
Characteristics of the model:
(METAL2010-2014, HSLA2011, EUROMAT2011, Steel Hydrogen2014, et c.)
Thermal evolution and T gradients (Heat Equation)
Phase transitions from Liquid to BCC (Thermodynamic Model)
Hydrogen diffusion as random walk, driven by chemical activation
gradient (... think of it as following a partial saturation gradient)
Interstitial solubility and saturation as function of temperature and
matrix phase or trap type and distribution
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
14. Introduction
The Model
Application to real processes
Conclusion
Model: Trapping
Each trap type characterised
by its characteristic release
energy barrier
Interaction of each of the
trap sites with lattice
Exchange with atmosphere
at free surfaces: local
equilibrium across the
surface (Sievert’s law)
E
Et
d
Trap_1 .. Trap_i .. Trap_n
Atmosphere
Lattice
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
15. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Application to real processes
What can we do with this model? (Very briefly)
Analysis of Casting (or any cooling process)
Development of new H extraction method
Analysis of Baking
... and much more!!
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
16. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Analysis of Casting (or any cooling process)
6
5
4
3
2
1
0
Fast cooling Slow cooling
-------------center piece--------
-12.5 -5 0 5 12.5
2
1
0
H content /ppm
Thickness /cm
0s
30s
150s
600s
1200s
1700s
45
40
35
30
25
20
15
0h
1h
10
6h
5
24h
42h 0
-----------center piece-----------
Fast cooling Slow cooling
-12.5 -5 0 5 12.5
15
10
5
0
H partial saturation
Thickness /cm
0s
600s
900s
1200s
1500s
1700s
0h
1h
6h
24h
42h
Steel: 25cm thick with 2ppm
Effect of cooling rate:
Fast cooling vs. Slow cooling
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
17. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Analysis of Casting (or any cooling process)
6
5
4
3
2
1
0
Fast cooling Slow cooling
-------------center piece--------
-12.5 -5 0 5 12.5
2
1
0
H content /ppm
Thickness /cm
0s
30s
150s
600s
1200s
1700s
45
40
35
30
25
20
15
0h
1h
10
6h
5
24h
42h 0
-----------center piece-----------
Fast cooling Slow cooling
-12.5 -5 0 5 12.5
15
10
5
0
H partial saturation
Thickness /cm
0s
600s
900s
1200s
1500s
1700s
0h
1h
6h
24h
42h
Steel: 25cm thick with 2ppm
Effect of cooling rate:
Fast cooling vs. Slow cooling
Effect of thickness: (5-50cm)
Effect of FCC to BCC transformation
temperature:
Steel A: 700oC vs. Steel B: 450oC
6
5.5
5
4.5
4
3.5
3
2.5
2
1.5
5 10 20 30 40 50
Max H content /ppm
Thickness /cm
Alloy A
Alloy B
Start H
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
18. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
Development of a new hydrogen extraction method
“Understanding hydrogen redistribution during steel casting, and its effective extraction by
thermally induced up-hill diffusion”
D. Gaude-Fugarolas, in: Journal of Iron and Steel Research International 18 supl.1.1 (2011)
159–163.
Also at proceedings: High Strength Low Alloy (HSLA2011) International Conference, Beijing,
China, 2011.
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
19. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
A severe temperature gradient forces hydrogen to flow towards the core
region of a component, where it can reach severe supersaturation
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
20. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
A severe temperature gradient forces hydrogen to flow towards the core
region of a component, where it can reach severe supersaturation
Actually, NO!!. The temperature gradient forces hydrogen to flow
towards higher temperature regions!!
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
21. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
A severe temperature gradient forces hydrogen to flow towards the core
region of a component, where it can reach severe supersaturation
Actually, NO!!. The temperature gradient forces hydrogen to flow
towards higher temperature regions!!
Then, why don’t we try instead to redirect the hydrogen flux
towards the surface?
(and eventually get rid of it)
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
22. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
Standard casting operation: Interstitial
element flux creates enriched regions at
the core of the piece
Pouring cup
Feeder
Casting
Riser
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
23. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
Standard casting operation: Interstitial
element flux creates enriched regions at
the core of the piece
Pouring cup
Feeder
Casting
Riser
Modified casting operation with a severe
thermal gradient towards the surface
being imposed, eliminating interstitials
Pouring cup
Feeder
Casting
Riser
Heating Element
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
24. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
5
4
3
2
1
0
-12.5 -5 0 5 12.5
H content /ppm
Thickness /cm
Heated Surface
10
1
0s
60s
0.1
300s
1200s
3600s
8400s 0.01
-12.5 -5 0 5 12.5
H partial saturation
Thickness /cm
Heated Surface
0s
60s
300s
1200s
3600s
7200s
7600s
8000s
8400s
Steel: 25cm thick with 2ppm
Surface I: Fast cooling
Surface II: Kept at high temperature
(i.e. 1500oC)
Temperature gradient maintained 2h
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
25. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Development of a new hydrogen extraction method
5
4
3
2
1
0
-12.5 -5 0 5 12.5
H content /ppm
Thickness /cm
Heated Surface
10
1
0s
60s
0.1
300s
1200s
3600s
8400s 0.01
-12.5 -5 0 5 12.5
H partial saturation
Thickness /cm
Heated Surface
0s
60s
300s
1200s
3600s
7200s
7600s
8000s
8400s
Steel: 25cm thick with 2ppm
Surface I: Fast cooling
Surface II: Kept at high temperature
(i.e. 1500oC)
Temperature gradient maintained 2h
Final H content 0.99ppm!!
i.e 50% Reduction!!
Partial Saturation during
treatment below 1.0 !!
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
26. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Analysis of Baking
Analysis of Baking
“On the effectiveness of baking as hydrogen embrittlement reduction treatment”
D. Gaude-Fugarolas, in: Proceedings of METAL2014, 21-23 May, Brno, Czech Republic, 2014.
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
27. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Treatment after cooling: Baking
Storage of the metal components in over at low warm
temperature (typically 150-230 oC) for a long period,
up to 24-48 hours.
The treatment aims to reduce internal stresses and to
reduce hydrogen content.
If treatment is not performed immediately after
casting and cooling, it might become ineffective.
Effectiveness of treatment varies.
Why does effectiveness of baking vary so much?
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
28. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Analysis of Baking
Hydrogen content: 1 ppm
Baking: 12h at 190oC or 300oC
Sites: Lattice, Dislocation, Grain boundary,
Precipitate ( Desorption to atmosphere)
Steel A: Allotriomorphic Ferrite (725oC), large
grain, low dislocation density
Steel B: Bainitic/Martensitic Ferrite (450oC),
small grain, high dislocation density
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
29. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Analysis of Baking
Hydrogen content: 1 ppm
Baking: 12h at 190oC or 300oC
Sites: Lattice, Dislocation, Grain boundary,
Precipitate ( Desorption to atmosphere)
Steel A: Allotriomorphic Ferrite (725oC), large
grain, low dislocation density
Steel B: Bainitic/Martensitic Ferrite (450oC),
small grain, high dislocation density
LATTICE Steel A
0.625
0.125
0.025
0.005
0.001
0 6 h 12 h
H conc /ppm
Time /s
(a0)
0.625
0.125
0.025
0.005
0.001
Steel B
0 6 h 12 h
H conc /ppm
Time /s
(b0)
0.625
0.125
0.025
0.005
0.001
0 6 h 12 h
H conc /ppm
Time /s
(a1)
DISLOCATION
0.625
0.125
0.025
0.005
0.001
0 6 h 12 h
H conc /ppm
Time /s
(b1)
GRAIN Steel A
0.1000
0.0100
0.0010
0.0001
0.0000
0 6 h 12 h
H conc /ppm
Time /s
(a2)
0.1000
0.0100
0.0010
0.0001
0.0000
Steel B
0 6 h 12 h
H conc /ppm
Time /s
(b2)
0.55
0.50
0.45
0.40
0.35
0 6 h 12 h
H conc /ppm
Time /s
(a3)
PRECIPITATE
0.55
0.50
0.45
0.40
0.35
0 6 h 12 h
H conc /ppm
Time /s
(b3)
“On the effectiveness of baking as hydrogen embrittlement reduction treatment”
D. Gaude-Fugarolas, in: Proceedings of METAL2014, 21-23 May, Brno, Czech Republic, 2014.
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
30. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Conclusions on Baking
The success of baking depends of the interaction of hydrogen
content, microstructure and trap distribution.
Some microstructures already saturate with low hydrogen contents,
making baking useless.
In general, baking is only effective when the microstructure is far
below saturation.
The baking temperature needs to be tailored to trap type and H
distribution.
Some defects may even increase their H content during baking.
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
31. Introduction
The Model
Application to real processes
Conclusion
Analysis of Casting (or any cooling process)
Development of a new hydrogen extraction method
Analysis of Baking
Future work
Future work
This is still work in progress...
Surface defects
Crack initiation
H absorption from atmosphere
To be presented at, may be, METAL2015, Brno, Czech Republic, May 2015.
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
32. Introduction
The Model
Application to real processes
Conclusion
Conclusion
Conclusion
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
33. Introduction
The Model
Application to real processes
Conclusion
Conclusion
To summarise...
Small amounts of hydrogen can endanger the integrity of critical
metal components.
A physical model has been presented offering a correct description of
hydrogen redistribution during manufacturing operations.
Several methods exist to reduce hydrogen embrittlement in metal,
but not always successful.
A new method has been presented to reduce hydrogen content using
of imposed temperature gradients.
(Patent filed in US, Europe, China, et c., Already awarded or in
process, and open for licensing).
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction
34. Introduction
The Model
Application to real processes
Conclusion
Thanks
Thank you for your attention!!
For more information, please visit (or email):
primeinnovation.net
dgaude@cantab.net
Daniel Gaude-Fugarolas, Ph.D, FCPS (dgaude@cantab.net) Understanding hydrogen redistribution and its extraction