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Carbon dioxide resource utilization in methanol products: Carbon emission projections, visual analysis, life cycle assessment

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... Carbon emission accounting is the basis for formulating effective carbon-reduction strategies, and carbon emission peak prediction is an important tool for evaluating and planning emission reduction paths [18]. Currently, to predict peak carbon emissions, researchers have used various methods, including scenario analyses, statistical models, and complex models, such as machine learning. ...
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Small Au, Cu, and Ni particles in contact with TiC(001) display a very high activity for the catalytic hydrogenation of CO2. The major product over these catalysts is CO which is produced by the reverse water gas shift reaction (RWGS, CO2 + H-2 -> CO + H2O). In the cases of Au/TiC(001) and Cu/TiC(001), a substantial amount of methanol is also produced, but no methane is detected. Ni/TiC(001) produces a mixture of CO, methanol, and methane. The highest catalytic activity is found for small two-dimensional particles or clusters of the admetals in close contact with TiC(001). The catalytic activity of the supported metals can be orders of magnitude higher than those-of Au(100), Cu(100), or Ni(100). Density functional calculations point to HOCO as a key intermediate for the generation of CO through the RWGS, with the production of methanol probably involving the hydrogenation of a HCOO intermediate or the CO generated by the RWGS.
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The amount of bottom ash formed in a pulverized coal-fired power plant was predicted by artificial neural network modeling using one-year operating data of the plant and the properties of the coals processed. The model output was defined as the ratio of amount of bottom ash produced to amount of coal burned (Bottom ash/Coal burned). The input parameters were the moisture contents, ash contents and lower heating values of the coals. The total 653 data were divided into two groups for the training (90% of the data) and the testing (10% of the data) of the network. A three-layer, feed-forward type network architecture with back-propagation learning was used in the modeling study. The activation function was sigmoid function. The best prediction performance was obtained for a one hidden layer network with 29 neurons. The learning rate and the tolerance value were 0.2 and 0.05, respectively. R2 (coefficient of determination) values between the actual (Bottom ash/Coal burned) ratios and the model predictions were 0.988 for the training set and 0.984 for the testing set. In addition, the sensitivity analysis indicated that the ash content of coals was the most effective parameter for the prediction of the ratio of bottom ash to coal burned.
Article
The low temperature (403–453 K) conversions of CO/hydrogen and CO2/hydrogen mixtures (6 bar total pressure) to methanol over copper catalysts are both assisted by the presence of small amounts of water (mole fraction ∼0.04–0.5%). For CO2/hydrogen reaction mixtures, the water product from both methanol synthesis and reverse water–gas shift serves to initiate both reactions in an autocatalytic manner. In the case of CO/D2 mixtures, very little methanol is produced until small amounts of water are added. The effect of water on methanol production is more immediate than in CO2/D2, yet the steady-state rates are similar. Tracer experiments in 13CO/12CO2/hydrogen (with or without added water) show that the dominant source of C in the methanol product gradually shifts from CO2 to CO as the temperature is lowered. Cu-bound formate, the major IR visible surface species under CO2/hydrogen, is not visible in CO/moist hydrogen. Though formate is visible in the tracer experiments, the symmetric stretch is absent. These results, in conjunction with recent DFT calculations on Cu(1 1 1), point to carboxyl as a common intermediate for both methanol synthesis and reverse water–gas shift, with formate playing a spectator co-adsorbate role.
Article
The only comprehensive study comparing structural decomposition analysis (SDA) and index decomposition analysis (IDA) was conducted around 2000. There have since been new developments in both techniques in energy and emission studies. These developments have been studied systematically for IDA but similar studies for SDA are lacking. In this paper, we fill the gap by examining the new methodological developments in SDA. A new development is a shift towards using decomposition methods that are ideal. We compare four such SDA methods analytically and empirically through decomposing changes in China's CO2 emissions. We then provide guidelines on method selection. Finally, we discuss the similarities and differences between SDA and IDA based on the latest available information.
Article
A global assessment of the potential impact of climate change on world food supply suggests that doubling of the atmospheric carbon dioxide concentration will lead to only a small decrease in global crop production. But developing countries are likely to bear the brunt of the problem, and simulations of the effect of adaptive measures by farmers imply that these will do little to reduce the disparity between developed and developing countries.
Article
There is increased recognition by the world’s scientific, industrial, and political communities that the concentrations of greenhouse gases in the earth’s atmosphere, particularly CO_2, are increasing. For example, recent studies of Antarctic ice cores to depths of over 3600 m, spanning over 420 000 years, indicate an 80 ppm increase in atmospheric CO_2 in the past 200 years (with most of this increase occurring in the past 50 years) compared to the previous 80 ppm increase that required 10 000 years.2 The 160 nation Framework Convention for Climate Change (FCCC) in Kyoto focused world attention on possible links between CO2 and future climate change and active discussion of these issues continues.3 In the United States, the PCAST report4 “Federal Energy Research and Development for the Challenges of the Twenty First Century” focused attention on the growing worldwide demand for energy and the need to move away from current fossil fuel utilization. According to the U.S. DOE Energy Information Administration,5 carbon emission from the transportation (air, ground, sea), industrial (heavy manufacturing, agriculture, construction, mining, chemicals, petroleum), buildings (internal heating, cooling, lighting), and electrical (power generation) sectors of the World economy amounted to ca. 1823 million metric tons (MMT) in 1990, with an estimated increase to 2466 MMT in 2008-2012 (Table 1).
Article
To analyze and understand historical changes in economic, environmental, employment or other socio-economic indicators, it is useful to assess the driving forces or determinants that underlie these changes. Two techniques for decomposing indicator changes at the sector level are structural decomposition analysis (SDA) and index decomposition analysis (IDA). For example, SDA and IDA have been used to analyze changes in indicators such as energy use, CO2-emissions, labor demand and value added. The changes in these variables are decomposed into determinants such as technological, demand, and structural effects. SDA uses information from input–output tables while IDA uses aggregate data at the sector-level. The two methods have developed quite independently, which has resulted in each method being characterized by specific, unique techniques and approaches. This paper has three aims. First, the similarities and differences between the two approaches are summarized. Second, the possibility of transferring specific techniques and indices is explored. Finally, a numerical example is used to illustrate differences between the two approaches.
Article
Utilization of carbon dioxide (CO2) has become an important global issue due to the significant and continuous rise in atmospheric CO2 concentrations, accelerated growth in the consumption of carbon-based energy worldwide, depletion of carbon-based energy resources, and low efficiency in current energy systems. The barriers for CO2 utilization include: (1) costs of CO2 capture, separation, purification, and transportation to user site; (2) energy requirements of CO2 chemical conversion (plus source and cost of co-reactants); (3) market size limitations, little investment-incentives and lack of industrial commitments for enhancing CO2-based chemicals; and (4) the lack of socio-economical driving forces. The strategic objectives may include: (1) use CO2 for environmentally-benign physical and chemical processing that adds value to the process; (2) use CO2 to produce industrially useful chemicals and materials that adds value to the products; (3) use CO2 as a beneficial fluid for processing or as a medium for energy recovery and emission reduction; and (4) use CO2 recycling involving renewable sources of energy to conserve carbon resources for sustainable development. The approaches for enhancing CO2 utilization may include one or more of the following: (1) for applications that do not require pure CO2, develop effective processes for using the CO2-concentrated flue gas from industrial plants or CO2-rich resources without CO2 separation; (2) for applications that need pure CO2, develop more efficient and less-energy intensive processes for separation of CO2 selectively without the negative impacts of co-existing gases such as H2O, O2, and N2; (3) replace a hazardous or less-effective substance in existing processes with CO2 as an alternate medium or solvent or co-reactant or a combination of them; (4) make use of CO2 based on the unique physical properties as supercritical fluid or as either solvent or anti-solvent; (5) use CO2 based on the unique chemical properties for CO2 to be incorporated with high ‘atom efficiency’ such as carboxylation and carbonate synthesis; (6) produce useful chemicals and materials using CO2 as a reactant or feedstock; (7) use CO2 for energy recovery while reducing its emissions to the atmosphere by sequestration; (8) recycle CO2 as C-source for chemicals and fuels using renewable sources of energy; and (9) convert CO2 under either bio-chemical or geologic-formation conditions into “new fossil” energies. Several cases are discussed in more detail. The first example is tri-reforming of methane versus the well-known CO2 reforming over transition metal catalysts such as supported Ni catalysts. Using CO2 along with H2O and O2 in flue gases of power plants without separation, tri-reforming is a synergetic combination of CO2 reforming, steam reforming and partial oxidation and it can eliminate carbon deposition problem and produces syngas with desired H2/CO ratios for industrial applications. The second example is a CO2 “molecular basket” as CO2-selective high-capacity adsorbent which was developed using mesoporous molecular sieve MCM-41 and polyethylenimine (PEI). The MCM41-PEI adsorbent has higher adsorption capacity than either PEI or MCM-41 alone and can be used as highly CO2-selective adsorbent for gas mixtures without the pre-removal of moisture because it even enhances CO2 adsorption capacity. The third example is synthesis of dimethyl carbonate using CO2 and methanol, which demonstrates the environmental benefit of avoiding toxic phosgene and a processing advantage. The fourth example is the application of supercritical CO2 for extraction and for chemical processing where CO2 is either a solvent or a co-reactant, or both. The CO2 utilization contributes to enhancing sustainability, since various chemicals, materials, and fuels can be synthesized using CO2, which should be a sustainable way in the long term when renewable sources of energy are used as energy input.
Article
Energy and the environment are two of the most important issues this century. More than 80 % of our energy comes from the combustion of fossil fuels, which will still remain the dominant energy source for years to come. It is agreed that carbon dioxide produced from the combustion process to be the most important anthropogenic greenhouse gas leading to global warming. Atmospheric CO(2) concentrations have indeed increased by almost 100 ppm since their pre-industrial level, reaching 384 ppm in 2007 with a total annual emission of over 35 Gt. Prompt global action to resolve the CO(2) crisis is therefore needed. To pursue such an action, we are urged to save energy without the unnecessary production of carbon emissions and to use energy in more efficient ways, but alternative methods to mitigate the greenhouse gas have to be considered. This Minireview highlights some recent promising research activities and their prospects in the areas of carbon capture and storage and chemical fixation of CO(2) in constructing a future low-carbon global economy with reference to energy source, thermodynamic considerations, net carbon emissions and availability of reagents.
Article
Few industrial processes utilize carbon dioxide as a raw material because it is the most oxidized state of carbon with a low energy level. However, using CO2 as a raw material do not necessarily help mitigate the greenhouse effect, although it is a green chemical reagent in many cases. The significance of the transformation of CO2 into useful chemicals should be attributed to the importance of utilizing a renewable feedstock. There are four methodologies to transform CO2 into useful chemicals: (i) using high-energy starting materials such as hydrogen, unsaturated compounds, small-membered ring compounds, and organometallics; (ii) choosing oxidized low-energy synthetic targets; (iii) shifting the equilibrium to the product side by removing a particular compound; and (iv) supplying physical energy such as light or energy. It is important to execute research on CO2 to increase the number of industrial applications by improving reactions for commercialization, to improve reactions with low catalytic performance, to establish foundations for science to research for new reactions and new catalysts, and to elucidate reaction mechanisms at the molecular level.
Article
The need to reduce the accumulation of CO(2) into the atmosphere requires new technologies able to reduce the CO(2) emission. The utilization of CO(2) as a building block may represent an interesting approach to synthetic methodologies less intensive in carbon and energy. In this paper the general properties of carbon dioxide and its interaction with metal centres is first considered. The potential of carbon dioxide as a raw material in the synthesis of chemicals such as carboxylates, carbonates, carbamates is then discussed. The utilization of CO(2) as source of carbon for the synthesis of fuels or other C(1) molecules such as formic acid and methanol is also described and the conditions for its implementation are outlined. A comparison of chemical and biotechnological conversion routes of CO(2) is made and the barriers to their exploitation are highlighted.
Carbon emission deduction model and application base on production function theory
  • Wu
Together development of ‘methanol economy’and ‘hydrogen economy’driven by CO2 utilization
  • Wang