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- The Rutgers Ecocomplex and Bio-Reactor landfill produces what fuel A. Biodiesel B. solid waste fuel C. Pyrolysis D. MethaneTwo-hundred fifty pounds per hour of iron pyrites containing 90% FeS2 and 10% gangue are burned with 20% excess air based on conversion to SO3. The cinder discharged from the burner contains no sulfur. No conversion to SO3 occurs in the burner. The burner gas is passed through a converter which effects a 98% conversion of SO2 to SO3. The converter gas is passed to an absorber where all the SO3 is absorbed by 80% H2SO4 solution, which becomes 100% H2SO4 solution in the process. Establish a basis of one hundred pounds of iron pyrites Calculate: (a) the burner gas analysis, (b) the converter gas analysis, (c) pounds of 100% H2SO4 produced per 24-h day, if waste gas analyzes 0.19% SO2, 4.14% O2 and 95.67% N2Fluid catalytic cracking (FCC) offers an excellent integration of the cracking reactor and the catalyst regenerator that provides the highest thermal efficiency. Explain this integrated system that facilitates the fluid catalytic cracking of gas oil. Please assist your explanation by sketching the side by side FCC unit
- Methanol (CH3OH) is produced in the reaction of carbon dioxide and hydrogen via the reaction and process given below: CO2+3H2→CH3OH+H2O The fresh feed to the process contains hydrogen, carbon dioxide, and 0.400 mol% inerts (I). The reactor effluent passes through a condenser that removes essentially all of the methanol and water formed and none of the reactants or inerts. The unreacted reactants and inerts are recycled to the reactor. To avoid buildup of the inerts in the system, a purge stream is withdrawn from the recycle. 100 mol/h of feed to the reactor (not the fresh feed to the process) contains 29.5 mol% CO2, 68.0 mol% H2, and 2.50 mol% inerts. The single-pass conversion of hydrogen is 46.71%. What is the recycle-to-fresh feed ratio?Balance each of the chemical equations shown below. Be sure to include values of 1 for any species that only have 1 equivalent involved in the reaction (i.e. empty inputs DO NOT correspond to the value "1"). Use integers for ALL coefficients.Here's the link https://www.youtube.com/watch?v=wY3ey4E-FRA
- SUBJECTS Log In Science Chemistry question & answer Mat Hender Asked 1yr ago. About 75 percent of hydrogen for industrial use is produced by the steam-reforming process. This process is carried out in two stages called primary and secondary reforming. In the primary stage, a mixture of steam and methane at about 30 atm is heated over a nickel catalyst at 800 degree C to give hydrogen and carbon monoxide: CH4 (g) + H2O (g) <=> CO (g) + 3 H2 (g) ; ΔH = 206 kJ/mol The secondary stage is carried out at about 1000 degree C, in the presence of air, to convert the remaining methane to hydrogen:CH4 (g) + (1/2) O2 (g) <=> CO (g) + 2 H2 (g) ; ΔH = 35.7 kJ/mol (a) What conditions of…Please answer the sub-units thank you!Methane (CH4) burns completely with 100% excess air in a steady-flow combustion process. Those entering and leaving the combustion process are at 25 C temperature and 1 atmosphere pressure, and the water between the end products of combustion is in the liquid phase. Calculate the heat transfer during the combustion process.
- Combustion of a 1.450 g sample of glucose yielded 23.01 KJ of heat. The calorimeter contained 1.900 kg of water; the bomb constant was 5378 J/degree C; the initial temperature of the bomb and the water was 22.45 degrees C. Predict the final temp of the system.Show complete solution. Box all final answers. Basis: 100 kmols of Burner gas (BG) See attached photos for possible answers.1 mol propane (C3H8) and stoichiometric amount of oxygen (O2) needed to combust propane was preheated to 400 K. After combustion, the products released are at 1500 K. The combustion products are H2O(l) and CO2(g). With 100% conversion was achieved, estimate the total heat released. Calculate the heat requirement for a reactor in combusting 1 mol of methane, CH4, with 25% excess air until the products reach a temperature of 1000 K. The reactants entered the reactor at 298.15 K and 100% conversion of methane is achieved. Assume air is approximately 21% O2 and 79% N2 and products are H2O(l) and CO2(g). Hint for both #1 and #2 – Combustion products at 298 K is CO2(g) and H2O(l). If the exiting temperature is above 373.15 K, H2O will leave as H2O(g). Therefore, you should account for the phase change of H2O(l) to H2O(g).