Dissertations / Theses on the topic 'Design of flue-gas duct'
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Slíva, Karel. "Návrh dvoutlakého horizontálního kotle na odpadní teplo." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2016. http://www.nusl.cz/ntk/nusl-254297.
Full textMaršík, Jaroslav. "Dvoutlaký horizontální kotel na odpadní teplo (HRSG)." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2015. http://www.nusl.cz/ntk/nusl-232157.
Full textMed, Lukáš. "Návrh dvoutlakého horizontálního kotle na odpadní teplo." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2016. http://www.nusl.cz/ntk/nusl-241924.
Full textChang, Sen-min. "Preliminary investigation on flue gas desulfurization in an in-duct spray dryer using condensation aerosols." Ohio : Ohio University, 1991. http://www.ohiolink.edu/etd/view.cgi?ohiou1183659888.
Full textHavlíček, Tomáš. "Výpočet a dimenzování konstrukce přechodového vedení." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2008. http://www.nusl.cz/ntk/nusl-228209.
Full textNorman, Christian G. "Design of a bench scale apparatus for the evaluation of the gamma alumina flue gas desulfurizaton process." Ohio : Ohio University, 1985. http://www.ohiolink.edu/etd/view.cgi?ohiou1184071211.
Full textLatcham, Jacob G. (Jacob Greco). "Heat exchanger design for thermoelectric electricity generation from low temperature flue gas streams." Thesis, Massachusetts Institute of Technology, 2009. http://hdl.handle.net/1721.1/54513.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 33).
An air-to-oil heat exchanger was modeled and optimized for use in a system utilizing a thermoelectric generator to convert low grade waste heat in flue gas streams to electricity. The NTU-effectiveness method, exergy, and thermoelectric relations were used to guide the modeling process. The complete system design was optimized for cost using the net present value method. A number of finned-tube compact heat exchanger designs were evaluated for high heat transfer and low pressure loss. Heat exchanger designs were found to favor either power density or exergy effectiveness to achieve optimal net present value under different conditions. The model proved capable of generating complete thermoelectric flue gas systems with positive net present values using thermoelectric material with a ZT value of 0.8 and second law efficiency of 13%. Complete systems were generated for a number of economic conditions. The best complete system achieved a first law efficiency of 1.62% from a 1500 C flue gas stream at an installed cost of $0.79 per watt.
by Jacob G. Latcham.
S.B.
Norman, Christian G. III. "Design of a bench scale apparatus for the evaluation of the gamma alumina flue gas desulfurization process." Ohio University / OhioLINK, 1985. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1184071211.
Full textKornelius, Gerrit. "The design of electrostatically augmented moving bed granular gas filters." Pretoria : [s.n.], 2003. http://upetd.up.ac.za/thesis/available/etd-05052005-095030/.
Full textChernov, Gregory S. "Design and evaluation of a technological process for bio-sequestration of carbon dioxide from industrial flue gas emissions." Connect to resource, 2010. http://hdl.handle.net/1811/45461.
Full textToman, Filip. "Výpočet tepelné bilance využití latentního tepla spalin pomocí kondenzátoru." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2018. http://www.nusl.cz/ntk/nusl-378488.
Full textHan, Yang. "Facilitated Transport Membranes for Carbon Capture from Flue Gas and H2 Purification from Syngas: From Membrane Synthesis to Process Design." The Ohio State University, 2018. http://rave.ohiolink.edu/etdc/view?acc_num=osu1543333780761185.
Full textZaidullina, Liliia. "Návrh dvoutlakého vertikálního kotle na odpadní teplo za plynovou turbínou na zemní plyn." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2018. http://www.nusl.cz/ntk/nusl-378733.
Full textPauliny, Jan. "Navrh dvoutlakého horizontálního kotle na odpadní teplo (HRSG) za plynovou turbínou na zemní plyn." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2016. http://www.nusl.cz/ntk/nusl-254218.
Full textHradil, Lukáš. "Posouzení kotle na odpadní teplo." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2009. http://www.nusl.cz/ntk/nusl-228700.
Full textMüller, Jan. "Kondenzační technika a odvody spalin." Master's thesis, Vysoké učení technické v Brně. Fakulta stavební, 2014. http://www.nusl.cz/ntk/nusl-226844.
Full textKung, Yuan-Chi, and 龔元琪. "Simulation of CO2 Capture in Flue Gas from a Power Plant and Concentrating Syngas after Oxy-Fuel Combustion and Dehydration Combined with Design and Analysis of Simulation Experiments by Pressure Swing Adsorption Processes." Thesis, 2018. http://ndltd.ncl.edu.tw/handle/accyeb.
Full text國立中央大學
化學工程與材料工程學系
106
In order to reduce carbon dioxide emissions that worsen our environment continuously, we could concentrate CO2 and let it become the high value-added product to improve it. To validate the accuracy of PSA program, we verified the simulation with the experiment of 2-bed 6-step PSA process at first. Next, this study could be taken into 2 parts and both of them used UOP 13X zeolite as adorbent. The first part of study, a 3-bed 9-step pressure swing adsorption(PSA) process for flue gas after desulphurization and water removal (15% CO2, 85% N2) of subcritical coal-fired power plant was designed. After simulation, we obtained a bottom product CO2 purity at 89.94%, a recovery at 89.54% while at feed pressure 2.6 atm, vacuum pressure 0.05 atm, feed temperature 298.14 K, adsorption time 390 s, cocurrent time 40 s, vacuum time 300 s, and pressurization equilibrium time 50 s. Also, the calculation of energy consumption is important. The mechanical energy consumption was estimated to be 1.38 GJ/tonne-CO2. In the second part of this study, based on the syngas gas emission rate of a 1 kW power plant, a scaled up 15 MW PSA process was designed to capture CO2 with over 99.9% high concentration CO2 product. Since the syngas of a gasifier after oxy-fuel combustion and dehydration produces 95% - 97.4% CO2, we used 95% CO2 and 5% N2 as our inlet gas. After simulation, we obtained a bottom product CO2 purity at 99.999944%, a recovery at 9.574%, a top product N2 purity at 98.44%, and a recovery at 94.09% while at feed pressure 5 atm, vacuum pressure 0.238 atm, feed temperature 338.14 K, bed diameter 131.678 cm, and bed length 407 cm. The mechanical energy consumption was estimated to be 2.53 GJ/tonne-CO2. At last, in order to find the optimal operating conditions, we combined the results of 15 MW PSA process with design and analysis of simulation experiments. After analysis, we obtained a bottom product CO2 purity at 99.999984%, a recovery at 11.0525% while at feed pressure 5.3 atm, vacuum pressure 0.2 atm, feed temperature 343.14 K, and step 5/10/15/20 time 55 s as the optimal results. The mechanical energy consumption was estimated to be 2.33 GJ/tonne-CO2.