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Dissertations / Theses on the topic 'Design of flue-gas duct'

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1

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.

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The focus of this thesis is a proposal of a horizontal dual-pressure heat recovery steam generator. The introductory part includes thermal calculation, as well as a design of the layout and a design of the heat transfer surfaces and the layout of the boiler. Individual chapters are broken down according to the outline of the proposal for the arrangement of the heating surfaces, according to the parameters of the flue gas and steam. The master thesis contains a scheme of a real heat transfer temperature diagram and it also includes the calculation of connecting and downcomer pipes and drums. The final part describes the calculation of the boiler draft loss. The main idea of the thesis is accompanied by the technical documentation of the drawing of the boiler.
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2

Maršík, 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.

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The Master’s thesis dealing with design of heat recovery steam generator with two pressure levels is split into nine sections. The first section describes the design and the layout of HRSG. The second part deals with heat calculation. The third section deals with design of flue-gas duct. The fourth part describes designs of individual heating surfaces, including steam superheaters, vaporizers and economizer. Next section shows the real temperature diagram and choice of the materials. The seventh section describes the calculation of outer pipelines and the eighth part deals with the drums design. The last section deals with the calculation of draft loss of steam generator.
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3

Med, 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.

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This master's thesis deals with thermal calculation and design of proportions of calorific components of a heat recovery steam generator (HRSG), which is placed behind a combustion turbine, for given parameters of exhaust gases and requested parameters of steam. In the first chapters is described the design, layout of HRSG and the thermal calculation. The next parts deal with the design of flue-gas duct and each individual heating surface. Next section shows computations of dimensions of drums, flooding pipes, transferring pipes and all other outer pipes. The chosen materials are described in one of the last chapters and the last chapter deals with calculation of draft loss of steam generator.
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4

Chang, 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.

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5

Havlíček, 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.

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The goal of this thesis is to create a methodic and a system, which would involve customized computing and consequent design of the transition duct using input and applied data effectively and would achieve optimized set of parameters. The methodic described in the thesis is applied on transition duct within air main ducting between the filter and gas turbine. Transition duct is a huge mounted assembly consisting of welded parts. NX 5 application was chosen as system environment of the thesis. Master model is a root for both design model and computing model. Weight and material optimization is a desired result which will serve as basis for designing. It is not the goal of this thesis to create one perfect computation model BUT to create a methodic, which would be manageable by any designer equipped by basic knowledge of engineering.
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6

Norman, 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.

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7

Latcham, 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.

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Thesis (S.B.)--Massachusetts Institute of Technology, Dept. of Mechanical Engineering, 2009.
Cataloged 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.
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8

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.

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9

Kornelius, 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/.

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10

Chernov, 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.

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11

Toman, 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.

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Thesis is focused on calculation of the condenser of flue gas, which is created by burning of natural gas. In the first part is theoretical overview of equations describing film condensation and physical properties of the flue gas. The second part deals with practical thermal calculation of the specified condenser. In third part parametric study is done in which a tempature of cooling water at inlet and the coefficient of excess air are changed. The last part of the thesis is dedicated to geometric design of the flue gas condenser whose required power is 8 MW.
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12

Han, 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.

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13

Zaidullina, 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.

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This Master’s thesis focuses on the design of vertical heat recovery steam generators. This work focuses on three main objectives. The first objective is to describe the heat recovery steam generators, there basic principle and construction. The second focal objective is thermal calculation, design of heat tranfer surfaces and choice of materials. The third objective was to calculate the boiler loss, hydraulic calculation and subsequent design of the drum dimensions.
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14

Pauliny, 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.

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Tato diplomová práce se zabývá návrhem dvojtlakého horizontálního kotle využívající teplo spalin za spalovací turbínou na zemní plyn. Zahrnuje návrh a výpočet jednotlivých výměníků, jejich základní uspořádání s ohledem na požadované parametry výstupní páry a dané vstupní a výstupní parametry spalin. Dále tato práce zahrnuje výpočet a konstrukční návrh parních bubnů, zavodňovacích trubek a převáděcích potrubí. Tato práce je zakončena výpočtem a prověřením tlakových ztrát mezi vstupem a výstupem kotle. Důležitou součástí této práce je přiložena výkresová dokumentace.
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15

Hradil, 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.

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This theses work is concerned with assessment of transfer line exchanger behind pusher furnace. First part is describing technical characteristic and parametres. The most important part of this theses is thermic calculation of the boiler. Last following part is concerned with suggestions of constructional modifications of heating surface for proper functioning of boiler. These modifications are demonstrated by scheme in the enclosure.
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16

Müller, Jan. "Kondenzační technika a odvody spalin." Master's thesis, Vysoké učení technické v Brně. Fakulta stavební, 2014. http://www.nusl.cz/ntk/nusl-226844.

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This thesis is developed as a proposal for heating for a primary school and kindergarten in the region of Brno-countryside. For the insulated building, a combination of heating and air-conditioning is proposed. The concept is designed so that the air-conditioning preheats the exterior air and the heating system warms the incoming air to a comfortable temperature. For the required thermal performance, sources of heat (for gas and pellets) and a layout solution for the boiler room is designed. Drainage of combustion products is proposed for both solutions. The project solution is per the extent of the construction permit. The theoretical part is linked with the practical part through the condensation boilers, their function and division, and drainage of combustion products. The experiment for the given topic was conducted on the drainage of combustion products. The pressure loss of the reverse knob was determined in relation to the flow rate of air in the condensation boilers as this loss is essential in assessing the drainage of combustion products.
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17

Kung, 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.

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碩士
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.
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