東華大學圖書館 |

語系: 繁體中文

說明(常見問題)

回圖書館首頁

手機版館藏查詢

登入

回首頁

切換: 標籤 | MARC模式 | ISBD

FindBook

Google Book

Amazon

博客來

Optimal Design of Intensified Processes.

紀錄類型:	書目-電子資源 : Monograph/item
正題名/作者:	Optimal Design of Intensified Processes./
作者:	Al-Duweesh, Farah M.
面頁冊數:	1 online resource (235 pages)
附註:	Source: Dissertations Abstracts International, Volume: 83-04, Section: B.
Contained By:	Dissertations Abstracts International83-04B.
標題:	Chemical engineering. -
電子資源:	http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=28767850click for full text (PQDT)
ISBN:	9798460437078

Optimal Design of Intensified Processes.
Al-Duweesh, Farah M.

Optimal Design of Intensified Processes. - 1 online resource (235 pages)

Source: Dissertations Abstracts International, Volume: 83-04, Section: B.

Thesis (Ph.D.)--University of California, Los Angeles, 2021.

Includes bibliographical references

Carbon and NOx emissions have been a major drawback in the industry of air pollution control. Monolith reactors have thrived from their effective use in reducing those air pollutants from both automotive and industrial power plants. This work focuses on the optimization of monolith reactor design by first developing a 3-D mathematical model for an isothermal, rectangular monolith reactor featuring first order irreversible volumetric and surface reactions. Then solving the species mass, continuity, momentum and heat balance equations necessary for each plug flow, fully developed laminar flow and developing fluid flow models, with a known inlet reactant mass fraction/concentration and volumetric flowrate. Finally, a systematic optimization algorithm technique is used depending on the fluid flow considered to optimize the non-convex optimization problem that aims for a maximum conversion subject to capital cost to production ratio and pumping/compression cost to production ratio that determines an upper bound on the fluid velocity. Comparison of results between each fluid flow model developed is discussed in each series.

Electronic reproduction.
Ann Arbor, Mich. :
ProQuest,
2023

Mode of access: World Wide Web

ISBN: 9798460437078Subjects--Topical Terms:

560457
Chemical engineering.
Subjects--Index Terms:

DesignIndex Terms--Genre/Form:

542853
Electronic books.

Optimal Design of Intensified Processes.
LDR:02422nmm a2200373K 4500 001 2359161
005 20230918120607.5
006 m o d
007 cr mn ---uuuuu
008 241011s2021 xx obm 000 0 eng d
020 $a 9798460437078
035 $a (MiAaPQ)AAI28767850
035 $a AAI28767850
040 $a MiAaPQ $b eng $c MiAaPQ $d NTU
100 1 $a Al-Duweesh, Farah M. $3 3699747
245 1 0 $a Optimal Design of Intensified Processes.
264 0 $c 2021
300 $a 1 online resource (235 pages)
336 $a text $b txt $2 rdacontent
337 $a computer $b c $2 rdamedia
338 $a online resource $b cr $2 rdacarrier
500 $a Source: Dissertations Abstracts International, Volume: 83-04, Section: B.
500 $a Advisor: Manousiouthakis, Vasilios I.
502 $a Thesis (Ph.D.)--University of California, Los Angeles, 2021.
504 $a Includes bibliographical references
520 $a Carbon and NOx emissions have been a major drawback in the industry of air pollution control. Monolith reactors have thrived from their effective use in reducing those air pollutants from both automotive and industrial power plants. This work focuses on the optimization of monolith reactor design by first developing a 3-D mathematical model for an isothermal, rectangular monolith reactor featuring first order irreversible volumetric and surface reactions. Then solving the species mass, continuity, momentum and heat balance equations necessary for each plug flow, fully developed laminar flow and developing fluid flow models, with a known inlet reactant mass fraction/concentration and volumetric flowrate. Finally, a systematic optimization algorithm technique is used depending on the fluid flow considered to optimize the non-convex optimization problem that aims for a maximum conversion subject to capital cost to production ratio and pumping/compression cost to production ratio that determines an upper bound on the fluid velocity. Comparison of results between each fluid flow model developed is discussed in each series.
533 $a Electronic reproduction. $b Ann Arbor, Mich. : $c ProQuest, $d 2023
538 $a Mode of access: World Wide Web
650 4 $a Chemical engineering. $3 560457
650 4 $a Mathematics. $3 515831
650 4 $a Atmospheric sciences. $3 3168354
653 $a Design
653 $a Optimization
653 $a Reaction kinetics
655 7 $a Electronic books. $2 lcsh $3 542853
690 $a 0542
690 $a 0405
690 $a 0725
710 2 $a ProQuest Information and Learning Co. $3 783688
710 2 $a University of California, Los Angeles. $b Chemical Engineering 0294. $3 2092146
773 0 $t Dissertations Abstracts International $g 83-04B.
856 4 0 $u http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=28767850 $z click for full text (PQDT)