Effect of hydrogen concentration on the explosion severity in a closed vessel / (Record no. 7636)

MARC details
000 -LEADER
fixed length control field 03731ntm a2200373 i 4500
001 - CONTROL NUMBER
control field vtls000102872
003 - CONTROL NUMBER IDENTIFIER
control field KUKTEM
005 - DATE AND TIME OF LATEST TRANSACTION
control field 20251117113357.0
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 180130t20172016my da f a m 000 0 eng d
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number THE0000818(Local)
039 #9 - LEVEL OF BIBLIOGRAPHIC CONTROL AND CODING DETAIL [OBSOLETE]
Level of rules in bibliographic description 201905271156
Level of effort used to assign nonsubject heading access points nazirah
Level of effort used to assign subject headings 201802081559
Level of effort used to assign classification fateeha
-- 201801301045
-- fateeha
040 ## - CATALOGING SOURCE
Original cataloging agency UMP
Language of cataloging eng
Transcribing agency UMP
Description conventions rda
090 ## - LOCALLY ASSIGNED LC-TYPE CALL NUMBER (OCLC); LOCAL CALL NUMBER (RLIN)
Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) FKKSA .A33 2017 r Bc.
100 0# - MAIN ENTRY--PERSONAL NAME
Personal name Mohd Aidil Awaluddin,
Relator term author.
245 10 - TITLE STATEMENT
Title Effect of hydrogen concentration on the explosion severity in a closed vessel /
Statement of responsibility, etc. Mohd Aidil Awaluddin
264 #1 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE
Place of production, publication, distribution, manufacture Kuantan, Pahang :
Name of producer, publisher, distributor, manufacturer UMP,
Date of production, publication, distribution, manufacture, or copyright notice 2017
264 #4 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE
Date of production, publication, distribution, manufacture, or copyright notice © 2016
300 ## - PHYSICAL DESCRIPTION
Extent xiii, 41 pages :
Other physical details illustrations (some color), charts ;
Dimensions 30 cm. +
Accompanying material 1 CD-ROM
336 ## - CONTENT TYPE
Content type term text
Source rdacontent
336 ## - CONTENT TYPE
Content type term text
Source rdacontent
337 ## - MEDIA TYPE
Media type term unmediated
Source rdamedia
337 ## - MEDIA TYPE
Media type term computer
Source rdamedia
338 ## - CARRIER TYPE
Carrier type term volume
Source rdacarrier
338 ## - CARRIER TYPE
Carrier type term computer dics
Source rdacarrier
347 ## - DIGITAL FILE CHARACTERISTICS
File type text file
Encoding format PDF
Source rda
500 ## - GENERAL NOTE
General note Faculty of Chemical & Natural Resources Engineering
502 ## - DISSERTATION NOTE
Dissertation note Project Paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2017
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc. note Includes bibliographical references
520 3# - SUMMARY, ETC.
Summary, etc. Hydrogen gas can be produced from steam reforming natural gas, and steam gasification process. Hydrogen is widely used for producing ammonia for fertilizer, petroleum refining, glass purification and many others application. Through the rapid discoveries for the hydrogen production, this lead to the severity of hydrogen explosion phenomenon and tough safety precautions in term of quantitative and qualitative were required. Thus, this study will discover the severity limit of hydrogen explosion. The objectives in this study are to know the maximum rate of pressure rise (dp/dt)max, maximum explosion pressure (Pmax), and to study the explosion in different vessel shapes. Pure hydrogen (99.9%) was used as the fuel and mix with air. The experiment were conducted in a 20-L spherical bomb with hydrogen content in air at 30% v/v and different equivalence ratio from Ø = 0.4 to 1 in Combustion Laboratory, Faculty of Chemical Engineering, Universiti Malaysia Pahang with two igniters of 10kJ at the centre of the vessel. The experiment was repeated three times to get the fit result. From the result obtained the maximum explosion pressure, Pmax and rate of pressure rise, dP/dt increase with increase of hydrogen concentration in air. This is due to the increase amount of fuel and more chemical reaction happened during the explosion. Higher explosion parameters were happened at stoichiometry concentration or at equivalence ratio 1 with Pmax 5.4 bar and dP/dt 1410.3 bar/s. In comparison between spherical and 2-in pipe and 4-in pipe, the 2-in pipe has higher explosion pressure of 9.1 bar at equivalence ratio 1. This is due to the quenching effect in larger diameter (0.1 m in 4-in pipe and 0.34 m in spherical vessel) plays a significant role on the explosion pressure development. Different result obtained on rate of pressure rise, dP/dt in these three vessel shapes. Explosion in the spherical vessel tends to have higher value of dP/dt at 1410.3 bar/s. High dP/dt means amount of burning rate and pressure generation to be released from the explosion is has severe condition. Thus this concluded that hydrogen-air mixture explosion is more severe in spherical vessel compare to explosion in cylindrical vessel.
610 20 - SUBJECT ADDED ENTRY--CORPORATE NAME
Corporate name or jurisdiction name as entry element Faculty of Chemical & Natural Resources Engineering
General subdivision Dissertations
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Universities and Colleges
General subdivision Dissertations
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Theses
Holdings
Withdrawn status Lost status Damaged status Not for loan Home library Current library Date acquired Total checkouts Full call number Barcode Date last seen Copy number Price effective from Koha item type
  Not lost   Not for loan UMPLIB GAMBANG UMPLIB GAMBANG 04/09/2019   FKKSA .A33 2017 r Bc. 0000122236 04/09/2019 1 04/09/2019 Final Year Report
  Not lost   Not for loan UMPLIB GAMBANG UMPLIB GAMBANG 04/09/2019   CD 11198 | FKKSA .A33 2017 r Bc. 0000122237 04/09/2019 1 04/09/2019 Final Year Report

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