Transesterification process to manufacture methyl ester of waste vegetable oil (Record no. 53526)

MARC details
000 -LEADER
fixed length control field 02649cab a2200277Ia 45 0
001 - CONTROL NUMBER
control field u201262
003 - CONTROL NUMBER IDENTIFIER
control field SIRSI
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 110706s2003 ua ss b eng d
040 ## - CATALOGING SOURCE
Original cataloging agency EAL
041 ## - LANGUAGE CODE
Language code of text/sound track or separate title eng
Language code of summary or abstract ara
090 ## - LOCALLY ASSIGNED LC-TYPE CALL NUMBER (OCLC); LOCAL CALL NUMBER (RLIN)
Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) ART MJAE V20 No4 SI 25
100 1# - MAIN ENTRY--PERSONAL NAME
Personal name Moussa, A. I.
240 10 - UNIFORM TITLE
Uniform title Misr journal of agricultural engineering, 2003 v.20 (4), Special issue
Medium [electronic resource]:
-- The 11th conference of Misr Society of Agricultural Engineering : Agricultural Engineering Roll in reducing losses and maximizing production, 15-16 October, 2003 (part 2).
245 10 - TITLE STATEMENT
Title Transesterification process to manufacture methyl ester of waste vegetable oil
Medium [electronic resource].
246 15 - VARYING FORM OF TITLE
Title proper/short title تصنيع الوقود الحيوي من الزيوت النبااتية المستعملة.
300 ## - PHYSICAL DESCRIPTION
Extent p.851-866.
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc. note Includes references.
520 ## - SUMMARY, ETC.
Summary, etc. Waste vegetable oils (WVO) can be transestrified to biodiesel for use as an alternative diesel fuel. You don't have to convert the engine to run it on biodiesel. The essential part of the process is the transesterification of waste vegetable oil with methano', in the presence of a catalyst, to yield the methyl ester of waste vegetable oil as a product and glycerin as a by-product. Experiments have been performed to deter-mine the optimum conditions for the preparation of biodiesel. The process varieties were. 1) oil to methanl ratio, 2) temperature 3) catalyst, 4) stirring time. The optimum conditions were: 1) oil to methanol ratio 5: 1 2) temperature of WVO 50°C. 3) the optimum amount of catalyst was 9.5 gm of sodium hydroxide to one liter of WVO gave a maximum conversion. 4) extremely vigorous agitation was not necessary after the reaction mixture became homogeneous (60 minute). Viscosity, viscosity index, cetane number pour point etc. of the biodiesel and WVO were measured. Engine tests have been carried out with the aim of measurements of torque, speed. fuel consumption, and compare the behavior of a diesel engine running on biodiesel with diesel fuel as a baseline. Fuel consumption was almost the same for diesel and biodiesel. Cost for the commercial production of biodiesel was found to be 0.53 LElliter at 20 % of biodiesel to diesel fuel. Costs are in 2003 Egyptian pound.
546 ## - LANGUAGE NOTE
Language note Summary in Arabic.
596 ## -
-- 1
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Vegetable oils as fuel.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Fuel.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Oils and fats.
773 0# - HOST ITEM ENTRY
Title Misr Journal of Agricultural Engineering, 2003 v.20 (4), Special issue, 15-16 October, 2003 (part 2).
Related parts 2003.v.20(4)SI
International Standard Serial Number 1687-384X
Control subfield nnas
Record control number u192786
856 40 - ELECTRONIC LOCATION AND ACCESS
Uniform Resource Identifier <a href="http://nile.enal.sci.eg/EALE/2003/MJAE/2003/4si/851.pdf">http://nile.enal.sci.eg/EALE/2003/MJAE/2003/4si/851.pdf</a>
Public note Full Text Article.
942 ## - ADDED ENTRY ELEMENTS (KOHA)
Koha item type Articles
Source of classification or shelving scheme Library of Congress Classification

No items available.


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