Wastewater Treatment by Ozone for Reuse in Arid Climates (M.Sc. Thesis) (Record no. 341923)

MARC details
000 -LEADER
fixed length control field 03982nam a2200181Ia 4500
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 031212s1987||||xx |||||||||||||| ||eng||
041 ## - LANGUAGE CODE
Language code of text/sound track or separate title English
082 ## - DEWEY DECIMAL CLASSIFICATION NUMBER
Classification number 628.1662378242
Item number ALA
100 ## - MAIN ENTRY--PERSONAL NAME
Relator term author
Personal name Al-Ahwal, Mohammad Shahin
9 (RLIN) 67261
245 #0 - TITLE STATEMENT
Title Wastewater Treatment by Ozone for Reuse in Arid Climates (M.Sc. Thesis)
260 ## - PUBLICATION, DISTRIBUTION, ETC.
Place of publication, distribution, etc. Jeddah :
Name of publisher, distributor, etc. College of Engineering King Abdul Aziz University,
Date of publication, distribution, etc. c1987
300 ## - PHYSICAL DESCRIPTION
Extent xxiii, 271 p.
Other physical details : ill
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc. note Includes Bibliographical References
520 ## - SUMMARY, ETC.
Summary, etc. Abstract:<br/><br/>The feasibility of ozone treatment of secondary wastewater effluent in arid climets was studied, using continuous flow and batch ozonation systems. Raw and secondary treated (prior to chlorination) wastewater was collected from “Al-Khomra ‘ sewage treatment plant in Jeddah, Saudi Arabia. A U-tube system of ozone contactor which was the most effective ozone absorption system was indicated in the literature was used in this study.<br/>Optimization of ozone dosages was carried out using different ozone dosages ranged from 4.8 to 10.55 mg/L, during batch ozonation. The optimum ozone dosage of 10.55 mg/L was used to study the ozone treatment efficiencies for different wastewater temperatures ranged from 20 to 42° C and different ozone contact times ranged from 0 to 100 minutes. <br/>The ozone treatment efficiencies were measured in terms of BOD, COD, Tss, T. Coliform, and Ammonia, pH values, residual ozone, and dissolved oxygen changes during the experiments The ranges of the removal efficiencies of the BOD5, COD, TSS, T. Coliform and ammonia, at 10.55 mg/L ozone dosage, wastewater temperature range from 20 to 42° C and at 100 minutes batch P ozonation, were 59 to 84.7%, 50 to 78%, 25.1 to 75.1%, 81.4 to 100%, and -18 to 39 % respectively. The higher the wastewater temperature the lower BOD, COD, T. Coliform removal efficiencies, and the higher TSS and ammonia<br/>removal efficiencies. The higher ozone dosage and/or ozone contact time the higher removal efficiencies. Tracer tests were carried out to find out the dispersion numbers of the ozone contactor (ranged from 0.521 to 1.186).<br/>Mathematical equations were determined by applying linear, multi linear, and polynomial regression analysis (using computer programs) to the experimental data to show the relationship between the main parameters (BOD5, COD, TSS, T. Col. Ammonia and pH) and wastewater temperatures, ozone dosages, and ozone contact time. The goodness of fit for the equations of wastewater temperature, ozone dosage, and ozone contact time, with BOD, COD, T. Col. and TSS were high was very low (less than 0.6) for ammonia. The higher correlation coefficients were reported in this study, and the lower coefficients were neglected. <br/>The effect of batch ozonation on the reduction of various metals such as Fe, Mn, Ca, Mg, Na, K, Cu, Cd, Pb, and Zn was also studied, at different wastewater temperatures and ozone dosages. The metals analyzed during the experiments were Fe, Mn, Ca, Mg, Na, K, Cu, Cd, Pb, and Zn.<br/>Batch ozonation reduced the metal concentration from the wastewater Ozonation helps to release heavy metals from wastewater due to leaching action. The flocs formed by organic matter during batch ozonation, absorb or adsorb metal particles which settled after ozonation Cd, and pb could not be detected during this study because the concentration of these metals were very small or undetectable.<br/>The quality of the ozonated wastewater effluents was not high because of the poor quality of the unozonated effluents which can be considered as a primary treated effluents. The quality of the ozonated wastewater, by considering all parameters does not meet the Saudi standards without any farther treatment. But if the ozonation followed by filtration or carbon adsorption the quality of the wastewater will be better and it will meet the Saudi standards for direct discharge.<br/>
650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Ozone Treatment Thesis
9 (RLIN) 67259
650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Wastewater Treatment Thesis
9 (RLIN) 67260
942 ## - ADDED ENTRY ELEMENTS (KOHA)
Koha item type Masters Thesis
Source of classification or shelving scheme Dewey Decimal Classification
Holdings
Withdrawn status Lost status Source of classification or shelving scheme Damaged status Not for loan Home library Current library Shelving location Date acquired Stock Type Total Checkouts Full call number Barcode Date last seen Accession Date Koha item type
    Dewey Decimal Classification     Government Document Section Government Document Section Govt Publication Section 20/10/2022 Donation   628.1662378242 ALA 64532 20/10/2022 01/07/2002 Reference Collection