A biological activated carbon-sequencing batch reactor for the removal of phenols (Record no. 12359)

MARC details
000 -LEADER
fixed length control field 05908cas|a2200481 a 4500
005 - DATE AND TIME OF LATEST TRANSACTION
control field 20260817171456.0
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 091008s1999 th uu|m rtt 0| a1eng d
035 ## - SYSTEM CONTROL NUMBER
System control number .b11784970
099 #9 - LOCAL FREE-TEXT CALL NUMBER (OCLC)
Classification number AIT Diss. no.EV-99-7
100 0# - MAIN ENTRY--PERSONAL NAME
Personal name Soydoa Vinitnantharat
245 12 - TITLE STATEMENT
Title A biological activated carbon-sequencing batch reactor for the removal of phenols
260 ## - PUBLICATION, DISTRIBUTION, ETC.
Place of publication, distribution, etc. Bangkok :
Name of publisher, distributor, etc. Asian Institute of Technology,
Date of publication, distribution, etc. 1999
300 ## - PHYSICAL DESCRIPTION
Extent 200 leaves
490 1# - SERIES STATEMENT
Series statement Dissertation ;
Volume/sequential designation no. EV-99-7
500 ## - GENERAL NOTE
General note A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Technical Science, School of Environment, Resources and Development
502 ## - DISSERTATION NOTE
Dissertation note Thesis (Ph.D.) - Asian Institute of Technology, 1999
520 ## - SUMMARY, ETC.
Summary, etc. Tluee tasks were carried out to study the capability of the BAC process for the removal of phenol and 2,4-DCP as a sole carbon source. A lignite based GAC 20 x 30 mesh size was used in this study. The first task was conducted to identify the comparative roles of the major reactions to remove phenol and 2,4-DCP in the BAC system. The major reactions considered were activated carbon adsorption-desorption, biosorption and biodegradation. Freundlich isotherm analysis was used to compare the performance of each reaction. Removal of phenol by biodegradation and adsorption predominated over biosorption. Removal of 2,4-DCP by activated carbon adsorption was much higher than by biodegradation and biosorption. The adsorption capacity (Kads) of phenol and 2,4-DCP decreased from 25.04 and 43.75 mg/g in single solute to 18.95 and 22.18 mg/g in bisolute. In the presence of by-product, Kads of phenol and 2,4-DCP in single solute decreased whereas in bisolute, only Kads of phenol decreased. In the desorption experiment, a small fraction of sorbed compounds was reversible particularly, this was conspicuous in the case of 2,4-DCP. Desorption of sorbed compounds increased in the presence of by-product with which about 90 % of phenol could desorbed. As the second task, the treatability of a mixture of phenol and 2,4-DCP in the BAC SBR system was investigated and compared with the conventional SBR system. Experiments were conducted by increasing the influent concentration, varying SRTs, varying GAC dosages, and changing the operation schedule of the SBR process. The difference in effluent concentrations between BAC-SBR and SBR was high at short SRTs and enlarged by increasing influent organic strength. Among different GAC dosages, there was no obvious change in the specific removal rate but the removal efficiency increased as the GAC dosage increased. The removal of phenol and COD reached 94%, and it reached 96% for 2,4-DCP in the BAC-SBR with 0.7 g/l GAC and SRT of 3 days. Only 86% for phenol and 84% for 2,4-DCP as well as COD were removed in the SBR. The removal efficiency of phenols in the BAC-SBR and SBR systems were improved when the idle time increased. However, the effluent concentration of phenols from SBR was about two times higher than that from the BAC-SBR. As the third task, bioregeneration of GAC loaded with phenol and 2,4-DCP was investigated in a batch and the BAC-SBR system. Bioregeneration of 1 g/l of GAC showed that the sequential assimilation of desorbed compounds in the bulk solution could induce the successive desorption of sorbed compounds from GAC. From SEM observation, the microorganisms were seen to be mainly colonized on the outer surface of GAC and some of them were scattered on the inner parts of GAC. The Freundlich adsorption model was applied to predict the amount of adsorbate remaining after bioregeneration in the batch experiment and in the BAC-SBR. The Freundlich parameters obtained from the adsorption isotherm taking into account the by-product effect on the adsorption could predict the amount of phenols remaining on GAC with high consistency. In the BAC-SBR, lll bioregeneration increased as SRT increased. During the BAC-SBR operation, GAC could adsorb phenols in the fill period and bioregeneration started in the react period. Extending the idle period could enhance the bioregeneration and buffer capacity consequently to decrease the irreversible adsorption part on the GAC in the BAC-SBR.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Sewage
General subdivision Purification
-- Phenol removal
700 0# - ADDED ENTRY--PERSONAL NAME
Personal name Preeda Pakpian,
Relator term Chairperson
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Ha, Sung-Ryong,
Relator term Examination committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Ozaki, Hiroaki,
Relator term Examination committee
700 0# - ADDED ENTRY--PERSONAL NAME
Personal name Chongrak Polprasert,
Relator term Examination Committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Rakshit, Sudip Kumar,
Relator term Examination Committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Ishibashi, Yoshinobu,
Relator term Examination committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Shin, Hang-Sik,
Relator term Examination committee
710 2# - ADDED ENTRY--CORPORATE NAME
Corporate name or jurisdiction name as entry element Government of Japan,
Relator term Scholarship donor
810 2# - SERIES ADDED ENTRY--CORPORATE NAME
Corporate name or jurisdiction name as entry element Asian Institute of Technology.
Title of a work Thesis ;
Volume/sequential designation no. EV-99-7
856 ## - ELECTRONIC LOCATION AND ACCESS
Materials specified Full-Text
Uniform Resource Identifier <a href="http://203.159.5.9/ait-thesis/detail.php?q=B11917">http://203.159.5.9/ait-thesis/detail.php?q=B11917</a>
907 ## - LOCAL DATA ELEMENT G, LDG (RLIN)
a .b11784970
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a 240329
998 ## - LOCAL CONTROL INFORMATION (RLIN)
Operator's initials, OID (RLIN) 0
Cataloger's initials, CIN (RLIN) 000411
First date, FD (RLIN) m
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-- u
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945 ## - LOCAL PROCESSING INFORMATION (OCLC)
l mnait
945 ## - LOCAL PROCESSING INFORMATION (OCLC)
l mnait
945 ## - LOCAL PROCESSING INFORMATION (OCLC)
l mnarc
945 ## - LOCAL PROCESSING INFORMATION (OCLC)
l mnarc
942 ## - ADDED ENTRY ELEMENTS (KOHA)
Koha item type 20-AIT Publication
942 ## - ADDED ENTRY ELEMENTS (KOHA)
Koha item type 40-Archives
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CREATED CREATED : 2000-11-04
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      Available for Loans Asian Institute of Technology Library Asian Institute of Technology Library AIT Publications 17/08/2026 50.00   AIT Diss. no.EV-99-7 30050120556849 17/08/2026 1 17/08/2026 20-AIT Publication
      Available for Loans Asian Institute of Technology Library Asian Institute of Technology Library AIT Publications 17/08/2026 50.00   AIT Diss. no.EV-99-7 30050120556823 17/08/2026 2 17/08/2026 20-AIT Publication
      Available for Loans Asian Institute of Technology Library Asian Institute of Technology Library Archives 17/08/2026 50.03   AIT Diss. no.EV-99-7 30050120556856 17/08/2026 3 17/08/2026 20-AIT Publication
      Available for Loans Asian Institute of Technology Library Asian Institute of Technology Library Archives 17/08/2026     AIT Diss. no.EV-99-7 30050160004775 17/08/2026   17/08/2026 40-Archives
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