Anaerobic Baffle Reactor (ABR) process for treating a slaughterhouse wastewater (Record no. 4339)

MARC details
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005 - DATE AND TIME OF LATEST TRANSACTION
control field 20260817162223.0
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 191197s1992 th uzm rtt 00| a1eng d
035 ## - SYSTEM CONTROL NUMBER
System control number .b11519368
099 #9 - LOCAL FREE-TEXT CALL NUMBER (OCLC)
Classification number AIT Diss. no. EV-92-1
100 0# - MAIN ENTRY--PERSONAL NAME
Personal name Praphon Kemmadamrong
245 10 - TITLE STATEMENT
Title Anaerobic Baffle Reactor (ABR) process for treating a slaughterhouse wastewater
260 ## - PUBLICATION, DISTRIBUTION, ETC.
Place of publication, distribution, etc. Bangkok :
Name of publisher, distributor, etc. Asian Institute of Technology,
Date of publication, distribution, etc. 1992
300 ## - PHYSICAL DESCRIPTION
Extent 189 leaves
490 1# - SERIES STATEMENT
Series statement Dissertation ;
Volume/sequential designation no. EV-92-1
500 ## - GENERAL NOTE
General note A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Engineering, School of Environment, Resources and Development
502 ## - DISSERTATION NOTE
Dissertation note Thesis (Ph.D.) - Asian Institute of Technology, 1992
520 ## - SUMMARY, ETC.
Summary, etc. Experiments on ABR were conducted to investigate its efficiency on organic carbon removal. Laboratory scale ABR units, made of PVC with dimensions of 0.25 x 0.15 x 0.32 m3 (width x depth x length), were used to treat the dissolved air flotation pre-treated slaughterhouse wastewater whose COD concentrations were 480 - 730 mg/L. The steady state performance was evaluated under organic loading rates (OLR) from 0.67 to 4.73 g COD/(L.d) and hydraulic retention time (HRT) of 2.5 to 26 h. The ABR was started up at an OLR of 0.67 g COD/(L.d) and at HRT of 26 h at ambient temperature (30 to 35' C during day time and 25 to 30' C during night time). The ABR unit was found to perform satisfactorily when operating from low OLR of 0.67 g COD/(L.d) up to 4.73 g COD/(L.d) at HRT of 2.5 h, in which the treatment efficiency of 75% was reached on a total COD basis and of 84% on a filtered COD basis. Based on COD mass balance in the ABR unit, sludge accumulation factor (Xacc) was in the range of 0.16 to 0.39 g VSS/g CODrcmovcd{u2022} and the conversion of COD removed into methane was in the range of 0.44 to 0.78 g CH4-COD/g CODrcmovcd· The sludge activities varied in the range of 0.066 to 0.293 kg CH4-COD/(kg VSS.d). Biagas produced contained 20 to 27% nitrogen, 69 to 73% methane and 2 to 4% carbon dioxide. Pilot-scale ABR experiments were conducted by using two or three upflow reactors in series. The results showed that between the OLR of 0.10 - 0.86 g COD/(L.d), the significant decrease of COD concentration within the first reactor was observed. The COD removal rates were found to increase from 0.09 to 0.66 g COD/(L.d) with increasing OLR from 0.10 to 0.86 g COD/(L.d); resulting in an average treatment efficiency of 77 -.86%. The results obtained from batch tests were used in computer simulation to determine the constant and reaction orders. The constant C of Compartments 1, 2, 3 and 4 were found to be 3.8x10- 7 , 1.9x10- 5 , 0.586 and 0.522, respectively and the reaction orders of Compartments 1, 2, 3 and 4 were 3.9, 3.1, 1 and 1, respectively. The finite difference method of the model coupling mass transfer into a biofloc with the reaction was applied to simulate the ABR performance. The model simulation of the laboratory-scale ABR process showed that the observed and predicted effluent dissolved COD concentrations agreed well between the OLR of 1.82 - 2.14 g COD/(L.d). (ii) The overall results obtained from this study have shown that ABR process is efficient for the treatment of slaughterhouse wastewater and compares favorably with other anaerobic systems.
650 10 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Sewage
General subdivision Purification
-- Biological treatment
700 0# - ADDED ENTRY--PERSONAL NAME
Personal name Chongrak Polprasert,
Relator term Chairperson
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Tran, Francis T.,
Relator term Co-Chairperson
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Verink, J.,
Relator term Examination Committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Mora, Jean-Claude,
Relator term Examination Committee
700 1# - ADDED ENTRY--PERSONAL NAME
Personal name Tyagi, R. D.,
Relator term Examination Committee
710 2# - ADDED ENTRY--CORPORATE NAME
Corporate name or jurisdiction name as entry element Royal Norwegian Government,
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 Dissertation ;
Volume/sequential designation no. EV-92-1
856 ## - ELECTRONIC LOCATION AND ACCESS
Materials specified Full-Text
Uniform Resource Identifier <a href="http://203.159.5.9/ait-thesis/detail.php?q=B16477">http://203.159.5.9/ait-thesis/detail.php?q=B16477</a>
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998 ## - LOCAL CONTROL INFORMATION (RLIN)
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Cataloger's initials, CIN (RLIN) 960708
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942 ## - ADDED ENTRY ELEMENTS (KOHA)
Koha item type 20-AIT Publication
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Koha item type 40-Archives
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      Available for Loans Asian Institute of Technology Library Asian Institute of Technology Library AIT Publications 17/08/2026   AIT Diss. no. EV-92-1 30050003058269 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   AIT Diss. no. EV-92-1 30050003058277 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   AIT Diss. no. EV-92-1 30050160004981 17/08/2026   17/08/2026 40-Archives
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