000			05926cas|a2200409 i 4500
005			20260818114820.0
008			170699s1996 th uzm rtt 00| a1eng d
035			_a.b11616192
099		9	_aAIT Diss no.ET-96-03
100	0		_aBui Tuyen
245	1	0	_aGasification of wood : _ba multi-stage approach
260			_aBangkok : _bAsian Institute of Technology, _c1996
300			_a113 leaves
490	1		_aDissertation ; _vno. ET-96-03
500			_aA dissertation submitted in partial fulfillment requirements for the Degree of Doctor of Engineering, School of Environment, Resources and Development
502			_aThesis (Ph.D.) - Asian Institute of Technology, 1996
520			_aAn experimental and theoretical investigation of the combustion of wood, as a single piece in air and a packed bed of pieces in a downdraft flaming pyrolysis reactor, was conducted. The results have been integrated and embodied in a multi-stage gasifier which, as the experimental tests showed, has better performance characteristics than conventional gasifiers regarding to the tar content and gas composition. The tar contamination of producer gas from conventional downdraft wood gasifiers, a recurrent headache for gasifier designers, has been identified as unavoidable because oxygen is completely consumed long before the wood pieces are completely devolatized. In a multi-stage gasifier flaming pyrolysis process is conducted in a separate reactor section, the first stage of gasifier, until the solid is completely carbonized. Another subsequent reactor section, the second · stage, where a secondary air supply is provided, is used for combustion of the pyrolysis gas and gasification of the residual char. This stage develops another temperature peak and thus is able to crack any tar that might escape oxidation. The direct phenomenological connection of the flame existence and its appearance over wood with the surface gas flux (SGF) emitted from pyrolyzing wood was investigated. The minimum flame sustaining SGF, which can also serve as the pilot ignition threshold, was determined to be about 5x10·3 kg-m·2 -s·1 {u2022} The ranges of the SGF for stable-smokeless flames were found to be quite narrow: from 15x10· 3 to 50x10·3 kg-m·2 -s·1 {u2022} At higher values of the SGF the flame was smoky indicating that combustion was incomplete. Combustion of single wood pieces in air was studied. There was found some critical size, specimens smaller than which would be ignited, burn with a flame and, produce a carbonaceous residue. Thin pieces burned more easily than thick ones but the duration of flaming combustion depended on the specimen size. Pieces thicker than the critical size did not sustain a continuous flame until volatiles were depleted, showing the need to use wood in relatively small sizes for gasification in down draft gasifier to obtain low tar gas. The opposed flow flame spread upward in a packed bed of wood pieces was studied experimentally for downdraft mode using a transparent reactor made of high temperature glass. The lower limit of supply air superficial cold velocity at which flame extinguished and the upper limit when blow off occurred were found to be about 0.02 and 0.3 mis respectively. Flaming pyrolysis of the bed was possible only at air supply within these limits. In the flame supporting air supply range, the flame spread rates were experimentally measured. Based on the knowledge gained from studies on combustion of single particle and packed bed, a multi-stage gasifier was constructed and tested. Basic conditions for successful operation of a multi-stage gasifier are favorable fuel size, air flow rate to maintain the flaming pyrolysis in the first stage and, appropriate distance between primary and secondary air supplies to ensure a sufficiently long residence time for complete wood devolatilization before the secondary air supply. Also, a proper amount of air need to be supplied to the second stage to raise temperature again; however, the solid consumption in the second stage should not cause a solid flow exceeding the opposed flow flame spread rate in the first stage. Under the optimal operation, a two-stage gasifier produced gas with tar content around 50 mg/Nm3 , about 80 times less than -ii- the best results that could be obtained with the similar size gasifier operating in conventional one-stage configuration. A one-dimensional mathematical model of a two-stage wood gasifier was developed for steady ;state operation. The numerical solution correctly predicts behavior of the gasifier qualitatively: two temperature peaks were developed, the first peak corresponded to the flame front in the first stage and the second peak was due to combustion in the second stage.
650		0	_aWood _xCombustion
700	1		_aBhattacharya, Sribas C., _eChairperson
700	1		_aLoof, Rainer, _eExamination Committee
700	0		_aSurapong Chiraratananon, _eExamination Committee
700	1		_aMartin, J., _eExamination committee
710	2		_aAsian Institute of Technology, _eScholarship donor
710	2		_aThe Government of Germany through the Deutsche, _eScholarship donor
810	2		_aAsian Institute of Technology. _tDisertation ; _vno. ET-96-03
856			_3Full-Text _u http://203.159.5.9/ait-thesis/detail.php?q=B14651
907			_a.b11616192 _bmnait _cy
902			_a240401
998			_b0 _c970724 _dm _ea _fy _g0
945			_lmnait
945			_lmnarc
942			_c22
942			_c40
909			_aBarcode : 30050120557409 _bCREATED : 2012-08-16 _cRECORD # : i12687170 _dLPATRON : 1022454 _eLCHKIN : 2014-02-03 _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 1 _jTOT RENEW : 0
909			_aBarcode : 30050160037072 _bCREATED : 2016-01-25 _cRECORD # : i12873780 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 0 _jTOT RENEW : 0
999			_c48680 _d48680