| 000 | 03728nas a2200385 4500 | ||
|---|---|---|---|
| 005 | 20260818095848.0 | ||
| 008 | 290998s1992 th r 000| eng d | ||
| 035 | _a.b10243458 | ||
| 099 | 9 | _aAIT Thesis no.ET-92-8 | |
| 100 | 0 | _aFu Xiaofeng | |
| 245 | 1 | 0 | _aEnergy management in corn alcohol distilleries in China |
| 260 |
_aBangkok : _bAsian Institute of Technology, _c1992 |
||
| 300 |
_a103 leaves : _bill. |
||
| 490 | 1 |
_aThesis ; _vno. ET-92-8 |
|
| 500 | _aA thesis submitted in partial fulfillment of the requirement for the degree of Master of Engineering | ||
| 502 | _aThesis (M.Eng.) - Asian Institute of Technology | ||
| 520 | _aThe energy consumption pattern in two corn alcohol distilleries in China, Liaoning Province, were investigated and analyzed. The electri city consumption was about 1 MJ e and steam consumption about 18.5 MJth per liter pure alcohol (1 p.a.) in bot h distilleries. Cooking and distillation consumed about 34 % and 56% of the total thermal energy , respectively. This study focused on analyzing the energy conservation potential of a) the vapor recompression cyc l e (VRC) system in distillation processes and b) biogas generated by anaerobic digestion of wastewaters (slops). As already mentioned, the largest energy consumer is distillation wit h a share of 56% (Longguan) and 57% (Shenyang) of the total energy consumption, respectively. A vapor recompression cycle system (heat pump), may reduce the total energy consumption (electricity+ steam) by 44% and 46%. Ass uming an initial investment of 18315$ (Longguan) and 27472$ (Shenyang), payback periods of about 3 and 4 years, respectively could be achieved. By applying the Contois kinetic model, the operating conditions of the existing HYBRID biogas plant were opt imi zed in regard to maximum volumetric me thane production rate (2 . 85 CH4 N m3/m3). The following conditions were proposed: HRT: 1.4 days, temperature: 40°C, substrate con centration: 23.4 CODo/l. If all the s lop (135 m3/d) would be treated, in Longgaun about 1,080 Nm3 CH4/d (about 8 Nm3 CH4/m3 slop) could be generated . This corresponds to 288 MJ/m3 slop at a slop : ethano l ratio of 14.71, to 4.23 MJ/l p.a.. The specific e n ergy consumption may replace 88% of the electricity consumpt ion. Actually, 38% of the slop is treated. Thus, the specific energy production from slop is 1.6 MJ/l p . a .. This could cover , at an energy conversion efficiency of 0.23 from methane to electricity. Only 36% of the electricity consumption could be replaced. And the energy bill will be reduced from 0 . 056 $/1 . p . a to 0.047 $/1 . p.a. (Longquan) and from 0.044 $/1.p.a . to 0 . 038 $/1.p.a. (Shenyang), respectively, calcu l ated with a e l ectricity cost 0.033 $/kWh. | ||
| 650 | 0 |
_aDistilleries _xEnergy concumption |
|
| 700 | 1 |
_aTentscher, Wolfgang, _eChairperson |
|
| 700 | 1 |
_aMora, J. A., _eExamination Committee |
|
| 700 | 1 |
_aYongping, Zhai, _eExamination Committee |
|
| 710 | 2 |
_aEEC, _eScholarship Donor |
|
| 810 | 2 |
_aAsian Institute of Technology. _tThesis ; _vno. ET-92-8 |
|
| 856 |
_3Full-Text _uhttp://203.159.5.9/ait-thesis/detail.php?q=B16250 |
||
| 907 |
_a.b10243458 _bmnait _cx |
||
| 902 | _a240401 | ||
| 998 |
_b2 _c951012 _dm _ea _fx _g0 |
||
| 945 | _lmnait | ||
| 945 | _lmnarc | ||
| 942 | _c22 | ||
| 942 | _c40 | ||
| 909 |
_aBarcode : 30050120386817 _bCREATED : 2012-09-21 _cRECORD # : i12766380 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 1 _iTOT CHKOUT : 0 _jTOT RENEW : 0 |
||
| 909 |
_aBarcode : 30050120367783 _bCREATED : 2016-08-06 _cRECORD # : i13024279 _dLPATRON : 0 _eLCHKIN : - _f# RENEWALS : 0 _g# OVERDUE : 0 _hIUSE3 : 0 _iTOT CHKOUT : 0 _jTOT RENEW : 0 |
||
| 999 |
_c37527 _d37527 |
||