레포트 (60)
[반응공학] 암모니아 합성(Ammonia synthesis)영문
Chemical Reactors Whit Heat Integration, Ph.D thesis, 1995.④ S. S. Elnashaie, M. E. Abashar And A. S. Al. Ubaid, Simulation and Optimization of an Industrial Ammonia Reactor, Ind. Eng, chem Res, Vol. 27,pp. 2015, 1988.⑤ D.C. Dyson and J.M. Sicon. A Kinetic Expression With Diffusion Correction for Ammonia⑥ Synthesis on Industrial Catalyst, Ind. Eng. Chem. Fundamental, Vol. 7, No. 4
15페이지 | 1,400원 | 2009.08.27
exchanger for the maintenance of the optimum temperature during the fermentation process.The typical operation mode in industrial submerged cultures is semi-continuous (Fig.4). This operation consists of the development of successive discontinuous cycles of acetification. At the end of every cycle, a given volume of acetic acid is discharged and refilled with mash. The best temperature for in
35페이지 | 2,500원 | 2012.07.25
[공학] Stimuli-Responsive Interface Structure(영문)
Chemical and conformationalchanges in PAA that occurwith changes in pHare responsible for this behavior.For cellulose whiskers, this involves the formation of a homogeneous aqueouswhisker dispersion, followed by gelation through solvent exchange with awatermisciblesolvent18. The whisker content of the gels can be controlled by theconcentration of the initial whisker dispersion, the ratio of
10페이지 | 1,200원 | 2012.07.10
[생명공학] 논문 요약-The Other Aspects of Algae-Derived Biofuel, Bioethanol(영문)
Chemical3. SaccharificationA. IntroductionB. Methodsi. Physiochemicalii. Enzymaticiii. Biologicaliii. Biological4.1 Yeast4.1.1 Saccharomyces cerevisiae4.1.2 Other yeast strains4.2 Zymomonas mobilis4.3 Zymobacter palmae4.4 Recombinant E.coli5. Separation and purification of ethanol from yeast5.1 Ethanol and water partitioning performance5.2 Solvent retention in the aqueous phase 5
26페이지 | 2,700원 | 2012.03.13