BIORREACTOR DE LECHO EMPACADO PDF

      No Comments on BIORREACTOR DE LECHO EMPACADO PDF

Se diseñaron los biorreactores, utilizando principios de similitud; para la producción del alcohol etílico, se diseñó un biorreactor del tipo Lecho Empacado . Inmovilización de levaduras en residuos lignocelulósicos para la producción de etanol en biorreactor de lecho empacado. En las fermentaciones realizadas en los biorreactores de lecho empacado con el biocatalizador (soporte + levaduras), se logró obtener un aumento en la.

Author: Arashira Vut
Country: Puerto Rico
Language: English (Spanish)
Genre: Marketing
Published (Last): 4 January 2013
Pages: 246
PDF File Size: 5.19 Mb
ePub File Size: 3.39 Mb
ISBN: 552-2-36559-992-4
Downloads: 74550
Price: Free* [*Free Regsitration Required]
Uploader: Bazuru

The results obtained in the continuous fermentations are significant if compared to the results obtained by other researchers [12]. The characterization made it possible to establish the microscopic structural differences between the four materials, as well as the differences in composition of lignin, cellulose, hemicelluloses and ash. We used a column Supelco gel CH with the following empacsdo Some of the disadvantages of these processes are: The kinectics of the immobilized cells was determined during 12 h in a batch fermentation with an initial amount of cells of 0.

However, despite this fact, it was found out that the absorption of sugars reaches a saturation point beyond which no absorption occurs and the concentration of sugars in the culture medium is kept constant.

For the continuous process, we used a time of residence of 3 h and a biorreactof of 1. Prior to the start of the continuous process, we performed a batch stage of 12 h. The choice of the carrier sizes and flow rates for immobilization in fermentation conditions within the studied ranges can be made by considering the best operating conditions. Most of these mechanisms are spontaneously generated enpacado contact between cells and carrier, so adsorption is one of the simplest mechanisms to perform, both in a laboratory and industrial level.

It has greatly contributed to the development of this research. El RT se compone de un vaso de precipitados de vidrio de ml. Biology of Microbial Communities – Interview. You must be signed in to post a comment.

Ajuste de mezcla de velocidad en un entorno necesario para establecer una frontera clara algas dentro del reactor Figura biorreacgor ; la zona de la biomasa de algas debe ser de aproximadamente cm de altura. The proposed hypothesis is that these materials are appropriate matrices for the immobilization of yeast cells, which allow high cellular activity, lasting stability and they enable continuous operation for the production of ethanol.

  LA MARCHA DE LA LOCURA BARBARA TUCHMAN EPUB DOWNLOAD

Please recommend JoVE to your librarian. Dyna, 73, We evaluated four different waste lignocellulosic materials: In order to confirm immobilization and determine the differences between the carriers, we obtained images by scanning electronic microscopy SEM. After drying, they were weighed again. System Setup and Basic Operation …. The fermentation time of 12 h.

Biotechnology and Bioengineering 64, pp. Skip to content Bioengineering.

Copy of biorreactor de lecho empacado by judith galvan bautista on Prezi

Some features of this site may not work without it. En un matraz aforado de 1 L, se disuelven 72, g de nitrato de potasio en aproximadamente ml de agua desionizada.

Although in this process high temperatures are applied to reduce significantly the initial microbial load of materials, we found the need of sterilization before they were used in the immobilization. However, this method of immobilization is not too viable on an industrial scale, due to the high cost of raw material and the relative complexity of preparation of the biocatalysts carrier-cell with respect to the operative lifetime of the process [4,21,14].

Analytic methods The total sugar quantification was performed by the DNS Dinitrosalicylic acid colorimetric method. As an alternative, continuous processes are brought up, which can reduce production costs, improve process efficiency and increase ethanol yield.

Un biorreactor Novela de alta densidad de cultivo de diversas comunidades microbianas

For the development of the protocol three solutions were evaluated: The baseline immobilization was performed by following the yeast immobilization protocol. The maximum theoretical biorrwactor of sucrose to ethanol is 0. The cellulosic materials are regenerable, reusable, sterilizable on heat, biologically and chemically stable under different fermentation conditions and with adequate mechanical resistance [18].

In the last two decades there has been an increase of research focused on developing new technologies for ethanol production from renewable sources, and the efforts have focused biorteactor the development of much more efficient production processes [1- 3].

Differences in yield may result from variations in the microenvironmental rmpacado generated within the bioreactor, probably caused by the particular characteristics of each carrier [19].

We have also established that the glucose syrup obtained from the enzymatic hydrolysis of cassava flour can be used as an alternative substrate in alcoholic fermentations.

  10 JURUS TERLARANG PDF

This indicates the potential that glucose syrup has as an alternative substrate for ethanol empacdao. For the wood shaving, the amount of immobilized biomass was obtained with a flow of 3.

Your institution must subscribe to JoVE’s Bioengineering section to access this content. Fill out the form below to receive a free trial or learn more about access: The amount of immobilized biomass was established by the modified dry-weight technique [9].

Show full item record. These results indicate that, despite of the total biorreaftor of sugars at the end of fermentation, not all of them were converted to ethanol. The ethanol concentration was determined by HPLC, by analyzing samples of the effluent of the reactors. To establish which of these mechanisms were involved in immobilization biorreacctor the lignocellulosic materials used, it is necessary to study each of these characteristics.

Carriers for immobilization The lignocellulosic waste used were wood shaving, cane bagasse, corn leave, and corn cob, which were obtained from some agro industries in the region. Immobilization yeasts cells, bioethanol, biofuels, lignocellulosic carriers, continuous fermentation. For the production of ethylic alcohol was designed a packed bed bioreactor, which was used for the fermentation of immobilized cells of Saccharomyce Cerevisae, microorganism that produced of ethylic alcohol and were it cultivated in Agar Saboraud produces pellets that were used lechho catch method in the immobilization; after the alcohol was analyzed by the Dichromate method to identify its alcoholic degree.

Continuous processes with immobilized cells are a good alternative for improving the efficiency and the performance of alcoholic fermentations. The fermenting medium used for the experiments was the following: Regarding materials composition, the percentages of lignin, cellulose, hemicellulose and ash that are presented in table 1there are different proportions in each material; these differences can directly affect yeast immobilization.

In the fermentations performed with glucose syrup, a higher amount of ethanol was obtained in the process that used corn cob as the carrier. Recibido el 5 de abril de