Cell density

Unit cell dimensions (A) Number of repeat units per cell Density (g cm 3)... [Pg.268]

Based on a seed density of 100 kg/m. Based on a cell density of 10 cells/m. ... [Pg.331]

Crystal Structure. The crystal stmcture of PVDC is fairly well estabhshed. Several unit cells have been proposed (63). The unit cell contains four monomer units with two monomer units per repeat distance. The calculated density, 1.96 g/cm, is higher than the experimental values, which are 1.80—1.94 g/cm at 25°C, depending on the sample. This is usually the case with crystalline polymers because samples of 100% crystallinity usually cannot be obtained. A dkect calculation of the polymer density from volume changes during polymerization yields a value of 1.97 g/cm (64). If this value is correct, the unit cell densities may be low. [Pg.430]

Type Unit cell Density Melting point, °C T °C... [Pg.346]

M. Luoma, P. Lappi, and R. Lylykangas, Evaluation of High Cell Density E-Flow Catalyst, SAE 930940, Society of Automotive Engineers, Warrendale, Pa., 1993. Good reference for mass-transfer limited model reactions. [Pg.495]

In the mass-transfer limited region, conversion is most commonly increased by using more catalyst volume or by increasing cell density, which increases the catalytic wall area per volume of catalyst. When the temperature reaches a point where thermal oxidation begins to play a role, catalyst deactivation may become a concern. [Pg.504]

Performance criteria for SCR are analogous to those for other catalytic oxidation systems NO conversion, pressure drop, catalyst/system life, cost, and minimum SO2 oxidations to SO. An optimum SCR catalyst is one that meets both the pressure drop and NO conversion targets with the minimum catalyst volume. Because of the interrelationship between cell density, pressure drop, and catalyst volume, a wide range of optional catalyst cell densities are needed for optimizing SCR system performance. [Pg.510]

Cultures of G. polyedra (L. polyedrum) are grown at 20 5°C in a supplemented sea water medium (Hastings and Sweeney, 1957 Hastings and Dunlap, 1986), under cool-white fluorescent lighting of a 12-hr light/12-hr dark cycle. The cultures are inoculated at densities of 100 to 500 cells/ml. After 2-4 weeks, cells are harvested by vacuum filtration on a filter paper at cell densities of 7,000-15,000 cells/ml, yielding 0.3-0.7 g wet cells per liter of culture. [Pg.251]

Pyrocystis lunula (clone T37) can be grown under light-dark cycles as well as under continuous illumination at 20 2°C, in f/2 medium (Guillard and Ryther, 1962) with 0.5% soil extract instead of silicate (Guillard, 1974). The growth is somewhat slower and harvesting may be carried out about 40 days after inoculation, at a cell density of 15,000-20,000 cells/ml. [Pg.251]

Fuqua, W. C.,Winans, S. C.,and Greenberg, E. P. (1994). Quorum sensing in bacteria the LuxR-LuxI family of cell density-responsive transcriptional regulators./. Bacteriol. 176 269-275. [Pg.396]

Figure 2.2 shows the cell density and DO level in a pilot-scale aeration vessel. The role of dissolved oxygen in the treatment system is absolutely vital. Therefore the DO level must be maintained at not less than 3-4 ppm in the wastewater for effective aeration. SCP production is veiy oxygen-dependent. The results would be very satisfactory if pure oxygen is used. [Pg.16]

Example 2.1 Calculate Cell Density in an Aerobic Culture... [Pg.20]

A strain of Azotobacter vinelandii was cultured in a 15 m3 stirred fermenter for the production of alginate. Under current conditions the mass transfer coefficient, kLa, is 0.18 s. Oxygen solubility in the fermentation broth is approximately 8 X 10 3 kgm-3.9 The specific oxygen uptake rate is 12.5 mmol g 1 h. What is the maximum cell density in the broth If copper sulphate is accidentally added to the fermentation broth, which may reduce the oxygen uptake rate to 3 mmol g 1 h 1 and inhibit the microbial cell growth, what would be the maximum cell density in this condition ... [Pg.20]

We make an assumption based on the fact that all of the dissolved oxygen in the fermentation broth is used or taken by microorganisms. In this case the DO goes to zero. The value for CAI can be zero since it is not given in the problem statement. Also the cell density has to be maximised. Therefore the above assumption is valid. In the above equation x represented the cell density, that is ... [Pg.20]

To achieve the calculated cell densities, other conditions must be favourable, such as substrate concentration and sufficient time. [Pg.21]

There is always a limit to the liquid phase oxygen transfer for high cell density because mass transfer is limited. Actual cases are ... [Pg.30]

The change of cell density with respect to time is given as follows ... [Pg.40]

In reality, oxygen concentration never reaches the concentration defined in the proposed model, since the microbial activities at optimal and maximum cell density would reach the point where oxygen depletion takes place.5... [Pg.45]

Periodic samples were taken at the starting point after introducing the inocula, on the fust, second and thud day of each experimental ran. The optical cell density, COD, carbohydrate concentration and dissolved oxygen were monitored for various air flow rates. The COD was measured by the closed reflux colorimetric method at 600 nm with a spectrophotometer using potassium dichromate as a reducing reagent.7 All organic chemicals... [Pg.46]

Further experiments were conducted in a large aeration tank, 15 litres batch system to study die dry weight cell density, COD, carbohydrate, dissolved oxygen and oxygen transfer modelling. Two different airflow rates, 5 and 10 litres/min, were applied. However,... [Pg.47]

Once there is an appreciable amount of cells and they are growing very rapidly, the cell number exponentially increases. The optical cell density of a culture can then be easily detected that phase is known as the exponential growth phase. The rate of cell synthesis sharply increases the linear increase is shown in the semi-log graph with a constant slope representing a constant rate of cell population. At this stage carbon sources are utilised and products are formed. Finally, rapid utilisation of substrate and accumulation of products may lead to stationary phase where the cell density remains constant. In this phase, cell may start to die as the cell growth rate balances the death rate. It is well known that the biocatalytic activities of the cell may gradually decrease as they age, and finally autolysis may take place. The dead cells and cell metabolites in the fermentation broth may create... [Pg.82]

Biostat. This is also known as a turbidostat. It is a system where cell growth is controlled and remains constant while the flow rate of fresh media does not remain constant. Cell density is controlled based on set value for turbidity, which is created by the cell population while fresh media is continuously supplied. A turbidostat is shown in Figure 5.8. [Pg.86]

In a chemostat and biostat or turbidostat, even with differences in the supply of nutrients and/or fresh media, constant cell density is obtained. The utilisation of substrate and the kinetic expressions for all the fermentation vessels are quite similar. It is possibile to have slight differences in the kinetic constants and the specific rate constants.3,4 Figure 5.9 shows a turbidostat with light sources. The system can be adapted for photosynthetic bacteria. [Pg.86]

The effect of substrate concentration on specific growth rate (/i) in a batch culture is related to the time and p,max the relation is known as the Monod rate equation. The cell density (pcell) increases linearly in the exponential phase. When substrate (S) is depleted, the specific growth rate (/a) decreases. The Monod equation is described in the following equation ... [Pg.92]

With cell recycling, chemostat efficiency is improved. To maintain a high cell density the cells in the outlet stream are recycled back to the fermentation vessel. Figure 5.10 represents a chemostat unit with a cell harvesting system. The separation unit is used for harvesting the cells and recycling then to the culture vessel to increase the cell concentration. [Pg.95]

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