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The silver mounting plate and mounting hardware reflect light. I have noticed that it reflects into the rear window. This might be a distraction during track events. A mitigation may be to paint the car camera mount black or to a color similar to the rear deck. A darker color absorbs sunlight and gets warmer than a silver finish. You ll have to make a decision on this trade-off.

Standard Rushton turbines of approximately one-third have traditionally been employed in fermentation processes. Bulk blending is also poor in highly shear thinning fungal broths, due to the tendency of Rushton turbines to compartmentalize. Buckland et al. (1988b) retro tted two standard Rushton turbines (D/T = 0.33) with two low power number (Po = 1.1) Prochem hydrofoil impellers (D/T = 0.45) in 800 L in Streptomyces avermitilis fermentations. Two fermenters each equipped with either two Rushton or two Prochems were operated at 300 and 330 rpm with power draws of 4.1 and 2.7 kW, respectively. The values of kL a, oxygen uptake rates and Avermectin titers in the two bioreactors were identical. Thus, the Prochem impellers were shown to be capable of providing the same oxygen transfer and product titers, while drawing about 50% less power. They attributed this to the increased well-mixed volumes generated by the Prochem impellers, leading to enhanced oxygen transfer rates. Such results have also been demonstrated in highly viscous xanthan fermentations (see Section 18.3.4). Buckland et al. (1988a) recommended that standard Rushton impellers could be replaced by low-powernumber agitators (preferably axial ow) such that the retro tting would result in similar operating speeds, torque, and power. In this manner, the same shaft, motor, and gearbox could be employed. Similar retro tting of such impellers in 19 000 L penicillin batch fermentations (Buckland et al., 1988b) demonstrated that the use of Prochem impellers at 1.96 W/kg resulted in higher productivity than Rushton turbines drawing 2.35 W/kg. These results were again explained in terms of enhanced bulk mixing and oxygen mass transfer.

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Since we do not know r except that it is a product from (10.7), the probability model (10.8) of x includes two parameters, W called the parameter of interest which we want to estimate, and the unknown function r = r1 rn called the nuisance parameter (function) which we do not care. Such a statistical model including an in nite or functional degree of freedom of nuisance parameters is called a semiparametric model. It is in general a di cult problem to estimate the parameter of interest, because of the existence of unknown functions. A method of estimating functions has been developed for estimation in semiparametric statistical models in the framework of information geometry (Amari and Kawanabe [40, 41]; see also Amari [21], Amari and Nagaoka [42] as for information geometry). The advantage of using the semiparametric approach is that we do not need to estimate the nuisance parameters: the probability density functions of source signals in blind separation and deconvolution problems. It is inferred from the theory of estimating functions that the batch estimator of the estimating equation converges to the true solution as the number of observed data tends to in nity. An estimating function in the present case is a matrix-valued function F (x, W ) = [Fab (x, W )] of x and W not including the nuisance parameter r, that satis es 1) 2) EW,r {F (x, W )} = 0, when W = W EW,r {F (x, W )} = 0, whenW = W , (10.9) (10.10)

Our basic bag now embellished with gluons, massive quarks, and approximate corrections for CM energy and zero-point motion, we confront the data. For light-quark bags we ignore contributions from the gluon field except for one-gluon exchange (for heavy quarks, or high angular momentum states corresponding to elongated bags, this may not be a good approximation).

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