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Yield of the Dimethoxypropane Hydrolysis Reaction vs Static Mixer Residence Time for three Kenics Helical Element Mixer

Yield of the intermediate C at the reactor outlet as a function of the hydrogen supply ratio Odat. Fixed reactor pressure P 0.81 MPa.

Yield of the intermediate product A as function of the dimensionless time Da for different dimensionless mixing times Dall t Jt .

Yield of the intermediate product as a function of conversion and the ratio of the rate constants, v.

Yield of the intermediate product as a function of conversion for different dimensionless mixing times M 2.

Yield of the intermediate product as function of the conversion and the ratio of rate constants. Irreversible first order reactions.

Yield of the OD formation versus laser fluence.

Yield of the principal products as a function of time

Yield of the W O W-type dispersion as a function of of the volume fraction of the W 0 emulsion in the final form of W O W emulsion. Reproduced with permission from Ref. 1. Copyright 1976 Academic Press.

Yield of thermolysis products as a function of tmeas for diol-based Hf compounds

Yield of TTB versus the number of cycles for samples of different compositions, , 1

Yield of turnip, radish, lettuce and cabbage with the six treatments .

Yield of various products from Au core Pd shell colloidal catalysts as a function of the pre-annealing temperature. Reactions were carried out in a C2H2 H2 mixture at 300 K .

Yield on electrons available for transfer to oxygen, Y ,v t, for aerobic growth with NH, as a nitrogen source. Theoretical limits due to the second law and C-limitation. Average of experimental data for various substrates, symbols as in

Yield Optimization with Ester 27

Yield pattern for various reactor types, for the selective hydrogenation ofcyclododecatriene to the mono-olefin.

Yield point vs. temperature and moisture content for DuPont Zytel

Yield prediction curves for lactation yield of about 7000 kg.

Yield prediction for a goat producing about 750 kg milk lactation.

Yield pressure of multicomponent vessels designed for optimum conditions .

Yield profiles of n-heptane pyrolysis, KAPP 14.5 psia, 0

Yield residence time dependences forthe in situ generation

Yield sign.

Yield spectra of C

Yield stability of IPR-2001



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