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By-product formation during fluoioalkylation.

By-product formation during fluoroalkylatioir

By-product formation during fluoroalkylation.

By-product formation during zinc dehalogenation.

By-product formation in simple aliphatic nucleophilic fluorination.

By-product formation in sulfonation of benzene , tube reactor

By-product formation in sulfonation of benzene with gaseous sulfur trioxide in a stirred-cell reactor in relation to initial benzene concentration and stirrer speed. 30 vol benzene in dichloroethane, T 35 C, 0.1 100 vol

By-product formation in tube reactor.

By-product formation on catalysts HDC-7 and HDC-25.

By-product selectivity, Xj, as a function of Damkoehler number based on k2. These data of Bourne in Sharratt show the increased by-product formation with increasing mixing time based on the engulfment model, Te- As the reaction rate for the second reaction, kiCe, increases, the mixing time must decrease to maintain yield.

By-product selectivity. As, as a function of Da based on k2- This data from Bourne show the increased by-product formation with increasing mixing time based on the engulf-ment model, Tp. As the reaction rate for the second reaction, k2Cfl, increases, the mixing time must decrease to maintain yield.

By-products accompanying Mannich synthesis.

By-products derived from AAN self-condensation.

By-products formation during 1,1,1-trichloroethane destruction on LaMn03 g.

By-products from OL-pinene

By-products generally formed during the bis-alkoxycarbonylation of styrene.

By-products in MTO and LPG condensates

By-products in the synthesis of P-aminokeioncs.

By-products of novolac synthesis.

By-Products Treatment Plant

Bycroft s di-O-methyl curvulaiin synthesis.

Bye-Product Plant with Wet Sulphate Recovery,

Byk G ulden s PPI project compounds.

Byk Gulden candidate drugs BY319, BY308, BY156, and BY178.

Bypass capillary rheometer, automatically monitoring polymer rheology during



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