Conditioner for flotation of coal

Claim 3

The method of claim 1 wherein the alkanolamine comprises an alkanolamine of the formula: (R.sub.3)(R.sub.2)N(R.sub.1) wherein R 1 is a β-hydroxyalkyl group or inertly substituted β-hydroxyalkyl group having from 2 to 5 carbon atoms; and R 2 and R 3 are independently R 1 , hydrogen, an alkyl group of from 1 to 4 carbon atoms or a monovalent group corresponding to the formula: (R.sub.4)(R.sub.5)N(CH.sub.2)y- wherein y is an integer of 2 or 3 and R 4 and R 5 are independently R.sub. 1, hydrogen, or alkyl having from 1 to 4 carbon atoms.

Claim 4

The method of claim 2 wherein the alkanolamine(s) bear only hydroxyethyl and ethylene moieties.

Claim 5

The method of claim 1 wherein the alkanolamine comprises diethanolamine, triethanolamine or di- tri- or tetra(hydroxyethyl)-ethylenediamine.

Claim 6

The method of claim 1 wherein the naphthenic acid/alkanolamine condensate is prepared by reacting from at least about 1 to about 5 moles of naphthenic acid for each mole of alkanolamine.

Claim 7

The method of claim 5 wherein the alkanolamine comprises diethanolamine and the condensate is prepared from about 1.9 to about 2.25 moles of the naphthenic acids for each mole of the alkanolamine.

Claim 8

The method of claim 1 wherein the coal has an oxidized surface.

Claim 9

The method of claim 1 wherein the aqueous frothing medium contains a fuel oil collector/conditioner.

Claim 10

The method of claim 8 wherein from about 0.02 to about 2.5 kilograms of the fuel oil are employed per ton of coal flotation feed (as calculated on a dry weight basis).

Claim 11

The method of claim 8 wherein the aqueous frothing medium further contains a condensate of an alkanolamine and a fatty acid or fatty acid ester.

Claim 12

The method of claim 10 wherein the naphthenic acid/alkanolamine condensate is employed in an amount of from about 10 to about 70 weight percent and the fatty acid/alkanolamine condensate employed in an amount of from about 30 to about 90 weight percent based on the weight of the naphthenic acid/alkanolamine and fatty acid/alkanolamine condensates.

Claim 13

The method of claim 8 wherein the aqueous frothing medium further comprises a frother.

Claim 14

The method of claim 12 wherein the frother is employed in an amount of from about 0.05 to about 0.5 kilogram frother per ton of coal feed (dry weight basis).

Claim 15

The method of claim 13 wherein the frother is methyl isobutyl carbinol or a polypropylene methyl ether having a weight average molecular weight between about 200 and about 600, or the reaction product of C 4-6 alcohols and propylene oxide.

Claim 16

The method of claim 13 wherein the frother is the reaction product of sucrose; or a monosaccharide, disaccharide, C 1-20 alkane or C 3-20 cycloalkane having three or more hydroxy groups with propylene oxide or a mixture of propylene oxide and ethylene oxide.