CA1141043A - Conditioner for flotation of oxidized coal - Google Patents

Abstract

ABSTRACT

Certain condensation products of a fatty acid or fatty acid ester and a hydroxyalkylated alicyclic nitro-gen-containing compound are useful as conditioners to improve the recovery of clean coal in a froth flotation process. The presence of these condensation products in the flotation medium is particularly effective to enhance the recovery of oxidized bituminous coal.

28,128-F

Description

COAL EMPLOYING CONDENSATES OF
FATTY ACIDS OR THEIR ESTERS WITH
N-HYDROXXALKYLATED
NITROGEN COMPOUNDS

This invention relates to the froth flotation of coal-containing ashes, coal sludge or coal-containing residues to recover coal containing a lower percentage of impurities. In particular, this invention relates to the use of a condensation product of a fatty acid or fatty acid ester and a N-hydroxyalkylated, nitrogen-containing compound as a conditioner for the flotation of finely divided coal.
.

The natural process of "coalification" inher-ently depo~its some non-combustlble mineral matter in association with the combustible carbonaceous soli~s.
Large fragments of non-combustible material can be removed by screening or other gravity concentration techniques, but other cleaning methods more efficiently lS remove fine material intimately associated with the car-bonaceous solids. Froth flotation of coal is used in the art to beneficiate finely-divided raw coal. Bitumi-nous coals generally possess a natural hydrophobicity, 28,128-F -1-~.
e~

~14~3 which results in the coal being floatable in the presence of a frother, such as methyl isobutyl carbinol, desirably with a relatively mild collector, such as kerosene. How-ever, anthracite coals, as well as coals of all grades in which the surface has been at least partially oxidized, float poorly in such a medium, resulting in the loss of significant amounts of combustible material with the tail fraction from the flotation.

The loading of the oil-type collector is gen-erally 0.1 to 2 pounds (0.045-0.91 kg) per 1000 kg of coal feed for bituminous coals of intermediate or low grade, with the loading being relatively greater for the flotation of lignite and anthracite coals. However, good recovery of oxidized coals or lignite coals can only be effected at such high loadings of the oil-type collector that significant amounts of inert material are floated along with the combustible materials. Sun suggests in Trans. AIME, 199:396-401 (1954), that fatty amines can be utilized as co-collectors in the flotation of oxidized coals to effect enhanced recovery. However, even these amine collectors effect only partial recovery of combust-ible material.

The deficiencies of the prior art processes mentioned above have been substantially ov~rcome by the present invention, which is a froth flotation process for beneficiating coal which comprises floating coal particles of flotation size in a frothing aqueous medium in the pres-ence of a fuel oil collector and an effective amount of a condensation product of a fatty acid or fatty acid ester and a compound represented by the formula I

28,128-F -2-~L4~

}
Y T T

wherein z is 0 or 1; x is 2 or 3; T at each occurrence is independently hydrogen, ethyl or methyl; Y is hydrogen or H-C-CH-OH
T T

R is ~ _ , R"- ~ - , ~ -N- , O-N- ~-N-~ 15 or CN

wherein R' is hydrogen or a C1-C20 aliphatic radical and R" is hydrogen or Y rN----~C 2 ~

L ~ Z

in which z, x, T and Y have the aforementioned meanings;
said condensation product being prepared using a molar ratio of at least about one mole of fatty acid or ester 28,128-F -3-for each mole of the compound of formula I, and said con-densation product being employed in its free form or as an acid deri~ative.

The compounds of formula I wherein z is 0, are readily prepared by the reaction of well-known morpho-line, piperazine, aniline, cyclohexylamine, cyclopentyl-amine or piperidine compounds (from which the univalent radical R is derived by deprotonation) with an alkylene oxide in the manner known to the art. Representative alkylene oxides include ethylene oxide, 1,2-propylene oxide, 1,2-butylene oxide, 2,3-butylene oxide, isobutyl-ene oxide and 2,3-pentylene o~ide. The hydroxyalkylation reaction is conveniently effected by bringing together in the stoichiometric ratio the nitrogen-containing reactant and the alkylene oxide in the liquid phase at a tempera-ture of from about 50C to about 150C. The piperazine, aniline, cyclohexylamine and cyclopentylamine moieties each have two active hydrogens borne by a nitrogen which can each be displaced by reaction with the alkylene oxide;
therefore, from 1 to 2 equivalents of alkylene oxide can be reacted with these moieties. The preferred alkylene oxide reactants are ethylene oxide and propylene oxide.
Mixtures of alkylene oxides are also operable hydroxyal-kylation reactants.

The compounds of formula I wherein z is 1, are prepared by (1) reacting a morpholine, piperazine, ani-line, cyclohexylamine, cyclopentylamine or piperidine com-pound with chloroacetonitrile (x = 2) or acrylonitrile (x = 3) at 50C to 120C, (2) hydrogenating the result-ing amine nitrile in a manner known to the skilled artisan, and (3) hydroxyalkylating the resulting diamine in the 28,128-F -4---5~

above~described marmer. Similar reactions to prepare a diamine are taught in U.S. Patents 3,363,758, issued to Cranberg et al., January 16, 1968; and 3,925,389, issued to Yeakey et al., December 9, 1975.

Generally, it is preferred in the compounds of formula I that Y is not hydrogen in at least one occur-rence. Particularly efficacious as conditioners are those condensates prepared by the reaction of a fatty acid with a compound represented by the formula I wherein R is ~ - or R"-N ~ - .

Preferably, in the second formula immediately above, R"
is Y-NtCH2~X
Y

wherein Y and x have the aforementioned meanings.

The fatty acid condensed with -the compounds of formula I can operably be an acid represented by the formula ,, D-C-OH

28,128-F -5-wherein D is an aliphatic radical having 4 to 22 carbon atoms. Oleic, lauric, linoleic, palmitic, stearic, myris-tic acids, and mixtures thereof are examples of operable acids. The esters corresponding to these fatty acids, such as glycerides, are also operable, but less preferred.
For reasons of economy, it is preferred to use crude mix~
tures of fatty acids, rosin acids, lignin and unsaponifi-able material, such as tall oil, coconut oil, palm oil, palm kernel oil, cottonseed oil, linseed oil, olive oil, peanut oil and fish oil. Tall oil or tall oil heads are especially preferred mixtures of fatty acids and rosin acids. Preferably, the tall oil reactant contains less than about 40 percent rosin acids by weight. Tall oil and tall oil heads are well-known compositions described in the Kirk-Othmer, Encyclo~edia_of Chemical Technoloqy, 2nd Ed., Vol. 19, pp. 614-629 ~1969).

The compound of formula I is condensed with a fatty acid or its ester by mixing these reactants and heating until the desired degree of condensation has taken place, as indicated by the quantity of water distilled overhead or infrared spectrophotometric analysis of the condensation product. Generally, a reaction temperature of from about 120C to about 250C is operable. The reac-tion is termed a condensation to distinguish it from the formation of the ammonium salt of the carboxylic acid at lower temperatures. Dependin~ on the reactant, the conden-sation product may be an ester, an amide or may be both these functional ~roups. Although it is desirable that the condensation reaction is substantially complete to make the most efficient use of the reactants, the conden-sation product is operable, but less effective, as a con-ditioner for coal in the presence of a substantial amount 28,128-F -6-of unreactea fatty acid and/or the uncondensed ammonium salt of the acid. The term "conditioner" indicates that the condensation product is primarily effective to enhance the hydrophobicity of the coal surface. The term "condi-tioner" is not intended to exclude the possibility thatthis condensation product or its salts act as a co-collec-tor with the fuel oil or kerosene collector. The term "condensation product" refers to not only the above--described condensation products in their free form, but also acid derivatives thereof, as described hereafter.

The above-described condensation products neu-tralized or partially neutralized with inorganic or organic acids are operable, but not preferred, as conditioners in the instant flotation process. These acid derivatives may be either a salt, partial salt or acid complex, depending on the acid and condensate employed. These derlvatives are frequently more readily dispersed in the aqueous flo-tation medium than are the parent compounds, but generally are less active. Common inorganic acids which can be used include phosphoric, nitric, boric, hydrochloric, hydrobro-mic, sulfuric and alkane sulfonic acids. Organic carbox-ylic acids which can be used include aliphatic mono-, di-, or tricarboxylic acids; lower alkyl carboxylic acids;
mono- or dihydroxy lower alkyl carboxylic acids and amino--substituted compounds thereof; and unsaturated aliphatic acids. Examples of these organic acids include formic, acetic, hydroxyacetic, propionic, ~utyric, isovaleric, lactic, gluconic, aminoacetic, malonic, succinic, adipic, malic, tartaric, glutaric, maleic, fumaric, citric, iso citric, aco~itic, oxalic, salicylic, benzoic, and naph-thenic acids. Fatty acids can also be employed for -this purpose, but are not as desirable as other lower organic 28,128-F -7-acids. The C1 to C4 organic acids are preferred. Ace-tic acid is particularly preferred to prepare so-called partial salts by the partial neutralization of the con-densation product with acetic acid.

The efficacy of the instant organic carboxylic acid condensation product is greatest when the reactants are condensed in a specific range of mole ratios. Advan-tageously, at least about one equivalent of fatty acid is condensed with each equivalent of a hydroxy or secondary amine moiety. To avoid waste of fatty acid, the number of moles of fatty acid and/or ester reacted with the com-pound of formula I should not exceed the number of moles of the compound of formula I multiplied by the average number of reactive sites on a molecule of the compound.
The term "reactive sites" refers to the exchangeable hydrogen substituents on the amine group(s) and the reac-tive hydroxyl substituents on the hydroxyalkyl group(s), which will react with the fatty acid or fatty acid ester to produce amides and esters, respectively. In the fore-going mole ratios, the moles of fatty acid in crude mix-tures derived from natural sources do not include the - moles of such minor generally inert components as unsa-ponifiable matter.

The loading of the condensation product in the flotation medium, which effects the greatest recovery of combustible carbonaceous matter with a tolerable amount of inert matter, is dependent upon such divPrse factors as the size, grade, degree of oxidation and inert matter con-tent of the coal feed, as well as the loading of frother and other adjuvants. The term "effective amount" is used herein to denote the amount of said compounds required to increase the recovery of coal by froth flotation in the 28,128-F -8-4~ 3 _g_ presence of fuel oil and a frother. Generally, where this conditioner is employed with only fuel oil and a frother, the condensate is advantageously employed in a ratio of from about 0.01 to a~out 1.0, preferably about 0.005 to about 0.5 kilograms, of condensate per 1000 kg of coal flotation feed.

The instant conditioner can be utilized in conjunction with co-collectors or other adjuvants, such as activators, conditioning reagents, dispersing reagents, frothing reagents and depressing reagents. Fuel oil is employed in the flotation medium as a collector and/or dispersing reagent. Representative fuel oils include diesel oil, kerosene, Bunker C fuel oil and mixtures therof. The fuel oil can generally be advantageously employed in a ratio of from about 0.2 to about 2.5 kilo-grams fuel oil per 1000 kg of coal flotation feed. The optimal loading of fuel oil in the flotation medium is influenced by numerous factors, such as the size, degree of oxidation and grade of the coal to be floated and the loading of the conditioner and frother. Therefore, the loading of ~he fuel oil should be optimi~ed empirically to effect the greatest selectivity and recovery during flotation. It is generally desirable to introduce the condensation product to the flotation medium in a fuel oil emulsion.

A frothing agent should be present in the flo-tation medium to promote formation of a froth. Conven-tional frothers, such as pine oil, cresol, isomers of amyl alcohol and other branched C4 to C8 alkanols are suitable for this purpose. However, methyl isobutyl car-binol and polypropylene glycol alkyl or phenyl ethers are 28,128-F -9-~lo--preferred as frothers, with polypropylene glycol methyl ethers havin~ a weight average molecular weight of from 200 to 600 being more preferred. The optimal loading of frother in the flotation medium is influenced by a number of factors, most important of which is the particle size, grade and degree of oxidation of the coal. Generally, a ratio of from about 0.05 to about 0.5 kilogram of frother per 1000 kg of coal feed is advantageous.

The coal to be floated by the instant process can suitably be anthracite, bituminous and subbituminous.
This process is preferably employed to float coal which cannot be floated with conventional frothers alone and is particularly effective in the flotation of bituminous coal of intermediate or low grade, where the surface of the coal is oxidized to an extent which significantly impedes the flotation of the coal by conventional methods.

The size of the coal flotation feed is impor-tant as generally particles larger than about 28 mesh (U.S. Sieve Size) are difficult to float. In typical operations, coal particles larger than 28 mesh, advanta-geously larger than 100 mesh, are separated from both the inert material mined therewith and more finely divided coal by gravimetric separation techniques. However, if a substantial fraction of the coal in the flotation feed is contained in particles larger than 28 mesh, i-t is desirable that the feed is comminuted prior to flotation.

The sized coal flotation feed in preparation for flotation is first optionally washed and then mixed with sufficient water to prepare an agueous slurry having 28,128-F ~10-a concentration of solids which promotes rapid flotation.
Generally, a solids concentration of from about 2 to about 20 weight percent solids, more preferably about 5 to about 10 weight percent, is preferred. The aqueous coal slurry is desirably conditioned with the condensation product, a frother, fuel oil and any other adjuvants by vigorously mixing or agitating the slurry prior to flotation in a manner known to the art. Generally for difficult to float coal, it is advantageous to contact with mixing the coal slurry with the conditioner and fuel oil for a period of time prior to flotation, so as to effect intimate contact of the conditioner and ~uel oil with substantially all of the coal. ~here the aqueous coal slurry is prepared in a containex distinct from the flotation cell and then is con-veyed to the flotation through conduits, the desired inti-mate contact can conveniently be attained by introducing the conditioner and fuel oil to the slurry upstream from the flotation cell. The frother, however, should be introduced to the slurry shortly before or during flota-tion to provide maximum frothing.

The coal is operably floated at the naturalpH of the coal in the a~ueous slurry, which can vary from about 3.0 to about 9.5 dependin~ upon the composition of the feed. However, a p~ adjustin~ composition is option-ally used as nececsary to adjust and maintain the pH ofthe aqueous coal slurry prior to and during flotation to a value from about 4 to about 9, preferably about 4 to about 8, which yenerally promotes the greatest coal recov-ery. If the coal is acidic in character, ~he pH adjusting composition can operably be an alkaline material, such as soda ash, lime, ammonia, potassium hydroxide or magnesium 28,128-F -11-hydroxide, with sodium hydroxide being preferred. If the a~ueous coal slurry is alkaline in character, a carboxylic acid, such as acetic acid, or a mineral acid such as sul-furic acid or hydrochloric acid is operable to adjust the pH.

The conditioned and pH-adjusted aqueous coal slurry is aerated in a conventional flotation machine or bank of rougher cells to float the coal. Any conventional rougher flotation unit can be employed.

The practice of the process of the instant invention can be used alone to beneficiate coal. Alter-natively, the process can be used in conjunction with secondary flotations following the instant process to effect even greater beneficiation of the coal.

The following examples illustrate the inven-tion. Unless otherwise indicated, all parts and percent-ages are by weight.

Examples 1-3 In a series of substantially identical flota-tion runs that differ principally in the identity of ~he frother and presence or absence of a conditioner, 200 grams of comminuted coal is diluted with deionized water to a slurry of 6.67 percent solids. The coal is a low grade, bituminous coal having a highly oxidized surface as indicated by the high oxygen content (14.3 percent) of the coal determined by conventional elemental analysis.
The fraction of the coal feed consisting of particles lar-ger than 25 mesh is separated, comminuted and then recom-bined with the remainder of the coal prior to dilution.
The comminuted coal feed is more than 90 percent particles 28,128-F -12-~ 3 smaller -than 80 mesh. The coal as charged to the slurry contains about 14.7 percent ash.

The conditioner is prepared by reacting (1) 1 equivalent of N-2-aminoethylpiperazine (AEP) with 2 equiv-alents of ethylene oxide (EO) or 1,2-butylene oxide (BO) at a temperature of 100C-135C for from 2 to 8 hours and ~2) condensing the resulting hydroxyalkylated product with three equivalents of tall oil fatty acid (TOFA) at a tem-perature from about 130C to about 225C until the reac-tion is substantially complete as indicated by infraredspectrophotometric analysis. This tall oil fatty acid, according -to analysis by conventional methods, contains 39 percent rosin acids, 29.3 percent oleic acid, 23 per-cent linoleic acid, 3.7 percent conjugated linoleic acid, 1.8 percent s-tearic acid and about 3 percent other acids and components.

The aqueous coal slurry is introduced into a flotation machine having a three-liter cell. The pH of the slurry is determined to be about 4. Sufficient aque-ous sodium hydroxide ~1.0 normal) is added to the slurryto adjust the pH to 7. The coal slurry is agitated for about seven minutes to thoroughly wet the coal, at which time a re~ined kerosene is added to the slurry to effect a loading of about 2.5 kilograms of kerosene per 1000 kg of coal feed. One-half milliliter (ml) of a 5 percent kerosene solution of one of the aforementioned condition-ers is added in each of two flotation runs. In a third run, the condensate of the AEP-BO adduct and the TOFA in the 5 percent kerosene emulsion is neutralized with ace-tic acid to a pH of 5 and the resulting partial acetate 28,128-F -13-salt is employed as the conditioner. One control flota~
tion run is also made, in which no conditioner is added with the kerosene.

Next, 0.04 ml of a polypropylene glycol methyl ether frothing agent having an average molecular weight of about 400 is added ~o the medium. The aqueous coal slurry is conditioned by agitation for one minute, after ~Ihich aeration of the medium is initiated and continued for four minutes. A frothy concentrate is collected during aeration.

10 The collected concentrate is first dried in an oven and then weighed. The percent recovery of coal by flotation is determined from the weight of coal ~i.e., total weight less weight of ash~ in the concentrate divided by the weight of coal in the 200-gram charge. A
one-gram sample of the concentrate is completely burned and the ash content of the concentrate is determined from the weight of the material remaining after combustion.
Table I tabulates the identity of the conditioner for each run as well as the percent recovery of coal and ash content in the concentrate.

TABLE I

Coal Ash Example Conditioner Recover~ Content (%2 1 AEP/EO/TOFA63.7 10.0

2 AEP/BO/TOFA65.7 10.7

3 AEP/BO/TOFA*37.8 9.2 Compa ative none35 9 9.1 *Acetate Salt.
*~Not an example of this invention~

28,128-F -14-Example 4 In a manner otherwise similar to Example 1, a condensate of 1 eguivalent of trihydroxyethylated N,N'--bis(3-aminopropyl)piperazine with 4 equivalents of tall oil fatty acid is employed as the conditioner. The tri-hydroxyethylated N,N'-bis(3-aminopropyl)piperazine is prepared by (1) reacting 1 equivalent of piperazine with 2 equivalents of acrylonitrile followed by (2) hydrogena-tion of the dinitrile intermediate to the corresponding diamine and (3) reacting the resulting N,N'-bis(3-amino-propyl)piperazine (1 equivalent) with 3 equivalents of ethylene oxide. This conditioner effects coal recovery of 57.0 percent with an ash content of 10.3 percent.

Example 5 In a manner otherwise similar to Example l, a condensate of 1 equivalent of N-(2-hydroxyethyl)mor-pholine with 1 equivalent of tall oil fatty acid is employed as the conditioner. This conditioner effects co~l recovery of 56.0 percent with an ash content of 10.3 percent.

Example 6 one equivalent of N-(3-aminopropyl~morpholine is reacted with 2 equivalents of ethylene oxide and the resulting dihydroxyethylated product (1 equivalent) is reacted with 2 equivalents of tall oil fatty acid. In a manner otherwise similar to Example 1, the above-described condensation product is used as the conditioner in the flotation of coal. This conditioner effects coal recov-er~ of 56.0 percent with an ash content of 10.3 percent.

28,128-F -15-Example 7 In a manner otherwise similar to Example 6, the condensate of dihydroxyethylated N-(3-aminopropyl)-morpholine (1 equivalent) and tall oil fatty acid (2 equivalents) is neutralized with acetic acid to a pH of 5 in a 5 percent kerosene emulsion and the resulting par-tial acetate salt is employed as the conditioner. This conditioner effec-ts coal recovery of 47.0 percent with an ash content of 10.6 percent.

28,128-F -16-

Claims (9)

1. A froth flotation process for benefici-ating coal which comprises floating coal particles of flotation size in a frothing aqueous medium in the pres-ence of a fuel oil collector and an effective amount of a condensation product of a fatty acid or fatty acid ester and a compound represented by the formula I

I

wherein z is 0 or 1; x is 2 or 3; T at each occurrence is independently hydrogen, ethyl or methyl; Y is hydrogen or , R is 28,128-F -17- , , , , , or , wherein R' is hydrogen or a C1-C20 aliphatic radical and R" is hydrogen or , in which z, x, T and Y have the aforementioned meanings;
said condensation product being prepared using a molar ratio of at least about one mole of fatty acid or ester for each mole of the compound of formula I, and said con-densation product being employed in its free form or as an acid derivative.

2. The process of Claim 1 wherein the coal is a bituminous coal having an oxidized surface.

3. The process of Claim 1 wherein the com-pound of formula I, Y at one or more occurrences is .

28,128-F -18-

4. The process of Claim 3 wherein R is or .

5. The process of Claim 4 wherein R is and R" is .

6. The process of Claim 1 or 5 wherein in each moiety of the formula in the compound of formula I, T at one occurrence is hydrogen and T at the other occurrence is hydrogen or methyl.

7. The process of Claim 1 wherein the con-densation product is present in its free form.

8. The process of Claim 1 wherein the con-densation product is present as an acetic acid neutra-lized derivative.

28,128-F -19-

9. The process of Claim 1 or 5 wherein the fatty acid or ester is a tall oil fatty acid, tall oil heads, a tall oil fatty acid ester, or a mixture thereof.

28,128-F -20-