This application is a continuation-in-part of application Serial No. 816,480, filed January 6, 1986. The present invention relates to N-secondary-alkyl- diorganoa inopyridinium salts useful as phase transfer catalysts for facilitating preparation of fluoroaromatic compounds (such as fluoronitrobenzene compounds.)

Fluoronitrobenzene compounds such as 2-fluoronitrobenzene, 4-fluoronitrobenzene, and

2,4-difluoronitrobenzene, are useful as intermediates for the synthesis of various herbicidal compounds, dyes, and the like. Such compounds have been prepared from corresponding chloronitrobenzene compounds by so-called halogen exchange reactions, illustrated as follows:

wherein MF represents an alkali metal fluoride salt. The reaction is generally conducted in an aprotic, polar, organic solvent, such as d meth lsu1fox ide, d imeth 1form- amide, te ra e h lenesu1fone (sulfolane), and the like.

Alkali metal fluoride salts are not soluble in •uch solvents. Therefore, the reaction mixtures usually contain two phases, i.e., solid and liquid phases or two immiscible liquid phases. Finger, et al., J. Am. Chem Soc. , 76, 6034 (1956) and Ouesel, et al., U.S. Patent

3,064,0S8 (1962) , describe the reaction of chloroni roben- rβnβ compounds with inely- ivided, solid potassium

fluoridβ in aprotic polar solvents to produce corresponding luoronitrobenzene compounds. Boudakian, et al., U.S. Patent 3,240,824 (1966), describe the reaction of o-chloronitrobenzene with solid potassium fluoride at 5 elevated temperatures, without any solvent or diluents, to produce o-fluoroni robenzene. Napier and Starks, U.S. Patent 3,992,432 (1976), describe a reaction involving two liquid phases. In the Napier and Starks reaction, the inorganic fluoride salt is dissolved in an aqueous phase,

- ^■ - and the chloronitrobenzene compound is dissolved in a water-immiscible, organic phase. The reaction is catalyzed by a quaternary salt, which reportedly transfers ions across the phase interface.

Use of quaternary salt phase-transfer catalysts

--" in solid-liquid, two phase reactions also has been known. For instance, Kunz, U.S. Patent 4,069,262 (1978), describes the production of 2-fluoroni robenzene by reacting 2-chloronitrobenzene with ultrafine particulate potassium fluoride in tetraraethylenesulfone solvent using a

20 macrocyclic ether (crown ether) or a quaternary ammonium halide (such as tetrabutylammonium chloride, benzyltrimethyl«j-a--oniu---. chloride, bβnzyltri_πethyl.β-B-raonium fluoride or bβnzyltriβthylajB-aonium chloride) as the catalyst. 5 Tull, et al., U.S. Patent 4,140,719 ( 1979) , describes the production of 2 ,4-di luoro-5-chloronitro¬ benzene by reacting 2, ,5-trichloronitrobenzene with a solid fluorinating agent selected from NaF, KF, CsF, and C^.^alkyl quaternary ammonium fluoride, and mixtures 0 thereof under substantially anhydrous conditions in the presence of a quaternary compound solid-liquid phase transfer catalyst. The liquid phase comprises an organic solvent in which the trichloro compound is soluble and the fluorinating agent is essentially insoluble.

Starks, "Selecting a Phase Transfer Catalyst," Chemtech (February 1980), pages 110-117, describes patterns that purportedly enable prediction of catalysts for anion transfer from aqueous or solid inorganic phases to organic phases.

North, U.S. Patent 4,287,374 (1981) discloses a process for the production of a monofluoronitrobenzene in which a monochloronitrobenzene is heated with an alkali metal fluoride and a phase transfer catalyst at a temperature of no more than 200*C, preferably 125*-170*C. , especially 140 -150'C. North discloses, as examples of such catalysts which may be used, long chain alkylammonium halides.

In general, halide-exchange reactions for preparing fluoronitrobenzene compounds by reacting chloronitrobenzene compounds with fluoride salts in aprotic, polar organic solvents in the presence of quaternary ammonium salt phase-transfer catalysts proceed at faster rates when conducted at elevated temperature relative to rates obtainable at lower temperature. However, quaternary ammonium phase-transfer catalysts employed in heretofore known methods are less stable at higher temperature and have been found to decompose or lose their catalytic activity at elevated reaction temperatures. Moreover, U.S. Patent 4,418,229 (to White), incorporated herein by reference, discloses that lower molecular weight catalysts, i.e., those having a total number of carbon atoms less than about 16, are less stable under the conditions (including elevated temperature) of the method of the invention disclosed therein than the therein preferred catalysts of higher molecular weight having about 16 or more carbon atoms.

The above cited White patent discloses the finding that in the conversion of chloronitrobenzene ("CNB") compounds to corresponding fluoronitrobenzene ("FNB") compounds using a quaternary ammonium salt phase-transfer catalyst at elevated temperatures, a high level of catalytic activity can be maintained by adding the catalyst to the reaction mixture incrementally during the course of the reaction.

However, there remains a substantial need in the art for new and improved catalysts and processes for preparing fluoroaromatic compounds such as fluoronitrobenzenes. The present invention substantially fulfills such need.

DESCRIPTION OF THE INVENTION

Generally stated, the present invention provides N-secondary-alkyldiorganoaminopyridinium salts represented by the formula

, -~

where:

R- and R- are monovalent or divalent organo radicals independently selected from substituted and unsubsti uted hydrocarbon radicals having from 1 to

13 carbon atoms and divalent alkylene radicals which together can be a part of a cyclic structure forming a ring having from 4 to 8 carbon atoms;

R^ is a monovalent secondary alkyl radical having from 3 to 10 carbon atoms and the formula

( Z ) R ^s - C - R ⁶

H where R ^s and R^ are independently alkyl radicals having from 1 to 8 carbojra atoms; and

X- is an anion selected from the goup consisting of fluoride, bromide and chloride.

The above salts are sometimes referred to herein s PYR salts.

In another aspect, the present invention provides an improved process for preparing a fluoro¬ aromatic compound (such as fluoronitrobenzene compound) by reaction of a corresponding chloroaromatic compound (such as a chloronitrobenzene compound) with potassium fluoride under halide-exchange conditions in the presence of a catalyzing amount of a phase-transfer catalyst.

The improvement comprises using as said catalyst a salt of formula 1 above.

Oε AILED P ^g SCRIPTION Of THE INVENTION AKD OF THE MANNER AND PROCESS OF MAKING ANO USING IT

Radicals included by R^ are for exasple 3-heρtyl, 2-octyl and 3-octyl. Preferably, R ³ has from 5 to 8 carbon atoms. Preferred R ³ radicals include secondary heptyl and secondary octyi.

In a preferred aspect, each of R^ and R~ has at least 2 carbon atoms. In this preferred aspect, radicals included by R- ⁴ are for example 3-heptyl and 3-octyl. Preferably, R ³ is 3-heptyl. Advantageously R and R ² are subtituted or unsubstituted hydrocarbon radicals having from 2 to 6 carbon atoms, such as methyl, butyl (e.g. n-butyl) and hexyl (e.g. n-hexyl). A preferred group of R*-N-R2 moieties includes dimethyla-mino, d i-n—butylamino and di-n-hexyla-mino. Another preferred --N-R2 moiety is -meth 1 i eridinylamino.

Included within the N-sec-alkyl-diorganoamino- pyridinium salts of formula (1) are, for example, ( ) N-3-heptyl-4-(N" ,N'-di-n-butylamino) yridinium chloride which has the formula

(ii) N-2-octyl-4-(N* ,N'-dimethyla ino) yridinium chloride which haβ the formula

CH

(lii) N-3-heptyl-4-( 4'-methylpipβridinyl) pyridinium chloride which has the formula

CK ₃ C

(iv) N-3-octyl-4( ' ,N*- i-n-butyl)pyridinium chloride which has the formula

n

(v) N-4-heptyl-4-(N' ,N*- i-n-butylamino) pyridinium chloride which has the formula

⁽ vi ⁾ N-3-h ^β ptyl-4-(N' ,N'-di-n-h«xylamino)pyri _d inium chloride which has the formula

The N-alkyldiorganoaminopyridinium salts of formula (1) can be made by alkylating diorganoamino- pyridines which can be made by reacting 4-hydroxypyridine with phosphorous pentoxide and a diorganoamine at 200 ^* C to 5300 ^# C, for example, 250 C as shown by the following equation:

50-80* where R! and 2 are as defined above. The alkylation of the above diorganoamino- pyridines can be achieved in a straight forward manner utilizing such reagents as 4-heptylbromide, 2-octylbromide , 3-heptylbromide , 3-octylbromide , etc. at ambient temperatures in an inert organic solvent, for example, chloroform or toluene. Reaction with such alkyl compounds, as well as the corresponding tosylate or mesylate can be facilitated by using higher temperatures such as refluxing toluene, or temperatures up to about 150*0

A preferred salt for use as a phase transfer catalyst in preparing fluoroaromatic (e.g. FNB) compounds from corresponding chloroaromatic (e.g. CNB) compounds is the salt of formula (i) . The best salt contemplated for 5 such use is the salt of formula (vi) .

The halide-exchange conditions generally include elevated reaction temperatures, which are high enough to provide sufficient energy of activation for the reaction. Although such reaction temperatures might cause some 0 catalyst inactivation, the temperature is preferably not so high as to cause rapid decay of catalytic activity or substantial decompostion of the reactants, the products, or the solvent. Although the reaction temperature may vary, depending upon the particular catalyst, solvent, and ~ reactants used, generally it may be, for example, from about 120°C to about 220 ^β C, preferably from about 160°C to about 215°C, and more preferably from about 205 ^β C to about 215°C.

Those skilled in the art will appreciate that a 0 variety of equipment and techniques may be utilized in the method of the present invention, and the invention is not limited to any particular equipment or technique. The method is generally conducted by charging the reactants, solvent and PYR salt catalyst into a reaction vessel which 5 is equipped with agitating and heating means. Advanta¬ geously, the entire amount of the reactants, solvent and PVK salt catalyst to be employed can be added initially. The reaction vessel may also advantageously include a reflux condenser or other means of recovering solvent 0 vapors and means for blanketing the reaction mixture with a dry inert gas, e.g., nitrogen. The reaction mixture is heated to the desired reaction temperature and agitated.

The halide-exchange reaction conditions employed in the present invention advantageously include substan- 5tially anhydrous reaction conditions. The presence of

watec in t _h e reaction can diminish yields and cesult in undesira _b le by-products. Various techniques may be used for dehydrating the reactants and solvent, such as vacuu -ιm ^r drying, azeotropic dis illation, chemical drying and the 5 like. Azeotropic distillation, for example with benzene, can _b e used for drying all of the reactants and solvents; _h o _w e _v er, any convenient and operable technique may be employed. Due to the deleterious effect of water, the reaction mixture is preferably substantially devoid of

10 water. Small amounts of water may be tolerated; however, a corresponding reduction in yield is generally experienced. Advantageously, the concentration of water in the reaction mixture is below about S wt. I and is preferably below about 1 wt. 1. based on the weight of the reaction

15 mixture.

The solvent for the catalyst, chloroaromatic ⁽ e.g. CNB ₎ compound, and fluoroaromatic (e.g. FNB ⁾ compound is an aprotic, polar, organic solvent, which preferably has a rela ^¬ tively high boiling point, e.g., a boiling point above about

20 190-C. Lower boiling solvents may be used; however, pressure reactors may be required for their containment. Solvents having boiling points below a desired reaction temperature may be employed by conducting the reaction under super tmospheric pressure in such reactors. Examples 5 of reaction solvents include d imethylsul oxide , sulfolane. _b is ₍ 2-me _th oxyec _h yl ₎ et _h er. bis 2-( 2-m thoxyethoκy ⁾ et ^h yl et _h er, hexamethylp _h osphocamide . N-methy1pyrol id inone , and _d imethylformamide. Dimet _h yl formamide and sulfolane are preferred solvents. Sulfolane is most preferred from the 0 standpoint of commercial attrac iveness.

The phase-transfer catalyst employed in the pres¬ ent method Is "luble - " <- « "action solvent in an amount sufficient to catalyze the reaction. The PYR salt may be

eraployed in any catalyzing amount, i.e. , in any amount effective for catalyzing the conversion of the chloroaromatic (e.g. CNB) compound to the corresponding fluoroaromatic (e.g., FNB) compound. In general, the amount may correspond, for example, to a molar ratio of PYR salt to chloroaromatic (e.g. CNB) compound of from about 0.005:1 to about 0.5:1, preferably from about 0.04:1 to about 0.15:1, most preferably about 0.08:1. In general, amounts of PYR salt corresponding to molar ratios of less than about 0.005:1 may not provide sufficient catalytic activity, while amounts corresponding to molar ratios of more than 0.5:1 may result in insufficient additional benefit to justify the additional cost. As indicated above, the entire amount of PYR salt to be used is preferably added initially. However, if desired, a portion may be added initially with incremental addition of the remainder during the course of the reaction. Incremental addition may be, for example, substantially in accordance with the invention disclosed in the above-cited White patent.

The fluoride ion is provided by an alkali metal fluoride salt which is generally present in an amount at least substantially stoichiometric to the chloro¬ aromatic (e.g. CNB) reactant. Preferred fluoride salts are I 5 potassium fluoride, rubidium fluoride, and cesium fluoride, and potassium fluoride is particularly preferred. The fluoride salt is advantageously finely-divided, to provide a greater superficial surface area which is accessible to the catalyst and the chloroaromatic (e.g. CNB) compound. 10Preferred concentrations of the fluoride salt range from about 1 to about 2 times the stoichiometric amount, most preferably from about 1.2 to about 1.6 times such amount. For example, in a method for producing a mono luoronitrobenzene compound, a preferred molar ratio of 5 fluoride salt to chloronitrobenzene compound is about 1.5:1. Lower concentrations of fluoride salts can result in diminished reaction rates, and, although higher concentrations can be used, no appreciable benefit is generally realized therefrom. 20 In the chloronitrobenzene compound used as a starting material in the present invention, the relative positions of the nitro and chloro substi uents, and the presence of other substituents on the ring can affect the reactivity of the starting compound. Generally, halogen 25exchange reactions involve compounds in which the chloride is in the ortho or para position with respect to the nitro group, and reactivity may increase when other electron-wi hdrawing groups are present on the ring. Compounds having chloro substituents in the meta as well as 30 ortho and/or para positions may be used as starting materials, but usually only the chloro groups in the ortho and para positions will undergo halogen exchange. Accordingly, the method of this

invention may be used for example for the synthesis of compounds such as 2- luoroni robenzene, 2-fluoro-3-chloro- ni robenzene, 4- luoroni robenzene. 2,4-difluoronitroben¬ zene, 5-chloro-2 ,4-di fluoroni trobenzene, and the like, from corresponding chloronitrobenzene compounds. The present method is particularly useful for the preparation of 4- luoronitrobenzene from 4-chloronitrobenzene and 2-fluoroni robenzene from 2-chloronitrobenzene.

The reaction is generally allowed to proceed until substantially all the chloroaromatic (e.g. CNB) compound has been converted to the corresponding fluoroaroβa ic (e.g. FNB) compound. A reaction time of from about 10 minutes to about 20 hours may typically be used, and the reaction will often be substantially complete after about 1 to about 6 hours. After the reaction is completed, the product can be recovered by any suitable procedure, such as extraction, istilla ion, steam distillation and the like. For some purposes, the purity of the crude reaction product, recovered as an organic phase after addition of water to the reaction mixture, will be satisfactory.

The method of this invention has been found to produce fluoronitrobenzene compounds in good yields with little formation of by-products.

Although the above description of the improved hal ide-exchange process of this invention has been given principally with reference to effecting conversion of chloro¬ aromatic (e.g. CNB) compounds to corresponding fluoro¬ aromatic (e.g. FNB) compoundβ in the presence of a solvent, the halide-exchange reaction can be carried out as a neat (i.e., solventless) reaction with the chloroaromatic (e.g. CNB) compound in "the melt" (i.e. in a molten state).

Chioroaromatic compounds suitable for use in the process of this invention include an acomatic ring, at least one chlorine atom as a substituent on the aromatic ring and at least one activating substituent located in an activating position on the ring for facilitating the desired nucleophilic substitu ion, i.e., exchange of fluorine for the chlorine. The activating substituent is an electron-w thdra ing agent, in¬ cluding for example: nitro; cyano; trifluoromethyl; chioro- carbonyl; luorocarbony1; phenylcarbon 1 wherein the phenyl moiety is unsubstituted or substituted with a substituent other than agents which are at least moderately strong electron- releasing agents (i.e., substituted with, for example, chloro, nitro, cyano, tri luoromethy I , and linear or branched alkyl qroups, preferably having from 1 to about 12 carbon atoms): henylstfl onyl wherein the phenyl moiety is unsubs i u ed or substituted with a substituent other than agents which are at least moderately strong eLee ron-releas ing agents (i.e. , substituted with, for example, chloro, nitro, cyano, trifluoro- methyl and linear or branched aLkyl groups, preferably having from L to about 12 carbon atoms); and a combination of three, four or five additional chlorine atoms. In general, the chlorine atoms to be exchanged are in the ortho and/or para positions relative to the activating agent.

The aromatic ring may be, for example, a benzene ring or a pyridine ring.

Suitable chloroaromatic compounds for use in this invention include, for example:

(a) 2-chlorobenzonit i le

4-chiorobenz ^' onitrile

2-chlorobenzo 1 chloride

4-chlorobenzoyl chloride

2-chlorobenzo 1 fluoride

4-chlorobenzo 1 fluoride

2-chlo o-benzot i Luoride

4-c loro-benzot i luo ide tetrachlorobenzene pentachlorobenzene hexachlorobenzene

(4, '-dichloro-)diphenylsulfone , ' -dichlorobenzophenone

3-chloro-phthal c anhydride

4-chloro-phthal c anhydride

3-chloro-phthalo 1 dichloride

4-chloro-phthaloy1 dichloride l,4-d chloroanthracene-9,10-dione -chloro- -( rifluoromethyl )pyrid ne

3-chloro-4-cyanop id ne

3-chloro-4-nitrop ridine.

2-chloroni robenzene

2, 3-dichloronitrobenzene

4-chloronitrobenzene

2 , 4-d ichloroni robenzene and

2,4.5-t ichloron robenzene.

The luoroaroma ic compounds resulting from carrying out the process of this invention using the illustrative chloroaromat c compounds (a) through (z) above are set forth below, followed by utilities for such resulting compounds:

2-fluorobenzon t ile

4-fluorobenzonitri le

2-fluorobenzoyl chloride

4- luorobenzoyl chloride

2- luorobenzoyl fluoride -fluorobenzoyl fluoride

2- luorobenzot i luoride

4-fluo obenzo ifluoride tet afluorobenzene 0 pen a luorobenzene hexafluorobenzene

( 4 , 4 '-di luoro-)diρhenylsulfone

4 , 4 ' -difluorobenzophenone

3-f luoro-phthal ic anhydride 5 4- luoro-phtha1 ic anhydride

3- luoro-phthaloyl dichloride

4-fluoro-phthaloyI dichloride

1, 4-d fluoroanthracene-9 , 10-d one

3-fluoro-4-(tci luo ome hyl Jpyridine

3- luo o-4-cyanoρy id ne

3- luoro-4-nitroρyridine.

2- luo onit ob nzene

2-fluo o-3-chloron trobenzene

4-fluoronitrobenzene

2 , -difluoronitrobenzene and

5-c oro-2,4-di luoronit obenzene.

Fluoroaroma ic compounds (a) through (f) can be hydrolyzed to the corresponding luorobenzoic acids, which are useful as interme iates for preparing herbicides and liquid

crystals. The trifuoromethyl products (g) and (h) are useful as intermediates for preparing herbicides and medicinal agents such as flumetramide. The polyfluoro- benzene compounds (i), (j) and ( ) are useful as intermediates for preparing plant growth regulators. The fluorosulfone compound (1) is useful as a crosslinking agent and as a monomer which can be polymerized to provide engineering plastics. The fluoroketone (m) is useful as a monomer which can be polymerized to provide engineering plastics. The fluoroanhydrides (n) and (o) and the corresponding acid chlorides (p) and (q) are useful for esterifying with polyols to prepare fluorinated polyesters which are useful as wear-resistant fibers. The fluorinated anthracene dione (r) can be converted by well known methods to 1,4-bis ((aminoalkyl)amino]-anthracene-9, 10-diones which are useful as antineoplastics. The fluoropyridine compounds (s), (t) and (u) and the fluoronitrobenzene compounds (v), (w), (x)/ (y) and (z) are useful as intermediates for making herbicides and dyes.

Praccice of this invention is further illus¬ trated by Che following non-limiting examples. All pares, percents and other amounts throughout this disclosure are by weight unless otherwise indicated.

EXAMPLE I

Me hanesuifon l chloride: (16.8 grams, 0.146 mole), 3-heptanol (17.6 grams, 0.146 mole) and toluene (200 ml) were mixed in a 500-ml round bottom flask. To the resulting mixture was slowly added triethyla ine (15 grams, 0.148 mole). The temperature of the resulting second mixture increased during the addition but it was maintained below 50 ^β C. The second mixture was stirred for a short period until the resulting reaction to the mesylate of 3-heptanol was sub- stantially completed, followed by cooling over about 15 minutes to room temperature (about 20°C) . Insoluble salts (principally amine hydrochiorides) were then removed from the second mixture by filtration. The resulting filtrate was added to a 500-ml round bottom flask (equipped with condenser, heater, stirrer and thermometer) containing N,N-dibutyiamino- pyridine (30.1 grams, 0.146 mole). The resulting mixture was refluxed for 3 hours and toluene was then removed under reduced pressure. The resulting residual oil was dissolved in dichioromethane (about 200 ml) and the result- ing solution was washed twice with lOO ml of saturated aqueous solution of sodium chloride. Dichioromethane was then removed under reduced pressure. Based on method of preparation, the resulting product (an oily salt) was N-(3-heptyl)-4-(N' ,N'-di-n-butylaraino) pyridinium chloride.

EXAMPLE II A mixture of 100 grams (Q-,635 mole) of 4-chloro- nicrobenzene (4-CNB) and 2 grams (0.00565 mole) of the N-3-hepCyl-4-(N' ,N'-di-n-buCylaraino) pyridinium chloride 5 prepared in Example I was heated sufficiently to melt the 4-CNB (co about Uθ-t2θ°C). Next, 56.6 grams (0.974 mole) of poCassium fluoride (oven dried aC 110"C under reduced pressure) was added Co the mixture. The resulting reaction mixture was heaCed to 210 ^β C with stirring for 4 hours, at

10 which time analysis of a sample of the reaction mixture by high pressure liquid chromatography (HPLC) showed a 60:40 ratio of the desired 4-fluoronitrobenzene product (4-FNB) to unreacted 4-CNB} The HPLC analysis was made using a Waters Bondapak* Ct8 reverse phase column, a 2-raicroliter

15 sample loop, a UV detector aC 254 nanometers and a dual pump. The solvent sysCera was a 1:1 raixCure of Che flows from pump A (1:1 methanol:water) and pump B (methanol). The combined flow ra e as 1.5 microiiters per minute. The peak areas of the resulting FNB (and residual CNIJ were measured using a

2 ₀ digicai inCegraCor. The above 60:40 racio is Che ra io of Che peak area of FNB to the peak area of CNB. This corres¬ ponds to about 60 mole percent conversion of the CNB to FNB and at a fast rate.

The resulting fluoronitrobenzene product can be

₂ 5 recovered in good yield by discontinuing heating and removing Che produce as disCiiiaCe by simple disCiilaCion under increa¬ singly lower pressure (co abouc 100 mm Hg absoluCe) , while heating as necessary Co raainCain an accepCable disCiilaCion race (e.g. aC a cemperaCure of Che mixCure of approximaCely

30 135-150 ^β C.

The above reaction procedure can be carried out wich similar resulcs in an aprocic polar solvenC such as sulfolane, followed by recovery of Che resulcing FNB product

in accordance with the above distillation procedure.

EXAMPLE III

Following the procedure of Example I except as indicated, methanesulfonyl chloride (35.53 grams, 0.3 mole) was reacted with an equimolar amount of 2-octanol in CH3CN (100 ml) in the presence of triethylamine (31.37 grams, 43.2 ml) to yield a mixture containing the mesylate of 2-octanol (0.3 mole, 62.4 grams theoretical). After removing insoluble salts (principally amine hydrochlor- ides) by filtration of the mixture, the filtrate was added to a solution of 4-dimethylaminopyridine (36.66 grams, 0.3 mole) in acetonitrile (100 ml). The resulting solution was refluxed for 4 hours. Acetonitrile was then removed from the resulting mixture under reduced pressure. The residual brown oil was dissolved in dichioromethane (100 ml) and the resulting solution was washed twice with 100 ml of saturated aqueous solution of sodium chloride. The resulting dichioromethane layer was contacted twice with 5 grams of charcoal and dried over magnesium sulfate. Dichioromethane was then removed under reduced pressure. The resulting brown oil was "recystallized" as a salt in two crops from a mixture of 100 ml of ethyl acetate and 4 ml of acetonitrile. Based on method of preparation, the resulting product was N-(2-octyl)-4-(N' ,N'-dimethylamino)- pyridinium chloride, which was obtained in amounts of 7.20 grams (first crop) and 2.90 grams (second crop) for a total of 10.1 grams (10% yield).

It is contemplated that the product can effectively be used as the phase transfer catalyst in the procedure of Example II.

BEST MODE CONTEMPLATED

The best mode contemplated for carrying out this invention has been set forth in the above description, for example, by way of setting forth preferred materials and operating conditions, including but not limited to preferred ranges and values of amounts and other non-obvious variables material to successfully practicing the invention in the best way contemplated at the time of executing this patent application.

It is understood that the foregoing detailed description is given merely by way of illustration and that many modifications may be made therein without departing from the spirit or scope of the present invention.