PROCESS FOR CONDUCTING CHEMICAL REACTIONS WITH FORMALDEHYDE

Abstract: A formaldehyde reactant is provided to a chemical process or reaction, in the form of a formaldehyde-alcohol complex, by contacting paraformaldehyde with from about 0.25 to about 3 mole equivalents of an aliphatic alcohol in the presence of a catalytic amount of a base. In a preferred embodiment the chemical process is a process for the production of an aromatic azomethine by reaction of an aniline with formaldehyde. The azomethine may then be used to produce a haloacetanilide.

Description: PROCESS FOR CONDUCTING CHEMICAL REACTIONS WITH FORMALDEHYDE Background and Prior Art This invention relates to the use of formaldehy reactants in chemical processes or reactions, particular those conducted in the presence of, or which generate som water. In a preferred embodiment, this invention relates a process for production of azomethines by reaction of an a line with formaldehyde, and also to a process for producti of haloacetanilides from anilines by reaction of the latt with formaldehyde to form azomethines, reaction of the az methine with an acyl halide and, if an N,N-disubstituted hal acetanilide is the ultimate product, further reaction with appropriate agent, for instance, an alcohol. Processes of this general type, resulting in t formation of haloacetanilides are described, for example, U.S. Patents 3,630,716, 3,637,847 and 4,097,262. In all thr patents, the first step involves the reaction of an optional substituted aniline with formaldehyde to produce an azomethi according to the general reaction In such processes, the physical state and nature the formaldehyde can pose handling and recovery problem Formaldehyde is generally commercially available in the fo of either an aqueous solution, such as formalin, or soli paraformaldehyde. Formalin, being a liquid, is easier handle than solids but the large amounts of water and alcoh associated with formalin pose disposal problems. Paraforma dehyde, being a polymeric solid, is less reactive and can fo polymeric impurities. Furthermore, if removal of unreact paraformaldehyde from the reaction mixture is require filtration or sublimation at elevated temperatures would necessary. These require expensive and high maintenance eq ment on the one hand, or can produce degradation of the d sired product (due to elevated temperature) , as well as fou ing of condenser tubes and other apparatus by deposited par formaldehyde. Additionally, formaldehyde related impuriti can be carried through the process, resulting in impuriti in the ultimate product. U.S. Patents 3,630,716 and 3,637,847 describe (e amples 36-47 of each) reaction of various anilines with fo maldehyde used in the form of the trimer trioxymethylene. some of these examples, the reaction is conducted in the pr sence of a small amount of tri ethylamine in ethanol, whi in other examples, no trimethylamine or methanol was presen This appears to be explained by the comments in British Pat 1,078,072, that "basic catalysts", such as trimethylamin may be used to neutralize any formic acid present in the fo maldehyde. The patent points out, however, that the reacti will proceed in the absence of a catalyst and this is demo strated by the presence of other examples in the two U. patents in which no catalyst was used. Two more recent patents provide expedients to dea with the problems of formaldehyde handling referred to above U.S. Patent 4,399,306 describes an overall proces for production of N-alkoxyalkyl haloacetanilides involving number of expedients, some of which are directed to the prob lems of formaldehyde handling. The patent points out that i the azomethine production step, formaldehyde is generally us in excess; that a stoichiometric amount of formaldehyde wil not result in complete reaction of the aniline. The paten further refers to the problems of formaldehyde in the reac tion products, including its appearance as an impurity in th azomethine as well as in the final haloacetanilide product This patent proposes a process which uses a stoichiometri amount of an aqueous formaldehyde solution in an apola solvent followed by dehydration to produce the azomethine d rivative. The aqueous formaldehyde solution is removed at temperature of 80°c to 140 β C. However, as pointed out abov the aqueous formaldehyde solution so removed must be dispos of. U.S. Patent 4,491,672 of Richarz et al. purports solve the problems arising from use of formaldehyde by carr ing out the production of the azomethine without a solven followed by distillation of the water at a pressure of le than 500 mbar, the distillation being carried out in the pr sence of an alcohol having a boiling point below 160°C. this process the formaldehyde is used in the form of a gas a compound which "forms formaldehyde under the reaction con tions, e.g. paraformaldehyde or trioxane". Paraformaldehy appears to be preferred. The present invention, however, provides formald hyde in a form which is more reactive and more usable, a which additionally can be recovered for reuse in the proces Summary of the Invention In brief, this invention relates generally to means for providing a formaldehyde reactant to a chemical p cess or reaction, comprising contacting paraformaldehyde wi from about 0.25 to about 3 mole equivalent of an aliphat alcohol, in the presence of a catalytic amount of a base, a providing the product of said contacting to the process reaction as a formaldehyde reactant. In a more specific embodiment, this invention co prises a process for the production of an aromatic azomethi by reaction of an aniline with formaldehyde, in which the f maldehyde is provided by (a) contacting paraformaldehyde wi from about 0.25 to about 3 mole equivalent of an aliphat alcohol in the presence of a catalytic amount of a base; a (b) contacting the product of step (a) with the aniline form the azomethine. Detailed Description of the Invention According to the general aspect of this inventio a reactive form of formaldehyde is provided to a chemical p cess or reaction in which formaldehyde is a reactant, and p ferably in which water is present or is generated. The wat may be present in up to 300 mole percent. The formaldehy is provided to the process or reaction in the form of a pr duct resulting from contact of solid paraformaldehyde wi from about 0.25 to about 3 mole equivalent of an aliphat alcohol (as defined below) in the presence of a catalyt amount of a base. For purposes of convenience, the produ of this contacting step will be referred to as a "formald hyde-alcohol complex", though other terminology may be used. In the contacting step, solid paraformaldehyde mixed with a lower aliphatic alcohol together with a catal tic amount of a base, which serves to catalyze depolymeriz tion of the paraformaldehyde with the alcohol. The alcoh which is used in this process is a lower aliphatic alcoh containing a straight or branched chain alkyl group havi from 1 to 4, preferably from 1 to 2, carbon atoms. In t process of this invention, the alcohol is utilized in amount of from about 0.25 to about 3 mole equivalent, prefe ably from about 0.35 to about 2 mole equivalent, most prefe ably from about 0.35 to about 1 mole equivalent, with respec to formaldehyde. Preparation of the formaldehyde-alcohol complex i preferably carried out at a temperature of about 85-95°C. A inert solvent, for instance, an aromatic solvent such a xylene, may also be present, but is not required. It has be found that formaldehyde-alcohol complexes so formed may b stored for periods of up to a year, or even more, and remai stable. Therefore, it is possible to prepare a substantia amount of such a complex at one time, which may then be use over time as needed. The base utilized may be an organic or inorgan base such as an alkali metal hydroxide, alkoxide, carbonat or oxide, or a tertiary amine. Tertiary amines are preferr Typical catalysts for this technique include sodium hydroxi potassium hydroxide, sodium methoxide, trialkylamines such trimethylamine, triethylamine, and tri-n-butylamine, a heterocyclic amines including pyridine, N-alkylpiperidin and -pyrrolidines (for example, N-ethylpiperidine and N-met pyrrolidine) , tetraalkylguanidines and fused bicyclic amin such as l,8-diazabicyclo(5.4.0)undec-7-ene and 1,5-diazab cyclo(4.3.0)non-5-ene. The basic catalyst is generally us in an amount of from about 0.01 to about 1, preferably fr 0.01 to about 0.05 mole equivalent, based on formaldehyde. Without being bound by any theory, it is believ that the product formed between the paraformaldehyde and al phatic alcohol is a complex which may be or include a hem acetal or diacetal of formaldehyde. Preparation of such he acetals is suggested in the text Formaldehyde by Frederick Walker, for example, at page 202. In any even irrespective of the physical or chemical form of the forma dehyde, it is found that by the use of this technique, t reaction between aniline and formaldehyde proceeds almost i stantaneously, as opposed to prior art techniques in whi reaction is much slower. Additionally, only a small exce of formaldehyde is required as opposed again to prior art t hniques in which formaldehyde was used in substantial exces for example, in U.S. Patents 4,399,306 and 4,491,672. In a preferred embodiment, this invention relat to using such an alcohol-formaldehyde complex in a process produce an aromatic azomethine according to the reaction: In this process, an optionally substituted anilin is reacted with formaldehyde, producing an azomethine an water. The aniline in general has the formula in which R represents hydrogen or one or more substituent which are relatively non-reactive with formaldehyde, particu larly alkyl, alkoxy, or halogen; n is generally at a value o from 0 to 5, and is preferably 0, 1, 2 or 3. Herbicidal ani lideε or haloacetanilides are often prepared from aniline having one or more such substituents in the ortho positio (s) Some typical starting anilines for this process, when used t ultimately prepare herbicidal anilides or haloacetanilides, include 2,6-dimethylaniline, 2,6-diethylaniline, 2-___ethyl,6- ethylaniline, 2-methyl,6-tertiarybutylaniline, 2-tertiary- butyl,6-haloanilines, 2,4-dimethylaniline, 2-tertiarybutyl- 5,6-dimethylaniline, 2,6-dimethyl-3,4,5-trichloroaniline, 2- methylaniline, 2-ethylaniline, 2-methoxyaniline, 2-ethoxyani- line, and other anilines mentioned in the patents referred to in the "Background and Prior Art" section above. In the case in which the process to produce azo¬ methines is the first step in a multi-step process to produce herbicidal haloacetanilides, the final product (typically termed an α-haloacetanilide, or more commonly α-chloroacetan- ilide) has the general formula in which R and n are as described above; X is a halogen, usu ally chloro or bromo and most usually chloro, and R is an of a number of substituents which have been described as com ponents of herbicidal compounds, the most common of which te to be various alkyl and alkoxyalkyl groups. Other substitu ents are described, for instance, in U.S. Patent 4,097,262. As is known in the art, the reaction of the anilin and formaldehyde is generally carried out in a hydrocarbo solvent, which forms an azeotrope with water at the reflu temperature of the solvent. Typical solvents include aromat solvents such as benzene, toluene, and xylene, and aliphati and cylcoaliphatic solvents such as n-hexane, n-heptane an cyclohexane. Depending on the solvent, the reflux temperatu of the reaction will range from about 80°C to about 140°C Preferred reaction temperatures are between about 80°C an 100°C, with the solvent and/or pressure being appropriatel chosen. The process for forming an azomethine according t this invention can be carried out in one or two stages or re actors. In the two-stage embodiment, the formaldehyde-alco hol complex is produced by first forming the formaldehyde-al cohol complex, by combining the paraformaldehyde, alcohol and base catalyst in an appropriate apparatus and then con tacting the resulting product with the aniline reactant in solvent. This two-stage embodiment can be carried out in tw separate pieces of apparatus, one for the production of th formaldehyde-alcohol complex and the other for the conduct o the reaction of formaldehyde (in the form of the complex) wi the aniline. Alternatively, the two-stage process can be ca ried out in a single piece of apparatus, with the formalde hyde-alcohol complex first being produced, and the anilin and solvent thereafter added, and the temperature raised t the reflux temperature of the solvent. In the single stage embodiment, all materials—th paraformaldehyde, the alcohol, the base catalyst, the anilin and the solvent—are mixed in a single reactor at a tempera ture below the reaction temperature. The reactor temperatur is then raised to that appropriate for the reaction. Durin the time when the temperature is being raised, the parafor maldehyde reacts with the alcohol and base catalyst to for the formaldehyde-alcohol complex, and once the appropriat reaction temperature is reached, the complex and the anilin react to form the azomethine product. One advantage of the use of the present process ov the prior art is that in general the reaction to produce th azomethine is run under reflux. In the prior art technique utilizing solid paraformaldehyde, it had been necessary t heat the paraformaldehyde, which would sublime and deposit o the condenser. The present technique avoids this pluggin problem. The formaldehyde or the formaldehyde-alcohol compl will condense and reform as the formaldehyde-alcohol complex which is a liquid. Another advantage of the process as practiced usin this invention is that the formaldehyde-alcohol complex wil react almost instantaneously with the aniline. In general, the reaction of the formaldehyde reac tant with aniline to produce the azomethine is carried out a known in the art. The presence of some water in the reactio system (up to about a few mole equivalents with respect t the aniline) at the start of the process is permissible an in fact may even assist in the initiation of the reaction. Also, the presence of water is believed to aid in minimizin the production of a biεalkoxymethylaniline impurity. Of course, water is a product of the formaldehyde- aniline reaction. It is removed from the reaction products by distillation. The formaldehyde and alcohol, and/or formal dehyde-alcohol complex are also removed by distillation. Preferably in the present process, the distillation is co ducted continually during most of the course of the reactio beginning shortly after the reaction itself commences. T water is removed with the solvent. The distillation is aze tropic or zeotropic, depending on the solvent. The progre of the reaction can be followed by gas chromatographic anal sis or other monitoring technique such as analyzing a samp of condensate for moisture content. Gas chromatograph analysis can be utilized to monitor the reaction product f the azomethine content, and the reaction is generally consi ered complete when the azomethine content (expressed as a r tio of azomethine to unreacted aniline) reaches about 98% ( alternatively when residual aniline content is less than 2% If analyzing for moisture content, the reaction is consider complete when the moisture content of the distillate is le than 150 ppm. After the reaction is complete, the product cooled to ambient temperature. A further advantage of the use of formaldehyd alcohol complexes, both in general and in the azomethine pr cess, is that the complex is easily removed from the reacti mixture by evaporation. The condensate recovered from t azeotropic distillation contains unreacted formaldehyde, a cohol, solvent, water, and base (if an organic base such as tertiary amine was used) . This condensate can be separat into organic and aqueous phases, with most of the formald hyde contained in the aqueous phase. The aqueous phase m be treated to remove formaldehyde and/or alcohol, if nece sary, is properly further treated if need be, and discarde The organic phase can be reused to dissolve more paraformal hyde for the next run. In a process for production of haloacetanilid through the azomethine, the reaction product from the az methine process is cooled to the appropriate temperature a contacted in the conventional manner with a haloacetylati agent, usually chloroacetyl chloride, in an appropriate so vent (which may be an aromatic or aliphatic hydrocarbon so vent such as those used for the azomethine process) . The p duct in this reaction is a 2- or o-halo (preferably chlor N-halomethyl (preferably chloromethyl) acetanilide which h the formula in which X is halo (u romo) and R is hal methyl (chloromethyl or bromomethyl) . Haloacetanilides this type are described as herbicides in U.S. Paten 3,630,716 and 3,637,847. If desired, these haloacetanilides can be furth reacted with an aliphatic alcohol to produce an N-alkoxyalk α-haloacetanilide, as shown for example in U.S. Pate 4,399,306. It has been found that the use of the present i vention in the process for producing the azomethine can yie to improved results in terms of either product purity or yie or possibly both, of the final haloacetanilide product, pa ticularly when a three-step process is utilized to produce a N-alkoxyalkyl-α-chloroacetanilide. In the conventional processes for production o haloacetanilides from anilines, the several steps are usuall carried out in separate reactors or apparatus, with removal cooling and purification of the reaction product after eac stage. If preferable or convenient, haloacetanilides, inclu ing N-alkoxyalkyl-α-haloacetanilides, can be similarly pro duced from the azomethine-containing reaction products ob tained with the present invention. However, it has also bee found that the use of this invention can produce an azomethi containing reaction product of sufficient quality that subse quent steps can be carried out in the same reaction apparatu without need for purification of the product between steps This permits a "one-pot" type of operation of the complet haloacetanilide process. Such a one-pot process can have economic and envi ronmental advantages. There is a substantial reduction i capital costs. Fewer washing steps are needed, reducing th amount of liquid waste. Ammonium chloride solids recovere from the final step are relatively pure and may be used (o sold) for the purposes such as electroplating, explosive manufacture, etc. The following represents examples of the use of th process of this invention: EXAMPLE I This example represents the conduct of the azo methine process in a two-step fashion, in which the formalde hyde reactant is first prepared and is then combined with th aniline reactant. A) Production of the formaldehyde reactant. In a react were charged 3.0 mole paraformaldehyde, 3.0 mole ethanol, 0. mole triethylamine, 1.0 mole xylene and 0.5 moles water. Th mixture was then heated to 85-90°C and agitated until the so lution was clear. B) In a reactor were placed 1 mole of 2-methyl,6-ethyl aniline and 2 moles of xylene. The contents of the reacto were then heated to about 90°C. The reaction was allowed to proceed with azeotropic dis tillation under atmospheric pressure at a temperature of abo 95°C, ranging up to 126°C. The reaction mixture was sparge with nitrogen during the distillation. The formaIdehyde ethanol complex was introduced slowly during the azeotropi distillation in 5 aliquots of about 0.5 mole each. The rea tion was monitored during this time by gas chromatograph analysis for area percent. This was carried out by removi a sample of the reaction mixture and adding two drops of to about four drops of chloroacetyl chloride and about 3 of chloroform to produce the N-chloromethyl-o-chloroacetan lide derivative. The resulting mixture was injected into gas chromatograph and the area % concentration ratio of th derivative to the corresponding haloacetanilide lacking t N-chloromethyl group calculated. This anilide forms as a r sult of the reaction of the chloroacetyl chloride with u reacted aniline. The reaction product was light amb colored. Analysis of the N-chloromethyl derivative as abo gave 96-97 area % of the N-chloromethyl derivative (corre ponding to the azomethine) and 2-3 area % corresponding the starting aniline. EXAMPLE II This example illustrates conduct of a three-step proce to produce an N-alkoxyalkyl α-chloroacetanilide and also sh use of a formaldehyde-alcohol complex which had been prepar and then stored for more than one year. A) Preparation of the Formaldehyde-Ethanol Complex Solutio In a reactor equipped with an agitator, a condenser, a heating mantle was added 20 moles paraformaldehyde, 20 mol of ethanol and 0.4 moles of triethylamine. The mixture w slowly heated under atmospheric pressure to reflux, which b gan at about 90°C until a clear solution was formed. The fo maldehyde-ethanol complex was relatively clear with no pr cipitation of solids on being stored for more than a year. B) Preparation of Azomethine with Formaldehyde-Ethanol Complex Solutions that had been stored for over a year In a reactor equipped with an agitator, a condenser, hea ing mantle, dropping funnel and a condensate receiving flas was charged 474 g (6 moles formaldehyde) of a year-ol formaldehyde-ethanol complex solution prepared as above, a 1696 g (16 moles) of xylene. The mixture was heated to abo 90°C and 550 g (4.0 moles) 2-methyl-6-ethylaniline was gradu ally added to the xylene-co plex mixture. The mixture wa allowed to reflux while the aniline was being added. Wh all the aniline was added, the reactor was insulated and t azeotropic distillation began under atmospheric pressure The temperature of the reaction mixture was allowed to in crease to about 125°C. The distillation was then continue under vacuum. The progress of the reaction was monitored the gas chromatography method discussed in Example I. Th reaction was complete within two hours after distillation be gan. About 1200 ml overhead distillate was recovered. Th reaction gave an aniline to azomethine conversion of abou 98.4 by area % analysis. C) Preparation of the N-Chloromethyl-α-Chloroacetanilide Intermediate The azomethine intermediate obtained above was cooled t about 80 to 90°C to it, over 30 minutes, was added a solutio containing 484 g (4.2 moles) of chloroacetyl chloride and 42 g (4.0 moles) of xylene. This reaction gave a 96.7% conver sion of the azomethine to the N-chloromethyl-α-chloroacetani lide intermediate by gas chromatographic area % analysis. D) Preparation of 2-Methyl-6-Ethyl-N-Ethoxymethyl-2-Chloro- acetanilide About 2208 g (48 moles) of anhydrous ethanol was added t the reaction mixture containing the N-chloromethyl-α-chloro acetanilide intermediate. The addition of ethanol to th haloacetanilide mixture was done over 40 minutes at tempera tures ranging from 45-84°C. At the end of the ethanol addi tion, about 66.3 g (3.9 moles) of gaseous ammonia was intro duced to the reaction mixture through a dip tube at about 50 60°C. When the pH of the reaction mixture was about 8-9, th addition of ammonia was stopped and the reaction was consid ered complete. This reaction gave a 98.6% conversion of th haloacetanilide intermediate to the N-ethoxymethyl-2-chloro acetanilide. The reaction mixture was then filtered to remove the a monia chloride solids. The filter cake was rinsed with sma amounts of xylene to remove residual product. The clear fi trate was recovered and washed with about 800 ml of 0.2% H solution. The mixture was phase separated in a separato funnel and the organic phase was stripped at 95°C for abo two hours. The final product contained 95.1 wt. % pure d sired chloroacetanilide with about 1.0 wt. % of the no chloromethylated haloacetanilide impurity. EXAMPLE III This example illustrates the preparation of formaldehyde alcohol complex and production of an azomethine in a sing reactor. In a flask equipped with an agitator, a condenser, and condensate receiving flask, were placed the following mater ials, sequentially: Paraformaldehyde (91% pure, 52.8 g, 1.60 moles) Ethanol (2B, 36.8 g, 0.80 moles) Triethylamine (3.1 g, 0.03 mole) Xylene (850 g, 8.0 moles) 2-methyl-6-ethylamine (98% pure, 138 g, 1 mole) The reactor was insulated and then heated slowly unde atmospheric pressure to reflux, which began at about 90°C The mixture was held under refluxing conditions for about 1 minutes, and then azeotropically dried by collecting the dis tillate in the condensate receiver and allowing the tempera ture to rise. The atmospheric distillation was continued un til the temperature reached 115 β C, and thereafter under vacu um. The temperature was maintained at about 115 β C and th reactor pressure was reduced gradually to 300-320 mHg. After completion, the product was cooled to ambient tem perature. This product contained about 4.3 moles xylene weighed 600 g, and had a content of the desired azomethine about 140 g. The total volume of distillate collected w about 560 ml; of this, about 49 ml was aqueous. EXAMPLE IV This example illustrates the use of the invention in co ducting the "one-pot" process for production of 2-methyl- ethyl-N-ethoxymethyl-2-chloroacetanilide from 2-methyl-6-et aniline in a single reactor. A) Preparation of the Aromatic Azomethine Intermediate In a reactor equipped with an agitator, a condenser, he ing mantle, dropping funnel and a condensate receiving flas was placed 95 g (1.2 moles) of formaldehyde-ethanol compl solution that had been previously prepared as in Example and 680 g of xylene (6.4 moles). The mixture was heated about 95°C. Then, 110 g (0.8 mole) of 2-methyl-6-ethylamine was add to the formaldehyde complex-xylene mixture at about 95°C, o 20-30 minutes. The reaction mixture was allowed to refl for a few minutes. Then, azeotropic distillation was allow to proceed under atmospheric pressure until the temperatu reached 120°C. At this temperature, the distillation was c tinued under vacuum (maximum about 250 mm Hg abs.) until t reaction was done. The overhead distillate, including t portion collected from atmospheric distillation, was 488 (600 ml) . It had 46 g of an aqueous phase and 442 g of o ganic. The moisture content of the last portion of the di tillate was about 100 ppm. B) Production of the N-Chloromethyl-α-Chloroacetanilide Intermediate The reaction mixture containing the azomethine was cool to about 70°C. A solution containing 97 g (0.84 moles) chloroacetyl chloride in 130 g (1.2 moles) xylene was th added slowly to the azomethine mixture. The temperature the reaction mixture was maintained at about 70°C until a the chloroacetyl chloride was added. At the end of the add tion, the reaction was considered complete. The purity N-chloromethyl-chloroacetanilide intermediate was 98.9% a of the non-chloromethylated haloacetanilide impurity, 1.0 as determined by gas chromatography area %. C) Production of the 2-Methyl-6-Ethyl-N-Ethoxymethyl-2-Chl acetanilide Product The reaction mixture with the N-chloromethyl-α-chloroac anilide intermediate was cooled to about 50 β C. Then gradua there was added 442 g (9.6 moles) anhydrous ethanol. Throu out the ethanol addition, the temperature of the reaction m ture was kept between 45 to 60°C. At the end of ethanol a dition, gaseous ammonia was introduced to the reaction mixt through a diptube to neutralize the mixture to a pH of 8- At this point, the reaction mixture formed a slurry and w considered complete. A sample of the final reaction mixtu showed 99.4% 2-methyl-6-ethyl-N-ethoxymethyl-2-chloroacetan lide with 0.6% non-chloromethylated haloacetanilide impuri by gas chromatography area % analysis. The slurry was filtered to remove the ammonium chlori solids. A white filter cake weighing about 114 g (wet) w recovered. The filtrate was a clear light amber solution a was stripped of xylene and ethanol at about 95 β C under ful vacuum for about two hours. This reaction produced a 96. wt. % pure 2-methyl-6-ethyl-N-ethoxymethyl-2-chloroacetani lide with 0.6 wt. % haloacetanilide impurity. The yield wa estimated to be 87.3% of the desired product based on 2 methyl-6-ethylamine.

Claims: WHAT IS CLAIMED IS: 1. In a process or reaction in which formaldehyde a reactant, the step of providing the formaldehyde in the f of a product produced by contacting paraformaldehyde with f about 0.25 to about 3 mole equivalents of an aliphatic alco having from 1 to 4 carbon atoms in the presence of a cataly amount of a base. 2. In a process for production of an aromatic az methine by reaction of an aniline with formaldehyde, the st of providing the formaldehyde in the form of a product pr duced by contacting paraformaldehyde with from about 0.25 about 3 mole equivalents of an aliphatic alcohol having fr 1 to 4 carbon atoms in the presence of a catalytic amount a base. 3. A process according to Claims 1 or 2 in which t paraformaldehyde is contacted with from about 0.35 to about mole equivalents of the alcohol. 4. A process according to any of Claims 1-3 in whi the base is a tertiary amine. 5. A process according to any of Claims 1-4 in whi the base is a trialkylamine. 6. A process according to any of Claims 1-5 in whi the alcohol is a onohydric aliphatic alcohol having from to 2 carbon atoms. 7. A process according to any of Claims 2-6 in whic the aniline has the formula in which R is one or more of hydrogen, alkyl, alkoxy, or hal gen and n is an integer of from 1 to 5. 8. A process according to any of Claims 2-7 in whic the reaction of aniline and formaldehyde is conducted in th presence of an aliphatic, cycloaliphatic, or aromatic hydro carbon solvent. 9. A process according to Claim 8 in which the para formaldehyde is first contacted with the alcohol and cataly¬ tic amount of base, and the resulting product is then mixed with the aniline and solvent. 10. A process according to any of Claims 2-8 in which the paraformaldehyde, alcohol, base, aniline and optionally, solvent, are mixed and the resulting mixture is heated to the reaction temperature. 11. A process according to any of Claims 2-10 carried out with continuous distillation of the water of reaction and in which a condensate containing water, solvent, formaldehyde and alcohol is recovered from the distillation, the condensat is separated into aqueous and organic phase, and the organic phase is contacted with paraformaldehyde to provide formalde¬ hyde reactant to a subsequent conducting of the aniline-forma dehyde reaction. 12. A process according to any of Claims 2-11, furthe comprising reacting the azomethine with a haloacetyl halide to produce an N-halomethyl-α-haloacetanilide. 13. A process according to Claim 12 further compri ing reacting the N-halomethyl-α-haloacetanilide with an al phatic alcohol to produce an N-alkoxyalkyl-α-haloacetanilid 14. A process according to Claim 13 in which all r actions are conducted in the same apparatus, without remov of reaction products after each step. 15. A process according to Claims 13 or 14 in whi the N-alkoxyalkyl-α-haloacetanilide is 2'-methyl-6'-ethyl- ethoxymethyl-2-chloroacetanilide.

Inventors: RODRIGUEZ GILBERT, RODRIGUEZ, GILBERT
Applicants: RODRIGUEZ GILBERT, RODRIGUEZ, GILBERT
Application year: 1992
Main classification: C07C41
IPC codes: C07C41, C07C47, C07C231, C07C233, C07C249, C07C251