Inhibiting formation of foulants in acrylonitrile manufacture or recovery

Abstract: The invention comprises a method of inhibiting the formation of foulants such as residues, gums and precipitates, polymeric tars and other highly oxidized carbonaceous tars which can be formed in the process of manufacture and recovery of acrylonitrile. The method comprises adding to the liquid or gaseous phases passing through, or stored in acrylonitrile process equipment, an effective antifouling amount of a dispersant which is stable in the environment within an acrylonitrile process and is neutral to the equipment used for the manufacture of acrylonitrile.

Description: The invention relates to a method of inhibiting the formation of foulants which are generated in an acrylonitrile production unit. The use of dodecylbenzene sulfonic acid containing products as antifoulants and dispersants in a vinyl acetate monomer production process is disclosed in US-A-4,902,824 which claims the use of benzene sulfonic acids in solvents as antifoulants for the vinyl acetate manufacturing process. Similar fouling problems occur in other production processes, as well. Although many hydrocarbon production processes are superficially similar, it is often the case that compositions which are effective for a given application in one process are totally unsuitable in another. As the present invention shows, the fact that benzene sulfonic acids effectively disperse foulant in the vinyl acetate manufacturing process, is not determinative of whether benzene sulfonic acids would also disperse foulant in acrylonitrile manufacturing processes. The nature of the monomers and of the fouling species in these areas are very different as described below. US 3 691 226 discloses use of lignosulfonate metal salts to absorb acrylonitrile from water to minimise deposits which otherwise foul heat transfer surfaces of heat exchangers used to cool water before recycling it into the system. FOULING SPECIES Vinyl Acetate Manufacturing poly(vinyl acetate), vinyl acetate oligomers, polymeric aldehydes, oxidation products Acrylonitrile Manufacturing poly(acrylic acid) poly(acrylamide) poly(acrylonitrile) MECHANISMS OF FOULANT FORMATION Vinyl Acetate Foulant Poly(vinyl acetate) and the vinyl acetate oligomers are formed by the free radical polymerization of vinyl acetate. Vinyl acetate dimers are formed by the addition of acetic acid across the carbon-carbon double bond of vinyl acetate. Aldol condensation of the aldehyde species result in oligomers and polymers. Other polymers related to the ethylene oxidation in the reactor section can also contribute to the acetic acid tower fouling. Acrylonitrile Foulant Poly(acrylonitrile), poly(acrylamide), and poly(acrylic acid) are formed by the free radical polymerization of acrylonitrile, acrylamide, and acrylic acid respectively. Acrylamide and acrylic acid are the products of the hydrolysis of acrylonitrile. It is not known whether the hydrolysis occurs before or after the polymerization. FOULANT SOLUBILITIES Poly(vinyl acetate) is soluble in vinyl acetate. Poly(acrylonitrile) is not soluble in acrylonitrile. The following tables list solvents and nonsolvents for poly(vinyl acetate) and poly(acrylonitrile). Poly(vinyl acetate) is soluble in common organic solvents. Poly(acrylonitrile) is soluble in relatively exotic solvents, but not in the more common hydrocarbon solvents or water. The solvents for poly(vinyl acetate) have dipole moments in the range of 0 - 2 D. The solvents for poly(acrylonitrile) have dipole moments in the range of 0 - 4.3 D. Solvents For Polymers of Vinyl Acetate and Acrylonitrile poly(vinyl acetate) solvents poly(acrylonitrile) solvents 2,4-dimethyl-3-pentanol 1,1,1-trichloro-3-nitro-2-propane allyl alcohol 2-hydroxyethyl methyl sulfone benzene 2-oxazolidone acetone 4-nitrophenol acetic acid 1,3,3,5-tetracyanopentane benzyl alcohol N,N-dimethyl-α,α,α-trifluoroacetamide carbon tetrachloride/ethanol acetic anhydride chlorobenzene bis(2-cyanoethyl)ether chloroform bis(4-cyanobutyl)sulfone dichloroethylene/ethanol 20:80. chloroacetonitrile dioxane chloroacetonitrile/water ethanol/water cyanoacetic acid glycol ether esters dimethyl sulfone glycol ethers dimethyl phosphite lower aliphatic esters dioxanone methanol DMA tetrahydrofurfuryl alcohol DMF THF DMSO toluene ε-caprolactam ethylene carbonate ethylene oxalate fumaronitrile γ-butyrolactone hydroxyacetonitrile maleic anhydride malonitrile methylene dithiocyanate nitric acid N-formylhexamethyleneimine N-methyl-β-cyanoethylformamide N-nitrosopiperidine nitromethane/water (94:6) phenylene diamines sulfuric acid tetramethylene sulfoxide Nonsolvents For Polymers of Vinyl Acetate and Acrylonitrile poly(vinyl acetate) nonsolvents poly(acrylonitrile) nonsolvents saturated hydrocarbons hydrocarbons mesitylene chlorinated hydrocarbons carbon tetrachloride alcohols ethanol (anhydrous) diethyl ether ethylene glycol ketones cyclohexanol 3,4-dimethyl sulfolane diethyl ether 1,6-hexanediamine higher esters C > 5 propyl formate carbon disulfide formamide water DMF dilute acids diethylformamide dilute alkalies methoxyacetamide dimethyloxamide ethylene urea acetonitrile acrylonitrile methoxyacetomitrile 1 -hydroxypropionitrile dimethylmalonitrile 1,1-dimethylsuccinonitrile methyl thiocyanate hexamethylene dithiocyanate aliphatic nitro-compounds 1-nitrophenol diethyl sulfoxide bis(2-hydroxyethyl) sulfoxide diethyl sulfone The foulant species for each process are different. Poly(vinyl acetate) is soluble in its monomer. Poly(acrylonitrile) is not. Foulant in the vinyl acetate process can result from addition across the carbon-carbon double bond of the monomer molecule. This does not occur in the acrylonitrile process. In summary, the foulant species in the vinyl acetate and acrylonitrile processes exhibit different physical characteristics. These differences include physical properties, solubilities and reactivities. The interaction of dispersants with foulant material is dependent on properties like polarity (which correlates with dipole moment) and solubility. Thus, the fact that dodecylbenzene sulfonic acid effectively disperses poly(vinyl acetate), does not predict that it will effectively disperse poly(acrylonitrile), a material that has considerably different solubility characteristics. It would therefore be an advance in the art if one could simply add an effective amount of an antifoulant to such acrylonitrile process equipment, so as to minimize or eliminate the possibility of such foulants forming and inhibiting the ability to achieve maximum use of the acrylonitrile process equipment. The invention comprises a method of inhibiting the formation of foulants such as residues, gums and precipitates, polymeric tars and other highly oxidized carbonaceous tars which can be formed in the equipment for manufacture or recovery of acrylonitrile. The method comprises adding to the liquid or gaseous phases passing through, or stored in acrylonitrile process equipment, an effective antifouling amount of an antifoulant having the structure R-(SO 3 ) n M wherein R is a hydrocarbonaceous group having from 1 to 34 carbon atoms chosen from linear or branched alkyl groups, aromatic, cyclic, alkaryl, aralky, or alkenyl groups, alkyl diphenyl ether groups, dialkyl naphthaline groups, or mixtures thereof; M is chosen from the group consisting of H, alkali metals, alkaline earth metals, ammonium cations, alkylamine cations, quaternary amine cations, or mixtures thereof; and n ranges from 1 to 6. The dispersant which has been found that meets all of these requirements, i.e. a dispersant that can inhibit the fouling caused by polymeric tars, residues, highly oxidized carbonaceous tars and debirs, and similar foulants as described above, while being compatible with the environment and chemicals used to manufacture acrylonitrile, without causing difficulties in the manufacture of such monomer, are primarily those dispersants which are alkyl sulfonic acids. These alkyl sulfonic acids are exemplified by such materials as dodecylbenzene sulfonic acid, methyl sulfonic acid, toluene sulfonic acid, alkyldiphenyl ether disulfonic acid, dialkyl naphthalene sulfonic acid, dodecyl sulfosuccinic anhydride, dodecyl sulfosuccinic acid, dioctyl sulfosuccinic acid or sulfosuccinate and similar materials. These sulfonic acids may be used as is, or may be formulated in a compatible solvent, and may include, optionally, other dispersants, other surfactants, antifoaming agents corrosion inhibitors, and similar ingredients. The antifoulant is preferably admixed with an organic polar solvent selected from the group consisting of alcohols, ethers, esters, ketones, nitriles or mixtures thereof. The antifoulant formulation preferably used is one that contains dodecylbenzene sulfonic acid, and/or its salts, optionally admixed and/or dissolved in an organic polar solvent, such as butyl cellosolve, an alkyl capped diether material available in commerce. These antifoulants can contain from 1 to 100 weight percent alkyl sulfonic acid, preferably dodecylbenzene sulfonic acid, and/or its salts, admixed and/or dissolved in a polar solvent, such a butyl cellosolve, an alkyl capped diether material available in commerce. In addition, the dodecylbenzene sulfonic acid may be present as its salts, particularly its quaternary ammonium or amine salts by neutralizing the sulfonic acid with various bases or with various amines, including polyamines. In addition to the dodecylbenzene sulfonic acid, other hydrocarbonaceous sulfonic acids may be used in the invention. These sulfonic acids may be alkyl sulfonic acids which can include, such organic sulfonic acids as toluene sulfonic acid, methane sulfonic acid, alkyldiphenyl ether disulfonic acid, dialkyl napthalene sulfonic acid, dodecyl sulfosuccinic anhydride, dodecyl sulfosuccinic acid, and dioctyl sulfosuccinic acid or sulfosuccinate. Representative of these sulfonic acids are those having the structure: R―(SO 3 ) n M wherein R is a hydrocarbonaceous group having from 1-34 carbon atoms chosen from linear or branched alkyl groups, aromatic, cyclic, alkaryl, aralkyl, or alkenyl groups, alkyl diphenyl ether groups, dialkyl napthalene groups and mixtures thereof; M is H, alkali metals, alkaline earth metals, ammonium cations, alkylamine cations, quaternary amine cations, and the like, or mixtures thereof; and n ranges from 1 to 6, preferably between 1-4, and most preferably is 1-2. Also included in such effective sulfonic acids are structures which include alkyl aromatic sulfonic acids or alkyl naphthenic sulfonic acids, as will be described in detail hereafter. The organic polar solvents (protic and aprotic) to be used are solvents such as butyl cellosolve or any of the ethylene oxide based cellosolve capped ether solvents, and may also include such organic polar solvents as the diethyl ether of tetraethylene glycol, polyethylene and polypropylene oxide alkyl ethers, and generally may also include other ether solvents, such as diethyl ether. In addition, other polar solvents that also function include certain organic acids, such as acetic acid, or such other polar solvents such as diacetone alcohol, linear alkyl and branched alkyl alcohols, such as methanol, ethanol, propanol, isopropanol, t-butyl alcohol. Admixtures of these polar solvents may also be used. Many more common solvents may also be used effectively with the claimed invention; esters, such as ethyl acetate, ketones, such as acetone, nitriles, such as acetonitrile and acrylonitrile, water (when blended with some of the above solvents), and admixtures of the above solvents. Also included are aliphatic and aromatic hydrocarbon solvents, dimethylacetmide (DMAC), dimethylformamide (DMF), dimethyl sulfoxide (DMSO), and heavy aromatic naphtha. The alkyl sulfonic acids described above are preferred when used in process streams at concentrations ranging from 1 ppm to 20,000 ppm, based on the weight ratios of the additive formulation to the process stream to which the formula is added. However, hydrocarbonaceous sulfonic acids, or their formulations can function as antifoulants at treatment concentrations ranging from 1-20,000 ppm, preferably between 5-1000 ppm, and most preferably, between 10-100 ppm (wt. %) treatment acid based on the process stream being treated. Also, as can be seen, although the alkyl sulfonic acids can be used as amine salts, the activities of some amines, such as the heavy amine condensate salts are not as good as the activities of the free acids. Therefore, it is most preferred to use the sulfonic acids of the instant invention as the free acid. The following examples are presented to describe preferred embodiments and utilities of the invention. Example 1 A sample of fouling deposit was obtained from a fouled acrylonitrile plant cooler. The deposit sample was ground together with dimethyl sulfoxide (DMSO) and the resulting suspension was filtered through 0.45µm filter. The dark brown filtrate (saturated solution of the foulant) was used for dispersion testing. 15 mL of organic layer separated from heads bottoms stream (also obtained from an acrylonitrile plant) was placed in a conical test tube and was treated with 100 µL of the filtrate solution. Immediately, solid material precipitated from the solution. This tube was labeled A. Another tube, labeled B, was filled with 15 mL of organic layer separated from heads bottoms stream and 100 µL of the filtrate solution. This tube was treated with 50 ppm of the material of the invention. Both tubes were capped, shaken for a few minutes, and observed. Within minutes a solid material precipitated to the bottom of tube A. No such material was observed in tube B. The tube stayed homogeneous and precipitate free - the fouling material in tube B remained suspended in the solution. Example 2 The organic layer separated from heads bottoms was added to three graduated centrifuge tubes. The tubes were labeled C, D, and E. Tube C was treated with the material of the invention. Tubes D and E were not treated with the material of the invention. The foulant solution was added to each tube to simulate the introduction of acrylonitrile fouling material. Tube C remained homogeneous and precipitate free. Tubes D and E displayed insoluble material which precipitated to the bottom of the tubes within a short time period. Tube E was subsequently treated with material of the invention. The tube was capped, shaken, and observed. After a short time period, tube E approached the quality of tube C, which was homogeneous and precipitate free. Thus, the material of the invention increased the dispersity of the fouling material within the acrylonitrile matrix prior to the foulant precipitation and after the foulant precipitation. Example 3 Tubes C and D from Example 2 were evaluated at temperature extremes to determine the performance stability of the material of the invention. The temperature range of interest was from 8 °C (46 °F) to 80 °C (176 °F). Tube C remained homogeneous and precipitate free throughout the temperature range of interest.

Claims: A method of inhibiting the formation of foulants in acrylonitrile monomer manufacturing or recovers equipment which comprises adding to the liquid or gaseous phases contained therein an effective antifouling amount of an antifoulant having the structure: R-(SO 3 ) n M wherein R is a hydrocarbonaceous group having from 1-34 carbon atoms chosen from linear or branched alkyl groups, aromatic, cyclic, alkaryl, aralkyl, or alkenyl groups, alkyl diphenyl ether groups, dialkyl naphthaline groups, or mixtures thereof; M is chosen from the group consisting of H, alkali metals, alkaline earth metals, ammonium cations, alkylamine cations, quaternary amine cations, or mixtures thereof; and n ranges from 1 to 6. A method according to claim 1 wherein the antifoulant is selected from the group consisting of dodecylbenzene sulfonic acid, methyl sulfonic acid, toluene sulfonic acid, dodecyl sulfosuccinic anhydride, dodecyl sulfosuccinic acid alkyldiphenyl ether disulfonic acid, dialkyl naphthalene sulfonic acid, dioctyl sulfosuccinic acid or sulfosuccinate, and mixtures thereof. A method according to claim 1 or claim 2 wherein the antifoulant is admixed with an organic polar solvent selected from the group consisting of alcohols, ethers, esters, ketones, nitriles or mixtures thereof. A method according to claim 3 wherein the organic polar solvent is admixed with water. A method according to claim 1 or claim 2 wherein the antifoulant is admixed with a polar solvent selected from the group consisting of acetic acid, diacetone alcohol, dimethylacetemide (DMAC), dimethylformamide (DMF), dimethyl sulfoxide (DMSO), water and mixtures thereof. A method according to claim 1 or claim 2 wherein the antifoulant is admixed with a solvent selected from the group consisting of aliphatic and aromatic hydrocarbons and mixtures thereof. A method according to claim 1, claim 2 or claim 3 wherein the effective antifouling amount of antifoulant ranges between 1-20,000 parts per million antifoulant, based on the process stream being treated. A method according to claim 7 wherein the effective amount of antifoulant ranges between 5-1000 parts per million. A method according to claim 8 wherein the effective amount ranges from 10-100 parts per million antifoulant.

Inventors: COOPER FREDRICK L, KIBALA PIOTR A, WEISMILLER MICHAEL C, COOPER, FREDRICK L., KIBALA, PIOTR A., WEISMILLER, MICHAEL C.
Applicants: NALCO EXXON ENERGY CHEM LP, NALCO/EXXON ENERGY CHEMICALS, L.P.
Application year: 1998
Main classification: C07C253
IPC codes: C07C253, C07C255