CYCLIC PHOSPHONITRILIC HALIDE PROCESS

Abstract: Cyclic phosphonitrilic halide trimer is made in high yield and at a rapid rate by adding NH₃ or ammonium halide to a pyridine-hydrogen halide complex and adding phosphorus pentahalide and a solvent for the trimer (e.g. monochlorobenzene) and heating the mixture to above 90°C to form trimer which dissolves in the solvent and then separating the trimer-solvent phase from the residue phase of pyridine-hydrogen halide complex and recovering trimer from the solvent phase and recycling the pyridine-hydrogen halide phase to a subsequent procedure conducted in the same manner. The process can also be adapted to provide linear species in high yield also.

Description: Cyclic phosphonitrilic halides can be reacted with alkali metal alkoxides and aryloxides to form derivatives that can be used as hydraulic fluids, flame retardants, or as plasticizers for high molecular weight polyphosphazenes. The most common cyclic polyphosphonitrilic halide is phosphonitrilic chloride trimer. A major use for trimer is in the manufacture of high molecular weight substantially linear polyphosphonitrilic chloride. The high molecular weight polymers can be obtained by merely heating the purified trimer at 220-300°C for a period of 12-48 hours. Preferably the polymerization is conducted in the presence of a very small amount of a Lewis Acid catalyst, e.g. AlCl₃, BCl₃ and the like. The linear high molecular weight polyphosphonitrilic chloride can be substituted by reaction with alkali metal alkoxides and/or aryloxides to form elastomers having very useful physical properties. These elastomers can be compounded and cured to form useful articles of manufacture. The conventional method for making cyclic phosphonitrilic chloride is to react phosphorus pentachloride with an excess of ammonium chloride in a suitable liquid reaction medium (e.g. monochlorobenzene or sym-tetrachloroethane) at a temperature of 120-150°C. This reaction takes several hours to complete and yields a mixture that is 75-80% trimer. A process has been reported by W. Sulkowski et al., Chem. Stos 26 (2) p. 245-252 (1982), in which pyridine is added to a well-ground mixture of phosphorus pentachloride and ammonium chloride causing the temperature to rise sharply to 180°C causing strong boiling presumeably of the pyridine. The reaction is complete in minutes giving a low yield of cyclic phosphonitrilic chloride product consisting mainly of trimer and tetramer. The reaction can also be conducted in sym-tetrachloroethane using quinoline as the nitrogenous base. Although this process is very rapid, it is not practical on a large scale because the large exotherm over such a short reaction period leads to an uncontrollable reaction. Also the yield of cyclics is low. Several references, including U.S. patent 4,567,028 to Tanino, et al., disclose the use of an inert organic solvent, such as chlorobenzene, in connection with the use of pyridine. It has now been discovered that when polyphosphonitrilic halide is made by reacting phosphorus pentahalide with ammonium halide in a hydrogen halide complex of a nitrogenous base, that the polyphosphonitrilic halide product can be separated from the residual nitrogenous base-hydrogen halide complex and that this residual complex can be recycled as the initial reaction medium for a process in which NH₃ or ammonium halide is added to the residual complex which is then reacted with phosphorus pentahalide to form polyphosphonitrilic halide. The phosphonitrilic halide is dissolved in a solvent for recovery. The reaction also forms additional nitrogenous base-hydrogen halide complex. The polyphosphonitrilic halide-solvent phase can be separated from the residue and the residue can be recycled to a subsequent procedure conducted in the same manner. The process is most useful in making cyclic phosphonitrilic halides. A preferred embodiment of the invention is a process for making a cyclic or linear polyphosphonitrilic chloride containing from 3 to about 7 (PNX₂) units in the case of cyclics and about 1 to 10,000 or more (PNX₂) units in the case of linears wherein X is halogen, by reacting 0.5-5.0 moles of PX₅ with about 1.0 mole of NH₄X in a reaction medium comprising a hydrogen halide complex of a nitrogen base selected from pyridine, substituted pyridines or mixtures thereof. The polyphosphonitrilic halide is then separated from the reaction mixture and the remaining hydrogen halide complex is recycled as at least part of the initial reaction medium of the next run carried out in the same manner. A more preferred embodiment of the invention is a process for making cyclic phosphonitrilic halide containing from 3 to 7 (PNX₂) units wherein X is halogen, said process comprising: (a) mixing 1-20 moles of a hydrogen halide complex of a nitrogen base selected from pyridine, substituted pyridines and mixtures thereof with 1 mole of NH₃ to form a solution or slurry of ammonium halide in said nitrogen base and/or hydrogen halide complex thereof, said solution or slurry having an ammonium halide:nitrogen base or hydrogen halide complex thereof mole ratio of 1:1-20, (b) adding phosphorus pentahalide and a solvent for cyclic phosphonitrilic halide to said solution or slurry in an amount which provides 0.5-5 moles of phosphorus pentahalide for each mole of ammonium halide, (c) reacting the resultant mixture at a temperature above 90°C up to reflux to form said phosphonitrilic halide and hydrogen halide complex of said nitrogen base, and (d) separating a solution of said cyclic phosphonitrilic halide in said solvent from a second phase comprising said hydrogen halide complex of said nitrogen base. The preferred nitrogenous bases are those that include in their structure a pyridine ring. Examples of these are pyridine, alpha-picoline, a-picoline, gamma-picoline, quinoline, isoquinoline, 7-methylquinoline, 2,3-dimethylquinoline, lepidine, quinaldine, acridine, quinolinic acid, nicotinic acid, 2-aminopyridine, 2-phenylpyridine, and mixtures thereof. The most preferred nitrogenous base is the compound pyridine. The foregoing nitrogenous bases are referred to collectively as pyridine and substituted pyridines. In the following discussion pyridine will be used for exemplification but it is understood that any of the other nitrogenous bases may be substituted for pyridine but not necessarily with equal results. Instead of pyridine or substituted pyridines, other nitrogen bases can be used. These include any tertiary amine that will form a hydrogen halide complex which can be molten at reaction temperature without decomposing. The initial hydrogen halide complex of the nitrogen base could be made by merely adding hydrogen halide to the nitrogen base but this is not a preferred method. In a highly preferred method which will be described later the hydrogen halide complex is the recycled residue from a previous procedure. If one chooses to separately make the hydrogen halide complex, any hydrogen halide can be used that will form a nitrogen base complex that is molten at reaction temperatures including HCl, HBr, HF and HI or mixtures thereof but the preferred hydrogen halide is HCl. In the following discussion HCl will be used to represent the hydrogen halide with the understanding that any of the other hydrogen halides could be substituted for HCl. The amount of HCl added is preferably in the range of 0.1-2.0 mole parts per mole part of pyridine. More preferably the amount is 0.2-1.0 mole parts HCl per mole part of pyridine. This would require 1-5 mole parts of pyridine to adsorb 1 mole part of HCl forming 1 mole part of pyridine-hydrogen chloride complex. Under these conditions with excess pyridine it is believed that the mono-HCl complex forms but whether the mono- or di-HCl complex forms is not critical to the success of the process. The reaction of HCl with pyridine is exothermic. Temperature is not critical so it can be carried out over a wide temperature range. Preferably it is conducted at a temperature high enough to maintain a liquid phase. Pure pyridine-hydrogen chloride complex has a melting point of 82°C. In a preferred mode, NH₃ is then added to convert at least part of the pyridine-HCl complex to NH₄Cl in situ. In the following discussion NH₄Cl can be any NH₄X salt. The amount of NH₃ can range from 0.01-1.0 mole parts per mole part of HCl in the complex. More NH₃ can be added but this will not have any affect on the reaction. A more preferred range is 0.25-1.0 moles of NH₃ for each 1-5 mole parts of pyridine-HCl complex. The temperature of the reaction mixture during addition of the NH₃ should be high enough to maintain the pyridine-HCl complex in the liquid phase. Although pyridine-HCl has a melting point of 82°C the impure mixture needs to be higher than this temperature to remain molten. Phosphorus pentahalide can be added to the reaction mixture before the NH₃, concurrently with the NH₃ or after the NH₃. It is generally more convenient to add the phosphorus pentahalide after adding the NH₃. Any phosphorus pentahalide can be used such as PCl₅, PBr₅, PBrCl₄, and PBr₂Cl₃,for example. The preferred phosphorus pentahalide is phosphorus pentachloride, PCl₅ which will be used in the following discussion with the understanding that any of the other phosphorus pentahalides can be substituted for the PCl₅. In an alternate mode of operation, the PCl₅ can be added prior to the NH₃ Since there isn't any NH₄Cl present at this stage, this can be conducted at higher temperatures, i.e. above 70°C up to reflux. Then the NH₃ can be added all at once or over a period of time to form NH₄Cl which readily reacts with the PCl₅ above 90°C up to reflux. Alternatively solid NH₄Cl could be added. The relative amount of reactants used in this mode of operation are the same as in the preferred mode. Returning to the discussion of the preferred mode, the amount of PCl₅ added on a mole basis can be more or less than the amount of NH₄Cl formed by the addition of NH₃ to the pyridine-HCl complex. When an excess of PCl₅ is used, the reaction prefers to form a linear phosphonitrilic chloride oligomer containing about 1-10,000 or more (PNCl₂) units. When the desired products are linear phosphonitrilic halide oligomers, it is preferred to react a molar excess of PCl₅ with the NH₄Cl. A useful ratio is 1.0-5 moles of PCl₅ per mole of NH₄Cl and more preferably 1-3 moles of PCl₅ per mole of NH₄Cl. In order to maximize the amount of cyclics, the amount of PCl₅ should not greatly exceed the amount of NH₄Cl and preferably is equal or slightly less than the amount of NH₄Cl on a stoichiometric basis. The amount of NH₄Cl closely corresponds to the moles of NH₃ added to form the NH₄Cl. A preferred amount of PCl₅ is 0.5-1.2 mole parts per mole part of NH₄Cl formed in the reaction mixture. More preferably the amount of PCl₅ is 0.75-1.1 moles per mole of NH₄Cl in the reaction mixture and most preferably 0.9-1.0. The PCl₅ is preferably added as a solution or slurry in a solvent for the cyclic phosphonitrilic chloride trimer although the phosphorus pentachloride can be added in a dry or molten form and solvent can be added separately either prior to or after the addition of the PCl₅ or after the reaction is complete. Alternatively the pyridine-hydrogen chloride complex, before or after NH₃ addition, can be added to the solution or slurry of PCl₅ in the solvent for cyclic trimer. Instead of adding PCl₅, chlorine and PCl₃ can be added to form PCl₅ in situ. Useful solvents for cyclic phosphonitrilic chloride trimer include any liquid that is substantially inert under the reaction conditions and which can serve to dissolve the cyclic trimer when it forms. The preferred solvents are the mono or poly halogenated aliphatic and aromatic hydrocarbons, especially the chlorinated hydrocarbons such as chloroform, carbon tetrachloride, 1,1-di-chloroethane, 1,2-dichloroethane, 1,1,1-trichloroethane, and sym-tetrachloroethane. The solvent can have a normal boiling point from about 30°C up to 250°C or higher. In general, the solvent should boil well above room temperature and below the decomposition temperature of the reaction mixture. A useful temperature range is from 35°C up to 250°C. These include solvents such as methylene chloride, propyl chloride, methylene bromide, bromochloromethane, butyl chloride, 1,2-dibromoethane, 1,1-dibromoethane, 1,2-dichloroethane, 1,1-dichloroethane, dichlorobenzene, dibromobenzene, trichlorobenzene, dichlorotoluene, dibromotoluene, and chlorobromobenzene. The lower boiling solvents, for example those having a normal boiling point from 35°C up to 120°C are preferably used when the main reaction is conducted without a solvent and the solvent is added after the reaction to extract the phosphonitrilic halide. This extraction is preferably conducted at a temperature high enough to maintain the hydrogen halide-nitrogen base complex in a molten state so the very low boiling solvents will require pressure in order to prevent boiling during the extraction step. More preferably the solvent should have a normal boiling point of at least 90°C up to the decomposition temperature of the reaction mixture so that the reaction of PCl₅ + NH₄Cl can be carried out without resorting to a pressure reactor. These solvents include 1,1,2-trichloroethane, sym-tetrachloroethane, 1,1,1,2-tetrachloroethane, monochlorobenzene, 2-chlorotoluene, 3-chlorotoluene, 4-chlorotoluene, monochloroxylenes, o-dichlorobenzene, m-dichlorobenzene, and p-dichlorobenzene. Monochlorobenzene is the preferred solvent. As mentioned above the solvent should have a normal boiling point above about 90°C so that the reaction to form cyclic trimer can be conducted above 90°C without resorting to a pressure system although the reaction may be conducted under pressure if desired. For example pressures up to 68.90 bar (1000 psig) or higher can be used. More preferably the solvent will have a boiling point of 90°-200°C, still more preferably 110°-200°C and most preferably 120-150°C. The amount of solvent is not critical as long as it is sufficient to dissolve the cyclic phosphonitrilic chloride produced in the reaction. A useful range is about 1-100 parts by weight solvent for each part by weight phosphorus pentachloride used in the reaction. Usually the solvent is introduced into the reaction mixture along with the PCl₅. This is not a critical limitation, however, as the solvent can be added at any time. For example, the entire reaction can be run without solvent and the solvent only used at the end to extract the polyphosphonitrilic halide from the pyridine-hydrogen halide heel. Alternatively, the solvent can be introduced at any stage or at multiple stages since its main function is to dissolve the product and extract it into a solvent phase. The phosphorus pentachloride-solvent mixture can be added to the pyridine-hydrochloride complex and NH₄Cl all at once or it can be added over an extended period of time. On a large scale it is preferred to add the PCl₅-solvent mixture to the pyridine-hydrochloride complex and NH₄Cl also containing a solvent for cyclic phosphonitrilic chloride over an extended period of time, for example from 1-8 hours or more. Operating in this manner, the reaction forms cyclic phosphonitrilic chloride trimer rapidly and in high yield. To maximize linear phosphonitrilic chloride yield the reverse addition is preferred. When making cyclic trimer, the overall idealized reaction disregarding any pyridine-HCl complex consumed and formed and other phosphazene species formed is represented by the following equation: 3PCl₅ + 3NH₄Cl → (PNCl₂)₃ + 12HCl The HCl evolved in the reaction converts any pyridine or substituted pyridines present to their HCl complex. Shown in a sequential manner starting with the initial pyridine-HCl complex the reaction sequence can be depicted as follows: I 1-20 moles Py-HCl + 1 mole NH₃ → 1 mole NH₄Cl + l mole Py + 0-19 moles Py-HCl II I + 0.5-1.2 mole PCl₅ → 0.5-1 (PNCl₂) units + 1-20 moles Py-HCl + 1-3 moles HCl + 0-0.5 moles NH₄Cl + 0-0.2 moles PCl₅ Thus the second reaction (II) regenerates the pyridine-HCl (Py-HCl) complex consumed by the initial reaction (I) by NH₃ in forming NH₄Cl. In fact the amount of HCl formed in the reaction of NH₄Cl with PCl₅ is so great that even if the initial reaction mixture contained only pyridine and ammonium chloride, the final reaction mixture would be phosphonitrilic chloride and pyridine-HCl complex unless the original reaction mixture contained over 4 moles of pyridine per mole of PCl₅. Some of the reactions involved in the overall process are exothermic and require caution. For example, if Py-HCl is made by the reaction of pyridine and HCl the reaction is very exothermic and requires care. Likewise if PCl₅ is added to pyridine an exothermic reaction occurs in forming a pyridine-PCl₅ complex. If PCl₅ is added to a mixture of Py-HCl, pyridine and NH₄Cl at a temperature over 80°C a reaction will ensue forming either cyclic or linear phosphonitrilic chloride depending upon reactant ratios. The reaction of PCl₅ with NH₄Cl to form phosphonitrilic chloride is in itself endothermic but the reaction evolves 4 moles of HCl for each (PNCl₂) unit formed and the HCl will react exothermically with pyridine to form Py-HCl until all the pyridine is consumed. However, if PCl₅ is added to a mixture of Py-HCl and NH₄Cl, the reaction is not exothermic since the reaction of PCl₅ with NH₄Cl is endothermic and there isn't any free pyridine to react with the HCl evolved. In another embodiment, the NH₃ and PCl₅ are added to the pyridine-HCl complex concurrently in the desired mole ratio so that the pyridine-HCl complex functions as a reaction medium. Any pyridine-HCl complex converted to pyridine by reaction with NH₃ with pyridine-HCl is immediately converted back to pyridine-HCl by HCl generated in the overall reaction. For example both NH₃ and a solution of PCl₅ in a solvent (e.g. chlorinated aliphatic or aromatic hydrocarbon having a normal boiling point over 90°C) in the mole ratio of 1 mole part NH₃ per each 0.5-1.2 mole parts of PCl₅ can be fed to molten pyridine-hydrochloride complex and reacted at a temperature of 90°C up to reflux to form cyclic phosphonitrilic chloride trimer in a single step. The cyclic trimer will extract into the solvent phase and the second phase will be mainly pyridine-HCl complex which may contain some NH₄Cl. The amount of pyridine-HCl complex reaction medium should be 1-20 mole parts, more preferably 2-4 mole parts, per each mole part of NH₃ or PCl₅ depending on which of these is present in the lower mole amount. In another embodiment, PCl₃, chlorine and ammonia are all concurrently fed to a pyridine-hydrogen chloride complex at temperatures from melting up to 200°C or higher to form phosphonitrilic chloride in one step. As in the other embodiments, the product is recovered by solvent extraction and the pyridine-HCl residue is recycled. Following the reaction to form phosphonitrilic chloride and regenerate pyridine-HCl complex by any of the foregoing routes, the reaction mixture is allowed to separate into two phases, a solvent phase which contains the phosphonitrilic chloride and a pyridine-HCl complex phase. This separation should be conducted at a temperature high enough to maintain the pyridine-HCl complex in a molten form although on a small scale it can be cooled to solidify the pyridine-HCl complex and the solvent phase containing the phosphonitrilic chloride merely poured from the solidified pyridine-HCl complex. The separation can be readily conducted by draining the molten pyridine-HCl from the bottom of the reaction vessel or by decanting or syphoning the solvent-phosphonitrilic chloride solution from the top of the reaction mixture. Linear phosphonitrilic chloride oligomers can be recovered from the solvent phase by conventional means such as by distillation or by mixing the solvent phase with a medium that is a non-solvent for the oligomer but a solvent for the solvent. Cyclic phosphonitrilic chloride trimer can be recovered from the solvent phase by conventional means such as by distillation or crystallization. In a most preferred embodiment of the invention the molten pyridine-HCl phase left as a "heel" following removal of the phosphonitrilic chloride-solvent phase, is recycled to the next process sequence. This eliminates the necessity of separately forming an initial pyridine-HCl complex. In fact the initial cycle of the present process would most preferably be conducted without forming pyridine-HCl by the separate step of adding HCl to pyridine but would be conducted by (i) adding PCl₅ to pyridine to form a pyridine-PCl₅ complex, (ii) mixing and reacting the pyridine-PCl₅ complex with a slurry of NH₄Cl in a solvent such as monochlorobenzene at a temperature above 90°C to form phosphonitrilic chloride and pyridine-HCl complex or by (a) adding a solution of PCl₅ in a solvent such as monochlorobenzene to a slurry or solution of NH₄Cl in pyridine at a temperature below 80°C to form a mixture comprising a pyridine-PCl₅ complex and NH₄Cl in a solvent and then (b) heating this mixture above 90°C up to reflux to cause a reaction which forms cyclic and/or linear phosphonitrilic chloride and generates pyridine-HCl complex. After the initial cycle, the pyridine-HCl complex is separated and the pyridine-HCl heel is recycled in accordance with the present invention. Still another embodiment of the same invention comprises a process for making phosphonitrilic halide, said process comprising (a) mixing 1-20 mole parts of a hydrogen halide complex of pyridine or a substituted pyridine with 0.5-5 mole parts of phosphorus pentahalide and a solvent for said phosphonitrilic halide to form a resultant mixture, (b) adding 1 mole part of ammonium halide to said resultant mixture and reacting at a temperature above 90°C to form said phosphonitrilic halide, (c) separating the solvent phase containing said phosphonitrilic halide from the pyridine-hydrogen halide phase, (d) recovering said phosphonitrilic halide from said solvent phase and (e) recycling said pyridine-hydrogen halide phase as at least part of said hydrogen halide complex of pyridine or substituted pyridine used in step (a) of a subsequent procedure carried out in substantially the same way. In this embodiment ammonium halide is used in place of ammonia. Following this, the process is substantially the same as w hen ammonia is used. The preferred ammonium halide is ammonium chloride and the preferred phosphorus pentahalide is phosphorus pentachloride. The same solvents and the same ratios are used with ammonium halide replacing ammonia on an equal mole basis. In the above embodiment it is most preferred to use 0.9-1.0 mole parts of PCl₅ per mole of NH₄Cl when the desired product is cyclic phosphonitrilic chloride and to use 1.0-5 moles of PCl₅ when the desired product is linear phosphonitrilic chloride. The above embodiments have in common with the others the recycle of the pyridine-HCl heel to the start of the next cycle. It is also contemplated to be within the scoop of the invention to use an operating scheme that alternates between embodiments on different cycles in a series. In other words, the first cycle can be conducted by reacting PCl₅ and ammonium chloride in pyridine, either sequentially or simultaneously to form a phosphonitrilic chloride-solvent phase and a pyridine-HCl phase. The phases are separated and the pyridine-HCl phase recycled to the next cycle. In the second cycle, ammonia and phosphorus pentachloride could be added to the pyridine-HCl complex and reacted to form a phosphonitrilic chloride-solvent phase and a pyridine-HCl phase. The pyridine-HCl phase could again be recycled to the next cycle. In the third cycle, ammonium chloride and phosphorus pentachloride could be added to the recycled pyridine-HCl and reacted to form a phosphonitrilic chloride-solvent phase and a pyridine-HCl phase and so forth. All of the embodiments involve the reaction of an ammonia compound (e.g. NH₃ or NH₄Cl) and a phosphorus pentahalide (e.g. PCl₅) in contact with a pyridine-HX or substituted pyridine-HX reaction medium and, after removal of a solvent phase containing phosphonitrilic halide, the recycle of the pyridine-HX or substituted pyridine-HX heel to a subsequent cycle as part of the initial reaction components. Thus, an embodiment of the invention is a process for making phosphonitrilic halide in high yield and at a fast reaction rate by (a) reacting ammonia or ammonium halide or mixtures thereof with phosphorus pentahalide or its precursors such as P + Cl₂ or PCl₃ + Cl₂, in a reaction medium comprising a hydrogen halide complex of a nitrogen base selected from pyridine, substituted pyridines or mixtures thereof and a solvent for cyclic phosphonitrilic halide to form a solvent phase containing said phosphonitrilic halide and a residue phase comprising a hydrogen halide complex of said nitrogen base, (b) separating said solvent phase from said residue phase, (c) recovering said phosphonitrilic halide from said solvent phase and (d) recycling said residual phase to the next cycle as at least part of the initial reaction medium. Stated in another way to more clearly point out where the key features of the process reside, the invention is an improvement in the known process for making phosphonitrilic halide by reacting ammonium halide and phosphorus pentahalide. The improvement comprises conducting the reaction in a reaction medium comprising a hydrogen halide complex of a nitrogen base selected from pyridine, substituted pyridines and mixtures thereof and a solvent for phosphonitrilic halides to produce a solvent phase containing the phosphonitrilic halide product and a residual or heel phase comprising mainly a hydrogen halide complex of the nitrogen base and then recycling the residual phase to a subsequent cycle of the same process as at least part of the initial reaction medium. Alternatively the reaction can be conducted without any solvent and th solvent added at the end to extract the phosphonitrilic halide from the heel. The phosphonitrilic halide is recovered from the solvent phase by conventional methods. The preferred reactants and ratios in the overall process as stated above are of course the same as in the sub-generic embodiments of t he overall process. The manner in which the process is conducted is shown in the following examples. EXAMPLE 1 An Initial Cycle In a reaction vessel fitted with a stirrer, reflux condenser, thermometer and heating means was placed 1,033 grams monochlorobenzene, 495 grams PCl₅ and 121 grams NH₄Cl. Then 500 grams of pyridine was added in small increments of about 30-40 ml each. The addition schedule and temperature was as follows: Time (min.) Pyridine Increment (ml) Addition Temp. (°C) 0 0 3 35 29 4 0 5 35 41 6 40 42 7 30 43 8 45 47 9 50 51 10 15 52 11 remainder 54 The mixture was then heated to reflux (about 130°C) over a 10 minute period and maintained at reflux for 60 minutes. Heating and stirring was stopped and two phases separated. The upper solvent phase was decanted from the lower "heel" phase. The solvent phase contained 89.5 weight percent of the phosphorus initially charged as PCl₅. This has now been converted to polyphosphonitrilic chloride which analyzed 77.4 weight percent cyclic trimer, 3.5 weight percent cyclic tetramer and the remainder higher cyclics and linear oligomers. EXAMPLE 2 A Recycle Run Using NH₄Cl To a reaction vessel containing the molten pyridine-HCl heel from Example 1 was charged 121 grams of NH₄Cl. A solution of 495 grams of PCl₅ in 1,049 grams of monochlorobenzene was prepared by stirring and heating the mixture above 100°C. This PCl₅ solution was fed to the molten pyridine-HCl heel in three increments as follows. Time (min.) Temp. (°C) Remarks 0 141 feed 25 seconds 1 128 2 125 20 128 21 131 feed 25 seconds 22 129 24 126 47 130 49 131 feed remainder (30 sec) 51 123 56 120 62 122 The mixture was then heated to reflux and stirred at reflux for about 1 hour. Heating and stirring was stopped and the phases separated. On further cooling the lower pyridine-HCl phase solidified. The upper phase was removed and found to contain 99.5 weight percent of the phosphorus initially charged to the reaction. The polyphosphazenes in the monochlorobenzene phase were 80.8 weight percent cyclic trimer, 2.2 weight percent cyclic tetramer and the balance higher cyclics and linear oligomers. The heel from Example 2 was again recycled to Example 3 conducted in substantially the same manner as Example 2. The pyridine-HCl heel from Example 3 was in turn recycled to Example 4 conducted in substantially the same manner. The results with these further recycle runs using NH₄Cl were as follows. Example Heel Recycled From Example Percent of P in Solvent Product Trimer Tetramer 3 2 92.6 80.7 2.4 4 3 77.6 79.1 1.4 EXAMPLE 5 An Initial Cycle In a reaction vessel was placed 3173 grams monochlorobenzene, 1,485 grams PCl₅ and 363 grams of NH₄Cl. This mixture was stirred and then 1500 grams of pyridine was added as follows. Time (min.) Temp. (°C) Total Pyridine Fed (ml) 0 25 0 1 34 110 2 44 200 3 49 250 4 50 5 58 350 6 70 400 7 73 425 20 68 21 78 500 87 55 88 62 600 89 63 675 91 61 1531 93 58 110 95 112 131 (reflux) 114 125 134 124 242 131 Heating and stirring was stopped and the phases separated. The solvent phase contained 86.2 weight percent of the initial phosphorus charged as PCl₅. The phosphorus was in the form of phosphonitrilic chloride and analyzed 79.1 weight percent trimer and 4.9 weight percent tetramer. EXAMPLE 6 A Recycle Run Using NH₃ The molten pyridine-HCl heel from Example 5 was placed in a reaction vessel. Then 3,068 grams of monochlorobenzene was added following which 70 grams of NH₃ was added at 129°C. After standing overnight, the reaction mixture was reheated in the morning to melt the pyridine-HCl complex and NH₃ feed was resumed for 63 minutes at 124-129°C to feed another 70 grams of NH₃ (total NH₃ feed 140 grams). After cooling to 54°C addition of 1,485 grams of dry PCl₅ was commenced in 100-200 gram portions over a 13 minute period at 54-57°C. Stirring was continued at 59-60°C for ten minutes and then external heat was applied for 6 minutes raising the temperature from 52° to 58°. Heat was removed and temperature rise continued reaching 110°C in 15 minutes. Heat was again applied and in 5 more minutes the reaction was at 130°C (reflux). Stirring was continued for 23 minu tes in the range of 117-130°C. Stirring was stopped and the phases separated. The lower phase solidified and the upper solvent phase was decanted. The solvent phase contained 77.7 weight percent of the phosphorus initially charged as PCl₅. The phosphorus was now polyphosphonitrilic chloride which analyzed 79.1 weight percent cyclic trimer, 3.8 weight percent cyclic tetramer and the balance higher cyclics and linear oligomers. The pyridine-HCl residual heel from Example 6 was then recycled to the initial reaction mixture in Example 7 and the residual heel from Example 7 was in turn recycled to the initial reaction mixture of Example 8. The results with the recycle runs were as follows. Example Heel Recycled From Example Percen of P¹ in Solvent Product Trimer Tetramer 7 6 83.5 82.8 3.6 8 7 78.0 83.7 3.1 EXAMPLE 9 An Initial Cycle In a reaction vessel was placed 1,038 grams of monochlorobenzene, 495 grams of PCl₅ and 121 grams of NH₄Cl. Then 500 grams of pyridine was fed slowly over a period of 10 minutes while keeping the temperature below 80°C. Then heat was applied and the temperature rose to reflux in about 4 minutes. Reflux was continued for 65 minutes and then the reaction mixture was filtered. The filtrate formed two phases. The upper solvent phase contained 88.3 weight percent of the phosphorus initially added as PCl₅ now in the form of polyphosphonitrilic chloride which analyzed 77.3 weight percent cyclic trimer, 3.8 weight percent cyclic tetramer and the balance higher cyclics and linear oligomers. The pyridine-HCl residual heel was saved for recycle. EXAMPLE 10 A Recycle Run Using NH₄Cl In a reaction vessel was placed the residual pyridine-HCl heel from Example 9 and 10 grams of pyridine (make-up for small pyridine losses). Then 121 grams of NH₄Cl was added. A solution of 495 grams of PCl₅ in 1,041 grams of monochlorobenzene was added to the mixture in increments over a 41 minute period as follows. Time (min.) Temp. (°C) Remarks 0 133 feed PCl₅ solution 20 seconds 13 131 feed PCl₅ solution 20 seconds 36 130 feed PCl₅ solution 20 seconds 41 123 feed PCl₅ solution 5 seconds 111 132 cook period over The molten product was filtered to remove a small amount of solids. The phases separated and the pyridine-HCl heel was recycled to the next run. The results of this example and subsequent recycle runs each using recycle from the prior run are shown in the following table. Example Heel Recycled From Example Percent of P in Solvent Product Trimer Tetramer 10 9 87.2 77.3 2.8 11 10 94.5 79.3 2.8 12 11 92.4 77.4 1.6 13 12 92.1 82.2 2.1 14 13 87.7 75.7 1.3 15 14 95.7 74.5 1.3 16 15 90.3 78.5 1.6 17 16 91.0 79.3 3.7 EXAMPLE 18 Synthesis of Pyridine Hydrochloride In a glass reaction vessel was placed 1955 grams (24.7 moles) of pyridine. While stirring, dry HCl was injected below the liquid surface while cooling the vessel in an ice bath. Temperature gradually rose and when 230 grams of HCl was in, the temperature was 48°C and the ice bath was removed. When 592 grams were in, the temperature was 119°C and all solids melted. When 915 grams (25 moles) of HCl were in, the temperature was 150°C and HCl breakthrough occurred. HCl feed was stopped. Co-Feed of Chlorine and PCl₃ A 154 gram (2.9 moles) quantity of NH₄Cl was added to the molten pyridine-HCl and then chlorine and PCl₃ were concurrently fed over a 50 minute period at 139-149°C. Total feed was 254 grams (3.58 moles) of chlorine and 366 grams (2.66 moles) of PCl₃. The reaction was stirred at 135-140°C for 1 hour and then the stirrer was stopped. No phase separation was noted. A 966 gram portion of cyclohexane was added to extract the phosphonitrilic chloride into a solvent phase and the phases were allowed to separate. The lower pyridine-HCl phase solidified on further cooling. The upper solvent phase excluding solvent was analyzed by NMR as follows: Phosphonitrilic Chloride as Cyclic trimer 33.2 weight percent Cyclic tetramer 19.0 weight percent Pentamer-hexamer 10.5 weight percent Higher cyclics and linears 37.3 weight percent As the above results demonstrate, the new process makes it possible to conserve pyridine or similar pyridine-type nitrogen bases and at the same time obtain the high reaction rate and trimer yields obtainable with the pyridine catalyzed trimer process.

Claims: A process for making a phosphonitrilic halide comprising reacting ammonia or ammonium halide and a phosphorus pentahalide in the presence of a pyridine-hydrogen halide complex or a substituted pyridine-hydrogen halide complex, providing a solvent for the phosphonitrilic halide so as to form a solvent phase containing said phosphonitrilic halide and a second phase comprising said pyridine-hydrogen halide complex, and recovering said pyridine-hydrogen halide complex for use in a subsequent reaction of said ammonia or ammonium halide and phosphorus pentahalide. A process as claimed in claim 1 in which said solvent is a chlorinated hydrocarbon. A process as claimed in claim 2 in which said chlorinated hydrocarbon is a chlorinated benzene. A process as claimed in claim 3 in which said chlorinated benzene is a monochlorobenzene. A process as claimed in claim 1 in which said solvent is monochlorobenzene and is present during the reaction of ammonia or ammonium halide and phosphorus pentahalide. A process as claimed in claim 1 in which said complex is initially formed in situ by adding pyridine or substituted pyridine to said ammonia or ammonium halide and phosphorus pentahalide. A process as claimed in any of the preceding claims in which said amonium halide is ammonium chloride and said phosphorus pentahalide is phosphorous pentachloride. A process as claimed in claim 1 in which the solvent is monochlorobenzene and is added to the reaction mixture after the formation of the phosphonitrilic halide.

Inventors: ADAMS, JAMES ROBERT, JR., JUNEAU, MATTHEW KEVIN, SULZER, MICHAEL, GERALD, TEDDER, JOSEPH BYRNE, JR.
Applicants: ETHYL CORPORATION
Application year: 1986
Main classification: C01B21
IPC codes: C01B21