PROCESS FOR PREPARING SODIUM-M-NITROBENZENESULFONATE

Abstract: Nitrobenzene is combined with at least one mole of SO₃, as 65% oleum, resulting in an exothermic reaction. The reac­ tants are combined slowly, and/or cooling is supplied, so as to keep the reaction temperature in the range between about 80° and 130°C. The resulting sulfonation mass is held at a temperature between about 80 and 130°C for a sufficiently long period of time to effect substantial completion of the sulfonation reaction. The sulfonation mass is then added to sufficient caustic soda to convert the acids therein to Na₂SO₄ and sodium m-nitrobenzenesulfonate. At a pH between 7 and 8.6 and at a temperature between 80° and 100°C, sufficient water is provided by, or added to, the resulting mass so that the sodium m-nitrobenzenesulfonate is dissolved therein and at least 60% of the Na₂SO₄ is precipitated, making it possible to separate the one from the other.

Description: PREPARATION OF SODIUM m-NITROBENZENESULFONATE This invention relates t, an improved process for preparing sodium m-nitrobenzenesulfonate by sulfonation of nitrobenzene using oleum. As was noted in British Specification 1,030,308, it has been conventional to use a large excess of sulfuric acid or olewm. as a sulfonating agent and a solvent in the sulfonation of nitro-aromatic compounds, resulting in the product being oStained in admixture with a large amount of sulfuric acid. The nitro-aromaticsulfonic acid was isolated from the reaction mixture by reacting the same with lime so as to convert the excess sulfuric acid to calcium sulfate which was removed by filtration. In the alternative, the nitro-aromaticsulfonic acid was isolated by the sodium chloride "salting cut" method. As pointed out in the British Specification, the former method is an uneconomic one; large amounts of calcium sulfate are formed which. must te washed with large amounts of water, and then the filtrate must be evaporated so as to recover te product. The "salting out" method has its disadvantages as well, as are further described in the British patent. A process for sulfonating nitro-aromatic compounds, including nitrobenzene,with SO3, so as to produce the sodium salt is disclosed in U.S. Patent 3,492,342. While the use of SO3 as a sulfenating agent avoids the production of large amounts of sulfuric acid, thereby dealing with a recovery problem common to this art, it has disadvantages as well. Such sulfonations with SO3 are attended by sultone formation, resulting in the consumption of significant quantities of reactants-. Mcreover, the S03 has a tendericy to polymerize. It is therefore necessary to supply heat to the equipment being used to dispense the SO3 so as to prevent plugging of the equipment by the polymers which are form. In In addition, the presence of a reasonable amount of sulfuric acid can be an advantage il processes for prepara- ing sulfonates such as sodium m-nitrobenzenesulfonate, because it is insoluble therein. FIAT FINAL REPORT NO. 1313, dated February 1, 1948, PB 85172, pages 187-191, discloses a method for preparing metanilic acid, starting with nitrobenzene, 98% sulfuric acid and 65% oleum (equivalent to 44% oleum). After the sulfonation reaction was completed, the reaction mass was diluted with water, and sodium sulfate and calcium carbonate ("carbid kalk") were added. Assuming that substantially all of the nitrcbenzene was converted to the sulfuric acid, the amount of sodium sulfate provided was insufficient to convert all of it to sodium m-nitrobenzenesulfonate. According to the present invention there is provided a process for the preparation of sodium m-nitrobenzenesulfonate which comprises reacting slightly more than one mole of SO3, as 65% oleum, per mole of nitrobenzene at a temperature between 800 and 1300C for a period of time sufficient to effect sulfonation of substantially all of the nitrobenzene; thereafter, at a temperature not higher than 105 C., combining the sulfonation reaction mass with sufficient caustic soda to convert substantially all of the sulfuric acid and the resulting m-nitrobenzenesulfonic acid to Na2S04 and sodium m-nitrobenzenesulfonate; at a pH between 7 and 8.6 and at a temperature between 800C and 1050C, sufficient water is provided by, or added to, the resulting mixture of salts that at least 602 of the Na2S04 is insoluble therein and the sodium m-nitrobenzene sulfonato is dissolved therein; and sus rating the insoluble Na2SO4 from the reaction mass at 80 to 105 C. In the sulfonation reaction of this invention, one uses a slight excess, e.g. 5 mole % SO3, as 65z oleurn, over the theoretical amount required. With careful handling, particularly efficient mixing, it is possible to combine the nitrobenzene with the oleum, starting at room temperature, relying on the exothermic nature of the reaction to provide the heat needed to effect sub stantially complete reaction of the nitrobenzene and the oleum. Nevertheless, it is advisable, from the standpoint of safety, to preheat the nitrobenzene to a tem,- perature between 800 and 130 C and then combine it with the 65% oleum. In any event, it is necossarxP that the temperature in the sulfonator be at least 80 C. Otherwise, the sulfonation mass could solidify. On the other hand, the sulfonation mass will decompose violently at 200 C or above. Consequentliy, one should operate the process at a temperature not exceeding 130 C. Preferably, one would preheat the -nitrobenzene to a temperature between 100 and 110 C and combine the oleum and the nitrobenzene while holding the temperature in that range, supplying cooling as needed. After all of the oleum and nitrobenzene have been combined with one another, the sulfonation mass is held at a temperature between 800 and 130 C, preferably 1000 110 C for period of time sufficient to assure sub stantiai completion of the reaction. The period of time needed for completion of sulfonation will, of course, depend upon the amount of nitrobenzene and the temperature at which the sulfonation reaction is conducted. Thus, the reaction goes more rapidly at higher tempera- ture. While the initial mixing of the oleum and nitrobenzene is exothermic, the reaction thereafter reauires that heat be supplied intermittently. Every effort should be made to convert substantially all of the nitrobenzene to the m-nitrobenzenesulfonic acid during the sulfonation reaction, since it would be difficult to remove the nitrobenzene later in the process. Following completion of the sulfonation reaction, the reaction mass should be combined with sufficient caustic soda to convert substantially all or the m nitrobenzenesulfonic acid and substantially all of the sulfuric acid in the system to sodium m-nitrobenzene- sulfonate and Na2SO4. In practice, a slight excess of caustic soda is used so as to assure substantially com- plete conversion of all of those acids to those salts. The amount of excess caustic soda is kept to a minimum, as it is necessary to neutralize substantially all of it before the final product is recovered. The sulfonation mass should be transferred to the aqueous caustic soda at a temperature between 80 and 130 C, preferably 85 to 110 C. Cooling should be supplied to the vessel in which tne sulfonation mass anc the aqueous caustic soda are combined, since the com- bine exothermically. Usually, the compounds are kept at a temperature below 105 C, as the charge may foam, preferably 95 to 100 C maximum. prior to combining the sulfonation mass with it, the aqueous caustic soda may be at any temperature above its freezing point and below 105 C, preferably about 20 C. The combined sulfonation mass and aqueous caustic soda should be main tained in the vessel in which they are combine for 2 period sufficiently long so that substantially all acidity has been eliminated. Moreover, maintaining that charge at those temperatures will rid the charge of the last traces of nitrobenzene. Thereafter, substantially all excess alkalinity, if any, should be reduced to a pH of 7-8.6, for example, by adding sulfuric aci to the system. At a pH between 7 and 8.6, and at a temperature between 800 and 1050C, sufficient water is provided by, or added to, the resulting mixture of salts, so that a least 60% of the Na2SO4 is insoluble therein while sub- stantially all of the sodium m-nitrobenzenesulfonate remains dissolved therein. Tne difference in the solubilities of the two salts forms a basis for their separation. One can remove the Na2SO4 by conventional Means, e.g. filtering, centrifuging, decanting, and the Preferably a filter press, preheated with in which the charge is filtered at a temperature between @@@ and 100 C, is used. This invention not only results in lower raw material costs, but it makes possible labor and other material savings because larger amounts of the final product can be manufactured in existing equipment in which one heretofore used a large excess of sulfuric acid as a solvent. Yields of the desired product are higher, and smaller amounts of by-product are'formea, the-latter contibuting to better pollution control. As smaller arXGunts of sulfuric acid are involved in the process and as only one filtration step is required, large excesses of water need not be evaporated. This invention isfurther illustrated in the example that follows, in which, unless othen7ise specified, percentages and parts are by weight and temperature is in degrees Celsius. EXAMPLE Into a cast iron jacketed sulfonator, equipped with an agitator, were charged 2600 parts (21.12 moles) of nitrobenzene which was heated to a temperature in the ran of between 100 and 1100C. Over a period of 2 hours, 2730 parts (22.16 moles) of 65% oleum ere added with agitation to the nitrobenzene while maintaining the temperature in the range between 1000 and 1100C hy supplying cooling liquid to the jacket of the sulfonator. Mixing of the oleum and nitrobenzene was continued for 8 hours, intermittently supplying heated fluid to the jacket so as to maintain the temperature between 1000 and 1100C. To the drowning tub (a cast iron kettle equipped with carbon steel coils which can be used to heat with steam or cool with water) were added 123S parts of water and 5736 parts of a 30% aqueous solution of caustic soda (1721 parts or 43.03 moles of NaOH). The sulfonation mass was added to the drowning tub. The temperature of the contents of the drowning tub rose to 950C, whereupon cooing water was passed through the coils to maintain the temperature at a maximum of 95 C during the 3-hour period used for completion of the drowning. The drowned mass did not smell of nitro- benzene. The pH was adjusted to 7.8 + 0.8 with 91 parts o 97% sulfuric acid; The contents of the drowning tub ere transferred to a filter press which had been preheated with steam, -and the charge to the filter press was filtered at 950 - 100 C over a period of 2 hours. It was found that filtration proceeded at a faster rate when no agitation was supplied to the drowning tub The filtrate weighed 10,005 parts, and unon analysis by titanous tritration, 43.9% was determined to be SoalurrI m-nitrobenzenesulfonate; it- also contained 4.4% Na2SO4 and 0.2 "sulfone." The filter cakecontained 1044 parts Na2SO4.

Claims: CLAIMS: 1. @ process for the preparation of sodium @@@zenesulfonate which comprises reacting slightly more than one mole of sO3, as 65% oleum, per mole of nitrobenzene at a temperature between 80 C and 130 C for a period of time sufficient to effect sulfonaLion of substantially all of the nitrobenzene; thoreafter, at a temperature not higher than 105 C., combining the sulfonation reaction mass with sufficient caustic soda to convert substantially all of the sulfuric acid and the resulting m-nitrobenzenesulfonic acid to Na2SO4 and sodium m-nitrobenzenesulfonate; at a pH between 7 and 8.6 and at a tem¯erature between 800 and 1050C, sufficient water is provided by, or added to, the resulting mixture of salts that at least 60% of the Na2 SO4 is insoluble therein and the sodium m-nitrobenzenesulfonate is dissolved therein; and separating the insoluble Na2S04 from the reaction mass at 800 to 105 C. 2. A process according to Claim 1 wherein the nitrobenzene and the oleum are combined at a temperature between 1000C and 11000 and the sulfonation reaction is performed at said temperature. 3. A process according to Claim 1 or Claim 2 herein the sulfonation mass and aqueous caustic soda are combined at about 200C, and the heat of the reaction is permitted to bring the reaction temperature to a maximum temperature between 950C and 10000. A. A process according to any one of the preceding claims wherein the Na2 SO4 is separated from the reaction mass in the solid state at a temperature between 95 C and 1000C. 5. A process according to any one of the preceding claims wherein the S03 is used in an excess of about 5% over the theoretisal amount required for complete sulforjation of the nitrobenzene. 6. A process for the preparation of sodium m-nitrobenzenesulfonate substantially as described in the foregoing specific Example. 7. Sodium m-nitrobenzenesulfonate whenever prepared by the process claimed in any one-of the preceding claims.

Inventors: BAUM, ARTHUR ALOYSIUS, ROTHMAN, LEONARD AARON
Applicants: E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1979
Main classification: C07C139
IPC codes: C07C67, C07C301, C07C309, C07C303