Novel Initiator For Preparing Alkanesulfonic Acids From Alkane And Oleum

Abstract

A compound of the formula (I)

Description

TECHNICAL FIELD

The present invention relates to a compound that can be employed as an initiator for manufacturing of alkanesulfonic acids, especially methanesulfonic acid, from alkane, especially methane, and oleum, to processes for manufacturing the compound according to the invention, and to a process for manufacturing of alkanesulfonic acid, especially methanesulfonic acid, using the compound according to the invention as an initiator, and to the use of the compound according to the invention in a device for performing the process for manufacturing of alkanesulfonic acid, especially methanesulfonic acid.

BACKGROUND

Alkanesulfonic acids are organic acids that can reach a similar acid strength as that of inorganic mineral acids, for example, sulfuric acid. However, in contrast to usual mineral acids such as sulfuric and nitric acids, the sulfonic acids are non-oxidizing and do not give off vapors that are harmful to health, as can be observed with hydrochloric and nitric acids. Further, many sulfonic acids, for example, methanesulfonic acid, are biologically degradable. The applications of sulfonic acids are many, for example, in cleaning agents, surfactants, as catalysts, and in organic synthesis, pharmaceutical chemistry, for example, as protective groups. The salts of sulfonic acids are employed, for example, as surfactants, for example, sodium dodecylsulfonate, or in the electroplating industry, especially as tin, zinc, silver, lead and indium, but also other metal, alkylsulfonates. The very high solubility of alkyl sulfonates plays an important role, in particular. Further, no harmful gases are formed in electrolysis, and the use of toxic compounds, for example, cyanide, which is common in many cases, is dispensed with.

INTRODUCTION AND SUMMARY OF THE INVENTION

The structurally simplest representative of alkanesulfonic acids is methanesulfonic acid. U.S. Pat. No. 2,493,038 describes the preparation of methanesulfonic acid from SO₃ and methane. US 2005/0070614 describes further methods for preparing methanesulfonic acid, and its application. The methods known in the prior art are in part complicated, cost-intensive, and lead to undesirable products because of the harsh conditions.

The reaction conditions in conventional processes of alkanesulfonic acid production can result in undesirable side products, which even manifest themselves as disturbing inhibitors in the production of alkanesulfonic acids. This may lead to termination of the actual reaction for preparing the alkanesulfonic acid, but also to impurities, formation of side products and poor yields, based on sulfur trioxide and methane.

WO 2007/136425 A2 discloses the use of the compound di(methanesulfonyl) peroxide (DMSP), which must be prepared by a complex electrolysis and, in addition, is a crystallizable highly explosive solid, as an initiator in a reaction in which methanesulfonic acid is formed from sulfur trioxide and methane

It is the object of the present invention to provide a compound that can be employed for the manufacturing of alkanesulfonic acids from alkane, especially methane, and sulfuric trioxide or oleum, allowing for an improved reaction control.

The object of the invention is achieved by a compound of the formula I

ALK—SO₂—O—O—SO₂OX,

• • wherein ALK is an alkyl group, especially a methyl, ethyl, propyl, butyl, isopropyl, isobutyl group, or a higher alkyl group, and X=hydrogen, zinc, aluminum, an alkali or alkaline earth metal.

In particular, the compound according to the invention is present in a mixture of the invention, which contains additionally at least one compound selected from the group consisting of formula II to XI, i. e. II, III, IV, V, VI, VII, VIII, IX, X, or XI:

and combinations thereof.

In another embodiment, the compound of the invention or the mixture of the invention is present in sulfuric acid or alkanesulfonic acid, especially methanesulfonic acid.

For example, the compound according to the invention with X═H, can be manufactured by a process comprising the following steps:

• • reacting alkanesulfonic acids, especially methanesulfonic acid, with hydrogen peroxide;
  • then adding oleum;
  • followed by the isolation of the compound.

In particular, the isolation can be effected by extraction, chromatography, precipitation, recrystallization, freeze-drying or similar methods under mild conditions.

In a particular embodiment of the process according to the invention, the isolation can be effected by means of precipitation or chromatography. Inert support materials and inert solvents, such as sulfuric or sulfonic acids, are employed therein. The use of organic solvents is also possible.

Inert support materials are in particular, those which do not negatively interfere with components being the actual reaction partners, e.g. by reducing the yield of the compound of the invention. Furthermore, inert support materials can either chemisorb or physisorb—or both—a chemical compound, without destroying its functionality or structure in an irreversible way. Examples are materials based on e.g. silicon dioxide, aluminum oxide, zirconium oxide and the like.

A mono-alkali peroxosulfate or alkaline earth peroxosulfate is reacted with alkanesulfonic acid halide, especially methanesulfonic acid halide, and the compound according to the invention can be separated from the alkali or alkaline earth halide formed. The alkali or alkaline earth halides formed can be removed by extraction or precipitation to obtain the pure peroxosulfate.

Another way to prepare the peroxosulfate product (X═H) is to react a mono-alkylperoxosulfate with chloro-, or bromo-sulfonic acid. The alkali or alkaline earth halides formed can be removed by extraction or precipitation to obtain the pure peroxosulfate.

If X=aluminum, zinc, alkali or alkaline earth metal, the respective compound can be obtained by an addition of the respective aluminum, zinc, alkali or alkaline earth metal alkaline base.

The invention also relates to the use of the compound according to the invention or of the mixture according to the invention as an initiator in a chemical reaction for manufacturing alkanesulfonic acids, especially methanesulfonic acid, from methane and oleum.

The invention also relates to a process for manufacturing of alkanesulfonic acids, especially methanesulfonic acid, comprising the steps stated below:

A solution containing sulfur trioxide or oleum is reacted with an alkane in a reactor. For alkanes with a low boiling point, the use of a high-pressure reactor is necessary. For pentane and higher alkanes, a common laboratory reactor is sufficient. In the case of gaseous alkanes, for example, methane, a pressure of 1-150 bar gas pressure is set. The initiator is added to this solution. The initiator is prepared by reacting an alkanesulfonic acid or a solution of such alkanesulfonic acid in a solvent with hydrogen peroxide, and optionally isolated. The concentration of the hydrogen peroxide may be 20-100% (w/w). Subsequently, the reaction is completed at 0-100° C. The raw product can be processed by extraction, crystallization, distillation or chromatography.

The invention further relates to the use of the compound of the invention in a device for performing the process according to the invention, wherein the device is comprising a first reactor 1 in which sulfur trioxide and alkane, especially methane, react with the compound according to the invention as initiator, a second reactor 2 in which the compound according to the invention is formed, a distillation means 3 for distilling the product formed in the first reactor 1, and a filling means 4, connections from reactor 2 to reactor 1, from reactor 1 to the distillation means 3, and from the distillation means 3 to each of the filling means 4, the second reactor 2, and the first reactor 1.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows schematically, in an exemplary way, a simple system according to the invention for the manufacturing of methanesulfonic acid according to the invention.

FIG. 2 shows a schematic layout of a preferred device.

DETAILED DESCRIPTION

The process according to the invention allows for alkane sulfonation, especially methane sulfonation, in a reactor system using oleum with alkane, especially methane, with addition of the compound according to the invention as an initiator. Advantageously, the raw product can be purified by distillation, which already yields a relatively pure alkanesulfonic acid, especially methanesulfonic acid, as a distillate.

The residue consists of sulfuric acid with a content of up to 10% alkanesulfonic acid, especially methanesulfonic acid (MSA). These distillation bottoms may be used 1) as a solvent for the continuous reaction in the reactor; 2) for the preparation of “fresh” oleum with pure sulfur trioxide; 3) by reacting hydrogen peroxide (30% to 100% (w/w) solution in water), the compound according to the invention can be prepared, which may be employed as an initiator or precursor for it.

ALK—SO₂—OH+H₂O₂→ALK—SO₂—O—O—H+H₂O.  Reaction scheme 1:

The compound according to the invention is capable of reacting with oleum to form a mixed acid peroxide. This yields the initiator, the compound according to the invention.

ALK—SO₂—O—O—H+SO₃→ALK—SO₂—O—O—SO₂—OH   Reaction scheme 2:

This mixed peroxo anhydride is characterized by a high reactivity as compared to DMSP (dimethylsulfonyl peroxide, H₃CSO₂—O—O—SO₂CH3), which is known from the prior art, for example, and which causes longer reaction times. At the same time, however, the selectivity of the DMSP in view of the formation of side products is obtained. In contrast, peroxodisulfuric acid (Marshall's acid) is very reactive and very little selective. The compound according to the invention combines the selectivity of DMSP with the reactivity of Marshall's acid.

In the following, the invention is further illustrated in an exemplary way taking the preparation of methanesulfonic acid as an example.

EXAMPLE 1

Preparation of the Initiator Solution

To a mixture consisting of 90 ml of 100% sulfuric acid and 10 ml of methanesulfonic acid, 3.4 ml of 70% (w/w) hydrogen peroxide is added dropwise with external cooling and intensive stirring.

Synthesis protocol:

In a 3.75 L autoclave, 1000 g of 36% (w/w) oleum is charged, and the temperature controlled to 50° C. After a pressure of 100 bar of methane gas was set, intensive stirring is performed with a stirrer from the company Parr. Now, the initiator solution is metered dropwise to the solution. The pressure drops to 35 bar within 5 hours. The yield is higher than 90%, based on sulfur trioxide. The reaction product contains 42% (w/w) methanesulfonic acid.

EXAMPLE 2

Preparation of the Initiator Solution

To a mixture consisting of 90 ml of 100% sulfuric acid and 10 ml of methanesulfonic acid, 3.4 ml of 70% (w/w) hydrogen peroxide is added dropwise with external cooling and intensive stirring.

Synthesis protocol:

In a 3.75 L autoclave, 1000 g of 36% (w/w) oleum is charged, and the temperature controlled to 35° C. After a pressure of 100 bar of methane gas was set, intensive stirring is performed with a stirrer from the company Parr. Now, the initiator solution is metered dropwise to the solution. The pressure drops to 35 bar within 5 days. The yield is higher than 90%, based on sulfur trioxide. The reaction product contains 42% methanesulfonic acid.

Characterization of monomethylsulfonyl peroxide:

Using different analytical techniques monomethylsulfonyl peroxide was characterized. Using mass spectroscopy the molecular weight was determined as M═191.94 g/mol. The ¹H-NMR (D₂SO₄) shows a signal for the Methylgroup at 3.43 ppm. A suitable way in order to measure the peroxide content is titration (Jander, Jahr, Maßanalyse, Theorie und Praxis der Titrationen mit chemischen und physikalischen Indikationen, 17. Auflage, Walter de Gruyter GmbH 2009, Berlin).

Claims

1. A mixture comprising a compound having a formula of ALK—SO2—O—O—SO2OX, wherein ALK is a branched or unbranched alkyl group, a methyl group, an ethyl group, a propyl group, a butyl group, an isopropyl group, an isobutyl group, or a higher alkyl group, and X═hydrogen, zinc, aluminum, an alkali or alkaline earth metal, andat least one compound selected from the group consisting of

2. A process for manufacturing a compound having a formula of ALK—SO2—O—O—SO2—OX (Formula I), wherein ALK is a branched or unbranched alkyl group, a methyl group, an ethyl group, a propyl group, a butyl group, an isopropyl group, an isobutyl group, or a higher alkyl group, and X═hydrogen, zinc, aluminum, an alkali or alkaline earth metal, comprising: reacting a mono-alkali peroxosulfate with an alkanesulfonic acid halide or a methanesulfonic acid halide, and separating the compound according to Formula I from the alkali or alkaline earth halide formed orreacting an alkali mono-alkylperoxosulfonate with chlorosulfonic acid or bromosulfonic acid, and separating the compound according to Formula I from the alkali or alkaline earth halide formed.

3. The process of claim 2 comprising reacting the mono-alkali peroxosulfate with an alkanesulfonic acid halide, wherein the mono-alkali peroxosulfate is a zinc peroxosulfate, an Aluminum peroxosulfate, or an alkaline earth peroxosulfate.

4. The process of claim 2 comprising reacting the alkali mono-alkylperoxosulfonate with chlorosulfonic acid or bromosulfonic acid, wherein the alkali mono-alkylperoxosulfonate is sodium methylperoxosulfonate, zinc mono-alkylperoxosulfonate, Aluminium mono-alkylperoxosulfonate or alkaline earth mono-alkylperoxosulfonate.

5. A process of making a compound comprising preparing an alkanesulfonic acid from a mixture comprising an alkane, oleum, and an initiator,wherein the initiator has a formula of ALK-SO2—O—O—SO2OX, wherein ALK is a branched or unbranched alkyl group, a methyl group, an ethyl group, a propyl group, a butyl group, an isopropyl group, an isobutyl group, or a higher alkyl group, and X═hydrogen, zinc, aluminium, an alkali or alkaline earth metal.

6. The process of claim 5 wherein the alkanesulfonic acid is methanesulfonic acid and the alkane is methane.

7. A process for manufacturing alkanesulfonic acids comprising: providing a solution containing sulfur trioxide/oleum;reacting the solution with an alkane in a reactor;setting the reactor at a pressure of from 1 to 150 bar;preparing an initiator by reacting an alkanesulfonic acid or a solutioncontaining the alkanesulfonic acid with a 30-100% (w/w) hydrogen peroxide solution, wherein the initiator has a formula of ALK-SO2—O—O—SO2OX (Formula I), wherein ALK is a branched or unbranched alkyl group, a methyl group, an ethyl group, a propyl group, a butyl group, an isopropyl group, an isobutyl group, or a higher alkyl group, and X═hydrogen, zinc, aluminium, an alkali or alkaline earth metaladding the initiator to the reactor;controlling the temperature of the reaction mixture at 0-100° C.; andpurifying the reaction product.

8. The process of claim 7 wherein adding the initiator to the reactor comprises adding the initiator in a solution that further comprises at least one compound selected from the group consisting of

9. The process of claim 7 wherein the alkanesulfonic acid is methanesulfonic acid and the alkane is methane.

10. The process of claim 7 wherein the reaction product is purified with distillation or extraction.

11. The process of claim 7 wherein X is H.

12. The process of claim 11 wherein ALK is methyl.

13. The process of claim 7 wherein X is zinc or aluminum.

14. The process of claim 7 wherein X is an alkali or alkaline earth metal.

15. The process of claim 7 wherein ALK is a methyl group.

16. The process of claim 7 wherein ALK is an ethyl group, a propyl group, a butyl group, an isopropyl group, or an isobutyl group.

17. The process of claim 7 wherein ALK is a pentyl group or a higher alkyl group.

18. The process of claim 7 wherein the reactor is reactor II with the process further comprising: a reactor I in which sulfur trioxide and alkane react with the compound of Formula I as initiator, anda distillation apparatus for distilling a product formed in the reactor I, with the reactor II being fluidly connected to reactor I to supply the initiator to reactor I.

19. The process of claim 19 wherein the distillation apparatus is fluidly connected to reactor I, reactor II, and a filling apparatus.

20. The process of claim 18 wherein the alkane is methane.