Abstract:
A composition of matter is disclosed which includes a major proportion of an organic di- or polysulfide, a catalytic amount of an amine/mercaptan mixture, and a stabilizing component in an amount sufficient to inhibit loss of catalytic activity in storage.

Description:
BACKGROUND 
     This invention relates to a composition of matter which is an organic di- or polysulfide incorporating a catalytic amount of an amine/mercaptan mixture and a stabilizer to provide a sulfur-solvent capable of dissolving unexpectedly large amounts of sulfur at a high rate with low loss of catalyst activity on storage. 
     In the processing of sour gas wells, sulfur may form deposits that can plug the well and cease production. These deposits have been prevented or dissolved by flowing solvents such as carbon disulfide, mineral and spindle oils, organic solvents and aqueous alkylamines downhole to dissolve the sulfur plug. The solvent is injected downhole and the well is allowed to soak for sufficient time to dissolve any existing sulfur plugs. Alternatively, the solvent can be injected continuously in amounts sufficient to prevent the formation of sulfur deposits. The above systems all have various disadvantages such as toxicity, flammability, corrosivity and limited ability to dissolve sulfur. 
     PRIOR ART 
     Dialkyl disulfides, either alone or blended with dialkyl sulfides, as disclosed in U.S. Pat. No. 3,531,160, have become the sulfur solvents of choice. Hyne et al. [Alberta Sulfur Research, Ltd. (ASRL), Quarterly Bulletin, Vol. XVIII, Nos. 2, 3 and 4, 1982, pp. 44+] have shown that lower dialkyl disulfides, especially dimethyl disulfide (DMDS) are preferred. Alone, the disulfides take up only a limited amount of sulfur; however, in conjunction with a suitable catalyst system, they can take up approximately 1.5 times their weight in sulfur at room temperature. 
     U.S. Pat. No. 3,846,311 teaches that a composition of one or more dialkyl disulfides and up to 10 weight percent of an unsubstituted saturated, aliphatic amine is capable of consuming over 200 weight percent sulfur after aging the composition. French patents 2,152,532 and 2,159,320 disclose similar compounds which are useful without aging. It is also taught in the art that adding a small amount of sulfur (5-40 weight percent) to the above compositions accelerates the rate of sulfur uptake (U.S. Pat. No. 4,239,630). 
     U.S. Pat. No. 4,290,900 teaches that the above sulfideamine composition is not as effective if vaporization occurs, which is often the case in deep wells where temperatures greater than 250° F. may be encountered. Therefore, they disclose the use of a composition of a dialkyl disulfide and a fatty acid amine (&gt;30 wt. %) which has been aged. Further, U.S. Pat. No. 4,248,717 teaches that the addition of 60 weight percent sulfur to the above composition accelerates sulfur uptake. 
     Hyne et al. (ASRL Quarterly Bulletin, Vol. XX, No. 3, pp. 1+) show that sodium hydrosulfide (NaSH) and dimethylformamide (used as a co-solvent) is an effective system for catalyzing sulfur uptake using DMDS. They also demonstrated, as reported in the aforementioned ASRL Quarterly Bulletin Vol. XVIII, that a variety of alkali salts of a series of thiophenols, in conjunction with dimethylformamide (DMF), catalyze sulfur uptake. It is known that the sulfur recovery systems of Hyne et al. have one major drawback; they are not storage-stable and lose activity within 3-10 days when standing at room temperature. 
     STATEMENT OF THE INVENTION 
     This invention is a composition comprising a di- or polysulfide, and a catalytic amount of a mixture comprising an amine and a mercaptan to which is added a suitable amount of a stabilizing agent to inhibit loss of catalytic activity. 
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     This invention is a superior, storage-stable composition for dissolving sulfur. The composition may be used whenever a requirement for sulfur removal exists. One application is to dissolve or prevent sulfur plugs in sour and super-sour oil and gas wells. 
     A disulfide or a polysulfide of a low sulfur rank can be used for the composition of this invention. The sulfur rank is defined as the average of the number of sulfur atoms between the two alkyl groups in a mixture of di- and polysulfides. A rank greater than 2 but less than 3 is considered low. A low sulfur rank is preferred since a polysulfide with a sulfur rank greater than 3 will have a limited capacity to take up additional sulfur. 
     The disulfide or polysulfide component of the composition of this invention has the formula 
     
         R.sup.1 SS.sub.A SR.sup.2 
    
     wherein R 1  and R 2  are independently selected from alkyl, aryl, alkaryl, alkoxyalkyl or hydroxyalkyl radicals of 1-24 carbons and A is the average number of internal sulfur atoms in the sulfide and ranges from 0 to 3. The most preferred embodiment is when R 1  and R 2  are methyl and A is 0, i.e., dimethyl disulfide. 
     Suitable amines of the catalyst mixture are selected from amines of the structure 
     
         R.sup.3 R.sup.4 R.sup.5 N 
    
     wherein R 3 , R 4  and R 5  are independently hydrogen, alkyl, alkaryl, aryl, cycloalkyl, hydroxyalkyl or alkoxyalkyl, and R 3  and R 4  may, together with the nitrogen, form a heterocyclic ring such as pyrrolidine, piperidine, morpholine or pyridine. The alkyl moiety of these amines generally contain from 1 to 30 carbon atoms. 
     Also suitable are polyamines of the general structure ##STR1## wherein R 6  -R 12  are independently selected from hydrogen, alkyl, cycloalkyl, aryl or alkaryl groups where the alkyl moieties have from 1 to 25 carbon atoms and x is an integer from 0 to 25. R 6  and R 7  and R 11  and R 12  may also, with the nitrogen, form a heterocyclic ring such as pyrrolidine, piperidine or morpholine. Bicyclic amines such as 1,4-diazabicyclo [2.2.2]-octane, 1,5. diazabicyclo[4.3.0]non-5-ene, and 1,8-diazabicyclo [5.4.0]undec-7-ene are also suitable catalysts. 
     The formulas 1, 2, 3, and 4 shown below are given as examples to demonstrate the types of polyalkyleneoxyamines and -polyamines that will act as catalysts for sulfur-uptake by disulfides or polysulfides of low sulfur rank. ##STR2## where R 13 , R 14 , R 16 , R 17 , R 20 , R 22 , R 23 , R 24 , R 25 , R 26 , R 27 , and R 28  are independently H, alkyl, alkaryl, hydroxyalkyl, alkoxyalkyl, haloalkyl, wherein the alkyl moieties have from 1 to 20 carbon atoms, or phenyl; R 18 , R 19 , and R 29  are independently H, alkyl, hydroxyalkyl, alkoxyalkyl, alkaryl wherein the alkyl moieties have from 1 to 10 carbon atoms, aryl, or --CONH 2  ; R 21  is the hydrocarbon residue of a triol; and b, c, d, e, f, g, h, x, y, and z are independently values of 0-200, provided, however, that the total of such values is no less than 2. 
     Jeffamines®, a series of poyakyeneoxyamines produced by the Texaco Chemical Company, are exemplary of the type of compounds that are suitable in the catalytic mixture for sulfur-uptake by disulfides or polysufides of low sulfur rank. Furthermore, any polyalkylene-oxy-compound which contains an amine functionality will be active. Additionally, formula 4 shows the hydrocarbon residue of a triol, such as glycerol, (R 11 ) as the base of the compound, although any other similar polyalkyleneoxyamine which incorporates any polyol as its base should also be effective. 
     Examples of Jeffamine® products which are preferred for this invention include those identified below under the alpha-numeric product designation. ##STR3## 
     Mixtures of one or more of the aforementioned amine catalysts are also suitable. The amines are incorporated in the composition in amounts sufficient to improve the sulfur uptake of the di- or polysulfide and preferably in an amount ranging from 10 ppm to 20 weight %, with 1-2 wt % being most preferred. 
     The catalyst mixture of this invention contains one or more mercaptans of the formula 
     
         R.sup.30 SH 
    
     where R 30  is independently alkyl, cycloalkyl, aryl, alkaryl, hydroxyalkyl or alkoxyalkyl wherein the alkyl moieties have from 1 to 25 carbon atoms. Also suitable are heterocyclic mercaptans such as 2-mercapto-benzothiazole and 4-mercaptopyridine and di- and polymercaptans such as ethanedithiol and propylenedithiol. The preferred mercaptans for use in the catalytic mixture of this invention include C 1  -C 25  alkyl mercaptans. The most preferred are C 8  -C 12  alkyl mercaptans. 
     The mercaptans are incorporated in the composition in amounts sufficient to activate the amine catalyst and enhance catalyst activity. Amounts within the range of 10 parts per million (ppm) to 20 weight %, preferably from 0.5 to 3%, based on the composition weight, are normally used. 
     The stabilizers which are useful in the composition of this invention in amounts sufficient to inhibit loss of catalytic activity on storage include compounds having the formula ##STR4## 
     R 31  -R 35  are independently hydroxy, linear or branched alkyl, cycloalkyl, aryl, alkaryl, hydroxy or alkoxyalkyl, hydroxy or alkoxy aryl, thioalkyl, thioaryl, amino alkyl or amino aryl wherein the alkyl moieties have from 1 to 25 carbon atoms. Examples of these stabilizers include hydroquinine, 2,6-di-tert-butyl-4-methylphenol (BHT), catechol and 4-tert-butyl-catechol (TBC). 
     Also suitable are compounds having the structure 
     
         R.sup.36 R.sup.37 NOR.sup.38 
    
     wherein R 36  and R 37  are independently alkyl, aryl, alkaryl, hydroxy or alkoxyalkyl wherein the alkyl moieties have from 1 to 25 carbon atoms, and R 38  is selected from hydrogen, alkyl, aryl, alkaryl, hydroxyalkyl or alkoxyalkyl wherein the alkyl moieties have from 1 to 25 carbon atoms. N,N-Diethylhydroxylamine (DEHA) is the most preferred stabilizer. 
     Amounts of the stabilizer, based on the weight of the composition, range generally from 10 ppm to 100,000 ppm, preferably from 500 to 1500 ppm with 1,000 ppm the most preferred. 
     EXAMPLES 
     Example 1 
     To 290.4 g of DMDS is added 1.5 g Jeffamine® D230 and the mixture is stirred for three hours. 2.7 g Jeffamine® ED600 and 2.7 g of t-butylmercaptan are then added. Two 100 mL aliquots were taken and to one was added the stabilizer 0.1 g DEHA and to the other the stabilizer 0.1 g t-butylcatechol (TBC). The sulfur uptake activity of these solutions after aging in storage was measured by adding 3.5 g powdered sulfur to 9.5 g of solvent and noting the time it takes for complete dissolution. The results of both fresh and aged solutions, summarized in Table 1, demonstrate the efficiency of DEHA and TBC as stabilizers of catalytic activity on storage of the sulfur-solvent composition. 
     A second set of tests was run following the procedure of Example 1 except that t-nonyl mercaptan was used instead of t-butylmercaptan. These results, also in Table 1, further show the efficacy of DEHA and TBC as stabilizers. 
     
                       TABLE 1______________________________________             Sulfur Uptake Times (sec.)             AgedExample  Mercaptan Stabilizer Fresh 40 days                                   136 days______________________________________1      t-Butyl   --         53    63    750  t-Butyl   0.1%   DEHA  53    45     50  t-Butyl   0.1%   TBC   53    49     552      t-Nonyl   --         51    571   960  t-Nonyl   0.1%   DEHA  51    53     50  t-Nonyl   0.1%   TBC   51    73    210______________________________________