• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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  • 引用文献
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  • 优先权
    • 专利摘要:
    1421250 Sulphonating olefins SNAMPROGETTI SpA 11 June 1973 [21 June 1972] 27780/73 Heading C2C [Also in Division C5] Sulphonates are produced by reacting olefins with alkali metal or ammonium bisulphite in a solvent medium including water and an alcohol, in the presence of oxygen and of a transition metal compound, and at a pH in the range 2-8À5 with the proviso that if the reaction temperature is below 60‹ C., the pH is in the range 5À5-8À5. Suitable transition metals include those of Groups I, VII and VIII, specifically Cu, Mn, Fe and Co. The bisulphite may be prepared in situ from SO 2 . The products include a substantial proportion of disulphonate and are said to be low in sodium sulphate.
    公开号:SU791224A3
    申请号:SU731927943
    申请日:1973-06-20
    公开日:1980-12-23
    发明作者:Нери Карло；Перротти Эмилио
    申请人:Аник С.П.А. (Фирма)；
    IPC主号:
    专利说明:

    t
    The invention relates to an improved process for the preparation of alkyl sulfonates, which are used in the manufacture of synthetic myad of funds.
    The patent technical literature describes various methods for producing alkyl sulfonates, including the fact that the olefin is reacted with alkali tO metal bisulfite while blowing air through the reaction mixture l.
    However, the reaction in these conditions proceeds slowly and it takes from 16 to 40 hours to achieve a satisfactory yield of the desired product 5.
    Also known are cnocoCto for the preparation of alkyl sulfonates using peroxide compounds, nitrites 2 and ultra violet or U-irradiation Z as promoters.
    However, the disadvantages of these methods include the formation of by-products, reducing the quality of the target product, and the complexity of the technological design process.
    The closest in technical essence to the present invention is a method for producing alkyl sulfonates, which consists in the fact that oL-olefin 30
    is reacted with an excess of alkali metal bisulfite in an aqueous alcohol in the presence of an oxidizing initiator, for example, benzoyl peroxide or sodium nitrite, and a variable-valence promoter salt at a temperature of 60-90 ° C with blowing oxygen or air through the reaction mixture. The yield of the target product is 90%, the content of sodium sulfate is not higher than 4% 4.
    The disadvantage of this method is the use of peroxides and nitrites to initiate the reaction, which leads to undesirable side reactions.
    The purpose of the invention is to simplify the process, eliminating the use of oxidizing initiators.
    The goal is achieved by the interaction of olefin with alkali metal bisulfite in the presence of manganese dioxide and oxygen in aqueous alcohol when heated. Bisulfite conversions are quantitative.
    The process is preferably carried out at a molar ratio of 1: (0.8. -1) alkaline metal olefin and bisulfite and a temperature below 100 ° C. Example 1. A glass reactor equipped with a stirrer and a Teflon partition, a glass electrode, an air bubbler, a charging funnel and a reflux condenser are used. 30 g of N328205 (corresponding to 0.3 mol of NaHSO) in 250 ml of water are dissolved in the reactor and 250 ml of isopropanol, robal south 100 ml of olefinic fraction Cg, having the following composition of s.-olefins, wt.% C-5-25.05, -, 04, C, 720.67; 68, the rest is internal olefins. The mixture is ampled down to pH 6 with 2 II. NaOH, heated in a nitrogen atmosphere to 80 ° C, is added 50 g (0.6-10 mol) of manganese dioxide and air is passed (1.5 l / h). Disulfide bisulfite is controlled by the iodometric method. During the reaction process, the pH increased to 8-8.5. After 1.5 h, the reaction is complete, the solution is filtered in a hot state, extracted four times with 80 ml of penta. The aqueous-alcoholic solution is evaporated, the residue is dried in vacuum, to obtain 65 g of non-hygroscopic white powder with the content of Nag SO / 5, 7% by weight. In the distillation of pentane, an excess of olefins (35 g) of the following composition was isolated, wt.%:, 78; , 56, 0.25.54, - 11/88. EXAMPLE 2 The experiment under the conditions of example 1 is repeated with a solvent containing 200 ml of water and 300 ml of iso-propanol. The reaction time is 1 h 15 min. 31 g of olefins are recovered, of the following composition, wt.%: CJj 21.33, 3b; C, 7 25.40; , 8l. The product contains 5% by weight, the product yield is 67 g. Example 3. Repeat the experiment under the conditions of example 1 with a solvent containing 150 ml of water and 350 MP of isopropanol. The reaction time is 40 min. 30 g of olefin of the following composition are isolated, wt%:, 30; , 58; 0.24.16; . 11,10. The weight of the dry product 70 g, the content of 3.8% by weight of Na ,. Example 4. The experiment was repeated under the conditions of Example 3, the solution was not buffered at the beginning (initial pH 4.7). The reaction time is 40 minutes. During the reaction, the pH is increased to 8.5. 34 g of olefins are recovered. Product weight 65 g, content 4.5% by weight N3220. Example 5. Under the conditions of Example 1, at the temperature, the solution was not buffered (initial pH 4.7). During the reaction, the pH decreases to 1.9, while the reaction rate drops sharply, after 3 hours and 40 minutes a product containing 90% by weight is obtained. Example 6. The experiment was repeated under the conditions of example 3 with the use of olefins isolated from previous experiments of the following composition, wt.%:, 67; C (; 24.12;; 87;, 70. The catalyst used in this experiment was also isolated from previous experiments. Reaction time 40 minutes. 34 g of olefin are recovered. 65 g of product are obtained with a content of 4.5% by weight. Example 7 The test was carried out in a glass reactor equipped with a stirrer and a Teflon septum. 60 g (0.6 mol) of N32520 in 150 ml of water and 350 ml of isopropanol were dissolved in the reactor, 200 ml of olefin fraction was added, and e was buffered at the beginning of the reaction to pH 5.5, heated to a nitrogen atmosphere, then air is passed at this temperature (3 l / h). The disappearance of the bisulfite controls comfort by iodometric method; the pH remains almost unchanged, the reaction is completed within 2 hours 15. When the product is precipitated according to the method of Example 1, 125 g of dry product is obtained with a content of Na2S04 of 13.7 g, 85 g of olefins are recovered. 0.24 mol (l / h) based on the average molecular weight of the product. Example 8. The experiment of example 7 is repeated with the addition of 100 mg of MnOg (1.2 x 10 3 mol) to the reaction mixture. During the reaction, the pH is increased to 8.5. The reaction is completed within 45 minutes, after filtration of the catalyst, 62 g of olefin and 158 g of dry product with a content of 4.3% by weight are isolated. The yield of the process is 0.9 mol (l / h). Example 9. To 30 g (0.3 mol) in 150 ml of water and 350 ml of isopropanol, 100 ml of an oC-olefin 50 mg (0.6.) MpOg are added, heated under nitrogen to 80 ° C, then air is passed at a flow rate of 1.5 l / h. the pH is maintained at about 4.5 by barbring as the pH rises. The reaction is completed within 40 minutes, then the pH is adjusted to 9 with NaOH, the catalyst is filtered through BcUOT, 50 g of olefin and 55 g of dry product containing 5.6% by weight, which consists almost entirely of sodium 1,2-dodecane disulfonate . Example 10 The experiment from Example 9 is repeated. The pH is adjusted to about 6.8 ° C using sodium hydroxide. The reaction is completed within 45 minutes, to obtain 31 g of olefin and 70 g of dry product containing 3.2% by weight, containing sodium monoalkanesulfonate about 210 mmol, sodium alkanisupononate 1.2 to about 40 mmol.
    权利要求:
    Claims (4)
    [1]
    1. A method for producing alkyl sulfonates by reacting an olefin with 6i: alkali metal sulfite in the presence of a promoter and oxygen in an aqueous alcohol with heating, characterized in that, in order to simplify the process, manganese dioxide is used as a promoter.
    [2]
    2. The method according to claim 1, characterized in that the process is carried out
    when the molar ratio of olefin and sodium bisulfite is 1: (0.8-1) and the temperature is lower.
    Sources of information taken into account in the examination
    1. US patent 2653973, cl. 260-543, published. 1953.
    2. US patent 3084186, cl. 260-513, published. 1963.
    [3]
    3. US patent number 3450749. class. 260-513, published. 1969.
    [4]
    4. USSR author's certificate number 197577, cl. C 07 C 139/00, 1967 (prototype).
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    同族专利:
    公开号 | 公开日
    ZA733784B|1974-09-25|
    AU5443473A|1974-10-17|
    CA1004686A|1977-02-01|
    JPS4962417A|1974-06-17|
    GB1421250A|1976-01-14|
    NO137089C|1977-12-28|
    BE801097A|1973-10-15|
    FR2189388A1|1974-01-25|
    CH576953A5|1976-06-30|
    SE417506B|1981-03-23|
    NL7308671A|1973-12-27|
    NO137089B|1977-09-19|
    ES416323A1|1976-05-01|
    JPS5414093B2|1979-06-05|
    FR2189388B1|1977-05-13|
    DE2331515C2|1982-09-16|
    IE38692B1|1978-05-10|
    DK137271C|1978-07-17|
    IE38692L|1973-12-21|
    LU67836A1|1973-08-28|
    NL155253B|1977-12-15|
    DK137271B|1978-02-13|
    IT956743B|1973-10-10|
    DE2331515A1|1974-01-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR1087994A|1953-01-12|1955-03-02|Bohme Fettchemie Gmbh|Process for preparing 3-oxypropane-1-sulfonic acid salts|
    US3275681A|1963-05-20|1966-09-27|Little Inc A|Catalytic system for the addition of bisulfites to olefins|
    GB1053773A|1964-02-19|
    US3479397A|1965-09-09|1969-11-18|Marathon Oil Co|Preparation of sulfonates by the reaction of olefins and bisulfite|
    DE1643585A1|1967-09-01|1971-07-01|Atlas Refinery Inc|Process for the preparation of alkanesulfonates|
    GB1363848A|1970-10-14|1974-08-21|Unilever Ltd|Preparation of alkane sulphonates|IT1045798B|1973-12-20|1980-06-10|Snam Progetti|PROCESS FOR THE PREPARATION OF ALCHYL SULPHONATE COMPOUNDS|
    DD154444A3|1980-07-11|1982-03-24|Roland Ohme|PROCESS FOR PRODUCING NEW SULFOBETAINS|
    DD154443A3|1980-07-11|1982-03-24|Detlef Ballschuh|PROCESS FOR PREPARING SULFOBETAINES|
    DD236521A1|1985-04-26|1986-06-11|Akad Wissenschaften Ddr|PROCESS FOR THE PREPARATION OF NEW 3,3,4-TRIMETHYL-4-SULFOMETHYL-PYRROLIDINIUM BEQUINES|
    CN1062556C|1997-12-05|2001-02-28|中国科学院新疆化学研究所|Process for producing alkyl sulfonate from gas of refinery plant|
    US7683209B2|2005-06-07|2010-03-23|E.I. Du Pont De Nemours And Company|Manufacture of hydrofluoroalkanesulfonic acids|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT25984/72A|IT956743B|1972-06-21|1972-06-21|PROCEDURE FOR THE PREPARATION OF ALKYLSULPHONATED COMPOUNDS|
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