• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1. METHOD OF OBTAINING DIMETSH1KARBONAT by contacting methanol with carbon monoxide and oxygen at 70-200 ° C C and elevated pressure in the presence of a catalyst, preposing a copper salt, containing an inorganic anion, selected from the group comprising C1 iBr, 0104, characterized in that, in order to improve the selectivity of the process, a copper salt is used as a catalyst, inorganic anion per copper cation. 2. The method according to p. 1.0 t liter yuschi by the fact that first methanol in the presence of a copper salt selected from the group CuCl, SyBr, CSC 0, is in contact with oxygen, and then with carbon monoxide. SP 3. Method POP.1, characterized in that J1TO, methanol is continuously brought into contact with oxygen and carbon monoxide.
    公开号:SU1115667A3
    申请号:SU772524854
    申请日:1977-09-27
    公开日:1984-09-23
    发明作者:Романо Уго；Тесси Ренато；Чиприани Джоаккино；Микуччи Лидио
    申请人:Аник С.П.А (Фирма)；
    IPC主号:
    专利说明:

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    Inventing otplsggs to the method of obtaining methylcarbonates "including; - - herd, distilled esterified alcohol - with carbon monoxide TI with oxygen in P1) and the catalyst, co iep / jcajnero salt, eGGLla" preferred: 11o salt 1. ; uni5 and ioi metal coz; di-U .GM. with a palp-1 before her vozmolil.m g with the number of peorgagichesk1-X aiopoz.
    The esters of carbonic acid 5 well lime) ;. Oiiii is used as a jjacTHoiJiTrejiefi and polymerizue1. CNH agiton for re-esterification reactions with glyphs i-i bnsphe olami in order to obtain polycarbonateB.
    A way; Some of the more 1UHpoxo are used to produce complex esters of smallpox in a reaction mixture of alcohol and (boereiioM or chloroformaginia 11ris1strigues of bases. Egg; half-way 1; 1 of them are taken from ri ynp, each ; -; KA1 e-G (hydroxides: and carbonaceous tselochv.})}; stals and ii; ejiO4iiO-3c-melted metals or pyridine and druga org; -; natural ogyuvani. Odley- ;; these methods are dangerous and -; ayutsk:;: lsa-hoi p; :) om: lenna pr1-lh) dan7 yu.
    And: and; if1 method; Oluchs; p-: karo :): a-TOV-, Oppovalnna ia reactit-; -ge-k / gu C: .BID current, okayyo carbon, and oxygen cord held in the presence of -; katg; lil-1g: i; from KOMfUiej coB metal, method; 1st as a result
     divalent states .--.
    However, the complexity of complexable catalysts with a five-core system, moreover, the method shows a definite sensation of exposure to water and,: Vuokieyi uvleood, formed in; -EU1H-: with the ophthalmic acid) during the reg-e; which leads to a low conversion rate of syirt. There are such difficulties with regard to the separation of the products of reactive and especially water and; levuokie -; SW:; Orde from the stream forming in the reactor and from the bulk of the catalyst, due to the fact that. Chigand usually has a net ori.ich.e. the base and there is some hydrolysis of ether, due to the presence of water in sietezm.
    The same reaction is likely in certain .jieHH ;; x ycJyuvi x in the presence of a proet; x metal salts, this fact was surprisingly surprising, since it was known until now that in the presence of such a catalytic system only polyfunctional alcohols are capable to
    reactions with; the formation of coal esters
    Co 1 KI5CJ O (bI. .I J,
    . Guides the way to. G ucheki esters of the angle of a single cue. Npj-interaction
    in accordance with: - alcohol e oif-icbso of urod in the Fisusen g: ions of divalent one, salt D of cobalt copper with, cer; cat two inorganic anions, such as SG .jBr; C10; and the like;
    on. OD1N1 cation g-hal-pas Eucodipturity byus1 eats); not only in a wide e; -.) Range (10-250 ° C) GDV1 noBhHireiH-ioM.
    C /; papins of this method are low; - OL ester of carbonic acid in some way JIabJJJudaet the image of the existing amount of halide alkyls, ethers and hydrogen halide ACID; J so the pH value of the solution
    with 1. (IiCB in with 1 1e - you are gPoy
    acidic, i.e., selectivity in the process is highly viable,
    .1, elvc) H3o6piiTeiiHB is higher-pi;} selek-1and}
     ,: - ssl-n:; eni this one, according to her; c y g hpuche.ni d; -1;.; e..i: 1carbonate .iu-g-e-.1, .1c G1; eroded: -t metha1-th.la with
    I, and H (,). HHOM d ;;.) In when -CyTciBMB tsat.alnagora- representing.; soool-i salt of copper, co.nergy chenu veor-, chi, 1, and: esk: - | th selected 1 P1: from —runp; as catalyst use
    Solv copper containing inorganic-1. A.won pa pa otsyn KaT.i, ioii ligdi,
    Srog-e -.- it, at the beginning MeTaiJoJv, in lirieutsgvi: copper salt, extruded, from the group-, Ci,; C I ,, (yggv: ,, ZjClG., Contact
    C: uschs, lorsdom ,, a z, z.tem - with a corner / ia;
    Metacol - just one time in a different way, a1r to kog, a beat with oxygen vv uvlerode oxide, the possibility of obtaining ethers
    The angle of KiicjiOTij lutegsch reaction corresponding to alcohol with carbon oxide and carbon, rock in the presence of a metal salt, belongs to groups 1B, PV 3 ii UH of periodic element systems, nr -1 than metal ion is the least useful — -; the number of inorganic avi iopes special
    gd, e R - hydrocarbon / | nd pa; n, 1kal, selected from alkyls, aryls or cycloalkyls,
    The reaction is carried out by dispersing or dissolving the corresponding metal salt in a solvent; as which you can use alcohol or other inert diluent.
    When using salts with a limited amount of inorganic anions, high acidity substances do not form during the reaction. The system remains at pH values of a weakly acidic character, so that the reaction itself is not disturbed and proceeds to obtain a high yield of carbonic ester, not accompanied by the formation of appreciable amounts of by-products.
    The reaction is carried out either by dispersing or dissolving the metal salt in among the solvent. As a result of this dispersion or dissolution, a stream of carbon monoxide and oxygen is directed, with carbon monoxide and oxygen being supplied either individually or in a mixture, either continuously or in batch cycles.
    The target product is isolated from the reaction mixture using simple physical methods. In the case of dispersion, for example, to remove the catalyst, sufficiently filtering followed by separation of the solution containing carbonic ester. The latter is then removed by distillation or crystallization.
    The method can be carried out using a variety of pressures and temperatures, the upper limits are dependent, for example; from durability of used compounds. Operating temperatures 70-200
    ° C, with carbon monoxide and oxygen pressures exceeding atmospheric pressure,
    Example 1. Teflon-lined autoclave with a capacity of 200 ml is charged with 100 ml of methanol and 10 g of copper bromide. Sistema is oxidized by oxygen at 60 ° C at an oxygen gauge pressure of 5 atm. within 90 minutes. At that, carbon monoxide is supplied to a gauge pressure of 12 atm and the temperature is brought to 80 ° C. Carbon monoxide is replaced in the system as it is used in the reaction so that it does not affect the total, The reaction is completed within 30 minutes - and the solution is analyzed
    with Grimany gas chromatography. Full copper conversion and selectivity of 95% dimethyl carbonate are obtained, residual copper oxidizes carbon monoxide to carbon dioxide. 4 anelogical follow-up cycles were carried out, with only a slight increase in the COj selectivity in time 1HN. In the fourth cycle, the molar ratio of carbon dioxide and dimethyl carbonate. 1: 9.
    Example 2 In the aparate described in p. Bri; ere, zagr -; -; 100 ml of methanol and 20 g of x.n.opHCTo: f copper, the systems are oxidized with oxygen up to 80 ° C at a manometric pressure of 10 atm for 60 MiiH. Then carbon oxides are supplied at a constant gauge pressure of 30 atm. I increase the temperature of the sherature to 00 ° C. The reaction lasts for 90 lat. After completion of the reaction, the copper remains at. completely restored condition The yield of dimethyl carbonate is 95%, while the residual copper is carbon dioxide and carbon dioxide. Fully selective for methanol is observed.
    PRPG.-er 3. The apparatus described in prig.; Ery, load 16.4 g, CCU and 26 g of etaiol. The system is oxidized with oxygen to 100 ° C and at manometric pressure; a pressure of 5 atm for 1–20 minutes, and reduced by carbon monoxide as ka ;; o1-; etic; pressure 50 atm. at 100 C 3 for 2 hours. After the completion of the reaction, copper is completely restored; The output dime .- :; 1-carbocate. more than 95%. Residual copper acid. emits carbon to dioxides ;; carbon, and selectivity relative to methanol is full.
    Prt1: -: 4, The apparatus described in the example is “loaded with 15 g of methanol and south of chlorine copper. 3.9g of sodium metplate is added to the system. In 20 g of methanol; way to neutralize any of the two chloride ions connected to the copper atom. The temperature of the reaction mixture is brought to 100 s, carbon monoxide is introduced at a gauge pressure of 6, atm. After 2 hours, complete recovery of copper to copper chloride occurs, methyl carbonate is obtained in a yield of approximately 90% of the theoretical value. The formation of small amounts of methyl chloride and dimethyl ether can be noted, but their content is less than 0.2%.
    S, 11
    Example 5. A ceramic-lined autoclave lined with 3 liters of methanol and 480 g of copper chloride, the temperature was raised to 70 ° C, oxygen was introduced at a pressure of 8 atm. until a full oxide of Lenin copper is reached, which is completed within about an hour. Then excess
    oxygen is released into the atmosphere and carbon monoxide is introduced at a constant gauge pressure of 5 atm. Within 3 hours, complete conversion of copper is observed. The selectivity of more than 95% relative to dimethyl carbonate, the residual copper oxidizes carbon monoxide to carbon dioxide. Selectivity relative to methanol is full. In the three subsequent cycles, the course of the reaction is the same as in the first, there is only a small increase in the carbon dioxide content between the reaction cycle and the subsequent processes.
    Example 6. The apparatus described in Example 5 is loaded with 3 liters of methanol and 480 g of copper chloride, increased to 100 ° C and oxygen is introduced at a manometric pressure of JO atm until complete oxidation of copper is reached, which takes about 30 minutes. The oxygen is removed to the atmosphere and carbon monoxide is introduced at a gauge pressure of 20 atm., while the temperature is maintained at 120 ° C. After 20 minutes the reaction is complete, the
    6
    Relation to dimethyl carbonate 92%. Residual copper oxidizes carbon monoxide to carbon dioxide. Example 7. In the apparatus described in example 5, load 3 liters of methanol and 480 g of copper chloride. At a thermostatically controlled system, at a temperature of 102 ° C, 150 standards, l / h, carbon monoxide and 50 nm are introduced. l / h oxygen at the same time with a full manometric pressure of 30 atm. The system is continuously released into the atmosphere, discharging 50 norms per hour, a L-gas & mixture consisting of 97% carbon monoxide, 2-3% carbon monoxide and 0.1-0.4% oxygen. After 4 hours, the conversion of methanol is 30%, and the selectivity relative to dimethyl carbonate is 95%.
    Example B. In the apparatus described in example i, load 16 g of copper sulfate and 30 ml of methanol. 3.8 g of lithium methylate are introduced into the system in 10 ml of methanol to neutralize half of the sulfate ion. Enter. Carbon monoxide at a pressure of 50 atm. The temperature is brought to 110 ° C. After 2 hours, copper is completely reduced to monovalent copper sulfate. Dimethyl carbonate is obtained in 75% yield relative to copper. Residual copper oxidizes carbon monoxide to carbon dioxide. The relative selectivity of methanol is complete.
    权利要求:
    Claims (3)
    [1]
    1. METHOD FOR OBTAINING DIME-
    TILKARBONATE by contacting methanol with carbon monoxide and oxygen at 70-200 ° C and elevated pressure in the presence of a catalyst, which is a copper salt containing an inorganic anion selected from the group consisting of C1 “, Br ~, 0 0 ^ characterized in that , in order to increase the selectivity of the process, a copper salt containing one inorganic anion per copper cation is used as a catalyst.
    [2]
    2. The method according to claim 1, with the fact that first, methanol in the presence of a copper salt selected from the CuC group), CuBr, CCCE, is contacted with oxygen, and then with carbon monoxide .
    [3]
    3. The method according to claim 1, characterized in that methanol is simultaneously introduced into contact with oxygen and carbon monoxide.
    SU <"1115667"
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    同族专利:
    公开号 | 公开日
    DE2743690A1|1978-04-06|
    DK157674B|1990-02-05|
    FR2366254B1|1980-10-17|
    LU78193A1|1978-01-23|
    JPS6058739B2|1985-12-21|
    BE859272A|1978-03-30|
    DK157674C|1990-07-09|
    FR2366254A1|1978-04-28|
    AT368123B|1982-09-10|
    JPS5344523A|1978-04-21|
    ATA696277A|1982-01-15|
    NL7710689A|1978-04-03|
    DE2743690C3|1980-01-10|
    GB1574188A|1980-09-03|
    DE2743690B2|1979-05-03|
    DK432077A|1978-03-31|
    IT1070574B|1985-03-29|
    CA1098535A|1981-03-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    EP0071286B1|1981-07-30|1985-08-28|Shell Internationale Researchmaatschappij B.V.|Process for the preparation of carbonate esters|
    DE3926709A1|1989-08-12|1991-02-14|Basf Ag|METHOD FOR PRODUCING DIALKYL CARBONATES|
    DE3926710A1|1989-08-12|1991-02-14|Basf Ag|METHOD FOR PRODUCING DIALKYL CARBONATES|
    DE4018228A1|1990-06-07|1991-12-12|Henkel Kgaa|FLOWABLE DRILL TREATMENT AGENTS BASED ON CARBONIC DIESTERS|
    DE4138755A1|1991-11-26|1993-05-27|Bayer Ag|METHOD FOR PRODUCING DIALKYL CARBONATES|
    DE4140259A1|1991-12-06|1993-06-09|Basf Ag, 6700 Ludwigshafen, De|METHOD FOR PRODUCING TERTIA AMINOXIDES|
    DE4203796A1|1992-02-10|1993-08-12|Bayer Ag|METHOD FOR PRODUCING DIALKYL CARBONATES|
    DE4325651A1|1993-07-30|1995-02-02|Bayer Ag|Process for the preparation of dialkyl carbonates|
    DE4339977A1|1993-11-24|1995-06-01|Bayer Ag|Process for working up the liquid reaction products from the copper-catalyzed production of dimethyl carbonate|
    DE4344159A1|1993-12-23|1995-06-29|Bayer Ag|Process for the preparation of dimethyl carbonate|
    US6258923B1|1999-06-11|2001-07-10|General Electric Company|Method for manufacturing dialkyl carbonate|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT27825/76A|IT1070574B|1976-09-30|1976-09-30|PROCEDURE FOR THE PREPARATION OF CARBONIC ACID ESTERS|
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