Nothing Special   »   [go: up one dir, main page]

CN1227218A - Process for the preparation of diaryl carbonates with improved selectivity - Google Patents

Process for the preparation of diaryl carbonates with improved selectivity Download PDF

Info

Publication number
CN1227218A
CN1227218A CN99101728A CN99101728A CN1227218A CN 1227218 A CN1227218 A CN 1227218A CN 99101728 A CN99101728 A CN 99101728A CN 99101728 A CN99101728 A CN 99101728A CN 1227218 A CN1227218 A CN 1227218A
Authority
CN
China
Prior art keywords
polyaniline
palladium
bromide
compound
carbon monoxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN99101728A
Other languages
Chinese (zh)
Other versions
CN1161320C (en
Inventor
R·V·肖德亚里
S·P·古普特
S·卡纳噶萨巴帕非
A·A·凯尔卡
S·雷德哈克里斯南
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SABIC Global Technologies BV
Original Assignee
General Electric Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by General Electric Co filed Critical General Electric Co
Publication of CN1227218A publication Critical patent/CN1227218A/en
Application granted granted Critical
Publication of CN1161320C publication Critical patent/CN1161320C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/96Esters of carbonic or haloformic acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

诸如碳酸二苯酯之类的碳酸二芳酯的制备方法,包括:在下述催化剂组合物存在下使诸如苯酚之类的羟基化合物与氧和一氧化碳进行反应;所述催化剂组合物包含诸如钯之类的ⅧB族金属元素或其化合物,诸如季铵或六烷基鈲的溴化物之类的溴化物源和处于部分氧化与部分还原态的聚苯胺。优选聚苯胺是搀入卤化物的,且呈与含有醚基或酯基的粘结剂聚合物和形成配合物的盐的共混物的形式。Process for the preparation of diaryl carbonates such as diphenyl carbonate, comprising: reacting a hydroxy compound such as phenol with oxygen and carbon monoxide in the presence of a catalyst composition comprising, for example, palladium Group VIIIB metal elements or their compounds, bromide sources such as quaternary ammonium or hexaalkylguanidine bromides, and polyaniline in partially oxidized and partially reduced states. Preferably the polyaniline is halide doped and in a blend with a binder polymer containing ether or ester groups and a complex forming salt.

Description

Improve the method that optionally prepares diaryl carbonate
Background of invention
The present invention relates to prepare the method for diaryl carbonate by carbonylation.Specifically, the present invention relates in carbonylation reaction, use the catalyst composition of simplifying.
Diaryl carbonate is by carrying out the valuable intermediate that transesterify prepares polycarbonate with the fusion bisphenol compound.This method for preparing polycarbonate than use the toxic gas phosgene as reactant, use such as the environmentally harmful chlorination aliphatic hydrocrbon of methylene dichloride and have the advantage that helps environment protection as the method for solvent.
The method that various carbonylation reactions by hydroxy aromatic compound and carbon monoxide and oxygen prepare diaryl carbonate is disclosed.In general, carbonylation reaction needs quite complicated catalyzer.Referring to, for example, United States Patent (USP) 5,231,210,5,284,964 and 5,399,734 and the common unsettled application serial no of owning together [RD-25582].Wherein said catalyst composition comprises the VIII B family metal metal of ruthenium, rhodium, palladium, osmium, iridium and platinum (that is: be selected from) or its title complex.They be used in combination such as bromide source such as bromination tetra-n-butyl ammonium and bromination Hexaethyl Guanidinium.
According to above listed patent and application, need other catalyst component.They comprise inorganic promotor, be typically, cobalt (II) salt and the title complex that can form the organic compound of title complex, the five tooth title complexs that particularly are mated, representational this class organic compound is a nitrogen-containing heterocycle compound, comprising: pyridines, bipyridyliums, terpyridyl, quinoline, iloquinoline derivative and diquinolyl class, aliphatic polyamines class such as quadrol and tetraalkyl ethylenediamines, crown ether-like, aromatics or aliphatic amidogen ether such as kryptofix 222 (cryptanes) and Schiff's base.Particularly preferred inorganic promotor is the title complex of cobalt (II) and two [3-(salicylic aldehyde amino) propyl group] methylamines in many examples.
Organic promoter also is necessary.They can comprise various terpyridyls, phenanthroline, quinoline and isoquinoline compound, comprising: 2,2 ': 6 ', 2 " terpyridyl, 4 '-methylthio group-2; 2 ': 6 ', 2 " terpyridyl and 2,2 ': 6 ', 2 " terpyridyl N-oxide compound; 1,10-phenanthroline, 2,4; 7,8-tetramethyl--1,10-phenanthroline, 4; 7-phenylbenzene-1,10-phenanthroline and 3,4; 7,8-tetramethyl--1,10-phenanthroline.General terpyridyl preferably, particularly 2,2 ': 6 ', 2 " terpyridyls.
Comprising in the presence of the catalyst composition of less composition, and particularly, it is desirable carrying out carbonylation reaction in the presence of the catalyst composition that does not need to comprise than expensive cobalt complex and terpyridyl.The present invention relates to the application of this catalyst composition.
Summary of the invention
The present invention is a kind of method for preparing diaryl carbonate, this method comprises: significant quantity concerning carbonylation at least a except comprising VIII B family's metallic element and compound thereof, do not contain other metallic elements, do not contain in the presence of the catalyst composition of terpyridyl yet, at least a hydroxy aromatic compound is contacted with oxygen and carbon monoxide, described catalystic material comprises VIII B family's metallic element or its compound, bromide source and the polyaniline that is in partial oxidation and partial reduction attitude.
Describe in detail; Preferred embodiment
Can use any hydroxy aromatic compound in the present invention.General preferred monohydroxyaromatic compound, for example phenol, cresols, xylenol and to cumyl phenol, most preferably phenol.Yet the present invention also can use dihydroxy aromatic compounds, for example; Resorcinol, Resorcinol and 2, two (4-hydroxy phenyl) propane of 2-or " dihydroxyphenyl propane ", this moment, product was a polycarbonate.
The basic reagent of other that uses in the method for the present invention is oxygen and carbon monoxide, and they and phenol reactant form needed diaryl carbonate.
Catalyst composition basal component is one of VIII B family metallic element used according to the present invention, is preferably palladium or its compound.Therefore, what be fit to is palladium black or is deposited on element palladium on the carbon, and palladium compound, the salt that forms as halogenide, nitrate, carboxylate salt, with aliphatic beta-diketon and comprise title complex such as the compounds of carbon monoxide, amine, phosphine class and alkene.Preferred organic acid the most often is C in most of examples 2~6The palladium of aliphatic carboxylic acid (II) salt and such as 2, the palladium of the beta-diketon of 4-diacetylmethane and so on (II) salt.General palladium (II) and 2 most preferably, 4-diacetylmethane palladium (II).
Catalytic material also contains bromide source.It can be quaternary ammonium or quaternary phosphonium bromide, perhaps six alkyl Guanidinium bromides.Often preferred Guanidinium salt; Comprise α, ω-two (five alkyl Guanidinium) alkane salts.Particularly preferably be the salt that contains 2~6 carbon atoms in the alkyl, particularly bromination tetra-n-butyl ammonium and bromination Hexaethyl Guanidinium.
According to the basic catalyst component of another kind of the present invention is the polyaniline of partial oxidation and partial reduction attitude.Polyaniline is well known in the art.This compound can prepare the aniline oxidation by electrochemistry or chemical process.
The typical method of preparation polyaniline is in water medium, in the presence of the acidic cpd that is fit to such as hydrofluoric acid or spirit of salt, to make the aniline oxidation with ammonium persulphate.When using spirit of salt, the pH of water medium is quite low, is generally below 1.0.This method is described in the Indian patent application of the S.Radhakrishnan that submitted in 1997 and S.Unde, and its exercise question is " being applied to the preparation method of the electrically conductive polyaniline of chemical-sensitive element ".It provides the polyaniline as partial oxidation and partial reduction material uniquely, wherein has and contains-C 6H 4The alternative quinonyl that the reduction of NH-structural unit part (about 40~60% weight) and containing is separated by trivalent nitrogen atom and the oxidized portion of phenylene.
One of the characteristic that occupies the polyaniline of critical role in the present invention is to have higher electroconductibility.But, often find that Zhi Bei polyaniline has the low electric conductivity that does not meet the requirements as stated above.
So, for the present invention, usually preferred use by slightly different method synthetic dope halid, particularly dope muriatic polyaniline composition, the step of described method comprises: the oxygenizement under low pH, with inert binder blend and coordination.In the method, aniline being dissolved in the acidic medium, generally is the spirit of salt aqueous solution, its pH scope is about 3.0~4.5, adds the oxygenant that is fit to again, generally is alkali-metal persulphate or iron(ic) chloride, general preferred as alkali persulphate, particularly Sodium Persulfate.The polyaniline that contains additive can be precipitated out from the gained reaction mixture when leaving standstill.Employing generally comprises filters and the exsiccant usual way, and it is separated.Then with itself and the binder polymer blend that contains ether or ester group; The polymkeric substance that is fit to comprises polyoxygenated alkane polyphenylene oxide and acrylate addition polymer.Resulting polymeric blends is dissolved in the suitable solvent; Mix with salt, for example cupric chloride with its formation title complex; Stirring is until obtaining the heavy-gravity slurry.This slurry can be used as catalyst component.
Following example explanation is as the polyaniline preparation of compositions method of catalyst component.
Example 1
10ml (milliliter) aniline is added drop-wise to the dense spirit of salt of 5.5g (gram) in the mixture of 150ml distilled water, the while vigorous stirring, formation pH is 4.3 transparent liquid.Slowly add the solution of 5.3g ammonium persulphate in 100ml water, stir simultaneously, allow reaction mixture at room temperature leave standstill 20 hours, so separate out a large amount of green brown precipitates.This mixture is poured into makes polyaniline precipitation in the 1000ml distilled water.
Sedimentary polyaniline is filtered, with distilled water wash several times, dry then.With its sample of 200mg (milligram) and 800mg molecular weight is about 3000 polyethylene oxide and the 20ml methanol mixed that contains the 80mg cupric chloride.This solution of vigorous stirring is until the thickness slurry that forms even color and luster and denseness.This slurry is the muriatic polyaniline of doping of needed partial reduction.
Example 2
9.3ml aniline is added drop-wise to the dense spirit of salt of 5.5g in the mixture of 150ml distilled water, the while vigorous stirring, formation pH is 3.8 transparent liquid.Slowly add the solution of 3.2g iron(ic) chloride in 20ml water, stir simultaneously, allow reaction mixture at room temperature leave standstill 24 hours, so separate out a large amount of light green precipitations.This mixture is poured into makes polyaniline precipitation in the 1000ml distilled water.
Sedimentary polyaniline is filtered, with distilled water wash several times, dry then.With its sample of 200mg (milligram) and 800mg molecular weight is about 3000 polyethylene oxide and the 20ml methanol mixed that contains the 80mg cupric chloride.This solution of vigorous stirring is until the thickness slurry that forms even color and luster and denseness.This slurry is the muriatic polyaniline of doping of needed partial reduction.
The ratio in employed in the method for the invention VIII B family metallic element source is, is enough to for per 800~10,000, preferred 2,000~5, and 000mol (mole) hydroxy aromatic compound provides the amount of about 1 grammeatom metallic element.Concerning every grammeatom VIII B family metallic element, use about 5~150, preferred about 20~50mol bromide source usually.The scope of the weight ratio of polyaniline and VIII B family metallic element compound is generally about 0.2~5.0: 1.
Infeed gas in reaction mixture, its ratio is about 2~50% (mole) oxygen, and rest part is a carbon monoxide.Gas can add respectively or add with the form of mixture, to the total pressure scope be about 10~250 normal atmosphere.General range of reaction temperature is about 60~150 ℃.In reaction vessel, can there be siccative.It generally is molecular sieve.For reaction is carried out as quickly as possible, preferably keep reaction pressure, till hydroxy aromatic compound transforms fully according to above-mentioned United States Patent (USP) 5,399,734.
The diaryl carbonate that generates by method of the present invention can adopt traditional method to separate.Often preferably form and the adducts of pyrolysis diaryl carbonate and hydroxy aromatic compound, as at United States Patent (USP) 5,239,106 and 5,312, such described in 955.
Following example explanation the present invention.
Example 3~5
In each high-pressure reactor (50ml volume), add each batch reaction thing, palladium (II) that reactant consists of about 20g phenol, 800mg Tetrabutylammonium bromide and different amounts and the polyaniline similar to example 1, described polyaniline is 50% reduction and 50% oxidation state, and its molecular weight is about 3380.The activation 3A type molecular sieve that about 4.5g is fresh places the basket that is fixed on each reactor head.
With the reactor sealing, with carbon monoxide cleaning twice,, be heated to 100 ℃, simultaneously vigorous stirring with 66.3 normal atmosphere carbon monoxide and 5.1 normal atmosphere oxygen superchargings.Fall the monitoring reaction process by record still internal pressure, and with gas make-up pressure, its condition is a carbon monoxide to the ratio of oxygen is necessary 2: 1.When reaction is finished,, and analyze the cooling of the material in the reactor.It the results are shown in the following table." phenol conversion " is the ratio that is converted into the phenol of product, and " selectivity " (for diphenyl carbonate) is to be the percent value of the diphenyl carbonate that is generated of benchmark in the total reaction product.
Example 345
Phenol, g palladium (II), the mg polyaniline, the mg molecular sieve, the g reaction times, hour phenol conversion, the % selectivity, % ?20.845????21.09????19.63 ?22????????22???????44 ?50????????9????????10 ?4.56??????4.0??????4.0 ?9?????????8????????8 ?25????????13.6?????47.2 ?40????????52???????6.0

Claims (17)

1.一种制备碳酸二芳酯的方法,该方法包括:在对羰基化作用来说有效量的至少一种除了包含ⅧB族金属元素及其化合物之外不含其他金属元素的、也不含三联吡啶的催化剂组合物存在下,使至少一种羟基芳族化合物与氧和一氧化碳相接触,所述催化剂材料包含ⅧB族金属元素或其化合物、溴化物源和处于部分氧化和部分还原态的聚苯胺。1. A method for preparing diaryl carbonate, the method comprising: at least one metal element containing Group VIIIB group metal elements and their compounds and containing no terpyridine in an effective amount for carbonylation At least one hydroxyaromatic compound is contacted with oxygen and carbon monoxide in the presence of a catalyst composition comprising a Group VIIIB metal element or compound thereof, a bromide source, and polyaniline in partially oxidized and partially reduced states. 2.按照权利要求1的方法,其中羟基芳族化合物是苯酚。2. A process according to claim 1 wherein the hydroxyaromatic compound is phenol. 3.按照权利要求2的方法,其中ⅧB族金属元素是钯。3. The method according to claim 2, wherein the Group VIIIB metal element is palladium. 4.按照权利要求3的方法,其中溴化物源是季铵或季磷溴化物,或溴化六烷基鈲。4. The method according to claim 3, wherein the bromide source is a quaternary ammonium or phosphonium bromide, or hexaalkylguanidine bromide. 5按照权利要求4的方法,其中溴化物源是溴化四正丁基铵,或溴化六乙基鈲。5. The method according to claim 4, wherein the bromide source is tetra-n-butylammonium bromide, or hexaethylguanidinium bromide. 6按照权利要求5的方法,其中钯化合物是醋酸钯(Ⅱ)或2,4-戊二酮钯(Ⅱ)。6. A process according to claim 5, wherein the palladium compound is palladium(II) acetate or palladium(II) 2,4-pentanedione. 7.按照权利要求4的方法,其中聚苯胺为还原部分占约40~60%(重量)的部分氧化和部分还原态。7. The method according to claim 4, wherein the polyaniline is in a partially oxidized and partially reduced state with reducing moieties comprising about 40 to 60% by weight. 8.按照权利要求7的方法,其中聚苯胺是搀入卤化物的。8. A method according to claim 7, wherein the polyaniline is halide-doped. 9按照权利要求8的方法,其中聚苯胺是搀入氯化物的。9. A method according to claim 8, wherein the polyaniline is chloride doped. 10.按照权利要求8的方法,其中聚苯胺的制备方法包括:在pH范围为约3.0~4.5的酸性水介质中用碱金属过硫酸盐或氯化铁进行氧化,与含有醚基或酯基的粘结剂聚合物共混,以及与和所述聚苯胺形成配合物的盐混合。10. The method according to claim 8, wherein the preparation method of polyaniline comprises: oxidizing with alkali metal persulfate or ferric chloride in an acidic aqueous medium with a pH range of about 3.0 to 4.5, The binder polymer is blended and mixed with a salt that forms a complex with the polyaniline. 11.按照权利要求10的方法,其中苯胺是用过硫酸钠氧化的。11. A process according to claim 10, wherein the aniline is oxidized with sodium persulfate. 12.按照权利要求10的方法,其中苯胺是用氯化铁氧化的。12. A process according to claim 10, wherein the aniline is oxidized with ferric chloride. 13.按照权利要求10的方法,其中该盐是氯化铜。13. A method according to claim 10, wherein the salt is copper chloride. 14.按照权利要求4的方法,其中氧和一氧化碳的比例是约2~50%(摩尔)氧,其余部分是一氧化碳。14. 4. The method of claim 4, wherein the ratio of oxygen to carbon monoxide is about 2 to 50 mole percent oxygen with the balance being carbon monoxide. 15.按照权利要求4的方法,其中钯的比例是,每2,000~5,000摩尔羟基芳族化合物约1克原子。15. A method according to claim 4, wherein the proportion of palladium is about 1 gram atom per 2,000 to 5,000 moles of hydroxyaromatic compound. 16.按照权利要求4的方法,其中聚苯胺与钯化合物的重量比范围为约0.2~5.0∶1。16. The method according to claim 4, wherein the weight ratio of polyaniline to palladium compound is in the range of about 0.2 to 5.0:1. 17.按照权利要求4的方法,其中对于每克原子钯来说,存在约5~150摩尔溴化物源。17. 4. The method of claim 4 wherein the source of bromide is present from about 5 to 150 moles per gram atom of palladium.
CNB991017285A 1998-02-03 1999-02-01 Process for the preparation of diaryl carbonates with improved selectivity Expired - Fee Related CN1161320C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN175/CAL/98 1998-02-03
IN175CA1998 1998-02-03

Publications (2)

Publication Number Publication Date
CN1227218A true CN1227218A (en) 1999-09-01
CN1161320C CN1161320C (en) 2004-08-11

Family

ID=11081344

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB991017285A Expired - Fee Related CN1161320C (en) 1998-02-03 1999-02-01 Process for the preparation of diaryl carbonates with improved selectivity

Country Status (6)

Country Link
JP (1) JPH11279114A (en)
KR (1) KR19990072367A (en)
CN (1) CN1161320C (en)
AR (1) AR016018A1 (en)
BR (1) BR9900615A (en)
ZA (1) ZA99367B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102557949A (en) * 2010-12-28 2012-07-11 中国石油化学工业开发股份有限公司 Process for producing diaryl carbonate
US12006299B2 (en) 2019-09-05 2024-06-11 Shell Usa, Inc. Process and system for the production of ethylene carbonate and/or ethylene glycol

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2466123C2 (en) * 2007-08-14 2012-11-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method of producing alkylene glycol

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102557949A (en) * 2010-12-28 2012-07-11 中国石油化学工业开发股份有限公司 Process for producing diaryl carbonate
CN102557949B (en) * 2010-12-28 2014-12-31 中国石油化学工业开发股份有限公司 Process for producing diaryl carbonate
US12006299B2 (en) 2019-09-05 2024-06-11 Shell Usa, Inc. Process and system for the production of ethylene carbonate and/or ethylene glycol

Also Published As

Publication number Publication date
ZA99367B (en) 1999-07-19
JPH11279114A (en) 1999-10-12
AR016018A1 (en) 2001-05-30
BR9900615A (en) 2000-04-11
CN1161320C (en) 2004-08-11
KR19990072367A (en) 1999-09-27

Similar Documents

Publication Publication Date Title
CN1187310C (en) Catalyst composition and method for producing diaryl carbonates using nitrile as promoter
GB1572291A (en) Production of aromatic polycarbonates
US20010020109A1 (en) Method and catalyst system for producing aromatic carbonates
CN1227218A (en) Process for the preparation of diaryl carbonates with improved selectivity
US5917077A (en) Method for preparing diaryl carbonates with improved selectivity
CN1427814A (en) Method and catalyst system for producing aromatic carbonates
US6680385B2 (en) Catalytic preparation of aryl methyl ketones using a molecular oxygen-containing gas as the oxidant
US6143913A (en) Method and catalyst system for producing aromatic carbonates
US6355597B1 (en) Catalyst system for producing aromatic carbonates
CN100388978C (en) Complex catalyst for homogeneous oxidative carbonylation of alcohol to carbonate, preparation process and use method thereof
CA2513979C (en) Cross-coupling reactions
CN1350514A (en) Method and catalyst system for producing aromatic carbonates
CN1349492A (en) Method and catalyst system for producing aromatic carbonates
JPH075511B2 (en) Method for producing carboxylate
CA1297889C (en) Pyridine ligands for preparation of organic carbonates
CN1349493A (en) Method and catalyst system for producing aromatic carbonates
US7084291B2 (en) Water resistant catalyst for the production of diaryl carbonates via the direct carbonylation of phenolic compounds
WO2000066534A1 (en) Method and catalyst system for producing aromatic carbonates
CA1260955A (en) Method of producing adiponitrile
WO2005023739A1 (en) Selective catalytic oxybromination of hydroxyaromatic compounds
DE69905232T2 (en) Process for the preparation of diaryl carbonates with improved selectivity
TWI359134B (en)
JP3982961B2 (en) Copper complex catalyst for oxidative polymerization of fluorophenol and oxidative polymerization method
US6153810A (en) Highly selective process for making o-arylbenzonitriles
JP2013513633A (en) Bimetallic complexes and their use in the preparation of diaryl carbonates

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: SAUDI ARABIA BASE CREATION PLASTICS IP PRIVATE CO

Free format text: FORMER OWNER: GENERAL ELECTRIC CO.

Effective date: 20080829

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20080829

Address after: Holland city Aupu zoom Bergen

Patentee after: Sabic Innovative Plastics IP

Address before: American New York

Patentee before: General Electric Company

C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee