EP0000563A1 - Procédé de préparation d'uréthanes aromatiques - Google Patents

Procédé de préparation d'uréthanes aromatiques Download PDF

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Publication number
EP0000563A1
EP0000563A1 EP78100468A EP78100468A EP0000563A1 EP 0000563 A1 EP0000563 A1 EP 0000563A1 EP 78100468 A EP78100468 A EP 78100468A EP 78100468 A EP78100468 A EP 78100468A EP 0000563 A1 EP0000563 A1 EP 0000563A1
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Prior art keywords
compound
formula
group
process according
carbon atoms
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EP78100468A
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German (de)
English (en)
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EP0000563B1 (fr
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Yutaka Hirai
Katsuharu Miyata
Makoto Aiga
Seiji Hasegawa
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Mitsui Toatsu Chemicals Inc
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Mitsui Toatsu Chemicals Inc
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Priority claimed from JP8844177A external-priority patent/JPS5424853A/ja
Priority claimed from JP8980577A external-priority patent/JPS5424854A/ja
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Publication of EP0000563A1 publication Critical patent/EP0000563A1/fr
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C271/00—Derivatives of carbamic acids, i.e. compounds containing any of the groups, the nitrogen atom not being part of nitro or nitroso groups
    • C07C271/06—Esters of carbamic acids

Definitions

  • This invention relates to improvements in the preparation of aromatic urethanes. More particularly, it relates to an improved process for preparing an aromatic urethane (hereinafter referred to simply as “urethane") which comprises reacting an aromatic nitro compound, an organic compound containing at least one hydroxyl group (hereinafter referred to simply as “hydroxyl i containing compound”), and carbon monoxide at elevated temperature and pressure in the presence of a catalytic system composed of a catalyst consisting of a platinum metal, a platinum metal compound, and/or a platinum metal compound-containing compound and a promoter consisting of a Lewis acid and/or a Lewis acid-containing compound.
  • urethane an aromatic urethane
  • hydroxyl i containing compound an organic compound containing at least one hydroxyl group
  • a catalytic system composed of a catalyst consisting of a platinum metal, a platinum metal compound, and/or a platinum metal compound-containing compound and a promoter consisting of a Lewis acid and/or a Lewis
  • U.S. Patent No. 3,338,956 describes a process wherein urethanes are prepared from alcohols, carbon monoxide, and nitro compounds with the aid of a rhodium chlorocarbonyl catalyst.
  • this process is not economically advantageous in the preparation of highly pure urethanes because the desired product is obtained only at low yield even if the urethanation reaction is carried out for a long period of time in the presence of a large amount of the catalyst.
  • urethanes can be obtained at a fairly high yield of 80 - 90 % even by using dinitro compounds as the main starting material.
  • the process has an industrially serious drawback in that the Lewis acid, e.g.
  • ferric chloride used as the promoter exerts a considerable corrosive action on metallic materials such as iron, stainless steel, and the like. Consequently, it is essential to use a reactor made of or lined with glass or tantalum in order to realize the process industrially.
  • a glass or tantalum reactor under the above-mentioned high temperature and pressure conditions poses further technical and economical problems.
  • a process for preparing an aromatic urethane which comprises reacting an aromatic nitro compound, a hydroxyl-containing compound, and carbon monoxide at elevated temperature and pressure in the presence of a catalytic system composed of a catalyst consisting of a platinum metal, a platinum metal compound, and/or a platinum metal compound-containing compound and a promoter consisting a Lewis acid and/or a Lewis acid-containing compound; wherein the improvement comprises adding an organic primary amino compound, a urea compound, a biuret compound, an allophanate compound, or a mixture thereof to the reaction system.
  • the aforesaid organic primary amino compound may be any of the compounds represented by the formula In the above formula (I), R represents a linear or branched alkyl group containing from 1 to 16 carbon atoms, a cycloalkyl group of 6 carbon atoms with or without an alkyl substituent containing from 1 to 3 carbon atoms, an aryl group with or without at least one alkyl substituent containing fran 1 to 6 carbon atoms, and these alkyl, cycloalkyl and aryl groups may further have a least one halogen, aryl, alkenyl, cyano, nitro,alkoxy, phenoxy, thioalkoxy, thiophenoxy, carbalkoxy, carbamate, carbamyl, carbaryloxy or thiocarbamyl substituent.
  • each of R', R" and R"' represents a hydrogen atom, a linear or branched alkyl group containing from 1 to 16 carbon atoms, a cycloalkyl group of 6 carbon atoms with or without an alkyl substituent containing from 1 to 3 carbon atoms, or an aryl group with or without at least one alkyl substituent containing from 1 to 6 carbon atoms, and these alkyl, cycloalkyl and aryl groups may further have at least one halogen, aryl, alkenyl, cyano, nitro, alkoxy, phenoxy, thioalkoxy, thiophenoxy, carbalkoxy or thiocarbanyl substituent; and R 1 represents .
  • a linear or branched alkyl group containing from 1 to 16 carbon atoms a cycloalkyl group of 6 carbon atoms with or without an alkyl substituent containing from 1 to 3 carbon atoms, or an aryl group with or without at least one alkyl substituent containing from 1 to 6 carbon atoms, and these alkyl, cycloalkyl and aryl groups may further have at least one halogen, aryl, alkenyl, nitro, alkoxy, phenoxy or carbamate substituent.
  • the urethanation reaction is carried out in the presence of a small amount of water and one or more of those organic primary amino compounds, urea compounds, biuret compounds, and allophanate compounds which can be derived from the starting aromatic compound.
  • the starting aromatic nitro compound is a compound of the formula where A represents a substituted or unsubstituted aromatic residue of an aromatic nitro compound from which the nitro group or groups are removed and x is an integer equal to from 1 to 4
  • the starting hydroxyl-containing compound is a compound of the formula where R 1 represents a linear or branched alkyl group containing from 1 to 16 carbon atoms, a cycloalkyl group of 6 carbon atoms with or without an alkyl substitutent containing from 1 to 3 carbon atoms or an aryl group with or without at least one alkyl substituent containing from 1 to 6 carbon atoms
  • these alkyl, cycloalkyl and aryl groups may further include at least one halogen, aryl, alkenyl, nitro, alkoxy, phenoxy or carbamate substituen, those organic primary amino compounds, urea compound, biuret compounds, and allophanate compounds which can be derived from the starting aromatic nitro compound are represented
  • the desired aromatic urethane can be prepared at a higher reaction rate, or in a shorter reaction time, than that attainable by the afore-mentioned processes.
  • the yield of the desired aromatic urethane is enhanced. The yield based on the starting aromatic nitro compound can even reach a substantially theoretical level depending on the amount of the aforesaid compound or compounds added to the reaction system.
  • reaction rate is further increased without reducing the yield of the desired product.
  • the aromatic nitro compounds useful as the main starting material in the process of the invention are those represented by the formula where A and x have the same meanings as defined in formula (V), and may be mononitro and polynitro compounds. They include, for example, nitrobenzene, dinitrobenzenes, dinitrotoluenes, nitronaphthalenes, nitroanthracenes, nitrobiphenyls,bis(nitrophenyl)alkanes, bis(nitrophenyl)-ethers, bis(nitrophenyl)thioethers, bis(nitrophenyl)sulfones, nitrodiphenoxyalkanes, nitrophenothiazines, and heterocyclic compounds such as 5-nitropyrimidine.
  • nitro compounds are nitrobenzene, o-, m-, and p-nitrotoluenes, o-nitro-p-xylene, 1-nitronaphthalene, m- and p-dinitrobenzenes, 2,4- and 2,6-dinitrotoluenes, dinitromesitylene, 4,4'-dinitrobiphenyl, 2,4-dinitrobiphenyl, 4,4'-dinitrodibenzyl, bis(4-nitrophenyl)methane, bis(4-nitrophenyl)ether, bis (2,4-dinitrophenyl)ether, bis (4-nitrophenyl)thioether, bis(4-nitrophenyl)sulfone, bis(4-nitrophenoxy)ethane, ⁇ , ⁇ ',-dinitro-p-xylene, oC, ⁇ '-dinitro-m-xylene, 2,4,6-trinitrotoluene, o-,
  • aromatic nitro compounds mononitro compounds such as nitrobenzene, o-, m- and p-chloronitrobenzenes, 2,3- and 3,4-dichloronitrobenzenes, etc. and dinitro compounds such as m- and p-dinitrobenzenes, 2,4- and 2,6-dinitrotoluenes, 1,5-dinitronaphthalene, etc. are preferred because they can be readily reacted with other reactants to give high yields of desired products which have wide applications in the manufacture of drugs, agricultural chemicals, polyurethanes, and the like.
  • hydroxyl-containing compounds useful in the process of the invention are those represented by the formula ! where R 1 has the same meanings as defined in formula (VI), and n is an integer equal to or greater than 1 and preferably in the range of from 1 to 3. They include monohydric and polyhydric alcohols having one or more hydroxyl groups attach to primary, secondary or tertiary carbon atoms, as well as monohydric and polyhydric phenols.
  • suitable alcohols are monohydric alcohols such as methyl alcohol, ethyl alcohol, n- and iso-propyl alcohols, n-, iso- and t-butyl alcohols, linear or branched amyl alcohol, hexyl alcohol, cyclohexyl alcohol, lauryl alcohol, cetyl alcohol, benzyl alcohol, chlorobenzyl alcohol, methoxybenzyl alcohol, etc.; dihydric alcohols such as ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, etc.; trihydric alcohols such as glycerol, hexanetriol, etc.; and further polyhydric alcohols.
  • monohydric alcohols such as methyl alcohol, ethyl alcohol, n- and iso-propyl alcohols, n-, iso- and t-butyl alcohols, linear or branched amyl alcohol, hexyl alcohol, cyclohexyl alcohol, lau
  • Suitable phenols are phenol, chlorophenol, cresol, ethylphenol, linear or branched propylphenol, butyl- and higher alkylphenols, catechol, resorcinol, 4,4'-dihydroxy-diphenylmethane, 2,2'-isopropylidenediphenol, anthranol, phenanthrol, pyrogallol, phloroglucinol, etc.
  • methyl alcohol, ethyl alcohol, and isobutyl alcohol are preferred because they'give higher yields of desired products at a higher reaction rate as compared with other hydroxyl-containing compounds.
  • the catalysts useful in the process of the invention include, for example, elemental palladium, rhodium and ruthenium; the halides, cyanides, thiocyanides, isocyan- ides, oxides, sulfates, nitrates and carbonyl compounds of these metals; the addition products or complexes of these compounds with tertiary amines such as triethylamine, pyridine, isoquinoline, etc. and the complexes of these compounds with organic phosphorus compounds such as triphenylphosphine, etc.; and mixtures of the foregoing.
  • These catalysts may be used either by adding them directly to the reaction syst,'m or by associating them with carriers such as alumina, silica, carbon, barium sulfate, calcium carbonate, asbestos, bentonite, diatomaceous earth, fullers's earth, organic ion exchange resins, inorganic ion exchange resins, magnesium silicate, aluminum silicate, molecular sieve, and the like and then adding them to the reaction system.
  • carriers may be added to the reaction system separately from the catalysts including elemental palladium, rhodium and ruthenium as well as compounds thereof.
  • elemental palladium and palladium compounds are preferrred. Specific examples are elemental palladium, palladium chloride, plalladium bromide, and elemental palladium associated with a carrier such as carbon or alumina.
  • the Lewis acids useful as the promoter in the process of the invention are, for example, those described in Jack Hine: “Physical Organic Chemistry” (McGra.w-Hill Book Co., New York, 1962) and imply Br ⁇ nsted acius. They include, for example, the halides, sulfates, acetates, phosphates, and nitrates of metals such as tin, titanium, germanium, aluminum, iron, nickel, zinc, cobalt, manganese, thallium, zirconium, copper, lead, vanadium, niobium, tantalum, mercury, etc.
  • Lewis acids are ferric chloride, ferrous chloride, stannic chloride, stannous chloride, aluminum chloride, cupric chloride, cuprous chloride, copper acetate, etc.
  • Lewis-acid-containing compounds and mixtures of Lewis acids and Lewis acid-containing compounds are also useful as the promoter in the process of the invention.
  • the aforesaid Lewis acid-containing compounds include, for example, complexes derived from Lewis acids and tertiary amines.
  • Specific examples of the complex-forming tertiary amines are triethylamine, N,N-diethylaniline, N,N-diethylcyclohexylamine, 1,4-diazabicyclo[2,2,2]octane, pyridine, picoline, isoquinoline, quinoline, etc.
  • nitrogen-containing heterocyclic compounds such as pyridine, picoline and isoquinoline are preferred.
  • the use of a complex derived from such a nitrogen-containing heterocyclic compound and a Lewis acid prevents the corrosion of the reactor by the Lewis acid, enhances the yield of the desired. product, and facilitates recovery of the catalyst, as compared with the use of the Lewis acid alone.
  • complexes derived from Lewis acids and organic phosphorus compounds are alo useful.
  • suitable organic phosphorus compounds are phosphines such as triphenylphosphine, dimethylphenylphosphine, bis-àiple- nylphosphinoethane, etc.
  • the components of such a complex may be added to the reaction system separately from each other, though the use of a previously formed complex is more effective.
  • the reaction rate is further increased by adding a small amount of water to the reaction system.
  • the amount of water added should be from 1 to 70 moles and preferably from 10 to 50 moles per mole of the starting aromatic nitro compound. If the amount is less than 1 mole, the addition of water will be virtually ineffective, while if the amount is more than 70 moles, the yield of the desired product will be greatly reduced.
  • the organic primary amino compounds useful in the process of the invention include, for example methylamine, ethylamine, propylamine, butylamine, pentylamine, hexylamine, ethylenediamine, propylenediamine, butylenediamine, hexanediamine, cyclohexylamine, cyclohexaldiamine, aniline, o-, m- and p-diaminobenzenes, 2-amino-4-carbamatetoluene, 4-amino-2-carbamatetoluene, 2-amino-6-carbamatetoluene, o-, m- and p-nitroanilines, 4-nitro-2-aminotoluene, 2-nitro-4-aminotoluene, 2-nitro-6-aminotoluene, 3-nitro-4-aminotoluene,4-nitro-3-aminotoluene, 2-nitro-3-aminoto- luene
  • aromatic amino coumpounds those which can be derived from the starting aromatic nitro compound are preferred.
  • nitrobenzene is used as the starting aromatic nitro compound
  • aniline is preferred.
  • 2-amino-4-nitrotoluene, 4-amino-2-nitrotoluene, 2-amino-4-carbamatetoluene, 4-amino-2-carbamatetoluene, and 2,4-diaminotoluene are preferably used when the starting aromatic nitro compound is 2,4-dinitrotoluene
  • 2-amino-6-nitrotoluene, 2-amini-6-carbamatetoluene, and 2,6-diaminotoluene are preferably used when the starting aromatic nitro compound is 2,6-dinitrotoluene.
  • urea compounds, biuret compounds, and allophanate compounds useful in the process of the invention are those represented by the respecti.ve formulae (VIII), (IX) and (X) in which, for example, A' is a phenyl group when the starting aromatic nitro compound is nitrobenzene or a tolyl group having a nitro, amino or carbamate.group when the starting aromatic nitro compound is dinitrotoluene.
  • Suitable solvents include, for example, aromatic solvents such as benzene, toluene, xylene, etc.; nitriles such as acetonitrile, benzonitrile, etc.; sulfones such as sulfolane, etc.; halogenated aliphatic hydrocarbons such as 1,1,2-trichloro-1,2,2-trifluoroethane, etc.; halogenated aromatic hydrocarbons such as monochlorobenzene, dichlorobenzene, trichlorobenzene, etc.; ketones; estes; and other solvents such as tetrahydrofuran, 1,4-dioxane, 1,2-dimethoxyethane, etc.
  • aromatic solvents such as benzene, toluene, xylene, etc.
  • nitriles such as acetonitrile, benzonitrile, etc.
  • sulfones such as sulfolane
  • the hydroxyl-containing compound and carbon monoxide are preferably used in amounts equal to at least 1 mole per mole of the nitro group of the starting aromatic nitro compound.
  • the amount of platinum metal or platinum metal compound used as the catalyst may vary widely according to the type thereof and other reaction conditions. However, on a weight basis, the amount of catalyst is generally in the range of from 1 X 10 -5 to 1 part, and preferably from 1 X 10 -4 to 5 X 10 -1 part, per part of the starting aromatic nitro compound when expressed in terms of its metallic component.
  • the amount of Lewis acid used as the promoter is generally in the range of from 2 X 10 -3 to 2 parts, and preferably from 5 X 10 -2 to 1 part, per part of the starting aromatic nitro compound.
  • the reaction temperature is generally held in the range of from 80° to 230°C, and preferably from 140° to 200°C.
  • the reaction pressure is generally in the range of from 10 to 1,000 kg/cm 2 G, and preferably from 30 to 500 kg/cm 2 G.
  • the reaction time depends on the nature of aromatic nitro compound used, the reaction temperature, the reaction pressure, the type and'amount of catalyst used, the type and amount of organic primary amino compound, urea compound, biuret compound, or allophanate compound added, the type of reactor employed, and the like, but is generally in the range of from 5 minutes to 6 hours.
  • the reaction mixture is cooled and the gas is discharged from the reactor.
  • the reaction mixture is subjected to any conventional procedure including filtration, distillation, or other suitable separation steps, whereby the resulting urethane is separated from any unreacted materials, any by-products, the solvent, the catalyst, and the like.
  • the urethanes prepared by the process of the invention have wide applications in the manufacture of agricultural chemicals, isocyanates, and polyurethanes.
  • Example 2 The procedure of Example 1 was repeated except that the aniline was replaced by 0.7 g of diphenylurea (Example 2). In addition, the procedure of Example 1 was repeated except that the aniline was omitted (Control 1). The results of Example 2 and Control 1, together with those of Example 1, are summarized in Table 1 below.
  • Example 3 The procedure of Example 3 was repeated except that the isopropylamine was replaced by a variety of primary amino compounds and urea compounds (Examples 4 - 11). In addition, the procedure of Example 3 was repeated except that the isopropylamine was omitted (Control 2). The results of Examples 4 - 11 and Control 2 are summarized in Table 2 below.
  • Example 3 The procedure of Example 3 was repeated except that the ethanol was replaced by 68 ml of isobutanol and the isopropylamine was replaced by 0.8 g of 2-amino-4-isobutyl- carbamatetoluene and 0.8 g of 4-amino-2-isobutylcarbama- tetoluene. After 160 minutes of reaction, the yield of diurethane was 99 %.
  • Example 13 The procedure of Example 13 was repeated except that the aminoethylcarbamatetoluenes were omitted. The reaction was carried out for the same period of time, or 120 minutes, as in Example 13. Analysis of the resulting solution revealed that the starting 2,4-dinitrotoluene was absent but the yield of mononitromonourethane was 15 % and that of diurethane was 80 %.
  • Example 14 The procedure of Example 14 was repeated except that the allophanate compound was replaced by 1.4 g of a biuret compound (formed by heating a mixture of 2,4-toluene diisocyanate and water). The absorption of carbon monoxide ceased in 120 minutes. Analysis of the resulting solution revealed that the yield of diurethane was 97 %.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
EP78100468A 1977-07-25 1978-07-21 Procédé de préparation d'uréthanes aromatiques Expired EP0000563B1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP8844177A JPS5424853A (en) 1977-07-25 1977-07-25 Preparation of aromatic urethane compound
JP88441/77 1977-07-25
JP89805/77 1977-07-28
JP8980577A JPS5424854A (en) 1977-07-28 1977-07-28 Preparation of aromatic urethane compound

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EP0000563A1 true EP0000563A1 (fr) 1979-02-07
EP0000563B1 EP0000563B1 (fr) 1982-05-12

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US (1) US4178455A (fr)
EP (1) EP0000563B1 (fr)
DE (1) DE2861807D1 (fr)
IT (1) IT1097336B (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0010585A1 (fr) * 1978-09-06 1980-05-14 Bayer Ag Procédé de préparation d'uréthanes
EP0014845A1 (fr) * 1979-02-02 1980-09-03 Bayer Ag Procédé de préparation d'uréthanes
EP0016948A1 (fr) * 1979-03-02 1980-10-15 Bayer Ag Procédé de préparation d'uréthanes

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4258201A (en) * 1979-01-29 1981-03-24 Halcon Research And Development Corp. Process for the manufacture of carbamates
DE2908251A1 (de) * 1979-03-02 1980-09-11 Bayer Ag Verfahren zur herstellung von urethanen
DE2908252A1 (de) * 1979-03-02 1980-09-11 Bayer Ag Verfahren zur herstellung von urethanen
US4260781A (en) * 1979-05-25 1981-04-07 Halcon Research And Development Corp. Process for the manufacture of carbamates
US4266070A (en) * 1979-05-25 1981-05-05 Halcon Research And Development Corp. Catalytic process for the manufacture of urethanes
US4621149A (en) * 1981-12-25 1986-11-04 Asahi Kasei Kogyo Kabushiki Kaisha Production of urethane compounds
US4709073A (en) * 1985-06-17 1987-11-24 Catalytica Associates Process for the preparation of urethanes
KR890005036B1 (ko) * 1985-09-04 1989-12-08 니홍 고강 가부시기가이샤 방향족 우레탄 및 그 중간생성물의 제조방법
US4876379A (en) * 1987-09-21 1989-10-24 Amoco Corporation Oxidative alkoxycarbonylation of amines and amine derivatives
DE68912856T2 (de) * 1988-09-13 1994-06-16 Babcock Hitachi Kk Verfahren zur Herstellung von Carbamidsäureestern.
US5130464A (en) * 1989-05-31 1992-07-14 Nkk Corporation Method of manufacturing aromatic urethanes
PL164286B1 (pl) * 1990-10-08 1994-07-29 Inst Chemii Przemyslowej Sposób wytwarzania estrów kwasu N-fenylokarbaminowego PL
US5578652A (en) * 1995-02-17 1996-11-26 Exxon Chemical Patents, Inc. Method of producing rigid foams and products produced therefrom
US5866626A (en) * 1995-07-03 1999-02-02 Exxon Chemical Patents Inc. Method of producing rigid foams and products produced therefrom
US20030158277A1 (en) * 1995-07-03 2003-08-21 Blanpied Robert H. Method of producing rigid foams and products produced therefrom
US6306919B1 (en) 1995-07-03 2001-10-23 Exxonmobil Chemical Patents, Inc. Thermosetting plastic foam
KR100239678B1 (ko) * 1997-05-13 2000-01-15 박호군 카바메이트류의 제조방법
US6748995B2 (en) * 2000-08-24 2004-06-15 Radio Frequency Services, Inc. Apparatus and method for manufacturing panels from wood pieces
CN102952022B (zh) * 2012-09-13 2014-04-09 赛鼎工程有限公司 二硝基甲苯连续制备二胺基甲苯的方法及使用的催化剂和催化剂的制备方法

Citations (1)

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Publication number Priority date Publication date Assignee Title
FR2314916A1 (fr) * 1975-06-17 1977-01-14 Mitsui Toatsu Chemicals Procede de preparation d'urethannes aromatiques

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GB1087896A (en) * 1965-07-06 1967-10-18 Ici Ltd Process for the manufacture of urethanes
US3956360A (en) * 1973-06-21 1976-05-11 Atlantic Richfield Company Process for the manufacture of urethanes
US3993685A (en) * 1974-10-21 1976-11-23 Atlantic Richfield Company Process for the production of urethanes

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2314916A1 (fr) * 1975-06-17 1977-01-14 Mitsui Toatsu Chemicals Procede de preparation d'urethannes aromatiques

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0010585A1 (fr) * 1978-09-06 1980-05-14 Bayer Ag Procédé de préparation d'uréthanes
EP0014845A1 (fr) * 1979-02-02 1980-09-03 Bayer Ag Procédé de préparation d'uréthanes
EP0016948A1 (fr) * 1979-03-02 1980-10-15 Bayer Ag Procédé de préparation d'uréthanes

Also Published As

Publication number Publication date
US4178455A (en) 1979-12-11
DE2861807D1 (en) 1982-07-01
IT1097336B (it) 1985-08-31
EP0000563B1 (fr) 1982-05-12
IT7826046A0 (it) 1978-07-24

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