DE1275041B - Process for the preparation of ª ‡ -hydroxyisopropylbenzenes - Google Patents
Process for the preparation of ª ‡ -hydroxyisopropylbenzenesInfo
- Publication number
- DE1275041B DE1275041B DEB85587A DEB0085587A DE1275041B DE 1275041 B DE1275041 B DE 1275041B DE B85587 A DEB85587 A DE B85587A DE B0085587 A DEB0085587 A DE B0085587A DE 1275041 B DE1275041 B DE 1275041B
- Authority
- DE
- Germany
- Prior art keywords
- parts
- diisopropylbenzene
- water
- benzene
- theory
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims description 10
- 238000002360 preparation method Methods 0.000 title claims 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 6
- KPJKMUJJFXZGAX-UHFFFAOYSA-N 2-chloropropan-2-ylbenzene Chemical compound CC(C)(Cl)C1=CC=CC=C1 KPJKMUJJFXZGAX-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 238000005660 chlorination reaction Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000007858 starting material Substances 0.000 claims description 3
- OKIRBHVFJGXOIS-UHFFFAOYSA-N 1,2-di(propan-2-yl)benzene Chemical compound CC(C)C1=CC=CC=C1C(C)C OKIRBHVFJGXOIS-UHFFFAOYSA-N 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims 6
- ODLMAHJVESYWTB-UHFFFAOYSA-N propylbenzene Chemical class CCCC1=CC=CC=C1 ODLMAHJVESYWTB-UHFFFAOYSA-N 0.000 claims 5
- 238000002844 melting Methods 0.000 claims 4
- 230000008018 melting Effects 0.000 claims 4
- 239000000047 product Substances 0.000 claims 4
- 238000003756 stirring Methods 0.000 claims 4
- 239000012043 crude product Substances 0.000 claims 3
- 239000000203 mixture Substances 0.000 claims 3
- SPPWGCYEYAMHDT-UHFFFAOYSA-N 1,4-di(propan-2-yl)benzene Chemical compound CC(C)C1=CC=C(C(C)C)C=C1 SPPWGCYEYAMHDT-UHFFFAOYSA-N 0.000 claims 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims 2
- -1 chlorine-1,3-diisopropylbenzene Chemical compound 0.000 claims 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 claims 2
- 239000005457 ice water Substances 0.000 claims 2
- 239000012452 mother liquor Substances 0.000 claims 2
- HIACAHMKXQESOV-UHFFFAOYSA-N 1,2-bis(prop-1-en-2-yl)benzene Chemical compound CC(=C)C1=CC=CC=C1C(C)=C HIACAHMKXQESOV-UHFFFAOYSA-N 0.000 claims 1
- UNEATYXSUBPPKP-UHFFFAOYSA-N 1,3-Diisopropylbenzene Chemical compound CC(C)C1=CC=CC(C(C)C)=C1 UNEATYXSUBPPKP-UHFFFAOYSA-N 0.000 claims 1
- VFNUNYPYULIJSN-UHFFFAOYSA-N 2,5-diisopropylphenol Chemical compound CC(C)C1=CC=C(C(C)C)C(O)=C1 VFNUNYPYULIJSN-UHFFFAOYSA-N 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims 1
- 241000282326 Felis catus Species 0.000 claims 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims 1
- 239000000460 chlorine Substances 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 239000013078 crystal Substances 0.000 claims 1
- 238000002425 crystallisation Methods 0.000 claims 1
- 230000008025 crystallization Effects 0.000 claims 1
- 238000004821 distillation Methods 0.000 claims 1
- 239000000706 filtrate Substances 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims 1
- 125000000325 methylidene group Chemical group [H]C([H])=* 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 239000002244 precipitate Substances 0.000 claims 1
- 230000001376 precipitating effect Effects 0.000 claims 1
- OLBCVFGFOZPWHH-UHFFFAOYSA-N propofol Chemical compound CC(C)C1=CC=CC(C(C)C)=C1O OLBCVFGFOZPWHH-UHFFFAOYSA-N 0.000 claims 1
- 238000000746 purification Methods 0.000 claims 1
- 238000001953 recrystallisation Methods 0.000 claims 1
- 238000007127 saponification reaction Methods 0.000 claims 1
- 239000002002 slurry Substances 0.000 claims 1
- 229910052938 sodium sulfate Inorganic materials 0.000 claims 1
- 235000011152 sodium sulphate Nutrition 0.000 claims 1
- BDCFWIDZNLCTMF-UHFFFAOYSA-N 2-phenylpropan-2-ol Chemical class CC(C)(O)C1=CC=CC=C1 BDCFWIDZNLCTMF-UHFFFAOYSA-N 0.000 description 3
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 150000001555 benzenes Chemical class 0.000 description 3
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical class CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical class CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- JLXSXLCMZQZKCS-UHFFFAOYSA-N 1-(2-chloropropan-2-yl)-3-propan-2-ylbenzene Chemical compound C(C)(C)C=1C=C(C=CC=1)C(C)(C)Cl JLXSXLCMZQZKCS-UHFFFAOYSA-N 0.000 description 1
- ITTZHNHXCRWVKL-UHFFFAOYSA-N 1-(2-chloropropan-2-yl)-4-methylbenzene Chemical compound CC1=CC=C(C(C)(C)Cl)C=C1 ITTZHNHXCRWVKL-UHFFFAOYSA-N 0.000 description 1
- UTCICDAGNWZQJO-UHFFFAOYSA-N CCC1=CC(CC)=C(C(C)(C)Cl)C=C1CC Chemical compound CCC1=CC(CC)=C(C(C)(C)Cl)C=C1CC UTCICDAGNWZQJO-UHFFFAOYSA-N 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 239000011260 aqueous acid Substances 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical class OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 150000004292 cyclic ethers Chemical class 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002432 hydroperoxides Chemical class 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- NXPHGHWWQRMDIA-UHFFFAOYSA-M magnesium;carbanide;bromide Chemical compound [CH3-].[Mg+2].[Br-] NXPHGHWWQRMDIA-UHFFFAOYSA-M 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 239000003799 water insoluble solvent Substances 0.000 description 1
- 239000003021 water soluble solvent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C22/00—Cyclic compounds containing halogen atoms bound to an acyclic carbon atom
- C07C22/02—Cyclic compounds containing halogen atoms bound to an acyclic carbon atom having unsaturation in the rings
- C07C22/04—Cyclic compounds containing halogen atoms bound to an acyclic carbon atom having unsaturation in the rings containing six-membered aromatic rings
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
DEUTSCHESGERMAN
PATENTAMTPATENT OFFICE
Int. CL:Int. CL:
Deutsche Kl.:German class:
Nummer:
Aktenzeichen:
Anmeldetag:
Auslegetag:Number:
File number:
Registration date:
Display day:
C07cC07c
12 ο-S/02
12 ο-2/0112 ο-S / 02
12 ο-2/01
P 12 75 041.3-42 (B 85587)P 12 75 041.3-42 (B 85587)
28. Januar 1966January 28, 1966
14. August 1968August 14, 1968
Es ist bekannt, daß a-Hydroxyisopropylbenzole durch Luftoxydation von Isopropylbenzolen über Hydroperoxyd-Zwischenstufen hergestellt werden können. Hierbei müssen jedoch entweder die nicht ungefährlichen Hydroperoxyde isoliert werden, oder aber das Verfahren liefert nur mäßige Ausbeuten. Zudem sind die erhaltenen Produkte unrein.It is known that α-Hydroxyisopropylbenzenes can be produced by air oxidation of isopropylbenzenes via hydroperoxide intermediates. Here, however, either the not harmless hydroperoxides have to be isolated, or else the process gives only moderate yields. In addition, the products obtained are impure.
Weiterhin ist aus dem »Journal of the General Chemistry of the USSR«, englische Ausgabe, Bd. 28 (1958), S. 3228 ff., bekannt, Umsetzung von Benzolcarbonsäureestern mit Methylmagnesiumbromid darzustellen. Dieses Verfahren hat jedoch nur wissenschaftliches Interesse.Furthermore, from the "Journal of the General Chemistry of the USSR", English edition, vol. 28 (1958), p. 3228 ff., Known to represent the reaction of benzene carboxylic acid esters with methylmagnesium bromide. However, this method is only of scientific interest.
Es wurde nun gefunden, daß man in eleganter Weise a-Hydroxyisopropylbenzole durch Hydrolyse von a-ChlorisopropylbenzoIen erhält, wenn man a-Chlorisopropylbenzole mit der mehr als 0,5fachen Gewichtsmenge Wasser bei Temperaturen unterhalb von +40° C umsetzt.It has now been found that one can elegantly a-Hydroxyisopropylbenzenes by hydrolysis of α-Chloroisopropylbenzenes are obtained when α-chloroisopropylbenzenes are used with more than 0.5 times the weight of water at temperatures below + 40 ° C implements.
Es ist überraschend, daß nach dem neuen Verfahren ausgezeichnete Ausbeuten erhalten werden, da sich bekanntlich «-Chlorisopropylbenzole leicht unter Abspaltung von Chlorwasserstoff zu Isopropenylbenzolen und deren niedermolekularen Polymeren zersetzen.It is surprising that excellent yields are obtained with the new process, since as is known, -chloroisopropylbenzenes readily form isopropenylbenzenes with elimination of hydrogen chloride and decompose their low molecular weight polymers.
Geeignete «-Chlorisopropylbenzole sind beispielsweise a-ChlorisopropylbenzoI und «-Chlorisopropylbenzol, das am Benzolkern einen oder mehrere Alkylsubstituenten trägt, insbesondere Alkylgruppen mit 1 bis 4 Kohlenstoffatomen, wie in den Verbindungen p-Methyl-a-chlorisopropylbenzol, m-Isopropyl-a-chlorisopropylbenzol und 2,4,5-Triäthyl-a-chlorisopropylbenzol. Insbesondere sind Di-(<x-chlorisopropyl)-benzole verwendbar, wie o-, m- und vorzugsweise p-Di-(«- chlorisopr opyl) - benzol, κ - Chlorisopropylbenzole sind durch Chlorierung von Isopropylbenzolen, beispielsweise nach der in der deutschen Patentschrift 1 022 203 beschriebenen Weise, bequem zugänglich. Die Herstellung von Di-(«-chlorisopropyl)-benzolen erfolgt in analoger Weise durch Chlorierung von Diisopropylbenzolen bei Temperaturen von —10 bis +4O0C, vorzugsweise —5 bis +150C, unter Belichtung mit sichtbarem oder UV-Licht, wobei man zweckmäßig in Abwesenheit von Lösungsmitteln arbeitet. Die derart erhältlichen Produkte sind sehr rein und liefern bei der Umsetzung nach dem vorliegenden Verfahren besonders hohe Ausbeuten.Suitable -chloroisopropylbenzenes are, for example, α-chloroisopropylbenzene and -chloroisopropylbenzene, which has one or more alkyl substituents on the benzene nucleus, in particular alkyl groups with 1 to 4 carbon atoms, such as in the compounds p-methyl-α-chloroisopropylbenzene, m-isopropyl-α-chloroisopropylbenzene and 2,4,5-triethyl-α-chloroisopropylbenzene. In particular, di- (<x -chloroisopropyl) benzenes can be used, such as o-, m- and preferably p-di - («- chloroisopropyl) benzene, κ - chloroisopropylbenzenes are obtained by chlorination of isopropylbenzenes, for example according to the German Patent specification 1 022 203 described manner, easily accessible. The production of di - ( «- chloroisopropyl) benzenes is carried out in an analogous manner by chlorination of diisopropylbenzenes at temperatures of -10 to + 4O 0 C, preferably -5 to +15 0 C, under exposure to visible or UV light, wherein it is expedient to work in the absence of solvents. The products obtainable in this way are very pure and give particularly high yields when converted by the present process.
Man verwendet Wasser in der mehr als 0,5fachen, vorzugsweise in der 1- bis 20fachen, insbesondere in
der 1- bis 5fachen Gewichtsmenge, bezogen auf den Ausgangsstoff. Bei Verwendung von geringeren Mengen
verläuft die Umsetzung unvollständig. Sehr hohe Wassermengen bringen keine weiteren Vorteile mehr,
Verfahren zur Herstellung von
a-HydroxyisopropylbenzolenWater is used in more than 0.5 times, preferably 1 to 20 times, in particular 1 to 5 times, by weight, based on the starting material. If smaller amounts are used, the reaction is incomplete. Very high amounts of water no longer bring any further advantages. Process for the production of
α-hydroxyisopropylbenzenes
Anmelder:Applicant:
Badische Anilin- & Soda-Fabrik
Aktiengesellschaft, 6700 LudwigshafenAniline & Soda Factory in Baden
Aktiengesellschaft, 6700 Ludwigshafen
Als Erfinder benannt:Named as inventor:
Dr. Franz Reicheneder,Dr. Franz Reicheneder,
Dr. Hugo Fuchs,Dr. Hugo Fuchs,
Dr. Georg Krusche, 6700 LudwigshafenDr. Georg Krusche, 6700 Ludwigshafen, Germany
insbesondere ist dann die Aufarbeitung der anfallendenin particular then is the processing of the accumulating
ao Salzsäurelösung nicht mehr lohnend. Für das Gelingen des Verfahrens ist ein intensives Durchmischen der beiden Phasen von Bedeutung. Zweckmäßig setzt man in geringer Menge handelsübliche, gegen verdünnte wäßrige Säuren stabile Emulgatoren zu, oder aberao hydrochloric acid solution no longer worthwhile. Intensive mixing of the important in both phases. It is advisable to use small amounts of commercially available versus diluted ones aqueous acids to stable emulsifiers, or else
»5 man arbeitet unter Zusatz von wasserlöslichen organischen Lösungsmitteln, die die Löslichkeit des a-Chlorisopropylbenzols in der wäßrigen Phase erhöhen. Geeignete wasserlösliche Lösungsmittel sind beispielsweise niedere Alkohole, Ketone, cyclische Äther, Nitrile, Säureamide oder Sülfoxyde. Beispielsweise seien genannt Methanol, Äthanol, Isopropanol, Aceton, Butanon, Tetrahydrofuran, Dioxan, Acetonitril, Form*· amid, Dimethylformamid, Pyrrolidon und Dimethylsulfoxyd. Man verwendet das Lösungsmittel im allgemeinen in der 0,5- bis 5fachen Gewichtsmenge, bezogen auf Wasser.»5 one works with the addition of water-soluble organic substances Solvents that reduce the solubility of α-chloroisopropylbenzene increase in the aqueous phase. Suitable water-soluble solvents are, for example lower alcohols, ketones, cyclic ethers, nitriles, acid amides or sulphate oxides. For example methanol, ethanol, isopropanol, acetone, butanone, tetrahydrofuran, dioxane, acetonitrile, form * amide, dimethylformamide, pyrrolidone and dimethyl sulfoxide. The solvent is generally used in 0.5 to 5 times the amount by weight, based on water.
Die Umsetzung wird bei einer Temperatur unterhalb von +4O0C durchgeführt, vorteilhaft bei —10 bis +3O0C, insbesondere bei 0 bis 25°C. Bei tieferen Temperaturen ist die Reaktionsgeschwindigkeit sehr gering, bei höheren Temperaturen isoliert man an Stelle der a-Hydroxyisopropylbenzole in zunehmendem Maße Isopropenylbenzole bzw. deren niedermolekulare Polymere.The reaction is carried out at a temperature below + 4O 0 C, advantageously at -10 to + 3O 0 C, in particular at 0 to 25 ° C. At lower temperatures, the reaction rate is very slow; at higher temperatures, isopropenylbenzenes or their low molecular weight polymers are increasingly isolated in place of the α-hydroxyisopropylbenzenes.
Zur Durchführung des Verfahrens werden, beispielsweise in einem Rührgefäß, das a-Chlorisopropylbenzol, Wasser und gegebenenfalls das Lösungsmittel einige Zeit, beispielsweise 10 Minuten bis 24 Stunden, bei Reaktionstemperatur durchmischt. Die organische Phase wird abgetrennt. In der wäßrigen Phase gelöste Reste können beispielsweise durch Extraktion mit einem wasserunlöslichen Lösungsmittel isoliert werden.To carry out the method, for example in a stirred vessel, the a-chloroisopropylbenzene, Water and optionally the solvent for some time, for example 10 minutes to 24 hours, mixed at reaction temperature. The organic phase is separated off. Dissolved in the aqueous phase Residues can be isolated, for example, by extraction with a water-insoluble solvent.
809 590/459809 590/459
Claims (1)
so oft wiederholt, bis das eingesetzte 1,4-Diisopropyl- y a UV lamp type »Osram 125 W HQA« irradiated. 70 parts of α-chloroisopropylbenzene are passed into a chlorine gas, diluted with about the 20 mixture of 80 parts of acetone and 80 parts of water, 2 to 5 times the amount of nitrogen, introduced through the 1,4-diiso. After stirring for 4 hours at 0 to 5 ° C propylbenzene. The internal temperature is taken up in methylene chloride and dried at about 0 to + 5 ° C kept. The chlorination is so long sodium sulfate. After removing the solution, continue until a crystal slurry has formed, which is distilled by means of "the residue is just left to mix in the oil pump. Then vacuum. 55 parts of α-hydroxyisopropyl are obtained from the 1,4-di- (" chloro- benzene, bp. Oil = 63 0 C (melting point = 21 ° C, isopropyl) benzene, and sets the mother liquor to nff = 1.5240). the yield is 89% of theory, further chlorination again. This Process becomes analvse
repeated until the 1,4-diisopropyl- y used
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB85587A DE1275041B (en) | 1966-01-28 | 1966-01-28 | Process for the preparation of ª ‡ -hydroxyisopropylbenzenes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEB85587A DE1275041B (en) | 1966-01-28 | 1966-01-28 | Process for the preparation of ª ‡ -hydroxyisopropylbenzenes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE1275041B true DE1275041B (en) | 1968-08-14 |
Family
ID=6982984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEB85587A Pending DE1275041B (en) | 1966-01-28 | 1966-01-28 | Process for the preparation of ª ‡ -hydroxyisopropylbenzenes |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE1275041B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4410734A (en) * | 1980-01-16 | 1983-10-18 | Basf Aktiengesellschaft | Optically active phenylpropane derivatives, their preparation and their use for the preparation of fungicides |
| US4486612A (en) * | 1983-03-23 | 1984-12-04 | The Dow Chemical Company | Method of preparing tertiary carbinols |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE439797A (en) * | ||||
| FR861835A (en) * | 1939-08-09 | 1941-02-18 | Belge Produits Chimiques Sa | Process for the preparation of mono or polyvalent alcohols |
| US2819319A (en) * | 1954-08-13 | 1958-01-07 | Pan American Petroleum Corp | Production of alcohols by hydrolysis of alkyl bromides |
-
1966
- 1966-01-28 DE DEB85587A patent/DE1275041B/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE439797A (en) * | ||||
| FR861835A (en) * | 1939-08-09 | 1941-02-18 | Belge Produits Chimiques Sa | Process for the preparation of mono or polyvalent alcohols |
| US2819319A (en) * | 1954-08-13 | 1958-01-07 | Pan American Petroleum Corp | Production of alcohols by hydrolysis of alkyl bromides |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4410734A (en) * | 1980-01-16 | 1983-10-18 | Basf Aktiengesellschaft | Optically active phenylpropane derivatives, their preparation and their use for the preparation of fungicides |
| US4486612A (en) * | 1983-03-23 | 1984-12-04 | The Dow Chemical Company | Method of preparing tertiary carbinols |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE976951C (en) | Process for the production of phenols by incomplete oxidation of benzene derivatives | |
| DE1643347A1 (en) | Process for the production of aromatic lactones | |
| DE1793183B1 (en) | Process for the preparation of trimethyl-p-benzoquinone | |
| DE2526851A1 (en) | METHOD FOR PRODUCING KETOISOPHORONE | |
| DE1275041B (en) | Process for the preparation of ª ‡ -hydroxyisopropylbenzenes | |
| EP0068372B1 (en) | Process for the preparation of 2-alkyl-4,4-diacyloxy-2-butenals | |
| DE1288086B (en) | ||
| DE1168420B (en) | Process for the preparation of isonitroso carbonyl compounds | |
| CH626332A5 (en) | ||
| DE2423316C2 (en) | Process for the production of 4-chloro-5-oxo-hexanoic acid nitrile and 6-chloro-5-oxo-hexanoic acid nitrile | |
| DE2702088A1 (en) | PROCESS FOR AUTOXIDATING A CYCLOAL CANON TO THE CORRESPONDING CYCLOALKANE-1,2-DIONE | |
| EP0663390B1 (en) | Process for the preparation of aromatic amides form aromatic carboxylic acids and urea | |
| DE2115944B2 (en) | PROCESS FOR THE PREPARATION OF O-SULFOBENZIMIDES | |
| DE2162949A1 (en) | Octahydroanthraquinones and tetrahydronaphthoquinones - prepn - from quinhydrone and dienes in diels-alder reaction | |
| AT262954B (en) | Process for the production of ɛ-caprolactone and its alkyl derivatives | |
| DE1568073A1 (en) | Process for the production of isopropenylbenzenes | |
| DE2521479C3 (en) | Process for the preparation of vinyl acetate epoxide | |
| DE900935C (en) | Process for the preparation of 12-bromo-3-acyloxy-5,7,9 (11) -pregnatrien-20-one addition products | |
| DE1643985C3 (en) | S-Isopropyl ^ nitro-phenyl-dimethyl-carbinol and 3,5-diisopropyl-4-nitro-phenyldimethylcarbinol and processes for their preparation | |
| DE2206863A1 (en) | 6-chloroisatoic anhydride prepn - from isatoic anhydride and sulphuryl chloride | |
| AT261572B (en) | Process for the production of ε-caprolactones | |
| DE1470191C (en) | Process for the preparation of 1-formylcolchicine derivatives | |
| DE1238454B (en) | Process for the preparation of carbonyl compounds | |
| DE1168885B (en) | Process for the production of tetrachlorosuccinic acid or its anhydride | |
| DE1915385A1 (en) | Process for the preparation of o-benzoylbenzoic acid |