Oxidation hydrolysis of iodoalkanes

Abstract: A process comprising preparation of an alkanol and elemental iodine by contacting an iodoalkane containing 1 to 20 carbons, water and molecular oxygen at a temperature in the range of 50° to 200°C and recovering the elemental iodine.

Description: This invention relates to the oxidation hydrolysis of iodoalkanes wherein an alkanol and elemental iodine are produced by contacting an iodoalkane, water and molecular oxygen. Since the iodine is in the elemental form, it can be easily recovered. A number of processes have been developed to recover iodine values from inorganic iodide containing compounds. For example, iodine is commercially recovered from deep well brines by chlorine oxidation. Iodine values can also be recovered by oxidation of acidic brines with cupric sulfate or ferric sulfate. Alternatively, electrolysis of ammonium iodide solutions has been disclosed in U.S. 3,975,439. The catalytic oxidation of ammonium iodide solutions by oxygen in the presence of copper catalysts has been disclosed in Japanese Patent Application Kokai No. 73489/1978. More recently, EP 0218998 discloses a process to recover elemental iodine from aqueous sodium iodide or a mixture of iodobenzene and NaI by acidification with carbon dioxide and oxidation with molecular oxygen. These processes do not provide for the recovery of elemental iodine from iodoalkanes or substituted iodoalkanes. U.S. 4,085,200 discloses a process for the thermochemical generation of methane and oxygen from water and carbon dioxide which utilizes as an intermediate step the hydrolysis of iodomethane to methanol, dimethyl ether, and aqueous HI; however, this process does not allow the product of elemental iodine or of an alkanol. Simple hydrolysis of iodoalkanes by water in principle will yield alkanol and aqueous hydriodic acid; however, this does not allow a commercially feasible process because the reaction equilibrium R-I + H₂O ⇆ ROH + HI lies far to the left, limiting the conversion to a few percent. Moreover, recovery of concentrated HI from the dilute aqueous medium is expensive. We have now found that the iodine values in iodoalkanes can be readily recovered in an economic fashion by carrying out a liquid phase oxidative hydrolysis whereby hydrolysis of the iodoalkane is carried out in the presence of molecular oxygen and water at temperatures above 100°C. Under these conditions, the HI liberated by hydrolysis is rapidly oxidized to elemental iodine. The net reaction is therefore R-I + 1/2 H₂O + 1/4 O₂ → ROH + 1/2 I₂. The iodine formed in this process is relatively insoluble in the aqueous medium and can be readily recovered by a variety of processes, including decantation where the iodine is molten, filtration when the iodine is solidified by cooling, or by extraction with a hydrocarbon solvent. The alkanol values can also be removed from the aqueous solution by distillation for low boiling alkanols, such as methanol or ethanol or by extraction for higher boiling, less hydrophilic alkanols. The iodoalkanes which can be employed by this process contain from one to 20 carbon atoms, and include primary, secondary, and tertiary iodoalkanes. Preferably, the iodoalkane is a secondary or primary iodoalkane with one to 5 carbon atoms. Suitable iodoalkanes include iodomethane, iodoethane, 1-iodopropane, 2-iodopropane, 1-iodobutane and 2-iodobutane. More preferably is a primary iodoalkane with one to three carbon atoms, such as iodomethane and iodoethane. The most referred iodoalkane is iodomethane. The reaction will occur at temperatures from 50°C to 250°C. At lower temperatures the reaction rate becomes unacceptably slow, while at the higher temperatures the reaction pressure becomes unacceptably high. Thus practical reaction temperatures are from 100°C to 200°C; preferred temperatures are in the range from 125°C to 175°C. The molecular oxygen can be supplied to the reaction in any convenient form, including air, enriched air, pure oxygen, and depleted air. The pressure of oxygen supplied can be varied from subatmospheric to superatmospheric, but superatmospheric pressures are preferred. Preferred total pressures range from 1 to 105 Kg/cm², with a more preferred range of 7 to 70.3 Kg/cm². The pressure of the reaction must be sufficient such that an aqueous phase is maintained in the reactor. The reaction can be run either continuously or in a batch mode. For large scale operation a continuous mode is preferred, while for small operation a batch mode may be preferable. The reaction time is dependent on the reaction temperature and pressure, but is in general between 10 hours and 10 minutes. Higher temperatures and pressures favor shorter reaction times. In the process of this invention no catalyst is required. This simplifies the process operation since catalyst removal equipment is not required and the additional expense of catalyst is not incurred. EXAMPLES The following examples illustrate the operation of the present invention. In each, the specified reactants were loaded into a 330-mL Hastelloy C ® autoclave and were subjected to the specified reaction conditions and times. The reaction product was then removed and submitted for analyses. All percentages are in weight %. Example 1 100 mL H₂O 10 mL iodomethane 120°C 14.0 Kg/cm² air one hour The reaction consumed all available oxygen. The reaction solution contained 81.82% H₂O, 3.85% methanol, and 12% iodine, and 0.0% iodomethane. In addition, several grams of crystalline iodine were found in the autoclave. Example 2 100 mL H₂O 10 mL iodomethane 150°C 28.1 Kg/cm² air one hour The reaction exhibited a 7 Kg/cm² pressure drop over 30 minutes. The reaction solution contained 89.7% water, 3.71% methanol, 3.78% iodine, and 0.0% iodomethane. In addition 15 grams of crystalline iodine were found in the autoclave. This example exhibits the high reaction rate for the oxidative hydrolysis reaction at 150°C. Example 3 100 mL H₂O 10 mL iodomethane 100°C 28.1 Kg/cm² air one hour The reaction solution contained 95.1% water, 1.15% methanol, 1.1% iodine, and 0.7% iodomethane. In addition, liquid iodomethane was found as a second layer. No crystalline iodine was found. This example exhibits the lower reaction rate for the oxidative hydrolysis reaction at 100°C. Example 4 100 mL H₂O 10 mL iodoethane 120°C 28.1 Kg/cm² air two hours The reaction pressure dropped 6.6 Kg/cm² over a period of one hour. The reaction solution contained 12.3% ethanol, 4.5% diethyl ether, 5.3% iodine, and 76.1% H₂O. In addition, 10.1 grams of crystalline iodine were found in the autoclave. Example 5 100 mL H₂O 10 mL 2-iodopropane 120°C 28.1 Kg/cm² air two hours The reaction pressure dropped 5.3 Kg/cm² over a period of one hour. The reaction solution contained 13.2% 2-propanol, 6.2% iodine, and 78.3% water. In addition, 3.4 grams of crystalline iodine were found in the autoclave.

Claims: A process comprising A. preparation of an alkanol and elemental iodine by contacting an iodoalkane or a substituted iodoalkane containing 1 to 20 carbons, water and molecular oxygen at a temperature in the range of 100° to 200°C, and B. recovering the elemental iodine. The process of Claim 1 wherein the iodoalkane contains 1 to 5 carbons. A process comprising A. preparation of methanol and elemental iodine by contacting iodomethane, water and molecular oxygen at a temperature in the range of 125° to 175°C, and B. recovering the elemental iodine.

Inventors: AGREDA VICTOR HUGH C O EASTMAN, RULE MARK C O EASTMAN KODAK, AGREDA, VICTOR HUGH C/O EASTMAN KODAK, RULE, MARK C/O EASTMAN KODAK
Applicants: EASTMAN KODAK CO, EASTMAN KODAK COMPANY
Application year: 1989
Main classification: C01B7
IPC codes: C01B7, C07C31, C07C29