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Propylene-oxide methylation

Methyloctane. see 4-Methyloctane Methylol. see Methanol Methylolpropane. see 1 -Butanol Methyloxirane. see Propylene oxide Methyl oxitol, see Methyl cellosolve 4-Methyl-2-pentanol acetate, see sec-Hexyl acetate 2-Methyl-2-pentanol-4-one, see Diacetone alcohol... [Pg.1495]

Methyl Methacrylate Propylene Oxide Methyl Parathion Isohexane Hexylene Glycol Methyl Amyl Alcohol Methyl Isobutyl Carbinol Methyl Akyl Acetate... [Pg.65]

PROPYLENE OXIDE Methyl oxirane, Propene oxide, 1,2-Epoxypropane Flammable Liquid, I 2 4 2 ... [Pg.108]

Methyl ethyl carbinol. See 2-Butanol Methylethylcetoxime. See Methyl ethyl ketoxime 1-Methyl ethylene carbonate. See Propylene carbonate Methyl ethylene glycol. See Propylene glycol Methyl ethylene oxide. See Propylene oxide Methyl ethyl glycol. See Propylene glycol 1-Methylethyl hexandecanoate. See Isopropyl palmitate 1-Methylethyl 2-hydroxypropanoate. See Isopropyl lactate 4,4 -(1-Methylethylidene) biscyclohexanol. See Bisphenol A, hydrogenated 4,4 -(1-Methylethylidene) bisphenol. See Bisphenol A 2,2 -((1-Methylethylidene) bis (4,1-phenyleneoxymethylene)) bisoxirane. See Bisphenol A diglycidyl ether... [Pg.1199]

Methyloxacyclopropane. See Propylene oxide Methyl oxide. See Dimethyl ether... [Pg.1204]

Methyloxirane S(-)-Methyloxirane. See Propylene oxide Methyl oxirane polymers. See Poloxamer 101 4-Methyl-y-oxo-benzenebutanoic acid compounded with 4-ethylmorpho-line (2 1). See4-Oxo-4-p-tolylbutyric acid adduct with 4-ethylmorpholine N-Methyl-N-(1-oxo-9-octadecenyl) glycine (Z)-N-Methyl-N-(1-oxo-9-octadecenyl) glycine. See Oleoyl sarcosine 4-Methyl-2-oxopentane. See Methyl isobutyl ketone... [Pg.1204]

Propylene oxide 1,2-epoxypropane, 1, 2-propylene oxide, methyl oxirane, methyl ethylene oxide, propileno oxido (Spanish), oxyde de propylene (French)... [Pg.13]

Hydroxylpropylmethyl Propylene oxide/methyl chloride 1.5-2.0 Sol H2O Paints... [Pg.839]

This oxidation process for olefins has been exploited commercially principally for the production of acetaldehyde, but the reaction can also be apphed to the production of acetone from propylene and methyl ethyl ketone [78-93-3] from butenes (87,88). Careflil control of the potential of the catalyst with the oxygen stream in the regenerator minimises the formation of chloroketones (94). Vinyl acetate can also be produced commercially by a variation of this reaction (96,97). [Pg.52]

Certain bacterial strains convert propylene glycol to pymvic acid in the presence of thiamine (15) other strains do the conversion without thiamine (16). Propylene oxide is the principal product of the reaction of propylene glycol over a cesium impregnated siHca gel at 360°C in the presence of methyl ethyl ketone and xylene (17). [Pg.366]

Isoprene [78-79-5] (2-methyl-1,3-butadiene) is a colorless, volatile Hquid that is soluble in most hydrocarbons but is practically insoluble in water. Isoprene forms binary azeotropes with water, methanol, methylamine, acetonitrile, methyl formate, bromoethane, ethyl alcohol, methyl sulfide, acetone, propylene oxide, ethyl formate, isopropyl nitrate, methyla1 (dimethoxymethane), ethyl ether, and / -pentane. Ternary azeotropes form with water—acetone, water—acetonitrile, and methyl formate—ethyl bromide (8). Typical properties of isoprene are Hsted in Table 1. [Pg.462]

Homopolymers of PO and other epoxides are named a number of ways after the monomer, eg, poly(propylene oxide) (PPO) or polymethjioxirane from a stmctural point of view, polyoxypropylene or poly(propylene glycol) or from the Chemicaly hstracts (CA) name, poly[oxy(methyl-l,2-ethanediyl)], a-hydro- CO-hydroxy-. Common names are used extensively in the Hterature and in this article. [Pg.348]

Propylene oxide is a colorless, low hoiling (34.2°C) liquid. Table 1 lists general physical properties Table 2 provides equations for temperature variation on some thermodynamic functions. Vapor—liquid equilibrium data for binary mixtures of propylene oxide and other chemicals of commercial importance ate available. References for binary mixtures include 1,2-propanediol (14), water (7,8,15), 1,2-dichloropropane [78-87-5] (16), 2-propanol [67-63-0] (17), 2-methyl-2-pentene [625-27-4] (18), methyl formate [107-31-3] (19), acetaldehyde [75-07-0] (17), methanol [67-56-1] (20), ptopanal [123-38-6] (16), 1-phenylethanol [60-12-8] (21), and / /f-butanol [75-65-0] (22,23). [Pg.133]

Trimethyl aluminum and propylene oxide form a mixture of 2-methyl-1-propanol and 2-butanol (105). Triethyl aluminum yields products of 2-methyl-1-butanol and 2-pentanol (106). The ratio of products is determined by the ratio of reactants. Hydrolysis of the products of methyl aluminum dichloride and propylene oxide results ia 2-methylpropeae and 2-butene, with elimination of methane (105). Numerous other nucleophilic (107) and electrophilic (108) reactions of propylene oxide have been described ia the Hterature. [Pg.135]

The hydroperoxide process involves oxidation of propjiene (qv) to propylene oxide by an organic hydroperoxide. An alcohol is produced as a coproduct. Two different hydroperoxides are used commercially that result in / fZ-butanol or 1-phenylethanol as the coproduct. The / fZ-butanol (TBA) has been used as a gasoline additive, dehydrated to isobutjiene, and used as feedstock to produce methyl tert-huty ether (MTBE), a gasoline additive. The 1-phenyl ethanol is dehydrated to styrene. ARCO Chemical has plants producing the TBA coproduct in the United States, Erance, and the Netherlands. Texaco has a TBA coproduct plant in the United States. Styrene coproduct plants are operated by ARCO Chemical in the United States and Japan, Shell in the Netherlands, Repsol in Spain, and Yukong in South Korea. [Pg.136]

Hydroperoxide Process. The hydroperoxide process to propylene oxide involves the basic steps of oxidation of an organic to its hydroperoxide, epoxidation of propylene with the hydroperoxide, purification of the propylene oxide, and conversion of the coproduct alcohol to a useful product for sale. Incorporated into the process are various purification, concentration, and recycle methods to maximize product yields and minimize operating expenses. Commercially, two processes are used. The coproducts are / fZ-butanol, which is converted to methyl tert-huty ether [1634-04-4] (MTBE), and 1-phenyl ethanol, converted to styrene [100-42-5]. The coproducts are produced in a weight ratio of 3—4 1 / fZ-butanol/propylene oxide and 2.4 1 styrene/propylene oxide, respectively. These processes use isobutane (see Hydrocarbons) and ethylbenzene (qv), respectively, to produce the hydroperoxide. Other processes have been proposed based on cyclohexane where aniline is the final coproduct, or on cumene (qv) where a-methyl styrene is the final coproduct. [Pg.138]

Methyl formate and propylene oxide have close boiling poiats, making separation by distillation difficult. Methyl formate is removed from propylene oxide by hydrolysis with an aqueous base and glycerol, followed by phase separation and distillation (152,153). Methyl formate may be hydrolyzed to methanol and formic acid by contacting the propylene oxide stream with a basic ion-exchange resia. Methanol and formic acid are removed by extractive distillation (154). [Pg.139]

Fiaal purification of propylene oxide is accompHshed by a series of conventional and extractive distillations. Impurities ia the cmde product iaclude water, methyl formate, acetone, methanol, formaldehyde, acetaldehyde, propionaldehyde, and some heavier hydrocarbons. Conventional distillation ia one or two columns separates some of the lower boiling components overhead, while taking some of the higher boilers out the bottom of the column. The reduced level of impurities are then extractively distilled ia one or more columns to provide a purified propylene oxide product. The solvent used for extractive distillation is distilled ia a conventional column to remove the impurities and then recycled (155,156). A variety of extractive solvents have been demonstrated to be effective ia purifyiag propylene oxide, as shown ia Table 4. [Pg.139]

The / f/-butanol (TBA) coproduct is purified for further use as a gasoline additive. Upon reaction with methanol, methyl tert-huty ether (MTBE) is produced. Alternatively the TBA is dehydrated to isobutylene which is further hydrogenated to isobutane for recycle ia the propylene oxide process. [Pg.139]

There are other commercial processes available for the production of butylenes. However, these are site or manufacturer specific, eg, the Oxirane process for the production of propylene oxide the disproportionation of higher olefins and the oligomerisation of ethylene. Any of these processes can become an important source in the future. More recentiy, the Coastal Isobutane process began commercialisation to produce isobutylene from butanes for meeting the expected demand for methyl-/ rZ-butyl ether (40). [Pg.366]

Oxirane Process. In Arco s Oxirane process, tert-huty alcohol is a by-product in the production of propylene oxide from a propjiene—isobutane mixture. Polymer-grade isobutylene can be obtained by dehydration of the alcohol. / fZ-Butyl alcohol [75-65-0] competes directly with methyl-/ fZ-butyl ether as a gasoline additive, but its potential is limited by its partial miscibility with gasoline. Current surplus dehydration capacity can be utilized to produce isobutylene as more methyl-/ fZ-butyl ether is diverted as high octane blending component. [Pg.367]

MethylceUulose is made by reaction of alkaU ceUulose with methyl chloride until the DS reaches 1.1—2.2. HydroxypropyhnethylceUulose [9004-65-3], the most common of this family of products, is made by using propylene oxide in addition to methyl chloride in the reaction MS values of the hydroxypropyl group in commercial products are 0.02—0.3. Use of 1,2-butylene oxide in the alkylation reaction mixture gives hydroxybutyhnethylceUulose [9041-56-9, 37228-15-2] (MS 0.04—0.11). HydroxyethyhnethylceUulose [903242-2] is made with ethylene oxide in the reaction mixture. [Pg.489]

Esterification is one of the most important reactions of fatty acids (25). Several types of esters are produced including those resulting from reaction with monohydric alcohols, polyhydric alcohols, ethylene or propylene oxide, and acetjiene or vinyl acetate. The principal monohydric alcohols used are methyl, ethyl, propyl, isopropyl, butyl, and isobutyl alcohols (26) (see Esterification Esters, organic). [Pg.84]

Propylene oxide — see Oxirane, methyl-Propylene ozonide — see 1,2,4-Trioxolane, 3-methyl-Propyliodone X-ray contrast and, 2, 520 Propynal... [Pg.750]

Treatment of (11 aS)-3-isopropyl-11 a-methyl-4-phenyl-1,6,11,11 a-tetrahy-dro[l,4]oxazino[4,3-6]isoquinolin-l-one (243) with 6N HCl in a pressure tube, then the reaction of the work-up residue with propylene oxide gave (3S)-3-methyl-l,2,3,4-tetrahydroisoquinoline-3-carboxylic acid (244) (99S704). [Pg.271]

Propylene oxide is similar in its structure to ethylene oxide, but due to the presence of an additional methyl group, it has different physical and chemical properties. It is a liquid that boils at 33.9°C, and it is only slightly soluble in water. (Ethylene oxide, a gas, is very soluble in water). [Pg.221]


See other pages where Propylene-oxide methylation is mentioned: [Pg.141]    [Pg.197]    [Pg.421]    [Pg.115]    [Pg.28]    [Pg.182]    [Pg.2996]    [Pg.141]    [Pg.197]    [Pg.421]    [Pg.115]    [Pg.28]    [Pg.182]    [Pg.2996]    [Pg.417]    [Pg.441]    [Pg.365]    [Pg.149]    [Pg.253]    [Pg.134]    [Pg.134]    [Pg.139]    [Pg.176]    [Pg.423]    [Pg.102]    [Pg.251]    [Pg.382]    [Pg.603]   
See also in sourсe #XX -- [ Pg.515 ]




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