Methanol, hydrolysis

Polycyclic aromatic hydrocarbons Volatile organic compounds Organic solvent, methanolic hydrolysis [86]... 

Solvent extraction with methanolic hydrolysis of the soil has been used to extract aromatic hydrocarbons. Significantly higher quantities of organics were recovered compared to the use of only an organic solvent extraction [41 ]. 

Extension of the C-tether to m = 2 can be achieved by subjecting diazo ketone 58 to the Wolff rearrangement using silver benzoate, triethyl-amine and methanol. Hydrolysis of the resulting methyl 4-methyl-4-[(E)-phenyldiazenyllpentanoate (74) (94%) yields the acid 75 (84%). Conversion of 75 into the mixed anhydride 76 followed by treatment with diazomethane gives 1 -diazo-5-methyl-5-[(E)-phenyldiazenyl]hexan-2-one (77) in low yield (19%) and methyl ester 74 (78%) (Scheme 18). 

SE reflux 2 h with 80% aqueous ethanol hydrolysis with 3-glucosidase SE ethanol SPE Polystyrene resin (NKAO) eluted with 20% ethanol SE 80% aqueous methanol hydrolysis ceUulase in 0.1 M acetate buffer pH 5.0 LLE ethyl acetate... 

Rethrolones and Related Compounds.—Electrolysis has featured prominently in two useful syntheses of rethrolones published this year. In one of these approaches 2,5-dimethoxydihydrofuran is first prepared by the anodic oxidation of the appropriate 2,5-disubstituted furan (80) in methanol hydrolysis of the electro-oxidation product with ion-exchange resin, followed by treatment with base, then completes the rethrolone synthesis (Scheme 21). Anodic oxidation of substituted cyclo-pentadienes in HOAc brings about ready introduction (1,4) of two oxygen functions into the diene leading to (81), which by a series of transformations can be converted into the rethrolone (82). ... 

Alkynes Methyl 3-bromopropionate reacted with furan at 80 °C to afford the stable cycloadduct 8, which was converted to a 9 1 endo/exo mixture of epimeric acetals 9 by treatment with sodium methoxide in methanol. Hydrolysis of the acetals 9 using Nafion-H led to the bicychc p-keto-esters 10 without noticeable epimerization [13]. In effect, methyl 3-bromopropionate acts as a methoxycarbonylketene equivalent, allowing the preparation of both epimers of 10 in three steps and good overall yield (Scheme 13.4). 

Figure 4.3 Iridium-catalyzed carbonylation of methanol. Hydrolysis of 4.14 and 4.15 is not shown and the organic cycle is on the left.

Prepared generally by ester interchange from polyvinylacelate (ethanoate) using methanol and base also formed by hydrolysis of the acetate by NaOH and water. The properties of the poly(vinyl alcohol) depend upon the structure of the original polyvinyl acetate. Forms copolymers. Used as a size in the textile industry, in aqueous adhesives, in the production of polyvinyl acetates (e.g. butynal) for safety glasses. U.S. production 1980... 

In view of the high cost of methyl iodide in the above preparation of anisole, and the fact that, unless absolute methanol is used, the ready hydrolysis of the methyl iodide may cause a low yield of the ether, the preparation of anisole may be ad antageously replaced by that of phenetole. I he reaction is not of course a methylation, but is nevertheless of the same type as that used in the preparation of anisole. 

Since an enzyme is a biological catalyst and therefore merely accelerates a reaction, it cannot alter the position of equilibrium in a reversible reaction. The hydrolysis of p-methylglucoside is reversible and emulsin should therefore be capable also of synthesising this compound frc n glucose and methanol. This synthesis can actually be carried out by the action of the enzyme on glucose dissolved in an excess of methanol, the excess of the alcohol throwing the equilibrium over to the left. Owing to experimental difficulties, this reaction is not here described. 

The reaction is applicable to the preparation of amines from amides of aliphatic aromatic, aryl-aliphatic and heterocyclic acids. A further example is given in Section IV,170 in connexion with the preparation of anthranilic acid from phthal-imide. It may be mentioned that for aliphatic monoamides containing more than eight carbon atoms aqueous alkaline hypohalite gives poor yields of the amines. Good results are obtained by treatment of the amide (C > 8) in methanol with sodium methoxide and bromine, followed by hydrolysis of the resulting N-alkyl methyl carbamate ... 

By increasing the molar proportion of the monocarboxylic acid, the yield of (II) is improved. Thus electrolysis of a mixture of decanoic acid (n-decoic acid capric acid) (V) (2 mols) and methyl hydrogen adipate (VI) (1 mol) in anhydrous methanol in the presence of a little sodium methoxide gives, after hydrolysis of the esters formed, n-octadecane (VII), tetradecanoic or myristic acid (VIH) and sebacic acid (IX) ... 

In this preparation, phenyi-2-nitropropene is reduced to phenyl-2-nitropropane with sodium borohydride in methanol, followed by hydrolysis of the nitro group with hydrogen peroxide and potassium carbonate, a variety of the Nef reaction. The preparation is a one-pot synthesis, without isolation of the intermediate. 

Aldehydes are easily oxidized to carboxylic acids under conditions of ozonide hydroly SIS When one wishes to isolate the aldehyde itself a reducing agent such as zinc is included during the hydrolysis step Zinc reduces the ozonide and reacts with any oxi dants present (excess ozone and hydrogen peroxide) to prevent them from oxidizing any aldehyde formed An alternative more modem technique follows ozone treatment of the alkene m methanol with reduction by dimethyl sulfide (CH3SCH3)... 

Hydrolysis of a compound A in dilute aqueous hydrochlonc acid gave (along with methanol) a compound B mp 164—165°C Compound B had the molecular formula CigHig04 it exhibited hydroxyl absorption in its IR spectrum at 3550 cm but had no peaks in the carbonyl region What IS a reasonable structure for compound B" ... 

About half of the wodd production comes from methanol carbonylation and about one-third from acetaldehyde oxidation. Another tenth of the wodd capacity can be attributed to butane—naphtha Hquid-phase oxidation. Appreciable quantities of acetic acid are recovered from reactions involving peracetic acid. Precise statistics on acetic acid production are compHcated by recycling of acid from cellulose acetate and poly(vinyl alcohol) production. Acetic acid that is by-product from peracetic acid [79-21-0] is normally designated as virgin acid, yet acid from hydrolysis of cellulose acetate or poly(vinyl acetate) is designated recycle acid. Indeterrninate quantities of acetic acid are coproduced with acetic anhydride from coal-based carbon monoxide and unknown amounts are bartered or exchanged between corporations as a device to lessen transport costs. 

Formic acid is currently produced iadustriaHy by three main processes (/) acidolysis of formate salts, which are ia turn by-products of other processes (2) as a coproduct with acetic acid ia the Hquid-phase oxidation of hydrocarbons or (3) carbonylation of methanol to methyl formate, followed either by direct hydrolysis of the ester or by the iatermediacy of formamide. 

Coproductioa of ammonium sulfate is a disadvantage of the formamide route, and it has largely been supplanted by processes based on the direct hydrolysis of methyl formate. If the methanol is recycled to the carbonylation step the stoichiometry corresponds to the production of formic acid by hydration of carbon monoxide, a reaction which is too thermodynamicaHy unfavorable to be carried out directly on an iadustrial scale. 

Hydrolysis of Dimethyl Terephthalate. Hoechst Celanese and Eormosa Chemical Eibers Corp. produce a polymer-grade terephthahc acid by hydrolysis of high purity dimethyl terephthalate. Hbls-Troisdorf AG hcenses a process with this step (70). Hydrolysis occurs at 260—280°C and 4500—5500 kPa (45—55 atm) in a hydrolysis reactor without catalysis. The overhead methanol and water vapor is separated and the methanol is returned to the dimethyl terephthalate section for reuse. The reactor hquid is crystallized, cycloned, washed, and further cooled. Einahy, the slurry is centrifuged and dried. The product has less than 25 ppm of 4-formylbenzoic acid and very low levels of other impurities. There may be several hundred parts per million of monomethyl terephthalate, which is incompletely hydrolyzed dimethyl terephthalate. 

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). 

Expect some product contamination if feed components can react with water, eg, ester will be partially hydrolyzed to acid and alcohol fate of reaction product species depends on above rules, eg, methanol from methyl ester hydrolysis probably not stripped out of bottoms stream. 

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