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Reaction ethyl acetate production

The progress of the reaction is monitored by thin layer chromatography, eluting with ethyl acetate (product Rf = 0.06, visualized and developed using UV light and KMn04 respectively). [Pg.85]

For each batch time, Figures 9.3 and 9.4 also show that the conversion and the yield for x D = 0.70 are higher than those for x D = 0.80. A higher reflux ratio (Figure 9.5) is required to produce ethyl acetate product at higher purity with consequently lower rate of reaction and lower conversion. [Pg.281]

Pervaporation membrane reactors are not a recent discovery. The use of a PVMR was proposed in a U.S. patent dating back to 1960 [3.6]. Though the technical details on membrane preparation and experimental apparatus were rather sketchy, the basic idea was described there, namely, the use of a water permeable polymeric membrane to drive an esterification reaction to completion. A more detailed description of a PVMR can be found in a later European patent [3.7], which described the use of a flat membrane (commercial PVA or Nafion ) placed in the middle of a reactor consisting of two half-cells. The reaction studied was the acetic acid esterification reaction with ethanol. For an ethanol to acetic acid ratio of 2, liquid hourly space velocities (LHSV) in the range of 2-5, and a temperature of 90 °C complete conversion of the acetic acid was reported. The use of PVMR for this reaction shows promise for process simplification, as indicated schematically in Figure 3.2, which shows a side-by-side comparison of a conventional and a proposed PVMR plant for ethyl acetate production. [Pg.99]

The heat flow rate Q and extent of reaction X for ethyl acetate production in a batch reactor. [Pg.787]

Besides the benefits of thermodynamic consistent models of chemical reactions, also the problems that can arise, when inconsistent models are used should be considered. Two examples will be discussed here, one in the present and the other in the following subsection. The example discussed first relates to ethyl acetate production by RD. [Pg.82]

Add in turn benzyl chloride (8 3 g., 8 o ml.) and powdered thiourea (5 gm.) to 10 ml. of 95% ethanol in a 100 ml. flask fitted with a reflux condenser. Warm the mixture on the water-bath with gentle shaking until the reaction occurs and the effervescence subsides then boil the mixture under reflux for 30 minutes. Cool the clear solution in ice-water, filter off the crystalline deposit of the benzylthiouronium chloride at the pump, wash it with ice-cold ethyl acetate, and dry in a desiccator. Yield, 11-12 g., m.p. 170-174°. The white product is sufficiently pure for use as a reagent. It is very soluble in cold water and ethanol, but can be recrystallised by adding ethanol dropwise to a boiling suspension in ethyl acetate or acetone until a clear solution is just obtained, and then rapidly cooling. [Pg.127]

Dissolve 10 g. of chloro- 2,4-dinitrobenzenet in 50 ml. of dioxan in a 250 ml. conical flask. Dilute 8 ml. of hydrazine hydrate with an equal volume of water and add this slowly with shaking to the dioxan solution, keeping the temperature between zo " and 25°. Heat under reflux for 10 minutes to complete the reaction and then add 5 ml. of ethanol and heat again for 5 minutes. Cool and filter oflF the orange 2,4-dinitrophenylhydra-zine. Recrystallise the dry product from ethyl acetate m.p. 200° (decomp.). Yield, 7 g. [Pg.263]

Allow a mixture of 0-5 g. of the tertiary amine and 0-5 ml. of colourless methyl iodide to stand for 5 minutes. If reaction has not occurred, warm under reflux for 5 minutes on a water bath and then cool in ice water. The mixture will generally set solid if it does not, scratch the sides of the tube with a glass rod. RecrystaUise the solid product from absolute alcohol, ethyl acetate, acetone, glacial acetic acid or alcohol-ether. [Pg.660]

Place a solution of 10 -4 g. of benzalacetophenone, m.p. 57° (Section IV,130) in 75 ml. of pure ethyl acetate (Section 11,47,15) in the reaction bottle of the catalytic hydrogenation apparatus and add 0 2 g. of Adams platinum oxide catalyst (for full experimental details, see Section 111,150). Displace the air with hydrogen, and shake the mixture with hydrogen until 0 05 mol is absorbed (10-25 minutes). Filter oflF the platinum, and remove the ethyl acetate by distillation. RecrystaUise the residual benzylacetophenone from about 12 ml. of alcohol. The yield of pure product, m.p. 73°, is 9 g. [Pg.734]

The problem is more complicated when the ambident nucleophile. 2-aminothiazole, reacts with an ambident electrophilic center. Such an example is provided by the reaction between 2-amino-5-R-thiazole and ethoxycarbonyl isothiocyanate (144), which has been thoroughly studied by Nagano et al. (64, 78, 264) the various possibilities are summarized in Scheme 95. At 5°C, in ethyl acetate, the only observed products were 145a, 148. and 150. Product 148 must be heated to 180°C for 5 hr to give in low yield (25%) the thiazolo[3.2-a]-s-tnazine-2-thio-4-one (148a) (102). This establishes that attack 1-B is probably not possible at -5°C. When R = H the percentages of 145a. 148. and 150 are 29, 50, and 7%, respectively. These results show that ... [Pg.61]

Other acetyl chloride preparations include the reaction of acetic acid and chlorinated ethylenes in the presence of ferric chloride [7705-08-0] (29) a combination of ben2yl chloride [100-44-7] and acetic acid at 85% yield (30) conversion of ethyUdene dichloride, in 91% yield (31) and decomposition of ethyl acetate [141-78-6] by the action of phosgene [75-44-5] producing also ethyl chloride [75-00-3] (32). The expense of raw material and capital cost of plant probably make this last route prohibitive. Chlorination of acetic acid to monochloroacetic acid [79-11-8] also generates acetyl chloride as a by-product (33). Because acetyl chloride is cosdy to recover, it is usually recycled to be converted into monochloroacetic acid. A salvage method in which the mixture of HCl and acetyl chloride is scmbbed with H2SO4 to form acetyl sulfate has been patented (33). [Pg.82]

Biacetyl is produced by the dehydrogenation of 2,3-butanediol with a copper catalyst (290,291). Prior to the availabiUty of 2,3-butanediol, biacetyl was prepared by the nitrosation of methyl ethyl ketone and the hydrolysis of the resultant oxime. Other commercial routes include passing vinylacetylene into a solution of mercuric sulfate in sulfuric acid and decomposing the insoluble product with dilute hydrochloric acid (292), by the reaction of acetal with formaldehyde (293), by the acid-cataly2ed condensation of 1-hydroxyacetone with formaldehyde (294), and by fermentation of lactic acid bacterium (295—297). Acetoin [513-86-0] (3-hydroxy-2-butanone) is also coproduced in lactic acid fermentation. [Pg.498]

Manufacture. PVBs are manufactured by a variety of two-stage heterogeneous processes. In one of these an alcohol solution of poly(vinyl acetate) and an acid catalyst are heated to 60—80°C with strong agitation. As the poly(vinyl alcohol) forms, it precipitates from solution (77). Ethyl acetate, the principle by-product, is stripped off and sold. The precipitated poly(vinyl alcohol) is washed to remove by-products and excess acid. The poly(vinyl alcohol) is then suspended in a mixture of ethyl alcohol, butyraldehyde, and mineral acid at temperatures above 70°C. As the reaction approaches completion the reactants go into solution. When the reaction is complete, the catalyst is neutralized and the PVB is precipitated from solution with water, washed, centrifuged, and dried. Resin from this process has very low residual vinyl acetate and very low levels of gel from intermolecular acetalization. [Pg.452]

Ethyl Acetate. The esterification of ethanol by acetic acid was studied in detail over a century ago (357), and considerable Hterature exists on deterrninations of the equiUbrium constant for the reaction. The usual catalyst for the production of ethyl acetate [141-78-6] is sulfuric acid, but other catalysts have been used, including cation-exchange resins (358), a- uoronitrites (359), titanium chelates (360), and quinones and their pardy reduced products. [Pg.416]

The reduction is effected exactly as in Procedure 8a but using 0.61 g (0.088 g-atom) of lithium. After the crude reaction product has been washed well on the filter with cold water, it is dissolved in ethyl acetate, the solution is filtered through the sintered glass funnel to remove iron compounds from the ammonia, and the filtrate is extracted with saturated salt solution. The organic layer is dried over sodium sulfate and the solvent is removed. The solid residue is crystallized from methanol (120 ml) using Darco. The mixture is cooled in an ice-bath, the solid is collected, rinsed with cold methanol, and then air-dried to give 12.9 g (85%), mp 129-132° reported for the tetrahydropyranyi ether of 3j5-hydroxypregn-5-en-20-one, mp 129-131°. [Pg.56]

The photolytic and thermolytic decomposition of azides in the presence of olefins has been applied to aziridine synthesis. However, only a limited number of steroid aziridines have been prepared in this manner. The patent literature reports the use of cyanogen azide at ca. 50° for 24 hours in ethyl acetate for the preparation of an A-nor- and a B-norsteroidal aziridine. The addition is believed to proceed via a triazoline. The reaction of cholest-2-ene with ethyl azidoformate takes place in a nonselective manner to produce a mixture of substances, including C—H insertion products. [Pg.30]

Preparation of 3a-Hydroxy-5) -pregn-17(20)-en-21-oic Acid . A solution of 15 g of 3a-acetoxy-5jS-pregnan-20-one in 290 ml of glacial acetic acid is treated with 13 g of bromine at room temperature. After complete addition of bromine the reaction mixture is heated at 40-50° for 30 min, and the product precipitated with water and filtered. The product is taken up in ethyl acetate (500-600 ml) and the resulting solution washed with dilute aqueous potassium bicarbonate. The solvent is concentrated in vacuo and the product crystallized from acetone to give 16g of dibromide mp, 173-175°. [Pg.178]

To a suspension of 12 g of the lactone in 80 ml of ethanol is added 51 ml of 1 JV sodium hydroxide over 30 min with maintenance of the reaction temperature at 10-20°. The solution is stirred at 22-25° for 18 hr during which time the product separates. After filtration and washing with two 25 ml portions of water, the wet cake is extracted into 150 ml of ethyl acetate. The organic... [Pg.191]

Androst-4-ene-3,17,19-trione (0.23g) is added to a precooled solution of 0.23 g of potassium hydroxide in a mixture of 1 ml of water and 5 ml of methanol. The reaction mixture is stirred at 5-10° under nitrogen for 3 hr, diluted with benzene (30 ml) and washed with water (2 x 10 ml). The aqueous layer is reextracted with benzene and the benzene solution dried and evaporated. The crude crystalline product is filtered through 8 g of Merck silicagel and eluted with benzene-ethyl acetate (9 1) to yield 0.19 g of 19-norandrostenedione (88%) mp 169-171° 141° (CHCI3). [Pg.273]


See other pages where Reaction ethyl acetate production is mentioned: [Pg.145]    [Pg.407]    [Pg.88]    [Pg.260]    [Pg.847]    [Pg.718]    [Pg.878]    [Pg.879]    [Pg.122]    [Pg.190]    [Pg.191]    [Pg.191]    [Pg.192]    [Pg.68]    [Pg.94]    [Pg.134]    [Pg.360]    [Pg.409]    [Pg.391]    [Pg.90]    [Pg.374]    [Pg.379]    [Pg.77]    [Pg.1322]    [Pg.124]    [Pg.231]    [Pg.411]    [Pg.434]    [Pg.299]   
See also in sourсe #XX -- [ Pg.88 , Pg.90 , Pg.109 , Pg.313 ]




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Ethyl production

Production ethyl-acetate

Reaction equilibrium ethyl acetate production

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