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Amides, purification

The general theory behind the process is that the hypohalite will convert the amide to a haloamide. This then spontaneously changes to the isocyanate when heated and decomposes to the amine from the water present. In effect, all that happens is that a Carbonyl (CO) group is stripped off the starting amide to yield the corresponding amine. Yields pre- purification are around 80%, post-purification average around 65%. Certain uses of the result-... [Pg.260]

Most by-product acetylene from ethylene production is hydrogenated to ethylene in the course of separation and purification of ethylene. In this process, however, acetylene can be recovered economically by solvent absorption instead of hydrogenation. Commercial recovery processes based on acetone, dimetbylform amide, or /V-metby1pyrro1idinone have a long history of successfiil operation. The difficulty in using this relatively low cost acetylene is that each 450, 000 t/yr world-scale ethylene plant only produces from 7000 9000 t/yr of acetylene. This is a small volume for an economically scaled derivatives unit. [Pg.394]

Polymerization Solvent. Sulfolane can be used alone or in combination with a cosolvent as a polymerization solvent for polyureas, polysulfones, polysUoxanes, polyether polyols, polybenzimidazoles, polyphenylene ethers, poly(l,4-benzamide) (poly(imino-l,4-phenylenecarbonyl)), sUylated poly(amides), poly(arylene ether ketones), polythioamides, and poly(vinylnaphthalene/fumaronitrile) initiated by laser (134—144). Advantages of using sulfolane as a polymerization solvent include increased polymerization rate, ease of polymer purification, better solubilizing characteristics, and improved thermal stabUity. The increased polymerization rate has been attributed not only to an increase in the reaction temperature because of the higher boiling point of sulfolane, but also to a decrease in the activation energy of polymerization as a result of the contribution from the sulfonic group of the solvent. [Pg.70]

Other options for the purification of CA include dissolution in hot water, aqueous ammonia, aqueous formaldehyde, or hot dimethylformamide followed by filtration to remove most of the impurities. The CA is recoverable by cooling the aqueous solution (84), acidifying the ammonium hydroxide solution (85), or cooling the dimethylform amide solution with further precipitation of CA by addition of carbon tetrachloride (86). Sodium hydroxide addition precipitates monosodium cyanurate from the formaldehyde solution (87). [Pg.420]

Amides are stable compounds. The lower-melting members (such as acetamide) can be readily purified by fractional distillation. Most amides are solids which have low solubilities in water. They can be recrystallised from large quantities of water, ethanol, ethanol/ether, aqueous ethanol, chloroform/toluene, chloroform or acetic acid. The likely impurities are the parent acids or the alkyl esters from which they have been made. The former can be removed by thorough washing with aqueous ammonia followed by recrystallisation, whereas elimination of the latter is by trituration or recrystallisation from an organic solvent. Amides can be freed from solvent or water by drying below their melting points. These purifications can also be used for sulfonamides and acid hydrazides. [Pg.63]

The checkers used 16.8 g. of Eastman Kodak Company cyanamide (P1995) without further purification. A convenient method of preparing cyanamide from commercial calcium cyan-amide has been described. According to the submitters, an aqueous solution of crude cyanamide is satisfactory in the present synthesis and is obtained by adapting this published procedure as follows. [Pg.10]

The phenylbenzamide is prepared from the acid chloride in the presence of Et3N (86% yield) and can be cleaved with 3% Na(Hg) (MeOH, 25°, 4 h, 81% yield). Most amides react only slowly with Na(Hg). Phenylbenzamides are generally crystalline compounds, an aid in their purification. ... [Pg.561]

A -( 1-Chloro- or bromoalkyl)amides are generally moisture-sensitive, unstable compounds, which are often directly used without further purification. Standard Lewis acids such as boron trifluoride-diethyl ether, aluminum(lll) chloride, zinc(II) chloride, tin(IV) chloride and titani-um(IV) chloride are used to generate the /V-acyliminium ion, although sometimes a catalyst is not necessary. [Pg.815]

In most of the studies discussed above, except for the meta-linked diamines, when the aromatic content (dianhydride and diamine chain extender), of the copolymers were increased above a certain level, the materials became insoluble and infusible 153, i79, lsi) solution to this problem with minimum sacrifice in the thermal properties of the products has been the synthesis of siloxane-amide-imides183). In this approach pyromellitic acid chloride has been utilized instead of PMDA or BTDA and the copolymers were synthesized in two steps. The first step, which involved the formation of (siloxane-amide-amic acid) intermediate was conducted at low temperatures (0-25 °C) in THF/DMAC solution. After purification of this intermediate thin films were cast on stainless steel or glass plates and imidization was obtained in high temperature ovens between 100 and 300 °C following a similar procedure that was discussed for siloxane-imide copolymers. Copolymers obtained showed good solubility in various polar solvents. DSC studies indicated the formation of two-phase morphologies. Thermogravimetric analysis showed that the thermal stability of these siloxane-amide-imide systems were comparable to those of siloxane-imide copolymers 183>. [Pg.35]

After salt break chiral acid 11 was converted to the methyl ketone 13 in essentially quantitative yield via the intermediacy of the Weinreb amide and processed as an oil without further purification (Scheme 9.6). The carbonyl group in 13 was then reduced to the secondary alcohol 16 using L-Selectride as previously described in 97% assay yield. We were pleased to find that an attainable reaction temperature of-50°C was sufficient to obtain high selectivity of >98 2, and that, in the absence of the reactive nitrile group, no issues were observed or during... [Pg.246]

The crude material to be used for desulfonamidation should be tested for absence of syw.-tribromoaniline by ascertaining its solubility in 1 N alkali. A clear, though colored, solution should result. If the solution is cloudy, purification of the impure material by dissolving it in alkali, filtering the solution, and reprecipitating the amide is essential. [Pg.27]

This novel resin-bound CHD derivative was then utilized in the preparation of an amide library under microwave irradiation. Reaction of the starting resin-bound CHD with an acyl or aroyl chloride yields an enol ester, which, upon treatment with amines, leads to the corresponding amide, thus regenerating the CHD. This demonstrates the feasibility of using the CHD resin as a capture and release reagent for the synthesis of amides. The resin capture/release methodology [126] aids in the removal of impurities and facilitates product purification. [Pg.367]

Let us consider the crystal growth of the three previous compounds which have retained our attention by their high nonlinear optical susceptibilities (POM, MAP, NPP) plus an additional one R(+)N-methylidene (gem-carbethoxiphenyl) amide of 4-N-dime-thylamino- benzylidene cyanacetlc acid -AMA, of potential interest but not yet investigated from the optical point of view. We look successively into their synthesis, purification, crystal growth and characterization. [Pg.94]


See other pages where Amides, purification is mentioned: [Pg.311]    [Pg.283]    [Pg.297]    [Pg.67]    [Pg.78]    [Pg.45]    [Pg.114]    [Pg.176]    [Pg.36]    [Pg.204]    [Pg.81]    [Pg.30]    [Pg.131]    [Pg.182]    [Pg.269]    [Pg.554]    [Pg.4]    [Pg.79]    [Pg.81]    [Pg.87]    [Pg.112]    [Pg.167]    [Pg.256]    [Pg.268]    [Pg.270]    [Pg.163]    [Pg.119]    [Pg.16]    [Pg.337]    [Pg.967]    [Pg.241]    [Pg.486]    [Pg.27]    [Pg.138]   
See also in sourсe #XX -- [ Pg.56 ]

See also in sourсe #XX -- [ Pg.56 ]




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