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Addition—Continual

P-Hydroxy-a-naphthaldehyde, Equip a 1 litre three-necked flask with a separatory funnel, a mercury-sealed mechanical stirrer, and a long (double surface) reflux condenser. Place 50 g. of p-naphthol and 150 ml. of rectified spirit in the flask, start the stirrer, and rapidly add a solution of 100 g. of sodium hydroxide in 210 ml. of water. Heat the resulting solution to 70-80° on a water bath, and place 62 g. (42 ml.) of pure chloroform in the separatory funnel. Introduce the chloroform dropwise until reaction commences (indicated by the formation of a deep blue colour), remove the water bath, and continue the addition of the chloroform at such a rate that the mixture refluxes gently (about 1 5 hours). The sodium salt of the phenolic aldehyde separates near the end of the addition. Continue the stirring for a further 1 hour. Distil off the excess of chloroform and alcohol on a water bath use the apparatus shown in Fig. II, 41, 1, but retain the stirrer in the central aperture. Treat the residue, with stirring, dropwise with concentrated hydrochloric acid until... [Pg.704]

Phthalide. In a 1 litre bolt-head flask stir 90 g. of a high quality zinc powder to a thick paste with a solution of 0 5 g. of crystallised copper sulphate in 20 ml. of water (this serves to activate the zinc), and then add 165 ml. of 20 per cent, sodium hydroxide solution. Cool the flask in an ice bath to 5°, stir the contents mechanically, and add 73-5 g. of phthalimide in small portions at such a rate that the temperature does not rise above 8° (about 30 minutes are required for the addition). Continue the stirring for half an hour, dilute with 200 ml. of water, warm on a water bath imtil the evolution of ammonia ceases (about 3 hours), and concentrate to a volume of about 200 ml. by distillation vmder reduced pressure (tig. 11,37, 1). Filter, and render the flltrate acid to Congo red paper with concentrated hydrochloric acid (about 75 ml. are required). Much of the phthalide separates as an oil, but, in order to complete the lactonisation of the hydroxymethylbenzoic acid, boil for an hour transfer while hot to a beaker. The oil solidifles on cooling to a hard red-brown cake. Leave overnight in an ice chest or refrigerator, and than filter at the pump. The crude phthalide contains much sodium chloride. RecrystaUise it in 10 g. portions from 750 ml. of water use the mother liquor from the first crop for the recrystaUisation of the subsequent portion. Filter each portion while hot, cool in ice below 5°, filter and wash with small quantities of ice-cold water. Dry in the air upon filter paper. The yield of phthalide (transparent plates), m.p. 72-73°, is 47 g. [Pg.772]

Benefits depend upon location. There is reason to beheve that the ratio of hydrocarbon emissions to NO has an influence on the degree of benefit from methanol substitution in reducing the formation of photochemical smog (69). Additionally, continued testing on methanol vehicles, particularly on vehicles which have accumulated a considerable number of miles, may show that some of the assumptions made in the Carnegie Mellon assessment are not vahd. Air quaUty benefits of methanol also depend on good catalyst performance, especially in controlling formaldehyde, over the entire useful life of the vehicle. [Pg.434]

Starting from stoichiometric conditions (< = 1) and then proceeding in the lean direction (< < 1), we anticipate that the peak fiame temperature will be reduced gradually. In addition, as the maximum temperature is lowered and the corresponding adiabatic fiame speed of an unstrained a = 0) fiame is reduced, we anticipate that the fiame will move closer to the plane of symmetry. Ultimately, as the fuel to air ratio is lowered below a critical value, radical production in the fiame will be severely restricted and the fiame will extinguish (lean extinction). The arclength continuation procedure will then generate unphysical solutions for additional continuation steps until a maximum value of the... [Pg.416]

Since many years, pectolytic enzymes have been widely used in industrial beverage processing to improve either the quality and the yields in fruit juice extraction or the characteristics of the final product [1,2]. To this purpose, complex enzymatic mixtures, containing several pectolytic enzymes and often also cellulose, hemicellulose and ligninolytic activities, are usually employed in the free form. The interactions among enzymes, substrates and other components of fruit juice make the system very difficult to be investigated and only few publications are devoted to the study of enzymatic pools [3-5], An effective alternative way to carry out the depectinisation process is represented by the use of immobilized enzymes. This approach allows for a facile and efficient enzymatic reaction control to be achieved. In fact, it is possible to avoid or at least to reduce the level of extraneous substances originating from the raw pectinases in the final product. In addition, continuous processes can be set up. [Pg.971]

In an acid-base titration you may either add acid to base or base to acid. This addition continues until there is some indication that the reaction is complete. Often a chemical known as an indicator will indicate the endpoint of a titration reaction, the experimental end of the titration. If we perform the experiment well, the endpoint should closely match the equivalence point of the titration, the theoretical end of the reaction. All the calculations in this section assume accurate experimental determination of the endpoint, and that this value is the same as the equivalence point. [Pg.71]

Molecules with more than two atoms have, in addition, continuously changing bond angles. These bending modes are indicated in Fig. 12-1. [Pg.245]

A primary difference is that a higher fluidization velocity is desired resulting in the need for an expanded deceleration zone, hence the extended conical expansion chamber. Additionally, continuous fluidization is desireable from both economical and functional points of view. For this reason, the filter housing is enlarged and designed to shake fines back into the batch without stopping fluidization or spraying. [Pg.159]

Start with a salt and add water in small increments, stirring well with a spatula after each addition. Continue until the salt can absorb no more water, as evidenced by free liquid (where it will take on the shape of the container but will not easily pour). Store indefinitely at room temperature in a manner to prevent substantial moisture gain or evaporation losses. [Pg.45]


See other pages where Addition—Continual is mentioned: [Pg.517]    [Pg.279]    [Pg.294]    [Pg.537]    [Pg.65]    [Pg.923]    [Pg.1253]    [Pg.78]    [Pg.581]    [Pg.726]    [Pg.517]    [Pg.772]    [Pg.261]    [Pg.217]    [Pg.241]    [Pg.385]    [Pg.374]    [Pg.543]    [Pg.545]    [Pg.547]    [Pg.549]    [Pg.551]    [Pg.553]    [Pg.555]    [Pg.557]    [Pg.114]    [Pg.89]    [Pg.287]    [Pg.1189]    [Pg.294]    [Pg.187]    [Pg.517]    [Pg.91]    [Pg.100]    [Pg.100]   


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Acid continued) additive

Addition reactions (continued

Addition reactions (continued Lewis base catalysts

Addition reactions (continued aldehydes

Addition reactions (continued alkenylation

Addition reactions (continued enones

Addition reactions (continued functionalized

Addition reactions (continued high enantioselectivity

Addition reactions (continued intermolecular

Addition reactions (continued intramolecular

Addition reactions (continued ketones

Addition reactions (continued oxidative

Addition reactions (continued synthesis

Addition reactions—continued Diels-Alder reaction

Addition reactions—continued bonds

Addition reactions—continued compounds

Addition reactions—continued electrophilic

Addition reactions—continued exothermic nature

Addition reactions—continued product

Addition reactions—continued stereochemistry

Addition—Continual phthalide

Aldehydes continued additions

Azines—continued activation by additional ring-nitrogen

Azines—continued covalent addition

Azines—continued mono-, covalent addition

Azines—continued poly-, covalent addition

Continuous-addition-of-reagent technique

Enantioselective reactions (continued asymmetric addition

Enantioselective reactions (continued conjugate addition

OBM with continuous addition of melt

ODM with continuous addition of melt

ODM with continuous addition of melt and solid

Paint coatings continued additives

Poly continuous addition, emulsion

Semi-continuous monomer addition

Steels continued alloying additions

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