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Condensation heat

Complementary to the matter of wetting is that of water repellency. Here, the desired goal is to make 6 as large as possible. For example, in steam condensers, heat conductivity is improved if the condensed water does not wet the surfaces, but runs down in drops. [Pg.470]

The hydrolysis of as little as 0 5 ml. of the ester can be carried out in the combined reflux-distillation apparatus shown in Fig. 38 (p, 63). Pass a stream of cold water through the vertical condenser. Place in the 10 ml. pear-shaped flask 0 5 ml. of the ester, 5 ml. of 10% NaOH solution and one or two minute fragments of unglazed porcelain and heat the mixture gently for 15 minutes so that the vapours do not rise more than about half-way up the vertical water ondenser. Now run the water out of the ver ical condenser, insert a thermometer at the top, and pass water through the inclined condenser. Heat the flask sufficiently strongly to collect 1--2 ml. of distillate. This is dilute ethanol. [Pg.100]

Place a mixture of 5 g. of camphor, 6 g. of powdered selenium dioxide and 5 ml. of acetic anhydride in flask fitted with a reflux water-condenser. Heat the flask in an oil-bath for 3 hours at 140-150 so that gentle boiling occurs shake the mixture from time to time. [Pg.148]

Add 10 g. of the crude hydrazobenzene to 80 ml. of ethanol contained in a flask fitted with a reflux water-condenser. Heat the mixture on a water-bath until the ethanol bolls, and then add 10 g. of zinc dust and 30 ml. of 30% aqueous sodium hydroxide solution. Remove the flask from the water-bath and shake the contents vigorously from time to time. After about 10 minutes, replace the flask on the water-bath and boil the contents for 3-5 minutes. Filter the mixture at the pump, transfer the filtrate to a beaker and cool in ice-water with stirring. The hydrazobenzene separates as colourless crystals, which are filtered off at the pump and drained. A portion when dried in a desiccator has m.p. 124°. [Pg.216]

Alternatively, place the mixture of alcohol and red phosphorus in a 500 ml. three-necked flask fitted with a mechanical stirrer, dropping funnel and double surface condenser. Heat the phosphorus - alcohol mixture to about 250°, and add the bromine whilst stirring vigorously. Work up the reaction product as above. [Pg.283]

Mix 100 g. of maleic acid (Section 111,143) and 100 ml. of tetra chloroethane in a 250 ml. Claisen or distilling flask provided with a thermometer, and attach a Pyrex Liebig condenser. Heat the flask in an air bath (Fig. 11, 5, 3) and collect the distillate in a measuring cylinder. When the temperature reaches 160°, 76 ml. of tetrachloroethane and 15-15-5 ml. of water are present in the receiver. Empty the water in the condenser and continue the distillation change the receiver when the temperature reaches 190°. Collect the maleic anhydride at 195-197°. Recrystallise the crude anhydride from chloroform. The yield of pure maleic anhydride, m.p. 54°, is 70 g. [Pg.376]

Drop 1 g. of sodium into 10 ml. of ethyl alcohol in a small flask provided with a small water condenser heat the mixture until all the sodium has dissolved. Cool, and add 1 g. of the ester and 0-5 ml. of water. Frequently the sodium salt of the acid will be deposited either at once or after boiling for a few minutes. If this occurs, filter oflF the solid at once, wash it with a little absolute ethyl alcohol (or absolute methylated spirit), and convert it into the p-bromophenacyl ester, p-nitro-benzyl ester or S-benzyl-tso-thiuronium salt (for experimental details, see Section 111,85). If no solid separates, continue the boiling for 30-60 minutes, boil oflF the alcohol, allow to cool, render the product just neutral to phenolphthalein with dilute sulphuric or hydrochloric acid, convert the sodium salt present in solution into a crystalline derivative (Section 111,85), and determine its melting point. [Pg.391]

Place a mixture of 1 0 g. of the hydrocarbon, 10 ml. of dry methylene chloride or ethylene dichloride or syw.-tetrachloroethane, 2 5 g. of powdered anhydrous aluminium chloride and 1-2 g. of pure phthalic anhydride in a 50 ml. round-bottomed flask fitted with a short reflux condenser. Heat on a water bath for 30 minutes (or until no more hydrogen chloride fumes are evolved), and then cool in ice. Add 10 ml. of concentrated hydrochloric acid cautiously and shake the flask gently for 5 min utes. Filter oflf the solid at the pump and wash it with 10-15 ml. of cold water. Boil the resulting crude aroylbenzoic acid with 10 ml. of 2 -5N sodium carbonate solution and 0 2 g. of decolourising carbon for 5 minutes, and filter the hot solution. Cool, add about 10 g. of crushed ice and acidify... [Pg.519]

Place 28 g. (27-5 ml.) of pure aniline and 28 g. (23 ml.) of purified methyl phosphate in a 500 ml. round-bottomed flask equipped with a reflux condenser. Heat gently at first and remove the flame when the vigorous and exothermic reaction commences. When the latter subsides. [Pg.572]

Method 2. Place 0-2 g. of cupric acetate, 10 g. of ammonium nitrate, 21 2 g. of benzoin and 70 ml. of an 80 per cent, by volume acetic acid -water solution in a 250 ml. flask fitted with a reflux condenser. Heat the mixture with occasional shaking (1). When solution occurs, a vigorous evolution of nitrogen is observed. Reflux for 90 minutes, cool the solution, seed the solution with a crystal of benzil (2), and allow to stand for 1 hour. Filter at the pump and keep the mother liquor (3) wash well with water and dry (preferably in an oven at 60°). The resulting benzil has m.p. 94-95° and the m.p. is unaffected by recrystallisation from alcohol or from carbon tetrachloride (2 ml. per gram). Dilution of the mother liquor with the aqueous washings gives a further 1 Og. of benzil (4). [Pg.715]

Place 52 g, of anthraquinone, 50 g. of granulated tin and 375 ml. of glacial acetic acid in a 1 htre round-bottomed flask fitted with a reflux condenser. Heat the contents of the flask to boihng and add 125 ml, of... [Pg.740]

Hydrolysis of methyl m-nitrobenzoate to m-nitrobenzoic acid. Place 90 -5 g. of methyl m-nitrobenzoate and a solution of 40 g. of sodium hydroxide in 160 ml. of water in a 1-htre round-bottomed flask equipped with a reflux condenser. Heat the mixture to boiling during 5-10 minutes or until the ester has disappeared. Dilute the reaction mixture with an equal volume of water. When cold pour the diluted reaction product, with vigorous stirring, into 125 ml. of concentrated hydrochloric acid. Allow to cool to room temperature, filter the crude acid at the pump and wash it with a httle water. Upon drying at 100°, the crude m-nitrobenzoic acid, which has a pale brownish colour, weighs 80 g. and melts at 140°, Recrystalhsation from 1 per cent, hydrochloric acid afibrds the pure acid, m.p. 141°, as a pale cream sohd the loss of material is about 5 per cent. [Pg.770]

Method 2. Place 90 g. of sodium benzenesulphonate (Section IV,29) (previously dried at 130-140° for 3 hours) and 50 g. of powdered phosphorus pentachloride (1) in a 500 ml. round-bottomed flask furnished with a reflux condenser heat the mixture in an oil bath at 170-180° for 12-15 hours. Every 3 hours remove the flask from the oil bath, allow to cool for 15-20 minutes, stopper and shake thoroughly until the mass becomes pasty. At the end of the heating period, allow the reaction mixture to cool. Pour on to 1 kilo of crushed ice. Extract the crude benzenesulphonyl chloride with 150 ml. of carbon tetrachloride and the aqueous layer with 75 ml. of the same solvent. Remove the solvent under atmospheric pressure and proceed as in Method 1. The yield is about 170 g., but depends upon the purity of the original sodium benzenesulphonate. [Pg.822]

Method 2. Place 48 g. (41 -5 ml.) of freshly-distilled furfural, 52 g. of dry malonic acid (1), and 24 ml. of dry pyridine (2) in a 500 ml. round-bottomed flask, fitted with a reflux condenser. Heat the flask on a boiling water bath for 2 hours, cool the reaction mixture and dilute with 50 ml. of water. Dissolve the acid by the addition of concentrated ammonia solution, filter the solution and wash the filter paper with a... [Pg.834]

Acid cleaners based on sulfamic acid are used in a large variety of appHcations, eg, air-conditioning systems marine equipment, including salt water stills wells (water, oil, and gas) household equipment, eg, copper-ware, steam irons, humidifiers, dishwashers, toilet bowls, and brick and other masonry tartar removal of false teeth (50) dairy equipment, eg, pasteurizers, evaporators, preheaters, and storage tanks industrial boilers, condensers, heat exchangers, and preheaters food-processing equipment brewery equipment (see Beer) sugar evaporators and paper-mill equipment (see also Evaporation Metal surface treati nts Pulp). [Pg.64]

Initially, the source of environmental risk from cooling water was assumed to be the pollutant discharged, ie, heat, in the form of the elevated temperature of the water released from the condensers. Heat is now recognized as being only one of several potential risks of power station cooling (Fig. 2). [Pg.472]

Spirai Compact, concentric plates no bypassing, high turbulence. Cross-flow, condensing, heating. Process corrosion, suspended materials. 0.8-1.5... [Pg.26]

The preceding discussion on reflux assumes that the condenser is not limiting when the reflux is raised. For a severely limited condenser, an evaluation must first be made of the condenser heat transfer before analyzing the effect of a reflux increase with Smith-Brinkley. Likewise, a limiting reboiler or trays close to flood would have to be evaluated prior to Smith-Brinkley calculations. [Pg.70]

The heat rejected at the condenser is the sum of the condensation heat and that required to cool the gas down to the condensing temperature. Since the gas is desorbed at a range of temperatures between and this should properly be evaluated as ... [Pg.316]

Takuma, M., Yamada, A., Matsuo, T., and Tokita, Y., Condensation Heat Transfer Characteristics of Ammonia-Water Vapor Mixture on a Vertical Flat Surface, Proc. 10th Inti. Heat Transfer Conf, Vol.3 pp395-400, 1994. [Pg.64]

The cost of condensers/heat exchangers ( ) is taken as l,500 (heat transfer area in m ). The overall heat-transfer coefficients for the dehumidification, the... [Pg.254]

Process flow diagrams (Figure 3.1.3-2) are more complex. They show all main flow streams, valves, vessels, condensers, heat exchangers, instrument locations, reflux columns, etc. Pressures... [Pg.68]

BBBOILEB HEAT DUTY = CONDENSER HEAT DUTY=... [Pg.98]

For duPont s Teflon tube (Vr-in. diameter) heat exchangers (Figure 10-8) for condensing, heating, and cooling service, the U values range from 15-35. Little or no fouling occurs on the Teflon surface. [Pg.90]

Based upon condensing heat load, log At and an assumed overall coefficient, U, estimate the required surface area. [Pg.121]


See other pages where Condensation heat is mentioned: [Pg.131]    [Pg.479]    [Pg.108]    [Pg.566]    [Pg.587]    [Pg.761]    [Pg.834]    [Pg.837]    [Pg.917]    [Pg.938]    [Pg.961]    [Pg.269]    [Pg.271]    [Pg.4]    [Pg.226]    [Pg.474]    [Pg.1270]    [Pg.1359]    [Pg.140]    [Pg.316]    [Pg.52]    [Pg.220]    [Pg.70]    [Pg.149]    [Pg.356]    [Pg.96]   
See also in sourсe #XX -- [ Pg.439 , Pg.440 ]

See also in sourсe #XX -- [ Pg.457 , Pg.459 ]




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Condensates specific heat

Condensation Heat-Transfer Phenomena

Condensation and Boiling Heat Transfer

Condensation average heat transfer coefficient

Condensation during heating

Condensation heat pipes

Condensation heat transfer

Condensation heat transfer coefficient

Condensation heat transfer fundamentals

Condensation heat transfer rate

Condensation heat transfer resistance

Condensation heating

Condensation molar heat

Condensation, heat-transfer coefficients for

Condensation, latent heat

Condensed-phase pyrolysis heat conduction

Condenser heat transfer

Condensers heat transfer coefficients

Condensers temperature-heat flow diagram

Condensing heat transfer

Condensing heat-transfer rates

Condensing heat-transfer rates condensate backup

Condensing steams heat flow

Condensing steams stirred tank heating

Dropwise condensation, heat transfer

Film condensation heat transfer rate

Heat Exchangers condensing liquids

Heat Exchangers shell side condensation

Heat Theorem to condensed systems

Heat condensers

Heat exchanger condensing vapors

Heat exchangers condensation

Heat exchangers condensers

Heat exchangers vacuum condensers

Heat exchangers, condensers Heaters, fired

Heat exchangers, condensers Humidification

Heat exchangers, condensers Integrating processes

Heat exchangers, condensers relative

Heat exchangers, condensers variation with flow

Heat steam condensation

Heat transfer coefficient surface condensers

Heat transfer coefficient, in condensation

Heat transfer coefficients condensing steam

Heat transfer coefficients, overall condensers

Heat transfer from film condensation

Heat transfer in condensation

Heat transfer total condenser design

Heat-transfer coefficient for film condensation

Heat-transfer equipment, condensers

Heat-transfer equipment, condensers costs

Heat-transfer equipment, condensers exchangers

Heating condensate recycling

Heating condensates

Heating condensing vapor

Heats of condensation

Latent heat of condensation

Overall heat transfer coefficient in condensation

Overhead condenser heat-removal

Phase change, heat transfer condensation

Product heating condensates

Shell and Tube Heat Exchanger with Condensing Steam

Shell-tube heat exchanger, condensate

Some further applications of the Heat Theorem to condensed systems

Specific condensation heat

Steam condensing heat transfer

Water condensation, latent heat

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