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Distillation pressure measurement

A minimum volatihty is frequently specified to assure adequate vaporization under low temperature conditions. It can be defined either by a vapor pressure measurement or by initial distillation temperature limits. Vaporization promotes engine start-up. Fuel vapor pressure assumes an important role particularly at low temperature. For example, if fuel has cooled to —40°C, as at arctic bases, the amount of vapor produced is well below the lean flammabihty limit. In this case a spark igniter must vaporize enough fuel droplets to initiate combustion. Start-up under the extreme temperature conditions of the arctic is a major constraint in converting the Air Force from volatile JP-4 to kerosene-type JP-8, the military counterpart of commercial Jet Al. [Pg.415]

The diazirines are of special interest because of their isomerism with the aliphatic diazo compounds. The diazirines show considerable differences in their properties from the aliphatic diazo compounds, except in their explosive nature. The compounds 3-methyl-3-ethyl-diazirine and 3,3-diethyldiazirine prepared by Paulsen detonated on shock and on heating. Small quantities of 3,3-pentamethylenediazirine (68) can be distilled at normal pressures (bp 109°C). On overheating, explosion followed. 3-n-Propyldiazirine exploded on attempts to distil it a little above room temperature. 3-Methyldiazirine is stable as a gas, but on attempting to condense ca. 100 mg for vapor pressure measurements, it detonated with complete destruction of the apparatus." Diazirine (67) decomposed at once when a sample which had been condensed in dry ice was taken out of the cold trap. Work with the lower molecular weight diazirines in condensed phases should therefore be avoided. [Pg.125]

Fig. 111.—Experimental values of the interaction parameter %i plotted against the volume fraction of polymer. Data for polydi-methylsiloxane M =3850) in benzene, A (New-ingi6). polystyrene in methyl ethyl ketone, (Bawn et aV ) and polystyrene in toluene, O (Bawn et alP) are based on vapor pressure measurements. Those for rubber in benzene, T (Gee and Orr ) were obtained using vapor pressure measurements at higher concentrations and isothermal distillation equilibration with solutions of known activities in the dilute range. Fig. 111.—Experimental values of the interaction parameter %i plotted against the volume fraction of polymer. Data for polydi-methylsiloxane M =3850) in benzene, A (New-ingi6). polystyrene in methyl ethyl ketone, (Bawn et aV ) and polystyrene in toluene, O (Bawn et alP) are based on vapor pressure measurements. Those for rubber in benzene, T (Gee and Orr ) were obtained using vapor pressure measurements at higher concentrations and isothermal distillation equilibration with solutions of known activities in the dilute range.
You are to specify an orifice meter for measuring the flow rate of a 35° API distillate (SG = 0.85) flowing in a 2in. sch 160 pipe at 70°F. The maximum flow rate expected is 2000 gal/hr and the available instrumentation for the differential pressure measurement has a limit of 2 psi. What size orifice should be installed ... [Pg.336]

The pressure was reduced to 600 mmHg and after 2 h the second portion of adipic acid (20.0 g) was added. The reaction was continued overnight at 400 mmHg before the third aliquot (16.97 g) was added. The volume of water in the distillate was measured as an indication of the extent of the reaction. The pressure was reduced to 10 mmHg over a period of 24 h and the reaction was left for another 48 h at this pressure to remove all traces of water and toluene and give the product polymer as a viscous oil. [Pg.180]

The water for the substrate was distilled from a Stokes still and foamed in a 600-ml. medium porosity sintered glass funnel the foam was removed several times by sweeping the surface. The water gave adequately stable base line readings for both the surface potential and surface pressure measurements. [Pg.221]

Colligative properties have many practical uses, including the melting of snow by salt, the desalination of seawater by reverse osmosis, the separation and purification of volatile liquids by fractional distillation, and the determination of molecular mass by osmotic pressure measurement. [Pg.462]

If you have distilled your product to isolate and purify it then you should already have the information required for reporting the boiling point It is important to quote the range of temperature (if observed) over which the compound distils, the pressure (measured as it is distilling), the vapour temperature (if measured), and the bath temperature. All these will be useful when you or anyone else come to repeat the work, and most of this information will be required at some time for a publication, report, or thesis. [Pg.255]

The chelates can be purified, and mixtures of the complexes can be separated by fractional sublimation and distillation. In the gas phase, in solution, and in the solid state, Tb(thd)3 emits a brilliant green fluorescence when irradiated at 3660 A. with an ultraviolet lamp. Fluorescence is also exhibited by Eu(thd)3, Dy(thd)3, and Sm(thd)3. The praseodymium complex is thermally stable in the gas phase when heated for prolonged periods of time. Vapor pressure measurements on this complex showed no increase in pressure when the sample was heated at 250° for 6 hours. Thermogravimetric analyses and discussions of trends in volatility of the rare-earth-thd chelates have been published. [Pg.98]

The measurement of pressure at the top of the distillation column is critical to valid distillation results because the observed vapor temperature must be corrected to the atmospheric equivalent temperature at standard pressure conditions (760mmHg). There is a general belief that the minimum pressure should be 2mmHg or greater for reasonably accurate measurements and correction to the atmospheric equivalent temperature. At pressures below 2mmHg, the pressure measurement is too inaccurate and a discontinuity can arise in the atmospheric equivalent temperature distillation curve from atmospheric to vacuum distillation. [Pg.132]

The compression or decompression of bovine serum albumin monolayers spread on an aqueous substrate at a pH near the isoelectric point can effect surface tension. The surface pressure changes depend on the distance between the position of the surface pressure measuring device and the compression barrier. This effect is minimal at a pH above or below the isoelectric point and undetected for small molecules (myristic acid and eicosyl sodium sulfate) even when the substrate contains substituted alkyl amines. A theory is proposed which attributes the above observation to surface drag viscosity or the dragging of a substantial amount of substrate with the BSA monolayer. This assertion has been experimentally confirmed by measuring the amount of water dragged per monolayer using the technique of surface distillation. [Pg.268]

The water was distilled twice from glass (initially from alkaline permanganate). It was subsequently twice distilled from quartz. Surface areas at most pressures were reproducible within 0.5 A2/molecule however, at low pressures, for gaseous isotherms, the error was somewhat greater. Surface potentials were also obtained but are not reported here. Surface potential values, however, confirm observations made with surface pressure measurements (8). [Pg.305]

The initial number average molecular weights (Mn) for the poly-(amic-acids) were between 10,000 and 20,000, and no attempt was made to optimize them. Dimethylacetamide solvent was distilled from calcium hydride under vacuum and stored under nitrogen. The resin solutions were stored also under nitrogen. The water content of the solvent was measured with a Porapak Q column in a Hewlett Packard 5750 gas chromatograph. Unless otherwise stated, the water concentration in the solvent remained below 0.05 vol %. Mn was determined from osmotic pressure measurements on a Hewlett Packard-Mechrolab 502 osmometer using ArRo Lab gel cellophane 600D membranes. [Pg.205]

Let us assume that we wish to separate a mixture of the Cg and C7 normal fatty acids, the mixture containing 81 mol% of the Cg component, and that we have to determine the number of separating stages necessary to obtain a top product of 96mol% and a bottom product of 0.5 mol% concentration. The distillation pressure is to be 20 mm Hg. The equilibrium curve for this mixture has not yet been measured it was calculated by formula (58) with tx = 2.10 (Fig. 63). [Pg.113]

Pressure measurement is a critical factor not only in the oil and gas industry but also for the operation of process equipment including reactors, distillation columns, pipelines, and for the measurement of flow rate. It is a scalar quantity and equals the perpendicular force exerted on a surface with the units of force per surface area ... [Pg.108]


See other pages where Distillation pressure measurement is mentioned: [Pg.747]    [Pg.309]    [Pg.10]    [Pg.8]    [Pg.9]    [Pg.228]    [Pg.67]    [Pg.43]    [Pg.87]    [Pg.43]    [Pg.571]    [Pg.115]    [Pg.918]    [Pg.1620]    [Pg.262]    [Pg.45]    [Pg.296]    [Pg.66]    [Pg.548]    [Pg.923]    [Pg.1616]    [Pg.40]    [Pg.94]    [Pg.162]    [Pg.167]    [Pg.341]    [Pg.354]    [Pg.444]    [Pg.751]    [Pg.157]   
See also in sourсe #XX -- [ Pg.132 ]




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