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Water equilibrium

S. C. Sharma, "Equilibrium Water Content of Gaseous Mixtures," Ph.D. dissertation. University of Oklahoma, Norman, 1969. Available from University Microfilms, Ann Arbor, Mich., order 69-8601. [Pg.517]

N. Y., 3rd edn, 1970]. Acetone was shaken with Drierite (25g/L) for several hours before it was decanted and distd from fresh Drierite (lOg/L) through an efficient column, maintaining atmospheric contact through a Drierite drying tube. The equilibrium water content is about lO M. Anhydrous Mg(C104)2 should not be used as drying agent because of the risk of EXPLOSION with acetone vapour. [Pg.84]

The nylons are hygroscopic. Figure 18.16 shows how the equilibrium water absorption of different nylons varies with humidity at room temperature. Figure 18.17 shows how the rate of moisture absorption is affected by the environmental conditions. [Pg.495]

Surface resistivity (of unexposed samples) Equilibrium water absorption... [Pg.862]

Figure 8-9. Equilibrium water dew points at different temperatures for gases. Figure 8-9. Equilibrium water dew points at different temperatures for gases.
Before dealing with these, it is necessary to refer briefly to the stability of thiosulphate solutions. Solutions prepared with conductivity (equilibrium) water are perfectly stable. However, ordinary distilled water usually contains an excess of carbon dioxide this may cause a slow decomposition to take place with the formation of sulphur ... [Pg.391]

When a solid, such as ice, is in contact with its liquid form, such as water, at certain conditions of temperature and pressure (at 0°C and 1 atm for water), the two states of matter are in dynamic equilibrium with each other, and there is no tendency for one form of matter to change into the other form. When solid and liquid water are at equilibrium, water molecules continually leave solid ice to form liquid water, and water molecules continually leave the liquid phase to form ice. However there is no net change, because these processes occur at the same rate and so balance each other. [Pg.411]

In contrast to TMC-DLLA, the mechanical properties at equilibrium water uptake of TMC-CL copolymers are not significantly different from those in the dry state as shown in Table 8.1. [Pg.230]

The water concentration in the unpigmented paint appears to be 0.14Z (m/m). In Table I the equilibrium water concentrations in paint films are given, 30-60 min after spraying, in dependence on the relative humidity. [Pg.233]

Table I. Equilibrium water concentrations In an unplgmented paint layer at different relative humidities (22 C) one hour after spraying... Table I. Equilibrium water concentrations In an unplgmented paint layer at different relative humidities (22 C) one hour after spraying...
The equilibrium relationships found by Sorrell (1977) were valid only for room temperature (22+2 °C) and, because samples were allowed to cure in sealed containers, for equilibrium water vapour pressures determined by the assembly of phases present. The phases which exist under such conditions were quite unequivocally found to be 4 1 5 and 1 1 2. However Sorrell pointed out that it is entirely possible that lower hydration states of either phase could be stable at higher temperatures or lower humidities. In particular the 4 1 4 phase (Feitknecht, 1933) may well be such a phase, particularly as one of the five waters of hydration is known to be held only loosely in the structure. Indeed, Sorrell reported that he observed a slight shoulder on the larger dehydration peak of the DTG curve of the 4 1 5 phase that might be assigned to the loss of this first water molecule. He did not, however, succeed in isolating or characterizing a 4 1 4 phase. [Pg.288]

Further stability models based on surface area, equilibrium water-content-pressure relationships, and electric double-layer theory can successfully characterize borehole stability problems [1842]. The application of surface area, swelling pressure, and water requirements of solids can be integrated into swelling models and mud process control approaches to improve the design of water-based mud in active or older shales. [Pg.62]

The equilibrium water vapor pressure over the materials in hydrate forms is greater than that over the materials in hydroxide forms. Elimination of water vapor and hence drying of the material occurs when the ambient water vapor pressure in the system is lower than the equilibrium water vapor pressures given by the above equations. To effect drying, there are two options. [Pg.344]

At a given ambient water vapor pressure (usually the level found in the open atmosphere), the temperature of the material is raised so that the equilibrium water vapor pressure over the hydrated material is higher than the ambient water vapour pressure. Generally, heating up to 400 °C is sufficient to remove all the water of crystallization from materials. This removal of water yields a material which may contain some more strongly bound water. To remove this water, the material requires to be heated to a higher temperature (400-600 °C) so that the equilibrium water vapour pressure exceeds the ambient water vapour pressure. For near-complete removal of the last traces of water, temperatures as high as 1000 °C may be required. In addition to the heat required to raise the temperature of the material, heat is also required for the evaporation of water, which is an endothermic process. The enthalpy of evaporation increases as the water content, and hence the equilibrium water vapor pressure, decreases. [Pg.344]

The other option available for drying involves subjecting the material to reduced pressures. By decreasing the ambient pressure, for example, by evacuation, to a level lower than the equilibrium water vapor pressure over the material, drying can be implemented. This option is particularly important when heating affects the material, in addition to drying it. [Pg.344]

Table 1.11 Equilibrium water vapor pressure of ice and the related specific density of the vapor (from [1.109]). Table 1.11 Equilibrium water vapor pressure of ice and the related specific density of the vapor (from [1.109]).
Fig. 1.101. Equilibrium water content in two different freeze dried products, each with two different amounts of product per vial. The equilibrium data are extrapolated from the +25 °C, respectively from the +40 °C values. SV1, U, SV8 see Fig. 1.100. Fig. 1.101. Equilibrium water content in two different freeze dried products, each with two different amounts of product per vial. The equilibrium data are extrapolated from the +25 °C, respectively from the +40 °C values. SV1, U, SV8 see Fig. 1.100.
Step 1. The substrate, RH, associates with the active site of the enzyme and perturbs the spin-state equilibrium. Water is ejected from the active site and the electronic configuration shifts to favor the high-spin form in which pentaco-ordinated heme Fe3+ becomes the dominant form-binding substrate. In this coordination state, Fe3+ is puckered out and above the plane in the direction of the sixth ligand site. The change in spin state alters the redox potential of the system so that the substrate-bound enzyme is now more easily reduced. [Pg.36]

An interesting point arises from this method. The particles of material are exposed to water vapour at a set humidity and hence the results equate to that humidity. The measured equilibrium absorption is substantially the same as the equilibrium absorption that would be obtained by immersion in an aqueous solution which would maintain the test humidity. As this implies, the equilibrium water absorption is reduced if the water is not pure. Hence, exposure to aqueous solutions should be made at the concentration of interest. As the humidity approaches 100% even small amounts of a salt have a significant effect on equilibrium absorption. [Pg.69]

BS 903-18, Physical testing of rubber. Determination of equilibrium water vapour absorption, 1973. [Pg.80]

The subsequently presented model of water sorption in PEMs reconciles vapor sorption and porosity data. At sufficiently large water contents exceeding the amount of surface water, T > equilibrium water uptake is controlled by capillary forces. Deviations from capillary equilibrium arising at A < can be investigated by explicit ab initio calculations of water at dense interfacial arrays of protogenic surface groups. ° In the presented model, the problem of Schroeder s paradox does not arise and there is no need to invoke vapor in pores or hydrophobicity of internal channels. Here, we will present a general outline... [Pg.371]

In an early study, Mauritz et al. investigated anion—cation interactions within Nation sulfonate membranes versus degree of hydration using FTIR/ ATR and solid state NMR (SSNMR) spectroscopies. An understanding of the dynamic ionic—hydrate molecular structures within and between the sulfonate clusters is essential for a fundamental understanding of the action of these membranes in ion transport. This information can be directly related to the equilibrium water swelling that, in turn, influences molecular migration. [Pg.323]

Figure 7. Equilibrium water-uptake or isotherm curve at 30 °C. The dashed line signifies the effect of Schroeder s paradox, a change in water uptake at the same chemical potential depending on the phase of water next to the membrane liquid is at A = 22. Figure 7. Equilibrium water-uptake or isotherm curve at 30 °C. The dashed line signifies the effect of Schroeder s paradox, a change in water uptake at the same chemical potential depending on the phase of water next to the membrane liquid is at A = 22.
Figure 4. Equilibrium water uptake curve for Nafion membrane (a) measurement at 30 (b) measurement... Figure 4. Equilibrium water uptake curve for Nafion membrane (a) measurement at 30 (b) measurement...
Sorption has been commonly described as an equilibrium process, in which the pesticide molecules are rapidly and readily exchanged between the sediment and aqueous phases. In this approach ( ), the equilibrium water phase concentration, (expressed relative to suspension volume) is related to the sediment phase concentration, (expressed relative to dry weight sediment), through... [Pg.223]

The most important and almost ubiquitous modulator is water. The modulating property of water was recognized early, and numerous attempts have been made to standardize the water content of adsorbents (9,40) and to relate it to the equilibrium water content of eluents (41, 42). The proce-... [Pg.42]

Trolard and Tardy (1987) calculated an equilibrium water activity of ca. 0.6 at 5 °C, 0.78 at 15 °C, 0.88 at 25 °C and 0.9 at 40 °C. At higher temperatures, hematite should be the stable phase even at an an2o of unity. Experimental confirmation of the importance of the relative humidity on the direction of the reaction is provided by the work of Torrent et al. (1982). This study also demonstrated that at aH2o < tho transformation offerrihydrite into more stable phases is very slow. [Pg.197]

While water is a major component of tropospheric particles, and hence largely determines the surface tension (y), organics found in particles may act as surfactants (see Chapter 9.C.2). In this case, their segregation at the air-water interface could potentially lead to a substantial surface tension lowering of such particles, which would lead to a lower equilibrium water vapor pressure over the droplet (Eq. (BB)) and hence activation at smaller supersaturations. This possibility is discussed in more detail in the next section. [Pg.801]

Fig. 6. Equilibrium water uptake of P(DEAEA-co-HEMA) samples with 30% (O) and 60% ( ) DEAEA with a crosslinking ratio of 0.003 mol EGDMA/mol monomers in a citrate-borate buffer solution as a function of pH... Fig. 6. Equilibrium water uptake of P(DEAEA-co-HEMA) samples with 30% (O) and 60% ( ) DEAEA with a crosslinking ratio of 0.003 mol EGDMA/mol monomers in a citrate-borate buffer solution as a function of pH...

See other pages where Water equilibrium is mentioned: [Pg.97]    [Pg.208]    [Pg.35]    [Pg.356]    [Pg.214]    [Pg.39]    [Pg.403]    [Pg.506]    [Pg.11]    [Pg.115]    [Pg.25]    [Pg.422]    [Pg.321]    [Pg.432]    [Pg.499]    [Pg.222]    [Pg.45]    [Pg.210]    [Pg.80]    [Pg.573]    [Pg.411]   
See also in sourсe #XX -- [ Pg.123 ]

See also in sourсe #XX -- [ Pg.333 ]

See also in sourсe #XX -- [ Pg.377 , Pg.378 , Pg.379 ]

See also in sourсe #XX -- [ Pg.24 ]




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Acetone-Methanol-Water Phase Equilibrium

Acetone/water equilibria

Acid-Base Equilibria in Water Ostwalds Dilution Law

Acid-base equilibria anion reaction with water

Acid-base equilibria autoionization of water

Acid-base equilibria cation reaction with water

Acid-base equilibria in water

Acid-base equilibria ion-product constant for water

Air-Water Equilibrium Conditions

Air-Water-Microlayer Equilibrium

Air-water equilibrium

Ammonia-Water Equilibrium

Ammonia-water equilibrium curve

Ammonia/water phase equilibrium

Ammonium bromide-ethanol-water isobaric vapor-liquid equilibrium

Calcite-water equilibrium

Carbon Dioxide-Water Equilibrium

Carbon dioxide equilibrium with water

Carbon dioxide water-atmosphere equilibrium

Chemical Equilibria in Mineral Water

Chemical equilibrium water ionization

Dimethyl sulfoxide, water, equilibrium

EQUILIBRIUM CONCEPTS IN NATURAL WATER SYSTEMS

Equilibrium between ferric chloride, hydrochloric acid, and water

Equilibrium composition of natural waters

Equilibrium constant for water

Equilibrium constant water

Equilibrium constant water exchange

Equilibrium in Pure Water

Equilibrium in natural waters

Equilibrium models of natural waters

Equilibrium of a Flat Pure Water Surface with the Atmosphere

Equilibrium of a Flat Water Solution

Equilibrium of a Pure Water Droplet

Equilibrium of water

Equilibrium partition coefficients waters

Equilibrium relationships, water-mineral

Equilibrium sour water

Equilibrium water activity

Equilibrium water effed

Equilibrium water fraction

Equilibrium water saturation

Equilibrium water uptake

Equilibrium, apparent water

Equilibrium, apparent water, vapour

Equilibrium-partitioning coefficient octanol-water

Equilibrium-partitioning coefficient water-solid

Ethanol-water equilibria

Ethanol-water vapour-liquid equilibria

Examples for Calculation of the Calcite-Carbonate-Equilibrium in Ocean Waters

Experimental approach of equilibriums between water vapor and hydrated salts

Fluid Phase Equilibria Involving Water

Formation water equilibrium crystallization

Gases equilibrium with water

Glucose equilibrium mixture in water

Ice-water equilibrium

Isobaric vapor-liquid equilibrium potassium acetate-ethanol-water

Kinetics and Equilibria of Arenediazonium Ions in Water

Methane Content of Water in Equilibrium with Hydrates

Methanol-water equilibrium constant

Methylethylketone/water equilibria

Natural water, chemical equilibria

Nitric Acid-Water Equilibrium

Phase equilibria lipid-water systems

Pure liquid compound-water equilibrium

Sucrose, equilibrium water content

Sulfur Dioxide-Water Equilibrium

The Water Equilibrium

The Water-Gas Equilibrium

Vapor equilibrium technique water control

Vapor-liquid equilibrium curve for the ethanol-water system

Vapor-liquid equilibrium data acetone/water

Vapor-liquid equilibrium data butanol/water

Vapor-liquid equilibrium data ethanol/water

Vapor-liquid equilibrium data methylethylketone/water

Vapor-liquid equilibrium ethanol-water

Vapor-liquid equilibrium water-benzene

Water Content of Liquid Hydrocarbon in Equilibrium with Hydrates

Water Content of Vapor in Equilibrium with Hydrate

Water Effects on Equilibria

Water Equilibrium in the Atmosphere

Water dissociation equilibrium

Water droplet equilibrium

Water dynamic equilibrium

Water equilibrium calculations

Water equilibrium condition

Water equilibrium content

Water equilibrium freezing point

Water equilibrium measurements

Water equilibrium state

Water equilibrium vapor pressure equation

Water in equilibrium

Water ionisation equilibrium

Water phase equilibria

Water sorption capillary equilibrium

Water sorption equilibrium conditions

Water sorption, equilibrium

Water thermodynamic equilibrium

Water vapor-liquid equilibrium runs

Water vapour, equilibrium pressure

Water, crystal structure equilibrium between phases

Water-hydrogen sulfide system, liquid-vapor equilibria

Water-undersaturated equilibria

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