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Water, free

Leaving the refinery, jet fuel has generally no free water and contains only a small quantity of dissolved water. But humidity from the air and tank breathing result in continuous intrusion of water that must be then removed by decanting and filtration. This is why jet fuel needs to be tested for its ability to separate the contained water. [Pg.250]

For jet fuels, the elimination of free water using filters and coalescers by purging during storage, and the limit of 5 ppm dissolved water are sufficient to avoid incidents potentially attributable to water contamination formation of micro-crystals of ice at low temperature, increased risk of corrosion, growth of micro-organisms. [Pg.250]

Under certain conditions of temperature and pressure, and in the presence of free water, hydrocarbon gases can form hydrates, which are a solid formed by the combination of water molecules and the methane, ethane, propane or butane. Hydrates look like compacted snow, and can form blockages in pipelines and other vessels. Process engineers use correlation techniques and process simulation to predict the possibility of hydrate formation, and prevent its formation by either drying the gas or adding a chemical (such as tri-ethylene glycol), or a combination of both. This is further discussed in SectionlO.1. [Pg.108]

This property is useful in helping to define the interface between fluids. The intercept between the gas and oil gradients indicates the gas-oil contact (GOG), while the intercept between the oil and water gradients indicates the free water level (FWL) which is related to the oil water contact (OWC) via the transition zone, as described in Section 5.9. [Pg.117]

In a reservoir at initial conditions, an equilibrium exists between buoyancy forces and capillary forces. These forces determine the initial distribution of fluids, and hence the volumes of fluid in place. An understanding of the relationship between these forces is useful in calculating volumetries, and in explaining the difference between free water level (FWL) and oil-water contact (OWC) introduced in the last section. [Pg.120]

The capillary pressure can be related to the height of the interface above the level at which the capillary pressure is zero (called the free water level) by using the hydrostatic pressure equation. Assuming the pressure at the free water level is PI ... [Pg.122]

This is consistent with the observation that the largest difference between the oil-water interface and the free water level (FWL) occurs in the narrowest capillaries, where the capillary pressure is greatest. In the tighter reservoir rocks, which contain the narrower capillaries, the difference between the oil-water interface and the FWL is larger. [Pg.123]

If a pressure measuring device were run inside the capillary, an oil gradient would be measured in the oil column. A pressure discontinuity would be apparent across the interface (the difference being the capillary pressure), and a water gradient would be measured below the interface. If the device also measured resistivity, a contact would be determined at this interface, and would be described as the oil-water contact (OWC). Note that if oil and water pressure measurements alone were used to construct a pressure-depth plot, and the gradient intercept technigue was used to determine an interface, it is the free water level which would be determined, not the OWC. [Pg.123]

Finally, it is worth remembering the sequence of events which occur during hydrocarbon accumulation. Initially, the pores in the structure are filled with water. As oil migrates into the structure, it displaces water downwards, and starts with the larger pore throats where lower pressures are required to curve the oil-water interface sufficiently for oil to enter the pore throats. As the process of accumulation continues the pressure difference between the oil and water phases increases above the free water level because of the density difference between the two fluids. As this happens the narrower pore throats begin to fill with oil and the smallest pore throats are the last to be filled. [Pg.124]

The most common contaminants in produced gas are carbon dioxide (COj) and hydrogen sulphide (HjS). Both can combine with free water to cause corrosion and H2S is extremely toxic even in very small amounts (less than 0.01% volume can be fatal if inhaled). Because of the equipment required, extraction is performed onshore whenever possible, and providing gas is dehydrated, most pipeline corrosion problems can be avoided. However, if third party pipelines are used it may be necessary to perform some extraction on site prior to evacuation to meet pipeline owner specifications. Extraction of CO2 and H2S is normally performed by absorption in contact towers like those used for dehydration, though other solvents are used instead of glycol. [Pg.252]

Before use, the marble chips are washed repeatedly with hot water, and then de-aerated by first etching them with concentrated hydrochloric acid and then boiling them with air-free water under reduced pressure. The chips are then rapidly transferred to the generator small chips should be used and the bulb... [Pg.482]

In superacidic systems, water is completely protonated and no equilibrium containing free water is indicated. However, the nonbonded electron pair of H30 is still a potential electron donor and at very high acidities can be further protonated (however limited the equilibrium with H30 may be). Thus the acidity of such superacidic systems can exceed that of H30 and the leveling ont is by that of H40 . We found that similar situations exist with other electrophiles, raising their electrophilic nature (electrophilicity) substantially. [Pg.192]

A sample blank of trihalomethane-free water can be kept with the samples at all times. If the sample blank shows no evidence for chloroform, then we can safely assume that the samples also are free from contamination. [Pg.577]

Dissolved matter lowers oxygen solubihty. At 20°C and 101.3 kPa (1 atm), the equihbrium concentration of dissolved oxygen in seawater is 7.42 mg/L. It is 9.09 mg/L in chloride-free water and 9.17 mg/L in clean water. This lessening of oxygen solubihty is of importance to wastewater treatment. The solubihty of atmospheric oxygen in a domestic sewage is much less than in distilled water (12). [Pg.339]

Polycarbophil binds free water and, therefore, increases the fluidity of stools. It is most active in the slightly acid or alkaline medium of the small... [Pg.200]

Dime putty is a form of lime hydrate in a wet, plastic paste form, containing free water. [Pg.164]

Solubility. High calcium limestone is only very faintly soluble in water. In cold C02-free water it is often regarded as insoluble. Between 17 and... [Pg.166]

Solid-Bed Dehydration. Sihca gel, bauxite, activated alurnina, or molecular sieves can be used for removing dissolved water to meet propane specifications. The soHd-bed dehydrators are used in a cycHc adsorption process. After an adsorption cycle has completed, the bed is heated with a purge gas or a vaporized Hquid-product stream for regeneration. If the latter is used, the Hquid product is condensed, separated from the free water, and returned to the process. After the beds are regenerated, they are cooled and returned to the adsorption cycle. [Pg.185]

Metallic magnesium and water [7732-18-5] react. Under normal atmospheric conditions or in pure or chloride-free water of high pH, the reaction is suppressed by the formation of an insoluble magnesium hydroxide [1309-42-8] film. [Pg.314]

Properties. The physical properties of the normal magnesium carbonates are given in Table 3, those of the basic magnesium carbonates in Table 4. Magnesium carbonate is insoluble in C02-free water. The solubiUty products, iC, for magnesium carbonate and some hydrates foUow (38). [Pg.341]

Drying a.nd Calcination. The simplest pyrometaHurgical operation is the evaporation of free water and the decomposition of hydrates and carbonates. A typical reaction is the decomposition of pure limestone [1317-65-3] CaCO, to calcium oxide [1305-78-8] and carbon dioxide ... [Pg.164]

The dielectric properties of most foods, at least near 2450 MH2, parallel those of water, the principal lossy constituent of food (Fig. 1). The dielectric properties of free water are well known (30), and presumably serve as the basis for absorption in most foods as the dipole of the water molecule interacts with the microwave electric field. By comparison, ice and water of crystaUi2ation absorb very Httie microwave energy. Adsorbed water, however, can retain its Hquid character below 0°C and absorb microwaves (126). [Pg.344]

At equihbrium, the specific composition of a concentrated phosphoric acid is a function of its P2 s content. Phosphoric acid solutions up to a concentration equivalent of about 94% H PO (68% P2O5) contain H PO as the only phosphoric acid species present. At higher concentrations, the orthophosphoric acid undergoes condensation (polymerization by dehydration) to yield a mixture of phosphoric acid species (Table 5), often referred to genericaHy as polyphosphoric or superphosphoric acid, H20/P20 = - 3, or ultraphosphoric acid, H20/P20 = - 1. At the theoretical P2O5 concentration for orthophosphoric acid of 72.4%, the solution is actually a mixture containing 13% pyrophosphoric acid and about 1% free water. Because the pyrophosphoric acid present is the result of an equihbrium state dependent on the P2 5 content of the solution, pure orthophosphoric acid can be obtained because of a shift in equihbrium back to H PO upon crystallization. [Pg.328]


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Addition polymerization, water-soluble free-radical

Air-free water

Analyte-free water blanks

Anion-free water

Bound and Free Water Molecules

Carbon Dioxide-Free Water

Carrier-free 1od1ne-l33, preparation from neutron-irradiated tellurium 1n water

Carrier-free 1od1ne-l33, preparation from neutron-irradiated tellurium in reactor cooling water

Catalyst-Free Strecker Reactions in Water

Cement free slurry water

Chromium-free, Iron-catalysed Water Gas Shift

Coal water-free

Dihydrogen water-free activation

Flow rate free-water approach

Flux removal from printed circuit boards - water-free cleaning processes

Free energy change primary water

Free energy change secondary water

Free energy of water

Free in water

Free movable water

Free radicals water effects

Free water clearance and renal concentrating ability

Free water definition

Free water level

Free water molecules

Free water molecules definition

Free water porosity

Free-energy barrier for escape of water molecules from protein hydration layer

Free-water knockouts

Hydrolysis water-free process

Ion-free water

Lipid-water interfacial free energy

Muscle free water

Preparation of water free from carbonic acid

Production of Pyrogen-free Water

Synthesis water-free zeolite

Water free energy

Water free energy calculations

Water free energy’ change

Water free molecule, normal modes

Water free radicals derived from

Water free-draining

Water hydration, free energy change

Water removal, free energy consequence

Water, volume, free

Water-free and high solid finishing formulations

Water-free cleaning processes in closed, one-chamber vapor defluxing systems

Water-free cleaning processes using HFE (hydrofluoroethers) in combination with a cosolvent

Water-free powders

Water-free products

Water-soluble free-radical addition

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