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Systems aqueous

Aqueous systems are by far the most common environments to which corrosion inhibitors are applied. Water is a powerful solvent capable of carrying many different ions at the same time, so requirements [Pg.137]

The main factors that may be considered in the application of corrosion inhibitors to aqueous systems are salt concentration, pH, dissolved oxygen concentration, and the concentrations of interfering species. [Pg.138]

To carry out SFEIP in homogeneous aqueous solutions, the radical mediator, as also the monomer and the polymers, should be soluble in the medium. A number of water-soluble monomers have been polymerized by the living radical process (Qiu et al., 2001). They include uncharged monomers, such as 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, oligo(ethylene glycol) methacrylate, 2-(dimethylamino)ethylmethacrylate, acrylic acid, etc., and charged/ionic monomers, such as sodium methacrylate, sodium vinylbenzoate (NaVBA) and sodium styrene sulfonate (NaSS). [Pg.592]

CRP/LRP methods have been applied in miniemulsion polymerization as it offers some unique technical advantages over an emulsion polymerization and can be regarded as a simpli ed model of emulsion polymerization, in which, ideally, all monomer droplets (of 50-500 nm size) are nucleated by entering aqueous oligoradicals and become polymer particles, while no new particles are nucleated by homogeneous nucleation, thus leading to simpler kinetic behavior. [Pg.592]

A major problem of CRP in emirlsion systems is that the process often leads to unstable latexes, mainly due to the sensitivity of the nucleation step, and is therefore still a challenge (Qiu et al., 2001 Cunningham, 2002 Charleux, 2003). The formation of unstable latexes has been explained by some very sped c features of the chain growth in CRP with respect to a classical free-radical polymerization, namely, slow and simultaneous growth of a large number of oligomers in the early stage of polymerization, which completely modi es the mechanism of particle formation. [Pg.592]

More recently, the CRP method has been improved signi cantly with the discovery of very ef cient acyclic nitroxides such as the stable acyclic phosphonylated nitroxide radical SGI (Fig. 11.15), which can control the polymerization of much broader range of monomers than cyclic nitroxides like TEMPO. The radical SGI has a larger equilibrium constant than most other nitroxides, including TEMPO, and is therefore suitable for polymerization temperatures as low as 90°C (SGI K = 1.9x10 mol dm at 125°C TEMPO K = 2.1x10 moldm- at 125°C). [Pg.593]

When water turns to ice does remember one time it was water When ice turns back into water does it remember it was ice  [Pg.73]

We have introduced the use of cellular automata modeling of water and possibly some other solvent, and have observed the influence of solutes on the emergence of properties in these complex systems. In this chapter we consider a few, more complex chemical systems that may lend themselves to cellular automata modeling. We will discuss several of these and then suggest some studies for the reader. [Pg.73]

The behavior of two liquids that are sparsely soluble in each other is a familiar one to any experimental chemist. If we shake ether and water in a separatory funnel and observe the system at equilibrium, we see that the liquids have settled in two layers. The reader is asked to identify which liquid is the bottom layer. If water and chloroform are shaken, the system again equilibrates [Pg.73]

In order, for the two liquids to separate into two phases, they must be very weakly soluble in each other. When exposed to each other by mixing or shaking in a separatory funnel, they may not interpenetrate each other s realm to any extent. At the molecular level, we infer that the two species of molecules have no significant affinity for each other, rather they are predominantly attracted to other molecules with the same structure. To model this aversion, the joining and breaking rules must encode this behavior. The cells of liquids X and Y must respond to rules typified by those shown in the parameter setup tables below. With these rules we anticipate that liquid X will favor associating with other X molecules, while molecule Y will be found predominantly among other Y molecules. [Pg.74]

It is observed that the CA dynamics, with these rules, results in a pattern in which clusters of X are scattered among clusters of Y. This is not what is seen in the laboratory. In reality, two immiscible liquids will separate into two layers, each responding to a different influence from gravity. What the CA model shows is the separation experienced in the weightlessness of space. A gravity rule must be added. [Pg.74]

The implications of the versatile reaction mechanisms depicted in Figs. 7-1 to 7-4 are profound with respect to the complete understanding and hence to the kinetic modeling of AOPs. Despite the complexity of these photo-initiated reactions, it is possible to model AOPs with sufficient precision if all the rate constants of OH radical reactions involved and those of all other elementary reactions are known (Crittenden et al., 1999). Most importantly, the structures and the concentrations of all intermediary reaction products must be known. In addition, photoreactor specific parameters have to be included, such as the incident photon flow d p and the dimensions of the irradiated volume. This task can be achieved for example [Pg.191]

The difficulties related to the elaboration of a complete reaction scheme of an AOP were demonstrated by Stefan et al. (1996) who investigated the oxidative de- [Pg.192]

Formic Acid Acetic Acid Oxalic Acid 4 [Pg.193]

COOH Pyruvic Acid (PA) CH3COOH Acetic Acid (AA) [Pg.193]

In a similar way a series of C5 to Ci intermediate products were identified during the H2O2-UV treatment of MTBE in aqueous solution (Tab. 7-1). This list of compounds demonstrates again the extraordinary complexity of reactions underly- [Pg.196]


HyperChem allows solvation of arbitrary solutes (including no solute) in water, to simulate aqueous systems. HyperChem uses only rectangular boxes and applies periodic boundary conditions to the central box to simulate a constant-density large system. The solvent water molecules come from a pre-equilibrated box of water. The solute is properly immersed and aligned in the box and then water molecules closer than some prescribed distance are omitted. You can also put a group of non-aqueous molecules into a periodic box. [Pg.201]

Other Propellants. Dimethyl ether (DME) [115-10-6] is finding use as an aerosol propeUant. DME is soluble in water, as shown in Table 5. Although this solubiHty reduces DME s vapor pressure in aqueous systems, the total aerosol solvent content may be lowered by using DME as a propeUant. The chief disadvantage is that DME is flammable and must be handled with caution. [Pg.348]

Biopolymer Extraction. Research interests involving new techniques for separation of biochemicals from fermentation broth and cell culture media have increased as biotechnology has grown. Most separation methods are limited to small-scale appHcations but recendy solvent extraction has been studied as a potential technique for continuous and large-scale production and the use of two-phase aqueous systems has received increasing attention (259). A range of enzymes have favorable partition properties in a system based on a PGE—dextran—salt solution (97) ... [Pg.80]

Thermochemical Liquefaction. Most of the research done since 1970 on the direct thermochemical Hquefaction of biomass has been concentrated on the use of various pyrolytic techniques for the production of Hquid fuels and fuel components (96,112,125,166,167). Some of the techniques investigated are entrained-flow pyrolysis, vacuum pyrolysis, rapid and flash pyrolysis, ultrafast pyrolysis in vortex reactors, fluid-bed pyrolysis, low temperature pyrolysis at long reaction times, and updraft fixed-bed pyrolysis. Other research has been done to develop low cost, upgrading methods to convert the complex mixtures formed on pyrolysis of biomass to high quaHty transportation fuels, and to study Hquefaction at high pressures via solvolysis, steam—water treatment, catalytic hydrotreatment, and noncatalytic and catalytic treatment in aqueous systems. [Pg.47]

Pressure sensitive adhesives typically employ a polymer, a tackifier, and an oil or solvent. Environmental concerns are moving the PSA industry toward aqueous systems. Polymers employed in PSA systems are butyl mbber, natural mbber (NR), random styrene—butadiene mbber (SBR), and block copolymers. Terpene and aUphatic resins are widely used in butyl mbber and NR-based systems, whereas PSAs based on SBR may require aromatic or aromatic modified aUphatic resins. [Pg.358]

M. Rafal and S. J. Sanders, "The ProChem System for Modeling/Simulation of Aqueous Systems," Proceedings of the Second International Mirlie House Conference onMqueous Systems, Warrenton, Va., May 10—14,1987. [Pg.60]

Several aqueous systems should be considered in a similar manner. For example, in the selective removal of divalent cations from a saturated salt solution, the hydrated resin gives up a portion of its normal water content as it contacts the salt stream. In so doing, the particles shrink, and the inner pathways for ion migration become smaller. [Pg.379]

Zeohtes are formed under hydrothermal conditions, defined here in a broad sense to include 2eoHte crystalli2ation from aqueous systems containing various types of reactants. Most synthetic 2eoHtes are produced under nonequilihrium conditions, and must be considered as metastable phases in a thermodynamic sense. [Pg.451]

Calcium Peroxide. Pure calcium peroxide [1305-79-9] Ca02, has been prepared, but the commercial product is a mixture made by reaction of calcium hydroxide and hydrogen peroxide. Commercial material contains either 60 or 75% Ca02 the remainder is a poorly defined mixture of calcium oxide, hydroxide, and carbonate. A well-defined octahydrate [60762-59-6] 8H20, can be crysta11i2ed from aqueous systems. [Pg.91]

The principal use of the peroxodisulfate salts is as initiators (qv) for olefin polymerisation in aqueous systems, particularly for the manufacture of polyacrylonitrile and its copolymers (see Acrylonitrile polymers). These salts are used in the emulsion polymerisation of vinyl chloride, styrene—butadiene, vinyl acetate, neoprene, and acryhc esters (see Acrylic ester polymers Styrene Vinyl polymers). [Pg.96]

Among the properties sought in the solvent are low cost, avadabihty, stabiUty, low volatiUty at ambient temperature, limited miscibility in aqueous systems present in the process, no solvent capacity for the salts, good solvent capacity for the acids, and sufficient difference in distribution coefficient of the two acids to permit their separation in the solvent-extraction operation. Practical solvents are C, C, and alcohols. For industrial process, alcohols are the best choice (see Amyl alcohols). Small quantities of potassium nitrate continue to be produced from natural sources, eg, the caUche deposits in Chile. [Pg.536]

In an aqueous system with large particles weU-separated by a distance, s, (D and 5 > t ) the electrostatic repulsion energy between two identical charged spheres may be approximated (1) ... [Pg.545]

If an adsorbed chemical group (anchor) is more strongly bound to the surface than a solvent molecule would be at that site, an equiHbrium expression may be written for the displacement of solvent by adsorbate. Adsorption is particularly strong if the chemical nature of the adsorbed group is similar to that of the particle surface for example, in aqueous systems perfluoroalkane groups adsorb weU on polytetrafluoroethene particles and aromatic polyethene oxides adsorb weU on polystyrene. [Pg.547]

Short-Chain Organics. Adsorption of an organic dispersant can reduce polarizabiHty attraction between particles, ie, provide semisteric stabilization, if A < A.p < A or A < A.p < A (T = dispersant) and the adsorption layer is thick. Adsorption in aqueous systems generally does not foUow the simple Langmuir profile because the organic tails on adsorbed molecules at adjacent sites attract each other strongly. [Pg.547]

A. R. Marsh, G. Klein, and T. Vermeulen, Polymerisation Kinetics and Equilibria of Silicic Acid in Aqueous Systems, No. LBL 4415, National Technical Information Service, Springfield, Va., 1975. [Pg.14]

Examples of nir analysis are polymer identification (126,127), pharmaceutical manufacturing (128), gasoline analysis (129,130), and on-line refinery process chemistry (131). Nir fiber optics have been used as immersion probes for monitoring pollutants in drainage waters by attenuated total internal reflectance (132). The usefulness of nir for aqueous systems has led to important biological and medical appHcations (133). [Pg.315]

Surface activity is not limited to aqueous systems, however. AH of the combiaations of aqueous and nonaqueous phases are known to occur, but because water is present as the solvent phase in the overwhelming proportion of commercially important surfactant systems, its presence is assumed in much of the common terminology of industry. Thus, the water-soluble amphipathic groups are often referred to as solubilizing groups. [Pg.232]

Similarly, the stabiUty of aqueous solutions of monoacetjlacetone or monotriethanolamine titanate complexes can be improved by the addition of glycol ethers (120). These solutions are useful ia appHcations ia which the catalytic, cross-linking, or film-forming actions of titanates are desired to take place ia aqueous systems. [Pg.149]

The second approach, changing the environment, is a widely used, practical method of preventing corrosion. In aqueous systems, there are three ways to effect a change in environment to inhibit corrosion (/) form a protective film of calcium carbonate on the metal surface using the natural calcium and alkalinity in the water, (2) remove the corrosive oxygen from the water, either by mechanical or chemical deaeration, and (3) add corrosion inhibitors. [Pg.268]

Zirconium forms anhydrous compounds in which its valence may be 1, 2, 3, or 4, but the chemistry of zirconium is characterized by the difficulty of reduction to oxidation states less than four. In aqueous systems, zirconium is always quadrivalent. It has high coordination numbers, and exhibits hydrolysis which is slow to come to equiUbrium, and as a consequence zirconium compounds in aqueous systems are polymerized. [Pg.427]


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Activity coefficient aqueous systems, chemical equilibrium

Aluminum aqueous system

Amines in aqueous system

Ammonia/nitrate aqueous system

Aqueous Additive Systems

Aqueous Buffer Systems

Aqueous Polyurethane Systems

Aqueous Solution Systems

Aqueous Systems with Additional Organic Solvent

Aqueous Systems without Additional Organic Solvent

Aqueous absorption systems

Aqueous biphasic separation systems

Aqueous biphasic systems

Aqueous biphasic systems extraction chromatography

Aqueous equilibria acid-base buffer systems

Aqueous interfaces simulation system

Aqueous microemulsions systems

Aqueous multiphase systems, phase

Aqueous multiphase systems, phase partitioning

Aqueous nitrate system, radiolysis

Aqueous polymer systems

Aqueous scrubbing system

Aqueous solution-precipitate system

Aqueous surfactant systems

Aqueous system, irradiated

Aqueous systems advantages

Aqueous systems binders

Aqueous systems chemical equilibrium

Aqueous systems dewetting

Aqueous systems distribution

Aqueous systems drying

Aqueous systems equilibrium constant derivation

Aqueous systems experimental results

Aqueous systems high polymers

Aqueous systems hydrogen bonds

Aqueous systems ionic strength

Aqueous systems ionic strength, solution reaction equilibria

Aqueous systems phase equilibrium

Aqueous systems redox state

Aqueous systems research background

Aqueous systems switching

Aqueous systems thermodynamics

Aqueous systems versus nonaqueous

Aqueous systems, bioreduction

Aqueous systems, reactions

Aqueous systems, scintillation flow

Aqueous systems, unit activity

Aqueous two-phase extraction system

Aqueous two-phase polymer systems

Aqueous two-phase polymer systems formed by SPs for use in bioseparation

Aqueous two-phase systems ATPS)

Aqueous vanadium systems

Aqueous-electrolyte systems

Aqueous-hexane biphasic system

Aqueous/organic cosolvent systems

Automata Models of Aqueous Solution Systems

Autoxidation aqueous model system

Binary aqueous system, phase

Binary aqueous systems

Binary aqueous systems, solubilization

Bioreduction in Aqueous Systems

Bioreduction in Biphasic Aqueous-Organic Systems

Biphasic aqueous—organic systems

Biphasic catalysts aqueous organic solvents, recyclable systems

CHEMICAL MODELING IN AQUEOUS SYSTEMS

CHEMICAL MODELING OF AQUEOUS SYSTEMS

CO2/aqueous hybrid system

CO2/aqueous hybrid system in fluoropolymer synthesis

Carbonylation aqueous biphasic systems

Chemical equilibrium, aqueous systems potentials

Closed aqueous system

Components aqueous systems, chemical equilibrium

Conductivity aqueous systems

Corrosion inhibition aqueous systems

Crosslinking aqueous systems

Description of Aqueous Systems

Diels-Alder reactions in non-aqueous polar systems

Dilute aqueous systems, kinetic studies

Dispersants in aqueous systems

Dispersion systems aqueous solution medium

Effect of High Hydrostatic Pressure on Aqueous Organometallic Systems

Electric potential, aqueous systems, phase equilibrium

Enthalpy aqueous systems

Entropy aqueous systems

Experimental Apparatus for Non-Aqueous Systems

Extraction of Metal Ions Based on Aqueous Biphasic Systems

Formulation process aqueous systems

Frozen aqueous systems

Frozen aqueous systems, reactions

Functional aqueous systems

Gelled aqueous systems

General Aspects of Transition Metal-Catalyzed Polymerization in Aqueous Systems

Gibbs energies aqueous systems

Gibbs-Duhem equations aqueous systems

Heat capacity aqueous systems

Higher aqueous-organic biphasic system

Hydroformylation and Carbonylation Reactions in Aqueous Biphasic Systems

Hydroformylation of Olefins in Aqueous-Organic Biphasic Catalytic Systems

Hydroformylations aqueous biphasic system

Hydrogen aqueous systems

In Thermodynamics of Aqueous Systems with Industrial Applications Newman

In Thermodynamics of Aqueous Systems with Industrial Applications Newman ACS Symposium Series American Chemical Society: Washington

Industrial applications aqueous systems

Inorganic aqueous chemical systems

Interaction with sodium dodecyl sulfate aqueous systems

Ion Extraction in Polyethylene Glycol Based-Aqueous Biphasic Systems

Ionic Equilibria in Aqueous Systems

Liquid phase models, aqueous systems

Low-cost aqueous two-phase system for

Low-cost aqueous two-phase system for affinity extraction

Magnesium aqueous system

Maillard model systems, aqueous

Manganese aqueous system

Metal-aqueous systems, electrode-electrolyte

Micellar catalysis aqueous systems

Micro-aqueous organic reaction system

Models dynamic aqueous systems

Monophasic aqueous-organic systems

Nitrogen-aqueous ethanol system

Nitrogen-aqueous ethanol system position

Non-aqueous solvent system

Non-aqueous systems

Olefin and Alkyne Polymerization in Aqueous Systems

Operation and Maintenance of UV System in Aqueous Environments

Organic compounds in aqueous systems

Organic-Aqueous Biphasic Systems General Considerations

Organic-aqueous two-phase system

Organometallic catalysis, aqueous biphasic systems

Packings, structured aqueous systems

Phase Equilibrium in Aqueous Systems

Phase equilibrium, aqueous systems distribution

Phase equilibrium, aqueous systems high polymers

Place of Reaction in Aqueous Biphasic Systems

Polymerization by Suzuki-Coupling in Aqueous Systems

Polymerization of Acrylamide with a Redox System in Aqueous Solution

Polymerization of Alkynes in Aqueous Systems

Preparative-scale Kinetic Resolution Using Aldolase Antibodies in a Biphasic Aqueous-Organic Solvent System

Protein aqueous systems

Protein partitioning in two-phase aqueous polymer systems

Proton transfer, hydrogen bonds aqueous systems

Rare earth metal compounds aqueous systems

Rare earths as corrosion inhibitors in aqueous systems

Re Complexes H3C-MO3 as an Example of Metal Variation in Potential Catalysts for Aqueous Systems

Reaction Gibbs energy, aqueous systems, chemical equilibrium

Recyclable systems, aqueous organic solvents

Semi-aqueous cleaning systems

Small Molecule Solutions Including Aqueous Systems

Soil-aqueous systems

Solution systems model aqueous solutions modeling

Solvents aqueous systems

Special Reactions in Homogeneous Aqueous Systems

Spin-lattice relaxation, aqueous system

Structure of aqueous systems

Supported aqueous-phase catalysis systems

Surfactant solubilization, phenanthrene soil-aqueous systems

Surfactants in aqueous systems

Synthesis in frozen-aqueous systems

Systems in aqueous media

Systems with Aqueous Electrolytes

THERMODYNAMICS OF SUPERCRITICAL AQUEOUS SYSTEMS

Technology and Applications of Aqueous Fluoropolymer Systems

Templates aqueous systems

The Aqueous Vanadium(III, IV and V) Systems

The electrode polarization in non-aqueous systems

Thermodynamic Properties of Aqueous Systems

Thermodynamic properties aqueous systems

Thermodynamics aqueous systems, chemical equilibrium

Traditional Free-Radical Polymerization in Aqueous Systems

Transition Metal-Catalyzed Polymerization in Aqueous Systems

Transition metal catalysis aqueous biphasic systems

Two-component Aqueous Systems

Water, properties aqueous systems

Zeta potential measurement, aqueous system

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