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Condensation processes

Both the reboiling and condensing processes normally take place over a range of temperature. Practical considerations, however, usually dictate that the heat to the reboiler must be supplied at a temperature above the dew point of the vapor leaving the reboiler and that the heat removed in the condenser must be removed at a temperature lower than the bubble point of the liquid. Hence, in preliminary design at least, both reboiling and condensing can be assumed to take place at constant temperatures. ... [Pg.341]

Evaporation processes usually separate a single component (typically water) from a nonvolatile material. As such, it is good enough in most cases to assume that the vaporization and condensation processes take place at constant temperatures. [Pg.355]

Dehydration can be performed by a number of methods cooling, absorption and adsorption. Water removal by cooling is simply a condensation process at lower temperatures the gas can hold less water vapour. This method of dehydration is often used when gas has to be cooled to recover heavy hydrocarbons. Inhibitors such as glycol may have to be injected upstream of the chillers to prevent hydrate formation. [Pg.250]

At first we tried to explain the phenomenon on the base of the existence of the difference between the saturated vapor pressures above two menisci in dead-end capillary [12]. It results in the evaporation of a liquid from the meniscus of smaller curvature ( classical capillary imbibition) and the condensation of its vapor upon the meniscus of larger curvature originally existed due to capillary condensation. We worked out the mathematical description of both gas-vapor diffusion and evaporation-condensation processes in cone s channel. Solving the system of differential equations for evaporation-condensation processes, we ve derived the formula for the dependence of top s (or inner) liquid column growth on time. But the calculated curves for the kinetics of inner column s length are 1-2 orders of magnitude smaller than the experimental ones [12]. [Pg.616]

There is always some degree of adsorption of a gas or vapor at the solid-gas interface for vapors at pressures approaching the saturation pressure, the amount of adsorption can be quite large and may approach or exceed the point of monolayer formation. This type of adsorption, that of vapors near their saturation pressure, is called physical adsorption-, the forces responsible for it are similar in nature to those acting in condensation processes in general and may be somewhat loosely termed van der Waals forces, discussed in Chapter VII. The very large volume of literature associated with this subject is covered in some detail in Chapter XVII. [Pg.350]

Natural gas Hquids are recovered from natural gas using condensation processes, absorption (qv) processes employing hydrocarbon Hquids similar to gasoline or kerosene as the absorber oil, or soHd-bed adsorption (qv) processes using adsorbants such as siHca, molecular sieves, or activated charcoal. Eor condensation processes, cooling can be provided by refrigeration units which frequently use vapor-compression cycles with propane as the refrigerant or by... [Pg.171]

The one-step route from 2-propanol coproduces diisobutyl ketone and acetone, and is practiced in the United States by Union Carbide (61). The details of a vapor-phase 2-propanol dehydrogenation and condensation process for the production of acetone, MIBK, and higher ketones have been described in recent patents (62,63). The process converts an a2eotropic 2-propanol—water feed over a copper-based catalyst at 220°C and produces a product mixture containing 2-propanol (11.4%), acetone (52.4%), MIBK (21.6%), diisobutyl ketone (6.5%), and 4-methyl-2-pentanol (2.2%). [Pg.490]

The main benefit of the Dow process was control of the polymer architecture. The polymer from the self-condensation process possessed a linear stmcture, but there were other difficulties. The monomer was cosdy and removal of the cuprous bromide by-product was difficult (17) ultimately, scale-up difficulties terrninated the Dow PPS development. However, there was a growing recognition that PPS was an attractive polymer with an excellent combination of properties. [Pg.441]

Polymerization and depolymerization of sihcate anions and their interactions with other ions and complexing agents are of great interest in sol—gel and catalyst manufacture, detergency, oil and gas production, waste management, and limnology (45—50). The complex silanol condensation process may be represented empirically by... [Pg.6]

The relative contributions from these processes strongly depend on the reaction conditions, such as type of solvent, substrate and water concentration, and acidity of catalyst (78,79). It was also discovered that in acid—base inert solvents, such as methylene chloride, the basic assistance requited for the condensation process is provided by another silanol group. This phenomena, called intra—inter catalysis, controls the linear-to-cyclic products ratio, which is constant at a wide range of substrate concentrations. [Pg.46]

The main synthetic route to high nuclearity metal carbonyl clusters involves a condensation process (/) a reaction induced by coordinatively unsaturated species or (2) a reaction between coordinatively saturated species in different oxidation states. As an example of (/), Os2(CO)22 can be condensed to form a series of higher coordinated species (89). [Pg.68]

The dephlegmator process recovers a substantially higher purity C2+ hydrocarbon product with 50—75% lower methane content than the conventional partial condensation process. The C2+ product from the cryogenic separation process can be compressed and further separated in a de-ethanizer column to provide a high purity C3+ (LPG) product and a mixed ethylene—ethane product with 10—15% methane. Additional refrigeration for the deethanization process can be provided by a package Freon, propane or propylene refrigeration system. [Pg.332]

Fig. 1. UOP catalytic condensation process for cumene synthesis. R = reactor RECT = rectifier DP = depropanizer RC = recycle column ... Fig. 1. UOP catalytic condensation process for cumene synthesis. R = reactor RECT = rectifier DP = depropanizer RC = recycle column ...
The primary results of all of these studies are that condensation occurs far more readily at the para position than at ortho and that methylolation tends to activate condensation much as it does methylolation. An important inference from these results is that steric factors appear to be quite influential in the condensation process,... [Pg.908]

As we have already mentioned, the cure of resoles takes place primarily through further extension of the condensation process, though the conditions are usually considerably different from those of synthesis. The changes in conditions normally include exposure to much higher temperatures and higher concentrations of polymer than are seen in resin synthesis. The pH of the medium may also... [Pg.912]

Gas Phase Adsorption - This is a condensation process where the adsorption forces condense the molecules from the bulk phase within the pores of the activated carbon. The driving force for adsorption is the ratio of the partial pressure and the vapour pressure of the compound. [Pg.405]

The reader is encouraged to select other chemical process condensation processes and obtain information on physical and chemical properties, healtli effects, and methods of manufacture, and causes for potential accidents. This is obviously an open-ended question, therefore no solution is provided. [Pg.281]

A variety of condensation processes can lead to cyclic hydroxamic acids. These involve either the condensation of two molecules or the intramolecular cyclization of a single compound. In some cases, a primary hydroxamic acid function is already present and formation of a cyclic compound can arise by suitable reaction on nitrogen. These processes will be dealt with first. [Pg.206]

For design of a new system, it is recommended that the results of the summation above be multiplied by 2 or 3 to establish the jet system inert (noncondensables) capacity, and add to this the non-condensed process vapors that are released into the jet suction system. [Pg.366]

Spiral 10-9A Compact, concentric plates Cross-flow, condensing. Process corrosion. 0.8-1.5... [Pg.7]

Figure 10-66 indicates the usual condensing process, which is not limited to a vertical tube (or bundle) as shown, but represents the condensing/cooling mechanism for any tube. The temperature numbers correspond to those of Figure 10-28. [Pg.116]

Pounds/hr air + non-condensables + process released air + process released non-condensables)/Hr s Air in leakage, lb/hr (6-7)... [Pg.366]

Additionally, the surfactant properties of filmers reduce the potential for stagnant, heat-transfer-resisting films, which typically develop in a filmwise condensation process, by promoting the formation of condensate drops (dropwise condensation process) that reach critical mass and fall away to leave a bare metal surface (see Figure 11.2). This function, together with the well-known scouring effect on unwanted deposits keeps internal surfaces clean and thus improves heat-transfer efficiencies (often by 5-10%). [Pg.536]

Dropwise condensation process Drum plates, inspection of Drumless delivery Drumless delivery service Dry ice blasting Dry lay-up... [Pg.848]


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ADDITION AND CONDENSATION POLYMERIZATION PROCESSES

Acidolysis-condensation process

Aerosol condensation processes

Bonded stationary phases condensation process

By Andrew Gilbert Physical Aspects of Photochemistry Photophysical Processes in Condensed Phases

Case study control of a reactor-condenser process

Condensate Stabilizer as a Gas Processing Plant

Condensates from coal processing

Condensation The process by which vapor

Condensation The process by which vapor molecules re-form a liquid

Condensation polymers processes

Condensed phase processes

Condenser vinyl chloride monomer process

Condensers process

Dense evaporation-condensation processes

Evaporation-condensation process

Example 6-5 Actual Capacity for Process Vapor Plus Non-Condensable

Flame-Chemical Vapor Condensation Process

Heat exchangers, condensers Integrating processes

Ligand elimination process, condensation

Liquid wastes process condensate

Molecular condensation process

Nanostructured materials condensation process

PART I PHYSICAL ASPECTS OF PHOTOCHEMISTRY Photophysical Processes in Condensed Phases

Particles condensation processes

Photolysis, condensed phase process

Photophysical Processes in Condensed Phases

Poly condensation process

Polymerization condensation process

Polyphenols condensation processes

Post condensation processes

Process Condensate (Methanol and Ammonia)

Process condensate

Process condenser, tube leak

Processing, thermoplastics condensation polymerization

QM/MM methods for simulation of condensed phase processes

Reflux condensers, with batch processing

Shock-condensation processes

Specific enthalpy condensation process

Steam condensation process

Synthesis processing, condensation process

Technological Schemes of Complex Oil, Gas and Condensate Processing Plants

Unsaturated polyesters condensation process

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