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Process results

Processes carried out with in-line mixing equipment are very similar to those with stirred tanks. They include the following three main classes  [Pg.404]

Additionally, there are applications where there is no analogy with stirred tanks, for example  [Pg.404]

Application Laminar Flow Turbulent Flow Measurement Criteria [Pg.405]

Liquid-liquid dispersion extraction/reaction X X Drop size, drop size distribution, mass transfer [Pg.405]

Gas-liquid dispersion with - X Drop size, total surface area [Pg.405]

The effect on the process of a change in operation of the mixer system (impeller, baffles, etc.) is the final measurement of performance. Thus, operations such as blending, uniform particle suspension, reaction, gas absorption, etc., may be acceptable under one physical system and not so to the same degree under a slightly modified one. The ratio per unit volume on scale-up must be determined experimentally. [Pg.323]

Generally as system size increases the impeller flow per fixed power input will increase faster than will the turbulence of the system. Even the same degree of turbulence is no insurance that the rates of mixing, mass transfer, [Pg.323]

Expected Proportions of Flow and Turbulence in a Mixing System [Pg.323]

Relative Impeller Diameter Percent Flow Percent Turbulence Relative Speed [Pg.323]

Operations such as blending, solids-suspension, dissolving, heat transfer and liquid-liquid extraction are typical of systems requiring high flow relative to turbulence, while gas-liquid reactions and some liquid-liquid contacting require high turbulence relative to flow. The case of (1) 100% of suspension—requires head to keep particles suspended and (2) 100% uniformity of distribution of particles—requires head for suspension plus flow for dis-U ibution. [Pg.323]


Condensation polymerization differs from addition polymerization in that the polymer is formed by reaction of monomers, each step in the process resulting in the elimination of some easily removed molecule (often water). E.g. the polyester polyethylene terephthalate (Terylene) is formed by the condensation polymerization (polycondensation) of ethylene glycol with terephthalic acid ... [Pg.321]

SWS are useful to obtain direct indications of hydrocarbons (under UV light) and to differentiate between oil and gas. The technique is applied extensively to sample microfossils and pollen for stratigraphic analysis (age dating, correlation, depositional environment). Qualitative inspection of porosity is possible, but very often the sampling process results in a severe crushing of the sample thus obscuring the true porosity and permeability. [Pg.129]

Figure 8 VIGRAL process results top left - amplitude tuid ToF vs. position plot top right - source histogram lower right the V-scan image lower left -specimen location and dimensions. Figure 8 VIGRAL process results top left - amplitude tuid ToF vs. position plot top right - source histogram lower right the V-scan image lower left -specimen location and dimensions.
A process resulting in a decrease in touglmess or ductility of a metal due to absorjDtion of hydrogen. This atomic hydrogen can result, for instance, in the cathodic corrosion reaction or from cathodic protection. [Pg.2732]

Electron transfer reactions are conceptually simple. The coupled stmctural changes may be modest, as in tire case of outer-sphere electron transport processes. Otlier electron transfer processes result in bond fonnation or... [Pg.2971]

In the fir.st iteration proces.s, the class values of the atoms of the structure. show information already known (the degree of the nodes). Hence Morgan takes the neighboring atoms into account. He considers the environment of an atom by summing class values of all directly adjacent atoms. This process results in a new class value called the extended connectivity (EC) value of the atom. The new EC value expresses indirectly the neighborhood of the adjacent atoms in a second sphere (Figure 2-43). [Pg.61]

The various welding processes result in systems of varying complexity. They include at least the electrode and a device for holding or feeding it, the work piece, the power source, and heavy-duty cabling to provide a complete electrical circuit. Provisions for supply and control of gas and control of wire feed and movement of the electrode assembly are required, depending on process type and degree of automation. [Pg.342]

Sodium Hydroxide. Before World War 1, nearly all sodium hydroxide [1310-93-2], NaOH, was produced by the reaction of soda ash and lime. The subsequent rapid development of electrolytic production processes, resulting from growing demand for chlorine, effectively shut down the old lime—soda plants except in Eastern Europe, the USSR, India, and China. Recent changes in chlorine consumption have reduced demand, putting pressure on the price and availabiHty of caustic soda (NaOH). Because this trend is expected to continue, there is renewed interest in the lime—soda production process. EMC operates a 50,000 t/yr caustic soda plant that uses this technology at Green River it came onstream in mid-1990. Other U.S. soda ash producers have aimounced plans to constmct similar plants (1,5). [Pg.527]

Deteriora.tlon. Ceramic objects are fragile, and mechanical damages through breakage and abrasions are the most likely source of destmction. Low fired ceramics can suffer through the rehydration of the body material this process results ia a complete loss of mechanical streagth. The preseace of soluble salts ia porous ceramic bodies has the same disastrous results as ia stoae (136). [Pg.426]

A more complex flavor development occurs in the production of chocolate. The chocolate beans are first fermented to develop fewer complex flavor precursors upon roasting, these give the chocolate aroma. The beans from unfermented cocoa do not develop the chocolate notes (84—88) (see Chocolate and cocoa). The flavor development process with vanilla beans also allows for the formation of flavor precursors. The green vanilla beans, which have Htfle aroma or flavor, are scalded, removed, and allowed to perspire, which lowers the moisture content and retards the enzymatic activity. This process results in the formation of the vanilla aroma and flavor, and the dark-colored beans that after drying are the product of commerce. [Pg.18]

AgF2 is prepared by the action of elemental fluorine on AgF or AgCl at 200°C. Both processes result in quantitative yields. Silver difluoride should be stored in Teflon, passivated metal containers, or in sealed quartz tubes. [Pg.235]

Before deciding on a LIMS product, a complete set of specifications for required functions of the LIMS should be written. The best time to do this is before any vendors have been contacted. Inviting vendors to participate in this process results in a specification which can be automatically fiilfilled by their product. A thorough understanding of current data management processes is necessary to draw up a specification (17), and vendors do not have it. [Pg.519]

The success of the process results from the fact that nowhere inside the furnace is heat extracted from the copper-saturated blast furnace buUion through a soUd surface. The problem of accretion formation (metal buUd-up), which has plagued many other attempts to estabUsh a copper dtossing operation of this type, does not arise. In the cooling launder, lead-rich matte and slag accumulate on the water-cooled plates, but these ate designed so that when they ate lifted from the buUion stream, the dross cracks off and is swept into the furnace via the cooled lead pot. [Pg.42]

Zinc. The electrowinning of zinc on a commercial scale started in 1915. Most newer faciUties are electrolytic plants. The success of the process results from the abiUty to handle complex ores and to produce, after purification of the electrolyte, high purity zinc cathodes at an acceptable cost. Over the years, there have been only minor changes in the chemistry of the process to improve zinc recovery and solution purification. Improvements have been made in the areas of process instmmentation and control, automation, and prevention of water pollution. [Pg.174]

When choosing the scale-up method, changes in other flow/power parameters and their impact on the process result must be considered. Figure 11 shows changes in important parameters for different scale-up bases. For example, scale-up based on same tip speed maintains the T / Ubut decreases P/ Uby 80%. T / Uis almost always increased on scale-up. Scale-up based on the same P/ Umeans a reduction in mixer speed by 66%, which also... [Pg.424]

In contrast to the sulfide ores, the lateritic ores were formed over long periods of time as a result of weathering of exposed nickel-containing rocks. The lateritic weathering process resulted in nickel solutions that were redeposited elsewhere in the form of oxides or siUcates. One type of laterite is nickeliferous limonitic iron laterite (Ee, Ni)O(OH) which consists primarily of hydrated iron oxide in which the nickel is dispersed in soHd solution. [Pg.2]


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See also in sourсe #XX -- [ Pg.66 ]




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Categories of information resulting from the design process in reactive distillation

Definition of Desired Process Result

Impact on Process Results

Mixing concepts, fundamentals Process results

Optimization process results

Other Process Results

Process development results

Process intermediate storage operational results

Process intermediate storage operational results from

Process mapping results

Process results, mixing

Process safety audit results

Processing the Results

Real-time optimization results processing

Results from process scale

Results of the Gas-Phase Polymerization Process Exergy Analysis

Results of the HP LDPE Process Exergy Analysis

Results of the Optimisation Process

Results of the Optimization Process

Results using simulated process

Results using simulated process measurements

Self-Determination as Result or Process

Simulation Results Process and Actuator Faults

Summary of results and process implications

Testing results statistical process control

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