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Or flow

Many experimental methods may be distinguished by whether and how they achieve time resolution—directly or indirectly. Indirect methods avoid the requirement for fast detection methods, either by detemiining relative rates from product yields or by transfonuing from the time axis to another coordinate, for example the distance or flow rate in flow tubes. Direct methods include (laser-) flash photolysis [27], pulse radiolysis [28]... [Pg.2115]

The latter contribute to the fluxes in time-varying conditions and provide source or sink terms in the presence of chemical reaction, but they have no influence on steady state diffusion or flow measurements in a non-reactive sys cem. [Pg.65]

Parallel processing and the RISC set give transputers a considerable speed advantage over conventional serial processors for handling information or flows of data. [Pg.420]

Immunosensors promise to become principal players ia chemical, diagnostic, and environmental analyses by the latter 1990s. Given the practical limits of immunosensors (low ppb or ng/mL to mid-pptr or pg/mL) and their portabiUty, the primary appHcation is expected to be as rapid screening devices ia noncentralized clinical laboratories, ia iatensive care faciUties, and as bedside monitors, ia physicians offices, and ia environmental and iadustrial settings (49—52). Industrial appHcations for immunosensors will also include use as the basis for automated on-line or flow-injection analysis systems to analyze and control pharmaceutical, food, and chemical processing lines (53). Immunosensors are not expected to replace laboratory-based immunoassays, but to open up new appHcations for immunoassay-based technology. [Pg.30]

Pipeline transport involves the appHcation of force to the material being moved, either through the use of pumps to transport Hquids, compressors to move gases, or flowing water to move soHds. In some appHcations, vacuum may create the pressure differential. [Pg.45]

Instrumental Interface. Gc/fdr instmmentation has developed around two different types of interfacing. The most common is the on-the-fly or flow cell interface in which gc effluent is dkected into a gold-coated cell or light pipe where the sample is subjected to infrared radiation (see Infrared and raman spectroscopy). Infrared transparent windows, usually made of potassium bromide, are fastened to the ends of the flow cell and the radiation is then dkected to a detector having a very fast response-time. In this light pipe type of interface, infrared spectra are generated by ratioing reference scans obtained when only carrier gas is in the cell to sample scans when a gc peak appears. [Pg.402]

Flow Regimes in Multiphase Reactors. Reactant contacting, product separations, rates of mass and heat transport, and ultimately reaction conversion and product yields are strong functions of the gas and Hquid flow patterns within the reactors. The nomenclature of commonly observed flow patterns or flow regimes reflects observed flow characteristics, ie, armular, bubbly, plug, slug, spray, stratified, and wavy. [Pg.508]

A special case of air atomization is high volume low pressure (hvlp) spray. In this case the air pressure at the spray gun is less than 70 kPa (10 psig) and there are relatively large (up to 0.32 cm) holes in the air cap to easily pass the low pressure air. This type of atomizer produces a soft or slow moving spray and is generally considered to be rather efficient in depositing the material on the workpiece. However, the use of low pressure air for atomization usually limits the viscosity and/or flow rate of the material that can be atomized. [Pg.330]

Impingement baffles or flow-distribution devices are recom-men oed for axial tube-side nozzles when entrance velocity is high. [Pg.1073]

What size tube or flow passage is available Small tubes plug unless filtration is installed. Size of filtering is needed from the supplier. [Pg.1087]

In design of separating chambers, static vessels or continuous-flow tanks may be used. Care must be taken to protect the flow from turbulence, which coiild cause back mixing of partially separated fluids or which could cany unseparated hquids rapidly to the separated-hquid outlet. Vertical baffles to protect rising biibbles from flow currents are sometimes employed. Unseparated fluids should be distributed to the separating region as uniformly and with as little velocity as possible. When the bubble rise velocity is quite low, shallow tanks or flow channels should be used to minimize the residence time required. [Pg.1442]


See other pages where Or flow is mentioned: [Pg.1440]    [Pg.1933]    [Pg.2672]    [Pg.2953]    [Pg.3030]    [Pg.91]    [Pg.285]    [Pg.354]    [Pg.81]    [Pg.81]    [Pg.106]    [Pg.353]    [Pg.264]    [Pg.248]    [Pg.177]    [Pg.50]    [Pg.223]    [Pg.255]    [Pg.317]    [Pg.332]    [Pg.487]    [Pg.219]    [Pg.108]    [Pg.110]    [Pg.35]    [Pg.15]    [Pg.202]    [Pg.224]    [Pg.248]    [Pg.88]    [Pg.95]    [Pg.139]    [Pg.163]    [Pg.209]    [Pg.637]    [Pg.694]    [Pg.874]    [Pg.959]    [Pg.1550]    [Pg.1562]   
See also in sourсe #XX -- [ Pg.3 , Pg.5 , Pg.8 ]




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Alignment by shear or extensional flow

Axial Dispersion or Dispersed Plug Flow (DPF) Model

Batch (or Plug Flow) Fermentors

Batch Operation or Flow-through Cells

Batch or Plug-Flow Fermenter

Batch or Steady-State Plug-Flow Reactor

Channel Flow with Soluble or Rapidly Reacting Walls

Cooling or heating of simple bodies in one-dimensional heat flow

Crystallization under deformation or flow

ESI-MS Concentration or Mass Flow Dependent

Flow Parallel to Field or Interface Gradient

Flow Past a Spherical Drop or Bubble

Flow of an incompressible viscoelastic liquid or solid

Flow or Line Mixers

Gas or Vapor Flow Rates

Heat Exchange Between Flow and Particles, Drops, or Bubbles

Heat Transfer Under Constrained Flow Past Particles, Drops, or Bubbles

High-Velocity Gas Flow with Friction, Heating, or Both

Industrial Equipment Batch or Continuous Flow

Irregular Flow or Melt Fracture

Jet Collision Turbulent or Swirling-flow Mixing

Modeling of Nonideal Flow or Mixing Effects on Reactor Performance

Perpendicular-Flow Filtration (Absolute or Sterile)

Plug Flow or Ideal Tubular Reactor (PFR)

Regenerative Fuel Cells or Redox Flow Batteries

Reverse flow from a product receiver or blowdown line back into the plant

Reversed, Mixed, or Cross-Flow

Shear flow outputs from a slot or cylindrical die

Sonic or critical flow

Transfer Between Particles, Drops, or Bubbles and Flows, with Volume Reaction

Transient or Pulsating Flows in Tubes

Unexpected Results Must Be Taught by, or Flow from the Patent Application

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