Recirculation currents

This term varies significantly with the nature of the fuel. Liquid fuels are characterized by the presence of recirculation currents induced by buoyancy. These currents homogenize the temperature distributions, reducing in-depth conduction. Nevertheless, convective motion transfers heat to the interior of the pool leading to an additional term of in-depth convection. Convective heat transfer in polymer melts has a similar behavior and could potentially have an important effect on burning rates nevertheless, the impact of polymer melt rheology on the flammability of materials is still a matter of great controversy. 

As the coal-feed jet decreases from its nozzle velocity, it entrains surrounding fluid to conserve its axial momentum and thereby sets up recirculation currents. The mass rate of material recirculated, mr, per mass rate of material fed, ra0, can be estimated from the following equation proposed by Thring (15) ... 

CMC bubbles of the same volume regardless of the Reynolds number [26]. In stirred liquids, the impeller disturbs the motion of bubbles and can accelerate or retard them, depending on the existence of recirculation currents. Nevertheless, the average residence time of PAA bubbles is expected to be lower than in inelastic fluids. Simple visual observation allowed us to confirm that the residence time of air bubbles in PAA was longer than in CMC, but not necessarily longer than in XTN... 

All vessels should be provided with a means of resuspending solids which have settled to the bottom. In some vessels, a simple mechanical agitator is sufficient. In others, steam or gas sparging can be used. In still other cases, more sophisticated systems may be required involving, for example, injection of an external liquid or slurry stream to induce strong internal recirculation currents. 

Small amounts of propionitrile and bis(cyanoethyl) ether are formed as by-products. The hydrogen ions are formed from water at the anode and pass to the cathode through a membrane. The catholyte that is continuously recirculated in the cell consists of a mixture of acrylonitrile, water, and a tetraalkylammonium salt the anolyte is recirculated aqueous sulfuric acid. A quantity of catholyte is continuously removed for recovery of adiponitrile and unreacted acrylonitrile the latter is fed back to the catholyte with fresh acrylonitrile. Oxygen that is produced at the anodes is vented and water is added to the circulating anolyte to replace the water that is lost through electrolysis. The operating temperature of the cell is ca 50—60°C. Current densities are 0.25-1.5 A/cm (see Electrochemical processing). 

The purified ziac solution is fed to the electrolyte recirculating stream at a rate that holds the composition of the electrolyte constant, commonly ranging from 100—200 g H2SO4 and 45—70 g Zn/L. Continuous monitoring of the density and conductivity of the spent acid aids ia control. This is important siace the range of acidity is narrow for maximum current efficiency at any given current density. 

The other reactions at the electrodes produce acid (anode) and base (cathode) so that there is a possibiUty of a pH gradient throughout the electrophoresis medium unless the system is well buffered (see Hydrogen-ion activity). Buffering must take the current load into account because the electrolysis reactions proceed at the rate of the current. Electrophoresis systems sometimes mix and recirculate the buffers from the individual electrode reservoirs to equalize the pH. 

Process Unit or Batch Unit A process unit is a collection of processing equipment that can, at least at certain times, be operated in a manner completely independent from the remainder of the plant. A process unit normally provides a specific function in the production of a batch of product . For example, a process unit might be a reactor complete with all associated equipment (jacket, recirculation pump, reflux condenser, and so on). However, each feed preparation tank is usually a separate process unit. With this separation, preparation of the feed for the next batch can be started as soon as the feed tank is emptied for the current batch. 

Current designs for venturi scrubbers generally use the vertical downflow of gas through the venturi contactor and incorporate three features (I) a wet-approach or flooded-waU entry sec tion, to avoid dust buildup at a wet-dry pmction (2) an adjustable throat for the venturi (or orifice), to provide for adjustment of the pressure drop and (3) a flooded elbow located below the venturi and ahead of the entrainment separator, to reduce wear by abrasive particles. The venturi throat is sometimes fitted with a refractoiy fining to resist abrasion by dust particles. The entrainment separator is commonly, but not invariably, of the cyclone type. An example of the standard form of venturi scrubber is shown in Fig. 17-48. The wet-approach entiy section has made practical the recirculation of slurries. Various forms of adjustable throats, which may be under manual or automatic control. 

Automated controls for flocciJating reagents can use a feedforward mode based on feed turbidity and feed volumetric rate, or a feed-back mode incorporating a streaming current detector on the flocculated feed. Attempts to control coagulant addition on the basis of overflow turbidity generally have been less successful. Control for pH has been accomplished by feed-forward modes on the feed pH and by feed-back modes on the basis of clarifier feedwell or external reaction tank pH. Control loops based on measurement of feedwell pH are useful for control in apphcations in which flocculated sohds are internaUy recirculated within the clarifier feedwell. 

To design an air recirculation system it is necessary to know the performances of fans, air cleaners, and exhaust hoods included in the current system. The equations described here include the source generation rate and the total airflow rate through the room, which could be difficult to measure. The ratio between source rate and flow rate has the unit of concentration and should in fact be equal to the concentration without recirculation. The equations could thus be transformed to include the contaminant concentration without recirculation instead of this ratio. In this way a direct comparison between concentration without and with recirculation is possible. By using the described equations it is then possible to design an air recirculation system to result in the demanded concentration in a workroom. 

The sprayed electrode boiler boiler is provided with a pump that draws BW from close to the bottom of the pressure vessel and circulates it back to the top of the vessel into an injection cylinder. From there the water is sprayed through multiple jets directly onto the electrodes, a current path is established, and steam is produced. However, the water flow is considerably greater than the steam evaporation rate, and the excess water is recirculated once more around the boiler... 

Once absorbed, ezetimibe undergoes extensive glucuronida-tion in the intestinal wall to the active metabolite (ezetimibe glucuronide). Ezetimibe and the active metabolite are entero-hepatically recirculated back to the site of action, which limits systemic exposure and may explain the low incidence of adverse effects (Table 9-9). Ezetimibe alone or with a statin is contraindicated in patients with active liver disease or unexplained persistent elevations in LFTs. Currently, clinical trials designed to determine ezetimibe s effects on CHD morbidity and mortality have not been completed. The time until maximum effect on lipids for ezetemibe is generally 2 weeks. 

DSA-02 oxide-coated Ti anode (DSA = Dimensionally Stable Anode) is placed, thus creating a large cathode volume. The effluent solution flows perpendicularly through the electrodes with a typical flow rate of 0.5 dm3 s-1. The flowthrough metal electrodes have an active area approximately 15 times their geometric area. The cell allows air sparging to increase the mass-transfer. The current efficiency is about 40% when the inlet concentration of the metal ions is 150 to 1500 ppm and the concentration at the out-let is about 50 ppm. The cell is currently used for the treatment of recirculated wash-waters from acid copper, copper cyanide, zinc cyanide, zinc chloride, cadmium sulphate, cadmium cyanide and precious metal plating and washwaters from electroless copper deposition. Since the foam metal electrodes are relatively expensive the electrodes... 

The vertical mixing is enhanced using a baffle system. This uses the gas lift principle on the front face to increase upward liquor flow. A corresponding downward flow of gas-free liquor is drawn down the back face of the baffle thus creating an increased vertical circulation. Measurements at the test facilities of ICIETB have demonstrated a recirculation flow ratio of recirculated flow to inlet flow of approximately 70 1, depending on the operating current density. 

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