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Without the cooperation of the receiver and sender higher layer protocols, there is only so much a FRAD can do to respond to the FECN and BECN bits If user applications continue to send in an unrestricted manner, the FRAD can either attempt to buffer the extra traffic, perform its own version of CIR enforcement (no frames that would be tagged DE = 1 by the switch are sent), or use a combination of the two approaches Modern FRADs do some amount of buffering of frames, usually quite a bit in an effort to smooth bursts in a process known as traffic shaping Many FRADs also respect the CIR, and even set the DE bit to 1 when the switch would in any case, although this is not technically the job of the FRAD.

In most cases where a FRAD, router or hardware device, responds at all to the FECN and/or BECN bits, it is by slowing down to the CIR level established for each DLCI affected by the congestion Bursts above the CIR on those DLCIs are buffered, if possible, or else discarded After all, frames above the CIR are not guaranteed delivery anyway Who cares if it is the FRAD or the switch that actually performs the discard.

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sound of your voice. You should experiment with this feature and see if you like the effect; if not, turn it off by clearing the check box.

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13-233 Continuous Flow Operation Continuous ow mixed reactors are most common in high-capacity processing operations Continuous ow reactions may be carried out in all the geometries discussed above: pipe and tee mixers, static mixers and other types of in-line mixers, and many types of stirred vessel Sizes of such reactors range from very small tee mixer reactors on the scale of 1 cm to stirred vessels holding thousands of liters of liquid with impellers in the range of 3 m or more in diameter Yields for very small continuous reactors may be studied in a pilot unit and applied directly to the plant, but yields for the very large reactors represent a severe design problem if the reactions are very mixing-rate sensitive These and the semibatch reactors discussed above bring major scale-up problems, even for single-phase chemical reactions.

Here, the result will never exceed 10 because FileMaker will return the lesser of the two values supplied. You can nest one expression within the other to ensure that YourNumber always falls within the range from 1 to 10:

1. Place the scrollbar near the item you plan to use as the data. 2. Select both. 3. Convert the group to a Scroll Panel or Data List component.

=MID(CELL( filename ,A1),FIND( ] ,CELL( filename ,A1))+1,LEN(CELL( filename ,A1)))

In both continuous ow and semibatch reactors, feed location and local turbulence intensity have a major effect on yield Multiple-phase chemical reactions cause even more complex scale-up problems, particularly if the mass transfer rate effects are compounded by chemical reaction yield effects in the reaction phase Continuous and semicontinuous ow reactors are sometimes used in ne chemical and pharmaceutical applications, primarily because some reactions require the high intensity of mixing that can only be achieved in in-line mixers (see Examples 13-3, 13-7, and 13-8a and discussion in 17) An important question for the design of continuous ow systems is: When can the classic perfectly mixed assumption (ideal CSTR) be used in a continuous ow stirred tank reactor The blend time concept can be used here If the blend time is small compared to the residence time in the reactor, the reactor can be considered to be well mixed.

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