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Chart notes

Figure 2-38C. Critical Pressure Ratio, r, for compressible flow through nozzles and venturi tubes. By permission, Crane Co., Technical Paper 410, 1957. Also see 1976 edition. See note at Figure 2-18 explaining details of data source for chart. Note P = psia p= ratio of small-to-large diameter in orifices and nozzles, and contractions or enlargements in pipes. Figure 2-38C. Critical Pressure Ratio, r, for compressible flow through nozzles and venturi tubes. By permission, Crane Co., Technical Paper 410, 1957. Also see 1976 edition. See note at Figure 2-18 explaining details of data source for chart. Note P = psia p= ratio of small-to-large diameter in orifices and nozzles, and contractions or enlargements in pipes.
Within the temperature range in which the third ester is eluted (on most columns, 110-140 C), sake two narks on the recorder chart noting the actual oven te) perature. [Pg.87]

Best practices. Therapies that researchers have found to be effective for a disorder. Chart notes (or progress notes). Notes in a client s chart that document treatment progress. [Pg.133]

Compare the two charts, note differences for potential problems needing resolution. [Pg.135]

Analysis The temperature v/ithin the shaft may vary with the radial distance r as vreli s. time, and the temperature at a specified location at a given time can be detetniined from the Heisler charts. Noting that the radius of the shaft is r- = 0.1-rti, from Fig, 4 16 we have... [Pg.258]

For every patient with a serum drug concentration ordered, the primary pharmacist writes a Clinical Pharmacokinetics note in the progress notes section of the patient s chart within 24 hours for normal or subthe-rapeutic concentrations. For supratherapeutic drug concentrations, the medical team is notified immediately if clinically warranted and a chart note written within 12 hours after the concentration was reported. The chart note contains all relevant patient information and pharmacokinetic parameters necessary to provide dosing and monitoring recommendations. ... [Pg.164]

Draw the best-fit line through the experimental points graphed in an X-Y (scatter) chart (Note it looks better if your chart starts with just the data points with no connecting lines.)... [Pg.19]

Figure 19 is an illustration of an SDC chart (shown diagrammatically, since we should now be quite familiar with the concepts from the previous more detailed illustrations). The data show PI values for C++ and C+ and indicate that there are different results according to the operator, because the same kit is being used. The reasons can be determined by examination of all the control values plotted as DDD charts. Note also that operator BB has a higher variation in results as judged hy the larger SD bars. In fact, operator BB has C++ and C+ values that are quite similar to each other, whereas there is a clear... [Pg.379]

Figure and draw a scale on appropriate graph paper so the upper control limit is placed approximately one quarter of the way from the top. If there is a lower control Umit, it should be placed 10-25% above the bottom of the chart. (Note the scale should begin with zero for most situations.)... [Pg.1845]

The holes into which these small screws will enter must be even smaller. (Hole diameters and shapes are specified by the screw supplier and are also shown on screw charts.) Note that there is a difference in hole size and shape 1) fm tapped thn s in I... [Pg.50]

To monitor the team s progress in meeting their goal, we graphed by month the reduction in average changeover time on a trend chart. Note that the dramatic... [Pg.336]

Use the DePriester charts. Note This is not trial and error. [Pg.109]

First, as with other analyses, define the scope of the analysis and the ground rules. Then collect the appropriate input data organize the data into procedures, personnel, and facilities/hardware and systematically evaluate the system or project using the PET user s guide and the PET chart. Note that multiple copies of the PET chart may be required. [Pg.192]

Table 10.1. While the design procedures for isothermal reactors and adiabatic reactors are straightforward to use, those for nonadiabatic reactors are complicated by the split boundary conditions on temperature. Procedures for nonadiabatic reactors are summarized in Figure 10.1 in the form of a flow chart. Note that q. (D) in Table 10.1 is the Euler version of q. 10.18 for numerical integration. Using the procedures given in Figure 10.1, a table of r versus Cout can be generated, from which the value of t corresponding to the desired conversion can be selected. Table 10.1. While the design procedures for isothermal reactors and adiabatic reactors are straightforward to use, those for nonadiabatic reactors are complicated by the split boundary conditions on temperature. Procedures for nonadiabatic reactors are summarized in Figure 10.1 in the form of a flow chart. Note that q. (D) in Table 10.1 is the Euler version of q. 10.18 for numerical integration. Using the procedures given in Figure 10.1, a table of r versus Cout can be generated, from which the value of t corresponding to the desired conversion can be selected.
Figure 3. Chemical shift values and ranges for B in three-coordinate compounds [BXYZ]. Where appropriate, X indicates the shift of the simplest methyl derivative. See Ref. 5 for ai extensive survey, and Ref. 8 for more extensive charts. Note that in donor solvents many species will be four-coordinate. Figure 3. Chemical shift values and ranges for B in three-coordinate compounds [BXYZ]. Where appropriate, X indicates the shift of the simplest methyl derivative. See Ref. 5 for ai extensive survey, and Ref. 8 for more extensive charts. Note that in donor solvents many species will be four-coordinate.

See other pages where Chart notes is mentioned: [Pg.68]    [Pg.73]    [Pg.132]    [Pg.289]    [Pg.250]    [Pg.382]    [Pg.143]    [Pg.148]    [Pg.1278]    [Pg.175]    [Pg.178]    [Pg.643]    [Pg.127]   


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