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Shaft stepped

The stress eoneentration faetor kf results from the keyway and must be used in torsional stress ealeulations. Faetor /c takes into aeeount the shaft step it must be used in the bending stress ealeulation. [Pg.624]

Fig. 10. Mass flow screw feeder designs, (a) Combined tapered shaft and variable pitch screw feeder where A represents a conical shaft and constant pitch (feed section) B, constant shaft and increasing pitch (feed section) and C, constant shaft and constant pitch (conveying section), (b) Stepped shaft screw feeder where A represents a stepped diameter shaft and constant pitch (feed section) and B, constant shaft and constant pitch (conveying section). Fig. 10. Mass flow screw feeder designs, (a) Combined tapered shaft and variable pitch screw feeder where A represents a conical shaft and constant pitch (feed section) B, constant shaft and increasing pitch (feed section) and C, constant shaft and constant pitch (conveying section), (b) Stepped shaft screw feeder where A represents a stepped diameter shaft and constant pitch (feed section) and B, constant shaft and constant pitch (conveying section).
For hi -pressure installations, it is possible to balance partially or fully the hydrostatic force on the rotating member of an internal seal by using a stepped shaft or shaft sleeve (Fig. 10-113). This method of... [Pg.941]

The number of speed reduetions is another way to classify conveyor drives. Most common of the speed-reduction methods is the two-step system, in which the motor is coupled to a speed reducer and the slow-speed shaft of the reducer is connected to the conveyor-drive shaft by a V belt or a roller chain. The second reduction not only permits the use of a simpler speed reducer but also allows a more flexible layout of the motor and reducer mounting plate. On many installations this eliminates the need for a specially designed drive mount. [Pg.1913]

Excessive mixing Limit agitator power input and provide proper of reactants or impeller design impurities which, Return process to pilot or development to rede-promotes process to eliminate or minimize this emulsification. problem Poor phase separa- tion resulting in L it shaft speed problems in subse- Monitor shaft speed quent processing, phase separation steps or in down- stream equipment. I" " de-emulsifiers CCPS G-29 Lees 1996... [Pg.60]

This deflection can be corrected easily during the alignment. For example, with the indicators in the upper position on the shaft, instead of starting at 0.000 inches, mark the positive value of the deflection of the bar determined in the previous step, and then rotate the shaft 180° to the bottom. Now the indicators will read 0.000 inches. [Pg.151]

The following illustration (Figure 13-15) shows a more realistic balance ratio. 70% of the face sees closing forced and 30% of the face (falling below the stepped sleeve on the shaft) does not. see closing force. [Pg.192]

The rotating shroud must be in close proximity to the blade tips within the tube. To get this proximity, a shaft-mounted plexiglass disc was suspended from above the blades. The plexiglass disc was machined as shown in Figure 7-13. The plexiglass tube was slotted so that the disc could be centered on the center line of the tube and its stepped section lowered through the two slots in the tube. Clearances between the slot edges and the disc were minimized. [Pg.287]

Figure 13-25. Unbalanced seal and balanced seal with step In shaft. Figure 13-25. Unbalanced seal and balanced seal with step In shaft.
In-house correlation of pumps should be made using gpm vs. cost with head as a parameter. These should result in step functions, since one size pump with different impellers can serve several flow rates and heads. Different correlations should be made for each type of pump. The price of a vertical multistage pump may be quite different from a horizontal splitcase multistage pump. A sump pump with a 15-ft drive shaft would cost more than a single-stage horizontal pump with the same gpm and head. [Pg.233]

Step 5. Solve for the shaft power substituting into Equation 4.7. [Pg.106]

Step 5. For the final step, compute the new shaft power value u ig ion 4.7. [Pg.108]

With the shaft speed and the tip speed calculated in Step 9 for the Section 2 stages, calculate an impeller diameter using Equation 5.15. [Pg.180]

Step 15. To complete the estimate, calculate the shaft power, using the conversion of 33,000 ft-lb/min/hp. [Pg.183]

Step 8. Calculate the shaft horsepower using Equation 4.7 and the mechanical losses from Figure 6-9 at the frame selection. Use the efli-ciencv Og =. 85 as recommended. [Pg.245]

Rather than evaluate each measurement point separately, plot the energy of each measurement point on a common shaft. First, the vertical measurements were plotted to determine the mode shape of the machine s shaft. This plot indicates that the outboard end of the motor shaft is displaced much more than the remaining shaft. This limits the machine problem to the rear of the motor. Based strictly on the overall value, the probable cause is loose motor mounts on the rear motor feet. The second step was plotting the horizontal mode shape. This plot indicates that the shaft is deflected between the pillow block bearings. Without additional information, the mode shaft suggests a bent shaft between the bearings. [Pg.814]

The last step in the installation process is verifying coupling and shaft alignment. With the exception of special application couplings such as spindles and jackshafts, all couplings must be aligned within relatively close tolerances (i.e., 0.001-0.002 inch). [Pg.997]

A thrust support for the spring either a collar keyed to the shaft or a step in the shaft. [Pg.216]

Between Points 1 and 2 in Figure B.2, the intake and discharge valves are closed and the gas in the cylinder is compressed from Px to P2. When the pressure reaches P2, the discharge valve opens and the gas is pushed from the cylinder between Points 2 and 3 in Figure B.2. Between Points 3 and 4, the intake and discharge valves are closed and any gas remaining in the cylinder is expanded to the intake pressure of Pi. Between Points 4 and 1, the intake valve opens and the suction stroke draws gas into the cylinder at pressure Pi. The total work for the cycle is the sum of the work for the four steps. The work required by the compression is often termed shaft work Ws. Thus ... [Pg.656]


See other pages where Shaft stepped is mentioned: [Pg.232]    [Pg.165]    [Pg.557]    [Pg.156]    [Pg.407]    [Pg.1095]    [Pg.1894]    [Pg.186]    [Pg.209]    [Pg.629]    [Pg.197]    [Pg.209]    [Pg.376]    [Pg.1]    [Pg.317]    [Pg.457]    [Pg.479]    [Pg.101]    [Pg.915]    [Pg.52]    [Pg.164]    [Pg.314]    [Pg.154]    [Pg.386]    [Pg.102]    [Pg.120]    [Pg.872]    [Pg.120]    [Pg.156]    [Pg.92]   
See also in sourсe #XX -- [ Pg.70 ]




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