Ingersoll-Rand

A simplified sketch of an air lift for this purpose is shown in Fig. 10-57. Ingersoll-Rand has developed empirical information on air-hit performance which is available upon request. 

FIG. 10-90 Clearance -control cylinder (Coutiesy of Ingersoll-Rand.)... 

Ingersoll-Rand Corporation, Cogeneration System Package for Micro-Turbines, Sales Literature—2000, Portsmouth, New Hampshire. 

Source Modified courtesy of the Gas Processors Suppliers Association and Ingersoll-Rand. 

Gibbs, C. W., Editor, Compressed Air and Gas Data, Woodcliff Lake, NJ Ingersoll-Rand, 1969. 

Figure 11-15. Channel valves. (Courtesy of Ingersoll-Rand Company.)...

Ingersoll-Rand First successful diesel-electric Late ASEA - Brown Bovari Electric locomotive rectifier... 

Figure 2-39. Discharge coefficients for liquid flow. By permission, Cameron Hydraulic Data, Ingersoll-Rand Co., Washington, N.J., 1979.

Shaw, G. V.. editor, and A. W. Loomis, Cameron Hydraulic Data, Ingersoll-Rand Co., Eleventh Pldition, 1942 and 16th ed, 1979, Ed. C. R. Westaway and A. W. Loomis, Ingersoll-Rand Co., Woodcliff Lake, NJ. 

Figure 3-6. Cross-section horizontal two-stage horizontal split case centrifugal pump. (Courtesy Ingersoll-Rand Co.)...

Centrifugal Pump Fundamentals, Form 7287, Ingersoll-Rand Co., Cameron Pump Division, P. O. Box 636, WoodcliffLake, N.J. 07657. 

Figure 6-1. Basic ejector components and diagram of energy conversion in nozzle and diffuser. By permission, Ingersoll-Rand Co.

Figure 6-7A. Flow diagram of three-stage ejector wHh counter-current barometric booster condenser and intercondenser. By permission, ingersoll-Rand Co.

Vapor Pressure Curves. (Courtesy Ingersoll-Rand Co.)... 

Temperatures are average existing at 40° latitude and are rounded to even numbers. fNegative exponent shows number af spaces the decimal point must be moved to the left. Courtesy Ingersoll-Rand Co. 

Figure 11-5. Surface-type condenser, steam jets with three boosters. (Used by permission Ingersoll-Rand Company.) tBased on required N.P.S.H. of pump. May be reduced by pump pit or by pump requiring less N.P.S.H.

Figure 11-58. Theoretical comparison of Joule-Thompson cooling effect with nitrogen vs. the use of a mechanical expander. (Used by permission Gibbs, C. W., (Ed.). Compressed Air and Gas Data, 1969. Ingersoll-Rand Co.)...

Figure 12-14F. Compressibility chart for air. (Used by permission Form 3519 D (1981), 1960. Ingersoll-Rand Company. All rights reserved.)...

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