Number
of Part
Name of Part
1Frame
2Main-bearing cap
3Main-bearing cap-bushing
4Fly-wheel
5Fly-wheel key
6Fly-wheel key set-screw
7Crank-shaft
8Crank-disc
9Crank-disc key
10Crank-pin
11Crank-pin cap
12Crank-pin cap set-screw
13Connecting-rod cap
14Connecting-rod cap-bushing
15Connecting-rod
16Piston
17Piston-pin
18Piston-pin bushing
19Piston-pin set-screw
20Piston, inside ring
21Piston, outside ring
22Adjusting-bolt for piston-pin end of connecting-rod
23Connecting-rod bolt
24Guard-plate
25Air-head
26Air-head gasket
27Air-head studs
28Inlet valve and stem
29Inlet valve-seat
30Inlet valve-spring
31Inlet valve-stem head
32Inlet valve-stem cotter
33Inlet valve-bonnet
34Outlet valve
35Outlet valve-spring
36Outlet valve-bonnet
37Water inlet pipe
38Water outlet pipe
39Air inlet pipe
40Air outlet pipe
41Unloader
42Main-bearing grease-cup
43Crank-pin grease-cup
44Piston-pin grease-cup
45Air-cylinder lubricator
46Main-bearing studs
47Main-bearing liners
48Unloader regulating-cylinder

The Norwalk standard compressor is shown in Figs. [361] and [362], the latter being a longitudinal section; Fig. [361] is a perspective view; the two compressors are driven by a single steam cylinder having an adjustable cut-off. The air valves are operated by a positive crank motion.

A view of a Pelton water wheel operating a compressor it shown in Fig. [363]. The cut represents a compound air compressor in which the valves are operated mechanically. The water which drives the wheel enters through the pipe and nozzle secured in the wheel pit, as represented.

Fig. [364] exhibits a belted duplex air compressor built by Allis-Chalmers & Co.

Fig. [365] shows a vertical duplex compressor driven by a belt.

Fig. 369.

All the latter, as may be seen by the engravings, have the positive valve motion operated by an eccentric. In selecting an air compressor the following points need consideration: 1, Number of cubic feet of free air required per minute; 2, Altitude, i.e., the number of feet above the sea level; 3, Steam pressure and air pressure.

The use of compressed air for operating mining pumps, while having advantages in some cases, is not to be recommended in all, particularly on account of the low efficiency of the plant as a whole. The loss due to leaks is serious, and the long line of piping with its numerous joints causes much trouble, delay and expense.