TABLE 22

HEAT UNITS PER POUND AND

WEIGHT PER CUBIC FOOT OF WATER

BETWEEN 32 DEGREES FAHRENHEIT AND

340 DEGREES FAHRENHEIT

_________________________________

| | | |

|Temperature|Heat Units| Weight |

| Degrees | per | per |

| Fahrenheit| Pound |Cubic Foot|

|___________|__________|__________|

| | | |

| 32 | 0.00 | 62.42 |

| 33 | 1.01 | 62.42 |

| 34 | 2.01 | 62.42 |

| 35 | 3.02 | 62.43 |

| 36 | 4.03 | 62.43 |

| 37 | 5.04 | 62.43 |

| 38 | 6.04 | 62.43 |

| 39 | 7.05 | 62.43 |

| 40 | 8.05 | 62.43 |

| 41 | 9.05 | 62.43 |

| 42 | 10.06 | 62.43 |

| 43 | 11.06 | 62.43 |

| 44 | 12.06 | 62.43 |

| 45 | 13.07 | 62.42 |

| 46 | 14.07 | 62.42 |

| 47 | 15.07 | 62.42 |

| 48 | 16.07 | 62.42 |

| 49 | 17.08 | 62.42 |

| 50 | 18.08 | 62.42 |

| 51 | 19.08 | 62.41 |

| 52 | 20.08 | 62.41 |

| 53 | 21.08 | 62.41 |

| 54 | 22.08 | 62.40 |

| 55 | 23.08 | 62.40 |

| 56 | 24.08 | 62.39 |

| 57 | 25.08 | 62.39 |

| 58 | 26.08 | 62.38 |

| 59 | 27.08 | 62.37 |

| 60 | 28.08 | 62.37 |

| 61 | 29.08 | 62.36 |

| 62 | 30.08 | 62.36 |

| 63 | 31.07 | 62.35 |

| 64 | 32.07 | 62.35 |

| 65 | 33.07 | 62.34 |

| 66 | 34.07 | 62.33 |

| 67 | 35.07 | 62.33 |

| 68 | 36.07 | 62.32 |

| 69 | 37.06 | 62.31 |

| 70 | 38.06 | 62.30 |

| 71 | 39.06 | 62.30 |

| 72 | 40.05 | 62.29 |

| 73 | 41.05 | 62.28 |

| 74 | 42.05 | 62.27 |

| 75 | 42.05 | 62.26 |

| 76 | 44.04 | 62.26 |

| 77 | 45.04 | 62.25 |

| 78 | 46.04 | 62.24 |

| 79 | 47.04 | 62.23 |

| 80 | 48.03 | 62.22 |

| 81 | 49.03 | 62.21 |

| 82 | 50.03 | 62.20 |

| 83 | 51.02 | 62.19 |

| 84 | 52.02 | 62.18 |

| 85 | 53.02 | 62.17 |

| 86 | 54.01 | 62.16 |

| 87 | 55.01 | 62.15 |

| 88 | 56.01 | 62.14 |

| 89 | 57.00 | 62.13 |

| 90 | 58.00 | 62.12 |

| 91 | 59.00 | 62.11 |

| 92 | 60.00 | 62.09 |

| 93 | 60.99 | 62.08 |

| 94 | 61.99 | 62.07 |

| 95 | 62.99 | 62.06 |

| 96 | 63.98 | 62.05 |

| 97 | 64.98 | 62.04 |

| 98 | 65.98 | 62.03 |

| 99 | 66.97 | 62.02 |

| 100 | 67.97 | 62.00 |

| 101 | 68.97 | 61.99 |

| 102 | 69.96 | 61.98 |

| 103 | 70.96 | 61.97 |

| 104 | 71.96 | 61.95 |

| 105 | 72.95 | 61.94 |

| 106 | 73.95 | 61.93 |

| 107 | 74.95 | 61.91 |

| 108 | 75.95 | 61.90 |

| 109 | 76.94 | 61.88 |

| 110 | 77.94 | 61.86 |

| 111 | 78.94 | 61.85 |

| 112 | 79.93 | 61.83 |

| 113 | 80.93 | 61.82 |

| 114 | 81.93 | 61.80 |

| 115 | 82.92 | 61.79 |

| 116 | 83.92 | 61.77 |

| 117 | 84.92 | 61.75 |

| 118 | 85.92 | 61.74 |

| 119 | 86.91 | 61.72 |

| 120 | 87.91 | 61.71 |

| 121 | 88.91 | 61.69 |

| 122 | 89.91 | 61.68 |

| 123 | 90.90 | 61.66 |

| 124 | 91.90 | 61.65 |

| 125 | 92.90 | 61.63 |

| 126 | 93.90 | 61.61 |

| 127 | 94.89 | 61.59 |

| 128 | 95.89 | 61.58 |

| 129 | 96.89 | 61.56 |

| 130 | 97.89 | 61.55 |

| 131 | 98.89 | 61.53 |

| 132 | 99.88 | 61.52 |

| 133 | 100.88 | 61.50 |

| 134 | 101.88 | 61.49 |

| 135 | 102.88 | 61.47 |

| 136 | 103.88 | 61.45 |

| 137 | 104.87 | 61.43 |

| 138 | 105.87 | 61.41 |

| 139 | 106.87 | 61.40 |

| 140 | 107.87 | 61.38 |

| 141 | 108.87 | 61.36 |

| 142 | 109.87 | 61.34 |

| 143 | 110.87 | 61.33 |

| 144 | 111.87 | 61.31 |

| 145 | 112.86 | 61.29 |

| 146 | 113.86 | 61.27 |

| 147 | 114.86 | 61.25 |

| 148 | 115.86 | 61.24 |

| 149 | 116.86 | 61.22 |

| 150 | 117.86 | 61.20 |

| 151 | 118.86 | 61.18 |

| 152 | 119.86 | 61.16 |

| 153 | 120.86 | 61.14 |

| 154 | 121.86 | 61.12 |

| 155 | 122.86 | 61.10 |

| 156 | 123.86 | 61.08 |

| 157 | 124.86 | 61.06 |

| 158 | 125.86 | 61.04 |

| 159 | 126.86 | 61.02 |

| 160 | 127.86 | 61.00 |

| 161 | 128.86 | 60.98 |

| 162 | 129.86 | 60.96 |

| 163 | 130.86 | 60.94 |

| 164 | 131.86 | 60.92 |

| 165 | 132.86 | 60.90 |

| 166 | 133.86 | 60.88 |

| 167 | 134.86 | 60.86 |

| 168 | 135.86 | 60.84 |

| 169 | 136.86 | 60.82 |

| 170 | 137.87 | 60.80 |

| 171 | 138.87 | 60.78 |

| 172 | 139.87 | 60.76 |

| 173 | 140.87 | 60.73 |

| 174 | 141.87 | 60.71 |

| 175 | 142.87 | 60.69 |

| 176 | 143.87 | 60.67 |

| 177 | 144.88 | 60.65 |

| 178 | 145.88 | 60.62 |

| 179 | 146.88 | 60.60 |

| 180 | 147.88 | 60.58 |

| 181 | 148.88 | 60.56 |

| 182 | 149.89 | 60.53 |

| 183 | 150.89 | 60.51 |

| 184 | 151.89 | 60.49 |

| 185 | 152.89 | 60.47 |

| 186 | 153.89 | 60.45 |

| 187 | 154.90 | 60.42 |

| 188 | 155.90 | 60.40 |

| 189 | 156.90 | 60.38 |

| 190 | 157,91 | 60.36 |

| 191 | 158.91 | 60.33 |

| 192 | 159.91 | 60.31 |

| 193 | 160.91 | 60.29 |

| 194 | 161.92 | 60.27 |

| 195 | 162.92 | 60.24 |

| 196 | 163.92 | 60.22 |

| 197 | 164.93 | 60.19 |

| 198 | 165.93 | 60.17 |

| 199 | 166.94 | 60.15 |

| 200 | 167.94 | 60.12 |

| 201 | 168.94 | 60.10 |

| 202 | 169.95 | 60.07 |

| 203 | 170.95 | 60.05 |

| 204 | 171.96 | 60.02 |

| 205 | 172.96 | 60.00 |

| 206 | 173.97 | 59.98 |

| 207 | 174.97 | 59.95 |

| 208 | 175.98 | 59.93 |

| 209 | 176.98 | 59.90 |

| 210 | 177.99 | 59.88 |

| 211 | 178.99 | 59.85 |

| 212 | 180.00 | 59.83 |

| 213 | 181.0 | 59.80 |

| 214 | 182.0 | 59.78 |

| 215 | 183.0 | 59.75 |

| 216 | 184.0 | 59.73 |

| 217 | 185.0 | 59.70 |

| 218 | 186.1 | 59.68 |

| 219 | 187.1 | 59.65 |

| 220 | 188.1 | 59.63 |

| 221 | 189.1 | 59.60 |

| 222 | 190.1 | 59.58 |

| 223 | 191.1 | 59.55 |

| 224 | 192.1 | 59.53 |

| 225 | 193.1 | 59.50 |

| 226 | 194.1 | 59.48 |

| 227 | 195.2 | 59.45 |

| 228 | 196.2 | 59.42 |

| 229 | 197.2 | 59.40 |

| 230 | 198.2 | 59.37 |

| 231 | 199.2 | 59.34 |

| 232 | 200.2 | 59.32 |

| 233 | 201.2 | 59.29 |

| 234 | 202.2 | 59.27 |

| 235 | 203.2 | 59.24 |

| 236 | 204.2 | 59.21 |

| 237 | 205.3 | 59.19 |

| 238 | 206.3 | 59.16 |

| 239 | 207.3 | 59.14 |

| 240 | 208.3 | 59.11 |

| 241 | 209.3 | 59.08 |

| 242 | 210.3 | 59.05 |

| 243 | 211.4 | 59.03 |

| 244 | 212.4 | 59.00 |

| 245 | 213.4 | 58.97 |

| 246 | 214.4 | 58.94 |

| 247 | 215.4 | 58.91 |

| 248 | 216.4 | 58.89 |

| 249 | 217.4 | 58.86 |

| 250 | 218.5 | 58.83 |

| 260 | 228.6 | 58.55 |

| 270 | 238.8 | 58.26 |

| 280 | 249.0 | 57.96 |

| 290 | 259.3 | 57.65 |

| 300 | 269.6 | 57.33 |

| 310 | 279.9 | 57.00 |

| 320 | 290.2 | 56.66 |

| 330 | 300.6 | 56.30 |

| 340 | 311.0 | 55.94 |

|___________|__________|__________|

The gain due to superheat cannot be predicted from the formula for the

efficiency of a perfect steam engine given on page 119. This formula is

not applicable in cases where superheat is present since only a

relatively small amount of the heat in the steam is imparted at the

maximum or superheated temperature.

The advantage of the use of high pressure steam may be also indicated by

considering the question from the aspect of volume. With an increase of

pressure comes a decrease in volume, thus one pound of saturated steam

at 100 pounds absolute pressure occupies 4.43 cubic feet, while at 200

pounds pressure it occupies 2.29 cubic feet. If then, in separate

cylinders of the same dimensions, one pound of steam at 100 pounds

absolute pressure and one pound at 200 pounds absolute pressure enter

and are allowed to expand to the full volume of each cylinder, the

high-pressure steam, having more room and a greater range for expansion

than the low-pressure steam, will thus do more work. This increase in

the amount of work, as was the increase in temperature, is large

relative to the additional fuel required as indicated by the total heat.

In general, it may be stated that the fuel required to impart a given

amount of heat to a boiler is practically independent of the steam

pressure, since the temperature of the fire is so high as compared with

the steam temperature that a variation in the steam temperature does not

produce an appreciable effect.

The formulae for the algebraic expression of the relation between

saturated steam pressures, temperatures and steam volumes have been up

to the present time empirical. These relations have, however, been

determined by experiment and, from the experimental data, tables have

been computed which render unnecessary the use of empirical formulae.

Such formulae may be found in any standard work of thermo-dynamics. The

following tables cover all practical cases.

Table 22 gives the heat units contained in water above 32 degrees

Fahrenheit at different temperatures.

Table 23 gives the properties of saturated steam for various pressures.

Table 24 gives the properties of superheated steam at various pressures

and temperatures.

These tables are based on those computed by Lionel S. Marks and Harvey

N. Davis, these being generally accepted as being the most correct.

Steam, Its Generation and Use · 第 65 / 217 题