(Part A) Machinerys Handbook 31st Edition Pages 1-1484

Heat Table 5. Average Specific Heats of Various Substances Substance Specific Heat Substance Machinery's Handbook, 31st Edition

370

Specific Heat 0.031 0.037 0.217

Alcohol (absolute) Alcohol (density 0.8)

0.700 Lead

0.622

Lead (fluid)

Aluminum Antimony Benzine Brickwork Cadmium Carbon Charcoal Brass

0.214 Limestone 0.051 Magnesia 0.450 Marble 0.094 Masonry, brick 0.200 Mercury 0.057 Naphtha 0.204 Nickel 0.200 Oil, machine 0.240 Paper 0.203 Phosphorus 0.094 Platinum 0.101 Quartz 0.215 Oil, olive

0.222 0.210 0.200 0.033 0.310 0.109 0.400 0.350 0.32 0.189 0.032 0.188 0.195 0.191 0.056 0.231 0.117 0.116 0.200 0.178 0.330 0.056 0.064 0.472 1.000 0.650 0.570 0.467 0.095

Chalk Coal Coke

Copper, 32 ° to 212 ° F (0–100 ° C ) Copper, 32 ° to 572 ° F (0–100 ° C )

Corundum Ether Fusel oil Glass Graphite Iron, cast Ice Gold

0.198 Sand 0.503 Silica 0.194 Soda 0.564 Silver

0.031 Steel, high carbon 0.201 Steel, mild 0.504 Stone (generally) 0.130 Sulfur 0.110 Sulfuric acid 0.115 Tin (solid) 0.126 Turpentine 0.122

Iron, wrought, 32 ° to 212 ° F (0–100 ° C) 32 ° to 392 ° F (0–200 ° C) 32 ° to 572 ° F (0–300 ° C) 32 ° to 662 ° F (0–350 ° C) Iron, at high temperatures: 1382 ° to 1832 ° F (750–1000 ° C) 1750 ° to 1840 ° F (954–1004 ° C) 1920 ° to 2190 ° F (1049–1199 ° C)

Tin (fluid) Water Wood, fir

0.213

0.218 Wood, oak 0.199 Wood, pine 0.500 Zinc

Kerosene

Table 6. Specific Heat of Gases

Constant Pressure

Constant Volume

Constant Pressure

Constant Volume

Gas

Gas

Acetic acid

0.412 0.238 0.453 0.508 0.217 0.245 0.121

… Chloroform

0.157 0.404 3.409 0.244 0.217 0.480

Air

0.168 0.399 0.399 0.171 0.176

Ethylene Hydrogen Nitrogen Oxygen Steam

0.332 2.412 0.173 0.155 0.346

Alcohol Ammonia Carbonic acid Carbonic oxide

Chlorine … Heat Loss from Uncovered Steam Pipes.— The loss of heat from a bare steam or hot- water pipe varies with the temperature difference between the inside of the pipe and the surrounding air. The loss is 2.15 Btu per hour, per square foot of pipe surface, per degree F of temperature difference when the latter is 100 degrees; for a difference of 200 degrees, the loss is 2.66 Btu; for 300 degrees, 3.26 Btu; for 400 degrees, 4.03 Btu; for 500 degrees, 5.18 Btu. Thus, if the pipe area is 1.18 square feet per foot of length, and the temperature difference 300 ° F, the loss per hour per foot of length = 1.18 3 300 3 3.26 = 1154 Btu.

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