Steam, Its Generation and Use
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Babcock Wilcox Company. Steam, Its Generation and Use
Steam, Its Generation and Use
Table of Contents
FONDERIES ET ATELIERS DE LA COURNEUVE CHAUDIÈRES
6 RUE LAFERRIÈRE, PARIS. WORKS: SEINE—LA COURNEUVE
EDMOND DUPUIS J. H. R. KEMNAL ETIENNE BESSON IRÉNÉE CHAVANNE CHARLES A. KNIGHT JULES LEMAIRE
TELEGRAPHIC ADDRESS: "BABCOCK-PARIS"
THE EARLY HISTORY OF THE GENERATION AND USE OF STEAM
BRIEF HISTORY OF WATER-TUBE BOILERS[1]
REQUIREMENTS OF STEAM BOILERS
REQUIREMENTS OF A PERFECT STEAM BOILER
THE CIRCULATION OF WATER IN STEAM BOILERS
WATER-TUBE VERSUS FIRE-TUBE BOILERS
TABLE 1. PLATE THICKNESS REQUIRED FOR VARIOUS CYLINDER DIAMETERS. ALLOWABLE STRESS, 12000 POUNDS PER SQUARE INCH, 200 POUNDS GAUGE PRESSURE, NO JOINTS
TABLE 2
HEAT AND ITS MEASUREMENT
TABLE 3. COMPARISON OF THERMOMETER SCALES
F = 9/5C+32° = 9/4R+32° C = 5/9(F-32°) = 5/4R. R = 4/9(F-32°) = ⅘C
TABLE 4
TABLE 5. BOILING POINTS AT ATMOSPHERIC PRESSURE
TABLE 6. LINEAL EXPANSION OF SOLIDS AT ORDINARY TEMPERATURES
TABLE 7. ACCURACY OF HIGH TEMPERATURE MEASUREMENTS[7]
TABLE 8. APPROXIMATE MELTING POINTS OF METALS[8]
TABLE 9. CHARACTER OF EMITTED LIGHT AND CORRESPONDING APPROXIMATE TEMPERATURE[9]
THE THEORY OF STEAM MAKING
PROPERTIES OF WATER
TABLE 10. WEIGHT OF WATER AT TEMPERATURES USED IN PHYSICAL CALCULATIONS
TABLE 11. VOLUME AND WEIGHT OF DISTILLED WATER AT VARIOUS TEMPERATURES[12]
TABLE 12. BOILING POINT OF WATER AT VARIOUS ALTITUDES
TABLE 13. SPECIFIC HEAT OF WATER AT VARIOUS TEMPERATURES
BOILER FEED WATER
TABLE 14. APPROXIMATE CLASSIFICATION OF IMPURITIES FOUND IN FEED WATERS THEIR EFFECT AND ORDINARY METHODS OF RELIEF
TABLE 15. SOLUBILITY OF MINERAL SALTS IN WATER (SPARKS) IN GRAINS PER U. S. GALLON (58,381 GRAINS), EXCEPT AS NOTED
CALCIUM SULPHATE AT TEMPERATURE ABOVE 212 DEGREES (CHRISTIE)
TABLE 16. REAGENTS REQUIRED IN LIME AND SODA PROCESS FOR TREATING 1000 U. S. GALLONS OF WATER PER GRAIN PER GALLON OF CONTAINED IMPURITIES[16]
FEED WATER HEATING AND METHODS OF FEEDING
TABLE 17. SAVING IN FUEL, IN PER CENT, BY HEATING FEED WATER GAUGE PRESSURE 180 POUNDS
TABLE 18
STEAM
TABLE 19. FACTORS OF EVAPORATION CALCULATED FROM MARKS AND DAVIS TABLES
TABLE 20
TABLE 21
TABLE 22
TABLE 23. PROPERTIES OF SATURATED STEAM
TABLE 24. PROPERTIES OF SUPERHEATED STEAM
MOISTURE IN STEAM
SUPERHEATED STEAM
TABLE 25
TABLE 26
PROPERTIES OF AIR
TABLE 27. VOLUME AND WEIGHT OF AIR AT ATMOSPHERIC PRESSURE AT VARIOUS TEMPERATURES _______________________________________ | | | | | | Volume | | | Temperature | One Pound | Weight One | | Degrees | in | Cubic Foot | | Fahrenheit | Cubic Feet | in Pounds | |_____________|____________|____________| | | | | | 32 | 12.390 | .080710 | | 50 | 12.843 | .077863 | | 55 | 12.969 | .077107 | | 60 | 13.095 | .076365 | | 65 | 13.221 | .075637 | | 70 | 13.347 | .074923 | | 75 | 13.473 | .074223 | | 80 | 13.599 | .073535 | | 85 | 13.725 | .072860 | | 90 | 13.851 | .072197 | | 95 | 13.977 | .071546 | | 100 | 14.103 | .070907 | | 110 | 14.355 | .069662 | | 120 | 14.607 | .068460 | | 130 | 14.859 | .067299 | | 140 | 15.111 | .066177 | | 150 | 15.363 | .065092 | | 160 | 15.615 | .064041 | | 170 | 15.867 | .063024 | | 180 | 16.119 | .062039 | | 190 | 16.371 | .061084 | | 200 | 16.623 | .060158 | | 210 | 16.875 | .059259 | | 212 | 16.925 | .059084 | | 220 | 17.127 | .058388 | | 230 | 17.379 | .057541 | | 240 | 17.631 | .056718 | | 250 | 17.883 | .055919 | | 260 | 18.135 | .055142 | | 270 | 18.387 | .054386 | | 280 | 18.639 | .053651 | | 290 | 18.891 | .052935 | | 300 | 19.143 | .052238 | | 320 | 19.647 | .050898 | | 340 | 20.151 | .049625 | | 360 | 20.655 | .048414 | | 380 | 21.159 | .047261 | | 400 | 21.663 | .046162 | | 425 | 22.293 | .044857 | | 450 | 22.923 | .043624 | | 475 | 23.554 | .042456 | | 500 | 24.184 | .041350 | | 525 | 24.814 | .040300 | | 550 | 25.444 | .039302 | | 575 | 26.074 | .038352 | | 600 | 26.704 | .037448 | | 650 | 27.964 | .035760 | | 700 | 29.224 | .034219 | | 750 | 30.484 | .032804 | | 800 | 31.744 | .031502 | | 850 | 33.004 | .030299 | |_____________|____________|____________|
P = 144 (14.7 + 60.3) = 10,800
TABLE 28
TABLE 29. WEIGHTS OF AIR, VAPOR OF WATER, AND SATURATED MIXTURES OF AIR AND VAPOR AT DIFFERENT TEMPERATURES, UNDER THE ORDINARY ATMOSPHERIC PRESSURE OF 29.921 INCHES OF MERCURY
COMBUSTION
TABLE 30. KINDLING TEMPERATURE OF VARIOUS FUELS
TABLE 31. OXYGEN AND AIR REQUIRED FOR COMBUSTION. AT 32 DEGREES AND 29.92 INCHES
BY VOLUME
TABLE 32. CALCULATED THEORETICAL AMOUNT OF AIR REQUIRED PER POUND OF VARIOUS FUELS
ANALYSIS OF FLUE GASES
N 3.036 (—————) × C[30] (12) CO_{2} + CO
( CO ) L' = 10,150 × (—————) (17) (CO + CO_{2})
TABLE 33. CONVERSION OF A FLUE GAS ANALYSIS BY VOLUME TO ONE BY WEIGHT
TABLE 34. DENSITY OF GASES AT 32 DEGREES FAHRENHEIT AND ATMOSPHERIC PRESSURE ADAPTED FROM SMITHSONIAN TABLES
CLASSIFICATION OF FUELS
(WITH PARTICULAR REFERENCE TO COAL)
TABLE 35. APPROXIMATE CHEMICAL CHANGES FROM WOOD FIBER TO ANTHRACITE COAL
TABLE 36. APPROXIMATE COMPOSITION AND CALORIFIC VALUE OF GENERAL GRADES OF COAL ON BASIS OF COMBUSTIBLE
THE DETERMINATION OF HEATING VALUES OF FUELS
TABLE 37. WEIGHT AND CALORIFIC VALUE OF VARIOUS GASES AT 32 DEGREES FAHRENHEIT AND ATMOSPHERIC PRESSURE WITH THEORETICAL AMOUNT OF AIR REQUIRED FOR COMBUSTION
TABLE 38. APPROXIMATE COMPOSITION AND CALORIFIC VALUE OF CERTAIN TYPICAL AMERICAN COALS
TABLE 39. SHOWING RELATION BETWEEN PROXIMATE AND ULTIMATE ANALYSES OF COAL
N = 6, R = 0, R' = .01, T = 20.29, T' = 22.83,
COMBUSTION OF COAL
TABLE 40. ANTHRACITE COAL SIZES
SOLID FUELS OTHER THAN COAL AND THEIR COMBUSTION
TABLE 41. ULTIMATE ANALYSES AND CALORIFIC VALUES OF DRY WOOD (GOTTLIEB)
TABLE 42
TABLE 43
TABLE 44. VALUE OF ONE POUND OF MILL BAGASSE AT DIFFERENT EXTRACTIONS
TABLE 45
LIQUID FUELS AND THEIR COMBUSTION
TABLE 46. COMPOSITION AND CALORIFIC VALUE OF VARIOUS OILS
TABLE 47. RELATIVE VALUE OF COAL AND OIL FUEL
TABLE 48. TESTS OF BABCOCK AND WILCOX BOILERS WITH OIL FUEL
GASEOUS FUELS AND THEIR COMBUSTION
TABLE 49. TYPICAL ANALYSES OF BLAST FURNACE GAS
TABLE 50. TYPICAL ANALYSES (BY VOLUME) AND CALORIFIC VALUES OF NATURAL GAS FROM VARIOUS LOCALITIES
TABLE 51. TYPICAL ANALYSES OF BY-PRODUCT COKE OVEN GAS
UTILIZATION OF WASTE HEAT
TABLE 52. TEMPERATURE OF WASTE GASES FROM VARIOUS INDUSTRIAL PROCESSES
CHIMNEYS AND DRAFT
D = KH. (25)
TABLE 53. AVAILABLE DRAFT. CALCULATED FOR 100-FOOT STACK OF DIFFERENT DIAMETERS ASSUMING STACK TEMPERATURE OF 500 DEGREES FAHRENHEIT AND 100 POUNDS OF GAS PER HORSE POWER. FOR OTHER HEIGHTS OF STACK MULTIPLY DRAFT BY HEIGHT ÷ 100
FOR OTHER STACK TEMPERATURES ADD OR DEDUCT BEFORE MULTIPLYING BY HEIGHT ÷ 100 AS FOLLOWS[52]
TABLE 54. STACK CAPACITIES, CORRECTION FACTORS FOR ALTITUDES
TABLE 55. STACK SIZES BY KENT'S FORMULA. ASSUMING 5 POUNDS OF COAL PER HORSE POWER
TABLE 56. STACK SIZES FOR OIL FUEL. ADAPTED FROM C. R. WEYMOUTH'S TABLE (TRANS. A. S. M. E. VOL. 34)
EFFICIENCY AND CAPACITY OF BOILERS
TABLE 57. DATA FROM WHICH HEAT BALANCE (TABLE 58) IS COMPUTED
(11CO_{2}+8O+7(CO+N)) (—————————)C ( 3(CO_{2}+CO) )
TABLE 58. HEAT BALANCE. B. T. U. PER POUND DRY COAL 14,225
1. OBJECT
2. PREPARATIONS
3. FUEL
4. APPARATUS AND INSTRUMENTS[63]
5. OPERATING CONDITIONS
6. DURATION
7. STARTING AND STOPPING
8. RECORDS
9. QUALITY OF STEAM[67]
10. SAMPLING AND DRYING COAL
11. ASHES AND REFUSE
12. CALORIFIC TESTS AND ANALYSES OF COAL
13. ANALYSES OF FLUE GASES
14. SMOKE OBSERVATIONS[71]
15. CALCULATION OF RESULTS
16. DATA AND RESULTS
17. CHART
18. TESTS WITH OIL AND GAS FUELS
TABLE DATA AND RESULTS OF EVAPORATIVE TEST SHORT FORM, CODE OF 1912
AVERAGE PRESSURES, TEMPERATURES, ETC
TOTAL QUANTITIES
HOURLY QUANTITIES AND RATES
CAPACITY
ECONOMY RESULTS
EFFICIENCY
COST OF EVAPORATION
THE SELECTION OF BOILERS WITH A CONSIDERATION OF THE FACTORS DETERMINING SUCH SELECTION
TABLE 59
TABLE 60. ACTUAL EVAPORATION FOR DIFFERENT PRESSURES AND TEMPERATURES OF FEED WATER CORRESPONDING TO ONE HORSE POWER (34½ POUNDS PER HOUR FROM AND AT 212 DEGREES FAHRENHEIT)
OPERATION AND CARE OF BOILERS
BRICKWORK BOILER SETTINGS
TABLE 61. APPROXIMATE CLASSIFICATION OF FIRE BRICK
BOILER ROOM PIPING
TABLE 62. DIMENSIONS OF STANDARD AND EXTRA STRONG[76] WROUGHT-IRON AND STEEL PIPE
TABLE 63. TUBE DATA, STANDARD OPEN HEARTH OR LAP WELDED STEEL TUBES
TABLE 64. RADIATION FROM COVERED AND UNCOVERED STEAM PIPES. CALCULATED FOR 160 POUNDS PRESSURE AND 60 DEGREES TEMPERATURE
TABLE 65
FLOW OF STEAM THROUGH PIPES AND ORIFICES
TABLE 66
TABLE 67. FLOW OF STEAM THROUGH PIPES LENGTH OF PIPE 1000 FEET
TABLE 68
HEAT TRANSFER
W R = 2.00 + .0014 - A
INDEX
PAGE
FOOTNOTES
Отрывок из книги
Babcock & Wilcox Company
Published by Good Press, 2019
.....
Boston, Mass. 9600 Horse Power of Babcock & Wilcox Boilers and
Superheaters Installed in this Station]
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