The person charging this material is re¬ sponsible for its return to the library from which it was withdrawn on or before the Latest Date stamped below. Theft, mutilation, and underlining of books are reasons for disciplinary action and may result in dismissal from the University. To renew call Telephone Center, 333-8400 UNIVERSITY OF ILLINOIS LIBRARY AT URBANA-CHAMPAIGN MG i 1 1981 jul 2 i lira B o ’n L161—0-1096 LIBRARY OF THE UNIVERSITY OF ILLINfil'' THE BOILER BOOK The Hartford Steam Boiler Inspection and Insurance Company A Collection of Reliable Data For Use in the Design and Installation of Boilers and Other Pressure Vessels. Compiled by H. E. DART, Superintendent of Engineering Department The Hartford Steam Boiler Inspection and Insurance Co., Hartford, Conn. 1920 Copyright 1920 The Hartford Steam Boiler inspection and Insurance Company I \i\M< MTb PREFACE F OR MORE than forty years the designs of the Engineering Department of this Company have been accepted as standards throughout the United States and have been copied into the most authoritative engineering hand¬ books and textbooks as well as the trade catalogs of the best-known boiler makers and dealers in materials required for boiler construction. We comply with a great many requests for data on boiler design and installation, the sources of inquiry ranging from college professors to firemen, from well-known steel com¬ panies-and large boiler-shops to steam-fitters, plumbers and brick-masons in small towns, from Canadian Government commissions and English boiler¬ makers to Cuban sugar plantations, and from wood-pulp mills in Maine to saw¬ mills in Oregon and cotton plantations in Louisiana. Our designs and standards have been disseminated principally in the form of blue-prints, over 83,000 prints having been sent out since the Engineering . Department was established. As a rule, however, each blue-print covers only one single phase of some particular subject and we have often thought that it r would be worth while to assemble some of the more commonly used data in the form of a pamphlet. This idea has been more forcibly brought to our attention since the promulgation of the Boiler Code of the American Society of Mechanical Engineers and its adoption by several states and cities. We adopted the Code as a standard as soon as it was published and made such minor changes in our old drawings, as were needed to comply with its requirements. All our newer drawings, tables, and other data have been designed in accordance with the provisions of the Code and, in view of the many inquiries which we receive regarding the Code and its application, it seems that such data ought to be especially valuable to those who are trying to follow the Code requirements. With these ideas in mind we have collected and published the data which appears on the following pages for the use of our friends. This little book is not intended as a treatise on boiler design but merely as a collection in convenient form, of data which we have found valuable in our Engineering Department and which we hope will prove of equal value to those who may have occasion to use it. The designs contained herein represent our ideas as to good practice in < boiler construction but it should be understood that we necessarily insure many v-~ boilers which do not comply therewith. THE HARTFORD STEAM BOILER INSPECTION AND INSURANCE COMPANY November 20, 1920. Hartford, Conn. 1022174 3 4 The Hartford Steam Boiler Inspection and Insurance Co INDEX A American Standard, Drilling and other details for Flanges and Fittings.. Areas of Circles,. Areas of Segments to be stayed in H. T. boiler heads,. B Basic Principles. Braces, Arrangement in H. T. boilers.. Diagonal Crowfoot, Proportions of. Spacing.... Stresses and Areas sup¬ ported by. Through, Proportions of. Stresses and Areas supported by. Bracing Heads of H. T. boilers,. Bricks, Number required for H. T. boil¬ er settings,. Bumped Heads, Allowable pressures on Butt-Joints. See “Joints.” C Circles, Circumferences and Areas of. . Circumferential Seams. See “Girth Seams.” Columns for Supporting H. T. boilers, Cast Iron, Round and Square,. Steel, H-Beams. Plate-and-Angle,. Connections, Boiler. Minimum num¬ ber of Pipe Threads in. Cylindrical Shells, Girth seams of. Allowable Pressures on. D Decimal Equivalents of Common Frac¬ tions, . Dished Heads, Allowable Pressures on, F Flanges and Fittings, Drilling and other Details,. Fractions, Decimal Equivalents of,.... Furnaces, Unstayed. Allowable Pres¬ sures on.. G Girth Seams, H. T. boilers,. Cylindrical Vessels with Solid Unstayed Heads. Grates, Size of, for H. T. boilers,. J Page Page Joints, Butt. Double-riveted,. 7 56 Triple-riveted,. 8, 9 57 to 65 Quadruple-riveted. 10, 11 20, 21, 22 Lap. Double-riveted. 13 Girth Seams. 14, 15 Single-riveted,. 12 5 Joints, Riveted. 6 17, 18, 19 L 23 23 Lap Joints. See “Joints.” P Plates, Steel. Weight per square foot, 47 24 Pressures, Allowable on Cylindrical Shells,. 16 25 on Spherical Heads, 31 to 35 26, 27 on Unstayed Fur¬ naces. 36, 37 17 to 22 43 R Rivets, Shearing Strength of,. 5 31 to 35 Rivet Heads, Proportions for,. 6 57 to 65 Riveted Joints. See “Joints.” S Safety Valves for Power Boilers,. 51 Number and size of for Fire-tube boilers. 52, 53 49 50 Number and size of for Water-tube boilers,... 54, 55 Size of boiler connections for two or three. 51 50 Settings for H. T. boilers, Dimensions,. 42 56 General description. 40, 41 15 Number of bricks required for,. 43 16 Shearing Strength of rivets,. 5 Smoke-Openings, Size of for H. T. boilers 44 Spherical Heads, Allowable pressures on 31 to 35 Staybolts, Allowable loads on,. 29 57 Least angle for given number of threads. 30 31 to 35 Maximum pitch,. 28 Stays and Staying. See “Braces” and “Bracing”. Steel Plates, Weights per square foot. . 47 56 Suspension of H. T. boilers,. 48 to 50 57 T 36, 37 Threads, Pipe. Minimum number in boiler connections. 56 Staybolt. Least angle for given number of,. 30 14 Tubes, Arrangement of in H. T. boilers 17, 18, 19, 46 15 44 For Fire-tube boilers, Standard dimensions,. 38 For Water-tube boilers and sup¬ erheaters, . 39 H H-Beams as Columns for Supporting H. T. boilers. 50 Heads, Bracing of in H. T. boilers. 17 to 22 Spherical,. 31 to 35 Heating Surface of H. T. boilers,. 46 Heights for Setting H. T. boilers. 45 Horsepower of H. T. boilers. 46 I I-Beams for Suspending H. T. boilers, Sizes of. 48 U Uptakes, Size of for H. T. boilers. 44 Unstayed Furnaces, Allowable Pres¬ sures on,. 36, 37 V Valves, Safety. See “Safety Valves.” W Weights of boiler tubes. 38 of H. T. boilers,. 47 of Steel plates per square foot, 47 Water, Weight of in H. T. boilers. 47 November, 1920. The H artf or d Steam Boiler Inspection and Insurance Co. 5 BASIC PRINCIPLES. The general rules and working stresses used in calculating the tables which appear on the following pages, are given below. These values are used in all the work of our Engineering Department. Minimum factor of safety = 5. Tensile strength of steel plates = 55000 lbs. per sq. in. Resistance of steel plates to crushing = 95000 lbs. per sq. in. Strength of rivets in single shear = 44000 lbs. per sq. in. Strength of rivets in double shear = 88000 lbs. per sq. in. The cross-sectional area of rivets is taken as the area of the rivet holes, it being assumed that all rivets will be properly driven so as to entirely fill the holes. All calculations are based on the use of steel rivets conforming to the requirements of the A. S. M. E. Boiler Code; no figures are given for iron rivets. Allowable Shearing Strength of Steel Rivets. Diameter of Rivet After Driving Cross-Sectional Area of Rivet After Driving Shearing Strength Single Shear Double Shear 1 he"—0.6875" 0.37122 sq. in. 16334 lbs. 32668 lbs. K"—0.7500" 0.44179 “ “ 19439 “ 3887S “ .8125" 0.51849 “ “ 22814 “ 45628 “ —0.8750" 0.60132 “ “ 26458 “ 52916 “ 1 he"—0.9375" 0.69029 “ “ 30373 “ 60746 “ 1" —1.0000" 0.78540 “ “ 34558 “ 69116 “ 1 14"—1.0625" 0.88664 “ “ 39012 “ 78024 “ 1 he"—1 • 1875" 1.1075 “ “ 48730 “ 97460 “ 1 he"—1-3125" 1.3530 “ “ 59532 “ 119064 “ 1 he"—1.4375" 1.6230 “ “ 71412 “ 142824 “ 6 The H a rtf or d Steam Boiler Inspection and Insurance Co. STANDARD PROPORTIONS FOR RIVET HEADS r Straight Base Cone Head Pan Head Button Head Button Head Double Radius Steeple Head Countersunk Head Flat Head Button Head Dimensions May Be Larger Or '/\o Smaller Than Those Shown. f RIVETED JOINTS Our designs for riveted joints have probably been copied and used more widely than any other data which we have issued. About four years ago we decided to make a complete new set of detail drawings for these joints because the tracings were getting worn so badly that it was impossible to make good blue prints from them. It seemed that this would be a good time to make any changes'in design which might be desirable on account of variations in boiler- shop practices and customs, so we wrote to several boiler-makers, asking for copies of the tables which they were using and inviting suggestions for changes. In practically every case the boiler-maker returned a nearly exact copy of the standards which we had adopted years before and no suggestions were offered for any radical changes. In making the new drawings, however, we simplified the designs in some cases by eliminating some of the small fractions of an inch in pitch dimensions, and in some of the designs we had to increase the back- pitch slightly to comply with the requirements of the A. S. M. E. Boiler Code. The tables which follow on Pages 7 to 13 show the various standard types of riveted joints with complete dimensions and with efficiencies computed in accordance with our usual practice as outlined on Page 5. Detail drawings are available for all of the butt-joint designs. Designs are included for lap-joints though we seldom use this style of joint for longitudinal seams except in the cases of small vessels or vessels which will not be subjected to heat. Special designs will be found on Pages 14 and 15 for lap-joints to be used in circumferential seams. The H a rtf or d Ste am Boiler Inspection and Insurance Co. 7 DOUBLE-RIVETED BUTT-JOINTS Typical Details of Design. (See table below for dimensions, efficiencies, etc.) Thickness of Plate Thickness of Straps Diameter of Rivet Hole Efficiency % Long Pitch Short Pitch A B C E A" A" n As" 82.8 4" 2" SA" 4 A" l As" 2H" W A 'As" 82.8 4" 2" 8 A* 4X" l As" 2 A" As" 9 . 4 " 'As" ■ 81.9 4 A" 2 A" 9 A" 5" l A" 2As" n /32" 1 As " 81.9 4 A" 2A" 9A" 5" l A" 2 As" H” As' ' As " 81.9 4 A" 2 A" 9As" 5" l A" 2 As" 'W As" 'As" 81.9 4 A" 2 A" 9A" 5" 1 A" 2 As" As" Vs" 'As" 81.3 5" 2 A" 11 A" 5 A" lAs" 2 A" H" 'As" 81.3 5" 2 A" nA" 5 A" lAs" 2 A" A" ‘As" 'As" 81.3 5" 2 A" 11 A* 5 A" l As" 2 A" NOTE—All joints in the above table fail by tearing the plate between rivet holes in the outer naw. For convenience in driving rivets the back-pitch (dimension E) may be increased, if desired, without affecting the joint efficiency, but it should not be decreased. 8 The Hartford Steam Boiler Inspection and Insurance Co. TRIPLE-RIVETED BUTT-JOINTS External View Typical Details of Design I" or dimensions, efficiencies, etc., see table on opposite page. The H a r tf or d Steam Boiler I ns p ection and Insurance Co 9 TRIPLE-RIVETED BUTT-JOINTS Table of Dimensions and Efficiencies (Letters refer to sketch on opposite page.) Thickness of Plate Thickness of Straps Diameter of Rivet Hole Efficiency % * Long Pitch Short Pitch A B c D E 4" 4" “4" 87.5 54" 24" 12" 734" 1 Vie" 14" 24" 9 4" X" n 4t 87.5 54" 234" 12" 734" 1 He" 14" 24 " 4o" 4" 13 4" 87.5 64" 34" 134" 834" 1 4" 14" 2Vfe" n 4" At 13 4" 87.5 64" 34" 134" 84" 1 4" 14" 24" 4" *At 13 4" 88.4 7" 34" 134" 84" 1 4" 14" 2 Vie" 13 4" 13 4" 88.4 7" 34" 134" 834" 1 4" 14" 2 Vie" W 4" 15 4" 87.9 7 4" 34" 154" 94" 1 Vie" 2" 24" H" 15 4" 87.9 74" 34" 154" 94" 1 7 4e" 2" 234" 4" W 15 4" 88.3 8" 4" 154" 94" 1 7 4e" 2" • 234" 11 At 7 4e" 15 4" 88.3 8" 4" 154" 934 " 1 Vfe" 2" 234" %" 7 4e" 1 At 86.7 8" 4" 17" 11" 1 4" 24" 3" 19 4" 4" l 14" 86.7 8" 4" 17" 11" 1 4" 24 " 3" 4" 4" 1 14" 86.7 8" 4" 17" 11" 1 4" 24 " 3" 4" l 14" 86.7 8" 4" 17" 11" 1 34 " 24 " 3" n Ac>" 4" l Vie" 85.6 84" 44" 184" 12" l 13 4e" 23/6" 34" 23 4>" X” 1 14" 85.6 84" 44" 184" 12" I’Vfe" 24" 34" 4" , 4" l *4" 85.5 84" 44" 184" 12" 1 13 4e" 24 " . 34" 25 4>" %" 1 14" 84.6 84" 44" 204 " 134" 2" 24 " 34 " n At 9 fe" i 4" 84.6 8 X" 44" 20 4 " 134" 2" 24" 34" 21 At 9/'' -'16 1 14" 84.2 84" 44" 204" 134" 2" 24" 34 " 4" 4" 1 5 4"* 84.1 84" 434" 204" 134" 2" 24 " 34" 29 4" 4" l 14" 83.6 834" 44 " 204" 134" 2" 24" 34" 15 4e" l %" l 14" 83.7 9" 44" 204 " 134" 2" 24" 34" 3 14" n A&" 1 14" 83.2 9" 44 " 204" 134" 2" 24" 34 " r X" l 14" 83.4 94" 44" 22" 14 4" 9 3/ " ^ /16 24" 34" NOTE—Joints for plate thicknesses from 2 %" to 1" (both inclusive) fail by tearing the plate between rivet holes in the second row and shearing a rivet in the outer row; this also applies to the joint for the Y" plate. All other joints in the above table fail by tearing the plate between rivet holes in the outer row. For convenience in driving rivets, either of the dimensions for back-pitch (D and E) may be increased without affecting the joint efficiency, but they should not be decreased. 10 The H a rtf or d Steam Boiler Inspection and Insurance Co. QUADRUPLE-RIVETED BUTT-JOINTS External View Typical Details of Design For dimensions, efficiencies, etc., see table on opposite page. The Hartford Steam Boiler Inspection and Insurance Co 11 QUADRUPLE-RIVETED BUTT-JOINTS Table of Dimensions and Efficiencies Thick¬ ness of Plate Thick¬ ness of Straps Diam. of Rivet Hole Effici¬ ency % Long Pitch Middle Pitch Short Pitch A B C D E F X" X" X VY 93.8 11 " 5X" 2X" 16X" 7X" 1 Ye" IX" 2X" 2 X" \Y X" l Ye" 93.8 11 " 5 X" 2X" 16X" 7X" 1 Ye" IX" 2YY 2 X" VY 9 4" l Ye" 93.8 13" 6 X" 3X" 18X" 8 X" 1 X" i YY 2VY 2 X" X VY vy x Ye" 93.8 13" 6 X" 3X" 18 YY 8 X" 1 X" l YY 2VY 2 X" YY Ye" l Ye" 94.2 14" 7" 3X" 19X" 8 X" 1 X" 1 YY We" 2 X" X VY Ye" l Ye" 94.2 14" 7" 3X" 19X" 8 X" l X" IYY We" 2 X" Ye" H" l Ye" 94.0 15X" 7X" 3 VY 21 YY 9X" 1 Ye" 2 " 2X" 3 VY X W H" l Ye" 94.0 15X" 7X" 3 VY 21 YY 9X" 1 Ye" 2 " 2X" 3 VY X" Ye" x Ye" 94.1 16" 8 " 4" 21 X" 9 X" 1 Ye" 2 " 2X" 3 VY VY Ye" X VY 94.1 16" 8 " 4" 21 YY 9X" 1 Ye" 2 " 2 X" 3 YY Ye" Ye" l Ye" 94.1 16" 8 " 4" 21 X" 9X" 1 Ye" 2 " 23X" 3 VY l *h” X" 1 Ye" 93.4 16" 8 " 4" 23X" 11 " 1 X" 2 X" 3" 3 VY YY X" 1 Ye" 93.4 16" 8 " 4" 23 VY 11 " 1 YY 2 X" 3" 3 VY X" 1 Ye" 93.4 16" 8 " 4" 23 YY 11 " 1 YY 2X" 3" 3 VY 1 Ye" X" 1 Ye" 92.8 16X" 8 X" 4X" 25 X" 12 " We" 2 X" 3X" 3 VY 2 VY X" 1 Ye" 92.8 16X" 8 X" 4X" 25X" 12 " We" 2 YY 3X" 3 VY YY X" 1 Ye" 92.7 16X" 8 X" ' 4X" 25X" 12 " We" 2YY 3X" 3 VY Ye" 1 Ye" 92.3 17" 8 X" 4X" 2,1 YY 13X" 2" 2 YY 3X" 3 X VY l Ye" *16 1 Ye" 92.3 17" 8 X" 4X" .21 YY 13X" 2 " 2 YY 3X" 3 13 4" Ye" 1 Ye" 91.8 17" 8 X" 4X" 21 YY 13X" 2 " 2 YY 3X" 3 X VY YY YY- 1 Ye" 91.2 17 YY 8 X" 4X" 28" 13 X" 2 " 2 YY 3X" 3 VY YY YY 1 Ye" 90.5 17 X* 8 X" 4X" 28" 13X" 2 " 2 YY 3X" 3 YY X VY x Ye" 1 Ye" 90.1 18" 9" 4X" 28X" 13X" 2 " 2 YY 3X" 3WY 3 VY l Ye" 1 Ye" 89.5 18" 9" 4 X" 28 YY 13X" 2 " 2 YY 3X" 3 X VY 1" X" ’ 1 Ye" 90.2 19" 9X" 4X" 30 X" 14X" 2 Ye" 2 YY 3X" 4 X" l W X" 1 Ye" 89.6 19" 9X" 4X" 30X" 14 X" 2 Ye" 2 YY 3X" 4 X" 1 Ye" X" 1 Ye" 89.0 19" 9X" 4X" 30X" 14X" 2 Ye" 2 YY 3X" 4 X" l VY X" 1 Ye" 88.5 19" 9 X" 4X" 30X" 14X" 2 Ye" 2 YY 3X" 4 X" 1 X" X" 1 Ye" 88.0 19" 9X" 4X" 30X" 14X" 2 Ye" 2 YY 3X" 4 X" 1 VY X" 1 Ye" 87.5 19" 9X" 4X // 30 YY 14X" 2 Ye" 2 YY 3X" 4 X" 1 Ye" VY 1 Ye" 87.7 20" 10" 5" 30X" 14 X" 2 Ye" 2 YY 3X" 4 VY 1 VY l Ye" 1 Ye 87.2 20" 10" 5" 30X" 14 X" 2 Ye" 2 YY 3X" 4 VY l X" VY ' 1 Ye" 86.8 20" 10" 5" 30 YY 14X" 2 Ye" 2 YY 3X" 4 VY NOTE—Joints for plate thicknesses from to 1 y A " (both inclusive) fail by tearing the plate between rivet holes in the third row and shearing the rivets in the two outer rows; this also applies to the joint for the Ti" plate. All other joints in the above table fail by tearing the plate between rivet holes in the outer row. For convenience in driving rivets, any of the dimensions for back-pitch (dimensions D, E, and F) may be increased, if desired, without affecting the joint efficiency, but they should not be decreased. 12 The Hartford Steam Boiler Inspection and Insurance Co. SINGLE-RIVETED LAP-JOINTS Typical Details of Design (See table below for dimensions, efficiencies, etc.) Thickness of Plate Diameter of Rivet Holes Efficiency % Pitch A Method of Failure X" 60.7 IX" l%" T. P. l W 60.3 IX" lWe" S. R. 13 4 " 59.4 2" IX" T. P. U A" 59.4 2" IX" T. P. X" 1S A" 58.3 2X" T. P. w l %" 58.3 2X" m* T. P. W' i %" 57.5 2X" IX" T. P. U A* i %>" 57.5 2X" IX" T. P. y*" i w 56.7 2X" IX" S. R. NOTE—In the column headed “Method of Failure,” “T. P.” indicates that the joint will fail by tearing the plate in the net section between rivet holes; “S. R.” means that the failure will be due to shearing rivets. The Hartford Steam Boiler Inspection and Insurance Co. 13 DOUBLE-RIVETED LAP-JOINTS Typical Details of Design (See table below for dimensions, efficiencies, etc.) Thickness of Plate Diameter of Rivet Holes Efficiency % Pitch A B A" 69.5 2^" l%" l A" Ik" 1 We" 69.5 2X" IWe" l A" A," 69.1 2H" 1A" 1 H" 69.1 2H" 1A" 1H" H" 68.9 3" VAS 2" 'AS 15 4" 68.9 3" w 2" W l W 68.5 sy&" 1H" 2A" 15 4" l W 68.5 1H" 2As" K" 1 %" 68.5 3 H” l H" 2'A" NOTE—All joints described by the above table will fail by tearing the plate in the net section between rivet holes. 14 The Hartford Steam Boiler Inspection and Insurance Co. LAP-RIVETED JOINTS FOR GIRTH SEAMS OF HORIZONTAL TUBULAR BOILERS In cases like that usually found in horizontal tubular boilers where 50% or more of the load which would act on an unstayed solid head of the same diameter as the shell, is relieved by the effect of tubes or through stays, the strength of the circumferential joints in the shell should be at least 35% of that required for the longitudinal joints; and when such circumferential joints are exposed to the products of combustion, the shearing strength of the rivets should be not less than 50% of the full strength of the plate corresponding to the thick¬ ness at the joint. The following table of single-riveted lap-joints is designed to meet the above conditions, using rivets of the same size as those in our standard designs for butt-joints. We do not advise the use of plates thicker than when the girth seams, under pressure, are exposed to. the fire or products of com¬ bustion and the table is therefore not extended beyond this limit. Thickness of Plate Diameter of Rivet Holes Pitch of Rivets ' \ Efficiency 1 of Joint Shearing Strength of Rivets in per cent of Solid Plate K" IK" 60.7 67.9 u /6" IK" 60.3 60.3 x *4" IK" 56.7 70.8 13 4" IK" 56.7 64.4 K" IK" 56.7 59.1 13 4" IK" 54.5 54.5 W 15 /fc" 2K" 55.9 59.4 'W 15 Te" 2K" 55.4 55.4 K" 15 4" 2K" 52.0 52.0 '■bo" 2 Kg" 50.4 50.4 %" 1 %" 2K" 53.3 53.3 In portions of girth seams which will be subjected to the hot fire, the rivet¬ ing should be started at the bottom of the boiler and carried up continuously on both sides, reaming the holes anew as the seam is riveted up to the full diameter of the boiler. I 15 The Hartford Steam Boiler Inspection and Insurance Co. LAP-RIVETED JOINTS FOR GIRTH SEAMS OF CYLINDRICAL VESSELS WITH SOLID UNSTAYED HEADS In horizontal tubular boilers, tanks and similar vessels it is customary for the sake of convenience, to use the same size of rivets in the girth seams as in the longitudinal seams. Where the heads of such vessels are not stayed by tubes or through braces the strength of the circumferential joints should be at least 50% of that required for the longitudinal joints of the vessel. The joints in the table below are designed to meet the above requirements and it should be under¬ stood that a higher efficiency could be obtained in some instances by using a different size of rivets. It is assumed in each case that the efficiency of the corresponding longitudinal joint is not greater than that of our standard design for Quadrupled-Riveted Butt-Joints as shown on Page 11. Thickness of Plate Diameter of Rivet Holes Single-Riveted Lap Joints Double-Riveted Lap Joints Pitch of Rivets Efficiency of Joint Pitch of Rivets Efficiency of Joint K" u 4" IK" 60.7 9 4" u 4" IK" 60.3 5 4" 13 4" IK" 56.7 “K" 13 4" IK" 56.7 H" 13 4" IK" 56.7 i3 4" 13 4" IK" 54.5 7 4" 15 4" 2 K" 55.9 ,5 4" 2K" 55.4 K" 15 -4" 2K" 52.0 17 4" 15 4" 214" 50.4 3" 68.8 9 ,6" 1 Kb" 2 K" 53.3 3K" 67.3 19 *32 1 Wb" > 3K" 67.3 K" l 14" 3K" 67.3 21 4" 1 14" 3K" 66 .5 u 4" l %* 3K" 68.3 2S 4" 1 Vb" 3K" 65.8 K" l 3 4" 3K" 63.0 25 4" i 5 4" 4" 67.2 13 4" l %!' 4" 66.6 27 4" 1 5 4" 4" 64.1 K" 1 5 4" 4" 61.9 29 4" 1 5 4" 4" 59.7 15 4" l 14" 4" 57.7 3 *4" l 5 4" 4" 55.9 l" l 7 4" 4 K" 57.7 l 14" l 7 4" 4K" 56.0 i Kb" l 7 4" 4K" 54.3 l 3 4" 1 7 4" 4K" 52.S i k" l 7 4" 4K" 51.3 l /4" l 7 4" 4K" 49.9 1 3 4" l 7 4" 4K" 48.6 l w 1 7 4" 4K" 47.4 1 K" l 14" 4K" 46.2 ALLOWABLE WORKING PRESSURES ON CYLINDRICAL SHELLS 16 The Hartford Steam Boiler Inspection and Insurance Co. _) PI W a m a O a W H W S <3 HH Q * 00 o t-H Qd. 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Rvt. ^OO^OC03COCD 00H^NO^DD03 003CO^CCNXQH rHrHr—IHHHHHfM o CO -S 4H a > h a C0fd'MCI0k0M'OJ>00c0O»O'-U>CD050005O'-U>05iO»0t0 COONmCJffiiOHOlCCOMHNOHOHCOOMOlCJffiCJO COiOtOCCOHfOiOtDOOOl^COMiONCOCinM'tDNCO HHHHNCICICJCIlMCincommMCOMMMMMMMiO Dbl. Rvt. iOCO^OGCOCOOOt}! CD 03 O 03 CO 03 X 03rfl0l>XO^C0^ T-Hi— J rHrHrH0303 03 03 lo a b/o a Pm o pp a a o -4—I 0) r- 1 H W H C/3 a ,ja a a co X P4 a - •—I a cr h * o ° n +-* C/3 . a £ P^ PC a3 —- 03 aJ ^ 5- 1 rH a G C/3 C/3 C/3 a a Lh +J a a C/3 a .a a . pp cr a C/3 a a c £ ^4 a “a PP a r- ^ bjo.S a C/3 o 'a x a £ C/3 a a +j a buo a o a C/3 a a o a 4-> C/3 a P4 a a £ a -m s a * f-H “ c £ a a .£ ’a bE a C/3 a » rH ”0 a a a ap >> 4-> a M-i a C/3 a O a a p t s. o M-h H a a r-1 a H a r— also. in a a a 17 The Hartford Steam Boiler Inspection and Insurance Co. ' oooooo ooooooo .'eftOOOOOO (1 ' 's>s oooooo v /OI ) OC) O O O / to/ 'o/OOOOOO ( •O', «b\OOOOOO V Vo) Voj()0()000 x \ P> OOOOOO ( ooooooo V' 9/ oooooo 4 - 3" Tubes 52-3^" Tubes 46-4" Tubes # ^ e Arrangement Of Tubes And Braces In 60 Inch Horizontal Tubular Boilers 18 The Hartford Steam Boiler Inspection and Insurance Co. OOOO ooooo ooooo ooooo OOOO / OOOO \ ooooo ooooo ooooo OOOO <0 Ui m D h k I VO 10 •o', ooooo X *OOOOOO \ '9-0000000^ ooooooo® ^OOOOOO ?/ OOOOOO f 2 OODOOO V- 4 OOOOOO ^ ^ 0000000 ^ ,0) 0000000^ NOOOOOO y *00000 / OOOO X OOOOOO 0000000 ooooooo, OOOOOO 1 OOOOOO/ ooooo ( oooool OOOOOOV OOOOOO ( 0000000 0000000 OOOOOO OOOO <0 or lii _J o CO OC < -J O m O H _l < I- z o N 0 : O I r o z vD >0 z «n UJ o < q: CD Q z < ooooooo^ oOooooo^ OOOOOO OOOOOO/^ OOOOOOVz OOOOOO v — 8088888® 0600000 / OOOOOO / 0600 X OOOO \ OOOOOO X 0000000 \ 00000000 N Qg RRRRR°<§> /O' 00000000 - :°: OOOOOOOO sr? 5\ W OOOOOOOO ( v ?' ,'o\ OOOOOOOO V s - roN \o; OOOOOOOO \o: ' OOOOOOOO ^ ,','ON OOOOOOOOO© o', \ojOOOOOOOOO '' ,0-, OOOOOOOO 7 v OOOOOOOO X X 0000 X Arrangement Of Tubes And Braces In 72 Inch Horizontal Tubular Boilers The H a rtf or d Steam Boiler Inspection and Insurance Co. 19 oqooo N OOOOOOO OOOOOOOO oooooooo OOOOOOO OOOOOOO / OOOOOOO OOOOOOO V OOOOOOO OOOOOOO oooooooo •oooooooo OOOOOOO OOOOO y ooo X OOOOO\ oooooo \ oooooo oooooo# OOOOO ^ OOOOO OOOOO / V OOOOO V h OOOOO OOOOO _ oooooo# oooooo OOOOOO / OOOOO / ooo y if) X LU _J o CD X < D CD D H _l < h z o N X o X I u z oo N z oooooooo A> oopooooo V = oooooooo ^ oooooooo ~ ooooooooo^ oopoooooo , oopooooo / oopoooo y ooooo / OOOOOO X v oopooooo N oopoooooo oopooooooo oooooooooo oooooooooo ooooooooo ooooooooo . ooooooooo / oopoooooo \ oopoooooo v oopoooooo oooooooooo oooooooooo oooooooooo •ooooooooo OOOOOOOO y oooooo 176-3" Tubes 138-3^" Tubes 108-4" Tub Arrangement Of Tubes And Braces In 84 Inch Horizontal Tubular Boilers 20 The H a rtf or d Steam Boiler Inspection and Insurance Co. AREAS TO BE STAYED IN HEADS OF HORIZONTAL TUBULAR BOILERS A | > i " t OOOOOOOO OTO o o o o O O O O O O 0|0 o o o o o o _r -JO o o o o o o OOOOOOOiOOOOOOO O O O O O O 'O o o o o o o o oooooo oooooo Odd 0-0 Old 0.0 Odd The diagram above shows a typical layout of tubes in the head of a hori¬ zontal tubular boiler, the areas which require bracing being indicated by shading. The distance of two inches (2") from the tubes where bracing is not required is taken as a constant for all sizes of boilers, all pressures and all head thicknesses but the distance supported by the flange of the head (indicated by the letter d) is dependent upon the pressure and the thickness of the head in each case. Values of d may be determined from the following table which is based on the formula: d_«i v p where d = unstayed distance from shell in inches. P = maximum allowable working pressure in pounds per sq. in. T = number of sixteenths of an inch in head thickness (T = 8 for head, 9 for head, etc.) The Hartford Steam Boiler Inspection and Insurance Co. 21 AREAS TO BE STAYED IN HEADS OF HORIZONTAL TUBULAR BOILERS—(Continued) Value of d or Distance Supported by Flange of Head Wrkng Pres.— Thickness of Head (Inches) ids. per sq. in. H 14 K % H n 4 V* 13 4 V* 1.0 50 4.24 4.95 5.66 6.36 7.07 7.78 8.49 9.19 9.90 10.61 11.31 60 3.87 4.52 5.16 5.81 6.46 7.10 7.75 8.39 9.04 9.68 10.33 70 3.59 4.18 4.78 5.38 5.98 6.57 7.17 7.77 8.37 8.96 9.56 SO 3.35 3.91 4.47 5.03 5.59 6.15 6.71 7.27 7.83 8.39 8.94 90 3.16 3.69 4.22 4.74 5.27 5.80 6.33 6.85 7.38 7.91 8.43 100 3.00 3.50 4.00 4.50 5.00 5.50 6.00 6.50 7.00 7.50 8.00 110 2.86 3.33 3.81 4.29 4.77 5.24 5.72 6.20 6.67 7.15 7.63 120 2.75 3.21 3.66 4.12 4.58 5.04 5.50 5.96 6.42 6.88 7.33 125 2.68 3.13 3.58 4.03 4.47 4.92 5.37 5.81 6.26 6.71 7.16 130 2.63 3.07 3.50 3.95 4.38 4.82 5.26 5.70 6.14 6.57 7.00 140 2.53 2.95 3.38 3.80 4.22 4.64 5.07 5.49 5.91 6.33 6.76 150 2.45 2.85 3.26 3.67 4.08 4.49 4.90 5.31 5.71 6.12 6.53 160 2.37 2.77 3.16 3.56 3.95 4.35 4.74 5.14 5.53 5.93 6.32 170 2.30 2.68 . 3.06 3.44 3.83 4.22 4.60 4.98 5.37 5.75 6.13 180 2.23 2.60 2.98 3.35 3.72 4.10 4.47 4.84 5.21 5.59 5.96 190 2.17 2.54 2.90 3.26 3.63 3.99 4.35 4.72 5.08 5.44 5.80 200 2.12 2.47 2.83 3.18 3.54 3.89 4.24 4.59 4.95 5.30 5.66 The outside radius of the flange of the head may be used for d if such radius is greater than the value given in the above table for the required pressure and thickness of head, except that the value obtained in this manner must not be greater than eight (8) times the thickness of the head. Referring again to the diagram on Page 20, the area of the rectangle shown by the wide cross-hatching can be easily determined from its length and width and the area of either segment can be calculated from the formula . 4(H-d-2) 2 / 2(R-d) 77 no Area ~ 3 V (H-d-2) °' 608 where H = distance from top (or bottom) of tubes to shell in inches. R = radius of the boiler head in inches, d = unstayed distance from shell in inches. Our Engineering Department can furnish blue-prints of a table giving areas of segments based on this formula for different values of the two terms (H-d-2) and (R-d) but the table is too large to print conveniently in a book of this size. On the following page, however, will be found a table giving areas of segments for cases where d (as defined above) is equal to three inches (3"). It will be found that the calculated value of d is usually greater than 3 inches and, in such cases, the areas given in the table will therefore be somewhat larger than actually required so that they will be on the safe side. 22 The Hartford Steam Boiler Inspection and Insurance Co AREAS TO BE STAYED IN HEADS OF HORIZONTAL TUBULAR BOILERS—(Concluded) Table Showing Net Areas of Segments of Heads Where d (as defined on Pages 20 and 21) is Equal to Three Inches (3") Height from Tubes to Diameter of Boiler (Inches) 24 30 36 42 48 54 60 66 72 7S 84 90 96 Shell, (Ins.) Area to be stayed, Sq. In. 8 28 33 37 40 43 47 51 53 55 58 60 63 65 8 K 35 41 46 51 55 59 63 66 70 74 76 80 82 9 42 49 56 62 67 72 76 82 86 90 92 95 98 9K 50 58 66 70 80 86 91 96 101 105 111 116 119 10 57 68 77 85 93 99 106 112 117 123 129 132 137 10K 66 78 89 98 107 114 123 131 135 142 147 153 160 11 74 88 100 111 121 130 138 147 155 161 169 174 183 11K 83 99 112 124 137 146 156 165 173 181 189 196 204 12 91 109 125 139 151 163 174 184 194 203 213 219 230 12K 120 138 153 167 180 193 204 216 224 234 243 252 13 132 151 168 183 197 211 224 235 247 256 267 279 13K 143 164 183 200 216 230 246 258 270 282 293 302 14 155 178 199 217 234 250 266 280 294 305 319 331 14^ 167 192 215 235 254 271 287 303 318 333 345 360 15 178 206 231 252 273 291 309 326 343 357 372 386 15K 220 247 271 291 312 332 350 368 382 400 417 16' " 235 263 289 312 334 355 374 394 411 423 443 16^ 249 281 308 332 357 380 399 420 436 457 475 17' 264 297 326 353 378 402 425 447 467 486 502 17K 314 345 374 400 426 449 471 494 516 536 18' " 331 365 396 424 450 476 500 520 543 564 18U 349 384 417 448 476 501 526 552 577 598 19 366 404 439 470 500 529 555 580 604 631 19K ► • • • 384 424 461 496 528 558 584 613 641 663 20' 401 444 483 519 552 583 613 642 667 699 20 K 464 505 543 578 613 643 675 706 729 21 485 528 568 604 640 673 705 733 766 21K 505 551 594 632 669 703 739 766 797 22' 526 574 618 658 697 734 769 800 835 22 K 597 643 687 726 765 800 835 867 23 620 668 713 754 796 830 869 906 23 K 642 695 740 784 827 866 904 945 24' 667 719 768 814 859 897 939 978 24 K 689 745 797 843 892 934 975 1018 25 714 771 825 875 922 966 1010 1051 25 K 737 798 855 907 956 1003 1047 1092 26' 761 824 882 936 987 1035 1083 1126 26K 850 909 968 1024 1073 1120 1167 27 877 939 998 1053 1106 1157 1202 27 K 904 968 1030 1089 1145 1195 1243 28' . .930 997 1060 1120 1177 1232 1279 28 K 1028 1092 1157 1211 1270 1321 29 1056 1123 1187 1248 1305 1360 29 K 1084 1155 1221 1284 1347 1400 30 1115 1187 1255 1321 1382 1442 30K 1218 1290 1358 1424 1480 31 1252 1324 1394 1459 1523 31K 1286 1359 1433 1496 1561 32 1317 1394 1467 1538 1605 32K 1430 1508 1575 1650 33 1465 1542 1617 1687 33 K 1500 1578 1655 1733 34 1536 1617 1695 1770 34 K 1654 1735 1816 35 1692 1775 1856 35H 1810 1900 36 1857 1941 36K 1984 37 2026 The H ar tf or d Ste am Boiler Inspection and Insurance Co. 23 PROPORTIONS OF DIAGONAL CROWFOOT STAYS Diagonal crowfoot stays should be made of solid, weldless mild steel. Each branch of a crowfoot should be designed to carry two-thirds of the total load for which the stay is designed, the fulfilment of-this requirement being proved by tests, if necessary. To develop the full strength of a stay, the com¬ bined cross-sectional area of the two rivets at each end should be at least one and one-quarter (lf4) times the cross-sectional area of the body of the stay. The net cross-sectional area through the center of each rivet hole in the blade of the stay should also be at least equal to one and one-quarter (1}4) times the cross- sectional area of the body of the stay, and the net area through the center of each rivet hole in the crowfoot should be at least one-half (}4) of the net area through a rivet hole in the blade. The following table has been calculated to meet the above requirements. Diameter Cross-sectional area Minimum Diam. Minimum cross-sectional Minimum cross-sectional of stay of body of stay of rivet holes area at A-A area at B-B 1 H* 0.9940 sq. in. 15 Ae" 1.2425 sq. in. 1.3844 “ “ 0.6213 sq. in.. 1%" 1.1075 “ “ 1" 0.6922 “ “ IJ4" 1.2272 “ “ 1" 1.5340 “ “ 0.7670 “ “ SPACING OF CROWFOOT STAYS The number of crowfoot stays needed in any case is determined by spacing requirements as well as by the size of the area to be supported. In general the spacing should conform to the following requirements: ( 1 ) The maximum spacing between the centers of rivets attaching the crowfeet of braces to the stayed surface should be determined by the value of p in the formula: j 135T 2 p = V-p~ ( 2 ) The distance between the edges of tube holes and the centers of rivets attaching the crowfeet of braces to the stayed surface should not exceed the value of p in the above formula. (3) The maximum spacing between the inner surface of the shell and lines parallel to the surface of the shell passing through the centers of rivets attaching the crowfeet of braces to the head should be deter¬ mined by the value of p in the formula: / 175^2 p=v— In the above formulae, P = maximum allowable working pressure, lbs. per sq. in. T = the number of sixteenths of an inch in the thick¬ ness of the stayed surface. (T = 8 for yl" plate, 9 for plate, etc.) 24 The H artf or d Steam Boiler Inspection and Insurance Co . STRESSES IN DIAGONAL CROWFOOT STAYS AND AREAS SUPPORTED THEREBY Because of the angularity of diagonal crowfoot stays with reference to the direction in which the load acts, greater cross-sectional areas are required than would be the case with direct stays. If a is the required area of a direct stay for any given conditions and A is the corresponding area for a diagonal stay, then A: a = L: l or A = —-—- L and l being measured as indicated in the sketch above. In horizontal tubular boilers L is usually not more than 1.15 times l and in such cases diagonal stays may be calculated as direct stays, allowing ninety per cent (90%) of the stress which would be permitted for such stays. For weldless mild steel direct stays not more than 120 diameters in length a stress of 9500 pounds per square inch is permissible so that the allowable stress for such diag¬ onal stays would be 8550 pounds per square inch; this is usually taken as 8500 pounds for easy figuring. In any unusual case the relation of L to / should be checked and the required area should be figured from the formula given if L is greater than 1.15 times /. The following table has been calculated to show the maximum areas supported by the usual sizes of diagonal stays under various pressures. It is based on a stress of 8500 pounds per square inch which is equiva¬ lent to 8449 pounds for 1 y& inch stays, 9414 pounds for l^fg inch stays and 10431 pounds for 1 Ti inch stays. Maximum Areas in Square Inches Supported by Weldless Mild Steel Diagonal Crowfoot Stays Pressure Lbs. per sq. in. Diameter of Stay Pressure Lbs. per sq. in. Diameter of Stay 1X" 1*4" IX" IX" 1 %" IX" 100 84 94 104 180 46 52 58 105 80 89 99 185 45 50 56 110 76 85 94 190 44 49 54 115 73 81 90 195 43 48 53 120 70 78 87 200 42 47 52 125 67 75 83 210 40 44 49 130 65 72 80 220 38 42 47 135 62 69 77 230 36 40 45 140 60 67 74 240 35 39 43 145 58 64 72 250 33 37 41 150 56 62 69 260 32 36 40 155 54 60 67 270 31 34 38 160 52 58 65 280 30 33 37 165 51 57 63 290 29 32 36 170 49 55 61 300 28 31 34 175 48 53 59 310 27 30 33 The H a rtf or d Ste am Boiler Inspection and Insurance Co. 25 PROPORTIONS OF THROUGH STAYS Through stays should be upset on the threaded end so that the net cross- sectional area at the root of the thread will be at least equal to the cross-sectional area of the body of the stay. The diameter of the outside washer should be at least 2yl times the diameter of the stay; in certain cases a greater diameter will be necessary to meet spacing requirements. The eye on the opposite end of the stay should be made by upsetting and drilling a hole for the pin rather than by welding. To develop the full strength of a stay, the cross-sectional area of the pin should be at least three-fourths (3^) of the area through the body of the stay and the cross-sectional area through the center of the eye should be at least twenty-five per cent (25%) greater than the area through the body of the brace. The pin should be turned to make a neat fit in the hole. The combined cross- sectional area of the rivets attaching each stay to the head should be at least twenty-five per cent (25%) greater than the area through the body of the stay. The following table shows the proportions of weldless steel through stays neces¬ sary to meet the above requirements. D Diameter of stay Cross-sectional area of body. (sq. in.) U Diameter of Upset* Minimum diameter of Washer Diameter of Pin Minimum cross-sectional area at A-A (sq. in.) Minimum combined area of rivets (sq. in.) 1" 0.7854 IK" 2K" K" 0.9S2 0.982 1 X" 0.9940 IK" 2K" 1" 1.243 1.243 IK" 1.2272 IK" 3K" IK" 1.534 1.534 l K" 1.4849 IK" 3K" IK" 1.856 1.856 IK" 1.7672 IK" 3K" IK" 2.209 2.209 IK" 2.0739 2 " 4K" IK" 2.592 2.592 IK" 2.4053 2K" 4K" IK" 3.007 3.007 IK" 2.7612 2K" . 4K" l— 4 \Ol oo\ 3.452 3.452 2 " 3.1416 2K" 5" IK" 3.927 3.927 2K" 3.5466 2K" 5 K" IK" 4.433 4.433 2K" 3.9761 2K" 5K" v- 2" 4.970 4.970 2K" 4.4301 23K" 6" 2K" 5.538 5.538 2K" 4.9087 3" 6K" 2K" 6.136 6.136 *Based on Sellers Standard Threads. 26 The H a rtf or d Steam Boiler Inspection and Insurance Co. STRESSES IN THROUGH STAYS AND AREAS SUPPORTED THEREBY For unwelded steel through-stays the allowable stresses should be figured in accordance with the following: Lengths not exceeding 120 diameters Lengths exceeding 120 diameters Diameters not exceeding IX" 9500 lbs. per sq. in. 8500 lbs. per sq. in. Diameters exceeding 1 X" 10400 lbs. per sq. in. 9000 lbs. per sq. in. On the above basis the following table has been prepared to show the maxi¬ mum areas in square inches which can be supported by through stays of different diameters and lengths under varying pressures, it being assumed that the stays will be proportioned in accordance with the requirements stated on Page 25. Maximum Areas in Square Inches Supported by Weldless Steel Through Stays Pres¬ sure (Lbs. per sq. IX" Diam. IX" Diam. IX" Diam. IX" Diam. IX" Diam. ir-3" Over 12'-6" Over 13'-9" Over 15'-0" Over 16'-3" Over in.) or less ll'-3" or less 12'-6" or less 13'-9" or less 15'-0" or less 16'-3" 100 94 84 116 104 141 126 167 150 215 186 105 89 SO 111 99 134 120 159 143 205 177 110 85 76 105 94 128 114 152 136 196 169 115 82 73 101 90 122 109 145 130 187 162 120 78 70 97 86 117 105 139 125 179 155 125 75 67 93 83 112 100 134 120 172 149 130 72 64 89 80 108 97 129 115 165 143 135 69 62 86 77 104 93 124 111 159 138 140 67 60 83 74 100 90 119 107 154 133 145 65 58 80 71 97 87 115 103 148 128 150 62 56 77 69 94 84 111 100 143 124 155 60 54 75 67 91 81 108 96 139 120 160 59 52 72 65 88 78 104 93 134 116 165 57 51 70 63 85 76 101 91 130 113 170 55 49 68 61 82 74 98 88 126 109 175 53 48 66 59 80 72 95 85 123 106 180 52 46 64 57 78 70 93 83 119 103 185 51 45 63 56 76 68 90 81 116 100 190 49 44 61 54 74 66 88 79 113 98 195 48 43 59 53 72 64 86 77 110 95 200 47 42 58 52 70 63 83 75 107 93 210 44 40 55 49 67 60 79 71 102 88 220 42 38 53 47 64 57 76 68 98 84 230 41 36 50 45 61 54 72 65 93 81 240 39 35 48 43 58 52 69 62 89 77 250 37 33 46 41 56 50 67 60 86 74 260 36 32 44 40 54 48 64 57 82 71 270 34 31 43 38 52 46 62 55 79 69 280 33 30 41 37 50 45 59 53 77 66 290 32 29 40 35 48 43 57 51 74 64 300 31 28 38 34 47 42 55 50 71 62 27 The Hartford Steam Boiler Inspection and Insurance Co Maximum Areas in Square Inches Supported by Weldless Steel Through Stays (Concluded) Pressure (Lbs. per sq. in.) 124" Diam. V/&" Diam. 2" Diam. 2 yi" Diam. 2 24" Diam. 17'-6" Over 18'-9" Over 20'-0" Over 21'-3" Over 22'-6" Over or less 17'-6" or less 18'-9" or less 20'-0" or less 21'-3" or less 22'-6" 100 250 216 287 248 326 282 368 319 413 357 105 238 206 273 236 311 269 350 303 393 340 110 227 196 261 225 297 257 335 290 376 325 115 217 188 249 216 284 245 320 277 359 311 120 208 180 239 207 272 235 307 265 344 298 125 200 173 229 198 261 226 294 255 330 286 130 192 166 220 191 251 217 283 245 318 275 135 185 160 212 184 242 209 273 236 306 264 140 178 154 205 177 233 201 263 227 295 255 145 172 149 198 171 225 194 254 220 285 246 150 166 144 191 165 217 188 245 212 275 238 155 161 139 185 160 210 182 237 205 266 230 160 156 135 179 155 204 176 230 199 258 223 165 151 131 174 150 198 171 223 193 250 216 170 147 127 16S 146 192 166 216 187 243 210 175 142 123 164 142 186 161 210 182 236 204 180 138 120 159 138 181 157 204 177 229 198 185 135 116 155 134 176 152 199 172 223 193 190 131 113 151 130 171 148 194 167 217 188 195 128 110 147 127 167 144 189 163 212 183 200 125 108 143 124 163 141 184 159 206 178 210 119 103 136 118 155 134 175 151 196 170 220 113 98 130 112 148 128 167 145 187 162 230 108 94 124 108 142 122 160 138 179 155 240 104 90 119 103 136 117 153 132 172 149 250 100 86 114 99 130 113 147 127 1 165 143 260 96 83 110 95 125 108 141 122 159 137 270 92 80 106 92 121 104 136 118 153 132 280 89 77 102 88 116 100 131 113 147 127 290 86 74 99 85 112 97 127 110 142 123 300 83 72 95 82 108 94 122 106 137 119 28 The Hartford Steam Boiler Inspection and Insurance Co. MAXIMUM PITCH IN INCHES FOR SCREWED STAYBOLTS WITH ENDS RIVETED OVER (For Flat Surfaces) Thickness of Plate (Inches) Pressure Lbs. per sq.inch Pi We XX A Pi u /6 Vi X V4 Pi 'Vi Vi '% pi 2 V4 X V4 23 4 25 8 We 30 7 Pi 35 7 pi 8 V4 40 6' We 7 pi 8 We 45 6 We 7 Vi 7 Pi 50 6 6 y 7 Pi 8 Pi 55 5'We 6 14 7 Pi 7!P4 60 5 We 6 ^ 6 13 /4 7 Pi 8 Vi 65 5 pi 5 y 6 Vi 7 P4 7 pi 70 5 14 5'We 6 We 6'Pi 7 Pi 8 3 /4 75 4 5 pi 6 We 6 1 /4 7 5 /4 7'We 80 4 y 5 We 5 pi 6 Pi 7 Pi 7'We 8 Pi 85 4 pi 5 Pi 5 y 6 '14 6 Pi 7 We 8 90 4 We 5 5 ®4 6 Pi 6 n /4 7 Pi 7'We 95 4 We 4 pi 5 We 6 6 Pi 7 Vi 7 pi 8 We 100 4 X 4 pi 5 We 5 13 4 6 pi 6 pi 7 Vi 8 *4 105 4 pi 4 pi 5 We 5!14 6 3 /4 5'We 7 Pi 8 110 4 4 % 5 We 5 We 6 We « Vi 7 V4 7'We 8 Pi 115 3 15 /4 4 We 4'We 5 We 5'We 6 Vi 6 pi 7 Pi 8 We 120 3 pi 4 Pi 4'We 5 We 5'We 6 Pi 6 Pi 7 K 8 8 Pi 125 3 Pi 4 X 4 Pi 5 We 5'We 6 Pi 6 pi 7 Pi 7 'We 8 We 130 3'V4 4 We 4 pi 5 Pi 5 We 6 6 Pi 7 3 /4 7'We 8 We 135 3 pi 4 Pi 4 Pf 6 5 5 Pi 5'We 6 pi 7 We 7 We 8 8 Pi 140 3 We 4 4 pi 4'We 5 Pi 5'We 6 We 5'We 7 Pi 7 pi 8 We 145 3 pi 3 l5 y fi 4 Pi 4 13 ^6 5 y 5'We 6 Pi 5'We 7 Pi 7 Pi 8 We 150 3 Pi 4 P4 4 P< 5 We 5 Pi 6 Vi 6 u /4 7 li 7 Pi 8 Vi 8 Pi 160 3 Pi 4 P4 4 Pi 5 5 We 5 Pi 6 Pi 5'We 7 Pi 7»Vi 8 Pi 170 3 Pi 4 14 4 14 4 Pi 5 Pi ^Vi 6 We 6 Pi 7 Pi 7 We 8 8 Pi 175 3 Pi 4 4 pi 4 13 /4 5 We 5 pi 6 V4 6 pi 7 Vfe 7 We 7 pi 8 5 i 180 3 We S'We 4 Vi 4 Pi 5 Pi 5 Pi 6 Pi 6 Pi 5'We 7 Pi 7 Pi 8 We 190 3 13 /ffi 4 We 4 pi 5 5 pi 3'We 6 Pi 6 Pi 7 Pi 7 9 4 7'We 8 We 200 3 Pi 4 Pi 4 pi 4 Pi 5 Pi 5'We 6 We 6 9 /4 6'Vi 7 Pi 7 Pi 8 Pi 210 3 Pi 4 4 Pi 4 Pi 5 Pi 5'We 6 We 6 We 6'Vi 7 Pi 7 We 7 15 /4 8 5 /4 220 3 P4 3 15 /4 4 Vi 4 Pi 5 5 We 5 pi 6 Pi 6 pi 7 7 Pi 7 Pi 8 Pi 8 Pi 230 3 Pi 3 13 y« 4 Vi 4 9 /4 4 pi 5 We 5 Pi 6 Pi 6 Pi 6 Pi 7 Vi 7 ?i 7'We 8 We 240 3 Pi 4 Pi 4 Vi 4 Pi 5 We 5 Pi 6 6 pi 6'Pi 7 Vi 7 Vi 7 y 8 Pi 250 3 u /4 4 4 Pi 4'V4 5 We 5 Vi 5 pi 6 Pi 6 9 /i 6'Vi 7 Pi 7 Pi 7'Vi The above table for pitch of staybolts on flat surfaces is based on the formula: ,-v? where p = maximum pitch between centers of staybolts, inches. P = maximum allowable working pressure, lbs. per sq. in. T = the number of sixteenths of an inch in the plate thickness. C = 112 for plates not over thick. C = 120 for plates more than 1 /(§ thick. For cylindrical furnaces which require staying, the pitch may be increased somewhat over that allowed for flat surfaces, the formula for such cases being P = C T 2 R P R —250 T where R = the internal radius of the furnace in inches and the other letters have the same significance as above. The Hartford Steam Boiler Inspection and Insurance Co. 29 ALLOWABLE LOADS ON SOLID STAYBOLTS WITH 12 V-THREADS PER INCH OF LENGTH The following table is based on a stress of 7500 pounds per square inch of net cross-sectional area and is intended for use with staybolts less than twenty (20) diameters long, screwed through plates, with ends riveted over. For use in boilers having a grate area in excess of fifteen (15) square feet, it is recommended that the outside ends of solid staybolts which have a length of eight inches (8") or less shall be drilled with a hole % inch in diameter to a depth of at least inch beyond the inside of the plate. The area of this hole must be deducted in figuring the net cross-sectional area of the staybolt and the table shows the allow¬ able loads under this condition as well as the allowable loads for solid staybolts which are not drilled. In each case the area is figured from the diameter at the bottom of the thread. Diameter of Staybolt (Inches) Diameter at Bottom of Thread (Inches) AREA AT BOTTOM OF THREAD (square INCHES) ALLOWABLE LOAD (LBS.) Not Drilled We" Hole Deducted Not Drilled Drilled (We" Hole) X 0.7500 0.6057 0.2881 0.2605 2160 1953 x We 0.8125 0.6682 0.3507 0.3231 2630 2423 H 0.8750 0.7307 0.4193 0.3917 3144 2937 l We 0.9375 0.7932 0.4941 0.4665 3705 3498 1 1.0000 0.8557 0.5751 0.5475 4313 4106 1 We 1.0625 0.9182 0.6622 0.6346 4966 4759 l H 1.1250 0.9807 0.7554 0.7278 5665 5458 1 We 1.1875 1.0432 0.8547 0.8271 6410 6203 1 K 1.2500 1.1057 0.9602 0.9326 7201 6994 1 We 1.3125 1.1682 1.0718 1.0442 8038 • 7831 l H 1.3750 1.2307 1.1897 1.1621 8922 8715 1 We 1.4375 1.2932 1.3135 1.2859 9851 9644 1 K 1.5000 1.3557 1.4435 1.4159 10826 10619 To figure the allowable pressure on a flat surface supported by staybolts the gross area supported by each stay should be determined from the full pitch dimensions and the net area can then be obtained by deducting the area occu¬ pied by the staybolt itself. The allowable working pressure in pounds per square inch is the quotient of the allowable load as given in the table divided by the net area supported. For example: With 1-inch staybolts pitched 5 inches on centers in each direction the gross area supported by each staybolt is 25 square inches and the net area is 25 minus 0.5751=24.4249 square inches. If each staybolt is drilled with a ^fg-inch hole the allowable load as given in the table is 4106 pounds and the allowable pressure will be 4106 divided by 24.4249 or 168 pounds per square inch. Of course the spacing and plate thickness must conform to the requirements as given on the opposite page for the stated pressure. 30 i The H artf or d Ste am Boiler Inspection and Insurance Co TABLES SHOWING THE LEAST ANGLE WHICH A STAYBOLT MAY MAKE WITH A PLATE TO SECURE A GIVEN NUMBER OF FULL THREADS (Based on V-threads, 12 to the inch) Table 1. 4 Full Threads DIAMETER OF STAYBOLT of Plate X" X" X" X" 1 " IX" IX" IX' X" 5,4" H" 90° * W 90° 89° 88.5° 89.5° 89° 0 00 90° 90° X" 83° 84° 83° 84° 84° 85° 85° 87° 9 4" 76° 78° 78° 81° 84° 83° 83° 85° X" 54° 68 ° 71° 75° 770 79° 80° 82° X" 48° 56° 64° 68 ° 71° 73° 770 X" O cc IC oq o oo cd •^cqooc to CO r-H C3 l> to CO rH GO tO TfMM O co oo o co tO tO CD 03 tO r-H CD CD N- GO GO 0 s ! 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ALLOWABLE WORKING PRESSURES ON SPHERICAL HEADS Plus Heads (Concave to Pressure) With Manhole The H a r tf o r d Steam Boiler Inspection and Insurance Co 33 108 1> ic 00 rH C3 t> lO N OOO CO Tf (NOOO ID CD H 05 NiOXHCO LO rH f'* rH rH oooo rf o Ot iM CO Tf CD CM X Tf LO LO CD 05 LO rH CD CD l> 00 00 CM X Tf 05 05 0500 rH rH LOnf-XX rH CM CM X X rH rH rH rH rH 102 rH CM X uosot-oo ©rH CM Tf ID CD t> 05 O H N Tf LO CD X 05 O CD (M 00 rH rH Tf o CD (M CM X X Tf 05 LO rH 1> Tf LO CD CD CO 05 ID tH t- t-' CD C5 X Tf o CD 05 O rH H rH rH rH CMXTfON CM CM X Tf Tf rH rH rH rH rH 96 lOOO 0>00i0 o LO rH CD rH CD rH CD rH CD rH CD CM t> CM t> CM co co 05 rH rH tOlMOUO (N CO 00 Tf CM 00 LO rH LO lo CD t> 00 Tf rH |> b- GO 05 05 Tf O tH CO O rH rH CM rH rH rH rH O CD X 05 CO X X Tf Tf LO rH rH rH rH rH 05 go oo t> CD CD LO LO Tf CO CO CM CM rH H O O 05 COCONNO 06 CD CO O rH CM t-Tf rHOO OtOOTf Tf LO CM C5 CD LO CD CD coor^Tf 00 05 05 o rH rH X LO rH rH tH CM CO rH rH rH rH X LO CM 05 CD X Tf lo lo CD rH rH rH rH rH 00 00 1>N CD O >D 05 Tf 00 CM t> rH CD O Tf C5 f0 00 N co H LD ^f 00 t-Tf CM HIM DNrf CM X Tf lO 05 CD Tf rH LO CD 1> 00 05 CD Tf rH 00 05 O rH rH rH 05 CD CO rH rH CM CO Tf rH rH rH rH X CD X rH CO Tf LO CD rH rH rH rH rH ooo oooo rH rH rH rH rH rH rH rH CM CM CM CM CM CM CM CM X 78 X CD Tf rH CM CM OX CD CO Tf rf iO Tf CM 000 CD t> 00 00 CD Tf CM O 05 O rH CM rH rH rH X CD Tf CM CM CO rf iO rH rH rH rH OOOtOTf N SO CD GO 05 tH t-I i—l rH i-H 50 000 N^ON Tf rH 00 Tf rH 00 LO CM GO ID N 05 CD CM 05 CD X 72 00 t> CD rH CM Tf CO CM O CO Tf lO CD 05 00 CD JO CD X 05 Tf CM rH O O rH CM CO rH rH rH rH X tH CD Tf CO Tf iO CD rH rH rH rH X CM O 05 X NXODO rH rH rH rH CM Tf O ^ 00 CO 00 CM NNCOH CD rH LO O LO 05 Tf 05 cooocooon 99 05 00 00 rH CM CD CD CO Tf lo CD LO LO Tf Tf l>G0 05 O rH CO CO CM CM rH CM CO Tf rH rH rH rH rH O O 05 LO CD t> t> rH rH rH rH 05 oo oo t> 00 05 O i-H N 1-11-1 N N N Tf 00 rH LO O Tf 00 N to O X5 05 MNHiDO w co 00 Tf o CD rH CO 05 rf O CD CM N Q 54 rH X Tf H(NC0 CD l>- 05 rH Tf ID CD 00 CM Tf LO t> 05 O rH CM rH rH rH 00 O CM CO CO lO CD l> rH rH rH rH LO CD X 05 X 05 O rH rH rH CM CM HXTf CDN X Tf LO CD N CM CM CM CM CM w 0* ooo fD rH rH ?H rH rH CM CM 0 X t-h iOCNQ Tf 1> o CO O h CO Tf rH rH rH rH CD 05 CM LO LO CD (X 05 rH rH rH rH Xnrf N O CM CO Tf CM CM CM CM O X CD 05 CM CD I> X 05 H CM CM CM CM X a OOt^SO LO Tf CM rH 005 00 CD LO Tf CO CM 005 X t> CD iO X CM H < w w 42 Tf 05 Tf rH CM Tf O Tf O Tf lo x o rH 05 CO 00 CO rH CO Tf CD rH r—^ rH rH CO CO 00 00 t>05 0N Hi—i N (N X CM CM X LO O X CM CM CM CM N CM N W N 05 rH CM Tf LO CM X X X X u C0I> O Tf 00 rH lo GO N CO 05 CO CD O Tf NHiOX CM LO 05 X CD ffl & o 36 tr Tf CM rH CO lO 05 CD Tf H CD C© O CM tH tH 00 CD CO O CO LO I> 05 rH rH rH rH 00 ID CO o ON Tf CO N N N N lo CM 05 N05HN CM CM X X 1> Tf rH 05 CD Tf CD X 05 rH X X X X Tf to D s < <& 30 20.8 41.6 62.5 83.3 104.1 125.0 145.8 CD LO CO rH CD N GO C5 O CO O CM rH rH CM CM 250.0 270.8 291.6 312.5 333.3 354.1 375.0 395.8 CD LO X rH o CD X 05 O rH co LO O Tf Tf Tf Tf LO O O rH i-H N N N CO CO Tf Tf LO LO LO CD ONNN 00 00 05 05 o 24 CD CM X (NiON Tf o co CM o co io oo rH iH rH rH 00 Tf o CD O CO CD 00 CM CM CM CM CM 00 Tf O rH CO O 05 CO CO CO CO CD N 00 Tf H Tf CD 05 Tf TjH Tf Tf OCD CM X LO CM Tf 05 CM LO LO LO LO CD Tf oon CD O Tf 00 (NcOOiD 05 CO f'- rH ID 05 CO t> rH LO O Tf X 22 oototo (M lOOO CO CM O GO rH rf !>• 05 rH rH tH rH 1> LO Tf CM CM LO 00 rH CM CM CM CO 0 05NCD rf O 05 CM CO CO CO Tf Tf CM rH 05 LO X rH X Tf Tf LO LO X CD LO X rH CD 05 CM LO X lO lo CD CD CD (N>ON o cm io r> OCM LOt> O CM LO t> O CM L0 I> OCMLONO 20 H (M CO CO CD O io CD t> 00 N ID 00 rH i—11—11—1 N O rH CM CO LO 00 rH rf CM CM CO CO LO CD GO !> O CO CD CO Tf Tf Tf O rH CM X O X CD 05 LO LO LO LO LO0NXO CM LO X rH LO CD CD CD 1> t> Tf rH 00 CD CO O 1> ID IN 05 CD CO rH 00 LOCMON Tf rH x CD X 00 rH Tf 05 Tf CO CD O rH 00 CO 00 co C0l> OTf rH rH CM CM SNt'H t- 1-t Tf 00 (N CO CD 00 CD rH CD O rH LO 00 CM Tf Tf Tf LO ID O ID 05 ID 05 N >D ID iDOtO Tf 05 X X X O CM CD 05 X ONNNX O rH rH oo oo 05 o O rH rH CM X X Tf LO CO r—( 05Xt^ CO l> rH rH CD IO Tf CO LO 05 X rH rH CM CM CM rH 005 rH LO 05 CM CO CO CO Tf GO CD LO CD o rf CO Tf LO LO LO LO Tf x CM CM CD O Tf CD CD t> 1> HOOGOS 00 N IO 05 CO i> oo oo oo 05 tooio >D N GO »D iHNTf O t'-cooco CM 05 LO CM ooiOi-n>itfi rH rfDCO rf GO CO rH CO CO l> CM CM CD rH iH CM CM CO 1—1 CD T—1 LO O Tf 05 CD Tf Tf Tf LO O LO 05 CO X CM CD LO LO CD CO Tf X XX rH LO O Tf I> X X CM CM CD r—I DXXCMN X 05 05 o o rH rH OH (50 05 O O H N x Tf LO LO SO t> GO 050 CM rH CM Tf CD lO o lo rH rH OOOiMTf O CD rH CD (N Ot CO CO CD 00 O N HCONN Tf Tf ID ID LO 05 rH CM tH CM CO CD CD IH tH x lo 05 X X X X X X 05 05 HXLONO Tf 05 Tf 05 io O O rH H CM rH rH rH rH rH 1 CJ •3 ness & St Se fG\oO X UD X & fc =5 t— t o' o' r i h i S: UAH —• s cc x C* n W r ft & % io'' .-«' s N H « » rH See Explanatory notes on Page 31. 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BSIM NUMH »■■■ ■■■■■ ”2322188! aaaaa umwdm aaaaaliiian BBattsaa jsaaaaai'.aaaaai iaaaa aaaaa .. aaaaaaaaaa bin*'« aaaaa ar^aa* -bb* vf«E l,V-S a- iaaaa-' «aiiimaaaaa aa^BaBaaBBaiaaBaB**aiBfiaaat 4 *.«a aaaaa a^iaa' 1 aaaaa aaaaa mmmm- _.*aara*iiiuBoaaBB»'-. dbE aaaaaalettr^ -*«»* urn's* ■**• - awna ,«aaaaaaaaaaaaB»-'^BaaaaBaaaaaaaS^!.aaaMaaaaiai**-^aaaB^paa^aa»'.BaaaJir%5^jaB^^aai iaaaa iBaa*ia»*^ flaaaa saaaa Baav^ B«a M«ai imi» :«aai ■■■ aaa»'. aaaaa vf isaaBiaa» a> .diB*BBaBaiBin»'^«BBCfl«a>BaaflBi*'4aaH(iBa«BL-JB'4BB iBBiiiaiMB r ^irgaCi. iaaaa •r~mmmmmmm9mmmmBm~r~*nmmmwmmmmMmnw~ £ mmmnwmummBmm* 0 : «aap a ar^a aa« r ^ bj»'u rjY>< i»*'^«aaaaaBBaaaBaBB-‘i«aaBBaaaaaaaaaB*^Bg$aBaaaaBaaa'^BaaBaSaaiMBa»^^Bafv # ] iaaaaaiaBBaaaBB*%«aaHaaBaasilaia''.«2iiili8BaBaBi»'..BaaaHBi.^.Baaa' «BBBak*^4 ?«•*■ iBaBB55aSBaa«'!;«BBBBBaBaBaaaaBa E t.BBaaBBaafiaBaaB-' < .aaaBaBBaaaKw , i»'.Ba«3aiBaaBBfi*>^Bi IBBBpaa»--«aBBBBBBBBaBBBBB*':«BBaBBBaBBBBBa*-.-BBBaBBBBBaiBaB' aBBUaB^OBaa'dilllt ibb**^«« a3aaaaaa Baaap aa*--aaiiiiBBiaitaa*%aa§aaiai §bbhb *r .**b bbbib iaaaa r '-aBt a^ .BBaaaaaaBBBBBBBBa» s .«BafifiBBHBBBBfS» 9 ^«(8iBBaBaaBBaaBP'’ tf aaaBB«BBp»i3i*: d aa«aaB^«] iaaaa aaaaa aaaai aaaaa bbb» c ~«aifi mibb iaaaaa»”-a iaaaa aaaaB aa«*- - iaaaa aiw-C* a»-. 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O 0 bEicvJ ■5 2 °2 a 0 <0 0 .. c D W Z E ft> a: n - -x o E o o O n ■°i 0<3 351 0 o-5tr tf) 0 o> 0)x- c c ft) w a 13 10 a d) i. c) 0 « o (D a i A O <0 c -D .b r ft) - "5 X ’5 T 3 t o 11 11 0 . Q o 0 c c — ft) r ft) 3 ^ 0 "ft) b: D 0 S <01 o 2 CM 0 ” in »n w O i- O CL c 3 O 0 CO 0- o CO i o 38 The Hartford Steam Boiler Inspection and Insurance Co. / % TUBES FOR FIRE-TUBE BOILERS Standard Dimensions Outside Diameter (Inches) Standard Thickness (Inches) Birming¬ ham Wire Gage. (Number)- Inside Diam. (Inches) Inside Circum¬ ference (Inches) Outside Circum¬ ference (Inches) Length of Tube per Sq. Ft. of Inside Surface (Feet) Length of Tube per Sq. Ft. of Outside Surface (Feet) Cross Sectional Area Inside (Sq. In.) Cross Sectional Area Outside (Sq. In.) Nominal Weight per Foot. (Pounds) 1 0.072 15 0.85 2.68 3.14 4.46 3.81 0.57 0.78 0.70 IK 0.072 15 1.10 3.47 3.92 3.45 3.05 0.96 1.22 0.90 IK 0.083 14 1.33 4.19 4.71 2.86 2.54 1.39 1.76 1.24 2 0.095 13 1.80 5.66 6.28 2.11 1.90 2.55 3.14 1.91 2K 0.109 12 2.28 7.17 7.85 1.67 1.52 4.09 4.90 2.75 3 0.109 12 2.78 8.74 9.42 1.37 1.27 6.08 7.06 3.33 3K 0.120 11 3.26 10.24 10.99 1.17 1.09 8.35 9.62 4.28 4 0.134 10 3.74 11.75 12.56 1.02 0.95 10.99 12.56 5.47 4 K 0.134 10 4.24 13.32 14.13 0.90 0.84 14.12 15.90 6.17 5 0.148 9 4.72 14.81 15.70 0.80 0.76 17.49 19.63 7.58 6 0.165 8 5.69 17.90 18.84 0.67 0.63 25.50 28.27 10.16 Tubes of the standard thicknesses given in the above table are suitable for pressures up to 175 pounds per square inch. For higher pressures the thickness of tubes should be increased in accordance with the following: For each increase of one gage in thickness above the standard gage shown in the table, the allow¬ able working pressure in pounds per square inch may be increased by an amount equal to the quotient of 200 divided by the diameter of the tube in inches. The H a rtf or d Steam Boiler I nspection and Insurance Co. 39 TUBES FOR WATER TUBE BOILERS AND SUPERHEATERS In water tube boilers and superheaters the maximum allowable working pressures for tubes should be determined from the formula: P = 18000-250 where P = maximum allowable working pressure in pounds per sq.'in. t = thickness of tube wall in inches. D = outside diameter of tube in inches. The following table, based on the above formula, shows the maximum allowable working pressures for tubes of various diameters and thicknesses. Gage Number on Birmingham Wire Gage Outside diameter of tube, in inches D 17 16 15 14 13 12 11 10 9 8 7 6 5 t = 0.058 t = 0.065 t = 0.072 t = 0.083 t = 0.095 t = 0.109 t = 0.120 t = 0.134 t = 0.148 t = 0.165 t = 0.180 t = 0.203 t = 0.220 K 434 686 938 1334 X 206 374 542 806 i094 .... .... .... .... .... .... l 218 344 542 758 1010 IK 166 278 454 646 870 1046 .... .... .... • • • • .... IK 124 225 383 557 758 916 1118 .... • • • • .... IK 146 278 422 590 722 890 i058 .... .... .... IK 203 326 470 583 727 871 1046 .... .... .... 2 146 254 380 479 605 731 884 1019 2K 198 310 398 510 622 758 878 i062 2X 153 254 333 434 535 657 765 931 1053 2K 117 208 280 372 464 575 673 824 935 3 170 236 320 404 506 596 734 836 3K 199 276 354 448 531 658 752 3K 167 238 310 398 475 594 681 3K .... .... 139 206 273 355 427 537 619 4 178 240 317 385 488 565 4K .... .... .... .... 186 254 314 406 474 5 1 .... .... .... 142 204 ■ 258 340 402 40 The H artf or d Steam Boiler Inspection and Insurance Co. HORIZONTAL TUBULAR BOILER SETTINGS Our setting plans for horizontal tubular boilers have recently been revised and the new drawings show certain features in greater detail than was formerly the case. For each of the common sizes of boilers we have four separate draw¬ ings, this number being necessary in order to clearly illustrate the difference between boilers with flush fronts and overhanging fronts and between boilers supported on the side walls and boilers suspended from overhead. Upon appli¬ cation to our Engineering Department blue-prints of any of these drawings will be furnished for use in setting boilers which we insure. In asking for such blue¬ prints it is necessary to state the diameter of the boiler, the length of tubes, the style of front (flush or overhanging) and the method of support. Our setting plans illustrate four different types of wall construction, as shown below: The design shown by Type I is probably used more extensively than any of the others. While it costs but little more than Type II, it has a distinct ad¬ vantage over that type as regards the prevention of air leakage into the furnace because the cracks will occur principally in the inner wall, leaving the outer wall intact. With a solid wall like that of Type II the cracks will extend clear through the brickwork, thus increasing the probability of air leaks with a resulting excess of air and a lower furnace efficiency. The air space has no virtue as a heat insulator; a double wall of this type will transmit just as much heat under given conditions as a solid wall of the same total thickness. Type III makes use of insulating bricks to reduce the amount of heat that is transmitted through the wall and thereby lost. These insulating bricks are made of different materials by different manufacturers and they are cut to the proper size so that they will lay up evenly with ordinary bricks. They have little mechanical strength in themselves so that it is best to use metal ties, as shown in the cut, for bonding the inner fire-brick section to the common brick on the outside. It is also advisable to use a uniform thickness of nine inches for the fire-brick lining in place of the 4^-inch lining with header courses as shown 41 The Hartford Steam Boiler Inspection and Insurance Co. for the other types. This type of construction makes a very good setting, costing somewhat more than either Type I or Type II. Type IV may be considered as similar to Type I with a steel casing substi¬ tuted for the outer wall and the air space filled with magnesia or other good insulating material. This makes a most excellent form of setting, the only drawback to its more general use being its greater cost as compared with other types. The insulating material reduces the heat radiation loss to a minimum and the steel casing prevents the even greater loss due to air leakage through the setting walls. Furthermore, a setting of this kind presents a very neat ap¬ pearance and requires less space than any of the other types illustrated. The sections shown are intended to apply to the side walls at the rear of the bridge wall. For the furnace section in front of the bridge wall, we advise that the walls be battered from the grate level to the closing-in line near the middle of the boiler shell. Our drawings show a batter of six inches in this height, thus making the walls that much thicker at the bottom. The illustration below is a typical longitudinal section through the center of a setting. On the four following pages will be found data on overall dimen¬ sions of settings, approximate numbers of bricks required for the various sizes and types, sizes of grates and the heights for setting boilers with different kinds of coal. These tables have been made up from our standard setting plans and it should be understood that they are inter-dependent. They are intended for use with hand-fired horizontal tubular boilers where the combustion rate does not exceed twenty-five (25) pounds of coal per square foot of grate surface per hour and the output is not more than twenty-five per cent (25%) above the nominal rating. -TWOVALVE5 of THE OUT6IDE-5CREW-ANO-VOKE TYPE 5HOULO BE USED IF BOILER IS CONNECTED TO A COnnON 5TEAM MAIN WITH ONE OR MORE QTHER BOILER*.Valve NEAREST BOILER SHOULD BE PRE FE RABLY OF TmE NON-RETURN TYPE. Escape Pipe shoulo BE OR AIMED BY A DRIP E LL OR OTHER SUITABLE MEANS WITH OPENING AT LEAST »"1N DIAMETER.^ ✓ StopValve SHOULD BE PLACED AS NEAR THE BOILER AS PRACTICABLE . H tN Sipe Vv* Set REAR EMOOiFSpiLER I INCH LOWER th^n front END. Union 2'oh 2j“ Biiow Off Pipe. Extra]he|avy Pipe and Fittings. Cover this trench with STEEL PLATE OR LOOSC BRIC K .N Steam Pipe should drain away from valve- Downward Pitch _ Drain required if two valves are USED. DRAIN PIPE Should have open END VISIBLE WHILE OPERATING MAIN VALVES- -—--’"** -IF ESCAPE PIPE IS USED IT SHOULD HAVE A DIAMETER AT LEAST EQUAL TO THAT OF THE SAFETY VALVE TO WHICH IT IS ATTACHED AND IF |T IS OVER SIX FEE T LONG IT SHOULO BE SUPPORTS O INOE PENOENTLY OF THE SAFETY VALVE WITH SUCH ARRANGE¬ MENT THAT NO STRAIN WILL COME ON THE VALVE BOOY. i — Damper with provision for (HAND OPERATION FROM FLOOR. ^Connection - , ■ : ■ FOR DRAFT GAGE. Center of fusible plug 2"above line of upper surface OF TUBES-—' " BlowOffPipe ShOULO HAVE TWO VALVES, OR VALVE ANO COCK IF PRES¬ SURE EXCEEDS 123 LBS.flOO LBS. I N Massachusetts). Clearance oft l ALL AROUND PIPE 1 INSIDE OF SLEEVE. L Space filled in with ASBESTOS / TO PREVENT AIR/" LEAKAGE. - / T —Sampling tube FOR FLUE-GAS ANALYSIS. .--Gate Valve OROINARILY LEFT WIDE OPEN . — Check Valve. y Globe Valve VlTH BOILER PRESSURE ON TOP OF DISK. s Asbestos Rope. Floor Level. Typical Longitudinal Section Through Center of Horizontal Tubular Boiler Setting. 42 The H a rtf or d Steam Boiler Inspection and Insurance Co Z o z % o X GO V) < & X fa fa HH o 03 fa < cc faZ fafa Oh O Z HH H H 03 fa H Z O co SI fa o X X o fa Q fa c Q Z < fa co co O z HH fa fa fa CO fa O co Z O HH CO Z fa 2 HH Q CO 'M a o H fa * 01 ) a *0D a C3 40 *H 0 ) k O s s s & Si ’ s & Si Si Sr Sr s s s s s s s s Si X X X X X X XXX XXX X X X X X X X X XXX XXX X X | 1 1 1 | | 1 1 1 1 1 1 ' 1 1 1 1 l 1 1 1 1 ! 1 1 1 1 1 1 > k Tt* F^ Ft Ft o o F- XXX 03 03 > Tf Tf 10 10 bb v v s XXX 05 05 t-H rH rH t-H rH t-H tH rH rH t-H rH t-H H H HH fa t-H rH rH H rH r— t— 1 -H H t-H tH rH t-H fa a. >- H rfa H-> fcO S & co co & & CO CO cb So s s s CO CO CO OOO & S OO CH >< H si ■u M 03 03 | | Si s 03 03 I | -11" -11" s s s ooo 1 1 1 OI M CM 1 i 1 s s 03 03 ) ) fa a; 1 1 l> 03 1 1 V. 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APPROXIMATE NUMBERS OF BRICKS REQUIRED FOR SETTING HORIZONTAL TUBULAR BOILERS IN ACCORDANCE WITH STANDARD SETTING PLANS Overhanging Fronts The Hartford Steam Boiler Inspection and Insurance Co 43 Type IV. Fire Brick 4,900 5,300 5,500 5,900 6,300 6,700 6.900 7,400 7.900 7,600 8,200 8,700 9,200 9,800 Com. Brick 16,000 17,400 18,500 19,900 20,100 21,600 22,200 23,800 25,500 24,400 26,200 28,000 28,600 30,300 CO Pi W 4 HH O PC Type III. Fire Brick 5,700 6,250 6,850 7,400 7,750 8,300 8,650 9,300 9,950 9,500 10,200 10,850 11,500 12,150 Com. Brick 17,000 18,400 19,600 21,100 21,200 22,800 23,100 24,800 26,400 25,400 27,300 29,100 29,900 31,700 O £ H t-H I-H a Fire Brick 4,900 5,300 5,500 5,900 6,300 6,700 6.900 7,400 7.900 7,600 8,200 8,700 9,200 9,800 cl >< H Com Brick 22,100 24,000 25.800 27.800 27,800 29,900 30,600 32,800 35,000 33,700 36,100 38,500 39,300 41,800 HH W Fire Brick 4,900 5,300 5,500 5,900 6,300 6,700 6.900 7,400 7.900 7,600 8,200 8,700 9,200 9,800 cu > H Com. Brick 23.100 25.100 27,000 29,000 29,000 31,200 31,700 34,000 36,200 35,000 37,500 40,000 40,800 43,300 > t—I Fire Brick 2,450 2,650 2,750 2,950 3,150 3,350 3,450 3,700 3,950 3,800 4,100 4,350 4,600 4,900 M CU > H Com. Brick 9,600 10,500 11,100 12,000 12,000 13,000 13.200 14.200 15,300 14,600 15,700 16,900 17,100 18,300 Til Fire Brick 3,350 3,650 3,900 4,250 4,350 4,700 4,900 5,300 5,700 5,350 5,800 6,200 6,450 6,850 4 W Com. Brick 10.500 11.500 12,100 13,100 13.100 14.100 14.100 15.100 16,200 15,600 16,700 17,900 18,300 19,500 — o PC W z o Type II. Fire Brick 2,450 2,650 2,750 2,950 3,150 3,350 3,450 3,700 3,950 3,800 4,100 4,350 4,600 4,900 Com. Brick 14,900 16,300 17,400 18,800 18,700 20,300 20,400 22,000 23,700 22,500 24,300 26,100 26,400 28,300 HH W Fire Brick 2,450 2,650 2,750 2,950 3,150 3,350 3,450 3,700 3,950 3,800 4,100 4,350 4,600 4,900 Oh >< H Com. Brick 15,800 17,300 18,300 19,900 19,700 21,300 21,300 23,000 24,600 23,600 25,400 27,200 27,600 29,500 Height From Floor to Center ^ % t^t> J J © © ?? % % 1 1 & % & OJ OJ OJ J J J ODOOOO & & te 0 05 0 J v 1 v 1 00 00 GO % % rtf ft# J J ©05 Length of Tubes rH rH O 00 rH rH ©oo rH rH booo H H booo H H (M 00 o rH CM Diam. of Boiler iO io & * O 3 3 © % % O CO co co te fc fc CM CM CM l>t^ fc i GO 00 GO % % ft# ft# 00 CO co -M s o ' HH &2 Fire Brick 5,000 5,400 5,600 5,900 0 0 00 H# 00 © © 7,000 7,500 8,000 7.800 8,300 8.800 9,500 10,100 J* H S.y 00 00 (N © 00 00 T —1 © 00 0 0 co 00 000 000 ft# ot^ 000 000 t-H © 00 ©0 Jh © Opp 00 cT rH r-H rH CM CM CM co ft# CM CM *0" go CM CM CM 03 0" CM CM CO CO CO CO CO C /3 Pi HH l-H HH M Fire Brick 6,050 6,600 6,950 7,500 7,850 8,400 8,800 9,400 10,050 9,650 10,350 11,000 11,850 12,550 w J >* H J B.y 00 00 © © 00 00 co 00 0 0 0 0 tr CO 000 000 ft# 0 000 000 0 ft# co 0 © © © © ft# O PQ Opp 05 0 rH GS| (M CO CM iM CD CM CM 0" co" 0 CM CM CO O cm" CO CO CO cb oo" co co O £ H Type II. Fire Brick 5,000 5,400 5,600 5,900 OO 0 0 Tt^oo 0 0 000 000 q©.o lUiUoo" 7.800 8,300 8.800 9,500 10,100 S u 00 0 0 00 0 00 00 00 00 0 0 OO © 000 000 ft# © © 000 000 rH © © © 0 © © © © oc 5 rti O (N(M CO 0 CM CO rH CO COCO o' GO CO CO CO 03 rH rfH COTf^ CO 03 00 00 0 ^ 00 0 0 © © OO 0 0 ■# 00 000 000 0 © 0 000 ©00 00 CO 00 0 © © © © ,-H l—i bi0 ©i© © © t>i>o 6 i>oooo © © w Ph >• H So 0 0 © © © © 00 0 0 rH rH 00 0 0 © T- 1 000 000 t> © (M 0 0 © © © © © rH © 0© © © oj ao Opp (N CM O CM CO CO CM © co co *O l> O CO CO © co ©’ •# ft# ■# 00 O .§ .a 00 00 ©t> OO 0 »o 00 0 0 0 0 0 (M ft# 000 0© 0 ©i>o ©©0 0 © © © HH ft# ©© © © i> © > HH > H s.a 00 00 rH O 00 0 0 00 00 00 0 0 CM CO 000 000 CO ft# hH © © © © 0 © t- © © © © © © CO © UPP co rH rH COrti rH rH LOO rH rH CO t> 00 rH rH rH 00 03 rH rH rH CM cm" co" CM CM j i—i o n Si .a 00 00 © OO 0*0 00 0 0 0 0 0 CM ft# 000 0 © 0 © 0 ©0© 0 © © © H -# o© © © i> © w HH CM CM CM CM CO CO CO Co" co ■# ft# £ w Oh >< H o So O O O O N 1 —1 OO OO CO l> OO 0 0 rH (> 000 000 © © i-H 000 0 © © © t> © © © 0 © © GO un © 00 rH rH 0 0" rH CM rH CM CM CM cm" co CM CM CM LO I >"03 CM CM CM ©OJ co co .§.a © 0 0 0 © r~ 00 0 © 00 © 0 0 0 0 CM ft# 000 0© 0 ©t>o OO© 0 © 0 © tH ■# © © © © 1- © HH fen CM CM CM (M co co" CO CO CO rf 10 Cd Ph H s.a OO OO N rH OO O O co 00 OO OO CO © 000 000 © © co ©0 © © © © hoco © © © © ft# OJ un I>© rH t-H OH CM CM CM CO CM CM co" *0 CM CM CM 1>" 03 " O CM CM CO OJ ft# CO CO 33 g|j 5 .Sf o § O £ % % J J & Ss J? % Is *TT & & % (M OJ (M 1 1 1 ^ & as 03 03 03 1 1 1 TT Kfefe U © © 00 00 00 000000 ©© £1 C /3 P£lh n a 03 3 H © rH rH v V. 0 00 rH rH ©So rH rH booo rH rH CM boob rH rH CM 00 © T-H OJ 4 H QJ £ u-4 r-; .£ 0-3 Q PP ft » ft# ft# © © % % 00 © © fe fc OO 0 0 * * ^ CM CM CM r> i> iil: 00 0000 fc % ft# ft# 00 00 O 52 #h OJ u o CJ ,5^ 23 42 a ^ aj o a rH JJ o O +J '£ a 22 52 O a o o \ 0 J m\ 04 C4 u O co CJ 2 D u O cn • rH co cd 42 ■ 2 D 52 aj O CO CJ buO ccj 3BBBklBBS. > 'WBBBaHBBBfflBSBBflBBBB ■ Bk'BB Bk'Bfl BUSH BBBB HSRBBi 6SWIBB BMW Si IB BBt^B BB^H BB^B BBBH BBBB HHHH BBBH iBHBBBHH&ttBBBBSHBBBBiiHBHHMMHi ISSillfclllfelll&llllllIll* EHHnHHH&BaHfcHBBHMflHHHSSBHHHHHBi! I BBBB BBBk'i BBBU BBBU BBBB BBBB BBBB i IBBBBBBBB^BBB^BBB^BBBBBBBBBBBI L» *1 CM CO in v VD CM CO ^ K) K) OJ CM d3niog do woxj.og oj_ S3ivao UlOdJ 3 DNVXSIQ < CQ O i For bituminous coals containing more than 35% volatile matter. (Illinois) For bituminous coals containing from 18% to 35% volatile. (Pittsburgh) For anthracite coal and semi-bituminous coal, containing less than 18% volatile. (Pocahontas, George’s Creek, etc.) 46 The Hartford Ste am Boiler Inspection and Insurance Co TABLE OF HEATING SURFACE AND HORSEPOWER FOR STANDARD SIZES OF HORIZONTAL TUBULAR BOILERS WITH MANHOLES BELOW TUBES Diameter of Boiler TUBES • HEATTNG SURFACE (Sq. Ft.) Horse- Power Length Diameter Number Tubes Shell Rear Head Total 54" 14' 3" 52 531 99 8 638 64 54" 16' 3" 52 607 113 8 728 73 54" 14' 3 K" 44 526 99 8 633 63 54" 16' 3K" 44 602 113 8 723 72 54" 14' 4" 36 494 99 7 601 60 54" 16' 4" 36 565 113 7 686 69 60" 16' 3" 74 864 125 9 998 100 60" 18' 3" 74 972 141 9 1122 112 60" 16' 3K" 52 711 125 10 846 85 60" 18' 3K" 52 800 141 10 951 95 60" 16' 4" 46 722 125 9 856 86 60" 18' 4" 46 812 141 9 962 96 66 " 16' 3" 94 1098 138 11 1247 125 66 " 18' 3" 94 1235 156 11 1402 140 66 " 16' 3 K" 74 1012 138 11 1161 116 66 " 18' 3 K" 74 1138 156 11 1305 131 66 " 16' 4" 56 878 138 11 1027 103 66 " 18' 4" 56 988 156 11 1155 115 72" 16' 3" 122 1425 151 13 1589 159 72" 18' 3" 122 1603 170 13 1786 179 72" 20' 3" 122 1781 188 13 1982 198 72" 16' 3 K" 98 1340 151 12 1503 150 72" 18' 3K" 98 1508 170 12 1690 169 72" 20' 3K" 98 1675 188 12 1875 188 72" 16' 4" 74 1161 151 12 1324 132 72" 18' 4" 74 1306 170 12 1488 149 72" 20' 4" 74 1451 188 12 1651 165 78" 16' 3" 146 1705 163 15 1883 188 78" 18' 3" 146 1918 184 15 2117 212 78" 20' 3" 146 2131 204 15 2350 235 78" 16' 3K" 112 1532 163 15 1710 171 78" 18' 3 K" 112 1723 184 15 1922 192 78" 20' 3K" 112 1915 204 15 2134 213 78" 16' 4" 91 1427 163 14 1604 160 78" 18' 4" 91 1606 184 14 1804 180 78" 20' 4" 91 1784 204 14 2002 200 84" 18' 3" 176 2312 198 17 2527 253 84" 20 ' 3" 176 2569 220 17 2806 281 84" 18' 3X" 138 2123 198 16 2337 234 84" 20' 3y 2 " 138 2359 220 16 2595 260 84" 18' 4" 108 1906 198 16 2120 212 84" 20' 4" 108 2118 220 16 2354 235 The above table is figured on the basis of ten (10) square feet of heating surface per boiler horsepower; the heating surface as calculated includes all of the inside tube area, one-half the area of the cylindrical portion of the shell, and two-thirds of the area of the rear head minus the combined cross-sectional area of the tubes. The Hartford Steam Boiler Inspection and Insurance Co 47 APPROXIMATE WEIGHTS OF HORIZONTAL TUBULAR BOILERS The weights of bare boilers as given in the following table are taken from data of the American Boiler Manufacturers’ Association, figures being given for boilers designed to operate at pressures of 125 pounds and 150 pounds. These weights do not include fronts, trimmings, grates or other castings. The amount of water contained in a boiler of given diameter and length will vary with the number of tubes and their diameter. The weights given in the last column are figured for average cases, with the boiler entirely filled and allowing 62.5 pounds per cubic foot of water. These weights should be added to the weights of the bare boilers in order to determine the total maximum weight of a boiler as installed, due allowance being made also for the weight of trimmings and other parts which are attached directly to the boiler and supported thereby. • Diameter of Boiler Length of Tubes Weight of Bare Boiler, Lbs. Weight of Water 125 lbs. Pressure 150 lbs. Pressure 54" 14' 9100 9700 11700 54" 16' 10100 10800 13400 60" 16' 12400 13400 16300 60" 18' 13600 14800 18400 66 " 16' 14900 16300 19100 66 " 18' 16400 17800' 21500 72" 16' 18400 20000 22500 72" 18' 20000 21700 25300 72" 20 ' 21700 23300 28100 78" 18' 25000 26400 29600 78" 20 ' 27100 28600 32900 Approximate Weights in Pounds per Square Foot of Flat Steel Plates Thickness (Inches) Weight (Lbs.) Thickness (Inches) Weight (Lbs.) l A 10.20 S A 25.50 9 4 11.48 26.78 % 12.75 28.05 14.03 29.33 H 15.30 H 30.60 I3 ^2 16.58 2 % 31.88 7 /f 6 17.85 ls /fe 33.15 19.13 2 % 34.43 K 20.40 7 A 35.70 17 /£> 21.68 2 9 32 36.98 % 22.95 15 ^6 38.25 19 & 24.23 *V6 1 39.53 40.80 The above table is based on a weight of 0.2833 pound per cubic inch for steel plate; this corresponds with a specific gravity of 7.854. 48 The H a rtf or d Steam Boiler Inspection and Insurance Co. I-BEAMS FOR SUSPENDING HORIZONTAL TUBULAR BOILERS The following table shows the sizes of I-beams which we recommend for the suspension of horizontal tubular boilers of the more common sizes. It is based on a maximum fiber stress of 12500 pounds per square inch, this conservative figure being used because of the fact that such I-beams are often required to carry loads in excess of those due to the boilers. In computing the table, the limiting spans and the locations of the points of suspension were taken from our standard setting plans. It should be understood that four I-beams are required in each case, the beams being bolted together in pairs as shown in the sketch below the table. Diameter of Boilers Length of Tubes Depth of I-Beams and Weight per Foot One Boiler Two Boilers Three Boilers 54" 16' 6"-12X lbs. 10"-30 lbs. 15"-42*lbs. 60" 16' 7"-15 12"-31K “ 18"-55 “ 60" 18' 7"-15 12"-35 18"-55 “ 66" 16' 7"-15 12"-40 18"-55 “ 66" 18' 8"-18 15"-42 lS"-60 “ 72" 16' 8"-18 15"-42 20"-65 “ 72" 18' 8"-18 15"—42 20"-65 “ 72" 20' 8"-18 18"-55 24"-80 “ 78" 16' 8"-18 18"-55 24"-80 “ 78" 18' 9"-21 18"-55 24"-80 “ 78" 20' 9"-21 18"-55 24"-80 “ 84" 18' 9"-21 18"-55 24"-80 “ 84" 20' 9"-21 20"-65 24"-90 “ The Hartford Ste am Boiler Inspection and Insurance Co . 49 COLUMNS FOR SUPPORTING HORIZONTAL TUBULAR BOILERS On this page and page 50 will be found tables to show the proper sizes of columns for suspended horizontal tubular boilers. Four types of columns are included, viz:—square cast-iron columns, round cast-iron columns, structural steel H-beams and built-up columns of the plate-and-angle type. No table is given for I-beam columns because the I-beam shape is poorly adapted for use as a column and is not recommended for this purpose. We also have designs for reinforced concrete columns and beams for the usual sizes of horizontal tubular boilers and can furnish copies of the same on application. The tables for column sizes in structural steel handbooks cannot be applied to the support of boilers, as a rule, because such tables are based on the assump¬ tion that the loads are direct and equally distributed over the cross-section of the column, or else balanced on opposite sides thereof, whereas in boiler installa¬ tions the loads are usually applied entirely at one side, thus introducing bend¬ ing stresses which must be taken into consideration. There is no simple solu¬ tion of the problem but it is a matter of much importance and allowance has therefore been made for this condition in the tables which follow. In these tables it is assumed that the columns are not built into the brickwork or braced in any other way against flexure. The maximum ratio of slenderness ( = the quotient of the unsupported length of the column divided by its radius of gyration) is taken at 120 for steel and 70 for cast iron. The maximum length as given in the tables for each case should not be exceeded. We realize that the designs are heavier than those used by some boiler¬ makers but we do not believe that lighter columns should be used except in cases where the loading is non-eccentric or where the columns are braced laterally so as to reduce the effective unsupported length. Sizes of Round Cast Iron Columns for Suspended Horizontal Tubular Boilers Diameter of Boilers (Inches) Length of Tubes (Feet) Maximum Length of Columns Diameter and Thickness of Columns One Boiler Two Boilers Three Boilers 54 16 10'-6" 7" x A" 7" x y 7" x 1" 60 16 ll'-0" 7" x A" 7" x y 7" x 1" 60 18 ll'-0" 7" x A" 7" x y 7" x 1" 66 16 12'—0" 8" x A" 8" x 1" 8" x lyy 66 18 12'-0" 8" x A" 8" x 1" 8" x 1H" 72 16 13'-0" 9" x y 9" x 1" 9" x i yy 72 IS 13'-0" 9" x H" 9" x 1" 9" x 1 y 72 20 13'-0" 9" x A" 9" x 1" 9" x lyy 78 16 13'-6" 9" x V*" 9" x 1" 9" x i yy 78 18 13'-6" 9" x H" 9" x 1" 9" x 1 H" 78 20 13'-6" 9" x A" 9" x 1" 9" x 1 X" 84 18 14'-0 // 9" x l 9" x 1 yy 9" x \yy 84 20 14'-0" 10" x l" 10" x 1" io" x i yy Sizes of Square Cast Iron Columns for Suspended Horizontal Tubular Boilers Diameter of Boilers (Inches) Length of Tubes (Feet) Maximum Length of Columns Width and Thickness of Columns One Boiler Two Boilers Three Boilers 54 16 10'-6" 6" X A" 6" X yy 6" X 1" 60 16 ll'-O" 6" X A" 6" X yy 6" X 1" 60 18 ll'-0" 6" X A" 6" X yy 6" X 1" 66 16 12'-0" 7" X A" 7" X yy 7" X 1" 66 18 12 , -0" 7" X A" • 7" X yy 7" X 1" 72 16 13'-0" 8" X A" 8" X y 8" X 1" 72 18 13'-0" 8" X A" 8" X y 8" X 1" 72 20 13'-0" 8" X A" 8" X y 8" X 1" 78 • 16 13'-6" 8" X A " 8" X y 8" X 1" 78 18 13'—6" 8" X A" 8" X yy 8" X 1" 78 20 13'-6" 8" X A" 8" X y 8" X 1" 84 18 14'-0" 8" X l" 8" X i" 8" X ly 84 20 14'-0" 8" X l" 8" X i" 8" X i y 50 The Hartford Steam Boiler Inspection and Insurance Co Sizes of H-Beams for Suspended Horizontal Tubular Boilers Diameter of Boilers Length of Tubes Maximum Length of Columns Depth of H- Beams and Weight per Foot One Boiler Two Boilers Three Boilers 54" 16' 10 '—6" 5"-18.7 lbs. 5"-18.7 lbs. 6"-23.8 lbs. 60" 16' ll'-O" 5"-18.7 “ 6"-23.8 “ 8"-34.0 “ 60" 18' ll'-O" 5"-18.7 “ 6"-23.8 “ 8"-34.0 “ 66 " 16' 12 '-0" 5"-18.7 “ 8"-34.0 “ 8"-34.0 “ 66 " 18' 12 '-0" 5"-18.7 “ 8"-34.0 “ 72" 16' 13'-0" 6"-23.8 “ S"-34.0 “ 72" 18' 13'-0" 6"-23.8 “ 8"-34.0 “ 72" 20 ' 13'-0" 6"-23.8 “ 8"-34.0 “ 78" 16' 13'-6" 6"-23.8 “ 8"-34.0 “ 78" 18' 13'—6" 6"-23.8 “ 8"-34.0 “ 78" 20 ' 13'-6" 8"-34.0 “ 84" 18' 14'-0" 8"-34.0 “ 84" 20 ' 14'-0" 8"-34.0 “ See explanatory notes on Page 49. Sizes of Plate-and-Angle Columns for Suspended Horizontal Tubular Boilers Diameter of Boilers Length of Tubes Maximum Length of Columns Sizes of Plates-and-Angles One Boiler Two Boilers Three Boilers 54" 16' 10' -6" 6" x 3" x 2" x y 6" x y 3" x 2" x y" 8" x y 3 y x 2 yx y 60" 16' ll'-O" 6" x y 3" x 2" x y" 8" x y 3" x 2 y" x %" 8" x y A ,f 3 y x 2 y x 54" 60" 18' ll'-O" 6" x y 3" x 2" x y" 8" x y 3" x2K"x %" 8" x 54" 3 y x 2y 2 " x H" 66" 16' 12'-0" 8" x X" 3" x 2 K" x %" 8" x y" 3K" X 2y" X 54" 8" x %" 4" x 3" x 54" 66" 18' 12'-0" 8" x y 3" x2M"x 8" x y 3 y x 2 W'x 54" 8" x y 4" x 3" x H" 72" 16' 13'-0" 8" x X" 3K" x 2 y" x y" 8" x %" 3K" x2K"x H" 8" x y 4" x 3" x !4" 72" 18' 13'-0" 8" x y" 3 y" x2K"x y 8" x 54" 3 y x 2 y x y 8" x y 4" x 3" x 14" 72" 20' 13'-0" 8" X X" 3 y"x 2 y"x y" 8" x 54" 4" X 3" x 54" 8" x y 4" x 3" x y 78" 16' 13'-6" 8" x y" 3y x2K"x y" 8" x y 4" x 3" x 54" s" x y 4" x 3" x y * GO 18' 13'-6" 8" x X" 3 y x 2 y x y 8" x 54" 4" x 3" x yi" 10" x y 5" x 3 y x y <1 00 20' 13'-6" 3 K" x 2 yf' x ®4" 8" x y 4" x 3" x 7 /4" 10" x y 5" x 3 y x 14" Tf« 00 18' 14'-0" 8" x y" 3%" x 2K" X 54" 8" X yi" 4" x 3" x Ffg" 10" x y 5" X 3K" X !4" 00 20' 14'-0" » 8" x y" 3 y* x 2%" x 54" 8" x y 4" x 3" x y 10" X y" 6" x 4" x y& n NOTE: The columns described in this table are intended to be constructed in accordance with the detail sketch at the left. For each size of boiler the size of the web plate is given above with the size of the angles underneath. Four angles are required in every case. Overall dimensions of the various column cross-sections may be determined by reference to the sketch. See explanatory notes on Page 49. The H artf or d Steam Boiler Inspection and Insurance Co . 51 SAFETY VALVES FOR POWER BOILERS The tables on the next four pages give data in regard to the sizes of flat-seat and 45-degree bevel-seat safety valves required for various pressures and for different sizes of boilers as determined by the nominal horsepower rating, this rating in each case being figured on the basis of ten (10) square feet of boiler heating surface per horsepower. "(See table on Page 46 for ratings of horizontal tubular boilers). The required relieving capacity of safety valves is based on six (6) pounds of steam per square foot of boiler heating surface per hour for water-tube boilers, five (5) pounds for other types when the pressure exceeds 100 pounds per square inch, and three (3) pounds for such types when the pressure varies between the limits of 15 pounds and 100 pounds per square inch, inclusive. Relieving capacities for intermediate sizes not given in the tables should be figured on the above basis. The required number and size of safety valves in any case should be deter¬ mined primarily from the relieving capacity which is dependent upon the lift of the valve as well as its diameter. As a matter of convenience, the tables show the number and diameter of valves required for various conditions based upon assumed lifts as given below: Diameter of Valve Assumed Lift 1" IK". IK" 2 " 2K" 3" 3K" 4" 4K" 0.04" 0.04" 0.05" 0.06" 0.06" 0.08" 0.09" 0 . 10 " 0 . 11 " The valve diameters given should be used with caution, the actual lift being considered in each case. When the lift differs from that assumed in the tables the relieving capacity of a valve can be calculated from one of the following formulae: W = 155(P+14.7) XD XL for flat-seat valves. W= 110(P + 14.7) XDXL for 45-degree bevel-seat valves. W = 50(P + 14.7) A for valves with seats of any angle, where W = the relieving capacity in pounds per hour. P = gage pressure in pounds per square inch. D = inside diameter of valve seat, inches. L = vertical lift of valve disk measured with 3% excess pressure, inches. A = relieving area in square inches = 3.1416XD XLXsine of seat angle. Sizes of Boiler Connections for Two or Three Safety Valves Mounted on a Single Base or Enclosed in a Single Casing Diameter of Each Valve Diameter of Opening to Boiler Two Valves Three Valves 1" IK" 2" IK" 2" 2K" IK" 2 K" 3" 2" 3" 3K" 2K" 4" 4K" 3" 4K" 6" 3K" 5" 7" 4" 6" 7" 4K" 7" 8" The H a rtf or d Steam Boiler Inspection and Insurance Co SAFETY VALVES FOR FIRE-TUBE BOILERS (Pressure Range from 15 lbs. to 100 lbs. Inclusive) Nominal Requirec NUMBER AND DIAMETER OF SAFETY VALVES REQUIRED WITH AVERAGE LIFT I1UI5C- povver Rating (Lbs. per Hr.) BEVEL SEAT FLAT SEAT 15 lbs. 25 lbs. 50 lbs. 75 lbs. 100 lbs. 15 lbs. 25 lbs. 50 lbs. 75 lbs. 100 lbs. 50 1500 1-4K' 1-4" 1-3" 1-3" 1-2" 1-4" 1-3 X" 1-3" 1-2" 1-2" 55 1650 2-3 K" 1-4" 1-3" 1-3" 1-2X" 1-4" 1-3 X" 1-3" 1-2" 1-2" 60 1800 2-3X" 1-4 K" 1-3 x' 1-3" 1-2X" 1-4" 1-3 K" 1-3" 1-2X" 1-2" 65 1950 2-3K" 1-4 K" 1-3X' 1-3" 1-3" 1-4 X" 1-4" 1-3" 1-2X" 1-2" 70 2100 2-4" 2-3K" 2-2X* 2-2" 2-2" 2-3" 2-3" 2-2" 2-2" 2-1K' 75 2250 2-4" 2-3 K" 2-3" 2-2" 2-2" 2-3X" 2-3" 2-2" 2-2" 2-1X" 80 2400 2-4" 2-3K" 2-3" 2-2 K" 2-2" 2-3 X" 2-3" 2-2K" 2-2" 2-1K" 85 2550 2-4" 2-3 K" 2-3" 2-2 X" 2-2" 2-3X" 2-3" 2-2X" 2-2" 2-1K" 90 2700 2-4^" 2-3K" 2-3" 2-2K" 2-2" 2-3K" 2-3" 2-2 X" 2-2" 2-1K" 95 2850 2-4>4" 2-4" 2-3" 2-2 X" 2-2" 2-3X" 2-3" 2-2 X" 2-2" 2-2" 100 3000 2-4 K" 2-4" 2-3" 2-3" 2-2" 2-4" 2-3 X" 2-3" 2-2" 2-2" 105 3150 2-4 K" 2-4" 2-3" 2-3" 2-2 X" 2-4" 2-3 X" 2-3" 2-2" 2-2" 110 3300 3-4" 2-4" 2-3" 2-3" 2-2 X" 2-4" 2-3K" 2-3" 2-2" 2-2" 115 3450 3-4" 2-4" 2-3 X" 2-3" 2-2X" 2-4" 2-3 X" 2-3" 2-2 X" 2-2" 120 3600 3-4" 2-4 K" 2-3X" 2-3" 2-2 K" 2-4" 2-3X" 2-3" 2-2K" 2-2" 125 3750 3-4" 2-4K" 2-3 X* 2-3" 2-2K" 2-4 X" 2-3X" 2-3" 2-2 X" 2-2" 130 3900 3-4" 2-4 K" 2-3X" 2-3" 2-3" 2-4 X" 2-4" 2-3" 2-2 X" 2-2" 135 4050 3-4K" 2-4K" 2-3 X" 2-3" 2-3" 2-4X" 2-4" 2-3" 2-2 X" 2-2" 140 4200 3-4 K" 2-4 K" 2-3 X" 2-3" 2-3" 2-4X" 2-4" 2-3" 2-3" 2-2" 145 4350 3-4 y 2 " 3-4" 2-3K" 2-3" 2-3" 2-4 X" 2-4" 2-3" 2-3" 2-2K" 150 4500 3-4K" 3-4" 2-4" 2-3" 2-3" 2-4 X" 2-4" 2-3" 2-3" 2-2K" 155 4650 3-4 K" 3-4" 2-4" 2-3" 2-3" 3-4" 2-4" 2-3" 2-3" 2-2 X" 160 4800 3-4 K" 3-4" 2-4" 2-3K" 2-3" 3-4" 2-4" 2-3 X" 2-3" 2-2K' 165 4950 4-4" 3-4" 2-4" 2-3 K" 2-3" 3-4" 2-4X" 2-3X" 2-3" 2-2K' 170 5100 4-4" 3-4" 2-4" 2-3K" 2-3" 3-4" 2-4 K" 2-3K" 2-3" 2-2X" 175 5250 4-4 K" 3-4 X" 2-4" 2-3 X" 2-3" 3-4" 2-4 X" 2-3X" 2-3" 2-2X' 180 5400 4-4K" 3-4 X" 2-4" 2-3 X" 2-3" 3-4" 2-4K" 2-3^2 " 2-3" 2-2K' 185 5550 4-4 K" 3-4K" 2-4" 2-3K" 2-3" 3-4 X" 2-4 X" 2-3K" 2-3" 2-2K" 190 5700 4-4 ys 3-4X' 2-4 X" 2-3 X* 2-3" 3-4X" 2-4 X* 2-3 X" 2-3" 2-3" 195 5850 4-4 K" 3-4 X" 2-4 X" 2-3 X* 2-3" 3-4K" 2-4 X" 2-3 X" 2-3" 2-3" 200 6000 4-4K" 3-4 X" 2-4 X" 2-3 K" 2-3" 3-4 X" 2-4 X" 2-3 X" 2-3" 2-3" 205 6150 4-4^2 " 3-4 X" 2-4 X" 2-3 X" 2-3 X* 3-4 x" 3-4" 2-3K" 2-3" 2-3" 210 6300 4-4 K" 3-4 X" 2-4 X" 2-4" 2-3 X" 3-4 X" 3-4" 2-3 X" 2-3" 2-3" 215 6450 4-4K" 3-4 X" 2-4 X" 2-4" 2-3 X" 3-4K" 3-4" 2-4" 2-3" 2-3" 220 6600 5-4 K" 4-4" 2-4 >4" 2-4" 2-3 X" 3-4 x" 3-4" 2-4" 2-3" 2-3" 225 6750 5-4 K' 4-4" 2-4 X" 2—4" 2-3K" 3-4 K" 3-4" 2-4" 2-3K" 2-3" 230 6900 5-4 K" 4-4" 2-4 X" 2-4" 2-3 X' 4-4" 3-4" 2-4" 2-3 X" 2-3" 235 7050 5-4K" 4-4K" 3-4" 2-4" 2-3X" 4-4" 3-4" 2-4" 2-3 X" 2-3" 240 7200 5-4 ys 4-4 X" 3-4" 2-4" 2-3K" 4-4" 3-4" 2-4" 2-3 X" 2-3" 245 7350 5-4K' 4-4 X' 3-4" 2-4" 2-3 X" 4-4 X" 3-4 X" 2-4" 2-3 X" 2-3" 250 7500 5-4 K" 4-4 X" 3-4" 2-4" 2-3K' 4-4 X" 3-4X" 2-4" 2-3X' 2-3" See explanatory notes on Page 51 The Hartford Steam Boiler Inspection and Insurance Co 53 SAFETY VALVES FOR FIRE TUBE BOILERS (For Pressures in Excess of 100 lbs.) Nom- Re¬ quired NUMBER AND DIAMETER OF SAFETY VALVES REQUIRED WITH AVERAGE LIFT Cilpcl- H. P. city BEVEL SEAT FLAT SEAT /T Ko XVd.1- \.L/DS. ing per hr.) 125 lbs. 150 lbs. 175 lbs. 200 lbs. 225 lbs. 250 lbs. 125 lbs. 150 lbs. 175 lbs. 200 lbs. 225 lbs. 250 lbs 50 2500 2-2" 2-1K" 2-1K" 2-1K" 2-1X" 2-1X" 2-1K" 2-lY" 2-1K" 2-1' 2-1" 2-1' 55 2750 2-2“ 2-2" 2-1 Y' 2-1Y" 2-1 Y" 2-1K" 2-1 Y" 2-1Y" 2-1K" 2-1 Y" 2-1" 2-1" 60 3000 2-2" 2-2" 2-1K" 2-1 Y" 2-1 Y" 2-1 Y" 2-1 Y" 2-1Y" 2-1 Y" 2-1 X" 2-1 Y" 2-1" 65 3250 2-2" 2-2" 2-2" 2-1Y" 2-1 Y" 2-1Y" 2-2" 2-1 Y" 2-1Y" 2-1Y" 2-lY" 2-1" 70 3500 2-2" 2-2" 2-2" 2-1K" 2-1 Y" 2-1Y" 2-2" 2-1Y" 2-1 Y" 2-1K" 2-1Y" 2-1Y 75 3750 2-2%” 2-2" 2-2" 2-2" 2-1 Y" 2-1Y" 2-2" 2-1Y" 2-1 Y" 2-1 Y" 2-1Y" 2-1Y SO 4000 2-2K" 2-2" 2-2" 2-2" 2-2" 2-1Y" 2-2" 2-2" 2-1 Y" 2-1 Y" 2-1 Y" 2-1Y 85 4250 2-2K" 2-2" 2-2" 2-2" 2-2" 2-1Y" 2-2" 2-2" 2-1 Y" 2-1K" 2-1 Y" 2-1Y 90 4500 2-2 Y" 2-2 K" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-1 Y" 2-1 Y" 2-1Y 95 4750 2-3" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-1 Y" 2-1 Y" 2-1Y 100 5000 2-3" 2-2 K" 2-2 K" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-2" 2-1 Y" 2-1 Y 105 5250 2-3“ 2-2 Y” 2-2 Y" 2-2" 2-2" 2-2" 2-2 Y" 2-2" 2-2" 2-2" 2-1 Y' 2-1 Y 110 5500 2-3" 2-3" 2-2 Y" 2-2" 2-2" 2-2" 2-2 Y" 2-2" 2-2" 2-2" 2-1K" 2-1Y 115 5750 2-3" 2-3" 2-2 Y” 2-2 Y" 2-2" 2-2" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 2-1 Y 120 6000 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 2-2" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 2-1Y 125 6250 2-3" 2-3" 2-3" 2-2 Y" 2-2" 2-2" 2-2 Y" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 130 6500 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 2-3" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 135 6750 2-3" 2-3" 2-3" 2-2 Y” 2-2 Y" 2-2" 2-3" 2-2 Y" 2-2" 2-2" 2-2" 2-2" 140 7000 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2 Y" 2-3" 2-2 Y" 2-2Y" 2-2" 2-2" 2-2" 145 7250 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-3" 2-2 Y" 2-2 Y" 2-2" •2-2" 2-2" 150 7500 2-3 K" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-3" 2-2 Y" 2-2 Y" 2-2" 2-2" 2-2" 155 7750 2-3 K" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-3" 2-3" 2-2 Y" 2-2" 2-2" 2-2" 160 8000 2-3 K" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2' 2-2" 165 8250 2-3 X" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 2-2" 170 8500 2-3 K" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 2-2" 175 8750 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" . 2-3" 2-2 Y" 2-2" 2-2" 180 9000 2-3 K" 2-3 Y" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2K" 2-2' 185 9250 2-314" 2-3 K" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 190 9500 2-3 Y“ 2-3K" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 195 9750 2-4" 2-3 K" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y" 2-2" 200 10000 2-4" 2-3 K" 2-3 Y" 2-3' 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y 205 10250 2-4" 2-3%" 2-3 Y" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y 210 10500 2-4" 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3" 2-3 Y' 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y 215 10750 2-4" 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3" 2-3 Y" 2-3" 2-3" 2-3" 2-2 Y" 2-2 Y 220 11000 2-4" 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3" 2-3 Y" 2-3" 2-3" 2-3" 2-2 Y" 2-2% 225 11250 2-4' 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3" 2-3 Y" 2-3" 2-3" 2-3" 2-3" 2-2Y 230 11500 2-4" 2-4" 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3 Y" 2-3" 2-3' 2-3" 2-3' 2-2 Y 235 11750 2-4" 2-4" 2-3 Y" 2-3 Y" 2-3" 2-3" 2-3 Y" 2-3" 2-3" 2-3" 2-3" 2-2 Y 240 12000 2-4' 2-4' 2-3 Y" 2-3 K" 2-3" 2-3" 2-3 Y" 2-3" 2-3" 2-3' 2-3' 2-2 Y 245 12250 2-4" 2-4' 2-3 Y" 2-3 Y" 2-3" 2-3' 2-3 Y" 2-3 Y" 2-3" 2-3' 2-3' 2-3" 250 12500 2-4K" 2-4" 2-3 K" 2-3 Y" 2-3" 2-3" 2-3 K" 2-3 Y" 2-3' 2-3" 2-3' 2-3" See explanatory notes on Page 51 54 The H a rtf or d Steam Boiler I nspection and Insurance Co SAFETY VALVES FOR WATER TUBE BOILERS Bevel Seat Nominal Rated Horse¬ power Required Capacity (Lbs. per Hr.) Number and Diameter of Safety Valves Require d with Average Lift 100 lbs. 125 lbs. 150 lbs. 175 lbs. 200 lbs. 225 lbs. 250 lbs. 275 lbs. 300 lbs. 100 6000 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 2-2" 2-2" 2-2" 2-2" 125 7500 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 2-2" 2-2" 150 9000 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 175 10500 2-4 X" 2-4" 2-3X" 2-3X" 2-3" 2-3" 2-3" 2-3" 2-3" 200 12000 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 2-3" 225 13500 3-4" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 250 15000 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-3 X" 2-3X" 2-3" 2-3" 275 16500 3-4 X" 3-4" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X* 2-3X" 2-3" 300 18000 3-4 X* 3-4" 3-4" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 2-3 X" 325 19500 4-4" 3-4K" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 350 21000 4-4 X" 3-4 K" 3-4" 3-4 2-4 X" 2-4" 2-4" 2-4" 2-3 X" 375 22500 4-4X" 4-4" 3-4X" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-4" 400 24000 4-4 X" 4-4" 3-4K" 3-4" 3-4" 2-4X" 2-4 X" 2-4" 2-4" 425 25500 4-4 X" 3-4 X" 3-4 X" 3-4" 2-4 X" 2-4 X" 2-4 X" 2-4" 450 27000 4-4 X" 4-4" 3-4 X" 3-4" 3-4" 2-4 X" 2-4 X" 2-4" 475 28500 4-4X" 4-4" 3-4 X" 3-4 X* 3-4" 2—IX* 2-4 X” 2-4 X" 500 30000 4-4K" 4-4 X" 3-4 X" 3-4X" 3-4" 3-4" 2-4 X" 2-4 X" 525 31500 4-4 X" 4-4" 3-4 X" 3-4" 3-4" 3-4" 2-4 X" 550 33000 4-4> 2 " 4-4" 3-4 X" 3-4 X" 3-4" 3-4" 2-4 X" 575 34500 4-4 X" 4-4 X" 3-4 X* 3-4 X" 3-4" 3-4" 3-4" 600 36000 4-4 X" 4-4" 3-4 X" 3-4 X" 3-4" 3-4" 625 37500 4-4 X" 4-4" 3-4 X" 3-4 X" 3-4" 3-4" 650 39000 4-4 X" 4-4 X" 3-4 X" 3-4 X" 3-4 X" 3-4" 675 40500 4-4 X" 4-4 X" 4-4" 3-4 X" 3-4 X" 3-4" 700 42000 4-4X" 4-4" 3-4 X" 3-4 X" 3-4 X" 725 43500 4-4 X" 4-4 X" 4-4" 3-4 X" 3-4 X" 750 45000 4-4 X" 4-4 X* 4-4" 3-4 X" 3-4 X" 775 46500 4-4 X" 4-4X" 4-4 X" 4-4" 3-4 X r/ 800 48000 4-4 X" 4-4 X" 4-4" 3-4 X" 825 49500 4-4 X" 4-4 X" 4-4" 3-4 X" 850 51000 4-4 X* 4-4 X" 4-4 X" 3-4 X" 875 52500 4-4X" 4-4X" 4-4" 900 54000 4-4X" 4-4 X* 4-4 X" 925 55500 4-4X" 4-4 X" 4-4X" 950 57000 4-4 X" 4-4 X" 4-4 X* 975 58500 4-4 X" 4-4 X" 1000 60000 4-4X" 4-4 X" See explanatory notes on Page 51 55 The H artj or d Steam Boiler Inspection and Insurance Co SAFETY VALVES FOR WATER-TUBE BOILERS (Concluded) Flat Seat Nominal Rated Horse¬ power Required Capacity (Lbs. per Hr.) Number and Diameter of Safety Valves Required with Average Lift 100 lbs. 125 lbs. 150 lbs. 175 lbs. 200 lbs. 225 lbs. 250 lbs. 275 lbs. 300 lbs. 100 6000 2-3" 2-2 X" 2-2" 2-2" 2-2" 2-2" 2-1 X" 2-1X" 2-1X" 125 7500 2-3" 2-3" 2-2 X" 2-2 X" 2-2" 2-2" 2-2" 2-2" 2-2" 150 9000 2-3 X w 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 2-2 X" 2-2" 2-2" 175 10500 2-3 H" 2-3 ^2 " 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 2-2" 2-2" 200 12000 2-4" 2-3 X" 2-3" 2-3" 2-3" 2-3" 2-2 X" 2-2 X" 2-2 X" 225 13500 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 2-3" 2-3" 2-2 X" 250 15000 2-4 x" 2-4" 2-3 X" 2-3 X" 2-3" *2-3" 2-3" 2-3" 2-3" 275 16500 2-4 X" 2-4" 2-4" 2-3 X" 2-3X" 2-3" 2-3" 2-3" 2-3" 300 18000 3-4" 2-4 X" 2-4" 2-3 X" 2-3 X" 2-3X" 2-3" 2-3" 2-3" 325 19500 3-4" 2-4 K" 2-4" 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 2-3" 350 21000 3-4" 2-4K" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 2-3" 2-3" 375 22500 3-4K" 3-4" 2-4 K" 2-4" 2-4" 2-3X" 2-3 X" 2-3 X" 2-3" 400 24000 3-4 X" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-3X" 2-3 X" 2-3X" 425 25500 3-4 X" 3-4" 3-4" 2-4 x" 2-4" 2-4" 2-3 X" 2-3 X" 2-3 X" 450 27000 4-4" 3-4 K" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-3 X" 2-3 X" 475 28500 4-4 K" 3-4 X" 3-4" 2-4X" 2-4 x" 2-4" 2-4" 2-4" 2-3X" 500 30000 4-4 X" 3-4 X" 3-4" 3-4" 2-4 K" 2-4 X" 2-4" 2-4" 2-3 X" 525 31500 4-4 K" 3-4 X" 3-4 X w 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 2-4" 550 33000 4-4 X" 4-4" 3-4 X ,; 3-4" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 575 34500 4-4 X" 4-4X" 3-4X" 3-4" 3-4" 2-4 X" 2-4 X" 2-4" 2-4" 600 36000 4-4 X" 3-4X" 3-4 X" 3-4" 2-4 X" 2-4 X" 2-4 X" 2-4" 625 37500 4-4 X" 3-4 X" 3-4 X" 3-4" 3-4" 2-4 X" 2-4 X" 2—4" 650 39000 4-4 X" 4-4" 3-4 X" 3-4" 3-4" 2-4 X" 2-4 X" 2-4 X" 675 40500 4-4 X" 4-4 X" 3-4X" 3-4 X" 3-4" 3-4" 2-4 X" 2-4 X" 700 42000 4-4 X" 4-4 K" 3-4 X" 3-4 X" 3-4" 3-4" 2-4 X" 2-4 X" 725 43500 4-4 x" 4-4" 3-4 X" 3-4" 3-4" 2-4 X" 2-4X" 750 45000 4-4 X" 4-4" 3-4 x" 3-4 X" 3-4" 3-4" 2-4X" 775 46500 4-4 X" 4-4" 3-4X" 3-4 X" 3-4" 3-4" 2-4X" 800 48000 4-4 X" 4-4 X" 3-4 X" 3-4 X" 3-4" 3-4" 3-4" 825 49500 4-4X" 4-4" 3-4 X" 3-4 X" 3-4" 3-4" 850 51000 4-4 X" 4-4" 3-4 X" 3-4 X" 3-4" 3-4" 875 52500 4-4 X" 4-4" 3-4 X* 3-4X" 3-4" 3-4" 900 54000 4-4 X" 4-4 X" 3-4 X" 3-4 X" 3-4 X* 3-4" 925 55500 4-4 X" 4-4X" 4-4" 3-4 X* 3-4 X" 3-4" 950 57000 4-4X" 4-4K" 4-4" 3-4 X" 3-4X" 3-4" 975 58500 4-4 X" 4-4" 3-4 X" 3-4 X" 3-4 X" 1000 60000 4-4 X" 4-4 X" 3-4 X" 3-4 X" 3-4X" See explanatory notes on Page 51 56 The H artf or d Steam Boiler Inspection and I nsur ance Co Drilling and Other Details for Flanges and Fittings (American Standard) Pressures Not Exceeding 125 Lbs. Pipe Size Diameter of Flanges Thickness of Flanges Number of Holes Siz e of Holes Diameter of Bolt Circle Size of Gaskets 1" 4" K" 4 K" 3" 1" x 2K" 1 K" 4K" K" 4 K" 3K" IK" x 2K' IK" 5" %" 4 K" 3K" IK" x 3K' 2" 6" K" 4 K" 4K" 2" x 4" 2K' 7" “K" 4 K" 5K" 2K"x 4K" 3* 7K" K" 4 K" 6" 3" x 5K" 3K" SK" 4 K" 7" 3K"x 6K' 4" 9" 8 K" 7K" 4" x 6K' 4K" 9K" 15 K" 8 K" 7K" 4K"x 6K' 5" 10" u i4" 8 K" 8K" 5" x 7K" 6' 11" l" 0 8 K" 9K" 6" x 8K" V 12K" l H’ 8 K* 10K" 7" x 9K" 8" 13K" l K" 8 K" UK" 8" x 10K" 9" 15" l K" 12 K" 13K" 9" x 12K" 10" 16" l %' 12 1" 14K* 10" x 13K" 12" 19" l K" 12 1' 17" 12" x 16" 14" 21" • l K" 12 IK" 18K" 14" x 17K' 125 Lbs. to 250 Lbs. Pressure Pipe Size Diameter of Flanges Thickness of Flanges Number of Holes Size of Holes Diameter of Bolt Circle . Size of Gaskets 1" 4K" “/«' 4 K" 3K" 1" x 2K" IK" 5" K" 4 K" 3K" IK" x 3K" IK" 6" 4 K" 4K" IK" x 3K" 2' 6K" K" 4 K" 5" 2" x 4K" 2K" 7K" l" 4 K" 5K" 2K" x 5" 3" . 8K" l K" 8 K" 6K" 3" x 5K" 3K" 9" 1 Ke" 8 K" 7K" 3K"x 6K" 4» 10" l K" 8 K" 7K" 4" x 7" 4K" ioK" l 8 K" 8 K" 4K" x 7K" 5" ii" l K" 8 K 9K" 5" x 8K" 6" 12K" l Ke" 12 K" 10K" 6" x 9K" 7" 14" 1 K" 12 l" 11K" 7" x 10K" 8" 15" l K" 12 l" 13" 8" x 12" 9" 16K" l K" 12 IK" 14" 9" x 12K" 10" 17K" l K" 16 IK" 15K' 10" x 14K" 12" 20K" 2' 16 IK" 17K" 12" x 16K" 14" 23" 2 K" 20 IK" 20K" 13K" x 19" Minimum Number of Pipe Threads for Connections to Boilers Size of Pipe Connection (Inches) 1 and K IK and 2 2K to 4 Inclusive 4K to 6 Inclusive 7 and 8 9 and 10 12 Number of threads per inch UK 11K 8 8 8 S 8 Minimum number of threads required in opening 4 5 7 8 10 12 13 Minimum thickness of material required to give above num¬ ber of threads (Inches) 0.348 0.435 0.875 1.000 1.250 1.500 1.625 The Hartford Steam Boiler Inspection and Insurance Co 57 Decimal Equivalents of Common Fractions Common Fraction Decimal Equivalent Common Fraction Decimal Equivalent Common Fraction Decimal Equivalent Common Fraction Decimal Equivalent We 0.0625 !4 0.03125 w 0.015625 S3 4t 0.515625 X .1250 Wi .09375 Wi .046875 "44 .546875 We .1875 Wi .15625 Wi .078125 37 4 .578125 X .2500 7 /?2 .21875 Wi .109375 3 % .609375 We 0.3125 9 ^2 0.28125 % 0.140625 4 14 0.640625 X .3750 "42 .34375 "4i .171875 .671875 We .4375 13 42 .40625 'W .203125 43 4 .703125 X .5000 'W 2 .46875 n 4i .234375 47 /64 .734375 We 0.5625 "42 0.53125 17 4i 0.265625 4 % 0.765625 X .6250 19 4 .59375 'W .296875 5 '4i .796875 1 We .6875 21 4 .65625 "4a .328125 53 4 .828125 X .7500 23 M 2 .71875 n 4i .359375 5 Wi .859375 'We 0.8125 2 % 0.78125 0.390625 57 4i 0.890625 X .8750 2 % .84375 "A* .421875 59 4i .921875 1 We .9375 29 4 .90625 2 ?4 .453125 e W .953125 1 1.0000 *W» .96875 .484375 .984375 Circumferences and Areas of Circles Diameter Circum¬ ference Area Diameter Circum¬ ference Area Diameter Circum¬ ference Area V6 0.0982 0.00077 116 3.2398 0.8352 2 W 2 6.3814 3.2405 We .1964 .00307 1 We 3.3379 .8866 2 We 6.4795 3.3410 W 2 .2945 .00690 1 3 M 2 3.4361 .9396 2 *4 6.5777 3.4430 X .3927 .01227 1 X 3.5343 .9940 2 X 6.6759 3.5466 W 2 0.4909 0.01918 1 % 3.6325 1.0500 2 W 2 6.7741 3.6516 We .5890 .02761 1 We 3.7306 1.1075 2 We 6.8722 3.7583 W 2 .6872 .03758 1 7 42 3.8288 1.1666 2 W 2 6.9704 3.8664 X .7854 .04909 1 X 3.9270 1.2272 2 X 7.0686 3.9761 W 2 0.8836 0.06213 1 % 4.0252 1.2893 2 ?4 7.1668 4.0873 We .9818 .07670 1 We 4.1233 1.3530 2 Me 7.2649 4.2000 "42 1.0799 .09281 1 "42 4.2215 1.4182 2"4t 7.3631 4.3143 H 1.1781 .11045 1 X 4.3197 1.4849 2 X 7.4613 4.4301 'W 2 1.2763 0.12962 l 13 4 4.4179 1.5532 2 'W 2 7.5595 4.5475 We 1.3744 .15033 1 We 4.5160 1.6230 2 We 7.6576 4.6664 "42 1.4726 .17258 l'W2 . 4.6142 1.6943 2'V%2 7.7558 4.7868 X 1.5708 .19635 1 X 4.7124 1.7672 2 X 7.8540 4.9087 "42 1.6690 0.22166 1 "42 4.8106 1.8415 2"42 7.9522 5.0322 We 1.7671 .24850 1 We 4.9087 1.9175 2 We 8.0503 5.1572 'W 2 1.8653 .27688 I'lii 5.0069 1.9949 2 "42 8.1485 5.2838 X 1.9635 .30680 l X 5.1051 2.0739 2 X 8.2467 5.4119 21 Ai 2.0617 0.33824 1 2 V6 5.2033 2.1545 2"4i 8.3449 5.5415 "Ae 2.1598 .37122 I'We 5.3014 2.2365 2 "Ae 8.4430 5.6727 "4i 2.2580 .40574 V-W 2 5.3996 2.3202 2 23 4 8.5412 5.8054 X 2.3562 .44179 1 x 5.497S 2.4053 2 X 8.6394 5.9396 "42 2.4544 0.47937 VW 2 5.5960 2.4920 2 "42 8.7376 6.0753 'We 2.5525 .51849 I'We 5.6941 2.5802 2'We 8.8357 6.2126 "42 2.6507 .55914 1 "42 5.7923 2.6699 2"4i 8.9339 6.3515 X> 2.7489 .60132 1 X 5.8905 2.7612 2 X 9.0321 6.4918 2 % 2.8471 0.64504 5.9887 2.8540 2 "42 9.1303 6.6337 "We 2.9452 .69029 I'We 6.0868 2.9483 2'We 9.2284 6.7771 3.0434 .73708 1*16 6.1850 3.0442 2 "42 9.3266 6.9221 1 3.1416 .78540 2 6.2832 3.1416 3 9.4248 7.0686 58 The Hartford Steam Boiler Inspection and Insurance Co. Circumferences and Areas of Circles Diameter Circum- Area Diameter Circum- Area Diameter Circum- Area ference ference ference 3 9.4248 7.0686 5 15.7080 19.6350 7 21.9911 38.4845 3 We 9.6211 7.3662 5 We 15.9043 20.1289 7 We 22.1875 39.1748 3 x 9.8175 7.6699 5 X 16.1007 20.6290 7 X 22.3838 39.8712 3 We 10.0138 7.9798 5 X 16.2970 21.1352 7 We 22.5S02 40.5738 3 x 10.2102 8.2958 5 X 16.4934 21.6475 7 X 22.7765 41.2825 3 We 10.4065 8.6179 5 We 16.6897 22.1660 7 We 22.9729 41.9973 3 X 10.6029 8.9462 5 X 16.8861 22.6906 7 X 23.1692 42.7183 3 We 10.7992 9.2806 5 We 17.0824 23.2214 7 We 23.3656 43.4454 3 X 10.9956 9.6211 5 X 17.2788 23.7583 7 X 23.5619 44.1786 3 % 11.1919 9.9678 5 We 17.4751 24.3013 7 We 23.7583 44.9180 3 x 11.3883 10.3206 5 X 17.6715 24.8505 7 X 23.9546 45.6635 VWe 11.5846 10.6796 5' We 17.8678 25.4058 7 1 We 24.1510 46.4152 3 x 11.7810 11.0447 5X 18.0642 25.9672 7 X 24.3473 47.1730 3 13 /4 11.9773 11.4159 5 13 4 18.2605 26.5348 7 13 4 24.5437 47.9369 3 X 12.1737 11.7932 5 X 18.4569 27.1085 7 X 24.7400 48.7070 3’54 12.3700 12.1767 5'We 18.6532 27.6884 7'We 24.9364 49.4831 4 12.5664 12.5664 6 18.8496 28.2743 8 25.1327 50.2655 4 We 12.7627 12.9621 6 We 19.0459 28.8665 8 We 25.3291 51.0539 4 X 12.9591 13.3640 6 X 19.2423 29.4647 8 X 25.5254 51.8486 4 ^4 13.1554 13.7721 6X6 19.4386 30.0691 8 We 25.7218 52.6493 4 X 13.3518 14.1863 6 X 19.6350 30.6796 8 X 25.9181 53.4562 4 *4 13.5481 14.6066 6 We 19.8313 31.2963 8 We 26.1145 54.2692 4 X 13.7445 15.0330 6 X 20.0277 31.9191 8 X 26.3108 55.0883 4 Xe 13.9408 15.4656 6X6 20.2240 32.5480 8 We 26.5072 55.9136 4 X 14.1372 ' 15.9043 6 X 20.4204 33.1831 8 X 26.7035 56.7450 We 14.3335 16.3492 6 We 20.6167 33.8243 8 We 26.8999 57.5826 4 X 14.5299 16.8002 6 X 20.8131 34.4716 8 X 27.0962 58.4263 4 u /4 14.7262 17.2573 6 1 Xe 21.0094 35.1251 &We 27.2926 59.2761 4 X 14.9226 17.7205 6 X 21.2058 35.7847 8 X 27.4889 60.1320 4 13 /4 15.1189 18.1899 6' 3 46 21:4021 36.4504 8 13 4 27.6853 60.9941 4 X 15.3153 18.6655 6 X 21.5984 37.1223 8 X 27.8816 61.8624 4 15 4e 15.5116 19.1472 6 15 X 21.7948 37.8004 8 l We 28.0780 62.7367 5 15.7080 19.6350 7 21.9911 38.4845 9 i 28.2743 63.6173 The H art ford Steam Boiler Inspection and Insurance Co 59 Circumferences and Areas of Circles Diameter Circum¬ ference Area Diameter Circum¬ ference Area Diameter Circum¬ ference Area 9 28.2743 63.6173 11 34.5575 95.0332 13 40.8407 132.7323 9 14 9 yi 9 We 28.4707 28.6670 28.8634 64.5039 65.3967 66.2956 U We 11 X 11 We 34.7539 34.9502 35.1466 96.1162 97.2053 98.3006 13 We 13 X 13 We 41.0371 41.2334 41.4298 134.0116 135.2971 136.5887 9 X 29.0597 67.2006 H X 35.3429 99.4020 13 X 41.6261 137.8865 9 We 9 H 9 We 29.2561 29.4524 29.6488 68.1118 69.0291 69.9526 11 We u X U We 35.5393 35.7356 35.9320 100.5095 101.6232 102.7430 13 We 13 X 13 We 41.8225 42.0188 42.2152 139.1903 140.5004 141.8165 9 X 29.8451 70.8822 11 X 36.1283 103.8689 13 X 42.4115 143.1388 9 We 9 X 9 x We 30.0415 30.2378 30.4342 71.8179 72.7598 73.7078 11 We li x ll 1 We 36.3247 36.5210 36.7174 105.0010 106.1392 107.2835 13 We 13 X 13 x We 42.6078 42.8042 43.0005 144.4672 145.8018 147.1425 9 X 30.6305 74.6619 11 X 36.9137 108.4340 13 X 43.1969 148.4893 9 x We 9 H 9 x We 30.8269 31.0232 31.2196 75.6222 76.5886 77.5611 ll x W> li X IDWe 37.1101 37.3064 37.5028 109.5907 110.7534 111.9223 13i We 13 X 13‘We 43.3932 43.5896 43.7859 149.8423 151.2014 152.5667 10 31.4159 78.5398 12 37.6991 113.0973 14 43.9823 153.9380 10 We 10 X 10 We 31.6123 31.8086 32.0050 79.5246 80.5156 81.5127 12 We 12 X 12 We 37.8955 38.0918 38.2882 114.2785 115.4658 116.6592 14 We 14 X 14 We 44.1786 44.3750 44.5713 155.3156 156.6992 158.0890 io X 32.2013 82.5159 12 X 38.4845 117.8588 14K 44.7677 159.4849 10 We 10 3/8 io We 32.3977 32.5940 32.7904 83.5253 84.5407 85.5624 12 We 12 H 12 We 38.6809 38.8772 39.0736 119.0645 120.2764 121.4943 14 We 14 X 14 We 44.9640 45.1604 45.3567 160.8870 162.2952 163.7095 io X 32.9867 86.5901 12 X 39.2699 122.7185 14 X 45.5531 165.1300 io We 10 x 10 iWe 33.1831 33.3794 33.5758 87.6240 88.6641 89.7103 12 We 12 X 12 x We 39.4663 39.6626 39.8590 123.9487 125.1851 126.4276 14 We 14 X 14‘We 45.7494 45.9458 46.1421 166.5566 167.9893 169.4282 10 x 33.7721 90.7626 12 X 40.0553 127.6763 14 X 46.3385 170.8732 10 iWe 10 X 10 iWe 33.9685 34.1648 34.3612 91.8210 92.8856 93.9563 12i We 12 X 12 1 We 40.2517 40.4480 40.6444 128.9311 130.1920 131.4591 14iWe 14 X 14iWe 46.5348 46.7312 46.9275 172.3243 173.7816 175.2450 11 34.5575 95.0332 13 40.8407 132.7323 15 47.1239 176.7146 60 The H ar tf or d Steam Boiler Inspection and Insurance Co Circumferences and Areas of Circles Diameter Circum- Area Diameter Circum- Area Diameter Circum- Area ference ference ference 15 47.124 176.715 20 62.832 314.159 25 78.540 490.874 X 47.517 179.672 X 63.225 318.099 X 78.933 495.795 X 47.909 182.654 X 63.617 322.062 X 79.325 500.740 X 48.302 185.661 x& 64.010 326.051 X 79.718 505.710 X 48.695 188.692 X 64.403 330.064 X 80.111 510.705 X 49.087 191.748 X 64.795 334.101 X 80.503 515.724 X 49.480 194.828 X 65.188 338.163 X 80.896 520.768 X 49.873 197.933 X 65.581 342.250 X 81.289 525.836 16 50.265 201.062 21 65.973 346.361 26 81.681 530.929 X 50.658 204.216 X 66.366 350.496 X 82.074 536.046 X 51.051 207.394 X 66.759 354.656 X 82.467 541.188 X 51.444 210.597 X 67.152 358.841 X 82.860 546.355 X 51.836 213.825 X 67.544 363.050 X 83.252 551.546 X 52.229 217.077 X 67.937 367.284 X 83.645 556.761 Va 52.622 220.353 X 68.330 371.542 X 84.038 562.001 X 53.014 223.654 X 68.722 375.825 X 84.430 567.266 17 53.407 226.980 22 69.115 380.133 27 84.823 572.555 X 53.800 230.330 X 69.508 384.465 x 85.216 577.869 Va 54.192 233.705 X 69.900 388.821 X 85.608 583.207 X 54.585 237.104 X 70.293 393.202 X 86.001 588.570 X 54.978 240.528 X 70.686 397.608 X 86.394 593.957 X 55.371 243.977 X 71.079 402.038 X 86.786 599.369 Va 55.763 247.450 X 71.471 406.493 X 87.179 604.805 X 56.156 250.947 X 71.864 410.972 X 87.572 610.266 18 56.549 254.469 23 72.257 415.476 28 87.965 615.752 yk 56.941 258.016 X 72.649 420.004 yk 88.357 621.262 Xa 57.334 261.587 X 73.042 424.557 X, 88.750 626.797 X • 57.727 265.182 X 73.435 429.134 X 89.143 632.356 X 58.119 268.802 X 73.827 433.736 X 89.535 637.940 X 58.512 272.447 X 74.220 438.363 X 89.928 643.548 Va 58.905 276.117 X 74.613 443.014 X 90.321 649.180 X 59.298 279.811 X 75.006 447.689 X 90.714 654.838 19 59.690 283.529 24 75.398 452.389 29 91.106 660.520 X 60.083 287.272 X 75.791 457.114 X 91.499 666.226 X 60.476 291.039 X 76.184 461.863 X 91.892 671.957 X 60.868 294.831 X 76.576 466.637 X 92.284 677.713 X 61.261 298.648 X 76.969 471.435 X 92.677 683.493 X 61.654 302.489 X 77.362 476.258 X 93.070 689.297 X 62.046 306.355 X 77.754 481.105 X 93.462 695.126 X 62.439 310.245 X 78.147 485.977 X 93.855 700.980 20 62.832 314.159 25 78.540 490.874 30 94.248 706.858 ( The Hartford Steam Boiler I nspection and Insurance Co 61 Circumferences and Areas of Circles Diameter Circum¬ ference Area Diameter Circum¬ ference Area Diameter Circum¬ ference Area 30 94.248 706.86 35 109.956 962.11 40 125.664 1256.64 A 94.640 712.76 A 110.348 969.00 A 126.056 1264.50 A 95.033 718.69 Va 110.741 975.91 A 126.449 1272.39 A 95.426 724.64 A 111.134 982.84 A 126.842 1280.31 A 95.819 730.62 A 111.526 989.80 A 127.234 1288.25 A 96.211 736.62 A 111.919 996.78 A 127.627 1296.21 Va 96.604 742.64 Va 112.312 1003.79 A 128.020 1304.20 A. 96.997 748.69 A 112.705 1010.82 A 128.413 1312.22 31 97.389 754.77 36 113.097 1017.88 41 128.805 1320.25 A 97.782 760.87 A 113.490 1024.96 A 129.198 1328.32 Va 98.175 766.99 A 113.883 1032.06 A 129.591 1336.40 A 98.568 773.14 A 114.275 1039.19 A 129.983 1344.52 A 98.960 779.31 A 114.668 1046.35 A 130.376 1352.65 A 99.353 785.51 A 115.061- 1053.53 A 130.769 1360.81 Va 99.746 791.73 Va 115.454 1060.73 A 131.162 1369.00 A 100.138 797.98 7 A 115.846 1067.96 A 131.554 1377.21 32 100.531 804.25 37 116.239 1075.21 42 131.947 1385.44 a 100.924 810.54 A 116.632 1082.49 A 132,340 1393.70 Va 101.316 816.86 A 117.024 1089.79 A 132.732 1401.98 H 101.709 823.21 A 117.417 1097.12 A 133.125 1410.29 A 102.102 829.58 A 117.810 1104.47 A 133.518 1418.62 102.494 835.97 A 118.202 1111.84 A 133.910 1426.98 Va 102.887 842.39 A 118.595 1119.24 A 134.303 1435.36 A 103.280 848.83 A 118.988 1126.66 A 134.696 1443.77 33 103.673 855.30 38 119.381 1134.11 43 135.088 1452.20 H 104.065 861.79 A 119.773 1141.59 A. 135.481 1460.66 Va 104.458 868.31 A 120.166 1149.09 A 135.874 1469.14 H 104.851 874.85 A 120.559 1156.61 A 136.267 1477.64 A 105.243 881.41 A 120.951 1164.16 A 136.659 1486.17 A 105.636 888.00 A 121.344 1171.73 A 137.052 1494.72 Va 106.029 894.62 A 121.737 1179.32 A 137.445 1503.30 A 106.422 901.26 A 122.129 1186.94 A 137.837 1511.90 34 106.814 907.92 39 122.522 1194.59 44 138.230 1520.53 H 107.207 914.61 A 122.915 1202.26 As 138.623 1529.18 Va 107.600 921.32 A 123.308 1209.96 A 139.016 1537.86 A 107.992 928.06 A 123.700 1217.67 y& 139.408 1546.56 A 108.385 934.82 A 124.093 1225.42 A 139.801 1555.28 Az 108.778 941.61 A 124.486 1233.19 A 140.194 1564.03 Va 109.170 948.42 A 124.878 1240.98 A 140.586 1572.81 A 109.563 955.25 A 125.271 1248.80 A 140.979 1581.61 35 109.956 962.11 40 125.664 1256.64 45 141.372 1590.43 62 The H a rtf or d Steam Boiler Inspection and Insurance Co Circumferences and Areas of Circles Diameter Circum¬ ference Area Diameter Circum¬ ference Area Diameter Circum¬ ference Area 45 141.372 1590.43 50 157.080 1963.50 55 172.788 2375.83 A 141.764 1599.28 As 157.472 1973.33 As 173.180 2386.64 y 142.157 1608.15 A 157.865 1983.18 A 173.573 2397.48 A 142.550 1617.05 As 158.258 1993.06 A 173.966 2408.34 A 142.942 1625.97 K 158.650 2002.96 A 174.358 2419.22 A 143.335 1634.92 As 159.043 2012.89 As 174.751 2430.13 y 143.728 1643.89 A 159.436 2022.84 A, 175.144 2441.07 As 144.121 1652.88 A 159.828 2032.82 As 175.536 2452.03 46 144.513 1661.90 51 160.221 2042.82 56 175.929 2463.01 A 144.906 1670.95 A 160.614 2052.85 As 176.322 2474.02 A 145.299 1680.02 A 161.007 2062.90 A 176.715 2485.05 A 145.691 1689.11 As 161.399 2072.97 As 177.107 2496.11 A 146.084 1698.23 A 161.792 2083.07 K 177.500 2507.19 A 146.477 1707.37 As 162.185 2093.20 As 177.893 2518.29 3 A 146.870 1716.54 A. 162.577 2103.35 A 178.285 2529.42 A 147.262 1725.73 As 162.970 2113.52 As 178.678 2540.58 47 147.655 1734.94 52 163.363 2123.72 57 179.071 2551.76 A 148.048 1744.19 As 163.756 2133.94 As 179.464 2562.96 A 148.440 1753.45 A, 164.148 2144.19 A, 179.856 2574.19 H 148.833 1762.74 As 164.541 2154.46 A 180.249 2585.45 A 149.226 1772.05 A* 164.934 2164.75 A 180.642 2596.73 A 149.618 1781.39 A 165.326 2175.08 As 181.034 2608.03 A 150.011 1790.76 A 165.719 2185.42 A 181.427 2619.35 A 150.404 1800.14 As 166.112 2195.79 As 181.820 2630.70 48 150.796 1809.56 53 166.504 2206.18 58 182.212 2642.08 A 151.189 1818.99 A 166.897 2216.60 As 182.605 2653.48 A 151.582 1828.46 A 167.290 2227.05 A 182.998 2664.91 H 151.974 1837.94 As 167.682 2237.52 A 183.390 2676.36 A 152.367 1847.45 A 168.075 2248.01 A 183.783 2687.83 A 152.760 1856.99 As 168.468 2258.53 A 184.176 2699.33 A 153.153 1866.55 A 168.861 2269.07 A 184.569 2710.85 A 153.545 1876.13 As 169.253 2279.63 As 184.961 2722.40 49 153.938 1885.74 54 169.646 2290.22 59 185.354 2733.97 A 154.331 1895.37 As 170.039 2300.84 A 185.747 2745.57 A 154.723 1905.03 A, 170.431 2311.48 A 186.139 • 2757.19 As 155.116 1914.72 As 170.824 2322.14 As 186.532 2768.84 A 155.509 1924.42 A 171.217 2332.83 A 186.925 2780.51 A 155.902 1934.15 A 171.610 2343.54 As 187.318 2792.20 A 156.294 1943.91 A 172.002 2354.28 A, 187.710 2803.92 A 156.687 1953.69 As 172.395 2365.04 As 188.103 2815.67 50 157.080 1963.50 55 172.788 2375.83 60 188.496 2827.43 The Hartford Steam Boiler Inspection and Insurance Co 63 Circumferences and Areas of Circles Diameter Circum- Area Diameter Circum- Area Diameter Circum- Area ference ference ference > 60 188.496 2827.43 65 204.204 3318.31 70 219.911 3848.45 X 188.888 2839.23 X 204.596 3331.08 X 220.304 3862.21 X 189.281 2851.04 X 204.989 3343.88 X 220.697 3875.99 X 189.674 2862.89 X 205.382 3356.71 X 221.090 3889.80 X 190.066 2874.75 X 205.774 3369.55 X 221.482 3903.63 X 190.459 2886.65 X 206.167 3382.43 X 221.875 3917.48 X 190.852 2898.56 X 206.560 3395.33 X 222.268 3931.36 X 191.244 2910.50 X 206.952 3408.25 X 222.660 3945.26 61 191.637 2922.47 66 207.345 3421.19 71 223.053 3959.19 x 192.030 2934.46 X 207.738 3434.17 X 223.446 3973.15 x 192.423 2946.47 X 208.130 3447.17 X 223.838 3987.12 X 192.815 2958.51 X 208.523 3460.18 X 224.231 4001.13 X 193.208 2970.57 X 208.916 3473.23 X 224.624 4015.15 X 193.601 2982.66 X 209.309 3486.30 X 225.017 4029.20 X 193.993 2994.77 X 209.701 3499.39 X 225.409 4043.28 X 194.386 3006.91 X 210.094 3512.51 X 225.802 4057.38 62 194.779 3019.07 67 210.487 3525.65 72 226.195 4071.50 X 195.172 3031.26 X 210.879 3538.82 X 226.587 4085.65 X 195.564 3043.47 X 211.272 3552.01 X 226.980 4099.83 X 195.957 3055.70 X 211.665 3565.23 X 227.373 4114.03 X 196.350 3067.96 X 212.058 3578.47 X 227.766 4128.25 X 196.742 3080.25 X 212.450 3591.74 X 228.158 4142.50 X 197.135 3092.56 X 212.843 3605.03 X 228.551 4156.77 X 197.528 3104.89 X 213.236 3618.34 X 228.944 4171.07 63 197.920 3117.25 68 213.628 3631.68 73 229.336 4185.39 X 198.313 3129.63 X 214.021 3645.05 X 229.729 4199.73 X 198.706 3142.03 X 214.414 3658.43 X 230.122 4214.10 X 199.098 3154.47 X 214.806 3671.85 X 230.514 4228.50 X 199.491 3166.92 X 215.199 3685.28 X 230.907 4242.92 X 199.884 3179.40 X 215.592 3698.75 X 231.300 4257.36 X 200.276 3191.91 X 215.984 3712.23 X 231.692 4271.83 X 200.669 3204.44 X 216.377 3725.75 X 232.085 4286.32 r 64 201.062 3216.99 69 216.770 3739.28 74 232.478 4300.84 X 201.455 3229.57 X 217.163 3752.84 X 232.871 4315.38 X 201.847 3242.17 X 217.555 3766.43 X 233.263 4329.95 X 202.240 3254.80 X 217.948 3780.04 X 233.656 4344.54 X 202.633 3267.45 X 218.341 3793.67 X 234.049 4359.16 X 203.025 3280.13 X 218.733 3807.33 X 234.441 4373.80 X 203.418 3292.83 X 219.126 3821.01 X 234.834 4388.46 X 203.811 3305.56 X 219.519 3834.72 X 235.227 4403.15 65 204.204 3318.31 70 219.911 3848.45 75 235.619 4417.86 64 The Hartford Steam Boiler Inspection and I nsur ance Co Circumferences and Areas of Circles Diameter Circum- Area Diameter Circum- Area ' Diameter Circum- Area ference ference ference 75 235.619 4417.86 80 251.327 5026.55 85 267.035 5674.50 x 236.012 4432.60 X 251.720 • 5042 .'27 X 267.428 5691.20 X 236.405 4447.37 X 252.113 5058.01 X 267.821 5707.93 X 236.798 4462.15 X 252.506 5073.78 X 268.214 5724.68 X 237.190 4476.97 X 252.89S 5089.58 X 268.606 5741.46 x 237.583 4491.80 X 253.291 5105.39 X 268.999 5758.26 X 237.976 4506.66 X 253.684 5121.24 X 269.392 5775.08 X 238.368 4521.55 X 254.076 5137.10 X 269.784 5791.93 76 238.761 4536.46 81 254.469 5153.00 86 270.177 5808.80 X 239.154 4551.39 X 254.862 5168.91 X 270.570 5825.70 X 239.546 4566.35 X 255.254 5184.85 X 270.962 5842.63 X 239.939 4581.34 X 255.647 5200.82 X 271.355 5859.57 X 240.332 4596,35 X 256.040 5216.81 X 271.748 5876.55 X 240.724 4611.38 X 256.432 5232.83 X 272.140 5893.54 X 241.117 4626.44 X 256.825 5248.86 X 272.533 5910.56 X 241.510 4641.52 X 257.218 5264.93 X 272.926 5927.61 77 241.903 4656.63 82 257.611 5281.02 87 273.319 5944.68 X 242.295 4671.76 X 258.003 5297.13 X 273.711 5961.77 X 242.688 . 4686.91 X 258.396 5313.27 X 274.104 5978.89 X 243.081 4702.09 X 258.789 5329.43 X 274.497 5996.04 X 243.473 4717.30 X 259.181 5345.62 X 274.889 6013.20 X 243.866 4732.53 X 259.574 5361.83 X 275.282 6030.40 X 244.259 4747.78 X 259.967 5378.06 X 275.675 6047.62 X 244.652 4763.06 X 260.360 5394.32 X 276.068 6064.86 78 245.044 4778.36 83 260.752 5410.61 88 276.460 i 6082.12 X 245.437 4793.69 X 261.145 5426.92 X 276.853 6099.41 X 245.830 4809.04 X 261.538 5443.25 X 277.246 6116.73 X 246.222 4824.42 X 261.930 5459.61 X 277.638 6134.07 X 246.615 4839.82 X 262.323 5475.99 X 278.031 6151.44 X 247.008 4855.25 X 262.716 5492.40 X 278.424 6168.82 X 247.400 4870.70 X 263.108 5508.83 X 278.816 6186.24 X 247.793 4886.17 X 263.501 5525.29 X 279.209 6203.68 79 248.186 4901.67 84 263.894 5541.77 89 279.602 6221.14 X 248.578 4917.19 X 264.286 5558.28 X 279.994 6238.63 X 248.971 4932.74 X 264.679 5574.81 X 280.387 6256.14 X 249.364 4948.32 X 265.072 5591.36 X 280.780 6273.67 X 249.757 4963.91 X 265.465 5607.94 X 281.172 6291.24 X 250.149 4979.54 X 265.857 5624.54 X 281.565 6308.82 X 250.542 4995.18 X 266.250 5641.17 X 281.958 6326.43 X 250.935 5010.85 X 266.643 5657.82 X 282.351 6344.07 80 251.327 5026.55 85 267.035 5674.50 90 282.743 6361.73 The Hartford Steam Boiler I nspcction and Insurance Co 65 Circumferences and Areas of Circles Diameter Circum¬ ference Area Diameter Circum¬ ference Area Diameter Circum¬ ference Area 90 282.743 6361.73 95 298.451 7088.22 100 314.159 7853.98 y 283.136 6379.41 y 298.844 7106.88 y 314.552 7873.63 y 283.529 6397.12 y 299.237 7125.57 y 314.945 7893.30 H 283.921 6414.85 y 299.629 7144.29 y 315.337 7913.00 y 284.314 6432.61 y 300.022 7163.03 y 315.730 7932.72 y 284.707 6450.39 y 300.415 7181.79 y 316.123 7952.46 K 285.100 6468.20 y 300.80S 7200.58 y 316.516 7972.23 14. 285.492 6486.03 14 301.200 7219.39 y 316.908 7992.03 91 285.885 6503.88 96 301.593 7238.23 101 317.301 8011.85 y 286.278 6521.76 y 301.986 7257.09 y 317.694 8031.69 y 286.670 6539.67 y 302.378 7275.98 y 318.086 S051.56 y 287.063 6557.60 y 302.771 7294.89 y 318.479 8071.45 K 287.456 6575.55 y 303.164 7313.82 y 318.872 8091.37 y 287.848 6593.53 y 303.556 7332.78 y 319.264 8111.31 y 288.241 6611.53 y 303.949 7351.77 y 319.657 8131.28 H 288.634 6629.56 14 304.342 7370.78 y 320.050 8151.27 92 289.027 6647.61 97 304.734 7389.81 102 320.442 8171.28 l A 289.419 6665.69 y 305.127 7408.87 y 320.835 8191.32 y 289.812 6683.79 y 305.520 7427.95 y 321.228 8211.39 H 290.205 6701.91 y 305.913 7447.06 y 321.620 8231.48 y 290.597 6720.06 y 306.305 7466.19 y 322.013 8251.59 H 290.990 ' 6738.24 y 306.698 7485.35 y 322.406 8271.73 y 291.383 6756.44 y 307.091 7504.53 y 322.799 8291.89 14 291.775 6774.66 14 307.483 7523.73 y 323.191 8312.08 93 292.168 6792.91 98 307.876 7542.96 103 323.584 8332.29 y 292.561 6811.18 y 308.269 7562.22 y 323.977 8352.53 y 292.954 6829.48 y 308.662 7581.50 y 324.369 8372.79 H 293.346 6847.80 y 309.054 7600.80 y 324.762 8393.07 y 293.739 6866.15 y 309.447 7620.13 y 325.155 8413.38 y 294.132 6884.52 y 309.840 7639.48 y 325.548 8433.72 y 294.524 6902.91 y 310.232 7658.86 y 325.940 8454.08 y 294.917 6921.33 y 310.625 7678.26 y 326.333 8474.46 94 295.310 6939.78 99 311.018 7697.69 104 326.726 8494.87 295.702 6958.25 y 311.410 7717.14 y 327.118 8515.30 y 296.095 6976.74 y 311.803 7736.61 y 327.511 8535.76 y 296.488 6995.26 y 312.196 7756.11 y 327.904 8556.24 y 296.880 7013.80 y 312.588 7775.64 y 328.296 8576.74 y 297.273 7032.37 y 312.981 7795.19 y 328.689 8597.28 y 297.666 7050.96 y 313.374 7814.76 y 329.082 8617.83 14 298.059 7069.58 y 313.767 7834•36 y 329.474 8638.41 95 298.451 7088.22 ! 00 314.159 7853.98 105 329.867 8659.01