Document ZJ8yodEEyYQLQmQNeV2B9w9YZ
FILE NAME: ZK/L DATE: : DOC#: BO/L DOCUMENT DESCRIPTION: d:Z
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JU~Y 1 95 1
VOLUME 95
Opera/lnq NO. 7
combined wi,,,
ENGINUR
ENGINEERING AND MANAGEMENT
The long look 'ahead-an editorial .
69
Crushers cinch fuel sizing and cleaning
73
Chemical feeding-direct to boilers
76
Electronics: Control for dc motors: Part 2
78
Th! balky ash-removal system-Case No. 2 in a series
80
.v.;cr'f midget produces piloting power
113
:l'1s"i:Jt:on cuts mercury-unit losses
150
POWER HANDBOOK-Part Two: Basic power services
81
feedwater chemistry
c ...... .... " 1.. ~ ....... ~t....IIC'+:
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Steam generation Steam turbines Diesels & gas engines Compressors & fans Refrigeration
82
Heating
100
86
.AJr cor.d!tiordng
102
90
Heat-transfer equipment 104
92
Lubrication
106
94
Insulation
107
96
Electrical machinery
108
98
Ac converters
112
PLANT OPERATION AND MAINTENANCE
BOILERS are hig hu"in .... " on thl' We"t Coa"t th.."e day". Long a hydro -trnn!!hold, California now turn .. to -It-arn po\\er 3, booming demand out.. trip, waler'power potential.
Our ('o, ..r ('allh," thi" tr"n'! in an illl'
pn'''"iw "hot of aB&: \'1/ radiant !wil"r at Pacific: Ca" &: EI...-tric'" \[0-'; wntling Sta tion. Wielding the ratchet hoist i-; a Illpmh"r of th, C C ~Ioore Co eredioa CCl'W.
Boil"r is one. 0 f six -l7S,OO)lh,p,rhr unit" supplying three lOO,OOO-kw turbinegt'nerator,.. One of the,e machines has been operating ahout a year, olh"r two, see serviee ,;oon. \Vith two mort' turhinegenerators and their boilers plannl'.! for 1952, this 1300-p"i 9S0-F outdoor plant promises to be the largest west of the \li",.i:'sippi. But til,':'e day" who can tell ~
Slash handhole-plate time-Operators' Notebook No. 43
5cale scots fast now that cooling-water gets care
Buying silent c',ain? Then you'd better start here Aim at best Oll ~ut for centrifugals
Hot maintenance 1'1-' for propeller pumps
H"re s how to build your own stroboscopic tachometer
Pructical Ideas
130
How to
Plant problems
136
Headwork
Arguments
142
Marmaduke
118 .120 122 124 126 128
1
146
148
READER SERVICE SECTION
, ~Iant [jr:ta ,heet: Number 229 152
equipment news
160
PJ'Ner news
154
Engineer's bookshelf
172
T.!chr:ical briefs
156
George Edwards
174
POWER
Vol 95-No. 7
(Member ABC and ABP)
,':')'04 1 t.....:
,1 .f with whi,h arc con,solidatcd Scien~~ and ,Industry. Th~ E'}Kint'u Re~'l:t'w. T1t~ Engintt'" Tilt'
i .~ rI " l-.If1t:IIlt'a and Opaalln~ Engfnt'a) IS published monthly with an addItIonal directory number
I \ PL:BLl- r':~\ ~:r~\'ft:a~;~(W~:&_IU\'Lnc: B1:m)~'t~G.l~~o ~~~,,~ ~~'o/1,\v ~~6~iJ.9t~.) :l~~ndCr.
,- .. 'Le. T1\ E. EDITOR!.-\L and ADVERTlSI:-OOG OFFICES: JJO W 4:nd St. New York lB. N. Y. ~""r , \\, \1..:GrJ.w. Prcsid.ent: Willard Chevalier. E~cculi\e Vice-President: Joscph A Gcrardi. ViccI;'':.' .(~~ ..I~d Treasurer; John J Cookc. Secretary; Paul Mont(~omcTY. -?cnior Vice-President. PubUcations
, t \~~~I.. ~~l~.h V~cc:Prl~~i'de;~it~ri~alD~~~~~O~{ ~fr~i'ati~~~d. Vice-President and Director of Adverusing;
11 ~. IlS'-'RIPTlO:O;S: Address correspondence to POWEa. Subscription Service. 330 W 4~nd St. :-OOcw York S ). Allo".' tcn days for change of address. Please indicate position and company connection on orders.
'f"'"~""; .n~1c COPies 50C. Subscription rates- U. S. and U. S. possessions: $4.00 for one year. $6.00 for two $..." t. 1.,n3Ja: $7.00 for one year. Sl1.00 for two years. All other countries: 515.00 for one year. S15.oo $/".-k .... 1) yeaN. Entered as s.econd-class matter January 26. 1949 at the post office at New York. N. Y. '\:1 r~:'~l~t r~~C~'~d~h 3. 1879. Printed in U.S.A. Copyright 1951 by McGraw-Hill Publishing Company. Int.:.
t'.l ! J~~I':" t lit .:t.rtidt.!'.~ arc indexed in ~oth the. Industrial. Arts Index and the Eng/nt!t;ring Index. POWER .l \ It-!. o\o,.'n mJex annu311Y.,~oplt.!'s of whl~h are av;,:u13blc un n:qur,;st to the ctlilonal otfkcs.
------------------------------------------------------------------------~
Next month ..
Right in the heat of the ba,,<'hall "ea"on we're pullin~ a trip1,' pia\' of our own. In Augu"t you'll find the lowdown on welJ,; and well pUlllpS in---(,lIullt ,'m! -three place,: basic fact .. in the E&\[ section, care and ~epair in PO&\I, tip" on testing in the Data Shed. Be ;:ure you cover all bases!
_-\t Sewaren they've gone all out to g' .. t ma"illllllll ll1.1b'"~l !lllritv. '1'011'11 see why in _-\ugu,t', ,tory on how they treat city water for evaporator feed.
Another .l/an 0/ Action story take,;
YOU to Ea"tman Kodak's I-bwkeve plant. it'll,; you how Wavne Farrl'll keep" on top of his job of making thi .. plant top" in efficiency. cleanline-...
Cot "om!' el,ttrit'otl "q"ip"lt'nt tu han;! 011 a w:.dl'~ Gr:lh Jim O'Collnor'" "hahy" "pt'cial -eetion Oil an('horsthat's where YOll'lI find all the n'~w wrinkles---and te"ted old onp:i-for doing: lhe joh !}ui,'kh' and easily.
.. and future months
Being readied for October: a 16-pg handbook on fans (both draft and ventilating l. It'll Ctlver ba"ic fan facts. types and arrangement .., construction, fan ch:uacteristics. drives and control. selecting and applying fan:', opt' rating and maintaining them.
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fiGURING HEAT LOSS, ECONOMIC THICKNESS
raWe*, lower right, shows loss for various .hicknesses of as~ magnesia insulation applied to pipelines or flat surfactS 300 deg F hotter than surrounding air. Data can be
uJt<i approximately for such insulations as mineral wool at!d ~ponge-felted asbestos. If temperature difference is
sreater or less than 300 F, apply factor from chart. I,XAMPLE: A 220-ft run of 4-in. pipe insulated with double-
standard insulation carries process steam (saturated) at
600 psig through. a room at 80 F. What is hourly heat loss? Solution. Pipe temperature is 490 F, from scale, so tem-
ptrature difference is 410 F. Factor from chart is 1.45.
Loss per ft of pipe run at 300 F, from table, is 89.4 Btu.
10tal less is 89.4 X 1.45 X 220 = 28,500 Btu per hr.
ECONOMIC THICKNESS. To figure economic thickness for
insulation, draw up a table for the specific job similar to one shown below for a heater.
Thickness,
UKhc!i
0
. 1
1 ~';' 2
2 I, '
J
Total insulation cost in:jtitl1ed
$200 260
' 318 374 429
Total yearly dollar
1055
$720 180 126 96 76 62
co.t of added insulation
thick~es~
$200 60 58 56 55
Years (or
Added added.a vsaving ing to pay
Rd<\p<\ cost
$540
0.37
54
1.11
30
1.93
20
2.80
14
3.92
Then pick the thickness that pays off in the time required
by your plant's financial policy. If insulation above has to
payoff within three yearg, use 2~-in.
Fr'.llIl M&.6Desia Insulation Manu!&cturers A.aocl&tton.
PRESSURETEMPERATURE SCALE
I +: iO I
I I
620 200
Gage pressure, psi
10
2I0 I
50 100 1 I1111I
150 200 I I
500 I II
1000 1400
III I I J I
TEMPERATURE CORRECTION FACTOR
(lIased on 300-deg F temperoture difference os normal)
la
1.7 16 1.5 1.4 1.3 12 I. I 1.0
2 09
~ 08
"- 07 0.6 05
V 0.4
Q.3
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1/ V
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y'
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1 11-
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02 O. I
o
00
2CO
300
400
500
Temperature difference, deg F
dual." ,ttlyarepetJo." ',:!
sed. 'c~: ','
petroleum. . ne soda.~. 11i~ soaps .~:
)otassium.~"
n in bear.J: ';ji; pressurd.l graphite,
0.-1' and yam ":'
Icants. 'ones) re ,.Cl>" .
undetl ~el1
~:;!'I:lr propertieS;
, avoidin& ,: ~: Iture addi- ,
-' .I~t.' important;Jf
serving as ~~~'
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. cdMM'ERCIAL ,<.'.;
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IN$UL~TION>'.. ,- .;.>.
-,
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KINDS ANO Sh 'PES
.'", ., OF
,
e : HEAT INSULATION
... - ".,. FOR
t .,., '" WARM SURFACES
0
I
0
~
'" ... :;:; :>
0
0
;;;~
"" ~ g.a ~ : ~
." Q.
c
~0 0 ]! Q. 0
V< :>
c:
g~
V< U :> -
'" ",,; '" ~ E - E ~ Q0j :0:;: .I. 0V< ~ _0 00 0u 0 o ."'c": .Q " .SE:>
g.8 .E:9 ~ ~
0 0
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0.=
E E 2.:!
o il.. <i
<t
IX)
Q. V< f/) 0
~
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u 0
<:'-'iJ 1 ""'" t@m~,.rytl)"f?
200 300 750 600 700 1000 1900 2500
r
F F ,-
r f
f
F
:....:..ose or granulated
.....- ...... ......
~ ~ T.ent
...... ...... .....
...,. ..... 3:anket~;'l
'A xHs
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,fleXible)
0t:fijJf! ~cards
blocks 1st Iff)
.:;- -=--
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VV VV
......
..... V ~ .....- .....- ......
f!!!!!!!if'"' 'JaIded"
,egnents'
~
Shaped sections
C.~
V
Y
..... V Y
V .....
Bricks E l
......
HEAT LOSS THROUGH 85 % MAGNESIA
(Multiply by correction factor from above chart)
Pipe Insulltion Heat size, thickness, loss, inches inches Btu'
P,p, Insul.tion He.t SiZI, thiCKness, loss. inches inChes Btu'
Pipe Insulation Hut size, thlcKnl!ss, loss, inches incnes Btu
1/2 7/8 (s) ~l.9
1112
40.8
1 29/32 (d,) 36.9
2
36.2
2 1/2
33.0
3
30.9
I 1/32 (s) g2.4
1 1/2
:4.0
2
63.0
2 S/32 (d,) 50.5
2 1!2
55.8
3
50.6
1 1/8 (s) 1nl
1112
138
2
\l)
2 5/16 (dl) 103
2 1/2
97 .~
3
86.4
3/4 7/8 (s) ~9.1
1 1/2
4~.7
I 29/32 (ds) 41.1
2
40.2
2 1/2
36.~
3
33.9
2 112 I !i32 (.) 106
I 1/2
!U
2
11.1
2 5m (ds) ;7.8
2 1/2
;2.4
3
56.6
1 1/8 Is) 1112 2
2~,:6(ds)
2 liZ 3
195 158 I2S 117 III
97.8
718 (s) 67.l
I 1/2
~1.7
I 29/32 (ds) 46.1
2
IS.J
2I 1
40.'
3
37.;
IV4 7,8 (si 79.5
1 1/2
~9.2
119131 (ds) 51.4
2
SI.1
2 112
45.7
3
41.J
1 112 7/8 (s) 8&.7
1112
R2
I 29/32 (ds) SU
2
~S.!
21!2
49.2
3
4~.O
11.32(') :13
I 1/2
%.9
2
81.0
2 5.32 (ds) 77.4
1 :.1
70,]
3
63.;
31.2 1 1 J2 Is) :37
1 1/1
:07
2
815
2\,31 (ds) 84.7
2 1.2
77.3
3
69.4
1 l.'8 Is) 141
1: 2
116
2
96.5
2 1.'4 (ds) 89.
2 1/2
83.6
3
74.7
11.'1 is) 2Z5
I 1/2
197
2
160
2 1. 1 ids) 136
3
119
10 1 L I ISI 2",.
1l.'Z
118
1
191
Itn (ds) 161
3
141
~~
U.c .;:; .~
.!!.S
!~i C:i~
1 1 112 2 2 1!2 3 31/1 4
96.2-69.9
~u
45.2 38.4 33.1
29.~
(s) SI..dard thickness lds' double-standard tllCkness. Btu per hour per !oot :;! pipe lenltn at 30(}-d~,F temperature dIfference. Btu ~r hour ~e, sQl:a~ foot of Insulatlol1 surface ~ 300~eiF temperature ditferencl!