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A,  C,  rlOVnN 
K. W. VAN    VALZAM 


,OGY 


AlvAOUR   ll-^STrrUir 


9  2  1 


621.5 

If  82 


UNivERsifTy  Lamm 


Digitized  by  tine  Internet  Arciiive 

in  2009  witii  funding  from 

CARLI:  Consortium  of  Academic  and  Researcii  Libraries  in  Illinois 


http://www.archive.org/details/proposeddesignfoOOhove 


A  PROPOSED  DESIGN  FOR  THE  REFRIGERA- 

TION  LABORATORY  FOR  THE  GREATER 

ARMOUR  INSTITUTE  OF  TECHNOLOGY 


12. 


A  THESIS 


PRESENTED    BY 

ALFRED  C.  HOVEN  AND  ROBERT  W.  VAN  VALZAH 

TO  THE 

PRESIDENT  AND  FACULTY 

OF 

ARMOUR  INSTITUTE  OF  TECHNOLOGY 

FOB  THE  DEGREE  OF 

BACHELOR  OF  SCIENCE 

IN 
MECHANICAL   ENGINEERING 


JUNE  2,  1921 


APPROVED 

ILLINOIS  INSTITUTE  OF  TECHNOLOGY       .      ^.^--^CT^/^/  ,^/.-.^,l 

PAUL  V.  GALViN   LIBRARY  '^"'""^  °'  ^'"""'"^  Engineering 

36  WEST  33RD  STREET 

CHICAGO,   IL    60616  °""  °'  Enemeenn.  Studies 

Dean  of  Cultural  Studies 


JTixe 


TAE-LE  OF  CONTENTS 

I .   INTRODUCTION 

II.   BUILDING 

A.  Mater-lal  and  Construction 

B .  Layout 

III.   EXPSRII'IENTAL  ROOMS 
A.  Insulation 
B'  Piping 

C .  Machines 

IV.   ICE  IMICING 

A.  Freezing  Tank 

B.  Water  Supply 
C  Machines 

V.   SMALL  I.'IACHINES 

A.  Creamery  Package  Refrigerating  Machine 
•  B.  Lipman  Refrigerating  Machine 

C.  Continental  Refrigerating  Machine 

D.  Frigldaire  Refrigerator 


.^981 


o 


PLATES 

PAai 

Autoraat-ic  Carbonic  Compressor  19 

York  Absorption  Machine  26 

York  Compression  Machine  52 

York  Piping  Layout  -  W;i,ter  and  Brine  36 

Raw  TiVater  Systeui  3S 

Creamery  Package  Compressor  43 

Creamery  Package  Refrigerating  Machine  45 

Continental  Refrigerating  System  48 

Li'pman  Refrigerating  Machine  52 

Frigidalre  Refrigerator  57 

Laboratory  Floor  Plan  59 


I.     introdiictiot: 

Although  refrlger:  tion  E.nd  the  production 
of  ice  by  artificial  means  was  known  to  the  a,nc- 
ientsjit  is  only  v/ithin  comparatively  recent 
times  that  improved  systeris  and  appare^tus  have 
enabled  operations  to  be  carried  out  on  a  cominer- 
cial  basis-  Fifty  years  ago  the  refrigeration  in- 
dustry was  in  its  infancy  but  great  strides  have 
been  made  since  then.  Last  year, in  America  alone, 
there  v/ei-e  over  seven  thousand  firms  directly  in- 
terested in  the  mechanical  production  of  cold. 

Few  people  realize  the  full  significance  of 
the  part  this  industry  plays  in  our  daily  life. 
Refrigerant  ion  machines  are  used  for  making  ice, 
for  chilling  fresh  kij.led  meat,  for  preserving 
perishable  foods, for  conditioning  of  air, for  mak- 
ing celluloid  films, and  for  many  other  industri- 
al "processes.  They  make  it  possible  for  the 
"Salty  Tar"  to  eat  fresh  foods  when  cruising  off 
the  South  Sea  Isles  while  his  sv/eetheart  sits  com- 
fortably in  an  air  cooled  movie  house  in  Brookl\Ti. 


4 

Because  the  future  of  the  Inductry  depends 
so  largely  on  tho  engineer, we  are  anxious  that 
the  New  and  Greater  Armour  Ii'.stitute  of  Technol- 
ogy shall  have  a  refrigeration  laboratory  v/hlch 
la,cks  not  a  single  detail  essential  to  complete 
experimentation.  Therefore  in  the  design  of  the 
new  laboratory  our  first  concern  has  been  for 
completeness,  '.'.'e  have  aimed  to  make  the  labora- 
tory of  the  greatest  possible  practical  value. 
The  units  chosen, each  in  its  class, represent 
the  best  in  modern  prs.ctice.  Together  they  cover 
very  thoroughly  the  present  day  methods  for  the 
production  of  cold. 

The  wor;:  done  by  refrigeration  machines  may 
be  divided  into  two  general  classes, as  follows: 

1.  The  Manufacture  of  Ice. 

2.  Cooliv.g  by  Direct  Absorption  of  Heat. 
To  re-oresent  the  first  class  of  work,  the 

new  laboratory  will  be  equipped  with  a  tank  for 
the  manufacture  of  ice  by  the  can  system, either 
on  direct  or  indirect  expansion, using  either  raw 
or  distilled  v/ater.  The  free:ring  may  be  done  by 
(O  an  aramonia  compressor,  (2)  a  carbon  dioxide 


5 
compressor,  or  (3)  cin   ammonia  absorption  machine. 

The  second  class  of  work  Is  represented  in 
the  three  insulated  rooms  located  at  one  end  of 
the  laboratory.  Each  of  these  rooms  may  be  cooled 
'Off  by  any  of  the  above  mentioned  machines.  One 
of  the  rooms  will  be  equipped  with  ste;:,m  coils 
and  Y/111  be  used  in  connection  with  experiments 
on  heating  and  ventilating. 

The  equipment  of  the  new  laborf-.tory  \illl 
also  Include  three  small  machines  of  the  type 
used  in  butcher  boxes, floral  shops, and  apart- 
ment buildings.  The  demand  for  machines  of  this 
type  is  growing  rapidly  s.nd  the  conpetitlon  is 
keen.  The  merchant  is  awakening  to  the  fact  ths.t 
the  ice  man's  muss  and  Irregularity  are  unneces- 
s8.ry  evils. 

One  machine  of  the  household  size  is  provid- 
ed to  afford  data  on  the  economy  and  reliability 
of  machines  designed  for  this  purpose.  The  field 
is  greater  than  Henry  Ford's, but  it  has  just  been 
entered. 


BIBLIOG-RAPKY 

The  Llechanlcal  Production  of  Cold 

Ewing 
The  Carbonic  Acid  Industry 

G-oosman 
Elements  of  Refrigeration 

G-reene 
Evaporating, Condensing, and  Cooling  Apparatus 

Hausbra.ad 
Modern  Refrlgers.tion  Llachines 

Lorenze  and  Pope 
MechanlcaJ.  Refrigeration 

Mac  In tyre 
Refrigeration, Cold  Storage, and  Ice  Making 

Tayler 
Complete  Catalogue  of  Ammonia  Valves  and  Fittings 

York  Manufa.cturing  Company 


II.  ^UILDIIIG 

MATERIAL  AND  CONSTRUCTION 

The  Refrigeration  Labo re-tor;:  for  the  Nevf  and 
G-reater  Armour  Institute  of  TechnolOG2-^  v;ill  be 
located  in  a  one  story  brick  building, sixty  feet 
v.-ide  and  one  hundred  thirty  feet  long.  The  build- 
ing will  be  fireproof  throughout.  The  inside  of 
the  W8.11s  shall  be  of  hollov/  tile  except  in  th-j 
offices, wash  rooms, and  experimental  rooms.  The 
walls  of  offices  and  v/ash  rooms  will  be  finished 
in  hard  plaster.  The  insulation, v/hich  forms  the 
walls  of  the  experimental  rooms, is  described  in 
the  part  of  the  thesis  devoted  to  the  rooms. 

The  floor  will  be  made  of  eight  inch  concrete, 
surfaced  v;ith  dust  proof  covering.  The  floor  in 
the  offices  will  be  of  a  selected  maple. 

The  roof  will  be  of  the  garage  type, support- 
ed by  posts  set  twenty  feet  apart.  On  the  roof, a 
platform  will  be  constucted  directly  above  the 
refrigerating  machine  to  be  used  in  cooling  the 
altitude  chamber.  This  platform  is  to  support  the 
atmospheric  condenser  to  be  used  in  connection 


vfith  that  machine. 

LAYOUT 

In  layin,3  out  the  refrigera,tion  laboratory 
the  ohject  sought  was  compactness  v.-lthout  crowd- 
ing or  inaccessibility.  The  future  of  the  labor- 
atory,with  Its  probable  expansion  and  moderniz- 
ing was  kept  constantly  in  view. 

The  entrance  to  the  office  and  the  labora- 
tory will  be  at  an  end  of  the  building.  The  off- 
ice will  be  adjoining  and  connected  to  the  vrash- 
room  and  lavatory.  The  work  bench  will  be  located 
jUEt  outside  of  the  wash-room.  The  Frigidaire  re- 
frigerator and  two  cases  for  exhibits  will  be 
placed  against  the  office  wall. 

The  other  end  of  the  labora,tory  v/ill  be  de- 
voted to  the  experimental  rooms.  There  will  be 
three  rooms  each  thirty  by  tv/enty  feet.  They  may 
may  be  cooled  by  any  of  the  three  machines  to  be 
located  near  the  rooms.  The  Automatic  Carbonic 
machine  will  be  in  front  of  the  rooms  and  the 
York  compression  and  absorption  machines  will  be 


9 
placed  near  either  v/:-,ll .  The  ice  tanlc  will  occu.tj 
the  "U"  fornied  by  these  three  machines. 

The  altitude  chanber  will  be  across  the  lab- 
oratory from  the  office.  It, and  its  equipment  v/111 
form  a  seperate  unit.  The  small  machines  villi   be 
placed  along  the  wall  between  the  altitude  chamber 
and  the  Yorlc  absorption  mc-chine. 


10 

III.   EXPERlIvIENTAL  ROOMS 

The  tonnage  of  refrigeration  devoted  to 
cooling  by  direct  absorption  of  heat  has  come 
to  exceed  that  devoted  to  the  manuf^.cture  of 
ice.  We  are  gradually  aproe,ching  an  iceless  age. 
In  order  th  t  the  problems  confronting  the  engin- 
eer T7ho  designs  coll  storage  houses  and  cooling 
rooms  may  be  thoroughly  studied, the  nev/  labora- 
tory will  contain  three  experimental  rooms. 

Each  room  will  be  thirty  feet  long  by  twenty 
feet  T;ide.  The  two  cold  rooms  will  be  ten  feet 
high, but  the  constant  temperature  room  will  be 
twenty  feet  high  to  permit  experimenting  with 
structures  of  more  than  one  story.  Each  room  vrill 
open  into  the  laboratory,  and  the  room.s  will  also 
be  interconnected.  The  wall  between  the  constant 
temperature  room  end  the  adjoining  cold  room  will 
contain  a  false  section  '.-hlch  can  be  removed. 
This  section  will  afford  an  opportunity  to  study 
heat  conductivity  of  large  sections  placed  be- 
tvfeen  any  desired  difference  of  temperature. 

An  altitude  chamber  ha,s  been  provided  for 


11 

the  automotive  department  to  be  used  in  testing 
aeroplane  motors  under  conditions  found  in  high 
altitudes.  All  the  necessa.ry  Instruments  and  ap- 
paratus Virill  be  furnished  by  the  automotive  dep- 
artment. The  room  will  be  8'  x  10'  x  S '  .  It  v/ill 
be  cooled  indirectly  by  a  two-stage  carbon  diox- 
ide compressor  designed  and  built  by  the  American 
Carbonic  Company.  This  machine  is  especially  a- 
dapted  to  the  work  which  will  be  asked  of  it; 
similar  machines  are  used  throughout  the  country 
for  just  such  work. 

Experiments  run  in  this  room  v/ill  require 
the  removal  of  about  150  tons  of  refrigera.ti jn 
per  day..- ■  A  ten  ton  machine  is  provided  to  be 
used  in  connection  v/ith  a  brine  tank  which  forms 
the  inner  walls  of  the  room, and  has  a  capacity 
of  650  cu .  ft.  of  brine.  By  running  the  refrig- 
erating machine  until  all  the  brine  is  frozen, a 
cape.clty  of  about  I80  tons  may  be  stored  up. 

A  ten  ton  York  atmospheric  condenser' will 
be  provided  for  use  in  connection  v/ith  the  al- 
titude cham.ber  and  in  experiments  on  the  effic- 
iency of  this  type  of  condenser. 


12 

INSULATION  ■ 
All  v;alln,partitlonG,  floors,  and  ceilings 
shall  be  made  of  Wonpareil  corkboard, manufact- 
ured by  the  Arnstrong  Cork  and  Insulation 
Company, and  shall  comply  to  the  follov.'lng  spec- 
ifications : 

TfALLS 
Directly  against  the  brick  walls, one  course 
of  three  inch  Nonpareil  corkboard  shall  be  erect- 
ed in  a  1/2  inch  bed  of  Portland  cement  mortar, 
mixed  in  the  proportion  of  one  part  of  Portland 
cement  to  tv/o  parts  of  clean,  sharp  sand,  all  vert- 
ical joints  being  broken.  A  second  course  of  three 
inch  Nonpareil  corkboard  shall  then  be  erected 
against  the  first  in  a  1/2  inch  bed  of  Portland 
cement, a.nd  additionally  secured  to  the  first  v:lth 
galvanized  wire  nails  or  V700den  skewers.  All 
joints  in  the  second  course  she.ll  be  broken  v/ith 
respect  to  all  joints -in  the  first  course.  All 
joints  shall  be  made  tight. 


13 

CEILING- 
The  insulation  against  the  ceiling  chc.ll  be 
the  same  as  that  specified  above  for  the  v;.  lis. 

FLOORS 
On  a  reasonably  smooth  and  level  concrete 
ba,se,  one  course  of  tjii'ee  inch  ITonpareil  cork- 
board  shall  be  laid  dovrn  In  hot  aspha,lt,all 
trancverse  joints  being  broken.  2  inch  x  3  inch 
sleepers  sha,ll  be  laid  dovrn  on  38  inch  centers. 
Between  the  sleepers, a  second  courseof  3  inch 
corkboard  shall  be  laid  on  hot  osphalt.  All 
joints  in  the  second  course  shall  be  broken  \rlth 
respect  to  all  joints  in  the  first  course.  All 
joints  shall  be  made  tight.  The  upper  surface 
shall  be  flooded  v/oth  hot  asphalt, approximately 
l/S  inch  thick.  T.&  G-.  flooring  shall  then  be 
securely  nailed  dovm  to  the  sleepers.  Selected 
maple  shall  be  used  for  the  flooring. 

?ARTITI01TS 
The  insulation  on  partitions  shall  be  ei-ect- 
ed  according  to  the  specifics.tions  laid  dovni  foz" 


14 

the  v/alls  except,  that  two  courser,  of  tv.-o-inch 
ITonparell  corhboard  shell  be  placed  on  each  side 
of  the  partition  proper. 

PIPING 

The  ammonia  coils  in  the  direct  expansion 
rooms  and  the  brine  colls  in  the  indirect  expan- 
sion rooms  shall  be  placed  on  each  thirty  foot 
v^all,  close  up  to  ceilin/j;.  Each  coil  shall  be  tv/o 
pipes  v/ide  and  ten  pipes  high, with  four  inches 
between  pipe  centers.  All  pipes  used  shall  be 
Byers '  2-inch  Virrought  iron  pipe. 

The  piping  specified  above  is  sufficient  to 
remove  3'^,'^-^^'^  B.T.U.  per  hour  with  a  ten  degree 
difference  in  temperature  betv/een  the  room  and 
the  brine  or  ammonia.  2.5  v/as  used  as  the  coef- 
ficient of  hect  transmission. 


15 

MCHIiJES 

The  machines  which  viere   chosen  to  cool  the 
experimenta,!  rooms, and  vfhich  are  also  used  for 
ice  making,  represent  the  entire  field  of  large 
scale  coumiercial  refrigeration.  The  compression 
system  is  represented  in  the  Automatic  and  York 
machines; the  absorption  system  is  represented  in 
the  York  absorption  machine.  By  means  of  these 
machines  a  comp;;,rison  of  ammonia  and  carbon  diox- 
ide refrigeration  may  be  obtained.  The  York  v/ill 
be  steam  driven; an  electric  motor  v;ill  drive  the 
carbon  dioxide  machine. 


16 

AUTOI/IATIC  CARBONIC  RSPRICr-^R/iTING  SYCTEM 

The  use  of  carbon  dioxide  as  a  refrigerating 
agent  is  increasing  ver^f  rc^pidl;/,and  the  condi- 
tions under  which  it  is  adrnitedly  superior  arg 
becoming  more  numerous,.  Carbon  dioxide  is  more 
powerful!  than  any  of  the  other  practical  refrig- 
erants. The  saving  in  space  vrtiich  results  from 
this  fact  is  often  of  such  great  importance  that 
it  becomes  the  deciding  factoi-. 

Safety  under  any  3,nd  all  conditions  is  per- 
haps the  most  valuable  characteristic  of  this 
gas; it  Is  non-Gxplosive,non-inflamable,and  non- 
asphyxiating.  It  is  this  property  v/hich  has  led 
to  its  almost  universal  adoption  for  use  in  hos- 
pitals,hotels, and  asylurds . 

■  Because  of  its  very  low  boiling  point, car- 
bon dioxide  has  come  into  great  favor  for  low 
temperature  work.  In  aerona.utical  experimenta.l 
work  and  in  the  manufacture  of  films  temperatures 
of  forty  to  seventy  degrees  belovf  zero  are  obtain- 
ed. 

Taking  these  valuable  features  as  a  basis  the 


17 

Automa.tic  Carbonic  Ilachine  Company  has  designed 
and  manufactured  a  machined  v;hich  hcs  every  favor- 
able point  built  into  it  and  which  applies  the 
natural  advanta.ges  of  this  go-s  in  a  thoi^oughly 
practical  and  simple  way.  A  copy  of  the  specifi- 
cations for  a  three  ton  system  d.s  taken  from  the 
contract  is" given  below. 


18 

COLIPRESSOR 

The  compressor  shall  be  of  the  automatic 
carbonic  safety  type, arranged  with  safety  pockets 
for  the  suction  and  discharge  valves, automatical- 
ly controlled  stuffing  box, pressure  controlling 
device, and  safety  valve. 

The  compressor  sha.ll  be  lubricated  in  the 
folloTang  manner:  A  tvfo  compartment  force  feed 
lubricating  pump  of  the  Kills-Mc  Canraa  type  shall 
be  provided.  One   compartment  of  the  pump  shall 
be  connected  v/ith  the  stuffing  box  of  the  com- 
pressor for  the  lubrication  of  the  same.  The 
otlier  compartment  of  the  pump  shall  be  used  for 
the  lubrication  of  all  bearings  and  moving  parts 
by  meansof  a  speciaJ  oil  distributor  with  a  vis- 
ible oil  supply  going  to  the  distributor  from  the 
lubricating  pump.  Independently-  oiled  valve  leads 
shall  be  connected  from  the  distributor  to  each 
bearing  and  moving  pa.rt. 

The  compressor  suction  and  disch-arge  valves 
shall  be  of  the  nevf  plate  type. 


19 


20 


CONDENSER 

The  condenser  shall  be  of  tlie  shell  type, 
v/lth  copper  cooling  coils,  for  the  circulation  of 
the  water, so  arranged  that  the  carbonic  gas  after 
liquifaction  will  be  cooled  to  the  lowest  temper- 
ature of  the  incoming  water, arranged  in  counter 
current  cycle. 

Each  condenser  shell  shall  be  designed  to 
meet  the  requirements  of  the  rules  issued  by  tlB 
Safety  Inspectors  of  the  Cities  of  Chicago  and 
New  York 


BRIDIE  COOLER 
The  brine  cooler  sha.ll  be  of  the  shell  type 
of  constuction  with  ample  copper  cooling  surface 
to  reduce  the  temperature  of  the  circulating 
brine  to  within  ten  (10)  degrees  of  the  tempera- 
ture of  the  evaporating  carbonic  gas  when  the 
temperature  of  evaporation  is  zero  degreesFahr. 


21 

AUTOriATIG  EXPAITSIOIT  VALVE 
The  valve  conurolllns  the  evaporation  of  the 
carbonic  gc.s  throush  the  brine  coolers  shall  be 
of  the  automatic  pressure  relation  type  requir- 
ing no   hand  adjustment.  This  valve  shall  ';e  pro- 
vided v/ith  two  diaphragms  operated  by  the  liquid 
a.nd  evaporating  pressures  in  such  a  v;ay  that  the 
valve  orifice  is  controlled  in  its  opening  by  the 
action  of  the  tv/o  pressures  on   the  two  diaphragms. 


WATER  FLOY;  CONTROL  VALVE 
The  overflov/  v;joter  from  the  condenser  shall 
be  provided  with  a  thermostatically  controlled 
valve  in  such  a  way  that  the  quantity  of  water 
is  controlled  and  regulated  in  accordance  with 
the  heat  quantity  going  into  the  condenser-. 
That  is,  the  control   v.-.lve  shall  allow,  automatic- 
ally, a  greater  amount  of  water  to  pass  through 
the  condenser  cooling  coils  whenever  the  heat 


22 
flow  into  the  condenser  incre:^ses,and  a  less 
quantity  of  water  with  a  decrease  of  heat  flov; 
into  the  condenser.  This  flow  of  water  shall  be 
cut  off  automatically  when  the  compressor  is 
shut  do  v7n,  and  shall  start  automatically  when  the 
compressor  is  started. 


OIL  SEPERATOR 
There  shall  be  co:anected  in  the  high  press- 
ure line,betY/een  the  compressor  and  the  condens- 
er, an  efficient  oil  separator  so  arranged  that 
the  entering  gas  is  deflected  in  the  direction 
of  its  flov/, reduced  in  velocity  so  that  the  en- 
trained oil  may  easily  be  deposited  on  a  suitable 
perforated  fumiel,the  gas  thereafter  passing  in- 
to the  u^per  pa.rt  of  the  seperator.  Suitable  neans 
to  draw  off  the  oil,v;ithout  ca-using  splashing  ■. . 
shall  be  Provided. 


i^5 
SCALE  TRAP 
A  scale  trap  similar  in  design  to  the  oil 
sepax'ator  shall  be  connected  at  a  suits.ble  lo- 
cation in  the  suction  pipe  leading  from  the  e- 
vaporators  to  the  compressor. 


24 
YOmi   ABSORPTION  REFRIGERATING  SYSTEM 

Absorption  machiiieG  viere   first  built  to  meet 
the  increased  demand  for  lov/  temperature  v/ork.In 
many  cases  these  machines  can  be  installed  and 
operated  more  economicaAly  than  any  other  type. 
This  method  of  refrigerivtion  is  especially  desir~ 
c.ble  for  the  temperatures  required  by  oil  refin- 
eries, fish  freezers, and  cold  storage  plc.nts. 

There  are  man;*"  cases  in  which  greatly  in- 
creased economy  has  been  obtained  in  existing 
compression  plants  by  using  the  exlicust  steam 
from  the  compression  plant  ;-uxiliaries  in  the 
ammonia  generator  of  an   absorption  machine.  It 
is  often  desirable  to  install  this  type  of  mach-  , 
Ine  in  hotels, apartment  housevS, hospitals,  or  elec-- 
trie  poY/er  plants, where  exhaust  steam  is  availa- 
ble. A  pressure  of  one  pound  gauge  is  sufficient 
for  satisfs.ctory  opera-tion. 

The  Yorlc  ".lanufac taring  Company  is  the  lead- 
ing m.aker  of  absorption  machines-  The  system  to  be 
installed  in  the  nevf  laboratory  will  be  designed 
by  them  to  raeet  the  following  specifications: 


25 
GENERATOR 

The  generator  shall  be  of  the  shell  and 
tube  type  and  shall  be  raade  of  cast  air  furnace 
iron  having  a  tensile  strength  of  not  less  than 
55,000  to  60,3";0  pounds  per  sq.uare  inch. 

No  rivets  shall  be  used  in  any  part  of  the 
shell;  all  seams  shall  be  welded,  thus  avoidin<j; 
leakage  due'  to  contract  lor.  and  expan3ion. 

The  shell  sh-:.ll  be  designed  for  use  with 
an  external  analyzer 


ANALYZER   . 
The  analyzer  shall  be  of  the  extenal  type. 
It  shall  consist  of  a  cast  air  furnace  iron  shell 
providedvrith  cast  iron  heat  exchanger  trays,  over 
which  the  incoming  strong  aqua  flov/s, counter  cur- 
rent to  the  outgoing  gas,  coming  in  direct  conta.ct 
with  the  same. 


26 


LTcat-^SMittais'iWTiagiwertKgTO.vwOTWf^MW^;  gg'gr^Tnjsigc^BEaaBffiigsHEiavgaafflaBgc'agJgga^^^ 


OOC//3LE 


AB^t?/?^T/0/\/        A^/ICH/NE 


27 

DSHYDR/iTOR 

The  dehydrc.tor  shall  be  of  the  double  pipe 
type,8.nd  provided  \ilth   all  the  necessary  fittings, 
valves, headers,  sta.nds,  and  a  drip  tray.  The  pipin^^ 
shall  be  of  selected  1  l/2"  and  3"  aramonia  pipe. 
All  parts  shall  be  made  of  cast  close  grained  air 
furno.ce  iron. 

The  combined  gas  and  water  vapor  shall  enter 
the  annular  spc.ce  of  the  coil  a,t  the  top,  and  leave 
it  at  the  botton, -vhere  it  shall  enter  the  drip 
trap, which  will  effectually  separate  the  condens- 
ed water  from  the  ammonia  g;-.,s  and  return  it  to 
the  generator, vhile  the  anliydrous  t.mmonia  passes 
on  to  the  ammonia  condenser.  The  cooling  water 
shall  be  circulated  counter  current  to  the  ammon- 
ia, entering  the  inner  c^il  of  the  pipe  at  the  bot- 
tom and  lea.ving  it  a,t  the  top. 


GOITDENSER  ^^ 

The  condenser  snail  be  of  the  double  pipe 
type, made  of  selected  1  l/4"  and  2"  ammonia  pipe, 
and  provided  with  all  the  necessary  stands, head- 
ers, valves,  and  fittings. 

The  gas  shall  enter  the  annular  spe.ce  at  the 
top, the  liquid  leaving  at  the  bottom, while  the 
cooling  waiter  enters  the  injier  pipe  at  the  bottom 
and  passes  through  ':he  coil  counter  current  to 
the  ammonia. 


EXCHANGER 
The  exchanger  shall  be  of  the  double  pipe 
type, made  of  selected  1  1/4"  and  2"  ammonia  pipe. 
It  shall  be  so  a.rranged  that  the  strong  and  v/eak 
liquor  shall  flow  counter  current  and  at  high 
velocity  so  that  a  good  hea.t  transmission  shall 
be  obtained.  The  strong  aqua  ammonit.  entering  the 
generator  shall  have  a  temperature  not  more  than 


29 
eight  degrees  below  the  temperature  in  the  gen- 
erator. 


WEAK   AQUA  COOLER 
The  \7eak  aqua  cjolei'  shall  be  of  the  double 
pipe  t^'pe  made  of  selected  1  1/4"  .and  2"  ammonia 
pipe.  The  v/eak  aqua  ammonia  shall  flovf  counter 
current  to  the  cooling  v/ater  and  its  temperature 
on  leaving  shall  not  be  more  than  five  degrees 
highei'  than  the  tempera.ture  of  the  cooling  water, 


ABSORBER 
The  absorber  shall  be  of  the  double  pipe 
type  of  2"  and  3"  selected  amraonia  pipe, complete 
with  stands, valves, headers, special  gas  and  weak 


30 
aqua  anmonla  injection  fitting/, and  purging  drum. 
The  cooling  v/ater  shall  flov/  through  the  inner 
pipe  counter  current  to  the  weak  aqua  ammonia 
and  the  amiuonla  gas. 


31 

YORK  COMPRESS  lOI-I  RITFRIC-ERATING  IIACHIl^IE 

The  ainrnonia  compression  refrlf^erating  syst- 
em Is  at  present  hj  far  the  moct  prevalent  meth- 
od of'  refrigeration.  The  machine  v/hich  vill  rep- 
resent this  field  is  now  located  in  the  present 
refrigeration  lahoi-jitory  of  the  AD^mour  Institute 
of  Technology.  It  is  complete  and  is  in  rtood  op- 
f.ra.ting  condition.  It  ha,s  been  used  for  experim- 
ental purposes  since  1911  vrith  very  satisfactory 
results. 

The  compressor  is  of  the  single  cylinder, 
single  acting, vertical  type.  It  is  driven  by  a 
horizontal, slide  valve  direct  coupled, ctem  en- 
gine. It  is  fitted  with  a  safety  head.  The  main 
shaft  is  of  forged  and  ha.mmered  steel.  The  con- 
necting rods  are  cast  steel  made  in  an  I-beam 
section.  The  piston  ia  fitted  with  metallic  pack- 
ing and  the  piston  rod  is  fitted  v/ith  soft  pack- 
ing. All  v/earing  and  bearing  surfaces  are  fitted 
with  automatic  oilers. 

The  ammonia  condenser  and  the  brine  cooler 
are  of  the  double  pipe  type  and  are  incased  in 
granulated  cork  to  reduce  the  radiation  losses. 


32 


it    /?    A'Ai    <Syts^ 


1-  /z-o 


.'•rwrmjniimMi^siniSC^iaTtV^iiVjaiSlStVVii^^ 


3  TOAT     yO/SK       COMfRE-SS/O/^      /^y^CH//V£ 


33 

Oil  which  is  candied  over  from  the  compres- 
sor is  removed  by  the  oil  separator  located  in 
the  high  pressure  line. 

The  v; eight  of  aniLionia.  used  during  any  run 
can  be  determined  hy   mea.ns  of  two  liquid  receiv- 
ers which  rest  on  platform  scales. 

An  exchanger  has  been  provided  so  that  the 
system  may  be  run  dry,V'fet,or  superheated. 

This  system  will  be  removed  to  the  new  lab- 
ora.tory  and  set  up  there  with  but  a  ver.y  fev/ 
changes  in  minor  details.  The  only  addition  to 
the  system  will  be  the  piping  to  the  rooms. 


34 

ICE  ■HAILING 

The  production  of  artificial  ice  has  increased 
to  such  an  extent  that,althour;^h  the  yearly  ice 
crop  produces  fluctuations  in  the  price  of  ice, 
the  public  is  no  longer  dependent  upon  the  wint- 
er v^eather  for  its  ice  supply.  In  spite  of  the 
hlQa   cost  of  material, labor, and  fuel, there  is  a 
gradual  decrease  in  the  expense  Involved  in  the 
production  of  a  ton  of  ice. 

Tlie  ice  tanlc  nov;  installed  in  the  present 
refrigeration  la,boratory  y^III  be  moved,  v/lth  its 
appurtenances, to  the  new  laboratory  and,  connected 
to  the  three  three-tai  refrigerating  machines. 
This  tank  is  six  by  fifteen  feet  and  has  a  cap- 
acity of  one  and  one  half  tons  of  ice.  It  contains 
thirty-six  one  hundred  pound  cans.  The  only  add- 
ition to  the  freezing  tank  will  be  the  air  head- 
ers for  the  raw  water  system. The  insulation  v'ill 
be  the  same  as  how  surrounds  the  tank. 


35 

WATER  SUPPLY 

With  the  development  of  the  Internal  com- 
bustion engine  e/ad   the  possibility  of  getting 
electrical  pov/ei'  at  a  sufficiently  low  rate  to 
justify  its  use  in  the  operation  of  ice  plants, 
there  has  come  a  remarkably  o^uick  change  from 
the  distilled  water  ice  plant  to  the  raw  waiter 
ice  plant. 

When  steam  v/sx  the  most  economical  and  sat- 
isfactiry  method  of  driving  compressors, the  ex- 
haust steam  from  the  driving  engine  vies   condens- 
ed, filtered,  and  reboiled.  From  the  reboiler  the 
steam  was  run  through  another  condenser  into  a 
holding  te.nk.  The  ice  can  filler  was  connected 
to  this  tank. 

In  the  new  laboratory, the  driving  unit  of 
the  York  compressor  will  furnish  the  stei.m  for 
the  distilled  water  method  of  making  ice.  All 
the  apparatus  necessary  for  the  operation  of  such 
a  system  is  installed  in  the  old  laboratory. 

The  rapidly  increasing  demand  for  raw  water 
plants  makes  it  inpera-tive  that  the  nev;   labora- 


"SVCl 


* 

-^ 

■    ']■      - 

1 

1 

1 

1 

I 

\ 

P/Pffs/G       L/iYOUT 


PfSTILLED      \A//ITEf?      »      BRINE 


37 

tory  contain  apparatus  necessary  for  the  nicinufac- 
ture  of  ice  from  raw  v/ater.  Because  of  its  sim- 
plicity and  economy  of  operation, the  York  high 
pressure  air  system  has  been  chosen  to  prevent 
the  formation  of  y/hite  or  snov/  ice. 

The  air  is  drawn  into  the  electrically 
driven  compressor  from  a  header  extending  above 
the  roof.  It  is  brought  up  to  the  necessary  press- 
ure, virhich  depends  upon  the  temperature  of  the 
brine, is  discharged  into  the  receiver, and  passes 
through  the  vrater  cooled  dehumidifier,  to  the  brine 
cooled  dehumidifier. 

This  dehumidifier  is  of  the  shell  and  tube 
type.  The  brine  is  circulated  through  the  coils, 
and  the  air  passes  around  them.  In  cooling  the 
air  the  moisture  is  frozen  off.  The  brine  cooler 
is  in  duplicate  so  that  the  frost  on  one  set  of 
colls  can  be  ths.wed  off  v;hile  the  other  is  doing 
the  final  work  of  cooling.  This  is  done  by  allov/- 
ing  the  air  from  the  water  section  to  pass  up 
through  one  chamber  and  dovm  through  the  other. 
The  brine  is  not  circulated  through  the  first 
chamber  and  the  air, being  warmer  than  the  frost 


38 


Socr/oi>/    %Sr^^/f^£fZ 


^E.Poc//\t&   l/w-t^^ 


LP.  G/iO&e. 


H.H  G^u&e. 


Aii^  CcMPfe^-^^o^ 


■^  \h<^y  Vy^i-\ 


W//e  /?/?y/A/G    y^ppy^/e/lTC/^   nD/?    /^/ikv    h/^T£:/^    Sy^t^m. 


39 
or  Ice  on  the  coils, melts  it  as  it  passes  up 
through  the  chamber;  then  it  cr3£Sf;s  over  into 
the  other  shell  and  comes  into  contact  v;ith  the 
coils  through  which  the  brine  is  being  circulated, 
It  is  thus  cooled  to  the  temperature  required  to 
dry  it  sufficiently  for  use  in  the  ice  can.  llhen 
the  temperature  of  the  air  leaving  the  second 
chamber  begins  to  rise, the  four-way  cock  is  throwr 
over,and  the  direction  of  flow  is  reversed.  The 
brine  is  made  to  flow  through  the  other  coil;..  A 
reversal  is  necessary  about  twice  a  day. 

An  electrically  driven  centrifu^^al  pump  is 
provided  to  circulate  the  brine. 

The  apparatus  to  be  Installed  will  be  large 
enough  to  use  in  connection  v/ith  experiments  in- 
volving air  conditioning. 


lilACHINES 
A  complete  description  of  the  machines  used 
for  ice  making  is  given  In  the  secti.>n  devoted 
to  the  experimental  roo:ns.  Any  one  of  the  three 
raa-chines  may  be  used  for  makin,--^,  ice. 


40 

SIiTALL  REFRIGERATION  I.IACHINES 

The  ton:ia{~e  of  reirlgere.tion  produced  "by 
snail  refrigeration  machines  will  perhaps  never 
equal  that  of  the  large  machines, but  the  number 
of  men  required  to  make  and  sell  them  and  to 
supply  the  necessary  service, will  soon  undoubted- 
ly, be  far  greater.  The  long  felt  need  for  depend- 
able, efficient  refrisercttlon,by  the  merchant  who 
does  not  conduct  an  exten.slve  business, has  been 
fulfilled  in  the  machines  now  built  for  his  needs. 

Uncertainty  of  both  prices  and  deliveries  - 
poor,  inefficient  refrigeration,  and  conseajaently 
spoiled  products  -  constitute  a  fev:  of  the  many 
losses  sustained  through  being  everlastingly  with- 
in the  power  of  the  ice  man;  all  of  them  work  to 
the  menace  of  those  dispensing  perishable  goods. 

The  thousands  of  merchants  who  today  are  pro- 
fiting and  benefiting  in  many  ways  through  the  a- 
gency  of  nechanical  refrigeratijn  would  not  re- 
turn to  the  use  of  ice  for  refrigeration  any  more 
than  they  viould  re- employ  the  ancient  lethods  of 
keeping  charge  accou  its  on  a  spindle, or  weighing 


41 

their  products  ^by  the  sense  of  touch. 

The  equipment  of  the  new  laboratory  will  in- 
clude three  rnachinec  suitable  for  groceries  or 
mcrkets  and  one  refrigerator  designed  for  house- 
hold use.  A  detailed  description  of  each  of  these 
machines  with  its  advantages  and  tie  field  it  cov- 
ers is  given  belov/.  Together  they  cover  this  branch 
of  foechanical  refrigeration  very  thoroughly. 


42 


CREAMERY  PACKAGE  RT^FRlGSRATINrT  SYSTSi 
TYPE  G 

The  Creamery  Package  Manufacturing  Company 
was  one  of  the  first  to  engage  in  the  manufacture  . 
of  refrigerating  machines.  Their  staff  of  service 
and  installation  engineers  are  the  peer, in  length 
of  experience  and  ski'i.ljOf  any  similar  organiza- 
tion in  the  country.  In  general  design  the  machines 
are  small  and  compact  and  take  very  little  room 
for  the  tonnage  developed.  They  are  ideal  for  belt- 
ing direct  to  electric  motors.  The  Type  C  repre- 
sents the  best  in  tv/in  cylinder  vertical  design 
for  this  caoacity.  The  wide  popularity  of  these 
refrigerating  systems  is  excellent  testimony  to 
the  efficiency  of  this  method.  TAiile  each  unit 
has  its  own  distinctive  features, the  ammonia  com- 
pressor is  of course  the  most  important. 

CP  vertical  ammonia  compressors, "master-built 
are  of  the  single  acting, enclosed, self-oiling  type. 
They  are  built  of  semi-steel  and  are  designed  f  )r 
long  and  constant  use.  The  bearings  are  exceeding- 
ly large  and  are  readily  renev/ed.  A  specially  de- 


'45 


CREAITTIRY  PACICAG-E   COMPRESSOR 


44 

signed  fly-v/heel, halving  the  spokes  at  the  side  of 
th.e  rlrn, brings  the  center  of  tlie  weight  over  the 
bearing, v/hlch  Is  the  stuffing  box  gland.  This 
gland  has  a  bracket  support  from  the  base  of  the 
machine  thus  avoiding  the  use  of  an  outboard,  bear- 
ing on   the  compressor  shr.ft  beyond  the  fly-Y/heel. 
The  crank  shaft  has  tv/o  bearings.  All  bases  are 
cast  with  a  sediment  pocket  at  the  bottom  to  keep 
the  oil  ;:  s  clean  as  posfjible. 

These  compressors  are  provide!  vrith  a  scale 
trap  on  the  suction  line, and  also  have  a  gas  trap 
in  tjie  suction  line  In  the  cylinder, providing  a 
large  supply  of  gas  to  drav/  on  v/hen  the  cylinder 
is  being  refilled  on  the  suction  stroke.  All  mach- 
ines are  provided  v;ith  by-passes  for  reversing  the 
operation  and.  pu.mping  out  all  pi',rts  of  the  systen 
for  repairs.  These  machines  are  provided  v/ith  saf- 
ety devices  Avhich  viill  prevent  liowlng  gaskets  in 
case  the  com'iressor  is  started  up  v/ithout  opening 
the  discharge  valve.  Suction  gas  pockets  are  con- 
nected to  the  base  of  the  machine  so  that  any  oil 
coming  back  to  the  machine  is  e-utomatically  trap- 


45 


CREAI.iERY  PACKAGE  REFRIGERATING  I.'IACHINE 


Sice  \^i£rv\< 


CREAMERY  PACKAGE  REFRIGEI^TILTC-  imCHiWE 


46 
"ped  in  the  base  of  the  compressor. 

The  C?  verticc.l  compressor  is  deslsned  viith 
a  double  trunk  piston,  the  bottom  pi.rt  serving  as 
a  cross-head  aiid  the  upper  part  servinrr  as  the 
piston  proper.  Both  are  provided  v/ith  rings  and 
equinpei  vjith  mutiple  poopet  valves.  The  valve 
lift  is  quick  and  the  opening  is  large-  The  valves 
are  made  of  tool  steel. 

This  compressor  h:.s  no  clearance  at  high 
speeds.  Its  cylinders  have  safety  heads  which  are 
perfectly  flat  on  the  bottom  and  its  pistons  are 
perfectly  flat  on  top.  The  piston  of  this  compress- 
or can  be  adjusted  for  clearance  by  shimming  up 
the  crank  pin  boxes-  Hence  at  every  revolution  all 
the  gas  which  has  been  drav/n  into  the  cylinder  is 
compressed  and  completely  discharged.  Because  of 
this  non-clearance  feature  the  GP  compressor  oper- 
ates at  the  same  high  efficiency  at  low  tempera- 
tures -s  it  does  Y/hen  operating  at  high  tempera- 
tures . 


47 

C01'ITII\TEMTAL  REFRIGERATING-  SYSTEI;! 

Continental  machinery  is  designed  and  man- 
ufactured v.'ith  the  one  idea, that  dependable  and 
satisfactory  service  is  remembered  long  aftei" 
price  is  forgotten.  For  durability  and  econofiiy 
their  line  of  refrigerating  machinery  is  excelled 
by  none.  The  continental  self-contained  refriger- 
ating unit  combines  the  entire  high  side  in  one 
machine. 

The  continental  is  a  cerni- enclosed  machine. 
In  operating  it  there  is  no  ammonia  in  the  crank 
case  to  nix  with  the  lubricating  oil.  -he  ammonia 
Is  taken  directly  into  the  cylinders  througii  the 
pipe  manifold.  Therefore  there  is  no  possibility 
of  pumping  lubricating  oil  from  the  crank  case 
over  into  the  cooling  coils-  Flooding  of  the  cool- 
ing coils  with  oil  a,nd  thereby  cutting  their  re- 
frigerating effect  is  impossible. 

Any  part  of  the  continental  may  be  inspected 
by  simply  closing  the  suction  and  discharge  stop 
valves  on  the  manifolds, and  removing  the  crank 


48 


CONTIIIENTAL  REFRIGERATING   SYSTEM 


49 
case  door,  the  plates  of  the  cylinder  nec':s,and  the 
cylinder  heiA. 

The  continental  1b  built  with. a  crocs  head 
similar  to  that  of  a  steam  enj^ine.  This  causes  a 
straight  vertical  movement  of  the  piston  which 
prevents  side  thrust  on  the  cylinder  vralls. 

The  stuffing  box  betv?een  the  cylinder  and 
the  crank  ca.se  prevents  the  ammonia  from  entering 
the  craiilr  case.  This  stuffing  box  is  of  special 
design  and  is  pa.cked  v/ith  3.   combination  of  fric- 
tionless  packing, one  side  of  which  is  in  contact 
v;ith  the  piston  rod,  and  a  diagona^lly  shaped  flex- 
ible packing  which  contracts  and  expands  accord- 
ing to  the  pressure  exerted  upon  it. 

One  of  the  best  features  of  the  continental 
is  the  adjustment  for  clearance.  This  is  accomp- 
lished bymeans  of  a  lock  nut  and  threaded  piston 
rod. 

The  shaft  is  made  of  a  solid  steel  forging, 
very  liberally  proportioned, giving  ample  strength 
and  assuring  continuous  service. 

The  continenta.l  is  equipped  v/ith  feather 
weight  suction  and  discharge  valves.  All  valves 


50 

and  their  seats  are  easily  removable  for  grindin^j. 

Safety  heads  are  provided  to  prevent  the  possibil- 
ity of  an  accident  in  case  of  a  charge  of  liquid 
being  C8.rried  over  into  the  cylinder. 

The  lubrication  is  automatic.  The  crank  case 
oil  lubricates  the  main  bee^rin^s,  the  connecting 
rod  bearings, and  the  cross-head.  The  oil  from  the 
mechanical  lubricator  is  pumped  directly  into  the 
space  in  the  stuffing  box  which  is  occupied  by 
the  spring.  Ammonia  in  the  cylinder  acts  as  a  par- 
tial lubricant  and  the  piston  rod,v;orking  in  a 
bath  of  oil  carries  sufficient  oil  to  the  cylin- 
der to  effect  perfect  lubrication  there. 

The  condenser  used  in  these  units  is  of  spec- 
ial compact  design  in  which  the  condenser  and  the 
liquid  receiver  are  combined.  The  co^nbina-tion  is 
located  in  the  base  and  is  easily  accessible 
through  large  liand  holes. 


51 

LI?:.IA^!  REFRICtERATING  r.IACHINE 

The  Lipman  Line  has  met  with  great  favor 
among  small  merchants  throughout  the  country  be- 
Cc'.use  of  its  compactness,  smooth  running, and  econ- 
omj^.  The  Lipraan  machine  is  full -automatic  and 
many  of  the  company's  sales  have  been  replacements 
of  much  larger  hand  operated  machines.  There  is 
no  longer  any  doubt  but  that  the  auto  matic  mach- 
ine is  the  most  satisfactory  solution  of  the 
small  merchant's  problems. 

The  Model  T^'^O  v;as  chosen  from  the  Lipman  Line 
as  a  typical  small-store  automatic  machine.  This 
machine  has  a  capacity  of  lOOOpounds  of  refriger- 
ation per  day.  The  s-ntire  high  side  is  erected 
on  a  rigiil  attra-ctive  stand.  All  pai-^ts  are  easi- 
ly accessible.  The  control  sv/itches  are  operated 
by  an  electrical  contact  exp^-nsion  thermostat. 

The  compressor  is  vertical, single  cylinder, 
and  single  acting.  It  is  an  enclosed  type.  It  is 
belt  driven  by  an  electric  motor.  The  belt  tens- 
ion is  kept  constant  by  a  counter  weight. 

An   efficient  oil  separator  is  provided  in 


52 


LIPLIAN  REFRIGERATING-  MACHINE 


the  high  pressure  2^s  line. 

The  condenser  is  of  the  shell  and  coil  type; 
the  cooling  water  runs  through  the  coll  and  the 
ammonia  flows  through  the  shell  counter  current 
to  the  coolinf^,  w?.ter. 


54 
THE  ICELESS  REFRIGERATOR 

Housekeeping  TiethodG  have  been  completely  re- 
volutionized in  the  past  tvio  decades.  Llodern  in- 
vention has  turned  the  labor  of  the  housekeeper 
into  a  real  pleasure,  -he  electric  stove  starts 
and  stops  its  cooking  ;7ith  a  turn  of  a  sv/it3h, 
the  vacuum  cle.,ner  keeps  the  house  spick  and  span 
and  the  electric  washer  takes  the  drudgery  out  of 
"blue  "londay".  And  nov^  we  have  the  iceless  refrig- 
erator. 

The  iceless  refrigerator  is  ecsentia-ly  a 
machine  for  keeping  food  dry  and  at  a  constant 
temperature  of  thirty-eight  to  forty- four  degrees 
Fahrenlieit.  It  is  a  scientific  fact  beyond  argu- 
ment that  food  spoils  rapidly  due  to  gera  grovfth 
at  temperatures  of  fifty  degrees  or  more.  To  prop- 
erly preserve  food  so  that  bacteria  cannot  flour- 
ish, the  temperature  must  be  kept  beloy?  forty-five 
degrees.  The  ordinary  ice  box  is  an  inefficient 
and  unsatisfactory  food  preserver  because  the  tem- 
perature is  always  too  high  and  because  it  for- 
ever varies  with  the  varying  quantity  of  ice  and 


the  flucbuo.tion  of  outbade  tern  ^er'atures  •  The  In- 
side temperature  cannot  be  c.ntrolled. 

A  Frigidaire  v/as  selected  as  the  laboratory's 
household  Tiachiae.  The  Frigidairs  Corporation  is 
a  division  of  -the  G-eneral  Motors  Corporation.  No 
Seles  are  made  outside  of  the  territory  covered 
by  Frigidaire  service.  The  principle  data  concern- 
ing this  refrigeratoi''  is  given  below. 


5''  ■ 
FRIGIDAIRE   • 
Model   B-9 

Total  V/eiG^T-t  -  855  lbs-  ' 

Total  Outside  Volu:::e   -   37.5cu.  ft. 

Total  Inside  Food  Gapacit^^  -   9  cu.  ft. 

Exterior  Dimensions   -  25"  x  39"  x  67". 

Interior  Dimensions 

Large  Food  Compartment   -  ■  38  1l/l6  x  14  5/8 

X  18  1/2,  inches. 
Small  Food  Compartment   -   15  1/8  x  16  1/2 
X  18  1/2  inclies- 

Total  Refrigerating  Capacity  -  700  B.T.U./hr. 

Type  of  Condenser  -  Water  Coil. 

Refrigerating  Chamber  -  A  jacketed  expansion 

unit  or  boiler  filled  vath  brine  made  up  of 
calcium  chloi'ide  and  w-ter-  This  brine  tanlc 
vreighs  about  one  hundred  pounds  when  charged. 

Brine  Tanl^  Temperature   -  Average  20  degrees  F. 
It  is  controlled  by  a  methyl  chloride  fill- 
ed gas  thermostat  which  stops  the  compressor 
at  16  degrees  •:  nd  starts  it  at  24  degrees. 
This  control  is  located  in  the  brine  tank. 


57 


Model  "B.9' 


1 .  Ice  Drawers 

2 .  Temperature  Damper 

3.  S;-nltary  Lining 

4.  ?/ater  Control 


5«  Shelves 

6.  Storage  Space 

7 .  Rubber  Seals 

8.  Starting  Control 


58 

Ice  Making  -   Thi-ee  trays  of  ''hree  pounds  cap- 
acity are  recessed  into  the  brine  tank. The 
maximum  time  of  freezing  is  eight  hours; 
the  cost  is  about  one   ce.it  for  tv;enty  four 
cubes . 

Compressor  -   T\70  cylinder, piston  type, driven 

through  four  to  one  gear  reduction  by  a  1/4 
horae  power  motor. 

Pood  Compartment  Temperature   -   33  to  44  degrees. 

Pood  Compartment  Control   -   Thermostatic  damper, 
controlling  circulation  of  air. 

Percent  Operating  Time   -   20  to  25,^ 

Normal  I.Iotor  Load   -   250  v/atts. 

Cost  of  Electricity   -  About  6</.   a  day  @  4^  per 
Kilowatt  hour. 

Quantity  of  Water  Usod  -  About  20  cu.ft.  per  day. 

Cost  of  Water   -  'i)4.38  per  year  3  60^2''  per  1,000 
cu,  ft. 


^9 


M£CH.    £/VG.    0£PT 


^K