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PLACE IN RETURN BOX to remove this checkout from your record.
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MDESIGIOPASPWOMED

”R m EAST LANSING SEWAGE TREATWT PLANT

A than Submitted to

m Faulty of
HIOHIGAH STATE GOLLEGE
Of
mzmm AND APPLIED SCIENCE

' .I
Z"

r} 1.

Arthur 1;." men

Oandidnto for the Dome of
Buholor of Satan“

Juno, 1930

THEbIS

103800

GONTENTS

Mm:
mmuh

mtor Bod: 1n com-1
Monsignor:
003011131011
Mutton!
Bibliography

Drums:

AOHOWW

I um to emu: my gratitude to P. R. Thu-m for
tho “no." um” and guidance he has 01150114“ to no
concerning thin problu.

Arthur L. smith.

1.

MODUGTIOI

m city of East Lmeing, niehigen he: a eenge treet-
lent plant, located west of Hmieon Road near the south
hunt er the Red Cedar River. The plant eeneiete or e.
ming etntion, Imhoff tanks, and sludge b'odl'.

It in deeired to present the design of euitebie
addition-1 treetment works to eeeemodnte the effluent
true the recent plant. The addition-t1 work. ere to
emiet of tvin doling ten}: feeding to Ieperete nouled
Cpl-inkling filter beds and e secondary eettling tank.

The final effluent ie to be discharged into the Red
cedar River.

FIL'PI‘IR III-IDS m GTEKIRAL

A twinkling filter bed my be deeoribed on being on
Mirioiel bed of broken atone on eleg, retained within
nlle and e ernooth vetorticmt mm. The floor ie
thoroughly drained. The treated sewage in ope-eyed intern
nittently but uniformly one possible over the entire eurfeoe
of the bed.

in the treated sewage ie applied to the bed en weenie
film pedmlly forms on the filter media where bacteria
thrive. The enepended matter in the eenge'olinge to the
erg-n10 Getting: and lo turned into more, etable cub-tame:
by the beeterie. '

Ihie type of filter bed undergo" periodioel unload-
ing of the organic material in the bed. Due to thie, it
in neeeeeary to give the bed effluent e eeoondery eettling
to clerify and remove the oottloeble eolide.

The eolide from the bed effluent may be retm'ned to
the preliminary treetz-uent tank for digeetiom. The liquid
m be turned into e nearby stream or body of voter.

Thi- treatment with preliminary end finel eedimente-
tion hoe been able to produce on effluent not subject to
putrefootion, lee in booteriel ommt end well Clarified
in eppeoreme. Effluente have been poodueed Ming over
90,! reduction of bacteria and 80 to 8575 reduction of the
bioohomieel oxygen demand of rev emce.

5.

Sprinkling filter: efford e comparatively oheep
nethed of producing e eteble effluent. They ere inexpen-
eive to operate and eeldom give trouble. The bode being
eeeembled of concrete, atone, tile, end cast iron eneuree

the bed ee being permanent and free from exoeeeive min-
tenenee.

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4.

MMATIOI

Before attempting any design it is necessary to
knot the conditions that have to be met and dealt with.

To design a treatment plant to serve the present Inhoff
tank effluent it is necessary to know the amount of
sewage the tank is capable of treating.

I computed the tank capacity using nominal design
units of two hours detention period, tvo cubic feet of
sludge storage per capita, effective channel length, and
one hundred gallons of sewage per capita per tventy-four
hours. I found the tank to be capable of serving ten
thoneand people vithout overloading.

As a hirthcr check I have taken results of a twenty-
fourhaur gaging of the East Lansing sever. This is
compiled in ”10 “0ng curve. Computations from
this curve show the tank to be treating slightly under
one million gallons of sewage per twenty-four hours.

The final effluent is to be discharged into the
Red Cedar River. It is desirable to try to keep the
bottom of the filter bed above the high stages of river
flow and to avoid additional pumping. However, there is no
.particulnr‘harm in allowing the river to :11]. the lever
_ section of the bed for brief and occasional periods vhen
the river is at an unusually high “38°-

! referred to Volume XXVI of the Daily Stages of
Principal Rivers of the United States for data concerning

5. 1

the Red Cedar River. I obtained the following:
Flood stage of the river .. elev. 829.80

31811003 ' ' ' ' ' 835 .70
Bank Full” " " " " 827 .80
WCt ' ' ' I! ' 822.40

The flood stage of the river is reached during the
spring months and periods of excessive rainfall. com-
paring these elevations with the elevation of the
Inhoff tank effluent which is 839.50, it is readily
' seen that to avoid pumping a low head filter plant
must be built. ,

Sewage treatment plants are desigied to allow for
future expansion and plant enlargement to aeoousaodate
the future populace. The present tank is located in
the northern side of the tract of land obtained for a
savage treatment plant. Sufficient room has been
allowed to place a similar Inhoff tank south of the
present tank. I believe it advisable to place the
additional treatment works in the northwestern part of
the land available and quite close to the river. This
vill allow for future enlargement on the present property.
it would be possible to provide for a complete dual system
of treatment.

6.

- GONCLUS IOU

I wish to submit the complete construction cost of
the filter bed which is the major expense envolved. l’
have estimated the cost to be $105,393.45.

  
 
   
   
  
  
 
    
  
   

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