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Encyclopaedia Britannica, 11th Edition, Volume 8, Slice 3 "Destructors" to "Diameter" By: Various |
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THE ENCYCLOPÆDIA BRITANNICA A DICTIONARY OF ARTS, SCIENCES, LITERATURE AND GENERAL INFORMATION ELEVENTH EDITION VOLUME VIII slice III Destructor to Diameter
DESTRUCTOR ( continued from volume 8, slice 2, page 0108. )
... in main flues, &c. (g) The chimney draught must be assisted with
forced draught from fans or steam jet to a pressure of 1½ in. to 2 in.
under grates by water gauge. (h) Where a destructor is required to
work without risk of nuisance to the neighbouring inhabitants, its
efficiency as a refuse destructor plant must be primarily kept in view
in designing the works, steam raising being regarded as a secondary
consideration. Boilers should not be placed immediately over a furnace
so as to present a large cooling surface, whereby the temperature of
the gases is reduced before the organic matter has been thoroughly
burned. (i) Where steam power and a high fuel efficiency are desired a
large percentage of CO {2} should be sought in the furnaces with as
little excess of air as possible, and the flue gases should be
utilized in heating the air supply to the grates, and the feed water
to the boilers. (j) Ample boiler capacity and hot water storage
feed tanks should be included in the design where steam power is
required. [Sidenote: Cost.] As to the initial cost of the erection of refuse destructors, few
trustworthy data can be given. The outlay necessarily depends, amongst
other things, upon the difficulty of preparing the site, upon the
nature of the foundations required, the height of the chimney shaft,
the length of the inclined or approach roadway, and the varying prices
of labour and materials in different localities. As an example may be
mentioned the case of Bristol, where, in 1892, the total cost of
constructing a 16 cell Fryer destructor was £11,418, of which £2909
was expended on foundations, and £1689 on the chimney shaft; the cost
of the destructor proper, buildings and approach road was therefore
£6820, or about £426 per cell. The cost per ton of burning refuse in
destructors depends mainly upon (a) The price of labour in the
locality, and the number of "shifts" or changes of workmen per day;
(b) the type of furnace adopted; (c) the nature of the material to be
consumed; (d) the interest on and repayment of capital outlay. The
cost of burning ton for ton consumed, in high temperature furnaces,
including labour and repairs, is not greater than in slow combustion
destructors. The average cost of burning refuse at twenty four
different towns throughout England, exclusive of interest on the cost
of the works, is 1s. 1½d. per ton burned; the minimum cost is 6d. per
ton at Bradford, and the maximum cost 2s. 10d. per ton at Battersea.
At Shoreditch the cost per ton for the year ending on the 25th of
March 1899, including labour, supervision, stores, repairs, &c. (but
exclusive of interest on cost of works), was 2s. 6.9d. The quantity of
refuse burned per cell per day of 24 hours varies from about 4 tons up
to 20 tons. The ordinary low temperature destructor, with 25 sq. ft.
grate area, burns about 20 lb. of refuse per square foot of grate
area per hour, or between 5 and 6 tons per cell per 24 hours. The
Meldrum destructor furnaces at Rochdale burn as much as 66 lb. per
square foot of grate area per hour, and the Beaman and Deas destructor
at Llandudno 71.7 lb. per square foot per hour. The amount, however,
always depends materially on the care observed in stoking, the nature
of the material, the frequency of removal of clinker, and on the
question whether the whole of the refuse passed into the furnace is
thoroughly cremated... Continue reading book >>
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