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DESTRUCTORS

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Originally appearing in Volume V08, Page 110 of the 1911 Encyclopedia Britannica.
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DESTRUCTORS . The name destructors is applied by See also:

English municipal See also:engineers to furnaces, or combinations of furnaces, commonly called " garbage furnaces " in the See also:United States, constructed for the purpose of disposing by burning of See also:town refuse, which is a heterogeneous See also:mass of material, including, besides See also:general See also:household and ash-See also:bin refuse, small quantities of See also:garden refuse, See also:trade refuse, See also:market refuse and often See also:street sweepings. The See also:mere disposal of this material is not, however, by any means the only See also:consideration in dealing with it upon the destructor See also:system. For many years past scientific experts, municipal engineers and public authorities have been directing careful See also:attention to the utilization of refuse as See also:fuel for See also:steam See also:production, and such progress in this direction has been made that in many towns its calorific value is now being utilized daily for See also:motive-See also:power purposes. On the other See also:hand, that proper degree of caution which is obtained only by actual experience must be exercised in the application of refuse fuel to steam-raising. When its value as a See also:low-class fuel was first recognized, the See also:idea was disseminated that the refuse of a given See also:population was of itself sufficient to develop the necessary steam-power for supplying that population with the electric See also:light. The economical importance of a combined destructor and electric undertaking of this See also:character naturally presented a somewhat fascinating stimulus to public authorities, and possibly had much to do with the development both of the See also:adoption of the principle of dealing with refuse by See also:fire, and of See also:lighting towns by See also:electricity. However true this phase of the question maybe as the statement of a theoretical scientific fact, experience so far does not show it to be a basis upon which engineers may venture to calculate, although, as will be seen later, under certain circumstances of equalized load, which must be considered upon their merits in each See also:case, a well-designed destructor plant can be made to perform valuable commercial service to an electric or other power-using undertaking. Further, when a system, thermal or otherwise, for the storage of See also:energy can be introduced and applied in a trustworthy and economical manner, the degree of See also:advantage to be derived from the utilization of the See also:waste See also:heat from destructors will be materially enhanced. The See also:composition of See also:house refuse, which must obviously affect its calorific value, varies considerably in different localities, Compost- according to the See also:condition, habits and pursuits of the tion and See also:people. Towns situated in See also:coal-producing districts quantity invariably yield a refuse richer in unconsumed See also:carbon of refuse. than those remote therefrom. It is also often found that the refuse from different parts of the same town varies considerably—that from the poorest quarters frequently proving of greater calorific value than that from those parts occupied by the See also:rich and See also:middle classes.

This has been attributed to the more extravagant habits of the working classes in neglecting to sift the ashes from their fires before disposing of them in the ash-bin. In See also:

Bermondsey, for example, the refuse has been found to possess an unusually high calorific value, and this experience is confirmed in other parts of the See also:metropolis. See also:Average refuse consists of See also:breeze (cinder and ashes), coal and See also:coke, See also:fine dust, See also:vegetable and See also:animal matters, See also:straw, shavings, cardboard, bottles, tins, See also:iron, bones, broken crockery and other matters in very variable See also:pro-portions according to the character of the See also:district from which it is collected. In See also:London the quantity of house refuse amounts approximately to 11 million tons per annum, which is See also:equivalent to from 4 cwt. to 5 cwt. per See also:head per annum, or to from 200 to 250 tons per r000 of the population per annum. See also:Statistics, however, vary widely in different districts. In the vicinity of the metropolis the amount varies from 2.5 cwt. per head per annum at See also:Leyton to 3.5 cwt. at See also:Hornsey, and to as much as 7 cwt. at See also:Ealing. In the See also:north of See also:England the See also:total house refuse collected, exclusive of street sweepings, amounts on the average to 8 cwt. per head per annum. Speaking generally, throughout the See also:country an amount of from 5 cwt. to ro cwt. per head per annum should be allowed for. A cubic yard of See also:ordinary house refuse weighs from 121-, to 15 cwt. See also:Shop refuse is lighter, frequently containing a large pro-portion of See also:paper, straw and other light wastes. It sometimes weighs as little as 74 cwt. per cubic yard. A load, by which refuse is often estimated, varies in See also:weight from r 5 cwt. to 11 tons.

The question how. a town's refuse shall be disposed of must be considered both from a commercial and a sanitary point of view. Various methods have been practised. Sometimes the Refuse household ashes, &c., are mixed with See also:

pail excreta, or disposal. with sludge from a sewage See also:farm, or with See also:lime, and disposed of for agricultural purposes, and sometimes they are conveyed in carts or by See also:canal to outlying and country districts, where they are shot on waste ground or used to fill up hollows and raise the level of marshland. Such plans are economical when suitable outlets are available. To take the refuse out to See also:sea in hopper See also:barges and sink it in deep See also:water is usually expensive and frequently unsatisfactory. At Bermondsey, for instance, the cost of barging is about 2S. 9d. a ton, while the material may be destroyed by fire at a cost of from See also:rod. to is. a ton, exclusive of See also:interest and sinking fund on the cost of the See also:works. In othercases, as at See also:Chelsea and various dust contractors' yards, the refuse is sorted and its ingredients are sold; the fine dust may be utilized in connexion with manure manufactories, the pots and pans employed in forming the See also:foundations of roads, and the cinders and vegetable refuse burnt to generate steam. In the See also:Arnold system, carried out in See also:Philadelphia and other See also:American towns, the refuse is sterilized by steam under pressure, the grease and fertilizing substances being extracted at the same See also:time; while in other systems, such as those of Weil and Porno, and of Defosse, See also:distillation in closed vessels is practised. But the destructor system, in which the refuse is burned to an innocuous See also:clinker in specially constructed furnaces, is that which must finally be resorted to, especially in districts which have become well built up and thickly populated. Various types of furnaces and apparatus have from time to time been designed, and the subject has been one of much experiment and many failures.

The See also:

principal towns in England which took the See also:lead in the adoption of the refuse destructor system were See also:Manchester, See also:Birmingham, See also:Leeds, See also:Heckmondwike, See also:Warrington, See also:Blackburn, See also:Bradford, See also:Bury, See also:Bolton, See also:Hull, See also:Nottingham, See also:Salford, Ealing and London. Ordinary furnaces, built mostly by dust contractors, began to come into use in London and in the north of England in the second See also:half of the 19th See also:century, but they were not scientific-ally adapted to the purpose, and necessitated the admixture of coal or other fuel with the refuse to ensure its See also:cremation. The Manchester See also:corporation erected a See also:furnace of this description about the See also:year 1873, and Messrs See also:Mead & Co. made an unsatisfactory See also:attempt in 187o to See also:burn house refuse in closed furnaces at See also:Paddington. In 1876 See also:Alfred Fryer erected his destructor at Manchester, and several other towns adopted this furnace shortly afterwards. Other furnaces were from time to time brought before the public, among which may be mentioned those of See also:Pearce and Lupton, Pickard, Healey, Thwaite, See also:Young, See also:Wilkinson, See also:Burton, Hardie, See also:Jacobs and Odgen. In addition to these the " Beehive " and the " See also:Nelson " destructors became well known. The former was introduced by See also:Stafford and See also:Pearson { d1.4rFOR,y ~fe'YI~ {{ {!{+{{ A I0$ of See also:Burnley, and one was erected in 1884 in the See also:parish yard at See also:Richmond, See also:Surrey, but the results being unsatisfactory, it was closed during the following year. The " Nelson " furnace, patented in 1885 by Messrs Richmond and Birtwistle, was erected at Nelson-in-See also:Marsden, See also:Lancashire, but being very costly in working was abandoned. The principal types of destructors now in use are those of Fryer, Whiley, Horsfall, See also:Warner, Meldrum, Beaman and Deas, Heenan and See also:Froude, and the " See also:Sterling " destructor erected by Messrs See also:Hughes and See also:Stirling. The general arrangement of the destructor patented' by Alfred Fryer in 1876 is illustrated in fig. I. An See also:installation upon this principle consists of a number of furnaces or cells, usu- Fryer's. ally arranged in pairs back to hack, and enclosed in a rectangular See also:block of See also:brickwork having a See also:flat See also:top, upon which the house refuse is tipped from the carts.

1 Patent No. 3125 (1876). Types of destructors. points in the See also:

design are the arrangement of the flues and flue outlets for the products of See also:combustion, and the introduction of a blast duct through which See also:air is forced into a closed ash-See also:pit. The feeding-hole is situated at the back of and above the furnace, while the flue opening for the emission of the gaseous products is placed at the front of the furnace over the dead See also:plate; thus the gases distilled from the raw refuse are caused to pass on their way to the See also:main flue over the hottest See also:part of the furnace and through the flue opening in the red-hot reverberatory See also:arch. The steam See also:jet, which plays an important part in the Horsfall furnace, forces air into the closed ash-pit at a pressure of about 4 to i in. of water, and in this way a temperature varying from 1500° to 2000° F., as tested by a thermo-electric See also:pyrometer, is maintained in the main flue. In a See also:battery of cells the gases from each are delivered into one main fine, so that a See also:uniform temperature is maintained therein sufficiently high to prevent noxious vapours from reaching the See also:chimney. The cells being charged and clinkered in rotation, when the fire in one is See also:green, in the others it is at its hottest, and the products of combustion do not reach the See also:boiler surfaces until after they have been mixed in the main flue. The See also:cast iron boxes which are provided at the sides of the furnaces, and through which the blast air is conveyed on its way to the See also:grate, prevent the See also:adhesion of clinker to the See also:side walls of the cells, and very materially preserve the brickwork, which otherwise becomes damaged by the tools used to remove the clinker. The wide clinkering doors are suspended by counterbalance weights and open vertically. The See also:rate of working of these cells varies from 8 tons per See also:cell per 24 See also:hours at See also:Oldham to to tons per cell at Bradford, where the furnaces are of a later type. The cost of labour in stoking and clinkering is about 6d. per ton of the refuse treated at Bradford, and 9d. per ton at Oldham, where the rate of See also:wages is higher.

Well-constructed and properly-worked See also:

plants of this type should give rise to no See also:nuisance, and may be located in populous neighbourhoods without danger to the public See also:health or comfort. Installations were put down at See also:Fulham (1901), Hammerton Street, Bradford (1900), See also:West See also:Hartlepool (1904), and other places, and the surplus power generated is employed in the production of electric energy. Warner's destructor,' known as the " Perfectus," is, in general arrangement, similar to Fryer's, but differs in being provided with See also:special charging hoppers, dampers in flues, dust-catching Warner's. arrangements, rocking grate bars and other improvements. The refuse is tipped into feeding-hoppers, consisting of rectangular cast iron boxes over which plates are placed to prevent the See also:escape of See also:smoke and fumes. At the See also:lower portion of the feeding-hopper is a flap-See also:door working on an See also:axis and controlled by an iron See also:lever from the tipping See also:platform. When refuse is to be fed into the furnace the lever is thrown over, the contents of the hopper drop on to the sloping See also:firebrick See also:hearth beneath, and the door is at once closed again. The door should be kept open as See also:short a time as possible in See also:order to prevent the See also:admission of See also:cold air into the furnace at the back end, since this leads to the lowering of the temperature of the cells and main flue, and also to paper and other light, refuse being carried into the flues and chimney. The flues of each furnace are provided with dampers, which are closed during the See also:process of clinkering in order to keep up the heat. The cells are each 5 ft. wide and 11 ft. deep, the rearmost portion consisting of a firebrick drying hearth, and the front of rocking grate bars upon which the combustion takes See also:place. The See also:crown of each cell is formed of a reverberatory firebrick arch having openings for the emission of the products of combustion. The flap dampers which are fitted to these openings are operated by See also:horizontal FIG.

3.-Meldrum's Destructor at See also:

Darwen. through the brickwork ptossthe hopper, and exception may also be taken to the continual flapping of front of the cell, where they are provided with levers or handles; the door when the clinker passes out, as cold air is thereby admitted thus each cell can be worked independently of the others. With the into the furnace. As in the Fryer cell, the outlet for the products of view of increasing the steam-raising capabilities of the furnace, forced combustion into the main flue is See also:close to the point where the crude See also:draught is sometimes applied and a tubular boiler is placed close to refuse is fed into the furnace, and the escape of unburnt vapours is the cells. The amount of refuse consumed varies from 5 tons to 8 tons thus facilitated. Forced draught is applied by means of a Roots per cell per 24 hours. At Hornsey, where 12 cells of this type are blower. The Manchester corporation has 28 cells of this type in use, in use, the cost of labour for burning the refuse is 92d. per ton. and the approximate amount of refuse burnt per cell per 24 hours is The Meldurm " Simplex " destructor (fig. 3), a type of furnace from 6 to 8 tons at a cost per ton for labour of 3.47 pence. which yields See also:good steam-raising results, is in successful operation Horsfall's destructor' (fig. 2) is a high-temperature furnace of at See also:Rochdale, See also:Hereford, Darwen, Nelson, Plumstead and Al Idrum's. See also:modern type which has been adopted largely in See also:Great See also:Britain and on See also:Woolwich, at each of which towns the production of steam Horsfall's. the See also:continent of See also:Europe. In it some of the general features is an important consideration. Cells have also been laid down at Ho of the Fryer cell are retained, but the details differ See also:con- Burton, See also:Hunstanton, Blackburn and See also:Shipley, and more recently at siderably from those of the furnaces already described.

Important Burnley, See also:

Cleckheaton, See also:Lancaster, Nelson, See also:Sheerness and See also:Weymouth. In general arrangement the destructor differs considerably from 3 Patent No. 18.719 (r888). aarrrwwate rrruv inoffensive. The serious nuisances thus produced in some instances led to the introduction of a second furnace, or " cremator," patented by C. See also:Jones of Ealing in 1885, which was placed in the main flue leading to the chimney-See also:shaft, for the purpose of resolving the organic matters See also:present in the vapour, but the greatly increased cost of burning due to this See also:device led to its See also:abandonment in many cases. This type of cell was largely used during the See also:early See also:period of the See also:history of destructors, but has to a considerable extent given place to furnaces of more modern design. A furnace 1 patented in 1891 by Mr See also:Henry Whiley, See also:superintendent of the scavenging See also:department of the Manchester corporation, is W61/ey's automatic in its See also:action and was designed primarily with a view to saving labour—the cells being fed, stoked and clinkered automatically. There is no drying hearth, and the refuse carts tip See also:direct into a shoot or hopper at the back which conducts the material directly on to movable See also:eccentric grate bars. These auto- matically See also:traverse the material forward into the furnace, and finally push it against a flap-door which opens and allows it to fall out. This apparatus is adapted for dealing with screened rather than unscreened refuse, since it suffers from the objection that the See also:motion of the bars tends to allow fine particles to drop through unburnt. Some difficulty has been experienced from the refuse sticking in the A large main flue, which also forms the dust chamber, is placed underneath the furnace hearths.

The Fryer furnace ordinarily See also:

burns from 4 to 6 tons of refuse per cell per 24 hours. It will be observed that the outlets for the products of combustion are placed at the back near the refuse feed opening, an arrangement which is imperfect in design, inasmuch as while a See also:charge of refuse is burning upon the furnace bars the charge which is to follow lies on the dead hearth near the outlet flue. Here it undergoes drying and partial decomposition, giving off offensive empyreumatic vapours which pass into the flue without being exposed to sufficient heat to render them entirely feed',. Hole feed,, See also:Floor .cs r ..~rur orr.. /f,. - 4 i=NW `~• t~r 9/See also:ast ddXL \ pia f/See also:Ito \ ~.~~..a''' \~• 1N. rieairedim.A.WASPiO.'id.TATeAval~ ,02'' s''rA M { Counterba/anc• I\\~**%%\See also:mss%~ /\ to furnace s y, ,._ lj door. _ 1 Ftfar+ace_ Ref use is shove/led from this opentny into furnace.. - 1 Patent No. 8271 (1891). See also:Patents No. 8999 (1887); No. 14,709 (1888) ; No.

22,531 (1891). those previously described. The grates are placed side by side without separation except by dead plates, but, in order to localize the forced draught, the ash-pit is divided into parts corresponding with the different grate areas. Each ash .pit is closed air-tight by a cast iron plate, and is provided with an air-tight door for removing the fine ash. Two patent Meldrum steam-jet blowers are provided for each furnace, supplying any required pressure of blast up to 6 in. water See also:

column, though that usually employed does not exceed i in. The furnaces are designed for hand-feeding from the front, but hopper-feeding can be applied if desirable. The products of combustion either pass away from the back of each fire-grate into a See also:common flue leading to boilers and the chimney-shaft, or are conveyed sideways over the various grates and a common fire-See also:bridge to the boilers or chimney. The heat in the gases, after passing the boilers, is still further utilized to heat the air supplied to the furnaces, the gases being passed through an air heater or continuous regenerator consisting of a number of cast ironpipes from which the air is delivered through the Meldrum " blowers at a temperature of about 300° F. That a high percentage (i5 to i8 %) of See also:CO2 isobtained in the furnaces proves a small excess of See also:free See also:oxygen, and no doubt explains the high fuel efficiency obtained by this type of destructor. High-pressure boilers of ample capacity are provided for the accumu-Iation during periods of light load of a reserve of steam, the storage being obtained by utilizing the difference between the highest and lowest water-levels and the difference between the maximum and working steam-pressure. Patent locking fire-bars, to prevent lifting when clinkering, are used in the furnace and have a good See also:life. At Rochdale the Meldrum furnaces consume from 531b to 66 lb of refuse per square See also:foot of grate See also:area per See also:hour, as compared with 22.4 lb per square foot in a low-temperature destructor burning 6 tons per cell per 24 hours with a grate area of 25 sq. ft.

The evaporative efficiency of the Rochdale furnaces varies from 1.39 lb to 1.87 lb of water (actual) per 1 lb of refuse burned, and an average steam-pressure of about 114 lb per square See also:

inch is maintained. The cost of labour and Fig. 4.—Beaman and Deas Destructor at Leyton. supervision amounts to Iod. per ton of refuse dealt with. A Lancashire boiler (22 ft. by 6 ft. 6 in.) at the Sewage Outfall Works, Hereford, evaporates with refuse fuel 2980 lb of water per hour, equal to 149 indicated See also:horse-power. About 54 lb of refuse are burnt per square foot of grate area per hour with an evaporation of 1.82 lb of water per See also:pound of refuse. The Beaman and Deas destructor' (fig. 4) has attracted much attention from public authorities, and successful installations are in operation at Warrington, See also:Dewsbury, Leyton, Beaman See also:Canterbury, See also:Llandudno, See also:Colne, See also:Streatham, Rotherhithe,. and Deas. See also:Wimbledon, Bolton and elsewhere. Its essential features include a level-fire grate with ordinary type bars, a high-temperature combustion chamber at the back of the cells, a closed ash-pit with forced draught, See also:provision for the admission of a secondary air-See also:supply at the fire-bridge, and a firebrick hearth sloping at an See also:angle of about 52°.

From the refuse storage platform the material is fed into a hopper mouth about 18 in. square, and slides down the firebrick hearth, supported by T-irons, to the grate bars, over which it is raked and spread with the assistance of See also:

long rods manipulated through clinkering doors placed at the sides of the cells. A secondary door in the See also:rear of the cell facilitates the operation. The fire-bars, spaced only s in. apart, are of the ordinary stationary type. Vertically, under the fire-bridge, is an air-conduit, from the top of which lead air blast pipes 12 in. in See also:diameter discharging into a hermetically closed ash-pit under the grate area. The air is supplied from fans (Schiele's patent) at a pressure of from 12 to 2 in. of water, and is con- trolled by means of baffle valves worked by handles on either side of the furnace, conveniently placed for the attendant. The forced draught tends to keep the bars cool and lessen See also:wear and See also:tear. The fumes from the charge drying on the hearth pass through the fire and over the red-hot fire-bridge, which is perforated longitudinally with air-passages connected with a small flue leading from a grated opening on the See also:face of the brickwork outside; in this way an See also:auxiliary supply of heated oxygen is fed into the combustion chamber. This ' Patents No. 15,598 (1893) and 23,712 (1893); also Beaman and Deas Sludge Furnace, Patent No. 13,029 (1894).chamber, in which a temperature approaching 2000° F. is attained, is fitted with large iron doors, sliding with See also:balance weights, which allow the introduction of infected articles, See also:bad See also:meat, &c., and also give See also:access for the periodical removal of fine ash f om the flues. The high temperatures attained are utilized by install ng one boiler, preferably of the Babcock & Wilcox water-See also:tube type, for each pair of cells, so that the gases, on their way from the combustion chamber to the main flue, pass three times between the boiler tubes. A secondary furnace is provided under the boiler for raising steam by coal, if required, when the cells are out of use.

The grate area of each cell is 25 sq. ft., and the See also:

consumption varies from 16 up to 20 tons of refuse per cell per 24 hours. In a 24-hours' test made by the superintendent of the cleansing department, Leeds, at the Warrington installation, the quantity of water evaporated per pound of refuse was 1.14 lb, the average temperature in the combustion chamber 2000° F. by See also:copper-See also:wire test, and the average air pressure with forced draught 22 in. (water-See also:gauge). At Leyton, which has a population of over 100,000, an 8-cell plant of this type is successfully dealing with house refuse and See also:filter See also:press cakes of sewage sludge from the sewage disposal works adjoining, and even with material,of this low calorific value the total steam-power produced is considerable. Each cell burns about 16 tons of the mixture in 24 hours and develops about 35 indicated horse-power continuously, at an average steam-pressure in the boilers of 105 lb. The cost of labour at .Leyton for burning the mixed refuse is about is. 7d. per ton; at Llandudno, where four cells were laid down in connexion with the electric-light station in 1898, it is Is. 3;d., and at Warrington 92d. per ton of refuse consumed. Combustion is See also:complete, and the destructor may be installed in populous districts without nuisance to the inhabitants. Further patents (See also:Wilkie's improvements) have been obtained by Meldrum See also:Brothers (Manchester) in connexion with this destructor. The Heenan furnaces are in operation at See also:Farnworth, See also:Gloucester, See also:Barrow-in-See also:Furness, See also:Northampton, See also:Mansfield, See also:Wakefield, Blackburn, Levenshulme, See also:Kings See also:Norton, See also:Worthing, Birmingham and Heenan other places, and are now dealing with over 1200 tons of refuse per See also:day. The general arrangement of this destructor some-what resembles that of the Meldrum type.

The cells intercommunicate, and the See also:

mechanical mixture of the gases arising from the furnace grates of the various cells is sought by the introduction of a special design of reverberatory arch overlying the grates. The See also:standard arrangement of this destructor embodies all modern arrangements for high-temperature refuse destruction and steam-power See also:generation. Destructors of the " Sterling " type, combined with electric-power generating stations, are installed at See also:Hackney (1901), Bermondsey (1902) and Frederiksberg (19o3)—the first-named plant being. probably the most powerful com- Sterling. bined destructor and electricity station yet erected. In these modern stations the recognized requirements of an up-to-date refuses destruction plant have been well considered and good calorific results are also obtained. In addition to the above-described destructors, other forms have been introduced from time to time, but adopted to a less degree; amongst these may be mentioned See also:Baker's destructor, Willshear's, See also:Hanson's Utilizer, See also:Mason's Gasifier, the See also:Bennett-Phythian, Cracknell's (See also:Melbourne, See also:Victoria), Coltman's (See also:Loughborough), See also:Willoughby's, and Healey's improved destructors. On the continent of Europe systems for the treatment of refuse have also been devised. Among these may be mentioned those of M. Defosse and M. Helouis. The former has endeavoured to burn the refuse in large quantities by using a forced draught and only washing the smoke.' Helouis has extended the operation by using the heat from the combustion of the refuse for drying and distilling the material which is brought gradually on to the grate. Boulnois and See also:Brodie's improved charging tank is a labour-saving apparatus consisting of a wrought iron See also:truck, 5 ft. wide by 3 ft. deep, and of sufficient length to hold not less than 12 hours' Destructor supply for the two cells which it serves. The truck, acres which moves along a pair of rails across the top of the soles. destructor, may be worked by one See also:man.

It is divided into compartments holding a charge of refuse in each, and is provided with a pair of doors in the bottom, opening downwards, which are supported by a See also:

series of small wheels See also:running on a central See also:rail. A special feeding opening in the reverberatory arch of the cell of the width of the truck, situated over the drying hearth, is formed by a firebrick arch fitted into a See also:frame capable of being moved backwards and forwards by means of a lever. The charging truck, when empty, is brought under the tipping platform, and the carts tip directly into it. When one of the cells has to be fed, the truck is moved along, so that one of the divisions is immediately over the feeding opening, and the See also:wheel holding up the bottom doors rests upon the central rail, which is continued over the movable covering arch. Then the movable arch is rolled back, the doors are released, and the contents are discharged into the cell, so that no handling of the refuse is required from tipping to feeding. This apparatus is in operation at See also:Liverpool, See also:Shoreditch, See also:Cambridge and elsewhere. Various formsof patent movable fire-bars have been employed ' Compte Rendu See also:des Travaux de la Societe des Ingenieurs Civils de See also:France, See also:folio 775 (See also:June 1897). in destructor furnaces. Among these may be mentioned See also:Settle's,' See also:Vicar's,' Riddle's rocking bars,3 Horsfall's self-feeding apparatus,' and Healey's movable bars ; 5 but complicated movable arrangements are not to be recommended, and experience greatly favours the use of a See also:simple stationary type of fire-See also:bar. A dust-catching apparatus has been designed and erected at See also:Edinburgh, by the Horsfall Furnace See also:Syndicate, in order to over-come difficulties in regard to the escape of flue dust, &c., from the destructor chimney. Externally, it appears a large circular block of brickwork, 18 ft. in diameter and 13 ft. 7 in. high, connected with the main flue, and situated between the destructor cells and the boiler.

Internally it consists of a See also:

spiral flue traversing the entire circumference and winding upwards to the top of the chamber. There is an interior well or chamber 6 ft. diameter by 12 ft. high, having a domed top, and communicating with the See also:outer spiral flue by four ports at the top of the chamber. Dust traps, baffle walls Other See also:accessory plant in use at most modern destructor stations includes machinery for the removal, crushing and various means of utilization of the residual clinker, stoking tools, air heaters or regenerators for the production of hot-air blast to the furnaces, superheaters and thermal storage arrangements for equalizing the output of power from the station during the 24-hours' day. The general arrangement of a battery of refuse cells at a destructor station is illustrated by fig. 5. The cells are arranged either side by side, with a common main flue in the rear, or back to back with the main flue placed in the centre and leading to a tall chimney-shaft. The heated gases on leaving the cells pass through the combustion chamber into the main flue, and thence go forward to the boilers, where their heat is absorbed and utilized. Forced draught, or Working of destructors. r~N _ e.r ..F 7f!-~•h~- .--' t?• - ENGI0( ry.ntA.,. T I P P I N G P L A r P O R M i~ i ~~\ ~ %m! ... ~~ **I \.vim ttN e c ~ 5 I tr.

GN/NNEY SNArr' weekly removal of the flue dust. The apparatus forms a large See also:

reservoir of heat maintained at a steady temperature of from 1500° to 1800° F., and is useful in keeping up steam in the boiler at an equable pressure for a long period. It requires no attention, and has proved successful for its purpose. Travelling See also:cranes for transporting refuse and feeding cells are sometimes employed at destructor stations, as, for example, at See also:Hamburg. Here the transportation of the refuse is effected by means of specially constructed water-tight iron wagons, containing detachable boxes provided with two See also:double-flap doors at the top for loading, and one flap-door at the back for unloading. There are See also:thirty-six furnaces of the Horsfall type placed in two ranks, each arranged in three blocks of six in the large furnace See also:hall. An electric See also:crane running above each See also:rank lifts the boxes off the wagons and carries them to the feeding-hole of each well. Here the See also:box is tipped up by an electric See also:pulley and emptied on to the furnace platform. When the travelling crane is used, the carts (four-wheeled) bringing the refuse may be constructed so that the See also:body of the See also:carriage can be taken off the wheels, lifted up and tipped direct over the furnace as required, and returned again to its frame. The adoption of the travelling crane admits of the reduction in See also:size of the main See also:building, as less platform space for unloading refuse carts is required; the inclined roadway may also be dispensed with. Where a destructor site will not admit ofan inclined roadway and platform, the refuse may be discharged from the See also:collecting carts into a lift, and thence elevated into the feeding-bins. 1 Patent No.

15,482 (1885). 2 Patents No. 1955 (1867) and No. 378 (1879). 3 Patent No. 4896 (1891). a Patent No. 20,207 (1892). 6 Patents No. 18,398 (1892) and No. 12,990 (1892). in many cases, hot blast, is supplied from fans through a conduit commanding the whole of the cells.

An inclined roadway, of as easy gradient as circumstances will admit, is provided for the See also:

conveyance of the refuse to the tipping platform, from which it is fed through feed-holes into the furnaces. In the installation of a destructor, the choice of suitable plant and the general design of the works must be largely dependent upon See also:local requirements, and should be entrusted to an engineer experienced in these matters. The following See also:primary considerations, however, may be enumerated as materially affecting the design of such works: (a) The plant must be simple, easily worked without stoppages, and without mechanical complications upon which stokers may See also:lay the blame for bad results. (bb) It must be strong, must withstand See also:variations of temperature, must not be liable to get out of order, and should admit of being readily repaired. (c) It must be such as can be easily understood by stokers or firemen of average intelligence, so that the continuous working of the plant may not be disorganized by See also:change of workmen. (d) A sufficiently high temperature must be attained in the cells to reduce the refuse to an entirely innocuous clinker, and all fumes or gases should pass either through an adjoining red-hot cell or through a chamber whose temperature is maintained by the ordinary working of the destructor itself at a degree sufficient to exclude the possibility of the escape of any unconsumed gases, vapours or particles. The temperature may vary between 150o° and 2000°. (e) The plant must be so worked that while some of the cells are being recharged, others are at a glowing red heat, in order that a high temperature may be uniformly maintained. (f) The design of the furnaces must admit of clinkering and recharging being easily and i quickly performed, the furnace doors being open for a minimum of time so as to obviate the inrush of cold air to lower the temperature in main flues, &c. (g) The chimney draught must he assisted with forced draught from fans or steam jet to a pressure of I2 in. to 2 in. under grates by water-gauge. (h) Where a destructor is required to See also:work without See also: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 See also:surface, whereby the temperature of the gases is reduced before the organic See also:matter has been thoroughly burned.

(i) Where steam-power and a high fuel efficiency are desired a large percentage of CO2 should be sought in the furnaces with as little excess of air as possible, and the flue gases should be utilized in See also:

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. As to the initial cost of the erection of refuse destructors, few trustworthy data can be given. The outlay necessarily depends, Cost 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 See also: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 See also: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 See also:capital outlay. The cost of burning ton for ton consumed, in high-temperature furnaces, including labour and See also:repairs, is not greater than in slow-combustion destructors. The average cost of burning refuse at twenty-four different towns through-out England, exclusive of interest on the cost of the works, is Is. i id. per ton burned; the minimum cost is 6d. per ton at Bradford, and the maximum cost 2s. Iod. per ton at See also:Battersea. At Shoreditch the cost per ton for the year ending on the 25th of See also: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 2olb 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. The amount of See also:

residue in the shape of clinker and fine ash varies from 22 to 37% of the bulk dealt with. From 25 to 30% is a very Residues: usual amount. At Shoreditch, where the refuse consists of about 8 % of straw, paper, shavings, &c., the residue contains about 29% clinker, 2•7% fine ash, .5 °A flue dust, and -6% old tins, making a total residue of 32'8%. As the residuum amounts to from one-See also:fourth to one-third of the total bulk of the refuse dealt with, it is a question of the utmost importance that some profitable, or at least inexpensive, means should be devised for its See also:regular disposal. Among other purposes, it has been used for bottoming for macadamized roads, for the manufacture of See also:concrete, for making paving slabs, for forming suburban footpaths or cinder footwalks, and for the manufacture of See also:mortar. The last is a very general, and in many places profitable, mode of disposal. An entirely new outlet has also arisen for the disposal of good well-vitrified destructor clinker in connexion with the construction of bacteria beds for sewage disposal, and in many districts its value has, by this means, become greatly enhanced. Through defects in the design and management of many of the early destructors complaints of nuisance frequently arose, and these have, to some extent, brought destructor installations into disrepute.

Although some of the older furnaces were decided offenders in this respect, that is by no means the case with the modern improved type of high-temperature furnace; and often, were it not for the great prominence in the landscape of a tall chimney-shaft, the existence of a refuse destructor in a neighbourhood would not be generally known to the inhabitants. A modern furnace, properly designed and worked, will give rise to no nuisance, and may be safely erected in the midst of a populous neighbourhood. To ensure the perfect See also:

crema- tion of the refuse and of the gases given off, forced draught is essential. This is supplied either as air draught delivered from a rapidly revolving See also:fan, or as steam blast, as in the Horsfall steam jet or the Meldrum blower. With a forced blast less air is required to obtain complete combustion than by chimney draught. The forced draught grate requires little more than the quantity theoretically necessary, while with chimney draught more than double the theoretical amount of air must be supplied. With forced draught, too, a much higher temperature is attained, and if it is properly worked, little or no cold air will enter the furnaces during stoking operations, As far as possible a balance of pressure in the cells during clinkering should be maintained just sufficient to pre-vent an inrush of cold air through the flues. The forced draught pressure should not exceed 2 in. water-gauge. The efficiency of the combustion in the furnace is conveniently measured by the " Econometer," which registers continuously and automatically the proportion of CO2 passing away in the waste gases; the higher the percentage of CO2 the more efficient the furnace, provided there is no formation of CO, the presence of which would indicate incomplete combustion. The theoretical maximum of CO2 for refuse burning is about 20 %; and, by maintaining an even clean fire, by admitting secondary air over the fire, and by regulating the dampers or the air-pressure in the ash-pit, an amount approximating to this percentage may be attained in a well-designed furnace if properly worked. If the proportion of free oxygen (i.e. excess of air) is large, more air is passed through the furnace than is required for complete combustion, and the heating of this excess is clearly a waste of heat. The position of the econometer in testing should be as near the furnace as possible, as there may be considerable air leakage through the brickwork of the flues.

The air supply to modern furnaces is usually delivered hot, the inlet air being first passed through an air-heater the temperature of which is maintained by the waste gases in the main flue. The modern high-temperature destructor, to render the refuse and gases perfectly innocuous and harmless, is worked at a temperature varying from 1250 to 2000 F., and the See also:

maintenance of such temperatures has very naturally suggested the possi- See also:Cab riNc bility of utilizing this heat-energy for the production of value. steam-power. Experience shows that a considerable amount of energy may be derived from steam-raising destructor stations, amply justifying a reasonable increase of See also:expenditure on plant and labour. The actual calorific value of the refuse material necessarily varies, but, as a general average, with suitably designed and properly managed plant, an evaporation of I lb of water per pound of refuse burned is a result which may be readily attained, and affords a basis of calculation which engineers may safely adopt in practice. Many destructor steam-raising plants, however, give considerably higher results, evaporations approaching 2 lb of water per pound of refuse being often met with under favourable conditions. From actual experience it may be accepted, therefore, that the calorific value of unscreened house refuse varies from i to 2 lb of water evaporated per pound of refuse burned, the exact proportion depending upon the quality and condition of the material dealt with. Taking the evaporative power of coal at lo lb of water per pound of coal, this gives for domestic house refuse a value of from A to i that of coal; or, with coal at 20S. per ton, refuse has a commercial value of from 2s. to 4s. per ton. In London the quantity of house refuse amounts to about I} million tons per annum, which is equivalent to from 4 cwt. to 5 cwt. per head per annum. If it be burned in furnaces giving an evaporation of 1 lb of water per pound of refuse, it would yield a total power annually of about 138 million See also:brake horse-power hours, and equivalent cost of coal at 20s. per ton for this amount of power even when calculated upon the very low estimate of 2 lb' of coal per brake horse-power hour, works out at over £123,000. On the same basis, the refuse of a See also:medium-sized town, with, say, a population of 70,000 yielding refuse at the rate of 5 cwt. per head ppr annum, would afford 112 indicated horse-power per ton burned, and the total indicated horse-power hours per annum would be 70,000X5 CWt. X I12 =1,960,000 I.H.P. hours annually. 20 If this were applied to the production of electric energy, the See also:electrical horse-power hours would he (with a See also:dynamo efficiency of 90%) 1,960 000X90 =1,764,000 E.H.P. hours per annum; See also:Ioo and the See also:watt-hours per annum at the central station would be 1,764,000 X 746 =1,315,944,000.

Allowing for a loss of to % in See also:

distribution, this would give 1,184,349,600 watt-hours available in lamps, or with 8-See also:candle-power lamps taking 30 See also:watts of current per See also:lamp, we should have 1,1 84 349,600 watt-hours 30 watts =39478,320 8-c.p. lamp-hours per annum; that is, 39,478,320 =563 8-c.p. lamp-hours per annum per 70,000 population head of population. Taking the loss due to the storage which would be necessary at 20 % on three-quarters of the total or 15% upon the whole, there would be 478 8-c.p. lamp-hours per annum per head of the population : i.e. if the power See also:developed from the refuse were fully utilized, it would supply electric light at the rate of one 8-c.p. lamp per head of the population for about 13 hours for every See also:night of the year. In actual practice, when the electric energy is for the purposes of lighting only, difficulty has been experienced in fully utilizing the thermal energy from a destructor plant owing to the want of adequate means of storage either of the thermal or of culties the electric energy. A destructor station usually yields a fairly definite amount of thermal energy uniformly throughout the 24 hours, while the consumption of electric-lighting current is extremely 'With medium-sized, steam plants, a consumption of 4 lb of coal per brake horse-power per 'hour is a very usual performance. Forced draught. irregular, the maximum demand being about four times the mean ,demand. The period during which the demand exceeds the mean is 'comparatively short, and does not exceed about 6 hours out of the 21, while for a portion of the time the demand may not exceed See also:Ath the maximum. This difficulty, at first regarded as somewhat See also:grave, is substantially minimized by the provision of ample boiler capacity, or by the introduction of feed thermal storage vessels in which hot feed-water may be stored during the hours of light load (say i8 out of the 24), so that at the time of maximum load the boiler may be filled directly from these vessels, which work at the same pressure and temperature as the boiler. Further, the difficulty above mentioned will disappear entirely at stations where there is a See also:fair day load which practically ceases at about the hour when the See also:illuminating load comes on, thus equalizing the demand upon both destructor and electric plant throughout the 24 hours. This arises in cases where current is consumed during the day for See also:motors, fans, lifts, electric tramways, and other like purposes, and, as the employment of electric energy for these services is rapidly becoming general, no difficulty need be anticipated in the successful working of combined destructor and electric plants where these conditions prevail. The more uniform the electrical demand becomes, the more fully may the power from a destructor station be utilized. In addition to See also:combination with electric-lighting works, refuse destructors are now very commonly installed in See also:conjunction with various other classes of power-using undertakings, including tram-ways, water-works, sewage-pumping, artificial slab-making and clinker-crushing works and others; and the increasingly large sums which are being yearly expended in combined undertakings of this character is perhaps the strongest See also:evidence of the See also:practical value of such combinations where these several classes of work must be carried on.

For further See also:

information on the subject, reference should be made to See also:William H. See also:Maxwell, Removal and Disposal of Town Refuse, with an exhaustive treatment of Refuse Destructor Plants (London, 1899), with a special Supplement embodying later results (London, 1905). See also the Proceedings of the Incorporated Association of Municipal and See also:County Engineers, vols. xiii. p. 216, xxii. p. 211, See also:xxiv. P. 214 and See also:xxv. p. 138; also the Proceedings of the Institution of See also:Civil Engineers, vols. cxxii. p. 443, cxxiv. p. 469, exxxi. p. 413, exxxviii. p. 508, cxxix. p.

434, cxxx. pp. 213 and 347, exxiii. pp. 369 and 498, cxxvni. p. 293 and cxxxv. p. 300. (W. H.

End of Article: DESTRUCTORS

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