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Municipal housecleaning

Chapter 44: Activated Sludge Process
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A practical manual surveys municipal methods for collecting and disposing of urban wastes—street refuse, ashes, rubbish, garbage, manure, and sewage—presenting operational practices, organization, equipment, regulations, and cost data. It describes street cleaning techniques, sewer systems and treatment options (sedimentation, septic and Imhoff tanks, filtration, chemical and biological processes, disinfection), and collection systems including districting, receptacle placement, frequency, and enforcement. Disposal technologies such as incineration, reduction, sanitary fills and land dumping are examined alongside possibilities for by-product revenue. The work also outlines public clean-up campaigns, inspection and propaganda methods, and managerial principles for improving sanitary efficiency and municipal economy.

Intermittent Sand Filters

As a final process of purification in sections where land and filter material are available at small cost the intermittent sand filter is superior to any other. This fact has been established by experience and experiments. The filter material may be clean, coarse sand or any other porous soil. If a natural area is available the method of construction is very much simplified and economical. The top soil is removed and used in embankments between the beds. If the water tables are low the beds are not underdrained. In artificial beds the size of the sand is important. While fine sand will give a more brilliant effluent than a coarser material, the sewage has to be applied in small doses with long periods of rest. The rate of purification is higher in coarse sand filters and the effluent while containing more bacteria is non-putrescible. About twenty-four inches of sand should cover the underdrains of tile, placed about five feet apart, and surrounded by small-sized gravel.

In some beds the entire bottom above the underdrain is covered with about six inches of gravel. In others the bottom is ridged, the underdrains being placed at the bottom of the valleys which are then partially or wholly filled with gravel. Risers are constructed at the head of the underdrain and an intercepting drain completes the system. The beds vary in size and number according to the amount of sewage to be treated. The operation of the filter is very important. The sewage must be applied rapidly in rotation to each bed until the surface is covered with about three inches of the liquid. The bed is then slowly drained and allowed to rest. Overdosing and lack of aeration cause clogging. The surface must at all times be kept clean and loose. To maintain this condition it is sometimes necessary to break up the surface to a small depth or periodically to remove the deposit on the surface.

In cold climates the operation of the filters in winter is difficult and the quality of the effluent somewhat impaired. Several methods have been adopted to prevent freezing. Some filter beds are ridged so that when dosed the sewage flows in gutters. The ice which forms at the top of the sewage remains suspended on the ridges, thus permitting succeeding doses to flow underneath the ice. In other plants the surface of the filter is scraped into small piles which form a support for the ice. It is claimed that by this method the cost of subsequent cleaning is less than when the beds are ridged.

The effluent in properly constructed and managed plants is clear and odorless. The bacterial purification is as high as ninety-nine per cent. The Massachusetts State Board of Health in one of its reports says, “When sewage filters slowly and intermittently through five feet of porous earth and sand, an effluent is obtained which is as free from organic matter, from ammonia and from nitrites as many a natural spring water.”

The only drawback noted to this process is the cost of treatment in large quantities where land and filter material are not available. Francis E. Daniels says that under such conditions the cost is almost prohibitive. For many cities sufficient area cannot be obtained at any price, and as population increases the difficulty will become greater.

The New York State Board of Health in general will approve only of the following rates of operation for different types of filters where suitable provision for preliminary treatment is made: Intermittent sand filters, 100,000 gallons per acre per day; contact beds, 100,000 gallons per acre per day per foot of depth; sprinkling filters, 300,000 gallons per acre per day per foot of depth. These rates of operation are based on a sewage contribution of 100 gallons per capita daily and no variation from these rates of filtration is allowed for any other per capita contribution of sewage. The allowable effective depths of said filters will in general range from three to five feet; contact beds from four to seven feet; sprinkling filters, from five to nine feet.

Broad Irrigation

Broad irrigation, or sewage farming, is the oldest process of sewage purification, but the constant increase in population has made it necessary for cities to adopt other methods because of the area of land necessary for such a plant. Two processes are used, surface irrigation and filtration, a greater area of land being required for the former. Sometimes the two are combined into one process. For filtration and irrigation the sewage is generally first subjected to sedimentation or screening and then flows on carefully prepared land on which crops are usually grown. The areas are underdrained and are equipped with distribution systems.

Local conditions determine the method of irrigation, the ridge and furrow system being most generally used. The efficiency of the process depends upon the quality of the soil and proper management. Among the factors which should enter into the selection of the site are the quality of the soil, composition of sewage, method of disposal, kind of crops to be planted, contours and slope of surface, nature of the sub-soil, sub-soil waters, transportation facilities, nature of streams, nature of adjacent property, and availability of water supply. The best lands consist of a fine layer of alluvium overlaying a sub-soil of gravel, chalk or other porous material. Various kinds of crops are grown on sewage farms and the revenues therefrom help to reduce the cost of operation. They also assist in the purification. The principal drawback are heavy transportation cost and a prejudice against sewage-grown produce. During the rainy season when the quantity of sewage requiring treatment is greatest, less sewage can be used for irrigation and the growing of crops of sewage farms. All evidence points to the fact that broad irrigation is on a steady decline, although the efficiency of the treatment under favorable conditions is very high.

Disinfection

When the bacterial efficiency of an effluent from either preparatory or final treatment is low and the effluent is discharged into a body of water from which water supplies are derived or shell fish are taken, disinfection is often found necessary. The purpose is to destroy objectionable bacteria and disease germs. Hypo-chlorite of lime and liquid chlorine are the two chemicals most commonly used. The principal advantages of the liquid chlorine over the hypo-chlorite according to plant supervisors and operators, are less cost of operation and space required for both apparatus and storage of materials, no loss of strength, no lime sludge, and no mixing tanks required. The claim is also made that it can be better controlled. Chlorine, however, is more expensive than hypo-chlorite and the control apparatus usually costs more. There is general agreement among engineers, that except as an emergency measure or under the above stated conditions, disinfection is too expensive a process on account of the amount of chemical required. This varies with the amount, method and degree of previous treatment of the sewage and the degree of bacterial elimination desired. Tests at the Cleveland Testing Station indicated that from five to seven parts per million of available chlorine will effect a bacterial removal of from eighty-five to ninety per cent.

Activated Sludge Process

Sewage treatment by aeration in the presence of sludge is the latest development in sewage disposal, and the process is attracting a great deal of attention in America. Milwaukee has constructed a plant to treat two million gallons of sewage a day. Houston, Texas, is operating a plant to treat the sewage for 160,000 persons, and Escanaba, Michigan, and Jersey City, N. J., have favored the process. Experiments are now being conducted in Milwaukee, Baltimore, Washington, Cleveland, Regina, Chicago, Lawrence, Mass., Brooklyn, New Haven, Conn., the University of Illinois and many other places. The efficiency and economy of the process as compared with others which have long been in use have not been completely established. The chief points in dispute are sludge disposal and cost, but the indications are that these questions will soon be satisfactorily answered.

The process consists of passing raw sewage through tanks from eight to twenty feet deep in which a certain amount of activated sludge is always present. To mix the sewage and the activated sludge air is forced into the bottom of the tank under low pressure of sufficient volume to keep the liquor violently disturbed. From this aerating tank the mixture passes to another or sedimentation tank where the sludge settles and from which the clear effluent passes over a weir to its final destination. In order to maintain the proper volume of activated sludge in the aerating tank a portion of the sludge is pumped back from the sedimentation tank. The balance of the sludge is pressed and used for fertilizer base. The Milwaukee experiments indicate that in order to produce a clear, non-putrescible effluent about four hours aeration is required, twenty per cent. of activated sludge maintained in the aerating tank, and about 1.75 cubic feet of free air supplied per gallon of sewage treated.

The effluent is clear, odorless and practically free from suspended matter. The sludge will begin to decompose after forty-eight hours and must be pressed and dried within that time. Chief Engineer, T. Chalkley Hatton, of the Milwaukee Sewerage Commission, estimates that the sludge can be reduced to a fertilizer basis for about $8.75 per dry ton, including overhead charges. Basing the value of the sludge produced upon a low price per unit, he finds that Milwaukee sludge is worth $12.50 per dry ton, which represents a clear profit of $3.75 a ton. From ten to twelve million gallons can be treated upon one acre of ground, which is about one-fifth the area required for sedimentation tanks and sprinkling filters. The reasons for the adoption of this process by Milwaukee after experimentation by competent engineers for more than a year are given by Mr. Hatton in a recent address before New York State city officials as follows: “It produces a better effluent than any other known process of sewage treatment except land treatment or intermittent sand filtration; it can be built upon a comparatively small area; it produces no objectionable odors or flies; it produces a sludge of sufficient value to meet the cost of its reduction to a fertilizer and therefore relieves the city of the difficult, complicated and wasteful method of sludge disposal common to all other processes; it is subject to complete and satisfactory control throughout its operation; it is not materially influenced by climatic conditions; occupying a small area, its first cost is less than any other known process from which an equal character of effluent can be obtained; its operating cost is not prohibitive.”

In a discussion before the Iowa Section of the American Waterworks Association Dr. Edward Bartow commended activated sludge for its value as a fertilizer. This has been proved, he said, by its chemical composition, by its reaction with various solids and by its effect on the growth of plants. Pot cultures and garden experiments have shown that the nitrogen is in a very available form.

E. E. Sands, City Engineer of Houston, Texas, bases this statement on results of experiments conducted for a year: “Our investigation has demonstrated that sewage can be disposed of anywhere that there is a vacant tract of land in the city without creating a nuisance and without any objectionable feature.” The total estimated cost for treatment will be about $9.14 per million gallons when the plant is run at the rate of 18,900,000 gallons per day. He estimates that the total cost for treatment by the Imhoff tanks and the sprinkling filters would be not less than $11 per million gallons.

After an extended investigation by their sanitary engineers, Armour & Company have concluded that the activated sludge method will satisfactorily purify the industrial wastes from their Packingtown factories. Assistant Superintendent, M. D. Harding, estimates that from data now available the cost per million gallons exclusive of depreciation, interest and repairs, will be $3.

When considering the applicability of this process to conditions in any city consideration should be given to the following points. The process requires competent supervision, which Mr. Hatton claims may be a blessing in disguise in view of the experiences of cities which, after having built disposal plants of various kinds, have left their operation to the kind mercies of Providence with disastrous results. This process also requires the expenditure for constant power. The cheaper the power the more adaptable the process is commercially; but if the unit is small and the power cost high, the operating cost may be too great. The sludge must be constantly treated to avoid nuisance. The process produces a high degree of purification. If the local conditions do not demand this the process might be too expensive in comparison with some other process which will produce a satisfactory effluent.

Other Processes

A few cities, including Oklahoma City and Santa Monica, Cal., have electrolysis treatment plants. The process consists in passing the sewage between a system of electrodes. The change is brought about by chemical reaction from newly formed chemical reagents produced by the decomposition of inorganic compounds already in solution. It is still regarded as an unestablished process.

Boston has within the last year been testing a new process of sewage purification invented and patented by a Boston chemist. By the addition of an acid, an attempt is made to precipitate the bulk of suspended matter and to form a sludge which can be dried and degreased thereby producing a salable and greaseless fertilizer as well as recovering valuable grease. Experiments by E. S. Dorr gave results so full of promise that arrangements were made for a study of the process under the supervision of the Sanitary Research Laboratory of the Massachusetts Institute of Technology. Robert Spurr Weston gives the results of this study in a recent issue of the American Journal of Public Health. His conclusions are that “with facts at hand the process would be very satisfactory for Boston from a sanitary standpoint, and is more promising economically than any other known method.” He includes in his comparison the activated sludge process. An experiment by Boston on a larger scale has been recommended.

Trade Wastes

Industrial trade wastes, such as those coming from canneries, breweries, woolen mills, laundries, dye and cleaning works, paper mills, iron foundries, gas works and packing establishments and others cause nuisances around disposal plants, and the problem of their proper disposal is more difficult of satisfactory solution than the treatment of domestic sewage. Some wastes can be treated with domestic sewage at the disposal works without any difficulty, others require special treatment before being allowed to enter the sewers and often it is desirable to keep certain wastes out of the main sewers and dispose of them independently. Each particular problem must be considered by itself with due regard both to conditions at the factory, the expense burden on the producer of the waste and to the body of water into which the effluent is to be discharged. There are instances where cities have reimbursed certain manufacturers for treating their wastes separately, and others where the manufacturers have reimbursed the city for the additional treatment required.

Sludge Disposal and Value

Authorities are generally agreed that the sludge problem is the center of the entire sewage problem, because it causes more trouble and is the most expensive part of the treatment. The method of handling it is just as important as the treatment of the sewage.

Wet sludge can be pumped out on land or into shallow places or it can be sent to sea in ships and allowed to sink. If pumped on land it must be spread out in very thin layers. If discharged into trenches it is ploughed into the ground after it has dried. In either case a large area of land is necessary and odors cannot be eliminated. Only cities located on or near the seashore can send their sludge to sea, and then the cost of disposal is rather high.

Sludge can be dried by pressing, in centrifugal drying machines, by mixing with some dry matter or by discharging upon drying beds. The cost of pressing is high, depending upon the amount of lime added, the kind of sludge pressed, and the size of the works. George S. Webster states that the average cost in large cities is ten cents per ton of wet sludge. It is especially applicable to chemical precipitation works as it must first be treated with lime or coal powder. When dried in machines the liquid contains much organic matter and is objectionable. The simplest method is to discharge the sludge upon drying beds of porous material and underdrained. The time for drying depends upon sewage treatment. Imhoff tank sludge will dry in less than a week, septic tank sludge in two weeks or more, and sludge from plain sedimentation will require about two months in summer and almost five months in winter. Cleveland, in order to overcome weather conditions at its experimental plant, built a covered sludge bed, modeled after standard greenhouse construction. The report from the Testing Station is that during summer the period of drying is approximately the same as or possibly a little longer than with open beds. Eliminating the three winter months, the station report says, it is possible to operate beds of this type so that one square foot of surface will dry 0.8 cubic feet of sludge per year. Francis E. Daniels suggests that sludge can be handled faster by drying a small portion at one time and removing it from the bed before the next portion is drained off.

Dry sludge can be used for fertilizer or for filling low lands or it can be incinerated. Its fertilizing value is disputed except when produced by the activated sludge method. The filling in method is economical. Authorities advise the consideration of incineration by cities which burn their garbage.

Dr. Imhoff’s recommendations are the use of sludge for agricultural purposes and for filling in low land. “In both cases,” he says, “the sludge must first be dried and this is best effected upon a drying bed after the sludge has been decomposed in an inoffensive, odorless manner, in a separate tank through which sewage does not flow.”

Many unsuccessful efforts have been made to extract the valuable ingredients from sewage, but to date the experience has been that they have been more costly to recover than they are worth. Dr. McLean Wilson, Sanitary Inspector of the West Riding of Yorkshire Rivers Board, believes that the valuable ingredients of sewage will ultimately be recovered and used since many capable experimenters are at work on the problem. H. W. Clark, Chemist of the Massachusetts State Board of Health, is of the opinion that sludge has some value and that “it seems inevitable that as the processes of drying, pressing and fat separation are improved and as nitrogen advances in price sewage sludge will become of greater agricultural value than at present.” Experiments have been made at the Philadelphia Sewage Testing Station by burning dry sludge and wet sludge mixed with fine coal. The results were unsuccessful. Experiments have also been made at the Cleveland station where it was found that the sewage sludge contained about one-half as much nitrogen and one-third as much phosphates as does the garbage tankage.

Management and Supervision

No matter how well a sewage disposal plant is designed or constructed it will not do its work in a satisfactory manner and produce desired results unless it is efficiently managed. Every plant should be in charge of a man who has knowledge of sewage disposal principles, is thoroughly familiar with his plant and who can act intelligently in an emergency. The New Jersey State Sewerage Commission in one of its reports notes the tendency of local authorities to permit the deterioration of disposal plants usually through inattention. “It cannot be too strongly urged on those charged with these, as of other public works, that a competent man in charge is a primary necessity and that the plant should be kept continuously in the highest state of efficiency.” The same condition is complained of by the California State Board of Health and other state organizations. In one of its bulletins the California State Board says that “some of the plants are operating very indifferently well and some very badly. The general situation shows plainly the need of expert advice to municipalities with respect to general methods and necessary efficiencies from some central authority.”

D. C. Faber, Industrial Engineer of the Iowa State College, goes so far as to claim that practically all nuisances in connection with plants can be traced directly to failure to give them attention. He says that even where plants have been found too small increased care in many cases could be made to offset lack of capacity.

In several states, such as New York, Pennsylvania, New Jersey, Kansas, Ohio and Massachusetts, the State Boards of Health have supervision over the designing of new plants and the operation of those established. The good results obtained as a result of this supervision are evidence that similar powers should be granted to all state boards of health.

With a plant designed to meet local conditions, properly constructed and efficiently managed, a city should have no difficulty in disposing of its sewage economically, in a sanitary manner and without creating a nuisance.

Table II (a)
 
SEWAGE DISPOSAL IN AMERICAN CITIES
 
Name of City General Data Sewerage System Sewage Pumping
Population General Description Plant Annual Cost of Operation[29] Gallons Treated Annually Average Number Gallons Treated Daily Per cent. of City’s Total Treated Kind of Sewerage System Preliminary Treatment What Percentage of Sewage is Pumped to Plant Gallons Pumped Annually Daily Capacity of Pumps Kind and Number of Pumps Annual Cost of Pumping Station Number of Feet Sewage is raised
Total Per Million Gals. Raised a Foot
Albany, N. Y. 110,000 Coarse screens, Imhoff tanks and pumping station.         Mostly combined Coarse screens and grit chamber. Large part. Three 10 M.G.D. each and three 15 M.G.D. each Three var. speed 24 in. and three const. 24 in. electric power.        
Atlanta, Ga. 200,000 Coarse screens, grit chambers, Imhoff tanks, sprinkling filters. $1.93 per M.G.X.   16,000,000 90%. Combined. Grate bars 1½ in. apart, and three grit chambers. Some. 50,000,000   Centrifugal electric power.      
Akron, Ohio 150,000 Screens, grit chambers, Imhoff tanks, sludge beds, sprinkling filters.         Separate and combined. Screens and grit chambers.              
Alliance, Ohio 22,000 Cameron tanks. Contact and intermittent sand filters. Imhoff tanks and slag contact beds now under construction. 2,200 per M.G.   3,000,000 100%. Separate. Grit chambers. None.            
Auburn, N. Y. 37,000 Two plants. Grit chambers, settling tanks, dosing tanks, contact beds. 8,500   675,000 22%. Separate with some surface water. Two grit chambers. None.            
Brockton, Mass. 63,000 Revolving screens, sand beds and sprinkling filters. 12,000 768,000,000 2,106,000 100%. Separate. Revolving screen. All.   6,000,000 Two Knowles triple expansion condensing steam power. $30,000 .975 40.
Bloomington, Ill. 12,000 Septic tank, center settling basin, 3 contact beds arranged around center basin, nozzle spray upon filter beds surrounding contact beds.   275,000,000 750,000 100%. Separate. Settling basin with weirs. None.            
Bristol, Conn. 15,000 Sand filter beds. 5,000   1,500,000 90%. Separate. None. None.            
Columbus, Ohio. 220,000 Grit chamber, screens, pumps, Imhoff tanks, sprinkling filters, final settling basins.   5,163,000,000 21,300,000 All for 242 days. Separate and combined. One in. and one-half in. vertical bar screens mechanically operated. Grit chamber. All once and 10% twice. 5,163,000,000 50,000,000 One 12 in. Worthington, one 20 in. Morris, two 18 in. and one 12 in. De Lavel. Electric power. $23,656 .16 21.6
Canton, Ohio. 70,000 Imhoff tanks, contact beds, crushed slag and gravel filter with automatic syphon, sludge drying beds, sand and pea gravel filling. Half of bed covered with greenhouse construction. Final effluent into creek. 20,000 700,000,000 1,900,000 95%. Separate. Coarse screens and grit chambers. None.            
Danbury, Conn. 23,000 Irrigation and filtration. 7,500   300,000   Mostly separate. Coarse screens and grit chambers. None.            
Dallas, Texas 120,000 Screens, grit chambers, Imhoff tanks and sludge beds.     10,000,000 All. Separate. Coarse screens and grit chambers. All.   22,500,000 Two centrifugal steam power.     42.
Fond du Lac, Wis. 20,000 Sewage collected in receiving well and pumped into Imhoff tanks. 3,200       Separate with cistern overflow connected with sanitary. Screens and grit chambers. All. 1,000,000 a day. 60,000,000 Four centrifugal electric power.      
Fresno, Cal. 40,000 Partial purification by settling and septic process, and disposal of effluent by irrigation of alfalfa. 1,000 1,825,000,000 5,000,000 All. Separate. Chamber for trapping crude oil. None.            
Gloversville, N. Y. 21,000 Primary and secondary settling tanks, screen chambers and dosing tanks, sprinkling filters, sludge drying beds and sand filters. 22,000 1,022,000,000 2,800,000 90%. Separate. Coarse screens. None.            
Houston, Texas 140,000 Activated sludge method, reinforced concrete aeration tanks, M.G. settling tanks and re-aeration tanks. Continuous flow, power houses and blowers. 9.25 per M.G. 6,570,000,000 18,000,000 All. Separate. Coarse screens and grit chambers for two-thirds of sewage. 105.2% some twice. 8,611,000,000 30,000,000 One air ejector six single centrifugal pumps. Electric power. $23,500 est. .136 .25.
Independence, Kas. 12,000 Cameron tanks and filter beds.         Separate.   None.            
Lackawanna, N.Y. 17,500 788,400,000 95%.         Separate. Grit chamber. 95%. 788,000,000 720,000 power. Centrifugal steam 9,000   18.
Milwaukee, Wis. 450,000 Trial plant operated since 1916. Now designing activated sludge plant to treat all sewage.     130,000,000   Separate with first wash from street. Coarse screens and grit chamber. 33%. 42,000,000 60,000,000 Three centrifugal, 20 million each. Electric power.     22.
Mt. Vernon, N.Y. 38,000 Settling tanks, single story septic type, constructed in five units. Sprinkling overhead Phelps nozzle, dosing tanks with automatic syphon. 17,675 750,000,000 2,000,000 75%. Separate with much wet weather infiltration. Coarse bar screens. 15%. 110,000,000 5,000,000 Two vertical centrifugal electric power.     26 ft. including friction.
New Britain, Conn. 55,000 Sand filtration. 12,000   4,000,000 All. Separate. None. None.            
Oswego, N.Y. 24,000               None.            
Pasadena, Cal. 42,000 Imhoff and septic tanks, sludge bed and sewage farm.   730,000,000 2,000,000 95%. Separate with first wash from street. None. None.            
Providence, R. I. 249,616 Settling tanks; disinfection. 54,954 9,078,620,000 24,872,000   Combined.   Yes.            
Philadelphia, Pa. 1,800,000 Pennypack Creek sewage treated   450,000,000 1,250,000 One-third of 1%. Combined first wash from street. Coarse screens and grit chamber. Yes. 450,000,000 4,000,000 One eight in. and one ten in. Worthington, vertical. By gas.     41.
Reading, Pa. 110,000   21,500 2,000,000,000 6,000,000 60%. Separate. Two grit chambers. All.   One 6 and the other 8 millions. Two centrifugal electric power. $14,500   39.
Rochester, N. Y. 248,465 Detritus tanks, fine screens Imhoff tanks. Plan made for effluent to run power plant. Sludge drying beds.     55,000,000 dry weather flow, 173,000,000 wet weather flow. All. Combined. Six detritus tanks and fine screens.              
Schenectady, N.Y. 87,000 Imhoff tanks and sprinkling filters. 23,000   72,000,000 70%. Separate and combined.   40%. 40,000,000 15,000,000 Five direct connected motor vertical centrifugal. $10,000   23.
Sumter, S. C. 12,000 Sewage only partly treated. A settling chamber only. No filtering bed. 8,000       Separate. Two grit chambers 20 x 30 ft. None.            
Tallahassee, Fla. 6,000 Single contact system, 3 beds, coke and sand, filtration with automatic apparatus. 2,500   100,000     Grit chamber. No.            
Woonsocket, R. I. 43,000 Screening basin and filters.     1,500,000   Separate. Coarse screens between screening basins and pump well. 100%.   2,200 per min. Centrifugal. By steam.     20⅓
Worcester, Mass. 170,000 Chemical precipitation, sand filters. 60,000 exclusive of depreciation and interest. 6,094,000,000   All dry weather flow and first part of storm water. Separate and combined. Grit chambers 2%.     Four centrifugal. Electric power. 5,509.35    
Table II (c)
 
SEWAGE DISPOSAL IN AMERICAN CITIES (Continued)
 
Name of City Industrial Wastes Sludge Disposal Final Treatment
Establishments Which Empty Wastes Into City’s Sewerage System What Kinds Are Treated Before They are Emptied Into Sewerage System Methods of Treatment Where Wastes are Purified Separately How is Sludge Disposed of Any Revenue from Disposal Plant Is Effluent Disinfected Is there a Secondary Settling Tank Per cent. of Suspended Matter Removed Per cent. of Bacteria Removed What Degree of Purity Required Is Plant Operating Satisfactorily If Not, Why? Distance of Plant from Center of City Any Odor at Plant
Albany, N. Y.           No.             Two miles.  
Atlanta, Ga. Steel mills, tin can works, gas works, coal and gas plants. From gas works. Plain sedimentation. Filling and fertilizer. None. No. No.       Yes.   4–7 miles. Not sufficient to cause inconvenience.
Akron, Ohio       Burned.     Yes.              
Alliance, Ohio       Dried on beds and hauled to farmers. None. No. No.       No. No technical supervision. Large quantities of roof water during storms. 1 mile. Yes.
Auburn, N. Y. None.         No. No.     Yes.   5 miles.    
Brockton, Mass. Shoe factory and tannery.     Fertilizer and fill. None. No. From sprinkl’r. 61.2. 95. As high as possible. Not entirely. Sand beds in operation 22 years and have reached capacity. 3 miles. During damp weather
Bloomington, Ill. No.         No.         Yes.   1½ miles. Not over 1,000 ft. under worst conditions.
Bristol, Conn.       Plowed into land             Yes.   2 miles. Not much.
Columbus, Ohio Tanneries, breweries, starch works, wool cleaners, packing plants. None.   Dried on beds and spread on city farm. None. No. Yes. 25. 80–90. Varies with stream and weather conditions. Some parts satisfactory others not. Insufficient capacity. 5 miles. Yes.
Canton, Ohio Various factories, including iron and steel; chief waste is rags. None.   Fertilizer.   None. No. 98.   85. Yes.   8 miles. Very little.
Danbury, Conn. Hat factories. None.   Fertilizer. $400. No. No.       Yes.   2½ miles. None from beds; sometimes when flow exceeds maximum it is turned into swamp, and during hot weather there is odor.
Dallas, Tex. Packing houses, laundries, dye works.         No.             3½ miles.  
Fond du Lac, Wis. Laundries, cleaning establishments. None.   Filling.     No.       Yes.   1 mile. No.
Fresno, Cal. Fruit canneries and packing houses. None.             30. No standard. Yes.   7 miles. Yes.
Gloversville, N. Y. Leather and canneries; 26% of total is trade waste. All. Settling tanks. Fertilizer and fill $300. No. Yes.       Yes.   2 miles. Some.
Houston, Tex. Pressed and dried         No. Yes. 95–98. 95–99. 85–90.     2.5 miles. None expected.
Independence, Kas.                            
Lackawanna, N. Y. None.         No. No.     90. Yes.   1 mile. No.
Milwaukee, Wis. Breweries, tanneries, soap works, laundries, hair works and packing houses. None.   Pressed, dried and sold for fertilizer.   No.   95. 95. 95.     Centre of city. No.
Mt. Vernon, N. Y.       Fill. None. No. No. 70. 80. Non-putrescible. Yes.   1 mile. A few days noticeable ¼ mile.
New Britain, Conn. Pickling liquor.     Fill. None. No.         No. Voids almost completely clogged by pickling liquor. 3 miles.  
Oswego, N. Y.                         ¼ mile.  
[31]Pasadena, Cal. Laundries.     Fertilizer. None. No.         Imhoff satisfactory septic “as well as can be expected of any septic tank.” 5 miles.    
Providence, R. I. Woolen mills, bleacheries, dye houses, jewelry factories.     Pressed and carried away on scows.     Yes.   Total bacterial 64%; B Coli 96.9.          
Philadelphia, Pa. No.     Fertilizer. None. Liquid Chlorine. Yes. 60. 100 acid formers. Absence of acid forming bacteria. Yes.   12 miles.  
Reading, Pa. Soap and dye works, tanneries, paper mills, breweries, laundries, hat factories, electroplating works.     Fertilizer. None. No. Yes. 71.1 exclusive of solids removed by grits. 86. State standard. Yes.   3 miles. Some at times of cleaning.
Rochester, N. Y.           Plans made for such.                
Schenectady, N. Y. Laundries, locomotive and electrical top of tanks.   Oil skimmed off Fill.   No. No. 40. 70.   Fairly so.   2½ miles. At first, but not now.
Sumter, S. C. None.       None. No.   Great Portion     No objection as it empties into swampy stream.   1½ miles. Slight as it empties at mouth of outfall.
Tallahassee, Fla. Chera Cola Works, and garages. None. All run into grit chamber before entering main.     No. Yes.       Yes.   1 mile. Only when cleaning grit chamber.
Woonsocket, R. I.           No. No. 100. 97.   Yes.   1 mile. No, except slight smell like dish water.
Worcester, Mass. Carpet mills, tanneries and dye works. None.   Fill and fertilizer. None. No. No. 87. No standard. Effluent from sand filter excellent; chemical precipitation poor.     3 miles. Very little.