Lagoon Design and Management For Livestock Waste Treatment and Storage

Prepared by:
James C. Barker
Professor and Extension Specialist
Biological and Agricultural Engineering
North Carolina State University, Raleigh, NC

Published by: North Carolina Cooperative Extension Service

Publication Number: EBAE 103-83

Last Electronic Revision: March 1996 (JWM)

The trend away from small dispersed livestock production units to larger specialized operations has increased management requirements for manure and wastewater. Utilization systems which conserve fertilizer nutrients often are more sophisticated, expensive and laborious for handling concentrated manure. Systems which pretreat manure for management ease usually result in a loss of fertilizer nutrients. Waste handling systems must meet water quality regulations, i.e., pollutants must not be discharged from livestock operations directly into surface waters. Economically feasible methods for treating livestock manure for stream discharge do not currently exist.

Lagoons became popular for livestock manure treatment as historic interest to utilize fertilizer nutrients by direct land application was replaced by desires to have more convenient systems for manure management. Originally viewed as a total disposal system; it is now recognized that in moisture excess regions, lagoons are one pretreatment process in an overall manure management plan. North Carolina has an annual rainfall surplus of about 18 inches in the mountains, 6 inches in the piedmont and 8 inches in the coastal plain. When the interior surfaces of the lagoon have biologically sealed, lagoons usually fill to capacity with wastewater and rainfall surplus after two or three years. When the filling process is complete, overflow will occur unless the operator is equipped to apply the excess liquid back to field crops, grassland or woodlots.

Definition Table 1 distinguishes lagoons for biological waste treatment from other common earthen waste storage structures. Lagoons act as digesters in which two major types of bacteria decompose organic matter into gases, liquids and sludge. Anaerobic bacteria, present in the intestinal tract of warm-blooded animals, do not survive in the presence of free oxygen. Aerobic bacteria require free elemental (dissolved) oxygen.

Advantages Lagoon systems for treatment of livestock waste are used because of:



Anaerobic lagoons are most commonly used for livestock waste treatment. Anaerobic bacteria can decompose more organic matter per unit lagoon volume than aerobic bacteria and are predominantly used for treatment of concentrated organic wastes. Since the anaerobic process is not dependent on maintaining dissolved oxygen, lagoons can be much deeper and require less surface area. Anaerobic decomposition of livestock waste can result in the production and emission of odorous gases, primarily hydrogen sulfide, ammonia, and intermediate organic acids. An anaerobic lagoon can be properly sized and managed, however, to operate with a minimum of disagreeable odor.

Table 1. Characteristics of Earthen Waste Treatment and Storage Structures

Waste   Earthen          Structure            Solids Handling Method
Type    Structure        Function            Content 
Semi-   stacking with    temporary storage    10-15% box-beater; side delivery
solid   liquid drainage                              flail; V-box expeller

Semi-   earthen basin;   temporary storage     4-12% liquid tank spreaders;
liquid  underfloor pit;                              hose-drag injection;
(slurry)above ground tank                            slurry irrigation

Liquid  primary lagoon   biological treatment    <4% sprinkler irrigation secondary lagoon temporary storage <1% sprinkler irrigation retention pond temporary storage <2% sprinkler irrigation ______________________________________________________________________________ 

Design Capacity Liquid volume, rather than surface area, is the basis for anaerobic lagoon design. Sizing criteria should emphasize major operational needs to control odor, minimize sludge buildup and manage nitrogen. As lagoon capacity increases, odor potential, rate of sludge buildup and pathogenic organisms decrease while nitrogen losses increase. Because bacterial activity increases at higher temperatures, lagoons work best in areas without cold winters. Lagoons in colder areas require more design treatment volume. Table 2 gives suggested livestock lagoon design treatment capacities for North Carolina.

The liquid capacity of an anaerobic lagoon (Table 2) should include the appropriate design treatment capacity, storage for accumulated sludge, and temporary storage for rainfall and wastewater inputs. In addition to this liquid capacity, surface storage for a 25-year, 24-hour rainfall (5 to 8.75 inches) and an additional foot of freeboard to prevent embankment overtopping should be provided. Table 2 estimates livestock lagoon liquid accumulation rates. These figures do not include fresh water inputs for flushing or lot surface drainage into the lagoon. Wastewater storage capacity should be figured for 180 days. Average high 180-day rainfall excesses in North Carolina range from 7 - 32 inches. Sludge accumulation rates given in Table 2 should be utilized to design the lagoon life expectancy.

Anaerobic lagoons are not used for treatment of cattle wastes without prior manure solids settling, separation or removal. Cattle wastes have a higher percentage of relatively nondegradable fibrous material which significantly increases the solids buildup rate in a lagoon.

Shape Lagoons may be round, square, rectangular, or irregularly shaped to fit existing terrain provided the perimeter does not contain unusually deep bays or pockets. Length-to-width ratios for rectangular lagoons should not exceed 4:1 to encourage even distribution of waste. Sideslopes generally vary from 1:1 in clay soils to 3:1 in sandy soils. A minimum liquid depth of 6 feet should always be maintained in an anaerobic lagoon. Maximum depths are dictated by soil and groundwater site constraints but may range up to 20 feet to minimize the surface area and to encourage dissolution of anaerobic gases. A level lagoon bottom is desirable but not absolutely necessary.

Site Investigation A site investigation by an agency with expertise similar to the Soil Conservation Service should be made to determine the soil characteristics and suitability for lagoon construction. Location on highly permeable soils which will not seal or shallow soils over high water tables or fractured or cavernous rock may allow groundwater contamination. Most properly planned livestock lagoons receiving raw manure eventually seal limiting soil permeability to as low as 10-6 cm/sec. The sealing mechanism is mainly physical, i.e., organic solids are trapped within soil pores at the soil surface. Biological mechanisms also help bind manure solids to soil particles thus strengthening the seal. Chemical constituents of manure such as sodium also tend to disperse soil particles. The predominance of professional opinion suggests that with proper initial site selection livestock lagoons have low potential for groundwater contamination.

Table 2. Livestock Anaerobic Lagoon Design Criteria

Animal                Unita  Average Lagoon Contents Lagoon Liquid Capacity
Type                         Animal   Accumulation
                              Live   _______________________________________
                             Weight  liquidb sludgec minimum  mean   maximum
                               lbs   gals/day ft3/yr   ft3     ft3     ft3
Dairy                per head 1400    25.5    260     1400    2100    4200

Beef                 per head  800     8.3    110      600     900    1800

Veal                 per head  200     2.5     29      150     225     450

  weanling-to-feeder per head   30     0.6      2       30      60      90
  feeder-to-finish   per head  135     2.7     10      135     270     405
  farrow-to-weanling per sow   433     8.8     23      433     866    1300
  farrow-to-feeder   per sow   522    10.6     28      522    1044    1566
  farrow-to-finish   per sow  1417    28.7    115     1417    2833    4250

Poultry, layer       per bird    4.0   0.07     0.63    10.0    12.5    15.0
       , pullet      per bird    1.5   0.03     0.22     3.8     4.7     5.6

a One-time animal or bird capacity.
b Does not include fresh flush water.
c No manure solids removal prior to lagoon input.

Management Figure 1 outlines a lagoon management scheme. New lagoons should be filled one-half full with water before waste loading begins. Start-up during warm weather and seeding with bottom sludge from a working lagoon will speed establishment of a stable bacterial population. Manure should be added to anaerobic lagoons as frequently as possible, preferably at least daily. Infrequent shock loadings can cause sharp increases in odor production and wide fluctuations in nutrient content. Lagoon liquid drawdown by irrigation should begin when the liquid reaches the maximum normal wastewater storage level. Liquid should not be pumped below the design treatment level so that adequate volume is always available for optimum bacterial digestion.

An anaerobic lagoon in proper balance will have a pH ranging from 7 - 8 (slightly basic). The pH in new lagoons without adequate dilution water or in overloaded lagoons can be reduced to 6.5 or less (acidic), thereby creating odor problems. This condition can be temporarily corrected by evenly distributing agricultural lime (preferably hydrated) to the liquid surface at the rate of one pound per 1000 cubic feet of lagoon volume.

Land Application Lagoon liquid should be land applied through irrigation equipment when it reaches the maximum normal wastewater storage level. Substantial amounts of nutrients can be provided to grassland, cropland, or woodlots, with application rates based on matching the available nitrogen content of the lagoon liquid to the fertilizer requirement of the crop. Nutrient concentrations vary widely among different lagoons and within individual lagoons seasonally. Applicators are strongly encouraged to periodically have lagoon samples analyzed to more accurately determine the amount of nutrients being applied. The NCDA Plant Analysis Lab analyzes waste samples for primary and micronutrients for a nominal fee. Table 3 gives typical characteristics of anaerobic lagoon liquid in lieu of actual test results.

Irrigation Equipment Liquid from lightly-loaded anaerobic lagoons can be applied through sprinkler nozzles 1/4-inch or larger. Single-nozzle, straight-bore sprinklers are recommended. Pump suction intakes should be floated approximately 18 inches underneath the lagoon liquid surface. Liquid from moderate to heavily loaded lagoons can be applied through 1/2- to 3/4- inch nozzles. Larger gun-type sprinklers with 3/4- to 2-inch nozzle diameters should be used for lagoons with high concentrations of solids or liquid sludge irrigation. Low-pressure systems in the 20 psi range with either high-rate or rotary impact nozzles less than 1/4-inch diameter are not recommended.

Table 3. Livestock Anaerobic Lagoon Liquid Characteristics

Animal              Total  Chemical Oxygen  Nitrogen      Phosphorus Potassium
Type               Solids   Demand (COD)    Total    NH3N       P2O5       K2O
                     %wb        mg/L       ---------lbs/acre-inch-------------
Dairy    mean       0.55        4100          137      88         77       195
         std. dev.  0.42        3000           72      25         50       122

Beef     mean       0.55        3200           83      45         77       129
         std. dev.  0.37        1400           39      16         67        45

Veal     mean         -           -            56      34         10        82
         std. dev.    -           -             -       -          -         -

Swine    mean       0.37        2100          136     111         53       133
         std. dev.  0.21        1500           70      14         35        79

Poultry ,mean       0.47        2800          179     154         46       266
         layer    std. dev.     0.27         1700      92         13        26

For solids contents under 4%, standard centrifugal irrigation pumps are recommended over specialized chopper pumps or cutter attachments. If a lagoon contains an appreciable amount of long-stemmed vegetation or large debris, this material should be removed and efforts made to prevent its recurrence. Pump power requirements for lagoon liquid are similar to those for water provided the solids content is less than 4%.

Sludge Removal Even with good bacterial digestion, significant amounts of sludge accumulate in an anaerobic lagoon. A lagoon can be designed for whatever sludge storage period desired (Table 2 and Figure 1). The rate of sludge buildup can be reduced by mechanical solids separation or gravity settling of the waste prior to lagoon input. This practice is particularly recommended for cattle wastes containing a high percentage of relatively nondegradable lignin and cellulosic fiber.

At some point the treatment capacity of most lagoons will be severely diminished by sludge accumulation. Table 4 presents some characteristics of livestock anaerobic lagoon sludge. Organic nitrogen compounds and phosphorus tend to accumulate in the sludge causing nitrogen levels up to 13 times higher than lagoon liquid levels and phosphorus up to 55 times higher than liquid levels. In addition to higher nutrient levels, the bottom sludge may also contain significant concentrations of heavy metals, salts and other trace elements. These factors dictate the need to have the sludge analyzed and expert agronomic advice sought prior to land application.

Lagoon sludge solids contents range from 6-13 % requiring careful selection of removal equipment. The most frequently used method consists of vigorous mixing of the sludge and lagoon liquid using a chopper-agitator impeller pump or pto propeller agitator. The sludge mixture is pumped through a large bore gun-sprinkler slurry irrigation system onto cropland followed by soil incorporation. Another alternative consists of partial lagoon dewatering followed by sludge agitation and finally pumping the slurry mixture into a liquid manure spreader for field spreading. A third alternative is lagoon dewatering followed by dragline dredging. The sludge may be hauled and applied directly to cropland by spreaders equipped to handle slurries, or stockpiled near the lagoon and allowed to further drain before spreading.

Solids Separation Lagoon management is eased by separating solids from raw or flushed manure prior to lagoon input. Removing fiber from cattle wastes and grit from poultry manure significantly reduces the lagoon solids buildup rate and associated pumping problems. Removal of oxygen-demanding solids in swine and poultry manure reduces the lagoon organic loading and lessens its odor potential. Beneficial uses of the recovered solids include bedding materials, supplements to animal feed rations, composting, and soil amendments.

To recover a relatively dry by-product, vibrating-screen, sloping stationary screen or pressure-roller mechanical separators are probably most advantageous. Waste is collected in a sump sized to store 3 - 4 days accumulation of manure plus dilution and flush water. A submersible or stationary bottom-impeller, agitator-lift pump mixes the waste into a slurry and pumps it across the separator where the liquid drains into the lagoon. Solids are dry enough to be handled by conventional materials handling equipment. Up to 30% of the total solids and 25% of the oxygen-demanding materials are removed.

Table 4. Livestock Anaerobic Lagoon Sludge Characteristics

Animal             Total Chemical Oxygen Nitrogen         Phosphorus Potassium
Type               Solids Demand (COD)   Total       NH3N       P2O5       K2O
                    %wb       mg/L       -----------lbs/acre-inch------------
Dairy     mean        6.1     23000        398        162        607       214
          std. dev.   4.1     16000        311        113        633       152

Beef      mean       11.4     51000       1037        464       1390       396
          std. dev.   5.8     26000        340        304        588       142

Swine     mean       13.0     81000        609        150       1340       193
          std. dev.   8.4     61000        360         44        965       133

Poultry , mean       11.0     13000        706        221       2510       341
  layer   std. dev.   5.7       -          223        116        908       202

A gravity settling basin may be less costly while removing 50% or more of the solids from liquid manure. Solids can be settled and filtered by a shallow basin (2 - 3 feet deep) with concrete floor and walls and a porous dam or perforated pipe outlet. It should allow access by a front-end loader to remove solids every 1 - 2 months. An alternative is an earthen settling basin for 6 to 12 months storage of solids. For flushed swine manure at least 0.55 gallon capacity per 135 pounds animal live weight per day of storage should be provided. The basin top width should be no more than 100 feet with a length-to-width ratio near 3:1 and a liquid depth of 8 - 10 feet. The basin contents should be thoroughly agitated and removed for land spreading either by liquid manure spreader or slurry irrigation. A third alternative consists of a large rectangular metallic or concrete settling tank with a 3:1 length-to-width ratio and an 8-feet liquid depth. Tank volume depends on a peak-flow wastewater detention time of 10 to 30 minutes. Most readily settleable solids in livestock manure settle in about 10 minutes although some additional settling occurs for hours. Tank inlets and outlets are baffled and solids are removed by automated skimmers and scrapers.


Naturally Aerobic (Oxidation Ponds) The main advantages of aerobic lagoons are that bacterial digestion tends to be more complete than anaerobic digestion with relatively odor-free end products. In naturally aerobic lagoons, oxygen diffusion occurs across the water surface. Algae also generate oxygen through photosynthesis which takes place when sunlight can penetrate the water depths. Water depths are rather shallow ranging from 3 to 5 feet. Because of the need for oxygen transfer, naturally aerobic lagoons are designed on the basis of surface area rather than volume. The USDA Soil Conservation Service recommends a maximum daily loading rate of 50 pounds of biochemical oxygen demand (BOD5) per acre of lagoon surface. Using these design criteria, Table 5 gives the amount of surface area required to maintain naturally aerobic lagoon conditions. Vast amounts of land are required for naturally aerobic lagoons - as much as 25 times more surface area and 10 times more volume than an anaerobic lagoon 10 feet deep. Thus, naturally aerobic lagoons are impractical for primary oxidation and are generally not recommended for treatment of livestock production wastes.

Mechanically Aerated Mechanically aerated lagoons combine the odor control advantages of aerobic digestion with relatively small surface requirements. Aerators are used mainly to control odors in sensitive areas and for nitrogen removal at limited land disposal sites. Aerated lagoons have successfully met these objectives by providing enough oxygen to satisfy 50% of the waste chemical oxygen demand (COD) assuming an aerator oxygen transfer rate of 3 pounds per horsepower-hour. The lagoon liquid surface should not exceed 1000 square feet per horsepower of aeration for floating surface aerators to insure complete surface influence. Liquid depths should be at least 10 feet. Table 5 gives mechanically aerated lagoon design criteria for livestock.

Table 5. Livestock Aerobic Lagoon Design Criteria

Animal                  Animal    Average   Naturally       Mechanically
Type                    Unita     Animal     Aerobic       Aerated Lagoon
                                   Live      Lagoon    ______________________
                                  Weight     Surface    Surface    Aeration
                                              Areab      Areac    Horsepowerd
                                    lbs        ft2        ft2         hp
Dairy                  per head   1400       2030       104         0.10
Beef                   per head    800       1150        44         0.044
Veal                   per head    200        180         6.3       0.0063
  weanling-to-feeder   per head     30         80         1.7       0.0017
  feeder-to-finish     per head    135        350         7.8       0.0078
  farrow-to-weanling   per sow     433        745        17         0.017
  farrow-to-feeder     per sow     522        900        20         0.020
  farrow-to-finish     per sow    1417       3660        82         0.082
Poultry, layer         per bird      4.0       11.5       0.32      0.00032
       , pullet        per bird      1.5        4.3       0.12      0.00012

a One-time animal or bird capacity.
b Loading rate = 50 lbs BOD5/surface acre/day; mean liquid depth = 4 ft.
c 1000 ft2/hp of aeration and a minimum liquid depth = 10 ft.
d 50% satisfaction of waste COD and oxygen transfer rate of 3 lbs/hp-hr.

A major disadvantage of mechanically- aerated lagoons is the expense of continually operating electrically-powered aerators. One large North Carolina producer determined the cost of aerator operation in 1979 to be $0.70 per feeder pig sold. Larger anaerobic lagoons may provide similar performance with less expense. Aerated lagoons also yield more sludge than anaerobic units because more input organics are converted to biomass. Suspension of bottom sludge by the aerators can cause increased lagoon liquid concentrations and stimulate foaming. Solids traps such as a septic tank type settling chamber between primary aerated and secondary lagoons can provide a convenient mechanism for solids collection and removal. Mechanically-aerated lagoon liquid nitrogen levels are significantly reduced.


Two-stage lagoons provide certain advantages over single primary lagoons. More than two lagoons in series is rarely beneficial. Secondary lagoons provide temporary storage prior to land application. Aerobic systems need a second lagoon to provide storage and allow the primary lagoon to function solely for biological treatment. A second stage also allows a maximum liquid volume to be maintained in primary anaerobic lagoons for stabilizing incoming wastes. For livestock operations which recycle lagoon liquid for open-gutter flushing where animals have direct access to flush water, a second lagoon provides some insurance against disease organisms being returned from the primary lagoon before a reasonable die-off period. Pumping from a secondary lagoon reduces the solids pickup common in primary lagoons due to seasonal water turnovers and biological mixing.

Sizing of secondary lagoons is not clearly defined or critical. North Carolina recommends that the second lagoon have 180 days of wastewater storage generated as indicated in Figure 1 plus enough volume for the combined 25-year, 24-hour rainfall storage from both lagoons.


Not Included:

Distributed in furtherance of the Acts of Congress of May 8 and June 30, 1914. Employment and program opportunities are offered to all people regardless of race, color, national origin, sex, age, or disability. North Carolina State University, North Carolina A&T State University, U.S. Department of Agriculture, and local governments cooperating.
EBAE 103-83