Saturday, 30 March 2019

receiving water standards

RECEIVING WATER STANDARDS

In the context of wastewater treatment, the term, 'receiving water ' is defined as a stream, river, lake, ocean or other body into which wastewater or treated effluent is discharged. The Central Pollution Control Board (CPCB) under the environment protection rules of 1986 in schedule VI, has set "General Standards for discharge of environmental pollutants" as effluents as given below:
  1. Colour and odour 
  2. Suspended solids not to exceed 100 mg/l
  3. Particulate size of suspended particles should pass through 850 micron IS sieve
  4. pH value should lie between 5.5 and 9
  5. Temperature should not exceed 5 C more than receiving water temperature
  6. Oil and grease should not exceed 10 mg/l
  7. Total residual chlorine should not exceed 1 mg/l
  8. Ammonical nitrogen as (N) should not exceed 50 mg/l
  9. Total kjeldahl as ammonia should not exceed 100 mg/l
  10. Free Ammonia should not exceed 5 mg/l
  11. BOD for 3 days at 27C should not exceed 30 mg/l
  12. COD should not exceed 250 mg/l
  13. Arsenic should not exceed 0.2 mg/l
  14. Mercury should not exceed 0.01 mg/l
  15. Lead should not exceed 1 mg/l
  16. Cadmium should not exceed 2 mg/l
  17. Hexavalent chromium (Cr6+) should not exceed 0.1 mg/l
  18. Copper should not exceed should not exceed 3 mg/l
  19. Zinc should not exceed 5 mg/l
  20. Selenium should not exceed 0.05 mg/l
  21. Nickel should not exceed 3 mg/l
  22. Cyanide should not exceed 0.2 mg/l
  23. Fluoride should not exceed 2.0 should not exceed 
  24. Sulphides should not exceed 2.0 mg/l
  25. Dissolved Phosphates should not exceed 5.0 mg/l
  26. Phenoile compounds should not exceed 1 mg/l
  27. Radioactive materials
    1. Alpha emitter should not exceed  10^-7 mg/l
    2. Beta emitter should not exceed 10^-6 mg/l
  28. Manganese should not exceed 2 mg/l
  29. Iron should not exceed 3 mg/l
  30. Vanadium should not exceed 0.2 mg/l
  31. Nitrate Nitrogen should not exceed 10 mg/l

Sunday, 24 March 2019

Sludge calculations

DAILY SLUDGE PRODUCTION OF WASTEWATER TREATMENT PLANT



Terms used & their notation
  • Q  -      Wastewater flow rate (m3/d) (Influent flowrate)
  • So  -      Influent Soluble Substrate Concentration (BOD or bsCOD g/m3)
  • S   -      Effluent Soluble Substrate Concentration
  • Xo,i -   nbVSS concentration in effluent (g/m3 or mg/l)
  • iTSS -   inert inorganic Total Suspended Solids (g/m3)
  • XT    -  Total MLVSS concentration (g/m3 or mg/l)
  • SRT  -   Sedimentation Retention Time (d)
  • VSSo - Influent Volatile Suspended Solids
  • Px,T, TSS - Daily Sludge production kg TSS/d
    Px,T, VSS - Daily Sludge production kg VSS/d
  • Kinetic coefficients
    • k - maximum rate of soluble substrate utilization (g COD/g . d)
    • y - biomass yield (g VSS/g COD)
    • kd - endogenous decay coefficient (g VSS/g VSS . d)
    • ks - half velocity constant (g COD/m3)
    • fd - fraction of cell mass that remains as cell debries (g VSS/g VSS)

CASE STUDY
  • Q = 1000 m3/d
  • So = 192 BOD or bsCOD g/m3
  • Xo, i = 30 g/m3
  • iTSS = 10 g.m3
  • XT = 2500 g/m3
  • SRT = 6 d
  • k = 12.5 g COD/g . d
  • y = 0.4 g VSS/g COD
  • kd = 0.1 g VSS/G VSS . d
  • ks = 1 g COD/m3
  • fd = 0.15 g VSS/g VSS
DAILY SLUDGE PRODUCTION 
Px, T, VSS = 82.17  kg VSS/d 

Saturday, 23 March 2019

Outfall design

OUTFALL DESIGN

An outfall is an underwater pipeline that discharges wastewater into receiving water. Even if the wastewater has received extensive treatment, it is desirable to dispose the effluent to minimize possible impairment to quality of receiving waters near point of discharge by using a diffuser. 
A diffuser is a section of the outfall, usually deepest and most seaward portion with small holes or ports along its length. These ports discharge wastewater in small quantities as opposed to the entire flow being discharged at one point.
Diffuser ports may be simple holes in the outfall pipe or short tubes extending from the pipe. The type of port used depends upon particular conditions of final installation. The various elements of outfall design process are:
  • Site selection
  • Outfall hydraulics
  • Dilution and Mixing
  • Diffuser port design
  • Pipe design
  • Pipe support systems
  • Construction methods
The design is phased into four elements:
  1. Feasibility study
  2. Pre-design
  3. Preliminary design and
  4. Final design
The flow diagram illustrating how various design components and phases are integrated is depicted in the chart below:


Site selection:
  • Discharge port for an outfall should be located in proximity to its companion wastewater treatment plant.
  • First step in outfall design is to determine feasibility of linking treatment plant to nearest receiving water.
  • This involves study of:
    • Topographic maps
    • Hydrographic charts
    • Literature of coastal processes like tides, waves, currents and geology
    • Characteristics of the site and obtaining related water quality data related to proposed receiving water
  • If the information suggests that, from the construction cost and water quality point of view one or more outfall routes is feasible, the pre-design engineering studies are commenced to select a final route or an alternative disposal system must be considered.
The following outfall siting criteria are considered in detail in the pre-design stage:
  • Bottom topography and turf zone
  • Physical oceanography
  • Water quality and
  • Wastewater soils and geology
A hydrographic survey of the general area of the proposed outfall alignment is performed using an electronic recording echo-sounding device combined with horizontal positioning system. Helicopters may be used as sounding platforms. Subsequently, profiles of bottom topography are plotted. Analysis of profiles will reveal potential outfall routes. It is desirable to have a continually declining grade for the outfall line. This prevents potential sludge build-up in low parts and accumulation of air at high points which can reduce the hydraulic capacity of the outfall. There is no ideal slope for locating the diffuser. A relatively flat slope is desirable. The diffuser port should be designed such that there should be equal discharge from  each side of the diffuser. This results in equal dilution. A mild slope is beneficial for achieving uniform port discharge. 
Penetrating the surf zone is most expensive and difficult phase of constructing an ocean outfall because of continuous wave attack in shallow water.
Sporadic storms....

Friday, 22 March 2019

Important terms explained

IMPORTANT TERMS

  • Unit processes
    • Unit process refers to chemical conversion of reactants into desirable products. Ex: Oxidation, Nitration, Hydrogenation, desulphurization of sulphur, etc
    • In unit process there is no physical change but chemical changes occur
    • Unit process is secondary
    • Unit process involve both physical and chemical changes
    • Unit process is a chemical conversion of reactants into desired products.
  • Unit operations
    • Unit operations refer to separation of products by physical means.    Ex: Absorption, Adsorption, Distillation, Membrane separation, mixing, agitation, drying, quenching, evaporation, crushing, grinding, crystallization,  separation, etc
    • Each step is one unit operation and the entire process is unit process
    • In unit operations, no chemical changes but physical changes occur
    • Unit operations is a physical change
    • Unit operations need to be performed in unit process
    • Unit operations involve physical changes only
    • Unit operation is separation of products by physical means
Both unit processes and unit operations are transformatory activities
  • Biological unit process
    •  Biological unit process make use of microbes for removal of dissolved organic matter from wastewater. The two types of biological unit processes are:
      • Aerobic biological unit process and
      • Anaerobic biological unit process
    • Biological unit processes carry out treatment of wastewater by microorganisms in the presence (aerobic) or absence of oxygen (anaerobic)
    • Examples of aerobic processes are:
      • Activated Sludge Process
      • Trickling filters
      • Aerobic stabilization ponds and
      • Aerated lagoons
      • Rotating Biological Contactors
      • Oxidation ponds
    •  Examples of anaerobic processes are:
      • Anaerobic sludge digestion
      • Anaerobic contact process
      • Anaerobic filters
      • Anaerobic lagoons or ponds
  • Treatment system
    • The type of combination used from the available unit operations and processes for treatment of a particular waste is known as treatment system.
  • Primary treatment system
    • As per the ongoing technology, the wastewater treatment system that includes all units of the preliminary treatment system such as 'sump and pump house' , 'approach channel', 'bar screen', 'grit chamber', 'parshall flume or velocity control device', 'skimming tank' and the 'primary sedimentation tank' together are known as the primary treatment system
  • Secondary treatment system
    • The removal of colloidal and soluble organic content is carried out in the secondary treatment system consisting of an aeration basin with return sludge facility or a trickling filter and a secondary sedimentation tank is called a secondary treatment facility
  • Waste stabilization ponds (Oxidation ponds)
    •  Waste stabilization ponds are large, man-made water bodies in which black water or grey water or fecal sludge are treated by naturally occurring processes under the influence of sunlight, wind, microorganisms and algae. They may be aerobic, anaerobic or facultative each having different treatment and design characteristics. These ponds are low on operation and maintenance and have high removal rate for pathogens and BOD. They require large surface areas and special expertise in design of such systems. The effluent contains high amount of Nitrogen and Phosphorus and hence can be used for agricultural purposes but not for recharge of groundwater.
  • Oxidation lagoons (Aerated lagoons)
    •  Oxidation lagoons or aerated lagoons operate on the principle of the activated sludge process
    • It consists of an earthen basin in which wastewater is fed only after screening
    • The wastewater is treated with or without recycling of sludge
    • Oxygen required is provided by surface aerators or submerged diffuse aeration system
    • The system assumes complete mixing and the flow of wastewater is continuous
  • Oxidation ditches (Extended Aeration Systems)
    • An oxidation ditch is a modified activated sludge biological treatment process that utilises long solids retention time to remove biodegradable organics. Oxidation ditches are typically complete mix systems.
    • Oxidation ditches are suitable for areas where land availability is high.
    • They are easy to maintain and adapt easily to shock loads.
  • Rotating Biological Contactor (RBC)
    • Rotating Biological Contactors also known as Rotating Biological Filters are fixed bed reactors consisting of stacks of rotating discs mounted on a horizontal shaft. They are partially submerged and rotated as wastewater flows through. The microorganisms are alternately exposed to atmosphere and wastewater, allowing both aeration and assimilation of dissolved organic pollutants and nutrients thereby degrading the pollutants
  • Up-flow Anaerobic Filter (UAF)
    •  An Up-flow Anaerobic Filter (UAF) is characterised by long detention time and production of anaerobic effluent. It uses physical removal mechanisms like flocculation, sedimentation and absorption. Anaerobic digestion also occurs in the bed. The bed is generally filled with gravel.
  • Up-flow Anaerobic Sludge Blanket
    • Up-flow Anaerobic Filter is also known as  Up-flow Anaerobic Sludge Blanket Reactor. In this treatment process, a blanket of biologically formed sludge granules act as a filter through which the wastewater is passed where solid-liquid separation takes place. The separated settling solids return to the active blanket zone while the liquid passes over the weir as effluent. The waste solids get attached to the biomass  and are stabilized. The gas produced as a result of stabilization is collected.
    • This process is an important option for sewage treatment in warm countries
  • Tertiary or Advanced Treatment System
    • Tertiary treatment is the final cleaning process that improves wastewater quality before it is reused, recycled or discharged to the environment. The treatment removes remaining inorganic compounds and substances such as Nitrogen and Phosphorus
    • Bacteria, viruses and parasites which are harmful to public health are removed in this stage
    • Alum is used to remove additional phosphorus and group the remaining solids together for easy removal in the filters
    • Due to addition of alum, tiny particles cluster together in masses called floc.
    • Filters are back-washed every 24 hours to remove accumulated floc.
    • Chlorine contact tank removes microorganisms in tertiary treated wastewater
    • Remaining chlorine is removed by adding sodium bisulphite
  • Granular media filtration
    • Any process that removes suspended particles through a porous medium is defined as filtration
    • Granular Media Filters can be:
      • Slow sand filters
      • Rapid sand filters 
      • Granular media types:
        • Mono media - Silica sand
        • Dual media - Anthracite coal or Granular Activated Carbon
        • Multimedia - Garnet
  • Ultrafiltration
    •  Ultrafiltration is a type of membrane filtration in which forces like pressure or concentration gradients lead to separation through a semipermeable membrane.
    • Suspended solids and solutes of higher molecular weight are retained on the retentate while water and low molecular weight solutes pass through the membrane in the permeate.
    • Ultrafiltration can be used to remove particulates and macro-molecules from raw water to produce potable water.
    • It can replace secondary or tertiary treatment in conventional water treatment systems or can be used as a standalone system
    • It is sometimes integrated in water treatment systems in the pre-treatment system
    • After ultrafiltration, the recycled water can be reused for a number of industrial purposes like boiler or cooling tower feed, water supplementation, pH adjustment, washing equipment and vehicles, fire protection, process rinse water for production lines, toilet flushing, dust control, construction activities and concrete mixing
    • Industries that consume large volumes of water or discharge toxic effluents employ ultrafiltration for reusing water
    • Ultrafiltration is frequently used to pretreat surface water, sea water and biologically treated municipal water ahead of reverse osmosis unit
  • Micro-strainers
    •  
  • Biological nitrification/denitrification
  • Ion exchange
  • Air stripping
  • Chemical processes
  • Reverse osmosis
  • Electrodialysis
  • Chemical precipitation
  • Adsorption
  • Treatment process vs Treatment system
  • Population projection
  • Flow rates and their fluctuations
  • Mass loading
  • Design criteria
  • Hydraulic flow diagram
  • Total solids, suspended solids, Total dissolved solids, Volatile solids, Fixed solids, Miineral solids
  • BOD
  • COD
  • Surfactants
  • Oil and grease
  • Alkalinity
  • Chlorides
  • Total Nitrogen as N
  • Sulphur
  • Total Phosphorus as P
  • Alkalinity as CaCO3
  • Heavy metals
  • Strength of wastewater
  • Design period
  • Flow variations
  • Daily flow rate
  • Average daily flow rate
  • Maximum daily flow rate
  • Minimum daily flow rate
  • Dry Weather Flow (DWF)
  • Concept of mass load
  • Detention period or Hydraulic Retention Time
  • Flow through velocity
  • Settling velocity
  • Hydraulic Loading or Surface Loading Rate or Over Flow Rate
  • Weir Loading Rate
  • Volumetric Loading or Organic Loading (BOD or COD or VSS loading)
  • Food to Microorganism ratio (F/M) 
    • The ratio of incoming BOD to MLSS, the F/M ratio is also known as the loading on the system and is calculated as kg of BOD per day per kg of MLSS in the aeration tank.
       
    • If the F/M ratio is low and the aeration period or detention time (in the aeration tank) is long, the microorganisms make maximum use of available food, resulting in a high degree of treatment. Such systems are known as extended aeration systems and are mostly used for isolated sources (small developments).
       
  • Mean Cell Residence Time or Solids Retention time
  • Basin Geometry (L:B:D for rectangular tanks) or (Diameter & side water depth for circular tanks)
  • Reactor
  • Sizing of units
  • Operation units are normally designed at peak flows
  • Determination of surface area
  • Determination of cross-sectional area
  • Stoichiometry
  • Rate of reaction
  • Homogeneous reaction
  • Heterogeneous reaction
  • Rate of reaction
  • Effect of temperature on reactions
  • Treatment units (Reactors)
  • Types of reactors
    • CFSTR
    • PFR
    • BR
    • AFR
    • FBR
    • PBR
    • SBR
  • Reactors in series
  • Primary settling tank; Types of settling
  • Concept of biological treatment
  • Aerobic process
  • Anaerobic process
  • Facultative process
  • Anoxic process
  • Suspended growth process
  • Attached growth or fixed film process
  • Bio-kinetic coefficients (Growth constants)
    • Microbial growth rate
    • Substrate utilization rate
    • Limiting substrate
    • Endogenous decay
  • Significant bio-kinetic coefficients
    • Specific growth rate
    • Yield coefficient
    • Maximum Substrate Utilization Rate Constant
    • Half velocity constant
    • Endogenous decay coefficient
  •  Reactor biomass and biomass yield
  • BOD rate constant
  • CODtotal
  • CODb = 1.6 * BOD
  • BODu/BOD5 = 1.5 (for domestic wastewater)
  • Organic loading
  • Quantity of air required
  • Diffuse aeration system
  • Surface aeration system
  • Power required for oxygenation
  • Volatile Suspended Solids (VSS)
  • Mixed Liquor Suspended Solids (MLSS)
    • The combination of the liquid and microorganisms undergoing aeration is known as mixed liquor, and the suspended solids are called Mixed Liquor Suspended Solids (MLSS).

       
  • Mixed Liquor Volatile Suspended Solids (MLVSS) - MLVSS/MLSS = 0.8
  • Sludge Volume Index (SVI)
  • Sludge wasting
  • ----
The Hydraulic Retention Time is the average time the liquid remains in the reactor while the Solids Retention Time (SRT) is the average time the solids remain in the reactor. SRT is also known as Sludge Age or Mean Cell Residence Time.



In extended aeration ponds have a diverse ecology thereby creating little to no biomass leading to savings in operational costs.

Thursday, 21 March 2019

Overland flow systems


Overland flow systems 
 

In overland flow, wastewater is sprayed onto an inclined vegetated terrace and slowly flows to a collection ditch. Purification is achieved by physical, chemical, and biological processes, and the collected water is usually discharged into a nearby stream.

  • Overland flow systems are used to achieve secondary treatment effluent quality for effluents coming from primary treatment facilities.
  • Overland flow systems ensure high removal of Nitrogen(N), Suspended Solids(SS) and Biochemical Oxygen Demand (BOD)
  • Overland flow systems apply previously treated wastewater to a vegetation covered graded land
  • Application is done by grated pipes or nozzles at top of slope or by sprinkler systems within the site
  • It is best suited for impermeable soils
  • Overland flow systems require:
    • low permeability soils
    • grading within 2 - 8%
  • Overland flow systems use the following mechanisms for removal of BOD and SS:
    • Biological oxidation
    • Sedimentation
    • Filtration
  • 75 - 90% of Nitrogen is removed by:
    • Plant uptake
    • Denitrification
    • Ammonia volatalization
  • 70 - 90% of Phosphorus can be removed by addition of alum of ferric chloride prior to land application. Phosphorus is removed by:
    • Fixation processes in soil matrix
    • Crop uptake
Effluent is collected in ditches and can be reused or discharged to a surface water body.
The treatment goal of overland flow systems is secondary treatment of wastewater and Nitrogen removal. In order to achieve these objectives the system requires a warm season. At the end of overland flow systems the effluent will have following characteristics:
  • BOD < 10 mg/L
  • TSS < 10 mg/L
  • Total Nitrogen < 10 mg/L 

Wednesday, 20 March 2019

Rapid infiltration systems

RAPID INFILTRATION SYSTEMS

  • In the rapid infiltration method, the wastewater is in large ponds called recharge basins. Most of it percolates to the groundwater, and very little is absorbed by vegetation. 
  • To employ this method for treatment of wastewater, soils must be highly permeable. 
  • Rapid Infiltration (RI) is also called soil aquifer treatment. 
  • RI uses the soil ecosystem to treat wastewater. It can treat a large volume of wastewater on a much smaller area of land than other land treatment systems. 
  • In RI systems, wastewater is applied to shallow basins constructed in deep and permeable deposits of highly porous soils. 
  • Wastewater application can be by flooding or by sprinklers. 

  • Treatment of wastewater occurs by
    •  filtration
    • adsorption
    • ion exchange
    • precipitation and 
    • microbial action as the wastewater moves through the soil matrix.
    • Phosphorus and most metals are retained in the soil while toxic organics are degraded or adsorbed.
  • As wastewater percolates through the soil, it can be collected or it can flow to native surface water or groundwater aquifers. 
  • If the groundwater table is relatively shallow, underdrains can be used to control groundwater mounding and recovery of renovated water.
  • The recovered water can be used for irrigating crops or for industrial use (beneficial uses).
  • Water that is not recovered can be used for recharging groundwater aquifers. 
  • A major cause of concern is increased nitrogen levels in aquifers surrounding RI systems. 
  • In order to address these concerns, the following modifications have been suggested:
    • RI sites may be located next to rivers or other surface water bodies provided the percolate flows to surface water body and not affect the general groundwater quality
    • Designing the system in such a way that the discharge rate only slightly exceeds the percolation rate thereby preventing adverse impact on the surrounding groundwater
    • Maximizing nitrification/de-nitrification reactions
    • Recycling percolate with maximum nitrate concenration.
Advantages
  1. RI is a simple and low cost wastewater treatment concept that has been in use for more than a century
  2. It can be used for treatment of both primary and secondary effluent from domestic and industrial wastewater
  3. Industries such a breweries, distilleries, food processing plants, paper mills and wool scouring plants use RI process for treatment of their effluent.
  4. This technique can be used in a variety of climates and different site locations.
  5. RI process do not need any special seasons for effective implementation
  6. Unless groundwater recharge and recovery is required, desirable sites are located immediately adjacent to surface waters thereby minimizing impact on general groundwater quality
  7. An underdrain system can be located wherever suitable soil and groundwater conditions exist.
  8. It is a gravity distribution method and consumes no energy
  9. No chemicals are required
  10. It is not affected by seasonal changes
  11. Effluent is of excellent quality
  12. It is a reliable process with sufficient resting periods
  13. It can be used for groundwater recharge, controlling groundwater levels, recovering renovated water for reuse or discharge to a particular surface water body and temporary storage of renovated water in the aquifer.
  14. The process is suitable for small plants where operator expertise is limited.
Disadvantages
  1. RI systems do not meet the stringent nitrogen levels required for discharge to drinking water aquifers
  2. Requires long term commitment of land area for treatment with minimal secondary benefits
  3. Requires annual removal of accumulated deposits of organic matter on infiltration surfaces in the basins
  4. May require occasional removal and disposal of top few inches of soil to expose clean material
  5. Clogging can occur when influent is received at high application rates from algal laden facultative lagoons and polishing ponds.

Design Criteria
  1. Primary design criteria for an RI system is site selection
  2. To ensure a successful design, the important factors to be evaluated are:
    1. Soil depth
    2. Soil permeability and
    3. Depth to groundwater
The other factors to be considered after selecting a suitable site are:
  1. Hydraulic loading rate
  2. Nitrogen loading rate
  3. Organic loading rate
  4. Land area requirement
  5. Hydraulic loading rate
  6. Infiltration system design and
  7. Groundwater mounding
The RI process is entirely dependent on soil and hydrogeological characteristics at a particular site.
  1. The soil must have sufficient hydraulic capacity to allow the wastewater to infiltrate and then percolate and move either to groundwater or underdrains.
  2. The fine top textured soil must be removed from site to utilize the underlying coarse soils as the basin bottom and percolation media.
  3. The top 5 to 10 ft of soil beneath the basin must be unsaturated at start of flooding to allow the expected treatment to occur.
  4. The subsurface conditions should ensure that the percolate can flow away from the site at expected rates.
  5. An underdrain can be used to remove renovated water.

Vermiculture


Vermiculture

Vermiculture is the culture of earthworms. The goal of vermiculture is to continually increase the number of worms in order to obtain a sustainable harvest. Vermicomposting is the process of converting organic material into a humus-like material known as vermicompost. Production of vermicompost requires maximum worm population density all the time. However, to produce more worms, the population density should be low enough that reproduction rates are optimised. The worm Eisenia fetida commonly known as 'compost worm', 'manure worm', 'red worm' or 'red wiggler' is extremely tough and adaptable can be found wherever piles of manure have been left to age for a few months. The compost worm has a capacity for very rapid reproduction.

Advantages
  1. Vermicompost is superior to conventionally produced compost
  2. Worms can be used on farms as high quality animal feed
  3. Vermicomposting and vermiculture are potential sources of supplemental income to farmers
Disadvantages
  1. Rapid production of vermicompost requires more labour
  2. It requires more surface area as worms being surface feeders do not operate in material more than one meter deep
  3. Vermicomposting is more vulnerable to environmental pressures like freezing and drought
  4. Start-up resources in the form of initial investment, time and labour are required
Compost worms need:
  1. A conducive environment to thrive called 'bedding'
  2. Food
  3. Adequate moisture (>50% water by weight)
  4. Adequate aeration
  5. Protection from temperature extremes
'Bedding' provides worms with a stable habitat. It should have the following essential characteristics:
  1. High absorbency
  2. Good bulking potential
  3. High Carbon:Nitrogen (C:N) ratio
The bedding material may be made-up of 'peat moss', 'horse manure', 'Newspaper' or 'paper mill sludge'. Selection of bedding material is very important to successful vermiculture. Manures are the most commonly used feed stock. The bedding must hold sufficient moisture for the earthworms to thrive. Worms cannot survive in anaerobic conditions. Earthworms thrive in temperatures in the range of 20s(C). Such temperature ranges stimulate reproduction. However, they die in temperatures exceeding 35(C). Compost worms will redistribute themselves according to temperature gradient.
Worms can survive in the pH range of 5 to 9. Worms are very sensitive to salts, preferring salt contents less than 0.5%. Few toxic components to earthworms are:
  1. De-worming medicine in manure
  2. Detergent cleansers, industrial chemicals and pesticides
  3. Tannins
Earthworms in ideal conditions reproduce quickly. Worm populations double every 60 to 90 days. Ideal conditions being:
  1. Adequate food
  2. Well aerated bedding with moisture content between 70 and 90%
  3. Maintaining temperature between 15 to 30 C
  4. Initial stocking densities more than 2.5 kg/m2 but less than 5 kg/m2
Stocking density refers to the initial weight of worm biomass per unit area of bedding. Starting with a population density less than stocking density will delay the onset of rapid reproduction. Population density of worms greater than stocking density results in low reproduction as there is greater competition for food and space. The most common densities for vermicomposting are between 5 and 10 kg/m2. Worm growers tend to stock at 5 kg/m2 and tend to split beds when the density has doubled. Following these guidelines, growers can expect doubling of biomass in 60 days. Theoretically a stock of 10 kg of worms can become 640 kg in after one year and 40 tonnes after two years. The barriers in achieving optimum rates of reproduction are:
  1. lack of knowledge and experience
  2. lack of dedicated resources
  3. lack of preparation for winter
Rule of thumb is that one ton of input results in one cubic yard of compost.
The most common pests and diseases that earthworms are at a risk of are:
  1. Moles
  2. Birds
  3. Centipedes
  4. Ants
  5. Mites
  6. protein poisoning
The three basic types of vermicomposting systems are:
  1. windrows
  2. beds or bins
  3. flow-through reactors
  • Vermiculture focuses on production of worms rather than vermicompost.
  • Vermicompost can be used as a method for destroying pathogens.
  • Vermicompost spread on land does not cause contamination of ground or surface water.
  • Vermicompost binds nutrients well thereby preventing nutrient run-off from agricultural land and ultimately preventing eutrophication of surface waters.
  • There is potential for using compost worms in natural filtration systems.
  • One of the principal benefits of vermicomposting is 'carbon sequestration'.
  • Vermicomposting also addresses the issue of worldwide depletion of carbon in soils. By consistent application of compost or vermicompost an increased level of carbon in soil has been seen.
  • Worms aerate the matter as they move through it resulting in fewer anaerobic areas and reduced methane emission.
  • One unit of vermicompost is as effective as five to seven times of fertilizer in promoting plant growth and yield. Vermicompost is more efficient at retaining nitrogen.
  • Earthworms have a very important role in counteracting 'the loss of biodiversity'.
  • Vermicompost has a high potential value monetarily.
  • Vermicomposting and vermiculture are environmentally beneficial processes that have great potential as components of sustainable agriculture.