Landfill  Leachate Treatment
Landfill  leachate is generated from liquids existing in the waste as it enters a landfill  or from rainwater that passes through the waste within the facility. The  leachate consists of different organic and inorganic compounds that may be  either dissolved or suspended. An important part of maintaining a landfill is  managing the leachate through proper treatment methods designed to prevent  pollution into surrounding ground and surface waters
The  physical appearance of leachate when it emerges from a typical landfill site is  a strongly odoured black, yellow or orange coloured cloudy liquid. The smell is  acidic and offensive and may be very pervasive because of hydrogen, nitrogen and  sulfur rich organic species such asmercaptans. 
If  leachates have a distinguishing characteristic, it is that they are variable.   Flows change based on the weather  – increasing during rainy periods, decreasing  during dry and waste concentrations can change dramatically over the life of the  landfill.   As a result, no landfill leachate is constant over time, and no two  leachates are the same.
When  the landfill is a few years old the dominated fermentation phase is acidogenic  and the leachate generated is generally referred as “young”.In that case, COD  and BOD reaches very high concentrations. The ratio  of BOD/COD is higherthan 0.7 and pH is low due to the high concentrations VFAs.  Landfill grater than 10 years old aregenerally in the methanogenic phase and  theleachate generated is referred to as “old”. Duringthe methanogenic phase,  bacterias are degradingthe VF-acids and reduce the organic strength ofleachate,  leading to the pH value higher than 7.In “old” leachate BOD decreases faster  than CODand the radio BOD/COD is stabilized on the levelless than 0.2  [2,4].Anaerobic treatmentprocess is used mainly for young landfill  leachate,which BOD5 and BOD5/COD ratio is very high[2]. However, Kettunen, et  al. [10] performedthe treatment with UASB reactor were municipal landfill  leachate was having COD higher than800 mg × dm−3 and the BOD/COD radio washigher  than 0.3.Anaerobic processes of landfill leachate inUASB reactor allow complete  removal of CODfrom 65 to 76% and BOD5 removal beyond90%  [11].
 
Table  1
Characteristics  of landfill leachate   
Parameter  Value 
COD,  mg O2 × dm−3 3500–4200
BOD5,  mg O2 × dm−3 380–420 
pH  8.2–8.4 
Alkalinity  mg CaCO3 × dm−3 4900–5200 
Chloride  mg Cl−× dm−3 1800–2500 
Ammonia  nitrogen, mg NH4+× dm−3890–994 
VFA,  mg CH3COOH × dm−3 500–900
landfill  leachate  quantity , 5%
UNITS OF TREATMENT  OF LANDFILL LEACHATE:  
1.       Collection  Sump: Areas  in which rainfall is higher than average typically have larger sumps. A further  criterion for sump planning is accounting for the pump capacity. The  relationship of pump capacity and sump size is inversed. If the pump capacity is  low, the volume of the sump should be larger than average. It is critical for  the volume of the sump to be able to store the expected leachate between pumping  cycles. This relationship helps maintain a healthy operation. Sump pumps can  function with preset phase times. If the flow is not predictable, a  predetermined leachate height level can automatically switch the system on.  Other conditions for sump planning are maintenance and pump drawdown. Collection  pipes typically convey the leachate by gravity to one or more sumps, depending  upon the size of the area drained. Leachate collected in the sump is removed by  pumping.
2.     UASB  Reactor: 
3.      Clarifier  Tank :
4.     Clear  Water Tank:
5.      Activated  Carbon Filter:
LITERATURE  STUDY: WASTE TO ENERGY CONCEPTS
Energy  recovery as electric power is a feature of all waste-to-energy  systems.
Evaluation  of the applicability of the technologies of biomethanation,  gasification/pyrolysis,incineration and landfilling as Waste-to-Energy options,  and their comparison against composting as a competing technology for waste  disposal, has shown the following:
•  Biomethanation  has emerged as a favoured technology for various urban and industrial  waste.
•  Gasification/pyrolysis  have a distinct promise, and although there are limitations to its uptake, these  can be overcome as the technology matures.
•  Incineration  is a mature technology for energy recovery from urban and industrial wastes and  has been sucessfully commercialized in the developed countries. The recent focus  has been on environmental compliance due to which it will become an expensive  option.
•  The  present trend is in favour of material recovery facilities and a shift away from  landfills for MSW  disposal in developed countries.
•  Compositing  is not a WTE option and does not come out as worthwhile waste treatment  process.
•  Technologies like  landfill with gas recovery and composting can become viable options for certain  locations in India, as a short to medium term  option.
 
Landfill  Leachate Treatment Technologies
Landfill  leachate may be characterized as a water-based solution of four groups of  contaminants ; dissolved organic matter (alcohols, acids, aldehydes, short chain  sugars etc.), inorganic macro components (common cations and anions including  sulfate, chloride, Iron, aluminium, zinc and ammonia), heavy metals (Pb, Ni, Cu,  Hg) , and xenobiotic organic compounds such as halogenatedorganics,  (PCBs, dioxins,  etc.).[4] 
Leachate  treatment technologies fall into two basic types, biological and  physical/chemical. In larger systems and depending on the treatment goals,  integrated systems which combine the two are often used.
The  typical processes used for pretreatment include equalization, aeration, pH  adjustment and metals removal.
The  most common biological treatment is activated sludge - a suspended-growth  process that uses aerobic microorganisms to biodegrade organic contaminants in  leachate. With conventional activated-sludge treatment, the leachate is aerated  in an open tank with diffusers or mechanical aerators. After the aeration phase,  the mixed liquor of microorganisms and leachate is pumped to a gravity  clarifier.
The  rotating biological contactor (RBC) is an attached-growth, aerobic, biological  treatment process in which a series of discs are partially submerged in a tank  of leachate. The disks eventually develop a slime layer, then rotational shear  forces strip off the excess solids and carry them with the effluent to a  clarifier, where they are settled and separated from the treated  waste.
The  carbon technique removes dissolved organics from the leachate. Although carbon  systems may be useful with some older leachates, the cost of the carbon in the  regeneration stage can make the process one of the most expensive treatment  options.
Advanced  Treatment The new landfill regulations have made some treatment systems  obsolete. Many landfill operators are now choosing new systems that produce a  cleaner effluent and can reduce capital and operating expenses. Such systems  include:
*  Recirculation and Injection. Direct recirculation distributes the leachate onto  the landfill in a semi-closed loop process. While promising, this system has  limitations of recirculating 100 percent of the leachate without literally  soaking the landfill.
*  Membrane Solution. Membrane technology can be adapted to many steps of  purification and keep clean-up standards at a high level. Membranes can remove  contaminants without extensive biological infrastructure or toxic  chemicals.
*  Reverse Osmosis (RO). Prior to 1988, reverse osmosis wasn't able to treat  leachate successfully due to the core membrane design of spiral-wound modules,  which were state-of-the-art at that time. While this method produced efficient  results, it also promoted bio-fouling and premature  clogging.
Disc  Tube technology, developed by the Rochem Group, has been installed in more than  35 European landfills to treat feed waters that would foul conventional RO  configurations. After the contaminated water is fed into the tubular chamber,  its flow is controlled as it passes through a system of discs and over flat  membrane cushions, removing clean water and concentrating the waste material.  The turbulent flow reduces the membranes' tendency to scale or foul and requires  cleaning less frequently.
The  system removes heavy metals, suspended solids, ammonia and hazardous  non-degradable organics including pesticides and herbicides without extensive  pre-treatment systems. The pure water is clean enough for direct discharge into  the environment and accounts for 75 to 92 percent of the leachate. The remaining  concentrate can then be recycled to the landfill or further  processed.
Siemens  Water Technologies' PACT®  systems combine biological treatment (activated sludge) with adsorption  (powdered activated carbon) so that physical and biological treatment occur  simultaneously. The system removes biodegradable and non-biodegradable  pollutants in a single process
The most cost  effective form of treatment for high levels of BOD, COD and ammonia is  intense biological  oxidation, and in the UK the sequential batch reactor is  the most common technology used. The sequence batch reactor (SBR) is a form of  activated sludge treatment.
Granular  activated carbon, in combination with biological pretreatment, is a proven and  economical technology which is effective in reducing Chemical Oxygen Demand  (COD), Adsorbable Organic Halogens (AOX), pesticides, solvents, organic  compounds and other toxic substances to the strictest legal National and EC  norms. The chemical composition and content of landfill leachate can vary  greatly between landfill sites. The age of the landfill, type of waste and  treatment processes already in operation are the parameters to be  considered.
COD  levels can range from 200mg/l to 2000mg/l. Carbon consumption is normally  dependent upon the COD adsorption rather than the AOX. Therefore COD will be the  determining factor in estimating carbon consumption.
However,  an aerobic system must be used after the UASB reactor for the effluent to meet  the standards defined for the proposed disposal  method.
 
Combined  treatment of leachate from sanitary landfill and municipal wastewater by UASB  reactors
This  study showed the potential of anaerobic treatment in an UASB reactor treating a  combination of domestic wastewater and leachate in a 5% volumetric ratio of  leachate. Under these conditions the reactor assimilated properly the leachate  fraction incorporated. With a HRT  of 8 h and a mean volumetric organic load of 2.84 kg m(-3) d(-1) COD removal  efficiencies around 70% were obtained,
When  installing a leachate treatment system, choose a plan that will provide the  maximum amount of long-term flexibility to assure compliance with future  regulations and discharge standards.
LEACHATE  RECYCLE  CONCEPT :The major  objective of gas studies is directed towards maximizing production rates of gas  by biodegradation of the waste while simultaneously reducing the period of time  that gas is evolved by recycling leachate. It describes potential means of  managing both leachate quality and quantity by leachate recirculation to aid in  decomposition of the waste while also treating the organic material in the  leachate and reducing the quantity of leachate that must be treated and hauled  away from the site.