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E n e r g y R e c o v e r y T e c h n o l o g y

IIEPL [Innovative Industrial Equipent Pvt Ltd] is pleased to present A PRACTICAL SOLUTION TO WASTE CONVERSION.

Complete Conversion of Waste into Energy Products using (Proprietary) ERT TECHNOLOGY

The Technology converts waste to Liquid Hydrocarbon, SYNGAS and PETCOKE in an environment friendly manner, thereby producing commercially viable products from waste.

Date:

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http://www.iieindia.tradeindia.com/


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1: EXECUTIVE SUMMARY IIEPL is - • Advisor to Government of Uttrakhand for Waste Conversion

projects.• Advisor to CSRI for assessment and implementation of waste

conversion projects. • The Waste treatment technology ERT (Energy Recovery

Technology) is the property of IIE Pvt. Ltd.. IIE Promoter Mr.

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Ravi Nafde is known as a pioneer of Design & Engineering for Energy Recovery Plants. He is a degree holder in Architectural Design from VRCE (now known as VNIT), Nagpur and has also pursued Industrial Design from IIT Powai, Mumbai

• ERT, a breakthrough technology, has been closely vetted and assessed by the R&D Department of Indian Oil Corporation. The technology has been successfully demonstrated to Pollution Control Board Authorities in Uttar Pradesh, Uttarakhand, Goa and Maharashtra for conversion of BIO-MEDICAL WASTE and UNSEGREGATED SOLID MUNICIPAL WASTE.

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2: TECHNOLOGY DESCRIPTIONFLOW CHART

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Segment A – Receipt and Preconditioning of Waste Segment B – Processing of Waste Segment C- Collection of By-products Segment D – Safe Handling and Storage of By-products NO Further Waste or Effluent Water is not a part of the process and can be reused

3. COMPLETE DISPOSAL OF WASTE EXAMPLE

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PROCESS IS CHEMICAL REACTION AND NOT BURNING• THERE IS NO PARTICULATE MATTER IN THE EMISSION. THE

EMISSION IS ONLY BURNED GASES.• THE MAXIMUM TEMPERATURE REQUIREMENT IS 350°C TO

500°C HENCE VERY LOW ENERGY IS CONSUMED• NO EMISSIONS UNDER THE CONTROLLED OPERATIONAL

CONDITIONS.

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6. EMISSION STANDARDS Suggested Air Quality Emission Standards

Under Environmental Protection Act, 1986Incinerator ERT

Particulate Matter 150 Nil Hydrochloric Acid [Mist] 5 0.3 – 3.0 % prior to

scrubbing

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Benzene 10 0.3 – 1.2 % Carbon mono-oxide [CO] 1% max Nil

Lead 10% Nil Formaldehyde 2 Nil Methane 25 8 -20 %Ethane 100 15 – 25 %

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7. PLANT PROCESS OUTPUT & USES OF THE BY-PRODUCTSThe ERT System produces:-Liquid FuelGas FuelPet Coke

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Executive SummaryState Government and the municipal corporations of various cities in India are undergoing a

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heavy crisis for waste disposal. The authorities are geared up for the collection of the waste but are unable to destroy/ eliminate dispose off the waste, which eventually is becoming a grave issue as the quantum and magnitude is increasing in geometric proportion.

As per the scope of work and intensity, Innovative Industrial Equipment Pvt. Ltd. [IIEPL] submits a proposal for an integrated approach in-line with the guidelines of MoEF / CPCB and MSW rules 2000 and the proposal submitted to the –

1. State Government of Uttra Khand for the legendary temple town of Kedarnathji,

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Rudraprayag, Uttrakhannd.2. State Government of Assam for the legendary temple of Kamakhya, Guwahati,

Assam.3. State Government of Uttar Pradesh for the legendary temple of Kashi Vishwanath,

Banaras, Uttar Pradesh.4. Mapusa Municipal Council, Mapusa, Goa.5. Ratnagiri Municipal Council, Ratnagiri Maharashtra.6. Uran & Panvel Municipal Council, Maharashtra.7. Waste plastics conversion for Lucknow, Nagar Nigam, Lucknow, Uttar Pradesh.

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8. Bio Medical Waste Conversion to SGPGI, Lucknow, Uttar Pradesh.9. Bio Medical Waste Conversion to Doon Hospital, Dehradun, Uttrakhand.

In pursuance of the implementation of CDP, this document is prepared as detailed proposal for elimination of solid waste, plastic waste without segregation. While preparing this report, we have tried to evolve a complete system in shape of a model for the effective management and with a vision of Clean Environment.

This proposal addresses the issues of conversion of waste, bio degradable and non

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biodegradable waste, mixing of waste in the water stream due to non conversion, silting of waste in the water bodies due to non disposal, leeching of the soil and pollution of underground water reserves thereby, enhancing the environment and aesthetics, preservation of historic structures as archeological assets, pollution abatement, community participation and public awareness and lastly revenue generation activities for the sustainability of the mechanism as follows –

1. Livelihood creation for people in the small town. 2. Clean environment as over 75 – 80 % of the total waste generated shall be collected.3. Use of ergonomic tools for managing waste. 4. Use of appropriate technology for waste disposal / conversion, also creating

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entrepreneurship opportunities.

There has been a significant increase in municipal solid waste (MSW) generation in India in the last few decades. This is largely because of rapid population growth and economic development in the country. The per capita of MSW generated daily in India ranges from about 100 gm in small towns to 500 gm in large towns and over 500 gms per person at tourists places. The increased MSW generation can be ascribed to our changing lifestyles, food habits and change in living standards. In India the amount of waste generated per capita is estimated to increase.

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This proposal shall serve as a guide for the coordinated resource development and management of environment. It shall consider data on the scope of development adequate for initial public use and an estimate of future requirements. It also presents an inventory and assessment of the land and water resources and related physical improvements, an analysis of resource use and a re-evaluation of existing and future needs required to protect and improve the values of the resource base.

This DPR has been prepared in accordance with guidance contained in the following:

A. MSW Rules 2000

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B. National Environmental Policy, 2006

Objectives of the Project:

Objectives for the proposed development are decided with consultation with concerned authorities and are as follows,

Assessment of environment: Assessment of present status of town with the help of detailed survey and data collection, collection of air & water sample for air & water

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quality monitoring. Identification of factor responsible for degradation of environment leading to global warming.

Desilting and weed control: Desilting will increase the water retention capacity of the water bodies. Storage of water is a crucial step of DPR program while considering natural factors. Control on aquatic weeds will encourage good water quality and control eutrophication. In addition this will keep check on pollution and soil erosion in the vicinity of lake.

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Restoration of natural ecosystem: The foremost step of the DPR is restoration of natural ecosystem of the town by waste disposal. Flourishing flora and fauna will require maintenance of critical micro and macro habitats in and around the town. Gradual sloping of the landscape will provide the riparian zone. Introduction of native tree species will provide good nesting sites for the birds.

Restoration of wild life habitats: Aforestation and restoration of wildlife habitats.

Increase in the aesthetic value of town and its surroundings: Town restored to its natural ecosystem will itself add to the aesthetics of the surrounding.

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Pollution Abatement Practices: The Town faces many anthropogenic problems. It gets polluted due to unsolved environmental issues of anthropogenic activities. Using bioremediation measures, town will be treated.

Suggestion on revenue generation activities: Last but not the least; a due consideration is given to the revenue generation activities through waste disposal. These considerations make the project sustainable.

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Background of 98



of theTechnology

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It our privilege to introduce, a technology for safe disposal of Solid Waste for the eco sensitive zones. We have been working on the safe disposal of Municipal Waste, Household Waste, Hotel & Restaurant Waste and Bio - Medical Waste and have demonstrated the technique to the various government authorities and statutory bodies such as Pollution Control Boards [Lucknow, Goa, Uttra Khand] of various states as one of the options for the Safe Disposal of Waste.

We are giving a brief report on the technology for the safe disposal of Bio Medical Waste, with the advantages of the system over the presently available technologies [incineration].

E R T [Energy Recovery Technology] of 98



Typical ERT plant performance is as follows - The process temperatures can be as high as 700° C for destroying infectious waste with no CO & CO2 emissions [there is no burning of the waste]. Process exit temperatures are less than 50° C.

Waste VOLUME reduction of 60% - 90% depending on the type of waste. The amount of residue Carbon black [Coke] on a WEIGHT basis is as high as 10% - 40% of the input.

E R T Emission systems now satisfy current EPA emission requirements.

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Conventional Waste Disposal [Incinerator] plants did not have adequate emission control devices and had very high emissions and gave the industry a bad reputation. Most plants have either upgraded their emission control systems or have been forced out of business.

Conventional Waste Disposal [Incinerator] plants still produce high levels of tars, dioxins, furans and char when compared to the air emissions from ERT plants.

Conventional Waste Disposal [Incinerator] plants processes can only produce steam and electricity, whereas the Hydrocarbon Gas [synfuel] from a gasification process can be used for many other applications.

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E R T plants prevent the release of new greenhouse gasses.

E R T plants prevent the release of tons of methane into atmosphere, assuming the same amount of trash is disposed in a landfill without methane recovery.

Most Waste Disposal facilities require some form of pre-sorting. In order to reduce the volumes of ash, inorganic are sorted out. They cannot handle all types of waste as the E R T does.

E R T plant has following equipment line:

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Raw material handling sectiono Shreddero Loading Conveyorso Lock feed system

Reactor Scrubbing and condensation system Condensers Receivers Hydrocarbon gas cleaning & burning system

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Oil storage system Hydrocarbon Gas cum diesel fired heating system Filtration and De-waxing system Cooling tower, Chillers, Pumps, Vacuum pump and other utilities Control Panel and alarm systems The System is microprocessor controlled, allowing

one individual to operate one processing reactor systems, including loading and temperature controls

Flue gases monitoring and disposal stack

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OUTPUT PRODUCTAt the end of process, polymer & Organic waste is converted into following products Mixed oil Carbon Black Hydrocarbon Gas [Syngas] Metal & non organic waste mixed with carbon black

TYPICAL INPUT- OUTPUT RATIOInput Waste Material Input Output

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Quantity

Mixed Wastes and other organic matter, including food waste, flowers, coconut shells, and fiber, paper, incense sticks, tec..

5000 Kgs

1000 1300 – above moisture 500 - 1000 lt of Industrial Fuel 1000 - 1500 Kg of Petroleum Gas 1500 - 2000 Kg of Carbon black &

Coke with other non plastics and non decomposable matter [Metal, Steel etc.]

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ERT advantages over Incinerators

SN Incinerator ERT

1.The incinerator shall be designed for capacity more than 50 kg/hr

Can be designed for any capacity

2.For 50 kg/hr capacity, the minimum hearth area shall be 0.75 sq. m (8 sq. feet)

For 50 kg feeding the feeding bin size is large, the plant size is less than 8 sq ft

3. The minimum flow of the flue gas in the There is no restriction on the flow of flue

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secondary chamber shall be 0.6m3/sec at 1050°C

gases as they are directly burned

4.Each incinerator must be installed with an air pollution control system

No pollution control system is required. Control systems are provided for monitoring and feed back

5. The size of the opening through which the waste is charged shall be larger than the size of the

Size of the bin only matters/ the plant is fed continuously @ 0.8 kg a minute and

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waste bag to be fed controlled by the feed material available

6.The volume of the primary chamber shall be at least five times the volume of one batch.For 50 kg primary chamber volume is 1.5 CUM

1 kg is equivalent to 500 ltr of gas at atmospheric pressure. Hence the chamber size is only 0.5 CUM

7.Minimum 100% excess air shall be used for overall design

No air is required. There is no burning of material in ERT

8. The refractory lining of the chamber shall be All the critical components are of SS and

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strong enough to sustain minimum temperature of 1000° C in the primary chamber and 1200° C in the secondary chamber

sustain higher temperature

9.The refractory & insulation bricks shall have minimum 115 mm thickness each & conform to IS:8-1983 & IS:2042-1972 respectively

Refractory bricks are brittle and required periodic changing. Ceramic insulation is used externally for insulation

10.The waste shall be fed into the incinerator in The waste is charged in shifts and fed into the

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small batches after the fixed interval of time plant continuously and automatically

11.

The Incinerator shell shall be made of mild steel plate of adequate thickness (minimum 5 mm thick) & painted externally with heat resistant aluminum paint suitable to withstand temperature of 250°C with proper surface preparation

The complete plant is of Stainless Steel requiring no surface maintenance. The Mild steel corrodes and cause accidents. The Stainless Steel do not corrode and hence accident proof

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12.The waste is manually charged in to the primary chamber of the incinerator.

The waste is charged in a bin and not handled manually

13.During the charging the operator is directly exposed to the furnace atmosphere

There is no direct exposure all operations can be monitored remotely

14.The device shall prevent leak age of the hot flue gas & any backfire

There is no reason to cause back fire. As the process is chemical reaction and not burning

15.Chimney / stack shall be as per IS:6533-1989 Chimney or stack is required for outlet of

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and shall be treated to avoid corrosion due to oxygen and acids in the flue gas

burned gases. Hence there is no Oxygen and Acids in the flue gas

16.The heat recovery system / heat exchanger is an additional cost if considered

The heat recovery system and energy recovery is inbuilt with the system. Hence no additional cost is involved

17.Hot flue gases include CO, CO2 and O2 from burning of the waste

Hot flue gases include CO, CO2 and O2 from burning of Hydrocarbon gases methane,

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ethane, pentane etc.Hence more eco friendly

18.

The heat input capacity of each burner shall be sufficient to raise the temperature in the primary and secondary chambers as 800±50°C and 1050±50°C

The maximum temperature requirement is 350°C to 500°C hence very low energy is consumed

19.Most incinerators do not comply with the There is no particulate matter in the

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emission limit of 150 mg/Nm3 (corrected to 12% CO2) for Particulate Matter

emission. The emission is only burned gases

Current DevelopmentsThe prospects and promises of the technology are phenomenal. We have demonstrated the

technology at SGPGI, Lucknow, by invitation of Uttar Pradesh Pollution Control Board & SGPGI authorities. The pollution control board authorities have taken the deep interest in the demonstration and looking at the advantages of the process have recommended the same to the SGPGI authorities.

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We have also demonstrated the technology at Vasco, GOA, by invitation of Department of Science & Technology, Goa State Pollution Control Board & Goa Energy Development Authority, Goa.

We are giving the table of chronological milestones achieved:-

5 to 7th March 2003

Trials and test runs on the mixed variety of Waste Plastics were tested by Indian Oil Limited at their Faridabad R & D Center.

9th March U.N.I. reported an exciting development from Nagpur. Fuel from hydrocarbons

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2003 locked in plastics. It is just rearranging a few bonds which ultimately results in the conversion of waste plastics into Energy.

June 2003 Trials and test runs on the variety of mixed and hazardous Waste Plastics were tested by Indian Oil Limited at their Faridabad R & D Center.

2004 India’s first ever Waste Plastic to energy plant was designed by IIE under close supervision of IOL R&D.

2005 India’s first ever Waste Plastics to energy plant was commissioned by IIE.

2007 Sixty two years after gaining independence, India faced with a lack of electricity in

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the countryside as only 30% of rural Indian households have access to sustained electricity supplies.

Early 2008 However, with India's economy growing at around 10% a year, the staggering financial outlay needed for the energy sector across the country to maintain such a growth pattern has prompted significant reforms.

16th & 17th October 2008

Energy Recovery Technology [ERT] is a truly sustainable waste management solution, diverting plastic waste from landfill and incinerators, utilizing the embodied energy content of plastics and producing a highly usable commodity

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that, due to its cleaner burning characteristics, is in itself more environmentally friendly than conventional fossil fuel was demonstrated at UREDA [Uttara Khand Renewable Energy Development Agency], Dehradun on the request from Hiltron [A State Government Organisation].

22 to 24th October 2008

Energy Recovery Technology [ERT] is a truly sustainable waste management solution, diverting plastic waste from BMW was demonstrated to SGPGI [Sanjay Gandhi Post Graduation Institute, Lucknow] and UPPCB [Uttar Pradesh Pollution Control Board], utilizing the embodied energy content of plastics and producing a highly usable commodity that, due to its cleaner burning characteristics, is in itself

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more environmentally friendly than conventional fossil fuel.

16 to 20th December 2008

Energy Recovery Technology [ERT] is a truly sustainable waste management solution, diverting plastic waste from MSW & BMW was demonstrated to DST [Department of Science & Technology] at MES, Vasco, Goa.

2009 Two ERT plants for MSW & two ERT plants for BMW are proposed by Hiltron at Uttarkhand.

One ERT Plant for BMW at SGPGI Hospital is proposed under the advice of UPPCB, Lucknow.

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One ERT Plant for BMW at GMC [Government Medical College] Bambolin, Goa is advocated by GEDA [Goa Energy Development Agency]

2012 One ERT Plant proposed in DPR and sanctioned by Lucknow Nagar Nigam, Lucknow Uttar Pradesh. 23 July 2012.

One ERT Plant proposed for the tourist township of Lonar [Known for its meteoric lake formation]

One ERT plant proposal for JSW Bellary is in process.

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Plant Specifications of 98



SAMPLE SPECIFICATIONS OF THE SETUP FOR SOLID WASTE CONVERSION

ParticularsFeed SectionMIXED WASTE Shredding / Sizing system / Storage binHopper - standard : 0.25 m³, Rotor diameter : 450 mm, Motor power: 5 kW, Rotor speed : approx. 50 - 5 rpm, Connected load : 400 V +/- 5 % / 50 Hz, Electrical control system Standard equivalent, Star delta starter, Anti - vibration foundation, V-Rotor with knife pockets, Type of knives : Concave ground reversible cutting knives (40x40mm), Super - Cut adjustable counter knife for maximum reduction of the cutting gap Offset rotor bearings, Stand alone Covered Day Bin : 1250 kg capacity two Nos. of MS, Electrically operated valve, Regulated discharge, Level sensor, Online weighing system, 2 No. 1 HP Vibrator Motors,

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ParticularsSupport Structures.Process EquipmentFeederType : Hardened Annealed screw Feeder, Service Continuous, Capacity : 10-60 kg/Hr., Position Horizontal, Pressure :10 kg/cm2, Speed : 2-5 m/sec, Length of Feeder : 2500 mm, Motor HP : 1&2 HP, Reduction Gear Worm type, Power Supply 200/240 / volts, 1 phase. 50 c/s, Insulation : Ceramic Wool, Cladding : SS, Support Structure.Reactor VesselRun / Day : 24, Material Characteristics Highly viscous Materials of construction : SS-306 &

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Particulars316, Insulation : Ceramic Wool, Feed rate : 10-60 kg/hr. Inlets & Outlets : Pressurised inlet from electrically heated screw feeder, Gaseous vents, Thermo couple wells, Non Plastics [Solid, metal & glass] and Coke extraction outlet. Output Rate : Hot Hydrocarbon Gases 5 – 40 kg/hr, coke and non plastic contents 1-10 kg/hr, Water cooled mechanical controls for continuous operations, Pressure Vessel : 0.0 –1.0 kg/cm2 , Temperature Vessel : 275 - 400 °C, Heating Load [oil startup & generated gas Electricity] : 10.0 kW [peak], Process Product : burned organic material, 15 – 30 kg/day, moisture, other gases, By product gas 20.0-30.0 kg/day, Material holding time 90-120 min, Insulation : Ceramic Wool, Cladding : SS, Supporting Structure

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ParticularsRecovery SystemInsulated piping for Hot Hydrocarbon gases handling, Cooling tower, hot gases Cooling condenser and gases separator, Moisture trap, gas Feeding system, Liquid storage and measuring set up. Liquid fuel storage and feeding system, Liquid fuel/diesel and PDF burner, PDF Gas burner.Feeder Catalyst with storage hopperType : Hardened Annealed screw Feeder, Service Continuous, Capacity : .015-0.150 kgs/Hr., Position Horizontal, Pressure : 2.0 kg/cm2, Speed : 0.01 m/sec, Width : 25 mm, Length of Feeder : 400 mm & 750, Motor HP : 0.25 HP & .5HP, Reduction Gear Worm type, Power

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ParticularsSupply 220/240 /volts, 1 phase .50 c/s, Skirting Supporting StructureStorage SectionStorage Tank LHCCoated after NDT / SR, Fabricated together and hydro-tested to IS 10987, Cast Steel Mountings, Nozzles, Lugs, Fill Connection, Dip Connection, Vent Connection, Piping, Flanges, Nuts & Bolts, Calibrated to IS 2009.Storage Tank Waste O/pCoated after NDT / SR, Fabricated together and hydro-tested to IS 10987, Cast Steel Mountings, Lifting Lugs, Vent Connection, Piping, Flanges, Nuts & Bolts and Calibrated to IS

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Particulars2009.Piping & AccessoriesElectric Resistance Welded Steel Pipes and tubes, Continuous cast, Fine Grain Low Carbon, High strength and corrosive resistance, High deformability and toughness, Max Pressure: 16 kg/cm², Modulus of rupture: 39 kg/mm², Tensile Strength : 20 kgf/mm², Stress relieved, Double flanged. BlowersCapacity about 100 cum/hr, Steel frame with air outlet and filter sacks, Fan type 0.5 kW, Drum diameter 200mm, Pipes diameter 75 mm, Mount rings and sealing, Emergency

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Particularsswitch.Chimney / exhaust [Optional]6.0 M High 75 mm Dia., Stand alone MS flue gases discharge, Support structure.Electrical, Power & Analytical SectionControl PanelConvenient display 3-digit LED display, Liquid level indication in inches / centimeters / or percent, A front panel switch, Electrical Control, Power Supply Unit, Contactors MCB, ELCB, Rotary Main Switch, Power ON/OFF Lamp, Terminal Connectors and Accessories, LCD Display Unit door mounted on the panel, Over Current Trip Feature is included, Controls /

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ParticularsDisplays Electrical Safety System preset, trip, and calibration in field. Inlets & Outlets.Compensating CableTwo core Instrumentation cables for Control wiring and cabling.A.C. Drive and controls0.183 KW, Supply frequency: 50/60Hz, Displacement Power Factor : [>0.98], Switching on input supply 1.1, 1.2, 1.3, 2 times /min, Digital input, Analog input, Pulse/encoder inputs, Digital outputs, Analog outputs, Control cards, Relay outputThermocouple / Thermocouple PID / Thermocouple Well / Pressure GaugeSimplex/Duplex as per IS, Range from - 200°C to + 1800°C in various designs. Variety of

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Particularsprotection sheaths like M.S. SS304, 316, 321, 446, (HRS), Nickel, Wrought Iron.Miscellaneous Hardware / Cable TrayCable / Wire, Electrical Material, C.I. Rose & S.T. Saddle switchgears, main switch, ELCB, MCB, capacitors, Control panels, fire retardant grade, 9600 Glow Wire Tested, Fully insulated, Miscellaneous electrical hardware and sub systems, protection devices etc. IS 309-3, IEC: 1989, Range:10A, 20A For Single Phase (2P+E), 250 V, 20A, 30A for Three Phase (3P+E), 440V

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ANALYSIS OF OUTPUT 0BTAINED FROM SOLID WASTE INDIAN OIL - COMPOSITIONAL DATA OF GAS ANALYSED

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Technology & Process

Plant Specification

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The plant and equipment classified as De-Polymerisation plant version V1.5 with Energy Recovery Technology [ERT] and design copyrights for the recovery of energy from Bio Medical Waste, first of its kind continuous plants with following technologies. The De-Polymerisation plant and equipment version V1.5 / installation are manufactured / performed by M/S Innovative Industrial Equipment Pvt. Ltd., Nagpur. No other make or model, process is available for this Design / Technology.

1. Feeding system

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The said disadvantage is overcome in the proprietary design by designing a continuous feed system operating under pressure at preheated temperature of 150 to 200 °C recovered from the burnt flue gases, avoiding the drawback the slide valve heating and waste burning. The waste feed is directly fed to the reactor, thus consequences of waste burning due to the high temperature is avoided. The problem of waste feed drop onto the closing surfaces of the lower valve is eliminated, thus in an extreme case the escaping of gas is prevented.

2. Oxygen trap and burning of the waste

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The new design of pressure feed mechanism avoids such blockages thereby ensuring the oxygen free environment in the system ensuring maximum conversion of the waste in to hydrocarbons and carbon black.

3. Whole waste feeder and shredded feederThis problem is avoided by using shredded material. This simplifies the material handling and the feeding system to be automated for a uniformly sized feed material.

4. Reactor Design

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The new design of the reactor is horizontal is wherein the continuous feed charging mechanism comprises an pressure feeding system operating at 150-200 °C. The pressure charging mechanism is advantageous, because it simply ensures the feed-in of the shredded waste at positive pressure and protection against gas leakage.

5. Heating systemThe new design of the reactor allows the burner heat at the extreme end of the horizontal reactor and tangentially placed allowing the temperature to rise towards the entry in gradation which is essential for the mixed waste feed.

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6. Residue removalThe new design of the reactor wherein the continuous residue removal feed charging mechanism comprising of volume reduction and screening of non hydrocarbon materials operating at 350-400 °C. The pressure mechanism is advantageous, because it ensures total conversion of the waste in the process and maximum conversion of the hydrocarbon.

7. Inorganic waste removalTo solve the residue removal problem volume reduction of the residue and introduction of the mechanical removal of the residue and lowering down of the removed residue is essentially embodied. This ensures the safe removal of the residue consisting of carbon

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black and non hydrocarbon contents of the waste feed. This ensures continuous removal of the residue.

The designs shall be soon patented for process innovations and technology used in the ERT process equipment.

Our endeavor to refine the system continues, for truly sustainable Waste to Energy Solution, diverting non organic and non recyclable Waste from Municipal Solid Waste, Bio Medical Waste, Industrial Waste and utilizing the embodied energy content and producing a highly

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usable commodity Fuel, that due to its cleaner burning characteristics, is in itself more environment friendly than conventional methods of waste disposal.

Design Specifications for version V1.4 [Design Specifications are proprietary and are subjected to change and improvement]

SN Particulars1. Can be designed for any capacity 2. For 50 kg feeding the feeding bin size is larger than the plant size [less than 8 sq ft]3. There is no restriction on the flow of flue gases as they are directly burned

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4.No pollution control system is required. Control systems are provided for monitoring and feed back

5.Size of the bin only matters/ the plant is fed continuously @ 0.8 kg a minute and controlled by the feed material available.

6.1 kg is equivalent to 500 ltr of gas at atmospheric pressure. Hence the chamber size is only 0.5 CUM

7. No air is required. There is no burning of material in ERT.8. All the critical components are of SS and sustain higher temperature.

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9.Refractory bricks are brittle and required periodic changing. Ceramic insulation is used externally for insulation.

10. The waste is charged in shifts and fed into the plant continuously and automatically.

11.The complete plant is of Stainless Steel requiring no surface maintenance. The Mild steel corrodes and cause accidents.The Stainless Steel do not corrode and hence accident proof.

12. The waste is charged in a bin and not handled manually.13. There is no direct exposure all operations can be monitored remotely.

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14.There is no reason to cause back fire. As the process is chemical reaction and not burning.

15.Chimney or stack is required for outlet of burned gases. Hence there is no Oxygen and Acids in the flue gas.

16.The heat recovery system and energy recovery is inbuilt with the system. Hence no additional cost is involved.

17.Hot flue gases include CO, CO2 and O2 from burning of Hydrocarbon gases methane, ethane, pentane etc. Hence more eco friendly.

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18.The maximum temperature requirement is 350°C to 500°C hence very low energy is consumed.

19.There is no particulate matter in the emission.The emission is only burned gases.

20.

FRAME: The frame is constructed of structural steel. Whenever the size of the module is not suitable for transportation by road, the modules shall be dismantled and reassembled at site. The frame shall be suitably painted and would be ready to be installed on the foundation.

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21.MATERIALS OF CONSTRUCTION: Materials of construction of all the equipment handling process fluids shall be SS-306 & SS-316.

22.

Control Panel: Convenient display 3-digit LED display, Liquid level indication in inches / centimeters / or percent, A front panel switch, Electrical Control, Power Supply Unit, Contactors MCB, ELCB, Rotary Main Switch, Power ON/OFF Lamp, Terminal Connectors and Accessories, LCD Display Unit door mounted on the panel, Over Current Trip Feature is included, Controls / Displays Electrical Safety System preset, trip, and calibration in field. Inlets & Outlets.

23. Thermocouple / Thermocouple PID / Thermocouple Well / Pressure Gauge

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Simplex/Duplex as per IS, Range from - 200°C to + 1800°C in various designs. Variety of protection sheaths like M.S. SS304, 316, 321, 446, (HRS), Nickel, Wrought Iron.

24.

Miscellaneous Hardware / Cable Tray Cable / Wire, Electrical Material, C.I. Rose & S.T. Saddle switchgears, main switch, ELCB, MCB, capacitors, Control panels, fire retardant grade, 9600 Glow Wire Tested, Fully insulated, Miscellaneous electrical hardware and sub systems, protection devices etc. IS 309-3, IEC: 1989, Range:10A, 20A For Single Phase (2P+E), 250 V, 20A, 30A for Three Phase (3P+E), 440V.

25. Recovery System: Insulated piping for Hot Hydrocarbon gases handling, Cooling tower, hot gases Cooling condenser and gases separator, Feeding system, Liquid storage and

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measuring set up. Liquid fuel storage and feeding system, Gas flaring.Process diagram:

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Conversion of Solid Waste in to Hydrocarbon

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Equipment and accessories for Solid Waste in to Hydrocarbon

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Test report for the output gas.

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