Chicken Burner – – – – 400 kgs feed a day.a miniature scale incinerator of shedding capability 30kg/hr= 1No. Be aware that it has to be mobile as this is meant for petroleum areas service tented camps. It needs to be petrol controlled as our place is remote. 150! Kg per individual resources LPG electrical burner to be used at the international airport. This is a necessity bu the biography security and protection and also security that all Worldwide flights require all rubbish sweltered inside a recognized time.Required lots ability is 150Kg
Burning Cost: 50kgs/hr Yes.
Chamber – – – – Primar 900 liters Extra: 300Litres
Burning Performance: >> 98% Yes

Burner Of Burning Capacity 30 kg/hr = 1 No

The Incineration System contains:

I. Main Heater with

A. Refractory lined Key as well as Added Chamber.
B. Refractory lined main billing door as well as ash cleansing door.

II i. 1 No. totally automated oil heating unit for major chamber.

III.Centrifugal required draft combustion air follower with electric motor.

IV.

V. Auto-loading in the type of Dual FDV mechanism with external entry

VI.

VII. High pressure Venturi scrubber of SS316 L

VIII.

XIV.

XVI. Caustic dosing system comprising of Tank- Agitator as well as also pump

XIV.

II i. 1 No.

III.Centrifugal forced draft combustion air fan with electrical motor.

V. Auto-loading in the type of Double FDV device with exterior entry
High pressure Venturi scrubber of SS316 L

VIII. Caustic dosing system making up of Container- Agitator as well as additionally pump

XIV.

XVII. Operati ng tools & & tackles like rake, hoe, shovel, 2 teeth scrapper.

XVIII. Caustic dosing system comprising of Tank- Agitator and also pump

XIV. GAS LDO DIESEL.

oElectro-ventilator distributing the secondary air, the regulation of the air flow being carried out by valves and

following the control of the automatic cycle.

Controls and regulations:

Control box watertight to dust, including:

A switch circuit breaker for each engine (ventilators and burners).

A timer with adjustable temporization for the regulation of each burner.

A regulator with digital watching for the temperature of combustion.

A regulator with digital watching for the temperature of post combustion.

Electric box

The incinerator shall be suitable to completely burn the sludge without the need to mix or blend it with any other

fuel. The incinerator shall be designed to meet the latest design criteria for minimization of smoke emission. The

incinerator shall also be used to burn both liquid and solid wastes simultaneously.

Supply, installation and testing of medical waste incinerator with a capacity of 75 kilograms / hour, operated by LPG

and including all accessories with chimney in accordance with the technical specifications and public health

regulations

(MEDICAL INCINERATORS)

Heavy Duty Steel Casing With Heat Retention Fiber

Design Air/ Gas Floe Access to Provide 2-Seconds Gas Retention Time

1x Diesel Fired ignition Burner with Thermostatic On-Off Temperature Control

Particulate/ Gas Combustion at 850C And Above

Zero Smoke or Odor Emissions At 850C And Above

Chimney

Stainless Steel Chimney Section (1 Meter)

Stainless Steel Stack Cap

Ash made from combustion takes the form of fly ash or bottom ash.  Fly ash is your fine particles taken away in the form of smoke whereas bottom ash is your course non-combustible and unburned substance that remains after the burn is complete. The type and amount of pollutants at the fly and bottom ashes depend upon what waste is burnt and completeness of the combustion procedure.

The completeness of combustion is determined by all of the following factors:

Temperature

The temperature generated is a function of the heating value of the waste and auxiliary fuel, incinerator or burn unit design, air distribution and combustion management.  Total combustion requires high temperatures. Usually, temperatures that exceed 650oC with a holding time of 1-2 seconds can cause complete combustion of most food and other common household waste.  Segregation of waste is necessary when using methods that don’t routinely achieve those temperatures. Double chamber incinerators, which can be made to burn complex mixtures of waste, hazardous waste and biomedical waste, has to offer a temperature greater than 1000oC and a holding time of one moment to ensure complete combustion and decrease dioxin and furan emissions.  When these high temperatures and holding times are achieved, waste will be wholly burnt and ashes, smoke and pollutant concentrations will likely be minimized.

Because exhaust gas temperatures vary from nearby to greater than 1000°C whenever a batch waste incinerator is used, optional air pollution control systems with evaporative cooling towers and scrubbers are rarely suggested. But it could be required to use these systems with big constant feed incinerators if further cleaning of exhaust gas is required by regulatory authorities. Holding time, otherwise called retention or residence time, is the length of time available to ensure the total mixing of air and fuel, and thus the total burning of waste. Low temperatures, very low heating values of this waste and reduced turbulence require that the holding time be raised to complete the combustion procedure. This will help in attaining the high temperatures at which waste can be completely burned. The total amount of mixing is affected by the form and size of the burn chamber and how the air is injected. Passive under-fire ventilation achieved during open burning does not lead to adequate turbulence for the burning of a huge variety of waste.  Also, it’s important not to overfill the burn chamber as airflow might be blocked and the amount of turbulence further reduced.  The more advanced incineration designs provide effective turbulence through the forced introduction of air directly into hot zones. The greater the burn temperature, holding time and turbulence that are achieved, the less effect the composition of this waste gets on completeness of the burn.

Because exhaust gas temperatures vary from ambient to greater than 1000°C each time a batch waste incinerator is used, optional air pollution control systems with evaporative cooling towers and scrubbers are seldom recommended. However, it may be necessary to employ these systems with large continuous feed incinerators if additional cleaning of exhaust gas is required by regulatory authorities.

Holding Time

Complete combustion takes time.  Holding time, otherwise known as retention or residence time, is the length of time available to ensure the complete mixing of air and fuel, and thus the complete burning of waste. Low temperatures, low heating values of the waste and reduced turbulence require that the holding time be increased to complete the combustion process.

Turbulence

The turbulent mixing of burnable gases with sufficient oxygen is needed to promote good contact between the burning waste and incoming air. This will help in achieving the high temperatures at which waste can be completely burned. The amount of mixing is influenced by the shape and size of the burn chamber and how the air is injected. Passive under-fire ventilation achieved during open burning does not result in sufficient turbulence for the burning of a wide variety of waste.  Also, it is important not to overfill the burn chamber as airflow may be blocked and the amount of turbulence further reduced.  The more advanced incineration designs provide effective turbulence through the forced introduction of air directly into hot zones.

Composition of the Waste

The heating value, wetness and chemical properties of the waste affect the combustion process and the pollutants that are contained in the resulting smoke and ash. The higher the burn temperature, holding time and turbulence that are achieved, the less effect the composition of the waste has on completeness of the burn.

Key Features: * All models with Dual combustion room. * Stainless Steel chimney/stack, long lifetime. *based on sequence * High temperature, long lifetime of incinerator. * Free or minimal installation onsite. * High burn rate, from 10kgs to 500kgs per hourto 6ton daily. * PLC Control Plane. *based on order New Design for pet animal cremation enterprise. * One year guarantee on incinerator and components in stock.

Program Scope: 1. Hospital& clinic: Iatric Waste, Infectious Waste, Dressing, Bio-Waste, Medicine. 2. Slaughter House &Pet Hospital &Farm: Dead Animal, Bio-Waste. 3. Laboratories, Remote Locations, Disaster Relief Operations, Animal Cremation

1    Basic Plant Design    An approved plant must have four distinct sections that demonstrate three principles of Turbulence, Residence Time and Temperature are inbuilt in the plant design .The regulated sections may include but not limited to:

Overall plant layout.
Feed chamber/ charging
Primary Combustion Chamber.
Secondary Combustion Chamber.
Particulate Scrubbers
Acid Gas Scrubbers
The stack/ chimney.
2    Feeding And Charging    Controlled hygienic, mechanical or automatic feeding methods have to be used which will not influence the air temperature in the primary and secondary chambers of the incinerator negatively.

No waste is to be fed into the incinerator:

1.    Until the minimum temperatures have been reached.
2.    If the minimum combustion temperatures are not maintained.
3.    Whenever the previous charge has not been completely combusted in the case of batch feeding.

4.    Until such time as the addition of more waste will not cause the design parameters of the incinerator to be exceeded.

3    Primary Combustion Chamber    The primary combustion chamber must:

1.    Be accepted as the primary combustion zone.
2.    Be equipped with a burner/s burning gas/fuel or low sulphur liquid fuels. Other combustion methods will be judged on merits.

3.    Ensure primary air supply is controlled efficiently
4.    Ensure minimum exit temperature is not less than 850oC

4    Secondary Combustion Chamber (Afterburner).    The secondary combustion chamber must:

1.    Be accepted as secondary combustion zone.
2.    Be fitted with secondary burner/s burning gas or low sulphur liquid fuel or any suitable fuel.

3.    Ensure secondary air supply is controlled efficiently.
4.    Ensure flame contact with all gases is achieved.
5.    Ensure residence time is not less than two (2) seconds.
6.    Ensure the gas temperature as measured against the inside wall in the secondary chamber & not in the flame zone, is not less than 1100oC.

7.    Ensure the oxygen content of the emitted gases is not less than 11%.
8.    Ensure both primary and the combustion temperatures are maintained until all waste has been completely combusted

5    Particulate Removers    A mechanical particulate collector must be incorporated after secondary combustion chamber for removal of particulate pollutants entrained in the flue gas stream. The particulate collectors may include any of the following or a combination thereof:

Cyclone separator
Electrostatic precipitators
Fabric filters
6    Chimney / Stack    1.    The chimney should have a minimum height of 10 meters above ground level and clear the highest point of the building by not less than 3 meters for all roofs. The topography and height of adjacent buildings within 50 meters radius should be taken into account.

2.    If possible the chimney should be visible to the operator from the feeding area.
3.    The addition of dilution air after combustion in order to achieve the requirement of these guidelines is unacceptable.

4.    The minimum exit velocity should be 10 m/s and at least twice the surrounding wind speed (Efflux velocity = wind speed x 2) whichever is higher to ensure no down washing of exiting gases.

5.    Point for the measurement of emissions shall be provided.

7    Instrumentation    Instrument for determining the inside wall temperature and not burner flame temperature must be provided for both primary and secondary chambers.

2.    An audible and visible alarm must be installed to warn the operator when the secondary temperature drops to below the required temperature.

3.    In addition to the above the following instruments may also be required.
A carbon monoxide and/or oxygen meter/recorder
A smoke density meter/recorder
A gas flow meter/recorder
A solid particulate meter/recorder
Any other instrument or measurement that may be considered necessary

8    Location / Siting    1.    Must be sited in accordance with the relevant local municipal authority planning scheme, the topography of the area and be compatible with premises in the neighborhood,

2.    Must be housed in a suitably ventilated room.

9    Emission Limits    1.    Combustion efficiency:

Combustion efficiency (CE) shall be at least 99.00%
The Combustion efficiency is computed as follows;

C.E=             % CO2           x 100
% CO2 + CO

2.    The temperature of the primary chamber shall be 800 ± 50o C

3.    The secondary chamber  gas residence time shall be at least 1 (one) second at 1050 ± 50o C, with 3% Oxygen in the stack gas.

4    Opacity of the smoke must not exceed 20% Viewed from 50 meters with naked eyes
5.    All the emission to the air other than steam or water vapour must be odourless and free from mist, fume and droplets.

6.    The Authority may require that the certificate holder have tests carried out by an accredited institution to determine stack and/or ground level concentrations of the following substances.

Cadmium and compounds as     Cd
Mercury                                      Hg
Thallium                                     Tl

Chromium                                  Cr
Beryllium                                    Be
Arsenic                                       As
Antimony                                    Sb
Barium                                        Ba
Lead                                            Pb
Silver                                          Ag
Cobalt                                         Co
Copper                                        Cu
Manganese                                  Mn
Tin                                               Sn
Vanadium                                     V
Nickel                                           Ni
Hydrochloric                                HCL
Hydrofluoric acid                         HF
Sulphur dioxide                           S02

7.    A 99.99% destruction and removal efficiency (DRE) for each principal organic hazardous constituent (POHC) in the waste feed where:

DRE = [(Win – Wout)/Win]*100
Where: Win = mass feed rate of the POHC in the waste stream fed to incinerator, and
Wout = mass emission rate of POHC in the stack prior to the release to the atmosphere.

8.    The average dioxin and furan concentration in the emissions should not exceed 80ng/m3 total dioxins and furans if measured for a period of 6 to 16 hours.

Note:
All pollutant concentrations must be expressed at Oo C and 1.013 x 10 5 N/m2, dry gas and 11% oxygen correction.

Oxygen correction is computed as:

Es =     21 – Os    x EM
21 – OM

Where:    Es    = Calculated emission concentration at the standard percentage oxygen concentration
EM    = Measured emission concentration
Os    = Standard oxygen concentration
OM    = measured oxygen concentration

10    Operation    1.    Materials destined for incineration should be of known origin and composition and must be only incinerated in a furnace that is registered for the particular type of waste.

2.    A record must be kept of the quantity, type and origin of the waste to be incinerated.
3.    The incinerator must be preheated to working temperature before charging any waste.
4.    The incinerator must not be overcharged.
5.    The incinerator must be in good working order at all times and must not be used if any component fails. Any malfunction should be recorded in a log book and reported to the relevant authority.

6.    The incinerator operator and all relevant staff must be trained to the satisfaction of the relevant control authority.

11    Housekeeping    The site where the incinerator is built must:

1.    Have running water.
2.    Have a solid floor.
3.     Have lighting if 24hrs operation
4.    Have fly ash containerization and storage before disposal.

12    Health & Safety (Protective Gear)    1.    Staff handling waste must be well trained on safe handling of hazardous wastes
2.     Staff must be provided with appropriate  protective gear such as, gas mask, aprons, gumboots, helmets, gloves, goggles.

3.     Caution and Warning signs must be provided.
4.     Fire fighting equipment must be provided
5.     There should be no smoking or eating on the site.