3 Medical Waste Incinerator of 20 kg/hr capacity with twin burner.Medical Waste Incineration Equipments. Our purpose for this task is to establish a plant in order to blaze Medical waste with 50 ton/day capability. Waste monitoring
Heater
* Outside dimension at base 6ft 1.8 m.
* Outside size at leading 4 1/2 feet 1.35 m.
* Internal size at base 3ft 0.9 m.
* Interior size at leading 3ft 0.9 m.
* Density of wall surface at base 18cm.
* Thickness of wall surface at leading 9cm.
* Perpendicular height of wall 4ft.
* Height of Iron bars from grate over ground 1ft

Material Required.
* Pool swish.
* 5 or 6 Iron bars regarding 4 1/2 feet 1.35 m long each.
* Amount of massive rocks for structure.
* 2 vacant kerosene tins for making air vent openings.
* 2ltrs of coal tar.
* 2 brushes.
* Framework 1ft-1 1/2ft deep is dug.
* Full of big stones as well as likewise puddle swish to ground degree.
* Uninhabited kero tins are following put right into position where the vent openings are to show up.
* Wall surface 1ft high is developed with pool swish.
* Iron bars are put in placement leaving a location of concerning 2cm-3cm in between the bars 4ft 1.2 m to be gotten to.
* Wall surface plastered smooth.Incinération à haute température pour la damage complète des déchets contaminés ou dangereux.
Principe de burning pyrolytique avec brûlage des fumées dans une chambre de post-combustion.
Incinérateur double chambre 900 ° C/1200 ° C de capacité 30 kg.
Equipé de: 1 brûleur de combustion + 1 brûleur de re-combustion + 1 laveur de fumées. Capacité de devastation horaire.
En poids: au moins 30 kg.
En quantity: au moins 200 litres.
Température:.
Burning: 900 ° C. Write-up combustion: 1200 ° C.
Puissance des brûleurs.
Burning: au moins 80 KW.
Article burning: 80 KW.
Puissance électrique: environ 2 KW.
Cheminée:.
Area: environ 30×× × × 30 centimeters.
Hauteur (minimum): au moins 8 m.
Dimension de la porte de chargement: environ 50X50 cm

Intermittent Feed (w/optional loader): .9 yd3/hr (.7 m3/hr) up to 8 hrs/day

 

 

 

 

Specifications: Length overall -9′-6″ (2896 mm) batch system w/o loader

 

 

 

 

18′-6″ (5639mm) w/optional loader system Width overall -7′-6″ (2820mm)

 

 

 

 

Height (w/o stack) -10′-0″ (3048mm) Approx. Weight – 14,000 lbs. (6364 kg) w/o

 

 

 

 

Loader

 

 

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.

 

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.

SOLID WASTE INCINERATOR

1

ea

 

 

1.5 MMBtu / hr waste combustion, providing 200-250 lb/hr (90-114 kg/hr)

 

 

 

 

Processing capacity for mixed waste streams with an average gross

 

 

 

 

HHV of 5500-8500 Btu/lb

 

 

 

 

Batch Operation: Approx. 1.9 yb3 (1.45 m3) per 4-6 hour operation cycle

Manual autoclave with vertical loading; gravity displacement type with possibility for Vacuum.

 

Capacity:      Up to 12 kg/h

 

Chamber size:      >150 liters

 

Material:       Stainless steel

 

Temperature:       134 °C

 

Further information:

 

Minimum autoclave chamber size shall be 150 liters and shall have a usable volume (loading basket) of 100 liters.

Shall work according to gravity air displacement principle.

The vacuum system shall be of a thermal shock type.

 

The pressure vessels should be pressure tight, the rising of the pressure (at a start pressure of below 80 mbar)

shall be lower than 1 mbar/min.

 

With in-build electrical heating elements for steam generation (heating elements > 4000 Kw).

Chamber and door shall be made from high quality stainless steel (e.g. AISI 3161).

Chamber in vertical position, it shall allow an easy loading/unloading of the loading basket.

 

2 Baskets of >100 l for the loading and unloading of waste shall be included. The baskets shall be designed for the

usage of non-heat resistant waste bags, a system for the collection and controlled release of free liquids and

condensate from the waste shall be incorporated.

The temperature measured at the reference measurement point of the treatment chamber shall not be lower than 105°C

(TDes 0+4). The treatment time shall be ≥30 minutes at 105°C, ≥20 minutes with a temperature used of ≥121°C (TDes

0+4) and ≥10 minutes with a treatment temperature of ≥ 134.

The steering of the treatment process should be semi-automatically as well as manual.

The Treatment Equipment shall be equipped with at least the following instruments:

o   treatment chamber temperature indicating instrument

otreatment chamber pressure indicating instrument

For the treatment of the outgoing air, a HEPA filter in combination with a condensation system should be used.

The filter shall be built in a way that a disinfection of the filter shall be possible in a built-in condition.

 

The filters must be heat resistant, steam resistant, hydrophobic and pressure resistant for the pressure difference.

 

Cooling down phase after treatment should be existent; the temperature of the waste should be not higher than 80°C

after finishing the cooling down process.

The pressure vessel should be equipped with a heat insulation, the maximum outer surface temperature should be < 50°

Equipped with main combustion  chamber and a second chamber  for reburning  designed to ensure  complete

combustion  of the gases  resulting  from  incomplete  combustion  of inert gases in the chimney, within the standards

recommended  by the World Health Organization;

 

7. Equipped with temperature controller to adjust the air of the combustion of the waste, and fuel flow in the

burners of the firing chamber and  re-burning  in order  to conserve power when reached the “stead state” of the

combustion process;

 

8. The control system must also be provided  with an audible alarm  in case of decrease  in temperature. The

characteristic of local power is three-phase 220/127V – 60Hz.;

 

9. The natural circulation of the gases will be induced in a chimney height at least 6 meters and diameter of

at least 40 centimeters, so that negative pressure  is sufficient to protect the operator from excess of fires or

dispersion  of noxious gases;

 

10. Supplied with electrical  control  panel  with  thermo-magnetic protection  and  command buttons; and,

 

11. Equipped with   pyrometers  meters/controller   of   thermocouple  temperature   with chromium-aluminium,

range  0-1200 Deg C (to  observe  the  temperature of the  first  and