Description        Minimum Requirements
Design standard    Multiple chamber incinerator to the design of EPA  standards, Air pollution control
Description of the Chimney    Top mounted, self supporting
Incinerator performance    150kg/hr
Refuse     Hospital waste and carcasses
Recommended Temperatures    Minimum 1000⁰C
Dimensions:
•    Length
•    Width
•    Height
•    Extra width for burners    At least 3000mm
Loading door opening    Minimum 700mm x 600mm
Hearth area    5.00square meters
Description or grate/hearth    A full hearth supplied to prevent contaminated liquids from flowing into the ash pit without being incinerated
Primary chamber volume    At least 3 cubic meters
Mixing chamber volume    At least 1 cubic meters
Settling chamber volume    At least 3 cubic meters
Weight excluding chimney    15, 000kg at manufacture
Firing tools supplied    Hoe, Poker and rake
Material of construction    •    Case – 5mm mild steel.
•    Bracing – Heavy angle and channel.
•    Hearth – 1550⁰C castable general purpose high strength, high abrasion resistant monolithic refractory concrete.
•    Ashing door – High grade cast iron.
•    Loading door – 5mm mild steel lined with 1550⁰C castable  general purpose high strength, high abrasion resistant monolithic refractory concrete.
Refractory  concrete:
•    Alumina content of refractory
•    Refractory thickness
•    Minimum 49%
•    At least 127mm.
Insulation  to walls     1000⁰C Castable insulation
Chimney stack:
•    Chimney
•    Height from base    •    3.5 mm mild steel
•    9 meters above ground level and clear the highest point of the building by not less than 3 meters
•    At least 560mm
•    At least 750Kg
Controls:
Draught

Air supply

Electric

•    Barometric indicator, door operated draught limiter

•    Built-in forced heated air ducts, primary and secondary (intensifier)
•    Control panel – Circuit breakers, main switch, timer, pilot lights, 2 set point pyrometer and one set point pyrometer.
Electricity supply required    415 Volts Three phase.
Auxiliary  fuel    Electrically operated only
Emission     Multiple chamber design with inbuilt emission control
Paint: Case and stack    400⁰C Heat Resistant Grey
Temperature of case    100⁰C

[China] Solid Waste Environmental online waste incineration industries development momentum is fierce, and the brightest of capital chasing even appear several times in the last year the price of handling fee diving, industry raised concerns about the vicious competition. “Thirteen Five” during garbage construction market investment space at 1000 billion yuan; the growing garbage incineration capacity of the operation of the facility, the regulatory level challenges. Many industry companies said in simple incineration links, market competition is too fierce, competitive professional enterprises should play in the field of business models and technological innovation.

Waste incineration industry momentum is fierce level of related facilities to be improved

“Twelve Five” is a fast-growing garbage incineration five years. According to relevant statistics, in 2015, the national city and county has accumulated garbage incineration capacity of about 233,000 tons / day. Waste incineration industries development momentum is fierce, and the brightest of capital chasing even appear several times in the last year the price of handling fee diving, industry raised concerns about the vicious competition. Which is still used as the main way of landfill waste, mostly due to the local authorities responsible for managing the operations, the market is not high, remain “low key.”

The future will continue to heat a cold do?

In this regard, some experts pointed out that, on the one hand, waste incineration will continue to grow, but the amount of accumulation and qualitative improvement of equal importance, particularly waste incineration emissions formal implementation of new standards for operation of the facility and set higher requirements; on the other hand landfill as an indispensable and irreplaceable resource, is still dealing with the mainstream. But to find out the remaining storage capacity, make good use of good management will become critical; at the same time, non-canonical transformation landfill, pollution, etc. also brought closure to repair the relevant market opportunities.

According to the deputy director of the Research Center for Environmental Health Engineering Department of Housing and General Workers Liujing Hao introduction, facility upgrades will be the next five years, important content. “China’s solid waste disposal facilities (landfill, incineration plant) construction and development is very fast, there are a number of construction and operation of the facility has a large room for improvement. There are many old landfills need to maintain and update, so as not to pollute the surrounding environment. Some of the early construction of incineration plants need to be upgraded or reset. ”

Incineration facilities is still on the rise

“Thirteen Five” during garbage construction market investment space at 1000 billion yuan; the growing garbage incineration capacity of the operation of the facility, the regulatory level challenges.

‘Facilities’ second five’ plan basically completed the goal. “China Urban Environmental Health Association and vice president, director of the Research Center for Environmental Health Engineering Department of Housing and Xu Wenlong said that according to” the “second five” national urban domestic garbage treatment facility construction plan, “clearly incineration project the total size of 307,200 tons / day. Although the end of 2015, the national total incineration capacity of 233,000 tons / day, but the size of the project currently under construction there of about 10 tons / day, and basically complete the planning and construction scale.

Planning and completion of high interest capital markets has a direct relationship. Construction and operation of waste incineration facility has become one of the segments of capital chasing the parties, after the project in a constant rise to fierce “fight.”

The next five years, incineration facilities construction market is still big? In this regard, the Executive President of the Institute of E20 Xue Tao believes that incineration facilities will maintain growth. “In the construction of garbage ‘Thirteen Five’ period, probably in the investment market space, building space is at 100 billion yuan.”

Xu Wenlong believes that new market does still have a better chance. Currently, most of the city and most of the county’s garbage can be effectively collected and treatment and disposal in sanitary landfill and incineration plants. But still there are gaps in waste disposal facilities, the new facility is still one of the main tasks of the current and the next five-year plan. “According to the relevant national planning, the national MSW incineration capacity in 2020 will exceed 40 tons / day in 2025 up to 50 tons / day. By then, China’s demand for incineration facilities will reach a relatively stable state.”

Accumulation in the continued qualitative improvement already started. From January 1 this year, all new country, has been running garbage incinerator must perform a new “garbage burning pollution control standards” (GB18485-2014) (hereinafter referred to as the new standard) of emission limits. New standards for conventional pollutants, dioxin contamination compared to the previous standard have more stringent requirements.

(Source: China Association of gravel)
Article Links: China Environmental Protection online http://www.hbzhan.com/news/detail/105016.html

chemical agents to be utilized:
10% heptyl (unsymmetrical dimethylhydrazine) water solution,
heptyl (unsymmetrical dimethylhydrazine) vapour with 0.8 to 1.0 kg/m3 concentration,
10% azotic (nitric) acid water solution,
azotic (nitric) acid vapour with concentration up to 1.1 kg/m3;
2.    neutralization method: thermal decomposition;
3.    neutralization temperature: +800?C to +1200?C;
4.    performance:
?    vapour capacity: 70 to 200 m3/h,
?    water solution capacity: 50 to 500 l/h;
5.    inlet pressure: up to 2 bars;
6.    automatic control system;
7.    overall dimensions shall allow for mounting the unit on a vehicle chassis.
medical waste incinerators manufacturers General Specifications
6mm plate steel sheel construction
11cm 1400 o C Refractory L iner
Temperature controlled Burners
Secondary combustion Burners
Interlock Switch on Load Doors
Separate Ash Door
One Second secondary Residence @ 1000 o C
400 ° C Silicone Based Paint Finish.
Alloy Temperature Sensor
Factory wired and tested
Capacity-20 kg / hr
Primary Chamber-1607 L
Hearth Area-1:36 sq. m
Secondary Chamber-694 L
Primary Burner (oil)-420,000 btu
Secondary Burner (oil)-900,000 btu
secondary Combustion-1/6 hp
Exhaust Stack-46cm x 6m
Electrical Service-220/50
Weight System-5.700 kg
Dimension “D”-152cm
Load Port Height- 60x 60 cm
Ash Port Height -36 x 36 cm

SHETLAND Islands Council is to introduce “door-to-door” recycling of glass and cans next summer – but paper, card and plastic will be burned in the Gremista incinerator after that was found to be the “best practicable environmental option”.

While the notion of burning garbage may seem counterintuitive to those seeking to make the planet greener, the local authority’s stance is backed up – at least in the short term – by Zero Waste Scotland.

The waste-to-energy plant burns material from Shetland, Orkney and occasionally the Highlands, and its output then powers SHEAP’s district heating scheme for homes in Lerwick.

Because Shetland is not connected to the national grid, SHEAP has to make up any shortfall in energy using power generated by oil-fired plants. As a result, the council says, it is less environmentally damaging to incinerate material rather than recycle it.

In April 2013 the council abandoned kerbside collection of recycled material in Lerwick and Scalloway – leaving householders to take plastic, glass, newspapers and cans to collection points instead.

The latest recycling rethink is the upshot of two studies commissioned by Zero Waste Scotland, and will cost the local authority £40,000 more than it presently spends on collecting waste and recyclable materials.

Meanwhile, opening hours for the local authority’s Gremista waste management site are to be cut to allow staff to spend more time sorting industrial waste prior to incineration.

It is to switch to opening between 1pm and 6pm on weekdays and from 11am to 3pm at weekends. That is a significant reduction on the current opening hours of 8am-8pm from Monday to Friday and 9am-5pm on Saturdays and Sundays.

It is expected a charge will be levied on commercial and business premises – accounting for an estimated 20 per cent of waste – for recycling glass and cans.

Infrastructure director Maggie Sandison said changes in legislation left the SIC with no option but to change tack. The situation remains in flux, with further legislative changes expected, and she suspects that in the long term the council will be “recycling more and incinerating less”.

Collecting glass and cans “at least” once a month from every islands household will raise the local authority’s overall recycling rate to around 12 per cent, compared to six per cent at present.

SIC infrastructure director Maggie Sandison.  SIC infrastructure director Maggie Sandison.  Shetland will continue to recycle the lowest percentage of material anywhere in Scotland, trailing far behind the SNP Government’s target of recycling 70 per cent of waste by 2025.

But Sandison’s report pointed out that Zero Waste Scotland recognised that –until an alternative heat source to the energy recovery plant is found – “environmental benefits of waste incineration to heat the district heating scheme outweigh the environmental benefits of recycling combustible materials in Shetland”.

A special derogation from environmental regulator SEPA will be required to allow the energy recovery plant to continue burning hard plastics.

She told members of the environment and transport committee on Monday that the plan was to begin the new recycling collection next summer.

Door-to-door collections will help sort municipal waste, but more staff resources will be required to ensure industrial waste is properly sifted through prior to incineration.

“It will require different staffing,” she told environment and transport committee members. “We’re looking to change the opening hours of the waste management facility in order to redeploy staff to sorting waste rather than just accepting it through the gates.”

Sandison said staff would spend the remainder of 2014 looking at the best way to collect recycling, with an eye to Orkney where a similar door-to-door service was recently rolled out.

While “bring sites” for recycling will no longer be used by the council, Sandison said talks were being held about putting in place more textile banks for the Salvation Army “and they can choose what ones they want to use”.

The committee backed the report’s recommendations without objection on Monday, a move welcomed by chairman Michael Stout.

“There are many, many threads to this,” he said, “and I think from my perspective this gives us the best way out of the particular set of circumstances that we find ourselves in.”

Councillor Steven Coutts said he felt there was an opportunity for the council to be “proactive” in encouraging folk to minimise the amount of waste they generate, meaning there would be less material to recycle or burn in the first place.

Sandison agreed, saying the council should also promote reuse, while government regulations should reduce the extent to which things like fruit and vegetables are “wrapped in vast amounts of plastic”.

“We’ll see less and less [waste] when charges incurred in the manufacture of waste start to make that unattractive,” she said. “There are going to be big changes in waste generation as well as recycling as legislation proceeds.”

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.

INCINERATEUR DE DECHETS HOSPITALIER hospital incinerator design

SPECIFICATIONS TECHNIQUES.
Capacité destructive de 55 Kg/h jour de déchets hospitaliers  avec un p?.c. i jusqu’à 3.200 Kcal/Kg
1)Type de déchet

hospitalier
2)Pouvoir calorifique inférieur                                                                        3.200 kcal/kg
3)Humidité                                                                                                          20%
4)Teneur  en cendres et/ou inertes                                                                       8%
5)Capacité destructive nominale                                                                         55 kg/h
6)Volume chambre de combustion                                                                     1,65 m3
7)Volume chambre postcombustion                                                                   2.1 m3
8)Temps  transit des fumées en post combustion /sec.                                       <2
9)Température minimale  en postcombustion                                                     1.100° C
10)Teneur d’oxygène libre en postcombustion                                                     6%
11)Attribution refuse confectionné en sachets                                                     HDPE
12)Dispositif de chargement?: hydraulique?; capacité de charge                           0.5 m3

13)Combustible prévu                                                                                           Gasoil
14)Br?leur en chambre de combustion                                                                  nbr?: 1
15)Br?leur en chambre de postcombustion                                                           nbr?: 2

CONSTITTUTION DE L’APPAREIL.
1.CHARGEMENT
Système de chargement hydraulique afin de pouvoir charger le four en toute sécurité même durant son  fonctionnement et

aussi assurer la puissance destructive globale de 450 kg/j?
Le système comprend?:
1-1Trémie de chargement de forme parallélépipédique de 0,5 m3 de volume, réalisée en t?le d’acier, bridés sur la paroi

frontale de la chambre de combustion et munie d’un couvercle à charnières  actionné par vérin hydraulique?.
Dimensions?:
oLongueur 1200 mm
oHauteur 700 mm
oLargeur  600
1-2Un poussoir hydraulique  assurera le chargement de la chambre de combustion
1-3 Une  porte de chargement  de la chambre de combustion constituée  d’une  guillotine  à vérin hydraulique  revêtue

de réfractaire
1-4Un central  hydraulique pour piloter tous les vérins de commande, comprenant?: réservoir, pompe, électrovannes et

tuyauteries

2.CHAMBRE DE COMBUSTION PRIMAIRE

2-1- Le bati est une  structure métallique cylindrique revêtue intérieurement  d’une couche d’isolant et d’une

couche de réfractaire.
2-2-Volume intérieur?: 1,65 m3
2-3-Aménagement
?portillon de décharge  des cendres?:  frontal?; monté sur double charnière et revêtu de réfractaire avec hublot

d’inspection
?La connexion à la chambre de chargement est revêtue de réfractaire
?La connexion  de la   chambre de combustion et de la chambre de post combustion est revêtue de réfractaire
?Installation des bruleurs
?Installation  du système  de distribution de l’air comburant
?Installation des  sondes  de mesure de la température
?Le bac de récolte des cendres  est en acier au carbone sur roulettes, équipé de racloir métallique permettant

l’évacuation manuelle des cendres
3.   BRULEUR DE LA CHAMBRE DE COMBUSQTION
Un bruleur de type à une flamme à l’air soufflé, alimenté par gasoil, équipé des dispositifs de sécurité  Puissance

thermique installée 165 KW.
4. AIR COMBURANT
Le système de distribution et dosage de l’air primaire en chambre de combustion comprend?:
?Ventilateur centrifuge
?Canalisations de distribution air
?Systéme de distribution d’air à 2 canaux
?Soupape de régulation de l’air motorisé selon les phases de cycle de fonctionnement et de la température

5. CHAMBRE DE POST COMBUSTION
5-1- Chambre de post combustion est installée au dessus du foyer  de combustion , elle  est constituée d’un

cylindre  métallique  revêtu intérieurement d’une couche d’ isolant et d’une couche de matériaux réfractaires.
5-2- Volume intérieur?: 2,1 m3
Est dimensionnée pour pouvoir  garantir  un temps de fumée de 2 secondes à 1100°C avec un pourcentage d’oxygène libre

d’au moins 6 %.
5-3 -Accessoires
?Trappe de visite boulonnée frontal pour permettre l’inspection périodique
?La liaison à la chambre de combustion est tapissée de réfractaire
?Installation les br?leurs
?Installation des sondes de mesure température
6. PRODUCTION DE L’AIR COMBURANT DE LA CHAMBRE DE POST COMBUSTION
?Ventilateur centrifuge
?Tuyauteries  de distribution d’air
?Série  de vannes de distribution  d’air
?Soupape de régulation de l’air soufflé  asservi par la sonde du débit  d’ oxygène

7. BRULEUR DE LA CHAMBRE DE POST COMBUSTION
Sont prévus 2 br?leurs du type à l’air soufflé au gasoil équipés  des dispositifs de sécurité.
A la mise en route du four les deux  br?leurs sont  allumés pour assurer la température minimale d’au moins 1100°C?;

ils restent en marche successivement  pour maintenir la température constante.
Puissance thermique installée (290 + 350) KW.

8. CHEMINEE D’EVACUATION
Constitué par un conduit métallique vertical de 8 m de long installée au-dessus de la  chambre de PC, diamètre 630 mm

en t?le d’acier au carbone avec garnissage intérieur en réfractaire

9. ARMOIRE ELECTRIQUE DE COMMANDE ET REGULATION
Composée  de?:
?Circuit  380 V- 50 HZ-3 phases
?Voyant sous tension
?Commande d’arrêt  général
?Voyant état des bruleurs
?Affichage des  températures  des deux chambres
?Minuterie des temps des cycles.
?Une variation des vitesses des ventilateurs
?Le tableau et les cablages sont prévus aux règles CEI avec protection IP 55
?Microprocesseur pour le contr?le et la régulation des températures, ainsi que les cycles d’opération
?Cablages réalisés selon les règles CEI.

10. INSTRUMENTATION DE CONTROLE ET DE MESURAGE CONTINU
Les  dispositifs suivants  sont prévus?:
1)Thermocouples pour la mesure de la température  en chambre de combustion? et postcombustion, à la sortie de

l’échangeur dans la section d’entrée du filtre
2)Système de mesure de la concentration d’oxygène dans les fumées humides a la sortie de la chambre de postcombustion

constitué de?:
?Sonde de mesure de l’oxygène à l’oxyde de zirconium
?Pompe à la membrane
?débitmètre

medical waste incinerator: medical waste and general waste
Capacity to burn waste: 400 — 500 kg/hr
Fuel: Diesel
Fuel Consumption: 10 litres/hr maximum
Incineration temperature: 950 – 1300 °c
Casing: thick (min 5 mm) Stainless steel casing and fully
insulated to withstand sea humidity
Voltage: 220/240 V or 380/415V
Frequency: 50 Hz
Feeding: automatic
Ash 1 leftovers removal: Automatic
Fuel gas filtration system: Yes
Warranty: 12 months
Staff training: Operator & Maintenance staff
Operation and service manuals: 3 sets each
Especifica??es Gerais     6 mm plate steel sheel construction
11cm 1400°C refractory Liner
temperature controlled Burners
secondary combustion burners
interlock switch on load doors
separete ash door
one secondary residence @ 1000°C
400°C silicone Based finish paint
alloy temperature sensor
factory wired and tested
Capacity    20kg/hr
primary Chamber    1607 L
Hearth area    1.36 aq.m
Secondary Chamber    694L
Primary burner (oil)    420.00btu
Secondary burner (oil)    900,000btu
Secondary combustion    1/6 hp
Exhaust stack    46cm x 6m
Electrical service     220/50
System weight    5,700kg
Dimension “D”    152cm
Doad port height e    60x60cm
Ash port height e    36x36cm
General Specifications    6mm plate steel sheel construction
11cm 1400 ° C refractory liner
temperature controlled Burners
secondary combustion burners
interlock switch on load doors
separete ash door
one secondary residence @ 1000 ° C
400 ° C silicone based paint finish
alloy temperature sensor
factory wired and tested
Capacity    20kg/hr
primary Chamber    1607 L
Hearth area    1:36 aq.m
Secondary Chamber    694L
Primary burner (oil)    420.00btu
Secondary burner (oil)    900,000 btu
Secondary combustion    1/6 hp
Exhaust stack    46cm x 6m
Electrical service    220/50
System weight    5.700 kg
Dimension “D”    152cm
Doad port height and    60x60cm
Ash port height and    36x36cm
medical, hospital, veterinary and industrial wastes by medical waste incinerator Process.
So, we’re interested with your Incinerator plants, and we’d like to get quotation and key features description of different capacities of your Incinerator plants, concerning: small models (5 – 25 kg/hr); medium models (25-50 kg/hr) and big models (50-100 kg/hr) and plus.