Tag: waste-incinerator

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d’inspection
7)Volume chambre postcombustion                                                                   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%.
? Soupape de régulation de l’air motorisé selon les stages de cycle de fonctionnement et de la température

5. CHAMBRE DE POST COMBUSTION
? Affichage des  températures  des deux chambres
8)Temps  transit des fumées en post combustion /sec.                                       <2 1-3 Une  porte de chargement  de la chambre de combustion constituée  d'une  guillotine  à vérin hydraulique  revêtue

de réfractaire
? Voyant état des bruleurs
Système de chargement hydraulique afin de pouvoir charger le four en toute sécurité même durant son  fonctionnement et

aussi assurer la puissance harmful globale de 450 kg/j?
2-3-Aménagement
6. PRODUCTION DE L’AIR COMBURANT DE LA CHAMBRE DE POST COMBUSTION
? Microprocesseur pour le contr?le et la régulation des températures, ainsi que les cycles d’opération
? Le bac de récolte des cendres  est en acier au carbone sur roulettes, équipé de racloir métallique permettant

l’évacuation manuelle des cendres
Sont prévus 2 br?leurs du type à l’air soufflé au gasoil équipés  des dispositifs de sécurité.
? Cablages réalisés selon les règles CEI.

10. INSTRUMENTATION DE CONTROLE ET DE MESURAGE CONTINU
: hydraulique? ; capacité de charge                           0.5 m3

13)Combustible prévu                                                                                           Gasoil
1. CHARGEMENT
? Commande d’arrêt  général
? Une variation des vitesses des ventilateurs
? Soupape de régulation de l’air soufflé  asservi par la sonde du débit  d’ oxygène

7. BRULEUR DE LA CHAMBRE DE POST COMBUSTION
? Systéme de distribution d’air à 2 canaux
? Canalisations de distribution air
? Trappe de visite boulonnée rectal pour permettre l’inspection périodique
2)Pouvoir calorifique inférieur                                                                        3.200 kcal/kg
14)Br?leur en chambre de combustion                                                                  nbr? : 1
Capacité destructive de 55 Kg/h jour de déchets hospitaliers  avec un p? . c. i jusqu’à 3.200 Kcal/Kg
3)Humidité                                                                                                          20 percent
oLongueur 1200 mm
5-3 -Accessoires
oLargeur  600
5-2- Volume intérieur? : 2,1 m3
5)Capacité destructive nominale                                                                         55 kg/h
? Tuyauteries  de distribution d’air
1-2Un poussoir hydraulique  assurera le chargement de la chambre de combustion
Dimensions? :
? Le tableau et les cablages sont prévus aux règles CEI avec protection IP 55
?
? Ventilateur centrifuge
2)Système de mesure de la concentration d’oxygène dans les fumées humides a la sortie de la chambre de postcombustion

constitué de? :
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? :
? Série  de vannes de distribution  d’air
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.
? Pompe à la membrane
4. AIR COMBURANT
? Ventilateur centrifuge
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
Les  dispositifs suivants  sont prévus? :
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? .
? La connexion  de la   chambre de combustion et de la chambre de post combustion est revêtue de réfractaire
? débitmètre

8. CHEMINEE D’EVACUATION

: 2

CONSTITTUTION DE L’APPAREIL.
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.
? Circuit  380 V- 50 HZ-3 stages
? Minuterie des temps des cycles.
? Installation des sondes de mesure température
? La connexion à la chambre de chargement est revêtue de réfractaire
: réservoir, pompe, électrovannes et

tuyauteries

2.
? La liaison à la chambre de combustion est tapissée de réfractaire
3.   BRULEUR DE LA CHAMBRE DE COMBUSQTION
? Voyant sous tension
? Installation des bruleurs
Le système de distribution et dosage de l’air primaire en chambre de combustion comprend? :
2-2-Volume intérieur? : 1,65 m3
? Sonde de mesure de l’oxygène à l’oxyde de zirconium

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 incinerator primary combustion price

environment contract management firm with planned operations 2013 in Indonesia and Thailand, and 2014 in West & East

Malaysia to execute those professional services in order to abide by the governments safety disposal requirements

for hospital and medical, clinical waste in the region and to meet the higher technical standard in this particular

field.small incinerators with filter (with minimum minimal pollution) for burning/combusting 5kg/hr, 10kg/hr, 15 kg/hr,

20kg/hr, 25kg/hr to 50kg/hr and 300kg/hr of SOLID ORGANIC DRY AND WET NON-HAZARDUOUS of any type (including hospital

wastes) per day or per hour. Should it be without a smoke, no fumes, no odour (odor ), no dust, no emission of solid

particles and with least minimal contamination (within national and global standards). Must be

healthy and okay with global standards. Ash contents after burning

should be 3-4%.

Within the framework of an environmental and medical equipment & technology consultation and joint purchasing, this

Procurement Bureau invites applicants for pre-qualification in the aim of primarily selecting capable companies to bid

for the above tender.

Our normal activities creates 2-5 tons of assorted waste materials per day which range from condemned carcasses, and medical incinerator main combustion price

other wastes all that need to be incinerated at above 800Centigrade measured flue exhaust gas.To be employed by little

hospitals and clinics to safely dispose of infectious and pathological wastes.

Load Capacity in the range of up to 200 kg
And to be designed to fulfill the Norms of Pollution Control / DEFRA, etc.. Tech:

Temperature Controlled Burner. Heavy-duty casing, to be a quality, rugged, reliable, economical Medical Waste

Incinerator with relevant control, easy to operate and self explanatory. Type of Fuel: Diesel / Oil or Petrol.
– Burning Rate approx. 50kg/Hour –

Incinerators to be very effective, fuel efficient with high / low capacity burn speeds

waste incinerator manufacturers china

Capacity    Not less than 500Kg/hr.

small capacity incinerators

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
2.     If the minimum combustion temperatures aren’t maintained.
Arsenic                                       As
Barium                                        Ba
5.     All the emission to the air apart from steam or water vapour has to be odourless and free of 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
21 – OM

Where:    Es    = Calculated emission concentration in the standard percentage oxygen concentration
Wout = mass emission rate of POHC from the stack before the release to the air.

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:
2.     Be fitted with secondary burner/s burning gas or low sulphur liquid gas or some other acceptable fuel.

3.     Ensure secondary air supply is controlled efficiently.
4.     The incinerator must not be overcharged.
6.     Ensure the gas temperature as measured against the inner wall at the secondary room & not in the flame zone, is less than 1100oC. Ensure the oxygen content of the emitted gases is less than 11%.
Manganese                                  Mn
A solid particulate meter/recorder
3.     The incinerator has to be preheated to working temperature before charging any waste.
Percent CO2 + CO

2.     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
6    Chimney / Stack    1.     The chimney should have a minimum height of 10 meters above ground level and clear the maximum point of the building by not less than 3 meters for all roofs. The topography and height of adjacent buildings within 50 meters radius ought to be taken into consideration.

2.     If possible the chimney needs to be visible to the operator from the feeding area.
3.     Whenever the previous charge hasn’t been fully combusted in the case of batch feeding. Until such time as the addition of more waste won’t cause the layout parameters of the incinerator to be surpassed.

3    Main Combustion Chamber    The main combustion chamber must:

1.     Be accepted as the main combustion zone.
The Combustion efficiency is computed as follows;

C.E=% CO2           x 100
Thallium                                     Tl

Chromium                                  Cr
Tin                                               Sn
Mercury                                      Hg
Hydrochloric                                HCL
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 Region and be compatible with premises in the area,

2.     Has to be placed in a suitably ventilated room. Combustion efficiency:

Combustion efficiency (CE) shall be at least 99.00%
Nickel                                           Ni
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    Feeding And Charging    Controlled hygienic, mechanical or automatic feeding methods have to be used which won’t 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.
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
Silver                                          Ag
OM    = measured oxygen concentration

10    Operation    1.     Materials destined for incineration should be of known origin and makeup and must be only incinerated in a furnace that’s registered for the specific type of waste.

2.     A record must be kept of the amount, type and origin of the waste to be incinerated.
3.     The addition of dilution air after combustion in order to reach the requirement of these guidelines is unacceptable. 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 greater to make sure no down washing of exiting gases.

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

7    Instrumentation    Instrument for determining the interior wall temperature rather than burner flame temperature has to be provided for both primary and secondary chambers.

2.     An audible and visible alarm must be set up 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.
4.      Fire fighting equipment must be provided
5.     The incinerator must be in good working order at all times and must not be used if any part fails. Any malfunction ought to be recorded in a log book and reported to the relevant authority.

6.     The incinerator operator and all relevant personnel 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.
Where: Win = mass feed rate of the POHC from the waste stream fed to incinerator, and
Antimony                                    Sb
4.     Ensure minimum exit temperature is not less than 850oC

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

1.    
Fabric filters
A smoke density meter/recorder
Acid Gas Scrubbers
3.     Have light if 24hrs operation
Vanadium                                     V
Beryllium                                    Be

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

Overall plant layout.
4.     Make sure fire contact with gases is achieved.
Electrostatic precipitators
Cobalt                                         Co
5.     Ensure residence time isn’t less than two (2) seconds.
Os    = Standard oxygen concentration
Primary Combustion Chamber.
5.      There should be no smoking or eating on the site.

3.      Caution and Warning signs must be provided.
Hydrofluoric acid                         HF
Lead                                            Pb
A carbon monoxide and/or oxygen meter/recorder
EM    = Measured emission concentration
2.     Have a good floor.
8.     Ensure both main and the combustion temperatures are maintained until all waste was fully combusted

5    Particulate Removers    A mechanical particulate collector has to 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
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 main air supply is controlled efficiently

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.

china medical incinerator

china medical incinerator Ability
? Typical Daily Max/Min January Temperature, 2-12°C.
? Disposal of both non-hazardous and hazardous waste streams (per waste inventory)
Design/Specifications
? Average Daily Max/Min June Temperature, 21-39°C
? The incinerators will be installed with visual alarms to alert operations of reduced temperature in the secondary chamber
diesel fuel / mains power operated,

the following containerized incinerators. (Kitchen and lodging and gray water and black water plant eliminating waste) we need incinerator is each function separate are all in one incinerator we need informed. Plant we installing for our lodging barge used in an offshore marine construction project.
programmable cycle

The Incinerators package shall be designed to function under the following conditions:
? Liquid waste streams shall be incinerated by an appropriate liquid injection system
thermostatic temperature control,
Medical waste incinerator,
? Incinerators must have a secondary combustion chamber with a minimum temperature range of 900c

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Temperature Controlled Burner. Incinerators to be designed to meet the Norms of Pollution Control. Technology: Heavy-duty casing, to be a quality, rugged, dependable, economical Incinerator with relevant control, easy to operate and self-contained. Units to be pre-assembled, pre-piped, pre-wired & tested before Transfer / Export.

Note: Similar Technology and / or Tenderers Proposals are welcome.

Within the framework of an environmental equipment & technology consultation and joint purchasing, this Procurement / Notary Bureau invites applicants for pre-qualification from the aim of primarily selecting capable companies to bid for the above tender.
The supply will include the special equipment for successful waste management as stated above for a brand new private environment contract management firm with planned operations 2013 in Indonesia and Thailand, and 2015 in West & East Malaysia to execute those professional services to be able to comply with the government security disposal requirements for animal waste from the area and to meet the higher technical standard in this particular field to be able to protect the public and contain contagious & infectious viruses and animal caused diseases. The spread of a new disease of pigs, also the ‘Nipah Virus Disease’, first evident in 1998 in S.E.Asia, which causes illness and death in both humans and pigs, is increasing again; as well as the sudden passing of sows and boars was recorded in pig farms in Malaysia and other areas in S.E. Asia.

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Waste Incineration HICLOVER Model TS75