|
|
¡¡
Nanjing Clover Medical
Technology Co., Ltd.
Tel: +8625-8461 0201
Fax: +8625-8461 0406
Email: [email protected]
Home
About Us
Contact Clover
Mobile
Incinerator
Small Incinerator Model
Model TS10 PLC
(10kg/hr.)
Model TS20 PLC
(20kg/hr.)
Model TS30 PLC
(30kg/hr.)
Model TS50 PLC
(50kg/hr.)
Model TS100 PLC
(100kg/hr.)
Large
Incinerator Model
Model
YD-30 (30kgs/Hr.)
Model
YD-50 (50kgs/Hr.)
Model
YD-100 (100kgs/Hr.)
Model
YD-150 (150kgs/Hr.)
Model
YD-200 (200kgs/Hr.)
Model
YD-300 (300kgs/Hr.)
Model
YD-500 (500kgs/Hr.)
Model
YD-600 (600kgs/Hr.)
Incinerator
Introduction
Company Certificate
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡ |
¡¡
Nanjing Clover Medical Technology
Co., Ltd.
Email:
[email protected]
Follow us
twitter.com/hiclovercom
Incinerator Model YD-100 is a middle
scale incineration machine for many different usage: for a middle
hospital sickbed below 500 units, for all small or big size family pets
(like Alaskan Malamute Dog), for community Municipal Solid Waste
Incineration, etc. The primary combustion chamber volume is 1200Liters
(1.2m3) and use diesel oil or natural gas fuel burner original from
Italy.
All our incinerator use stainless steel chimney, not steel.All our
incinerator have two combustion chamber at least, not single chamber.
All fuel burner from Italy made with famous brand, best quality.
300kgs per hour burning rate incinerator is well liked by market because
this model can be medical waste incineration equipment for big hospital
and also very good for other solid waste treatment with lowest cost,
even if big size animals also can be feed into the combustion chamber.
The primary combustion chamber volume is 2.4m3, big enough for common
size animals. For shipping transport, YD-300 can be loaded into 40¡¯feet
full high container.
Big size combustion chamber up to 4.0m3 and Internal Dimensions is 257 x
147 x 108cm with feeding door opening 108 x 128cm. This model can be a
small waste incineration factory with little amount of budget funds. If
end customer use this for farm to burn animals like cow, horse or camel,
contact with us now.
|
Model |
YD-200 |
|
Burning Rate |
200 kgs/hour |
|
Feed Capacity |
400 kgs |
|
Paimary Combustion Chamber |
2000 Liters |
|
Secondary Combustion Chamber |
500 Liters |
|
Mix Combustion Chamber |
Yes |
|
Smoke Filter Chamber |
Yes |
|
Feed Mode |
Manual |
|
Voltage |
220V/380V |
|
Power |
1.03Kw |
|
Fuel Type |
Diesel Oil/ Natural Gas/LPG |
|
Burner |
Italy Original |
|
Oil Consumption (Diesel Oil) |
20-44 kg/hour |
|
Gas Consumption (Natural Gas) |
12--41.2 m3/hour |
|
Internal Dimensions |
180 x 115 x 96cm (paimary chamber) |
|
External Dimensions |
270 x 185 x 380cm (without chimney) |
|
Temperature Monitor |
Yes |
|
Oil Tank Capacity(if oil fuel) |
300 Liters |
|
Door Opening |
59 x 81cm |
|
Chimney Length |
10.0 Meters |
|
Chimney Type |
Stainless Steel |
|
Equipment Gross Weight |
7600 kgs |
|
Operation Technical Specifications |
|
Paimary Chamber Temperature |
800¡æ--1000¡æ |
|
Secondary Chamber Temperature |
1000¡æ-1200¡æ |
|
Residency Time |
2.0 Sec. |
|
Burning Efficiency |
£¾98% |
|
Waste Lower Calorific Power |
3000Kcal |
THIRD SCHEDULE
(Regulations 26, 47)
STANDARD FOR TREATMENT AND DISPOSAL OF WASTES
A. Classification of Incinerators
Class 1: Industrial Plants Burning Waste as an Additional/Alternative
Fuel
Incinerators in which the waste serves as the fuel or supplementary fuel
in an industrial process (e.g. the use of cement kilns or any other
industrial boilers or furnaces for the disposal of noxious or hazardous
materials).
Class 2 Industrial Incinerators
Class 2A: Commercial
Incinerators for the disposal of waste that contains hazardous,
potential hazardous and bio-medical waste where the operator exceeds 100
Kg/day.
Class 2B: Small Scale Incinerators for Private Use
Incinerators for the disposal of hazardous, potential hazardous and
bio-medical waste where the operator does not exceed 100 kg/ day.
Class 3: General waste Incinerators
Incinerators for general waste that is non toxic, non hazardous, non
medical or does not contain organic halogens, i.e., selected customs,
police, contraband goods, offices waste, commercial waste and industrial
wastes) where the operator does not exceed 1 ton/ day.
STANDARDS, GUIDELINES, CRITERIA, PROCEDURE FOR INSTALLING/OPERATING
INCINERATORS
No. Parameter Standards, Guideline, Criteria and Procedure
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 ---build by local customer
Primary Combustion Chamber. --yes
Secondary Combustion Chamber. --yes
Particulate Scrubbers---- filter brick chamber included
Acid Gas Scrubbers---none
The stack/ chimney. --yes
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:
Until the minimum temperatures have been reached.¡ªmanual feeding
If the minimum combustion temperatures are not maintained. --yes
Whenever the previous charge has not been completely combusted in the
case of batch feeding. --yes
Until such time as the addition of more waste will not cause the design
parameters of the incinerator to be exceeded. --yes
3 Primary Combustion Chamber The primary combustion chamber must:
Be accepted as the primary combustion zone. --yes
Be equipped with a burner/s burning gas/fuel or low sulphur liquid
fuels. Other combustion methods will be judged on merits. --yes
Ensure primary air supply is controlled efficiently--yes
Ensure minimum exit temperature is not less than 850oC¡ª800-1000 oC
4 Secondary Combustion Chamber (Afterburner). The secondary combustion
chamber must:
Be accepted as secondary combustion zone. --yes
Be fitted with secondary burner/s burning gas or low sulphur liquid fuel
or any suitable fuel. --yes
Ensure secondary air supply is controlled efficiently. --yes
Ensure flame contact with all gases is achieved. --yes
Ensure residence time is not less than two (2) seconds. --yes
Ensure the gas temperature as measured against the inside wall in the
secondary chamber & not in the flame zone, is not less than
1100oC.¡ª1000-1200 oC
Ensure the oxygen content of the emitted gases is not less than
11%.--yes
Ensure both primary and the combustion temperatures are maintained until
all waste has been completely combusted--yes
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--- filter brick
6 Chimney / Stack
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.¡ª6 meter already, can plus 4
meters, free cost
If possible the chimney should be visible to the operator from the
feeding area.¡ªaccording to local site
The addition of dilution air after combustion in order to achieve the
requirement of these guidelines is unacceptable.--yes
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. .--yes
Point for the measurement of emissions shall be provided. .--yes
7 Instrumentation Instrument for determining the inside wall temperature
and not burner flame temperature must be provided for both primary and
secondary chambers.--yes
An audible and visible alarm must be installed to warn the operator when
the secondary temperature drops to below the required temperature.
--none
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--none
8 Location / Siting
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,
Must be housed in a suitably ventilated room.
---according to local site
9 Emission Limits
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
The temperature of the primary chamber shall be 800 ¡À 50o C
The secondary chamber gas residence time shall be at least 1 (one)
second at 1050 ¡À 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
All the emission to the air other than steam or water vapour must be
odourless and free from mist, fume and droplets.
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
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.
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 ¨C 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
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.
A record must be kept of the quantity, type and origin of the waste to
be incinerated.
The incinerator must be preheated to working temperature before charging
any waste.
The incinerator must not be overcharged.
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.
The incinerator operator and all relevant staff must be trained to the
satisfaction of the relevant control authority. ---according to local
site
11 Housekeeping The site where the incinerator is built must:
Have running water.
Have a solid floor.
Have lighting if 24hrs operation
Have fly ash containerization and storage before disposal.
---according to local site
12 Health & Safety (Protective Gear)
Staff handling waste must be well trained on safe handling of hazardous
wastes
Staff must be provided with appropriate protective gear such as, gas
mask, aprons, gumboots, helmets, gloves, goggles.
Caution and Warning signs must be provided.
Fire fighting equipment must be provided
There should be no smoking or eating on the site.
---according to local site
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡
¡¡ |
|