It features unique and advanced merits with compact size, high burning effect, reasonable burning technology, high degree of non-harm etc.It is an ideal choice for waste treatment of hospitals, hotels and various areas.
Features:
(1) Gasifiedpyrolysis incineration is used for burning many kinds of waste.
(2) Waste can be burned once everyday by gasified incineration.
(3) Gasified incineration, mixed incineration and burnout treatment ensures low emission standard of dust,dioxin etc.
(4) Totally enclosed operation is suitable for treating infectious waste to avoid secondary pollution.
(5) Compact structure and small land occupation.
Nanjing Clover Medical Technology Co.,Ltd.
Tel: +86-25-8461 0201
Mobile: +86-13813931455(whatsapp/wechat)
Website: www.hiclover.com
Email: [email protected]
Email: [email protected]
Website: www.hiclover.com
Email: [email protected]
Email: [email protected]
| Items/Model | TS10(PLC) | TS20(PLC) | TS30(PLC) | TS50(PLC) | TS100(PLC) |
| Burn Rate (Average) | 10 kg/hour | 20 kg/hour | 30 kg/hour | 50 kg/hour | 100 kg/hour |
| Feed Capacity(Average) | 20kg | 40kg | 60kg | 100kg | 200 kg |
| Control Mode | PLC | PLC | PLC | PLC | PLC |
| Combustion Chamber | 100L | 210L | 330L | 560L | 1200L |
| Internal Dimensions | 50x50x40cm | 65x65x50cm | 75x75x60cm | 100x80x70cm | 120x100x100cm |
| Secondary Chamber | 50L | 110L | 180L | 280L | 600L |
| Smoke Filter Chamber | Yes | Yes | Yes | Yes | Yes |
| Feed Mode | Manual | Manual | Manual | Manual | Manual |
| Voltage | 220V | 220V | 220V | 220V | 220V |
| Power | 0.5Kw | 0.5Kw | 0.5Kw | 0.7Kw | 0.7Kw |
| Oil Consumption (kg/hour) | 5.4–12.6 | 7.8–16.3 | 10.2–20 | 12.1–24 | 14–28 |
| Gas Consumption (m3/hour) | 6.2–11.4 | 8–15.7 | 9.8–20 | 9.9–26.1 | 10–32.2 |
| Temperature Monitor | Yes | Yes | Yes | Yes | Yes |
| Temperature Protection | Yes | Yes | Yes | Yes | Yes |
| Oil Tank | 100L | 100L | 100L | 100L | 200L |
| Feed Door | 30x30cm | 45x40cm | 55x50cm | 70x55cm | 80x60cm |
| Chimney | 3Meter | 3Meter | 5Meter | 5Meter | 10Meter |
| Chimney Type | Stainless Steel | Stainless Steel | Stainless Steel | Stainless Steel | Stainless Steel |
| 1st. Chamber Temperature | 800℃–1000℃ | 800℃–1000℃ | 800℃–1000℃ | 800℃–1000℃ | 800℃–1000℃ |
| 2nd. Chamber Temperature | 1000℃-1200℃ | 1000℃-1200℃ | 1000℃-1200℃ | 1000℃-1200℃ | 1000℃-1200℃ |
| Residency Time | 2.0 Sec. | 2.0 Sec. | 2.0 Sec. | 2.0 Sec. | 2.0 Sec. |
| Gross Weight | 1500kg | 2200kg | 3000kg | 4500kg | 6000kg |
| External Dimensions | 140x90x120cm | 160x110x130cm | 175x120x140cm | 230x130x155cm | 260x150x180cm |
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
Overall plant layout
Feed chamber/charging
Primary combustion chamber
Particulate scrubbers
Acid gas scrubbers.
The stack/chimney.
Minimum capacity of primary chamber = 0.10cubic meters
Burn rate (rate of waste incineration) = 10 kg per hour
Should have a full width counterbalance loading door allowing easy access to the main chamber for loading and removing ash.
Controlled hygienic mechanical feeding that does not negatively influence the air temperature in the primary and
Overall plant layout
Feed chamber/charging
Primary combustion chamber
Particulate scrubbers
Acid gas scrubbers.
The stack/chimney.
Minimum capacity of primary chamber = 0.10cubic meters
Burn rate (rate of waste incineration) = 10 kg per hour
Should have a full width counterbalance loading door allowing easy access to the main chamber for loading and removing ash.
Controlled hygienic mechanical feeding that does not negatively influence the air temperature in the primary and
secondary chambers of the incinerator shall be used.This chamber should be equipped with burners that use low sulphur fuel.
The chamber should ensure a minimum exit temperature of 850 degrees centigrade.
This unit should operate at over 1100 deg C to ensure complete combustion.
This chamber should be equipped with burners that use low sulphur fuel.
Heavy-duty steel casing
High quality refractory lining and insulation
Large full size top load door and liquid retention sill.
1 x oil fired ignition burners operated on/off
Combustion efficiency (C.E) shall be at least 99.00% where C.E = %Carbon dioxide x 100 / [% Carbon dioxide + carbon monoxide]
The temperature of the primary chamber shall be 800 +/- 50 degrees centigrade
The secondary chamber gas residence time shall be at least 1 second at 1050 +/- 50 degrees centigrade with 3% oxygen in the stack gas.
Opacity of the smoke must not exceed 20% viewed from 50 metres with naked eyes.
All the emission to the air other than steam or water vapour must be odourless and free of mist, fume and droplets.
A 99.99% destruction and removal efficiency (DRE) for each principal organic hazardous constituent (POHC) in the waste feed where DRE [ ( Win – Wout) /Win ] x
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 emission should not exceed 80mg/m3 total dioxins and furans if measured for a period of 6 to 16 hours.
The chamber should ensure a minimum exit temperature of 850 degrees centigrade.
This unit should operate at over 1100 deg C to ensure complete combustion.
This chamber should be equipped with burners that use low sulphur fuel.
Heavy-duty steel casing
High quality refractory lining and insulation
Large full size top load door and liquid retention sill.
1 x oil fired ignition burners operated on/off
Combustion efficiency (C.E) shall be at least 99.00% where C.E = %Carbon dioxide x 100 / [% Carbon dioxide + carbon monoxide]
The temperature of the primary chamber shall be 800 +/- 50 degrees centigrade
The secondary chamber gas residence time shall be at least 1 second at 1050 +/- 50 degrees centigrade with 3% oxygen in the stack gas.
Opacity of the smoke must not exceed 20% viewed from 50 metres with naked eyes.
All the emission to the air other than steam or water vapour must be odourless and free of mist, fume and droplets.
A 99.99% destruction and removal efficiency (DRE) for each principal organic hazardous constituent (POHC) in the waste feed where DRE [ ( Win – Wout) /Win ] x
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 emission should not exceed 80mg/m3 total dioxins and furans if measured for a period of 6 to 16 hours.
