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BETTER
8421299090
It consists of feeding system, reaction system, control system, mixing and absorption system, security system.
NaCLO3+2HCL→CLO2+1/2CL2+NaCL+H2O
Raw material:sodium chlorate(GB/T1618-1995, content≥99%),
hydrochloric acid(GB320-93, concentration≥31%).
(1) For production of compound disinfectant (chlorine dioxide as main, chlorine gas as auxiliary), calculated by available chlorine, CLO2 content>75%.
(2) Flow-meter dosage system for transferring raw material ensures simple operation, accurate material
input, un-blockage and stable performance.
(3) Main reaction pot adopts imported compound material that is temperature-resistant, anti-corrosion with long life time.
(4) Total convertible rate of raw material≥85%,low energy consumption.
(5) Semi-auto run of machine, no need of extra worker if there’s enough material.
(6) Upper-positioned material basket is suitable for low water pressure area.
1g available chlorine consumes 0.65g sodium chlorate and 1.3g hydrochloric acid
Model | Available chlorine output(g/h) | Pressure(Mpa) | DN1(mm) | DN(mm) | Power(Kw) |
BT-50 | 50 | ≥0.20 | 25 | 32 | 1.0 |
BT-100 | 100 | ≥0.20 | 25 | 32 | 1.0 |
BT-200 | 200 | ≥0.20 | 25 | 32 | 1.0 |
BT-300 | 300 | ≥0.20 | 25 | 32 | 1.0 |
BT-500 | 500 | ≥0.20 | 25 | 32 | 1.0 |
BT-800 | 800 | ≥0.25 | 25 | 32 | 1.0 |
BT-1000 | 1000 | ≥0.25 | 32 | 40 | 2.0 |
BT-2000 | 2000 | ≥0.25 | 32 | 40 | 2.0 |
BT-3000 | 3000 | ≥0.30 | 32 | 40 | 2.0 |
BT-4000 | 4000 | ≥0.30 | 40 | 50 | 2.0 |
BT-5000 | 5000 | ≥0.30 | 40 | 50 | 2.0 |
BT-6000 | 6000 | ≥0.30 | 40 | 50 | 3.0 |
BT-7000 | 7000 | ≥0.30 | 40 | 50 | 3.0 |
BT-10000 | 10000 | ≥0.30 | 50 | 60 | 3.0 |
BT-15000 | 15000 | ≥0.30 | 50 | 60 | 3.0 |
BT-20000 | 20000 | ≥0.30 | 50 | 60 | 3.0 |
It consists of feeding system, reaction system, control system, mixing and absorption system, security system.
NaCLO3+2HCL→CLO2+1/2CL2+NaCL+H2O
Raw material:sodium chlorate(GB/T1618-1995, content≥99%),
hydrochloric acid(GB320-93, concentration≥31%).
(1) For production of compound disinfectant (chlorine dioxide as main, chlorine gas as auxiliary), calculated by available chlorine, CLO2 content>75%.
(2) Flow-meter dosage system for transferring raw material ensures simple operation, accurate material
input, un-blockage and stable performance.
(3) Main reaction pot adopts imported compound material that is temperature-resistant, anti-corrosion with long life time.
(4) Total convertible rate of raw material≥85%,low energy consumption.
(5) Semi-auto run of machine, no need of extra worker if there’s enough material.
(6) Upper-positioned material basket is suitable for low water pressure area.
1g available chlorine consumes 0.65g sodium chlorate and 1.3g hydrochloric acid
Model | Available chlorine output(g/h) | Pressure(Mpa) | DN1(mm) | DN(mm) | Power(Kw) |
BT-50 | 50 | ≥0.20 | 25 | 32 | 1.0 |
BT-100 | 100 | ≥0.20 | 25 | 32 | 1.0 |
BT-200 | 200 | ≥0.20 | 25 | 32 | 1.0 |
BT-300 | 300 | ≥0.20 | 25 | 32 | 1.0 |
BT-500 | 500 | ≥0.20 | 25 | 32 | 1.0 |
BT-800 | 800 | ≥0.25 | 25 | 32 | 1.0 |
BT-1000 | 1000 | ≥0.25 | 32 | 40 | 2.0 |
BT-2000 | 2000 | ≥0.25 | 32 | 40 | 2.0 |
BT-3000 | 3000 | ≥0.30 | 32 | 40 | 2.0 |
BT-4000 | 4000 | ≥0.30 | 40 | 50 | 2.0 |
BT-5000 | 5000 | ≥0.30 | 40 | 50 | 2.0 |
BT-6000 | 6000 | ≥0.30 | 40 | 50 | 3.0 |
BT-7000 | 7000 | ≥0.30 | 40 | 50 | 3.0 |
BT-10000 | 10000 | ≥0.30 | 50 | 60 | 3.0 |
BT-15000 | 15000 | ≥0.30 | 50 | 60 | 3.0 |
BT-20000 | 20000 | ≥0.30 | 50 | 60 | 3.0 |