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MICRO BUBBLE-SCRUBBER SYSTEM

MICRO BUBBLE-SCRUBBER SYSTEM
Product Description

MECHANISM Through non-throttle reverse nozzle, the solution jet into scrub tube reverse against the flue gas, and the gas collides with the liquid, forming a strong turbulent zone in the gas-liquid interface area. The fluid momentum reaches equilibrium, the gas and liquid are in close contact to produce a stable turbulent bubble zone. The bubble zone floats in the airflow and rises and falls with the relative momentum of the gas and liquid phases.

APPLICATION & INDUSTRIES




 

DESCRIPTION




 

STRUCTURAL

lHIGH-EFFICIENCY GAS-LIQUID / SUB-MICRON PARTICLE REMOVAL DEVICE
lGAS DISTRIBUTION DEVICE / WATER-SAVING DEVICE
lCONDENSING GAS-LIQUID SEPARATION DEVICE (NO FLUSHING)

 


 

STRUCTURAL

QUENCH/FLUID TANGENTIAL-DIRECTION DEVICE

Turbulent bubble flow / wall protection / full utilization of evaporation latent heat
The maximum mixing density in limited volume
1s achieve the saturation temperature to avoid the formation of dioxins

HIGH GAS SPEED TUBE

Reduces tube diameter and occupied area effectively
No internal design to ensure smooth gas path
Large effective reaction area

REVERSE JET NOZZLE

High solid content solution can be handled (max 20%)
High viscosity dust can be removed
Viscous solution can be handled
None-atomized solution, lower mist entrainment

HIGH EFFICIENT GAS-LIQUID/SOLID SEPARATING SYSTEM

High-efficiency gas-liquid / sub-micron particle removal device
Forced oxidation device
Gas distribution device / water-saving device
Condensing gas-liquid/solid separation device (no flushing)

 



 

TYPICAL PROCESS FLOW OF DUSTY FLUE GAS ULTRA-LOW EMISSION

PROCESS CHARACTERISTIC:
Impact foam scrub technology coupling efficient filler process
High purification efficiency, exhaust emission<10ppm
Less equipment and piping, instrumentation, pumps, etc.
Compact system, small footprint

 


 

PROCESS CHARACTERISTIC

Micro bubble scrubbing technology coupling condensation internals

High removal efficiency, particle size>5μm can be removed
Less equipment and piping, instrumentation, pumps, etc.
Compact system, small footprint.
30%~50% less discharge compares to traditional scrubber.

 



 

PERFORMANCE

SUITABLE FOR HIGH VOLUME AND LOAD FLUCTUATION CONDITIONS
Suitable for limited space
Higher gas volume can be treated under the same space scale
Ability to adapt 50%~120% fluctuation
SUITABLE FOR HIGH VISCOSITY, EASY PLUGGING AND VISCOUS CONDITIONS
High solid content solution can be handled (max 20%)
High viscosity dust can be removed
Viscous solution  can be handled
SUITABLE FOR MULTI-CONDITION COUPLING CONDITIONS
Gas quench + dust removal + acid gas absorption + forced oxidation
Simple operation with minimal controls
HIGH EFFICIENCY
Efficiency >99%, far beyond the traditional scrubber.
Particle size>2.5μm can be removed

 


 

LITHIUM IRON PHOSPHATE PRECURSOR PHOSPHORUS FLUE GAS SYSTEM

Micro bubble scrubber system Traditional process pain points:
High viscosity dust, easy to block the nozzle and pipeline
Risk of inspection and maintenance(Contain toxic CO)
Low recovery of phosphorus
Advantage:
Additional recovery of yellow phosphorus 144 t/a
Less floor area (4 stages to 2 stages)
Less maintenance, more safety for operator

SULFUR RECOVERY UNIT FLUE GAS SYSTEM

Micro bubble scrubber system Traditional process disadvantages:
Large fluctuate (minimum load 30%)
Strong sulfuric acid corrosion
Easy blocked pipelines and nozzles of spray tower
Advantages:
Long-term running system
Overall cost is reduced by 36 %
Moderate resistance promotes SO3 removal
Outlet SO2 concentration<10mg/m3

POLYSILICON SLURRY HYDROLYSIS FLUE GAS SYSTEM

Micro bubble scrubber system Traditional process disadvantages:
Small particle size, easy coalesced and blocked
Sampling port spraying solution easy to hurt operator
Advantages:
Long-term running system
Effectively relieves the spray of sampling port
Emission dust concentration<15mg/m3
Emission HCI concentration<10mg/m3

CCUS CO2 flue gas purification and waste heat recovery system

Micro bubble scrubber system Traditional process disadvantages :
Unreasonable utilization of heat
High energy consumption of cooling system
Advantages:
Improve waste heat recovery efficiency, meanwhile obtain high purity CO2
Less floor area
50~150 % system load regulation ability
Flue gas temperature after condensation<40℃

 


 

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