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Cooperation Intent Form
UASB Anaerobic Reactor
The UASB reactor wastewater is introduced as uniformly as possible into the bottom of the reactor, and the wastewater passes upward through a sludge bed containing granular sludge or flocculent sludge. Anaerobic reactions occur in the process of contact between wastewater and sludge particles. The biogas produced in the anaerobic state (mainly methane and carbon dioxide) causes an internal circulation, which is beneficial for the formation and maintenance of granular sludge. Some of the gas formed in the sludge layer adheres to the sludge particles, and the attached and non-attached gas rises to the top of the reactor. The sludge rising to the surface hits the bottom of the gas emitter of the three-phase reactor, causing degassing of the sludge flocs with attached gas bubbles. After the bubbles are released, the sludge particles will settle to the surface of the sludge bed, and the attached and unattached gases are collected in the plenum of the three-phase separator at the top of the reactor.
Category: Anaerobic reactor
Product Details
Product Introduction
The UASB reactor wastewater is introduced as uniformly as possible into the bottom of the reactor, and the wastewater passes upward through a sludge bed containing granular sludge or flocculent sludge. Anaerobic reactions occur in the process of contact between wastewater and sludge particles. The biogas produced in the anaerobic state (mainly methane and carbon dioxide) causes an internal circulation, which is beneficial for the formation and maintenance of granular sludge. Some of the gas formed in the sludge layer adheres to the sludge particles, and the attached and non-attached gas rises to the top of the reactor. The sludge rising to the surface hits the bottom of the gas emitter of the three-phase reactor, causing degassing of the sludge flocs with attached gas bubbles. After the bubbles are released, the sludge particles will settle to the surface of the sludge bed, and the attached and unattached gases are collected in the plenum of the three-phase separator at the top of the reactor.


Equipment parameters
|
Model |
Diameter φ(mm) |
Height H(mm) |
Volume load (KgCOD/m³ · d) |
Biogas gas production (m³/KgCOD) |
Scope of use |
|
L-UASB-4-7 |
4000 |
7000 |
3~6 |
0.2~0.4 |
Papermaking, alcohol production, food processing, soy products processing, Landfill leachate, aquaculture wastewater, starch wastewater, etc. |
|
L-UASB-5-8 |
5000 |
8000 |
3~6 |
||
|
L-UASB-7-9 |
7000 |
9000 |
3~6 |
||
|
L-UASB-7-10 |
7000 |
10000 |
1~10 |
||
|
L-UASB-8-10 |
8000 |
10000 |
5~10 |
||
|
L-UASB-8-12 |
8000 |
12000 |
5~10 |
||
|
L-UASB-9-12 |
9000 |
12000 |
5~10 |
||
|
L-UASB-9-14 |
9000 |
14000 |
5~10 |
Anaerobic reactors are divided into the first generation, the second generation and the third generation of anaerobic reactors:
|
Comparison and summary of advantages and disadvantages and application scope of anaerobic digestion reactor |
|||||
|
Sequence |
Type |
Name |
Advantages |
Disadvantages |
Scope of application |
|
1 |
first generation |
CADT |
Simple structure, small investment |
Long hydraulic retention time and inconvenient management |
Organic wastewater with high concentration and high suspended solids |
|
2 |
CSTR |
Simple structure, small investment, simple operation and management |
Low volume load rate, low efficiency and poor effluent quality |
Suitable for sludge treatment with high SS content |
|
|
3 |
ACP |
Less investment, simple operation and management, high volume load rate, strong load capacity. |
Relatively long residence time and relatively poor effluent quality |
Suitable for organic wastewater with high concentration and high suspended solids |
|
|
4 |
USR |
High processing efficiency, not easy to block, less investment, simple operation and management, high volume load rate |
Relatively strict structural constraints, small monomer volume |
Suitable for organic wastewater with high solid content |
|
|
5 |
PFR |
Less investment, simple operation and management, low energy consumption |
The volume load rate is low, the efficiency is low, the reactor is easy to block, and the temperature is unstable |
Suitable for sludge treatment with high SS content |
|
|
6 |
Second Generation |
AF |
High treatment efficiency, strong load tolerance, relatively good effluent quality |
The investment is large, and the reactor is easy to short-circuit and block. |
Suitable for organic wastewater with low SS content |
|
7 |
AFBR |
Good internal mixing state, strong load resistance, fast starting speed |
Large investment and high equipment maintenance costs |
Suitable for organic wastewater with low SS content |
|
|
8 |
UASB |
High treatment efficiency, strong load resistance, relatively good effluent quality, simple process structure |
Relatively large investment, strict requirements for wastewater SS content |
Suitable for organic wastewater with low SS content |
|
|
9 |
Third Generation |
EGSB |
High treatment efficiency, strong load tolerance, relatively good effluent quality |
Relatively large investment, strict requirements for wastewater SS content |
Suitable for organic wastewater with less SS content and relatively low concentration |
|
10 |
IC |
High processing efficiency, not easy to block, less investment, simple operation and management, high volume load rate, good impact load effect |
Relatively long residence time and relatively poor effluent quality |
Suitable for organic wastewater with low SS content |
|
IC anaerobic reactor IC


Keywords: UASB Anaerobic Reactor