IS 70901985AI Search Enabled✦ AI Generated

Guidelines for rapid mixing devices

IS 7090:1985 provides comprehensive guidelines for the design, construction, and operation of rapid mixing devices used in water treatment plants to ensure effective and uniform dispersion of coagulants. It covers mechanical mixers (vane, propeller, jet types) and hydraulic mixers (hydraulic jump, baffled channels), focusing on parameters like velocity gradient, detention time, and power requirements. This standard is essential for engineers and professionals involved in designing and maintaining water treatment rapid mixing systems in India.

11Sections
51Clauses Indexed
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1985Edition
Public Health EngineeringCategory
Alternative search terms: IS 7090 PDF, IS 7090 pdf free download, IS 7090 free download pdf, IS7090 PDF, IS-7090 PDF, IS 7090 1985 PDF, IS 7090:1985 PDF, IS 7090-1985 PDF, IS 7090 (1985) PDF, IS 7090 1985 edition PDF, IS 7090 edition 1985 PDF

What This Standard Covers

IS 7090:1985 provides comprehensive guidelines for the design, construction, and operation of rapid mixing devices used in water treatment plants to ensure effective and uniform dispersion of coagulants. It covers mechanical mixers (vane, propeller, jet types) and hydraulic mixers (hydraulic jump, baffled channels), focusing on parameters like velocity gradient, detention time, and power requirements. This standard is essential for engineers and professionals involved in designing and maintaining water treatment rapid mixing systems in India.

Who Uses This Standard

  • Water Treatment Plant Engineers
  • Public Health Engineers
  • Civil and Environmental Engineers
  • Mechanical Engineers specializing in water infrastructure
  • Water Quality Control Specialists
  • Municipal Water Supply Authorities
  • Water Treatment Equipment Manufacturers

Key Topics Covered

Mechanical rapid mixing devices
Hydraulic mixing methods
Velocity gradient and detention time
Design parameters for vane, propeller, and jet mixers
Materials and construction guidelines
Power requirements and motor specifications
Hydraulic jump and baffled channel design
Maintenance and operational considerations
Control systems and motor starters
Performance criteria for rapid mixers
Coagulant dispersion techniques
Safety and structural requirements

Table of Contents

1Scope

IS 7090 - Scope Key Points & Tables

Scope Summary:

  • Covers mechanical and hydraulic mixing devices for water treatment.
  • Defines detention time, velocity gradient, and power input for mixers.
  • Includes specifications for hydraulic jump rapid mixing.

Key Table: Mechanical Mixing Devices (Clause 3.1.3)

Detention Time (sec)Velocity Gradient (s⁻¹)Net Power Input (W/m³ tank volume)Net Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power values are at 30°C water temperature.


Hydraulic Jump (Clause 5.1) Specifications:

  • Velocity before jump: 3 to 3.5 m/s
  • Head loss ≥ 300 mm at design flow
  • Provides rapid mixing without mechanical units

Hydraulic Mixing Channel (Clause 1.5):

  • Baffle angle: 40° to 90° to channel wall
  • Minimum velocity at baffle: 1.5 m/s
  • Channel walls: brick/stone masonry or RCC, smooth finish
  • Minimum freeboard: 150 mm

This standard guides design for effective mixing in water treatment, ensuring proper energy input and flow conditions for coagulation and rapid mixing.

2Definitions

IS 7090 - Key Definitions & Specifications

1. Definitions (Clause 2.0)

  • Standard terms related to rapid mixing in water treatment.
  • Includes mechanical mixing devices, hydraulic jump, motor types, etc.

2. Mechanical Mixing Devices (Clause 3.1.3, Table 1)

Detention Time (s)Velocity Gradient (s⁻¹)Net Power Input (W/m³ tank volume)Net Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6
  • Note: Power calculations assume water temperature 30°C.

3. Hydraulic Jump (Clause 5.1)

  • A rapid mixing method without mechanical units.
  • Water velocity: 3 to 3.5 m/s in a sloping flume.
  • Head loss at design flow: ≥ 300 mm.
  • Kinetic energy dissipated in a pool ensures turbulence and mixing.

4. Motor Specifications (Clause 3.2.6)

  • For vane/propeller mixers:
    • Totally enclosed fan-cooled (TEFC) motors, IS:325-1978.
    • Cooling method IC 41 (IS:6362-1971).
    • Protection: IP 54 or better (IS:4691-1985).

Summary Diagram: Flash Mixer Layout

flowchart LR
    RW(Raw Water Inlet Main) --> FM(Flash Mixer Chamber)
    FM --> CP(Chemical Dosing Pipe)
    FM --> DP(Delivery from Flash Mixer)
    DP --> SB(Strainer Box)
    SB --> IV(Isolating Valve)
    IV --> PUMP(Pump Suction)

This concise overview covers key definitions, power input data, hydraulic jump criteria, and motor specs per IS 709

3Design Considerations and Construction

IS 7090: Key Design & Construction Specifications

1. Hydraulic Mixing (Clause 1.5)

  • Baffle angle: 40° to 90° with channel wall.
  • Minimum velocity: 1.5 m/s while negotiating the baffle.
  • Materials: Main channel walls - brick masonry, stone masonry, or RCC, finished smooth to avoid weed growth.
  • Baffle: Concrete or brick, similarly finished.
  • Freeboard: Minimum 150 mm above water surface.

2. Mechanical Mixing Devices (Clause 3.1.3)

Detention Time (s)Velocity Gradient (s⁻¹)Net Power Input (W/m³ tank volume)Net Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Power values based on 30°C water temperature.

3. Hydraulic Jump (Clause 5.1)

  • Velocity before jump: 3 to 3.5 m/s.
  • Headloss: Minimum 300 mm at design flow.
  • Purpose: Rapid mixing via turbulence without mechanical units.

Summary Diagram: Hydraulic Mixing Channel Setup

flowchart LR
    A[Inlet Water] --> B[Channel Wall]
    B --> C[Baffle (40°-90° angle)]
    C --> D[Velocity ≥ 1.5 m/s]
    D --> E[Outlet]
    style B fill:#f9f,stroke:#333,stroke-width:2px
    style C fill:#bbf,stroke:#333,stroke-width:2px

Note: Use smooth finishes on masonry/concrete surfaces to prevent weed growth and ensure hydraulic efficiency.

3.1Mechanical Mixing Devices

IS 7090: Mechanical Mixing Devices Key Points

1. Recommended Detention Time, Velocity Gradient & Net Power (Clause 3.1.3, Table 1)

Detention Time (s)Velocity Gradient (G, s⁻¹)Net Power Input (W/m³ tank volume)Power Input (W/m³/h water treated)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power values based on water temperature 30°C.


2. Propeller Mixer Design (Clause 3.1.4)

  • Impeller speed: 400 rpm (large) to 1400 rpm (small)
  • Tank diameter to impeller diameter ratio: 5:1 to 3:1
  • Tank height to diameter ratio: 1:1 to 3:1
  • Blades mounted on vertical/inclined shaft producing axial flow.

3. General Notes (Clause 4.1)

  • Mechanical mixers: effective, low headloss, adjustable speed.
  • Require electrical energy and regular maintenance.

Formula for Power Input (P):

[ P = \mu \times G^2 \times V ]

Where:

  • (P) = Power input (W)
  • (\mu) = Dynamic viscosity of water (Pa·s)
  • (G) = Velocity gradient (s⁻¹)
  • (V) = Volume of tank (m³)

flowchart LR
    A[Tank Dimensions]
    B[Impeller Diameter]
    C[Rotation Speed (400-1400 rpm)]
    D[Velocity Gradient (G)]
    E[Power Input (P)]
    A --> B --> C --> D --> E

This summarizes key IS 709

3.2Components of Mechanical Mixers

IS 7090: Components of Mechanical Mixers - Key Specifications & Formulas

1. Mechanical Mixing Devices (Clause 3.1)

  • Mixers include vane or propeller types, centrally installed in chambers.
  • Shaft max unsupported length: 3 m to avoid vibration.
  • Shaft speed: 60 to 100 rpm.

2. Recommended Detention Time, Velocity Gradient & Power Input (Clause 3.1.3, Table 1)

Detention Time (s)Velocity Gradient (G, s⁻¹)Power Input (W/m³ tank volume)Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6
  • Power calculations assume water temperature at 30°C.

3. Motor Specifications (Clause 3.2.6)

  • Motor type: Totally enclosed fan-cooled (TEFC), conforming to IS 325-1978.
  • Cooling method: IC 41 per IS 6362-1971.
  • Protection: Minimum IP 54 enclosure per IS 4691-1985.

Additional Notes:

  • Vane mixers have inlet either top or bottom; top inlet requires level adjustment to avoid water heading.
  • Proper design per Table 1 ensures efficient mixing.

flowchart LR
    RawWaterInlet --> FlashMixerChamber
    FlashMixerChamber --> DeliveryFromMixer
    DeliveryFromMixer --> ChemicalDosingPipe
    ChemicalDosingPipe --> PointOfApplication
    FlashMixerChamber --> MotorDrivenPump

This layout illustrates typical jet type flash mixer flow.


Summary: Use Table 1 for power and velocity gradient selection, maintain shaft length ≤3 m, rpm 60-100, and select a TEFC motor

3.3Motors and Controls

IS 7090: Motors and Controls - Key Formulas & Specifications

Motor Selection (Clause 3.1.2)

  • Net Power Input = Power from Table 1 (see below)
  • Motor Capacity = Net Power Input / (Overall Efficiency)
  • Assume Overall Efficiency ≤ 75% to account for electrical & mechanical losses.

Table 1: Recommended Power Input for Mechanical Mixing Devices

Detention Time (s)Velocity Gradient (s⁻¹)Net Power Input (W/m³ tank volume)Net Power Input (W/m³/h water flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power values assume water temperature at 30°C.

Motor Specifications (Clause 3.2.6)

  • Motor Type: Totally enclosed fan-cooled (TEFC)
  • Cooling Method: IC 41 (IS 6362-1971)
  • Enclosure Protection: Minimum IP 54 (IS 4691-1985)
  • Applicable for vane or propeller mixers.

Controls (Clause 3.4)

  • Push button control at unit; remote control optional.
  • Starters: Star-delta type, oil-immersed break type (IS 8544 Part 2-1977).
  • Enclosure Protection: Minimum IP 54 (IS 2147-1562).

Motor Capacity Calculation Example:

[ \text{Motor Capacity} = \frac{\text{Net Power Input}}{0.75} ]

If Net Power Input = 288 W/m³ (for 30 sec detention), [ \text{Motor Capacity} = \frac{288}{0.75} = 384 \text{ W/m}^3 ]


flowchart TD
    A[Determine
4Painting of Fabricated Parts

IS 7090 - Painting of Fabricated Parts: Key Points

  • Primer: Use Red Oxide (Zinc Chromate) as primer.
  • Coats: Apply 1 coat of primer + at least 3 coats of finishing paint after erection (Clause 4.1).

Relevant Table: Mechanical Mixing Devices (Clause 3.1.3)

Detention Time (sec)Velocity Gradient (s⁻¹)Net Power Input (W/m³ tank volume)Net Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power calculations at 30°C water temperature.


Additional Specifications

  • Motor for mixers: Totally enclosed fan-cooled type, IP54 protection, conforming to IS:325-1978 and IS:6362-1971 (Clause 3.2.6).
  • Starter: Star-delta type as per IS:8544 (Part 2)-1977.
  • Enclosures: Protection rating IP54 as per IS:2147-1562.

Summary for Painting Fabricated Parts

  • Use Red Oxide Zinc Chromate primer.
  • Apply 1 primer coat + minimum 3 finishing coats post-erection.
  • Follow motor and starter specs for hydraulic mixing devices if applicable.
flowchart LR
    A[Fabricated Part] --> B[Apply 1 Coat Red Oxide Primer]
    B --> C[Apply 3+ Coats Finishing Paint]
    C --> D[After Erection]

This ensures corrosion protection and durability as per IS 7090.

5Hydraulic Mixing

Hydraulic Mixing as per IS 7090

Key Specifications:

  1. Mechanical Rapid Mixing (Clause 3.1.1 & Table 1):
    • Detention Time: 20 to 60 seconds
    • Velocity Gradient (G): 300 to 900 sec⁻¹
    • Net Power Input: Varies with detention time and velocity gradient
Detention Time (s)Velocity Gradient (sec⁻¹)Power Input (W/m³ tank volume)Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power values are for water at 30°C.

  1. Hydraulic Jump Mixing (Clause 5.1):

    • Velocity in flume: 3 to 3.5 m/s
    • Headloss at design flow: ≥ 300 mm
    • Rapid mixing achieved by turbulence from hydraulic jump without mechanical units.
  2. Motor Specifications (Clause 3.2.6):

    • Totally enclosed fan-cooled motors (IC 41)
    • Protection: IP 54 or better
    • Conforms to IS:325-1978, IS:6362-1971, IS:4691-1985

Formula for Velocity Gradient (G):

[ G = \sqrt{\frac{P}{\mu V}} ]

  • (P) = Power input (W)
  • (\mu) = Dynamic viscosity (Pa·s)
  • (V) = Volume of fluid (m³)

Conceptual Diagram: Hydraulic Jump Mixing

flowchart LR
    A[Coagulant Injection] --> B[Sloping Widening Flume]
    B --> C[High Velocity Flow (3-3
5.1Hydraulic Jump

Hydraulic Jump (IS 7090 Key Points):

  • Definition: Sudden transition in open channel flow from supercritical (high velocity, low depth) to subcritical flow (low velocity, high depth), causing turbulence and energy dissipation.
  • Velocity in flume: 3 to 3.5 m/s before jump.
  • Head loss: Minimum 300 mm at design flow to ensure adequate mixing.
  • Purpose: Provides rapid mixing without mechanical devices by dissipating kinetic energy in a pool downstream.

Important Specifications:

  • Coagulant introduced before flume.
  • Flume is open, sloping, and widening.
  • Turbulence from jump ensures effective mixing.

Hydraulic Jump Formulas:

ParameterFormulaDescription
Froude Number (Fr)( Fr = \frac{V}{\sqrt{g y}} )V = velocity (m/s), y = depth (m), g = 9.81 m/s²
Sequent Depths Relation( \frac{y_2}{y_1} = \frac{1}{2} \left( \sqrt{1 + 8 Fr_1^2} - 1 \right) )y1 = initial depth, y2 = sequent depth after jump
Energy Loss (hL)( h_L = \frac{(y_2 - y_1)^3}{4 y_1 y_2} )Head loss due to jump (m)

Design Notes:

  • Ensure flow velocity before jump is 3–3.5 m/s.
  • Head loss ≥ 0.3 m for effective mixing.
  • Use a sloping, widening flume to facilitate jump formation.
flowchart LR
    A[High Velocity Flow] -->|Supercritical| B[Hydraulic Jump]
    B -->|Energy Dissipation| C[Low Velocity Flow]
    C --> D[Slow Moving Pool]
    D --> E[Effective Mixing Zone]

This ensures rapid initial mixing in water treatment without mechanical mixers.

5.2Baffled Channels

Key Specifications & Formulas for Baffled Channels (IS 7090):

  • Definition (Clause 2.5): Baffled channels have fins/blades on alternate opposite walls to promote flow mixing.

  • Design Velocity (Clause 5.2):
    Design channel velocity (excluding baffles) = 0.6 m/s

  • Baffle Plate Material (Clause 3.2.9):
    Mild steel conforming to IS: 1730 (Part 1)-1974

  • Baffle Angle & Velocity (Clause 1.5 Table 5):

    • Baffle angle with channel wall: 40° to 90°
    • Minimum velocity near baffle: 1.5 m/s
  • Construction:

    • Main walls: Brick/stone masonry or RCC, finished smooth
    • Baffles: Concrete or brick, similarly finished
    • Minimum freeboard: 150 mm

Design Summary Table

ParameterValue/Specification
Channel velocity (no baffle)0.6 m/s
Velocity near baffle≥ 1.5 m/s
Baffle angle40° to 90°
Baffle materialMild steel (IS:1730 Part 1-1974)
Wall materialBrick masonry / Stone / RCC
Minimum freeboard150 mm

Flow Around Baffle Concept (Mermaid Diagram)

flowchart LR
    A[Inflow] --> B{Baffle Plate}
    B -->|Flow splits| C[Flow around baffle end]
    C --> D[Mixing zone]
    D --> E[Outflow]

Note: Ensure smooth finishes to prevent weed growth and maintain hydraulic efficiency.

AnnexuresRecommended Detention Time, Velocity Gradient, and Power Input

Here are the key formulas, tables, and specifications from IS 7090 for Detention Time, Velocity Gradient, and Power Input:


1. Detention Time (t)

  • Time water is retained in the rapid mix unit.
  • Formula:
    [ t = \frac{V}{Q} ]
    where:
    • ( V ) = volume of water in the mixer (m³)
    • ( Q ) = flow rate (m³/s)

2. Velocity Gradient (G)

  • Rate of velocity change perpendicular to flow (sec⁻¹).
  • From power input and viscosity:
    [ G = \sqrt{\frac{P}{\mu}} ]
    where:
    • ( P ) = power input per unit volume (W/m³)
    • ( \mu ) = absolute viscosity of water (N·s/m²)

3. Recommended Values (Table 1 from Clause 3.1.3)

Detention Time (s)Velocity Gradient (sec⁻¹)Power Input (W/m³)Power Input (W/m³/h Flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Note: Power values are for water at 30°C.


Summary:

  • Design detention time: 20 to 60 seconds
  • Velocity gradient: 300 to 900 sec⁻¹
  • Power input increases with decreasing detention time and increasing velocity gradient.

flowchart LR
    A[Water Flow Q] --> B[Rapid Mix Unit Volume V]
    B --> C[Calculate Detention Time t = V/Q]
    C --> D[Select Velocity Gradient G (300-

Popular Questions About IS 7090

?What are the recommended velocity gradients and detention times for different types of rapid mixers?

IS 7090 Recommendations for Rapid Mixers:

  • Detention Time: 20 to 60 seconds at design flow.
  • Velocity Gradient (G): 300 to 900 sec⁻¹.
  • Net Power Input: Varies with detention time and velocity gradient.
Detention Time (s)Velocity Gradient (sec⁻¹)Power Input (W/m³ tank volume)Power Input (W/m³/h flow)
60300721.2
503601041.4
404501621.8
306002882.4
257204142.9
209006483.6

Additional Notes:

  • Velocity gradient ( G ) is calculated by:
    [ G = \sqrt{\frac{P}{\mu}} ]
    where ( P ) = power input per unit volume (W/m³), and ( \mu ) = absolute viscosity of water (Pa·s).

  • Detention time ( t ) = Volume of mixer / Flow rate.

This ensures effective rapid mixing for coagulation in water treatment.

Loading diagram...
?Which materials are specified for construction of mixer components like shafts, vanes, and baffles?

According to IS 7090, the materials specified for mixer components are:

  • Vanes: Made of mild steel conforming to IS 1730 (Part 1)-1974 (steel plates for structural/general engineering).
  • Propellers: Made of cast steel conforming to IS 2644-1979 (specification for high tensile steel castings).
  • Shafts: While not explicitly mentioned, shafts are typically made from mild steel or carbon steel with adequate strength and toughness, following general engineering standards (e.g., IS 2062 for structural steel).

Key Points:

  • Vanes = Mild steel (IS 1730 Part 1)
  • Propellers = Cast steel (IS 2644)
  • Shaft max unsupported length = 3 m (to avoid vibration)
  • Shaft speed = 60 to 100 rpm

This ensures durability and structural integrity of the mixer under operating conditions.

Loading diagram...
?How does the standard define and differentiate between mechanical and hydraulic mixing devices?

IS 7090 differentiates mechanical and hydraulic mixing devices as follows:

Mechanical Mixing Devices (Clause 3.1, 4.1)

  • Use mechanical energy (usually electric motors).
  • Common types: vane type, propeller type, jet type mixers.
  • Advantages:
    • Effective mixing with little headloss.
    • Operation adjustable by changing rotation speed.
    • Unaffected by small flow fluctuations.
  • Disadvantages:
    • Require electrical energy.
    • Need regular maintenance and supervision.

Hydraulic Mixing Devices (Clause 1.1)

  • Use hydraulic energy (flow-induced turbulence).
  • Types include hydraulic jump and baffled channels.
  • Operate without external power; rely on flow conditions.
  • Suitable where mechanical energy or power supply is limited.

Summary Table

FeatureMechanical MixersHydraulic Mixers
Energy SourceElectrical/mechanicalFlow-induced hydraulic energy
Typical TypesVane, Propeller, JetHydraulic jump, Baffled channel
ControlSpeed variation possibleFlow-dependent
MaintenanceRequires regular maintenanceMinimal
HeadlossLowVaries with flow
Loading diagram...

This classification helps select appropriate mixers based on power availability, maintenance capacity, and flow conditions.

?What are the power and motor requirements for vane and propeller type mixers?

Power and Motor Requirements for Vane and Propeller Type Mixers (IS 7090)

  • Propeller Mixers (Clause 3.1.4):

    • Speed range: 400 to 1400 rpm (lower rpm for large diameter, higher for smaller).
    • Tank to impeller diameter ratio: 3:1 to 5:1.
    • Tank height to diameter ratio: 1:1 to 3:1.
    • High flow displacement with axial currents.
    • Power depends on impeller size, fluid properties, and desired flow but generally requires high-speed motors capable of maintaining 400-1400 rpm.
  • Vane Type Mixers (Clause 3.1.3):

    • Shaft speed: 60 to 100 rpm.
    • Maximum unsupported shaft length: 3 m to avoid vibration.
    • Installed centrally with vanes, designed per Table 1 (not provided here).
    • Requires lower speed motors with sufficient torque for vane resistance.
  • General (Clause 4.1):

    • Mechanical mixers require electrical motors.
    • Power rating depends on tank size, fluid viscosity, and mixer type.
    • Regular maintenance and supervision needed.

Typical Power Estimation Formula (General guideline):

[ P = k \times \rho \times N^3 \times D^5 ]

Where:

  • (P) = Power (W)
  • (k) = Constant depending on impeller type
  • (\rho) = Fluid density (kg/m³)
  • (N) = Rotational speed (rps)
  • (D) = Impeller diameter (m)

Loading diagram...

Summary: Propeller mixers require high-speed motors (400–1400 rpm) with power depending on impeller size; vane mixers operate at lower speeds (60–100 rpm) with motors sized for torque and vibration control. Both need

?How should hydraulic jumps and baffled channels be designed to achieve effective rapid mixing?

Design of Hydraulic Jumps and Baffled Channels for Effective Rapid Mixing (IS 7090)

  • Hydraulic Jump (Clause 5.1):

    • Coagulant is introduced upstream of a sloping, widening flume.
    • Water velocity in flume: 3 to 3.5 m/s.
    • Water falls into a pool of slow-moving water, causing a hydraulic jump.
    • This jump dissipates kinetic energy, creating turbulence for rapid mixing.
    • Minimum headloss: 300 mm at design flow to ensure sufficient energy dissipation.
  • Baffled Channel (Clause 2.5):

    • Baffles (fins, blades, plates) are installed alternately on opposite walls.
    • Spacing allows flow around ends, promoting thorough mixing.
    • This arrangement increases turbulence and mixing efficiency.
  • Additional Guidance (Clause 3.1.1):

    • Mechanical mixers (for comparison) use detention times of 20-60 seconds.
    • Velocity gradient (G) range: 300 to 900 s⁻¹.
    • Hydraulic jumps and baffled channels achieve mixing by turbulence, not mechanical agitation.

Summary Table: Hydraulic Jump Design Parameters

ParameterValue
Velocity in flume3 - 3.5 m/s
Minimum headloss≥ 300 mm
Mixing mechanismTurbulence via jump

Loading diagram...

In essence, design hydraulic jumps with sufficient velocity and headloss to generate turbulence, and arrange baffled channels with alternate baffles to promote flow disruption and mixing.

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