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Full Analysis of Dissolved Air Flotation (DAF) Technology: Theory, Parameter Optimization and Practical Engineering Application

In the water treatment industry, whether it is water purification for domestic use, urban sewage treatment, or industrial wastewater discharge to meet standards, dissolved air flotation (Dissolved Air Flotation, abbreviated as DAF) technology is one of the indispensable core processes. As an efficient solid-liquid separation technology, DAF is widely applied in various fields such as food, printing and dyeing, papermaking, and petrochemicals due to its high processing efficiency, small site area,and wide adaptability to water quality. Based on the master's thesis "Theoretical and Applied Research on Dissolved Air Flotation Water Purification Technology", combined with actual engineering cases, this article comprehensively disassembles the core principles, system composition, process parameter optimization, and equipment selection techniques of DAF technology. It also provides a practical technical parameter table and fault diagnosis guide to help industry practitioners quickly master the key points of DAF technology and solve various problems in actual engineering.

dissolved air flotation system for industrial wastewater


I. Core Principle of DAF Technology: Understanding the Underlying Logic of "Bubble Separation"


Many practitioners using DAF equipment only know that it can remove suspended solids, oils and other impurities from wastewater, but they have little understanding of its core principle, which leads to a passive situation in terms of parameter adjustment and fault handling later. In fact, the working logic of DAF is not complicated. The core lies in achieving efficient separation of pollutants from water through four key steps: "aeration - release - adhesion - separation". The specific process is as follows:

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1. Dissolution stage: In this stage, air is fully mixed with water under high pressure, allowing the air to dissolve into the water and form supersaturated dissolved air water. The core of this stage is to ensure the efficiency of air dissolution, laying the foundation for the generation of tiny bubbles in the subsequent process. This is also the fundamental difference between DAF technology and ordinary air flotation technology.

2. Release stage: The supersaturated dissolved gas water is passed through a dedicated release device, which rapidly depressurizes it to atmospheric pressure. At this point, the dissolved air in the water will rapidly precipitate, forming a large number of tiny bubbles. The particle size of these bubbles is typically controlled within the range of 20-100 μm (bubbles of this size have the best ability to adhere to pollutants and can float stably).

3. Attachment Stage: The tiny bubbles fully come into contact with the suspended matter, colloidal particles, and oil and other pollutants in the wastewater. By virtue of the surface tension of the bubbles, the pollutants are firmly adhered to the surface of the bubbles, forming a "bubble-pollutant" complex. It should be noted that if the pollutant particles in the wastewater are too fine, a coagulant needs to be added in advance to cause the fine particles to aggregate into larger flocs, thereby enhancing the attachment effect.

4. Separation stage: The "bubble-pollutant" complex has a lower density than water and will rapidly rise to the surface under the influence of buoyancy, forming a floating scum layer. The scum is removed by the scraping equipment, while the purified clear water is discharged from the bottom, thus completing the solid-liquid separation process.

In simple terms, the core advantage of DAF technology lies in "microscopic bubbles" - the smaller the bubbles and the more uniform their distribution, the larger the contact area with the pollutants, and the higher the separation efficiency. This is also one of the core directions for optimizing subsequent process parameters.

dissolved air flotation design specifications


II. Core Components of the DAF System: Four Major Components Determine Processing Effect


A complete DAF system is not a single device; it consists of four core components: the aeration system, the release device, the air flotation tank (flow field design), and the auxiliary system. The performance of each component directly affects the processing efficiency of the entire system, and none of them can be missing. Based on the engineering practical experience in the paper, we have detailedly dissected the core requirements and design points of each component:

small scale dissolved air flotation unit

1. Gas dissipation system: The "heart" of DAF

The dissolved gas system is the core for generating supersaturated dissolved gas water. It mainly consists of a dissolved gas tank, an air compressor, and a circulating water pump. Its performance directly determines the efficiency of air dissolution and the quality of subsequent bubbles. In the paper, through numerous experiments, it was concluded that the pressure, liquid level, residence time of the dissolved gas tank, and the air supply volume of the air compressor are the key factors affecting the dissolved gas effect.

Design Key Points: The dissolved air tank is recommended to have a vertical structure. The volume should be determined based on the treatment water volume, and the residence time should be controlled within 2 to 5 minutes. The air compressor should be an oil-free type to prevent oil contamination of the water body. The air supply volume should match the circulating water volume. The head of the circulating water pump needs to meet the requirements of the dissolved air pressure. Usually, it should be controlled at 0.3 to 0.5 MPa to ensure that the air can be fully dissolved in the water.


2. Release mechanism: The "generator" of tiny bubbles
The function of the release device is to rapidly and uniformly release the air from the supersaturated dissolved gas water into tiny bubbles. The structural design of this device directly affects the bubble size and the uniformity of distribution. The paper compared the performance of various release devices (needle type, orifice plate type, jet type), and concluded that the jet type release device produces the smallest bubble size (20-50 μm), the most uniform distribution, the best effect in adhering to pollutants, and is less prone to clogging, making it suitable for most engineering scenarios.
Notes: The release device should be cleaned regularly to prevent impurities from blocking the pore size, which could cause the bubble size to increase and the separation efficiency to decrease; During installation, it should be evenly distributed on the bottom of the air flotation tank to ensure that the bubbles can fully contact with the wastewater.


3. Air flotation tank: The "main battlefield" for separation (key to flow field design)

The air flotation tank is a place where the "bubble-pollutant" complex rises and separates. The design of the flow field directly affects the separation efficiency - if the flow field is not uniform, it will cause bubble aggregation, water flow short-circuiting, and problems such as pollutants not being able to rise effectively and clean water carrying debris. In the paper, through numerical simulation and engineering experiments, the flow field design of the air flotation tank was optimized:
(1) Pool selection: Horizontal flow aerated sedimentation tanks are suitable for most scenarios. They have a simple structure and are easy to construct. The water flow speed is controlled at 0.1 - 0.3 m/s, ensuring that the bubbles have sufficient time to rise (10 - 20 minutes).
(2) Flow diversion device: At the inlet of the air flotation tank, a diversion plate is installed to prevent water flow from directly impacting the bubbles, ensuring that the sewage and the dissolved air water can be fully mixed; at the outlet, an overflow weir is set up to ensure uniform effluent and prevent floating debris from entering the clear water area.

(3) Sludge scraping device: A continuous sludge scraping machine is selected. The scraping speed is controlled at 0.5 - 1 m/min to prevent the sludge from being scraped off too quickly, which could cause the sludge to break and re-enter the water body.


4. Auxiliary System: Ensuring the stable operation of the system

The auxiliary system includes the coagulation dosing system, the sludge discharge system, and the control system. The coagulation dosing system is used to add coagulants such as PAC and PAM to cause fine pollutants to coalesce into flocs, enhancing the adhesion effect of bubbles; the sludge discharge system is used to remove the settled sludge at the bottom of the air flotation tank to prevent sludge accumulation from affecting the flow field; the control system is used to monitor parameters such as dissolved air pressure, water flow velocity, and liquid level, enabling automatic operation and reducing labor costs.


III. Optimization of DAF Process Parameters: Step-by-step guidance to achieve optimal conditions


In many engineering projects, the operation effect of DAF equipment is poor, not due to the quality issue of the equipment, but because the process parameters are set improperly. In the paper, through orthogonal experiments, the influence of four core parameters - dissolved gas pressure, reflux ratio, dosage of coagulant, and bubble particle size - on the treatment effect was systematically studied. The optimal parameter ranges under different scenarios were obtained and compiled into the following technical parameter table, which is convenient for practitioners to directly refer to and use:
Application Scenario Dissolved Air Pressure (MPa) Recycle Ratio (%) Coagulant Dosage (mg/L) Bubble Size (μm) Treatment Efficiency (SS Removal %)
Water Purification (Low Turbidity) 0.3-0.4 15-20 20-50 30-60 ≥90
Municipal Wastewater Treatment (Pretreatment) 0.4-0.5 20-30 50-100 40-80 ≥85
Food Industry Wastewater (Oily) 0.4-0.6 25-35 80-150 20-50 ≥92
Textile Industry Wastewater (High Color) 0.35-0.55 20-25 100-200 30-70 ≥88
Paper Industry Wastewater (Fibrous) 0.45-0.6 30-40 120-180 20-60 ≥93

Additional Note: The above parameters represent the optimal range based on the foundation. During actual operation, adjustments may be made based on the influent water quality (turbidity, SS content, pollutant types), and the treatment volume. For instance, when the SS content in the influent water is too high, the return ratio and the dosage of coagulant can be appropriately increased; when the oil content in the water is high, the bubble particle size can be reduced to enhance the adhesion effect.

dissolved air flotation for oil water separation


IV. DAF Engineering Application Cases: Practical References for Different Scenarios


Theoretical combination with practice is the core value of the DAF technology. The paper includes multiple DAF engineering cases from different fields, covering water supply, urban sewage, and industrial wastewater. Three typical cases are selected and their design parameters, operation effects, and precautions are detailedly analyzed to provide practical reference for practitioners (keywords: DAF engineering cases, solvothermal air flotation industrial application, DAF wastewater treatment cases):

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Case 1: Water Supply Purification Project of a City's Waterworks

Project scale: The treated water volume is 200 m³/d. The raw water is surface water with a turbidity of 20-50 NTU. The main pollutants are algae, plankton and fine silt. The required effluent turbidity is ≤ 1 NTU.

DAF system design: A horizontal-flow air flotation tank is adopted. The volume of the dissolved air tank is 10 m³. The jet-type release device is used. The pump's head for circulation is 0.4 MPa. The return ratio is 20%. The dosage of coagulant is 30 mg/L (PAC).

Operation effect: The effluent turbidity is stable at 0.5 - 0.8 NTU, with a SS removal rate of 92% and an algae removal rate of 95%. It meets the drinking water standards for tap water. The operation energy consumption is 0.35 kWh/m³, the treatment cost is relatively low, and the land area is only one-third of that of the traditional sedimentation tank.


Case 2: Oil-containing wastewater treatment project of a food processing factory

Project scale: The treated water volume is 100 m³/d. The wastewater contains 500-800 mg/L of oil, 1000-1500 mg/L of SS, and 800-1200 mg/L of COD. The effluent is required to have an oil content of ≤ 10 mg/L and a COD concentration of ≤ 100 mg/L.

DAF system design: Utilize a shallow air flotation tank (with optimized flow field design), with a dissolved gas pressure of 0.5 MPa, a reflux ratio of 30%, a dosage of 120 mg/L for the coagulant (PAC + PAM combined addition), and the bubble particle size controlled within 20-50 μm.

Operation effect: The oil content in the effluent is ≤ 8mg/L, the SS removal rate is 94%, the COD removal rate is 75%, fully meeting the industry discharge standards. Through DAF pretreatment, the subsequent biochemical treatment load is reduced by 30%, significantly saving operating costs.


Case 3: Deep Treatment Project for Wastewater from an Ink and Dye Factory

Project scale: The treated water volume is 120 m³/d. After the wastewater undergoes biochemical treatment, the problems of high color and excessive fine suspended solids still exist. The color is 50-80 times higher, and the SS content is 100-150 mg/L. The required effluent color should be ≤ 10 times and SS ≤ 20 mg/L.

DAF system design: A vertical flow aerated tank is adopted. The dissolved air pressure is 0.45 MPa, the return ratio is 25%, the dosage of coagulant is 150 mg/L, and a de-colorizing agent is additionally added. The release device is evenly distributed to optimize the flow field and avoid short-circuiting.

Operation effect: The effluent color is ≤ 8 times the standard, the SS removal rate is 88%. The treated wastewater can be recycled, achieving water resource recovery and utilization. This saves the company approximately 150,000 yuan in water expenses annually.

dissolved air flotation tank for food processing wastewater


V. DAF Equipment Selection, Energy Consumption Analysis and Fault Diagnosis


For engineering practitioners, equipment selection, energy consumption control, and fault handling are the key factors ensuring the long-term stable operation of the DAF system. Based on the research results in the paper, a practical guide has been compiled to help everyone avoid selection mistakes, reduce operating costs, and quickly solve faults.

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DAF Model Qmax (m³/h) Piping Connections (DN) Physical Dimensions (m)
Inlet Outlet Sludge Vent L L1 W W1 H H1
DAF-002 2 DN50 DN50 DN100 DN100 3.4 2.5 3.4 1.2 2.2 1.7
DAF-003 3 DN50 DN50 DN100 DN100 3.7 2.8 2.4 1.2 2.2 1.7
DAF-005 5 DN80 DN80 DN100 DN100 4.0 3.0 2.4 1.2 2.2 1.7
DAF-010 10 DN100 DN100 DN100 DN100 4.6 3.8 2.7 1.4 2.4 1.9
DAF-015 15 DN125 DN100 DN150 DN100 5.6 4.5 2.9 1.7 2.5 2.0
DAF-020 20 DN150 DN150 DN150 DN100 5.9 4.8 3.2 2.0 2.5 2.0
DAF-030 30 DN150 DN150 DN150 DN100 6.8 5.5 3.2 2.2 2.7 2.2
DAF-040 40 DN200 DN150 DN150 DN100 8.0 6.7 3.6 2.6 2.7 2.2
DAF-050 50 DN200 DN150 DN150 DN100 8.4 7.0 3.6 2.6 2.7 2.2
DAF-060 60 DN250 DN200 DN150 DN100 9.9 8.4 3.8 2.8 2.9 2.4
DAF-070 70 DN250 DN200 DN150 DN100 10.5 9.0 3.8 2.8 2.9 2.4
DAF-080 80 DN250 DN250 DN150 DN100 12.0 10.5 4.0 3.0 2.9 2.4
DAF-100 100 DN300 DN250 DN150 DN100 12.0 10.5 4.2 3.2 2.9 2.4
DAF-120 120 DN300 DN250 DN150 DN100 12.5 11.4 4.4 3.4 2.9 2.4

Misconception 1: Blind pursuit of "large processing capacity" - When selecting equipment, it is sufficient to reserve 10-20% of the actual processing water volume. Excessively large equipment will lead to increased energy consumption and higher investment costs.

Misconception 2: Ignoring water quality compatibility - For oily wastewater, release devices and slag removal devices that can withstand oil contamination should be selected; for highly corrosive wastewater, 304 stainless steel materials should be used to prevent equipment corrosion.

Misconception 3: Focusing solely on equipment price while neglecting after-sales service - DAF equipment requires regular maintenance. When selecting the equipment, it is necessary to choose a manufacturer that has a complete after-sales system and can provide on-site debugging and troubleshooting services.

Selection core principle: Based on the treatment scenario (wastewater supply/ sewage/wastewater from industrial sources), the quality of incoming water, and the treatment volume, determine the tank type, dissolved air system, and release device type. Prioritize the selection of energy-saving equipment (such as oil-free air compressors, efficient dissolved air tanks), while also considering the investment cost and operating cost.


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