Summary of zero-discharge technologies for high-salt wastewater! Which technology can achieve "zero discharge"?


Published Time:

2023-05-08

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01 Overview

High-salinity wastewater refers to wastewater with a total salt concentration of at least 1%. It mainly comes from chemical plants and the collection and processing of oil and natural gas. This wastewater contains various substances (including salts, oil, organic heavy metals, and radioactive substances). The sources of saline wastewater are widespread, and the volume is increasing year by year. Removing organic pollutants from saline wastewater is crucial to environmental impact. When using biological treatment methods, high concentrations of salts inhibit microorganisms. Physical and chemical methods require large investments, high operating costs, and difficulty in achieving the desired purification effect.

 

Since the 1990s, with the rapid development of China's textile industry, the scale of the dyeing industry has expanded rapidly, and the production and use of dyes have increased. As a result, a large amount of high-COD, high-chromaticity, high-toxicity, high-salinity, and low B/C dye wastewater has been generated. According to statistics, in 2009, the total amount of dye wastewater produced by the dyeing industry reached 2.43 billion tons, accounting for more than 80% of the total wastewater discharge from the textile industry. This type of dye wastewater has the characteristics of "four highs and one low," and is related to the types of dyes used. At the same time, in dye production, the enrichment of salts in the discharged wastewater is mainly caused by the production process and the addition of process aids. For example, in the comprehensive wastewater of a certain dye factory in Jiangsu Province, the mass fraction of chloride alone is as high as 60 g/L. It can be seen that how to efficiently treat high-salinity and high-pollution dyeing wastewater, separate chloride from the qualified water, and meet the requirements of freshwater resource recycling has become a difficult problem in dyeing wastewater treatment.

 

  In chemical production, the pesticide production process also produces a large amount of high-salinity wastewater. According to statistics, the annual output of pesticides nationwide is 476,000 tons. Among them, the production of organophosphorus pesticides accounts for more than 50% of the pesticide industry. The characteristics of this type of pesticide wastewater are: high organic matter concentration, complex pollutant components, high toxicity, difficult degradation, and unstable water quality. For example, in the production process of the herbicide glyphosate, the concentration process will produce high-concentration phosphate and sodium chloride wastewater, with a COD of about 50000 mg/L and a salt content of up to 150 g/L. For this type of high-COD, high-salt pesticide wastewater, effective treatment measures must be taken. Otherwise, it will cause serious environmental pollution.

 

  In addition, high-salinity wastewater is also produced in other chemical production processes. For example, in the production of soda ash by the ammonia-soda process, the soluble salt content of the wastewater discharged from the system after ammonia stripping generally reaches 15% to 20%, most of which is CaCl2 and NaCl. In the coal chemical industry, after the high-salinity wastewater undergoes a thermal concentration process, the discharged concentrated wastewater has a salt content of more than 20%. For high-salinity wastewater produced in chemical production, due to its different origins from different chemical products and production processes, the properties of high-salinity wastewater also vary. Therefore, for various high-salinity wastewaters directly produced in chemical production, it is necessary to classify them according to their different sources and properties and select the optimal process for treatment.

 

With the continuous proposal and trial implementation of policies and proposals for zero discharge of high-salinity wastewater in recent years, on the one hand, the enthusiasm for zero discharge has remained unabated, and zero-discharge projects continue to be launched; however, on the other hand, enterprises often find it difficult to bear the high costs, and the implementation of the technology also faces difficulties, with few projects truly achieving zero discharge. This gap between ideal and reality has also made enterprises calm down and cautiously practice zero discharge in combination with their own needs and the actual situation of the project.

02 Relevant Policies

 

The concept of zero discharge was initially enforced in the United States in the 1970s due to industrial wastewater affecting river water quality. Subsequently, Australia's first industrial wastewater zero-discharge project was also mandatory due to policy regulations. This shows that the guiding role of policies on zero discharge is very prominent. In recent years, the continuous tightening of environmental regulations has put forward higher requirements for the treatment and disposal of high-salinity wastewater, which is particularly prominent in China's coal chemical and thermal power industries.

• 2006

Technical Regulations for Wastewater Treatment Design of Thermal Power Plants (DL/T 5046-2006)

Desulfurization wastewater should be prioritized for reuse. If there are no reuse conditions, it should be treated and discharged according to standards; for power plants with hydraulic ash removal, desulfurization wastewater can be directly used as ash-washing water.

• 2015

Guiding Opinions on Regulating the Demonstration Work of Coal-Based Fuels (Draft for Comments)

All process wastewater is reused, circulating water wastewater is not discharged, and wastewater treatment has no secondary pollution.

• 2015

Environmental Access Conditions for Modern Coal Chemical Construction Projects (Trial)

In areas lacking receiving water bodies, effective measures should be taken to deal with high-salinity wastewater to prevent pollution of groundwater, atmosphere, and soil.

• 2016

“Thirteenth Five-Year” Plan for Power Development

The discharge of wastewater from thermal power plants meets the standards at a rate of 100%.

• 2017

Technical Policies for Pollution Prevention and Control in Thermal Power Plants

Water pollution prevention and control in thermal power plants should follow the principles of classified treatment and multiple uses of water. Thermal power plants are encouraged to achieve the recycling of wastewater without external discharge.

• 2017

“Thirteenth Five-Year” Plan for the Demonstration of Deep Processing of Coal Industry

New demonstration projects without receiving water bodies will utilize crystallization and salt separation technologies to resource utilize high-salinity wastewater and achieve zero wastewater discharge.

• 2017

Technical Policies for Pollution Prevention and Control in Thermal Power Plants

It is encouraged to use evaporation drying or evaporation crystallization treatment processes to achieve zero discharge of desulfurization wastewater.

• 2018

Approval Principles for Environmental Impact Assessment Documents of Thermal Power Construction Projects (Trial)

Desulfurization wastewater is reused after separate treatment.

• 2018

Technical Guide for Circular Economy Practices in the Thermal Power Industry (Coal-fired Power Generation Enterprises) (Draft for Comments)

Desulfurization wastewater should be treated with lime treatment, coagulation, clarification, and neutralization before reuse. It is encouraged to use evaporation drying or evaporation crystallization treatment processes to achieve zero discharge of desulfurization wastewater.

03 Process Technology Analysis

 

Zero liquid discharge (ZLD) and resource recovery process requirements for high-salt wastewater aim to maximize the separation and recovery of various substances under technically and economically feasible conditions, such as water reuse, salt crystallization, or acid-base production. Single-salt solutions primarily focus on concentration and recovery, while complex salt solutions prioritize salt separation and resource recovery. Currently, a pretreatment → concentration → evaporation crystallization system is commonly used to treat high-salt wastewater, achieving zero or near-zero discharge, with the resulting salt solids disposed of or recovered.

 

▲ Typical Zero Liquid Discharge Process Diagram

 

The key factor determining the cost of ZLD is the wastewater treatment capacity of the evaporation crystallization system. If high-concentration pretreatment can be achieved before the wastewater enters the evaporation crystallization stage, the cost of zero liquid discharge for high-salt wastewater will be significantly reduced. Numerous concentration technologies exist, and based on the treatment object and applicable range, high-salt wastewater concentration technologies are mainly divided into thermal concentration and membrane concentration technologies. Early ZLD systems primarily used thermal concentration technologies for brine concentration, including mechanical vapor compression (MVC) and the currently more widely used mechanical vapor recompression (MVR). Other thermal desalination technologies, such as multi-stage flash (MSF) and multi-effect distillation (MED), are mainly used in seawater desalination and have no reported applications in ZLD processes.

 

Mechanical Vapor Compression Technology

MVC technology has been used for decades, with continuous development of heat recovery devices. However, high energy consumption and the need for high-quality electricity remain the biggest limitations to its widespread application. Typically, 20-25 kWh of electricity is consumed per ton of water treated, which has become the benchmark for other ZLD concentration technologies and the direction for energy saving and emission reduction in other technologies. In addition to high energy consumption, MVC also has high investment costs, requiring the use of high-quality and expensive materials, such as titanium and stainless steel, to prevent corrosion by boiling brine.

▲ MVR Principle Diagram

 

To reduce the energy consumption of MVC, RO and MVC processes are often coupled in practical engineering. Using RO for pre-concentration can significantly reduce energy consumption, and the synergistic effect of the two achieves zero liquid discharge of high-salt wastewater. The addition of RO can save 58-75% of energy and 48-67% of operating costs. However, there are two major limitations to applying RO to zero discharge: membrane scaling/fouling and relatively low concentration capacity.

 

Membrane Concentration Technology

New membrane concentration technologies include membrane distillation, forward osmosis, and electrodialysis, which are used as further concentration processes for RO concentrate, with the effluent then entering the crystallization process. The advantages, limitations, and energy consumption analysis of various membrane concentration technologies are shown in the table below.

Technology Name

Advantages

Limitations

Energy Consumption Analysis

RO

Energy-efficient, mature technology, modular

Limited concentration capacity, salt concentration upper limit is ~75,000 ppm, prone to fouling

Seawater: 2-6 kWh/m³ of produced water

Backwashing: 1.5-2.5 kWh/m³ of produced water

ED/EDR

High concentrated salinity (>100,000 ppm), not easily fouled, modular

High energy consumption when treating high-salinity wastewater, cannot remove uncharged pollutants

7-15 kWh/m³ of influent

(Influent salinity >15000 ppm)

FO (thermal NH₃/CO₂ draw solution)

High concentrated salinity (>200,000 ppm), utilizes low heat, not easily fouled, modular

Very low flux at high salinity, NH₃ may affect effluent water quality, relatively new technology with few successful cases

21 kWh/m³ of influent (average influent salinity 73000ppm, recovery rate 64%)

MD

High concentrated salinity (>200,000ppm), utilizes low heat, not easily fouled, modular

Low flux, low recovery rate, volatile pollutants require further treatment if present, relatively new technology with few successful cases

40-45 kWh/m³ of produced water

22-67 kWh/m³ of produced water

MVC Concentrator

Mature technology, high concentrated salinity

High energy consumption, high investment and maintenance costs, high-temperature operation, can only utilize primary energy

20-25 kWh/m³ of influent

28-39 kWh/m³ of influent

Membrane Distillation Technology

Membrane distillation is a process where water vapor is driven through a hydrophobic microporous membrane by vapor pressure difference (temperature difference) and then condensed into pure water. Membrane distillation theoretically has a 100% retention rate; low operating temperature, waste heat can be utilized; low operating pressure; low equipment investment; almost no membrane fouling problems, and long service life.

Forward Osmosis Membrane Concentration Technology

Forward osmosis utilizes the osmotic pressure of concentrated brine to allow water molecules in the wastewater to pass through the forward osmosis membrane into the salt side, achieving the separation of water and pollutants. The brine is then desalinated by reverse osmosis to achieve water resource recovery. The two core technical issues of forward osmosis are: the selection of forward osmosis membrane materials and structure; and the selection of the draw solution. Yale University developed NH3/CO2 as a thermal draw solution, which can be regenerated at a moderate temperature of 60°C, significantly reducing energy consumption compared to MVC.

 

Cutting-edge Zero Liquid Discharge Technology for Saline Wastewater

Temperature Swing Solvent Extraction (TSSE) technology

On April 30, 2019, a paper titled "Membrane-less and Non-Evaporative Desalination of Hypersaline Brines by Temperature Swing Solvent Extraction" was published in Environ. Sci. Technol. Lett., a top journal in the environmental field, instantly attracting widespread attention from the industry. The article introduces a novel solvent extraction desalination method designed by researchers at Columbia University in New York, which can efficiently and cost-effectively extract freshwater from saltwater. It is called "Temperature Swing Solvent Extraction" or TSSE. This method uses a solvent with temperature-dependent water solubility. The solvent is added to the saltwater, allowing it to float above the denser salt-containing liquid. At room temperature, water from the saltwater is absorbed into the solvent. After this stage, the solvent is extracted and heated at 70°C. The solvent's "temperature swing" properties then separate it from the water, and the resulting desalinated water settles to the bottom and is collected. Compared to thermal and membrane methods, this method is energy-efficient, has low investment costs, and can desalinate high-salt industrial wastewater with salinity more than seven times that of seawater. However, it is currently still in the laboratory research stage. How to scale up and achieve stable operation is the key to the further development of this technology. Let's wait and see.

Technologies Worth Noting

 

MVR Technology

This system solution is a closed-loop system that can recycle wastewater and energy, saving energy and reducing maintenance costs. Evaporator technology is one of the top choices for achieving zero wastewater discharge in enterprises. It can reuse up to 98% of the recyclable distillate through the evaporator. The distillate is of high quality, so it can be directly fed back into the production cycle or discharged directly. The evaporator is simple to use, highly flexible and safe, and is specifically designed for 24/7 operation.

Technical Advantages:

  • Suitable for difficult-to-degrade industrial wastewater, stable performance

  • Repetitive use of heat achieves extremely low energy consumption

  • Distillation and concentration output does not require the use of additional pumps

  • Advanced control devices and touch screen ensure high and intuitive operational comfort

  • Built-in on-demand cleaning system

  • Stronger corrosion protection

  • For wastewater with more serious pollution and foaming

 

 

Osmosis-Assisted Reverse Osmosis Technology

Technology Name: Integrated Multi-stage Osmosis-Assisted Reverse Osmosis (OARO) Salt Concentration Evaporator

Its innovative technology cleverly combines the principles of reverse osmosis and forward osmosis to achieve efficient and low-cost salt concentration. This technology has broad application prospects in the fields of salt concentration and zero discharge. The reason why general RO is difficult to concentrate to a higher multiple of salt solution is mainly because the external pressure of reverse osmosis has reached the limit of osmotic pressure and can no longer be further concentrated. Using the principle of osmotic pressure, a small amount of salt is added to the outlet of the reverse osmosis membrane to reduce the pressure difference between the two sides of the membrane, so that on the one hand, further concentration can be achieved, and on the other hand, the external pressure can be reduced, saving energy and reducing consumption.

Technical Advantages:

  • The solution can be concentrated to near saturation (26% for NaCl)

  • Increase process recovery rate to 75%

  • Save energy, 5-10 kWh per cubic meter of recovered liquid

  • No thermal concentrator required

  • Reduce saltwater treatment costs by up to 50%

 
 

EDR Technology

Flex EDR is an advanced electrodialysis reversal (EDR) system that utilizes Saltworks' new generation of ion exchange membranes. It requires less pretreatment, tolerates oil and high organics, selectively removes ions, and requires no chemical additives. It has been applied in industrial fields such as flue gas desulfurization wastewater chloride removal and water reuse, selective salt separation of high-salt wastewater in coal chemical industry, lithium separation and recovery, and desalination of produced water in enhanced oil recovery in oil fields.

Technical Advantages:

  • Durable Design

    Based on ion exchange membranes and stacks with high elasticity and extensibility, it can withstand oil, organic matter, oxidants (bleach), acids (pH 0), alkalis (pH 12), and suspended solids (<30 μm).

  • Selective Ion Removal

    Removes monovalent ions without soda softening, changing the scaling water chemistry, and recovering valuable salts.

  • Ultra-high Concentration, Flexible Operation

    Concentrates concentrated water to 180,000 mg/L, and can be combined with reverse osmosis to optimize the system.

  • Intelligent self-cleaning strategy maintains high salt load and high water recovery rate

  • High degree of modularity, easy to scale up, or add to existing processes

 

Membrane Distillation Technology

Technology Name: Membrane Distillation Technology

Using vacuum membrane distillation technology with hollow fiber membranes, the water recovery rate can reach 97%, and energy consumption can be reduced by 80% compared to traditional thermal methods. Suitable for the treatment of high-salt wastewater such as mining wastewater, RO concentrate, and brackish water.

The treatment of saline wastewater is difficult and costly. Hollow fiber vacuum membrane distillation (HF-VMD) technology provides a unique solution. This process recovers and reuses the maximum amount of high-quality pure water from challenging industrial wastewater. The KMX system has higher recovery rate, brine saturation, and capacity factor than traditional evaporator/crystallizer systems, and significantly reduces energy demand. The system has low maintenance requirements, small footprint, modularity, scalability, and applicability to various industrial wastewaters.

Technical Advantages:

  • No crystallization required, one-step process converts concentrated brine into wet salt cake

  • 40-60% higher recovery rate than RO, up to 97%

  • Low maintenance costs, no heat transfer interface or scaling on membrane surface

  • Low energy consumption, 80% lower energy consumption than evaporator or crystallization processes

  • Low cost, salt recovery and reuse, approximately 1-3 years to recover costs