| Water color | Removal rate ≥90%, colorless or light-colored transparent |
| Delivery Time | 20 work days |
| Working voltage | 3 ~ 15 V (DC, safe voltage) |
| Processing volume | 1 ~ 1000 m³/day (modular parallel operation) |
| Inlet water requirements (pre-treatment recommended) | SS ≤ 100 mg/L, oils ≤ 100 mg/L, pH 3~11 (wide adaptability range) |
| Supply Ability | 5 sets/month |
| effluent COD | Removal rate 30%~95% |
| Equipment Material | PP / Stainless Steel / Titanium |
| Payment Terms | L/C,T/T |
| Ammonia nitrogen in effluent | Removal rate 50%~90% |
| Installed power | 5 ~ 600 kW (depending on water quality concentration and treatment target) |
| Model Number | CQDHX |
| Place of Origin | China |
| Brand Name | aa ss |
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Product Specification
| Water color | Removal rate ≥90%, colorless or light-colored transparent | Delivery Time | 20 work days |
| Working voltage | 3 ~ 15 V (DC, safe voltage) | Processing volume | 1 ~ 1000 m³/day (modular parallel operation) |
| Inlet water requirements (pre-treatment recommended) | SS ≤ 100 mg/L, oils ≤ 100 mg/L, pH 3~11 (wide adaptability range) | Supply Ability | 5 sets/month |
| effluent COD | Removal rate 30%~95% | Equipment Material | PP / Stainless Steel / Titanium |
| Payment Terms | L/C,T/T | Ammonia nitrogen in effluent | Removal rate 50%~90% |
| Installed power | 5 ~ 600 kW (depending on water quality concentration and treatment target) | Model Number | CQDHX |
| Place of Origin | China | Brand Name | aa ss |
| High Light | electrochemical wastewater treatment equipment ,fine chemical wastewater treatment equipment ,electrochemical treatment for chemical wastewater | ||
I. Product Overview
Fine chemical wastewater is one of the most challenging types of industrial wastewater treatment. Fine chemicals encompass numerous sub-sectors, including pharmaceutical intermediates, pesticide intermediates, dyes/pigments, surfactants, fragrances and flavors, electronic chemicals, water treatment agents, adhesives, and coating additives. Its wastewater exhibits distinct industry characteristics: a wide variety of products, complex production processes, and frequent batch changes—leading to diverse wastewater sources, extremely complex compositions, and drastic fluctuations in water quality and quantity; extremely high COD concentrations; the presence of large amounts of recalcitrant aromatic compounds, heterocyclic compounds, halogenated hydrocarbons, nitro compounds, and polymers; strong biotoxicity (many intermediates have significant inhibitory effects on microorganisms); high salt content (Cl⁻, SO₄²⁻, Na⁺, NH₄⁺, etc.); typically extremely low BOD₅/COD ratios (0.02~0.15), resulting in very poor biodegradability; and the frequent presence of organic solvents, catalyst residues, unreacted raw materials, and byproducts.
The challenges and key difficulties of treating wastewater from fine chemical industries are extremely prominent:
Frequent biochemical system failures—Residual pesticides/pharmaceutical intermediates, nitro compounds, and halogenated hydrocarbons in the wastewater are highly toxic to activated sludge. Even after hydrolysis and acidification pretreatment, the biochemical system is frequently impacted, leading to sludge bulking and even death.
Dramatic fluctuations in water quality due to product switching—Fine chemical enterprises often operate intermittently. When switching between different products, the COD of the wastewater can surge dramatically within hours, and the types of toxic substances change simultaneously, which traditional biochemical systems cannot adapt to.
Extremely poor biodegradability—Aromatic rings, heterocyclic rings, and polycyclic aromatic hydrocarbons have stable structures, with a B/C ratio often below 0.10, making them almost unusable by microorganisms.
High salinity further inhibits biochemical processes—When salinity is >3%, the osmotic pressure of conventional activated sludge systems becomes unbalanced, leading to the death of a large number of microorganisms.
This system employs electrochemical oxidation technology and can be flexibly configured in multiple stages of fine chemical wastewater treatment: For pretreatment and detoxification of high-concentration mixed raw water—it directly treats high-COD raw water (without dilution). Through direct anodic oxidation and electrocatalysis, hydroxyl radicals (·OH) and active chlorine, along with other strong oxides, rapidly attack stable structures such as aromatic rings, heterocycles, nitro groups, and halogenated groups, breaking bonds and opening rings within 1-2 hours, significantly reducing biotoxicity. The B/C ratio is increased from 0.02-0.10 to over 0.30, creating safe and biodegradable influent conditions for subsequent biological systems.
For advanced treatment of biological effluent—it deeply removes residual recalcitrant COD and color from biological effluent, stably meeting direct discharge or reuse standards, achieving zero chemicals, zero solid waste, and zero hazardous waste.
For high-salt mother liquor/evaporation pretreatment—it removes COD and color from high-salt wastewater, improves the whiteness and purity of evaporated crystallized salt, significantly reduces the discharge of evaporation mother liquor, and achieves resource recovery of high-salt wastewater.
Addressing high-concentration, intermittent emissions during product switching—this system rapidly responds to sudden changes in water quality, treating high-concentration/high-toxicity wastewater as it is generated, thus preventing disruption to the entire plant's wastewater system.
The entire process consumes only electricity, without adding any chemical agents or generating secondary pollutants such as iron sludge, saturated carbon, or concentrated liquid. It operates at ambient temperature and pressure, with a working voltage of 3-15V DC, making it safe and easy to use. The electrochemical unit can adapt to water quality changes within minutes through current adjustment, providing a key technological solution for addressing the three core challenges of "complex water quality, drastic fluctuations, and high toxicity" in fine chemical wastewater treatment systems.
II. Difficulties in fine chemical wastewater treatment and solutions with this equipment
|
Address the difficulties |
Electrochemical solutions |
|
Frequent product batch changes and drastic fluctuations in wastewater COD and toxic substance types within hours over a biological system that it cannot adapt to. |
Fast electrochemical response - online detection of COD/toxicity indicators, automatic current adjustment to match treatment intensity, response to water quality changes in minutes, no need to wait for biochemical acclimation (several weeks) |
|
It contains a large amount of recalcitrant aromatic/heterocyclic/halogenated/nitro compounds, with an extremely low B/C ratio (0.02~0.10), making it almost impossible to degrade by simple biochemical methods. |
Electrochemical hydroxyl radicals (·OH, 2.80 V) attack stable molecular structures—aromatic ring opening, heterocycle breakage, nitro group removal, and halogen removal—increasing the B/C ratio to over 0.30. |
|
Many intermediate/active-substance residues are highly toxic to microorganisms, leading to frequent poisoning, expansion, and even collapse of biochemical systems. |
Electrochemical rapid oxidation destroys toxic functional groups (nitro, halogen, cyano, unsaturated lactones, etc.), reducing the effluent bacterial inhibition rate from >90% to <20%, ensuring safe reception by the biological system. |
|
The wastewater has a high salt content and high osmotic pressure, which leads to the death of a large number of activated sludge cells. |
Electrochemical processes are not inhibited by high salt concentrations—the higher the salt content, the higher the yield of active chlorine, and the oxidation efficiency is actually enhanced; high-salt wastewater can be directly treated before proceeding to biological treatment (after the salt content has been neutralized) or evaporation. |
|
When high-COD, high-salt mother liquor is directly evaporated, organic matter accumulates, leading to a large amount of mother liquor being discharged (3%~10%), and the crystalline salt turning yellow or black, resulting in poor quality. |
Electrochemical pretreatment removes 50%–80% of COD and ≥90% of color, reduces mother liquor discharge rate to 1%–2%, and produces crystallized salt with a whiteness ≥85, thus transforming "waste salt" into "product salt." |
|
Small volumes of high-concentration wastewater (such as reactor cleaning water and filtration mother liquor) have extremely high COD, and the cost of transporting and disposing of hazardous waste is high. |
Electrochemical on-site treatment significantly reduces COD (removal rate 50%~80%), and the treated waste is then discharged into the plant's integrated wastewater system, greatly reducing the amount of hazardous waste transported out of the plant. |
|
High-concentration intermittent emissions during product switching (such as reactor washing water) impact the entire plant's wastewater system. |
An electrochemical emergency regulation and treatment unit is installed—it automatically switches to treatment when high-concentration wastewater is generated, and the treated wastewater flows smoothly into the comprehensive regulation tank, eliminating the risk of shock discharge. |
III. Working Principle
Fine chemical wastewater enters the electrochemical reactor after being screened, settled, or filtered to remove suspended solids. Based on the characteristics of the wastewater and the treatment objectives, efficient purification is achieved through the following oxidation pathways:
(1) Direct electro-oxidation (core pathway of aromatic ring/heterocyclic ring opening and bond breaking)
A large number of recalcitrant aromatic and heterocyclic compounds in fine chemical wastewater are directly oxidized by losing electrons on the anode surface:
Aromatic compounds (benzene series, naphthalene series, biphenyls, etc.): The benzene ring is hydroxylated by active oxygen species on the anode surface, and then oxidized to open the ring, generating small molecule organic acids (maleic acid, oxalic acid, acetic acid, etc.), which greatly improves the bioavailability of microorganisms
Heterocyclic compounds (pyridine, quinoline, thiazole, furan, imidazole, etc.): Heterocyclic rings containing N/S/O are oxidized to open the ring on the anode surface, and N is released in the form of NH₃ or N₂, eliminating the cyclic biological toxicity
Nitro compounds (nitrobenzene, nitrobenzene, etc.): The nitro group is reduced at the cathode or oxidized at the anodic surface, the benzene ring is opened, and the mutagenicity is eliminated
Halogenated compounds (chlorobenzene, brominated compounds, etc.) : Carbon-halogen bonds break on the anode surface, halogens are removed in ionic form, and the biodegradability of organic matter is significantly improved after dehalogenation. Organic matter containing unsaturated bonds (olefins, alkynes, etc.): Unsaturated bonds are oxidized and broken, and converted into acids, alcohols, etc.
(2) Indirect electro-oxidation
Anode electrolysis of water generates hydroxyl radicals (·OH), and at the same time, the chloride ions naturally present in the wastewater (fine chemical wastewater generally contains Cl⁻) are electrolyzed to generate active chlorine (Cl₂, HOCl, OCl⁻):
Hydroxyl radicals perform non-selective oxidative attacks on various organic matter, especially effective for opening aromatic rings and breaking heterocyclic rings.
Active chlorine diffuses into the solution to supplement the oxidation of pollutants that have not directly contacted the anode, and efficiently removes ammonia nitrogen.
Chloride ions are recycled in the reaction and continuously participate in oxidation.
(3) Simultaneous improvement of COD reduction and biodegradability
Synergistic effect of direct oxidation and indirect oxidation: Large molecular recalcitrant organic matter → Ring opening/bond breaking → Small molecule organic acids, alcohols, aldehydes
Some organic matter continues to oxidize → CO₂ + H₂O (COD mineralization)
The treated effluent BOD₅ increases significantly (large molecules are converted into small molecule degradable substances), COD decreases, and the B/C ratio increases from 0.02~0.10 to over 0.30, providing a high-quality degradable carbon source for subsequent biochemical systems.
(4) Deactivation effect of toxic functional groups
One of the core goals of electrochemical oxidation is to precisely attack toxic functional groups to "deactivate" them—the nitro group of nitrobenzene is removed, the C-X bond of halogenated products is broken, and the heterocycle opens to release N. After the toxic groups are destroyed, even if the molecular skeleton is not completely mineralized, its inhibitory effect on microorganisms is basically eliminated, and subsequent biochemical systems can safely and efficiently continue to degrade residual small molecules.
(5) Color elimination
The chromophores are oxidized and broken, and the wastewater changes from dark to colorless or light transparent.
IV. Core Advantages (Targeting Fine Chemical Wastewater)
|
Advantages |
illustrate |
|
Rapid inactivation of biotoxicity |
Within 1-2 hours, toxic functional groups such as nitro, halogen, heterocyclic, and unsaturated lactones are destroyed, reducing the bacterial inhibition rate in the effluent from >90% to <20%, thus completely eliminating the problem of poisoning in the biological system. |
|
Significantly improve biochemical properties |
The B/C ratio increases from 0.02~0.10 to 0.30~0.50, the COD removal rate of the biochemical system increases by 50%~80%, and the total COD removal rate of the overall system can reach more than 95% |
|
Directly treats high-concentration raw water without dilution. |
Direct treatment avoids the ineffective cycle of "dilution-treatment-reconcentration," significantly reducing the amount of water to be treated and the scale of equipment required. |
|
Rapid response to water quality fluctuations |
Fine chemical products are frequently switched (every few hours to several days), and electrochemistry can complete parameter matching within minutes through current adjustment, without the need for weeks of biochemical acclimatization. |
|
Adapted to high-salt environments |
Salt (NaCl, Na₂SO₄, etc.) does not inhibit the reaction—the higher the Cl⁻ concentration, the higher the yield of active chlorine and the stronger the oxidation efficiency; high salt is no longer a limiting factor. |
|
Simultaneous removal of COD, ammonia nitrogen, color and toxicity |
A single system completes multi-target purification, replacing the traditional multi-stage process of "pretreatment + hydrolysis acidification + deep oxidation," significantly simplifying the process. |
|
Zero reagent dosage, only electricity consumption |
There are no chemical procurement, transportation, or storage processes, eliminating the risk of chemical leaks and ensuring a safe operating environment. |
|
Safe operation at normal temperature and pressure |
Operating voltage 3~15V DC, no high voltage, no high temperature, no flammable or explosive risks. |
V. Technical Parameters (Customizable)
|
parameter |
scope |
|
Processing volume |
1 ~ 1000 m³/day (modular parallel operation) |
|
Installed power |
5 ~ 600 kW (depending on water quality concentration and treatment target) |
|
Working voltage |
3 ~ 15 V (DC, safe voltage) |
|
effluent COD |
Removal rate 30%~95% |
|
Ammonia nitrogen in effluent |
Removal rate 50%~90% |
|
Water color |
Removal rate ≥90%, colorless or light-colored transparent |
|
Equipment Material |
PP / Stainless Steel / Titanium |
|
Inlet water requirements (pre-treatment recommended) |
SS ≤ 100 mg/L, oils ≤ 100 mg/L, pH 3~11 (wide adaptability range) |
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VI. Process Location
Option 1: Pretreatment Detoxification
Fine chemical wastewater (raw/mixed water) → Bar screen/equalization tank → Sedimentation/flotation (SS and floating oil removal) → Electrochemical treatment equipment (ring-opening, removal of nitro/halogen/heterocyclic toxicity, B/C ratio enhancement) → Intermediate tank/buffer tank → Biological system (hydrolysis acidification + A/O or A²/O) → Discharge meeting standards
Explanation: The electrochemical detoxification unit is located before the biological system, undertaking the core functions of "toxicity elimination + ring-opening + B/C ratio enhancement." This is the most critical and indispensable process in fine chemical wastewater treatment—if fine chemical wastewater without electrochemical detoxification directly enters the biological system, the system operation risk is extremely high, with frequent poisoning and collapse. After detoxification, the effluent B/C ratio is ≥0.30, the COD removal rate of the biological stage is significantly improved, and the overall system operation is stable and reliable. This configuration is particularly suitable for fine chemical enterprises with complex wastewater compositions and frequent product switching.
Option 2: Advanced Treatment to Meet Standards (For cases where COD in the effluent from biological treatment still fails to meet standards)
Fine Chemical Wastewater → Pretreatment → Biological System → Secondary Sedimentation Tank → Electrochemical Advanced Treatment Unit (Removal of Residual Stubborn COD and Color) → Compliant Discharge/Reuse
Explanation: When the COD and color of the effluent from biological treatment still cannot meet the discharge standards, an electrochemical advanced treatment unit is added after the biological system. This unit deeply removes residual aromatic polymers, humic substances, and other stubborn COD, reducing the COD to the discharge/reuse standard.
Option 3: Pretreatment Detoxification + Advanced Treatment
Fine Chemical Wastewater → Electrochemical Detoxification Unit (Before Biological Treatment) → Biological System → Electrochemical Advanced Treatment Unit (After Biological Treatment) → Compliant Discharge/High-Quality Reuse
Explanation: For newly built fine chemical wastewater treatment plants or projects with extremely strict discharge standards, an electrochemical unit is installed both before and after the biological treatment. The front end ensures the stable and efficient operation of the biological system, while the back end ensures that the effluent consistently meets the most stringent discharge standards. With the two systems working together, the system has the strongest resistance to shocks and the highest certainty in water output.
Company Details
Business Type:
Manufacturer,Exporter,Trading Company,Other
Year Established:
2005
Total Annual:
$5 million-$6 million
Employee Number:
40 people~60 people
Ecer Certification:
Verified Supplier
Company Profile AA SS AQUA HITECH CO., LTD. was established in 2005 in Shenzhen, China. It is a leading technology enterprise specialized in the design, manufacturing, installation, commissioning and maintenance of technical solutions for high-difficulty industrial wastewater treatment ... Company Profile AA SS AQUA HITECH CO., LTD. was established in 2005 in Shenzhen, China. It is a leading technology enterprise specialized in the design, manufacturing, installation, commissioning and maintenance of technical solutions for high-difficulty industrial wastewater treatment ...
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