Carbon Fibre Manufacturing Wastewater: Acrylonitrile, Solvent and Cyanide Control
Carbon fibre plants combine a polymerisation problem with a thermal conversion problem, and each contributes its own wastewater. Polymerisation and spinning leave acrylonitrile monomer and spinning solvent. Pre-oxidation and carbonisation, the high temperature steps, generate scrubber liquor containing hydrogen cyanide and ammonia. The first is a recovery question; the second is a safety question, and it comes first.
Cyanide from the Furnace Steps
Pre-oxidation stabilises the fibre in air, and carbonisation drives off everything that is not carbon under inert atmosphere. Both release gases — hydrogen cyanide, ammonia, and a range of volatile organic products of thermal decomposition. Scrubbing that gas stream produces a liquid effluent containing cyanide.
This is the stream that governs the design, because hydrogen cyanide is acutely toxic and the consequences of getting it wrong are not environmental but immediate. Treatment by alkaline chlorination is well established: raise pH above 10, oxidise with hypochlorite to cyanate, then hydrolyse further if complete destruction is required.
Alternative routes include hydrogen peroxide oxidation, ozone, and biological cyanide degradation in a dedicated acclimatised stage. Alkaline chlorination remains the most commonly specified because it is predictable and easy to monitor. We have written about the downstream implications separately in Shipyard, Dry Dock and Marine Vessel Wastewater Treatment system.
Instrument it. Free cyanide monitoring and interlocks on the scrubber liquor discharge are worth the cost. Do not rely on the downstream plant as the barrier.
Acrylonitrile in Polymerisation and Spinning
Acrylonitrile is the monomer for polyacrylonitrile precursor, and residual monomer appears in polymerisation wash water and in spinneret and coagulation bath cleaning liquors. It is toxic, volatile, and regulated tightly in both air and water. A related discussion worth reading here is Sand, Gravel and Aggregate Washing Water Treatment.
Recovery first. Stripping recovers acrylonitrile for return to the process and removes the acute toxicity before treatment. Where concentrations justify it, this is straightforwardly economic rather than merely compliant. Plants dealing with comparable loads face many of the same trade-offs covered in Green Hydrogen Electrolyser Ultrapure Feedwater.

What remains degrades biologically, but slowly and with acclimatisation. Shock loads are damaging — the same pattern seen with other nitrile-bearing streams — so equalisation and metered feed of concentrated liquors are worth specifying.
Acrylonitrile hydrolyses to acrylamide and then to acrylic acid under alkaline conditions. That pathway is worth knowing about because acrylamide is itself regulated, and treating with caustic without understanding the intermediate products can create a second problem.
Spinning Solvent
The solvent depends on the spinning route. Dimethyl sulphoxide, dimethylacetamide, dimethylformamide and aqueous sodium thiocyanate are all in commercial use, and each behaves differently in wastewater. Where several streams need joint treatment, Ready-Mix Concrete Washout Water Treatment is the more detailed reference.
What Our Project Data Actually Shows
Across 42 commissioned plants where we hold complete COD records, influent COD ranged from 200 to 172,000 mg/L and treated effluent from 50 to 5,000 mg/L. Average removal across that set is 87.1% — not a marketing figure, but the measured mean.
That average is worth pausing on. It sits well below the 95%-plus numbers most suppliers quote, because the set includes genuinely difficult streams. On some electroplating and municipal duties the installed configuration only reaches about half the influent COD, and saying that up front is more use to you than a number the plant will never hold.
| Metric | Measured value |
|---|---|
| Plants with complete COD records | 42 |
| Influent COD range | 200 – 172,000 mg/L |
| Treated COD range | 50 – 5,000 mg/L |
| Average influent COD | 11,914 mg/L |
| Average treated COD | 264 mg/L |
| Average COD removal | 87.1% |
| Wastewater types covered | 30+ |
| Delivery period on record | 2021–2022 |
Organic solvents such as DMSO and DMAC contribute a substantial COD load and are moderately biodegradable, but they carry nitrogen that converts to ammonia. They are also recoverable — distillation of coagulation bath liquor is standard practice, and improving recovery beats treating.
Sodium thiocyanate routes avoid the organic solvent but introduce thiocyanate, which oxidises to cyanide under some conditions and requires specific handling. Confirm which route your precursor line uses before specifying anything.
Where solvent recovery is already efficient, the residual load is usually small enough that conventional biology handles it. Where recovery is poor, the solvent dominates the load and no downstream design will look good.

Sizing Agent and Emulsion
Surface treatment and sizing apply an emulsion — typically epoxy or polyurethane based with surfactants — to protect the fibre during handling. Wash water from these stages carries sizing as a stable emulsion with the familiar behaviour: it does not settle, it coats biomass, and it causes foaming. Where several streams need joint treatment, PFAS and AFFF Firefighting Foam Contaminated Water Treatment is the more detailed reference.
Treat it as an emulsion-breaking problem. Acidification with coagulation and dissolved air flotation handles it predictably. Recovering the sizing phase is sometimes possible and always preferable to emulsifying it further.
Foam control is worth designing in rather than dosing for. Covered reactors with mechanical foam breaking perform better than chemical antifoam on a continuous emulsion load.
Design Priorities
Segregate three things at minimum: cyanide-bearing scrubber liquor, acrylonitrile and solvent-bearing process water, and sizing wash water. They have different answers and blending them produces a stream that is worse than any of the parts.
Treat cyanide as a safety system first and an environmental one second.
Invest in recovery before treatment. On this duty, solvent and monomer recovery consistently outperform end-of-pipe engineering on both cost and performance.
Why Choose Baihuipu as Your Manufacturer
Picking a supplier for this kind of plant is mostly about who carries the risk when something goes wrong. We have built this equipment for more than twenty years, and we are the ones who fabricated it, programmed the controls and will still answer the phone three years from now.
Own Factory, Real Capacity
Tanks, skids, control panels and membrane housings are built in our own Guangdong facility. Nothing critical is subcontracted, which is why we can commit to delivery dates and hold quality across a batch instead of hoping the shop floor gets it right.
Documentation You Can Actually Audit
Each system ships with as-built drawings, material certificates, welding records and a functional specification. If a client's own consultant wants to review the process calculation basis, we hand it over rather than treating it as proprietary.
Two Decades of Field Data
Food and beverage, chemicals, electroplating, textile dyeing, mining, municipal work — we have commissioned across all of them. The useful part is not the project count, it is having seen how plants fail in year seven and designing those failures out.
We Engineer the Whole Train
Screening, equalisation, biological or chemical treatment, membranes, evaporation, brine handling — the complete line comes from one organisation. Process design, mechanical, electrical and PLC programming sit under the same roof, so there is no gap for finger-pointing at handover.
Spare Parts and After-Sales Support
We carry membranes, pumps, blowers, diffusers and instruments for every system we supply. Remote support through the PLC is standard on most builds, and on-site service covers commissioning, training and urgent callouts.
Twenty-Plus Export Markets
We have shipped to the United States, Canada, Russia, Indonesia, India, Nigeria and Vietnam among others. Crating, export documentation and certificates are handled in-house, which keeps customs surprises to a minimum.
Certification and Export Practice
CE marking is standard and we work to ISO 9001 procedures. Where a project calls for specific material grades, pressure vessel certification or ATEX-rated equipment, we build to that standard and ship the full documentation pack.
Getting Started
Send us a water analysis and your production profile and we will tell you honestly what the process should look like and roughly what it costs to build and run. Reach our engineering team on WhatsApp: +86 13631765076 or via hkbhp.com.
WhatsApp: +86 13631765076
Frequently Asked Questions
Do you handle installation and operator training?
Every unit we supply is commissioned by our own engineers. Training happens on site with your actual operators, and the O&M manual covers routine work plus troubleshooting. Remote diagnostics through the control system are included for the first year.
Can the plant be modified later if our production changes?
Yes, if you tell us about likely expansion up front. Leaving room in the civil works and oversizing the equalisation tank costs far less than retrofitting later. Carbon Fibre Manufacturing Wastewater rarely fails because of bad chemistry — it usually fails because nobody planned for the second production line.
How do you handle sludge from this process?
Sludge handling is where most budgets quietly blow out. We size dewatering against realistic solids production, and we usually recommend a filter press for this duty. The disposal route — landfill, incineration, or a licensed contractor — should be confirmed before commissioning.
