Powder activated carbon (PAC) is activated carbon ground to a fine particle size — typically 80% passing 200 mesh (75 µm) or finer. Unlike granular activated carbon (GAC) that sits in a fixed bed, PAC is dosed directly into liquid streams, mixed, and then removed by settling or filtration.
PAC is the fastest and most flexible way to add activated carbon treatment to any process. No vessels, no plumbing changes — just dose and filter. This guide covers PAC types, specifications, applications, and how to source it for your operation.
| Factor | PAC (Powder) | GAC (Granular) |
|---|---|---|
| Contact method | Dosed into liquid,
mixed, filtered out |
Liquid flows througha fixed
carbon bed |
| Capital cost | Low — needs only a dosing system and
existing clarifier/filter |
High — needs adsorption vessels,
piping, backwash system |
| Operating cost | Higher carbon consumption per volume treated | Lower carbon consumption
(longer contact time, better utilization) |
| Best for | Intermittent dosing, seasonal events, emergencies,
taste/odor control, decolorization |
Continuous treatment, large
volumes, trace contaminant polishing |
| Carbon reuse | Typically single-
use (removed with sludge) |
Can be reactivated and reused
multiple times |
| Flexibility | High — adjust dose
rate instantly based on conditions |
Fixed — bed changeout needed to
adjust capacity |
| Particle size | 80%+ passing 200 mesh (75 µm) | 8×30, 12×40, or similar mesh
ranges |
Rule of thumb: Use PAC when you need flexible, on-demand treatment without capital investment in adsorption vessels. Use GAC when you have continuous treatment needs and want lower long-term carbon costs through bed reactivation.

| Type | Matières premières | Key Characteristics | Typical Applications |
|---|---|---|---|
| Wood-based PAC | Sawdust,
wood chips |
High mesopore volume,
excellent decolorization, lower density |
Sugar refining, food/beverage
decolorization, pharmaceutical purification |
| Coal-based PAC | Bituminous or
lignite coal |
Balanced micropore
/mesopore, good all-round adsorption, cost-effective |
Municipal water treatment,
industrial wastewater, general purpose |
| Coconut shell PAC | Coconut shell | High micropore volume,
high hardness (less relevant for powder), highest cost |
Pharmaceutical, food-grade
applications requiring high purity |
For most industrial applications, wood-based PAC is the default choice. Its high mesopore volume makes it the best decolorizer, and it's produced through phosphoric acid activation which gives it naturally high mesopore content. Coal-based PAC is preferred for water treatment where broad-spectrum adsorption matters more than decolorization.
| Paramètres | What It Measures | Typical Spec Range | Why It Matters |
|---|---|---|---|
| Indice d'iode | Micropore adsorption
capacity (ASTM D4607) |
800–1200 mg/g | Higher = better for small
molecule removal (taste, odor, solvents) |
| Bleu de méthylène
number |
Mesopore adsorption
capacity |
120–280 mg/g | Higher = better for
decolorization (large color molecules adsorb in mesopores) |
| Particle size
(passing 200 mesh) |
Fineness | 80–95% | Finer = faster adsorption
kinetics but harder to filter out |
| Humidité | Water content | ≤10% | You're paying for carbon,
not water |
| Teneur en cendres | Inorganic mineral
residue |
3–15% | Lower ash = higher purity,
critical for food/ pharma applications |
| pH | Acid or alkaline
character |
3–5
(acid-activated) or 8–11 (steam-activated) |
Must match
process pH requirements |
| Iron content | Fe contamination | <0.1% for
food grade |
High iron causes
discoloration in some food processes |
The two most important specs for PAC selection:

| Application | Recommended PAC Type | Key Spec | Typical Dose Rate |
|---|---|---|---|
| Municipal drinking
water (taste/odor) |
Coal-based or
wood-based |
Iodine ≥900 mg/g | 5–30 mg/L |
| Décoloration du sucre | Wood-based
(phosphoric acid activated) |
MB ≥200 mg/g,
low ash |
0.1–0.5% by
weight of sugar |
| Edible oil refining | Wood-based,
acid-washed |
MB ≥180 mg/g,
low iron |
0.5–2% by
weight of oil |
| Pharmaceutique
purification |
Coconut shell or
wood-based, food grade |
Low ash, low iron,
USP/EP grade |
Process-specific |
| Industrial wastewater
(COD/color) |
Wood-based
or coal-based |
MB ≥150 mg/g,
Iodine ≥800 |
50–500 mg/L |
| Chemical decolorization
(glycerin, citric acid) |
Wood-based | MB ≥220 mg/g | 0.2–1% by weight |
| Emergency spill
response |
Any available PAC | Fine particle size
for fast kinetics |
Depends on
contaminant |
For specific guidance on PAC in water treatment, see our article on PAC for water treatment. For food industry decolorization, see our guides on décoloration du sucre and glycerin decolorization.
| Packaging Option | Typical Weight | Best For |
|---|---|---|
| Paper bags
(multi-layer kraft) |
20–25 kg | Small to medium users,
manual handling |
| Jumbo bags
(FIBC) |
500–1000 kg | Large users with
forklift/crane unloading |
| Bulk (pneumatic
tanker) |
20+ tons | Very large continuous
users (municipal water plants) |
Huamei Carbon manufactures wood-based and coal-based powder activated carbon for water treatment, decolorization, chemical purification, and industrial wastewater applications. Available in 25 kg bags, jumbo bags, or bulk. Minimum order: 10 tons (one 20ft container).
📱 WhatsApp: +86 181-3792-7803
📧 Email: sale@huameicarbon.com
🌐 Website: www.huameicarbon.com
Powder activated carbon (PAC) has a particle size where 80%+ passes 200 mesh (75 µm). It's dosed directly into liquids, mixed, and removed by filtration. Granular activated carbon (GAC) has larger particles (typically 0.5–4 mm) and is used in fixed-bed adsorption vessels that liquid flows through. PAC is faster-acting but single-use; GAC is slower but reactivatable.
Wood-based PAC is better for decolorization in most cases. Its phosphoric acid activation process creates a high proportion of mesopores (2–50 nm), which is where large color molecules adsorb. Coal-based PAC has more micropores, making it better for small molecules like taste and odor compounds. For sugar, oil, and chemical decolorization, wood-based PAC with methylene blue number ≥200 mg/g is the industry standard.
It varies by application and contaminant loading. For sugar decolorization: 0.1–0.5% by weight of sugar. For edible oil refining: 0.5–2% by weight of oil. For wastewater treatment: 50–500 mg/L depending on COD and color levels. The best approach is to run a bench-scale dosing trial — test increasing PAC doses on your actual product to find the minimum effective dose.
Yes, when food-grade specifications are met. Food-grade PAC must have low ash (<5%), low iron (<0.1%), no heavy metal contamination, and meet regulatory requirements (FDA, EU, or local food contact standards). Wood-based and coconut shell PAC are most commonly used in food applications. Always request food-grade certification and COA from your supplier.
Generally no. PAC is typically single-use — it's mixed into the process stream and removed with sludge or filter cake. The fine particle size makes it impractical to recover and reactivate. This is the main cost trade-off vs GAC: PAC has lower capital cost but higher ongoing carbon consumption. For processes with high carbon usage, consider switching to a GAC fixed-bed system for lower long-term cost.
Activated carbon is used in natural gas processing at multiple stages — from wellhead gas cleanup to pipeline-quality polishing. Each stage targets different contaminants and requires different carbon specifications.
This guide covers the main gas treatment applications, the carbon types and specs for each, and how to specify carbon for your gas processing project.
Industrial gas treatment with activated carbon targets these contaminant groups:
| Contaminant | Sources | Why It Must Be Removed | Carbon's Role |
|---|---|---|---|
| H₂S | Natural gas,
biogas, syngas |
Toxic, corrosive,
poisons catalysts |
Catalytic oxidation
(impregnated carbon) or adsorption |
| Mercaptans
(R-SH) |
Natural gas, LPG | Odor, corrosion | Physical adsorption +
catalytic oxidation |
| Mercury
(Hg⁰) |
Natural gas
(0.01–5,000 µg/Nm³) |
Poisons aluminum
heat exchangers in LNG plants, environmental hazard |
Chemisorption on
sulfur-impregnated carbon |
| BTEX | Natural gas,
associated gas |
Contaminates glycol,
causes emissions |
Physical adsorption
in micropores |
| Siloxanes | Biogas,
landfill gas |
Forms abrasive SiO₂
deposits in engines |
Physical adsorption |
| COV | Process vents,
tank emissions, fugitive sources |
Emissions compliance,
health hazard |
Adsorption with optional
thermal desorption |

Mercury in natural gas, even at trace levels (µg/Nm³), destroys the aluminum brazed heat exchangers used in LNG cryogenic processing. A single mercury excursion can cause liquid metal embrittlement that costs millions in repairs and months of downtime.
Sulfur-impregnated activated carbon is the standard mercury guard in LNG feed gas treatment. The sulfur reacts with elemental mercury to form mercuric sulfide (HgS), a stable and non-volatile compound trapped permanently in the carbon pores.
Spécifications :
Mercury removal beds are non-regenerable — the carbon is replaced when capacity is exhausted. Bed life ranges from 3–10 years depending on inlet mercury levels.
For natural gas with H₂S levels below 1,000 ppm, impregnated activated carbon provides a simpler alternative to amine systems. This is common for small-to-medium gas fields, marginal wells, and gas gathering stations where installing an amine plant isn't economical.
For a comprehensive guide to H₂S removal with activated carbon — including biogas, natural gas, and refinery applications — see our detailed article on activated carbon for sulfur removal.
Key specs for gas sweetening:
Triethylene glycol (TEG) dehydration systems absorb BTEX along with water from natural gas. When the glycol is regenerated, BTEX is released — creating an emission source that may require control under environmental regulations.
An activated carbon bed on the glycol regeneration vent captures BTEX before it enters the atmosphere. The carbon can be thermally regenerated or replaced periodically.
Spécifications :
Gas processing plants, compressor stations, and storage facilities produce VOC emissions from process vents, tank breathing losses, and fugitive sources. Activated carbon adsorption is the standard control technology when:
Fixed-bed carbon adsorbers with two beds in alternating adsorption/regeneration cycles are the standard configuration. The regenerated VOCs can be recovered as liquid or routed to a flare.
Spécifications :
Biogas upgrading to biomethane (renewable natural gas) requires removal of H₂S, siloxanes, and VOCs before the gas enters membrane or PSA upgrading systems. Activated carbon handles all three contaminant groups, often in a multi-stage configuration:
For detailed biogas and landfill gas treatment specifications, see our sulfur removal guide.

| Application | Target | Carbon Form | Imprégnation | Key Spec | Bed Life |
|---|---|---|---|---|---|
| LNG mercury
guard |
Hg⁰ | Pellet
3–4 mm |
Sulfur
(10–15%) |
Hg capacity,
low pressure drop |
3–10 years |
| Natural gas
H₂S |
H₂S | Pellet
3–4 mm |
KOH or KI | H₂S cap ≥0.15 g/g | 6–18 months |
| Mercaptan
odor |
R-SH | Granular
4×10 |
NaOH or virgin | Iodine ≥900 | 12–24 months |
| BTEX from
glycol |
BTEX | Granular
4×10 |
None | CTC ≥50%,
SA ≥900 |
6–12 months
(regenerable) |
| VOC emission control | Mixed VOCs | Pellet
3–4 mm |
None | CTC ≥60%,
butane ≥25% |
3–5 years
(regenerable) |
| Biogas H₂S | H₂S + siloxanes | Pellet
3–4 mm |
KOH | CTC ≥60%, pH 9–11 | 6–12 months |
When sourcing carbon for gas treatment, provide your supplier with:
Huamei Carbon produces coal-based charbon actif en granulés for gas treatment applications, including H₂S removal, mercury guard beds, VOC control, and biogas upgrading. We offer virgin, KOH, KI, NaOH, and sulfur-impregnated grades in pellet diameters from 0.9 mm to 8 mm.
📱 WhatsApp: +86 181-3792-7803
📧 Email: sale@huameicarbon.com
🌐 Website: www.huameicarbon.com
Coal-based pellet activated carbon (3–4 mm diameter) is the standard for most gas purification applications. Pellet form provides low pressure drop and uniform gas distribution in fixed-bed vessels. For mercury removal, the carbon is impregnated with sulfur. For H₂S removal, KOH or KI impregnation is standard.
Yes. Sulfur-impregnated activated carbon (10–15% sulfur loading) is the standard mercury guard bed in LNG and gas processing plants. Mercury reacts with sulfur to form stable HgS trapped in the carbon pores. These beds typically last 3–10 years and achieve outlet levels below 0.01 µg/Nm³.
Iron sponge is cheaper per ton but has lower H₂S capacity per volume, creates pyrophoric waste, and can't handle mercaptans or other contaminants. Activated carbon — especially impregnated grades — has higher capacity, produces non-hazardous waste, and can be specified for multi-contaminant removal. For operations above 100 Nm³/hr, activated carbon typically has lower total cost of ownership.
It depends on the application and contaminant loading. Mercury guard beds: 3–10 years. H₂S removal (KOH-impregnated): 6–18 months. VOC adsorbers with regeneration: 3–5 years. Biogas H₂S: 6–12 months. Higher inlet concentrations and higher flow rates shorten bed life.
Pellet carbon is generally preferred for gas-phase applications because the uniform cylindrical shape provides more predictable pressure drop and better gas distribution than irregularly-shaped crushed granular carbon. Pellet carbon also generates less dust during loading and operation. Granular carbon is used where higher surface area per volume is needed, such as BTEX guard beds on glycol systems.
Activated carbon is used across the petroleum refining process — from protecting amine systems to treating refinery wastewater. The specific carbon type, form, and specification depend on where in the refinery it's deployed and what it needs to remove.
This guide covers the main applications of activated carbon in petroleum refining, the specifications that matter for each, and how to source the right grades.
A typical refinery uses activated carbon in at least four process areas:
| Process Area | What Carbon Removes | Carbon Type | Typical Volume |
|---|---|---|---|
| Amine system
guard bed |
Surfactants, hydrocarbons,
degradation products |
Coal-based granular,
8×30 mesh |
5–20 tons
per charge |
| Produced water
treatment |
Oil, dissolved organics,
BTEX, phenols |
Granular or pellet,
à base de charbon |
10–50 tons
per system |
| Naphtha and
gasoline sweetening |
Mercaptans,
disulfides |
Impregnated granular
or pellet |
2–10 tons
per bed |
| Refinery
wastewater |
COD, BOD, oil &
grease, phenols, PAHs |
Granular (fixed bed)
or powder (dosing) |
Varies widely |
Amine-based gas treating systems (MEA, DEA, MDEA) remove H₂S and CO₂ from refinery gas streams. Over time, the amine solution picks up contaminants — surfactants from upstream processes, hydrocarbon condensates, heat-stable salts, and amine degradation products. These contaminants cause foaming, corrosion, and reduced treating capacity.
An activated carbon guard bed installed on the lean amine circulation loop adsorbs these contaminants before they accumulate to problem levels. This is one of the highest-value applications of activated carbon in a refinery — a $15,000–30,000 carbon charge can prevent millions of dollars in amine system downtime and replacement costs.
Spécifications :
Coal-based carbon is preferred over coconut shell for amine guard beds because its mesopore structure adsorbs the larger organic molecules (surfactants, heavy hydrocarbons) that cause foaming. Coconut shell's micropore-dominant structure is less effective for these larger molecules.
Produced water from oil and gas operations contains dissolved and dispersed hydrocarbons, BTEX (benzene, toluene, ethylbenzene, xylene), phenols, and other organic compounds. Regulatory discharge limits for oil and grease are typically 10–30 mg/L, and BTEX limits may be below 1 mg/L.
Activated carbon treats produced water either as a polishing step after oil-water separators and flotation, or in combination with other treatment technologies. For offshore platforms where space is limited, activated carbon's compact footprint is a significant advantage.
Spécifications :
Mercaptans (R-SH) give petroleum products an unpleasant odor and contribute to equipment corrosion. The Merox process uses a fixed-bed of activated carbon impregnated with a caustic solution and a metal chelate catalyst to oxidize mercaptans to disulfides, which are then extracted.
Activated carbon's role here is dual: it serves as the catalyst support for the Merox reaction and adsorbs residual sulfur compounds. The carbon bed needs replacement when catalytic activity drops, typically every 2–5 years.
Spécifications :

Refinery wastewater contains a complex mix of hydrocarbons, phenols, sulfides, ammonia, and suspended solids. After primary separation and biological treatment, activated carbon serves as a tertiary polishing step to meet discharge limits — particularly for COD, phenol, and PAH (polycyclic aromatic hydrocarbon) concentrations.
Two approaches are common:
GAC specifications:
PAC specifications:
Beyond the four main areas, activated carbon is also used in refineries for:
| Application | Preferred Base | Form | Key Parameters | Why This Carbon |
|---|---|---|---|---|
| Amine
guard bed |
Coal-based | Granular
8×30 |
Iodine ≥900,
ash ≤8% |
Mesopores capture
large surfactant molecules |
| Produced
water |
Coal-based | Granular
8×30 or 12×40 |
Iodine ≥1000,
hardness ≥95% |
High capacity for
dissolved organics + BTEX |
| Merox
sweetening |
Coal-based | Granular
4×10 or 8×30 |
SA ≥900 m²/g,
ash ≤6% |
Mesopore structure
for catalyst support |
| Wastewater
GAC |
Coal-based | Granular
8×30 or 12×40 |
Iodine ≥950 | COD + phenol
adsorption |
| Wastewater
PAC |
Wood or coal | Powder
200–325 mesh |
MB ≥180 mg/g | Rapid contact in
biological systems |
| Hydrogen
PSA |
Coal-based | Pellet 3–5 mm | High crush
strength |
Mesopore + low
dust for PSA cycling |
Pattern: coal-based activated carbon dominates petroleum applications. The mesopore-rich structure handles the large organic molecules common in refinery streams, and the mechanical hardness stands up to the pressures and flow rates in industrial vessels.

When requesting a quote for refinery-grade activated carbon, provide:
Huamei Carbon supplies coal-based granular and charbon actif en granulés for petroleum refining applications. We've supplied amine guard bed carbon, produced water treatment carbon, and wastewater polishing carbon to refineries across the Middle East, Central Asia, and Southeast Asia — including 77 tons for MDEA purification in Kazakhstan.
📱 WhatsApp: +86 181-3792-7803
📧 Email: sale@huameicarbon.com
🌐 Website: www.huameicarbon.com
Coal-based granular activated carbon (8×30 or 12×40 mesh) is the standard for most refinery applications, including amine guard beds, produced water treatment, and wastewater polishing. Coal-based carbon's mesopore structure is better suited for adsorbing the large organic molecules common in refinery streams than coconut shell carbon.
A carbon guard bed on the lean amine circulation loop adsorbs surfactants, hydrocarbon condensates, and amine degradation products that cause foaming and corrosion. The carbon is typically changed out every 6–12 months. This is one of the most cost-effective uses of activated carbon in a refinery.
Yes. Granular activated carbon effectively removes dissolved hydrocarbons, BTEX, and phenols from produced water. It's typically used as a polishing step after oil-water separation and flotation. Coal-based GAC with iodine number ≥1000 mg/g and high attrition resistance is recommended.
It varies widely by refinery size and configuration. A medium-sized refinery (100,000–200,000 BPD) might use 20–80 tons of activated carbon per year across amine guard beds, wastewater treatment, and other applications. Large integrated refineries with multiple amine trains and extensive wastewater treatment can use 100+ tons annually.
Amine guard beds: every 6–12 months. Produced water beds: every 6–18 months depending on oil loading. Wastewater GAC: every 12–24 months, or when effluent quality targets are no longer met. Merox beds: every 2–5 years. Regular monitoring of effluent quality tells you when it's time.
If you've requested quotes from multiple suppliers for coconut shell activated carbon, you've probably noticed the price gap can be enormous — sometimes 2x or more between the lowest and highest offer for what appears to be the same product.
That gap isn't random. It comes down to a handful of measurable variables that directly affect production cost, performance, and your total cost of ownership. This guide breaks down what actually drives coconut shell activated carbon pricing so you can evaluate quotes with confidence instead of just chasing the lowest number.
Let's start with the numbers. FOB China pricing for coconut shell granular activated carbon in 2026:
| Type de produit | Typical Application | FOB China Price (USD/ton) |
|---|---|---|
| Standard coconut shell GAC | Water treatment, récupération de l'or,
gas phase |
$3,000–3,800 |
That's the range, but a range this wide isn't very useful unless you understand what pushes the price toward one end or the other. The answer is almost always the same few variables.

Here are the seven factors that have the biggest impact on your per-ton cost:
Iodine number is the single biggest price driver. Higher iodine means more activation time in the kiln, lower yield from the same batch of coconut shell, and tighter quality control. The relationship is roughly linear up to about 1050 mg/g, then the curve gets steeper.
A basic 800-iodine grade for aquarium or simple filtration sits at the low end of the price range. A 1200+ iodine gold recovery grade with 98%+ hardness pushes toward the top. The difference? Yield loss. To push iodine above 1150 while maintaining high hardness, the activation process burns off more raw material. You start with more coconut shell to get less finished carbon.
For water treatment, hardness above 95% is usually fine. For gold recovery, you need 98%+ because the carbon circulates through high-shear CIL/CIP circuits and any breakage means gold loss — literally. Achieving high iodine and high hardness simultaneously requires careful kiln control, which costs more.
If a supplier quotes you high-iodine carbon at a suspiciously low price, check the hardness spec. Odds are they've sacrificed hardness to hit the iodine target, and that tradeoff will cost you more in the field than you saved on procurement.
Acid-washed (AW) grades go through an additional hydrochloric acid treatment to reduce ash content and lower pH. Acid-washed coconut shell carbon typically ranges from $1,850 to $3,100/ton FOB China, depending on the base grade. This processing is critical for:
The price reflects the chemical cost, extra processing time, wastewater treatment from the acid rinse, and lower yield from the leaching step.
If your application doesn't require acid-washed carbon, don't pay for it. Standard grades work perfectly well for industrial wastewater, VOC treatment, and most gold recovery applications.
Common coconut shell granular sizes include 4×8, 6×12, 8×30, 12×40, and 20×50 mesh. The pricing impact comes from screening yield:
The key point: particle size alone rarely drives more than a 5–10% price difference. If you're seeing huge gaps between mesh sizes from the same supplier, question why.
Most coconut shell activated carbon sold globally is produced in Indonesia, Philippines, India/Sri Lanka, Vietnam, or China. The coconut shell feedstock quality varies by origin:
Raw shell prices fluctuate seasonally and with coconut oil market conditions (shell is a byproduct of copra/coconut oil production). When coconut oil prices spike, shell supply tightens and carbon prices follow.
Volume matters, but not as dramatically as you might think:
| Order Size | Typical Impact |
|---|---|
| Trial order (10–13 tons / 1 × 20GP) | Standard pricing, MOQ level |
| One full container (26–28 tons / 1 × 40GP) | 3–5% better than trial |
| Multi-container (50–100+ tons) | 5–10% better, negotiable terms |
| Annual contract (200+ tons/year) | Best pricing, priority production scheduling |
The biggest cost savings from volume aren't actually in the per-ton carbon price — they're in freight. Shipping 28 tons in one 40GP container costs far less per ton than shipping 13 tons in a 20GP. If your budget allows, maximizing container utilization is the easiest way to reduce your landed cost.
In 2026, ocean freight from China to major destinations varies significantly by route:
When comparing quotes, always compare on the same Incoterm. An FOB China quote looks cheaper than a CIF quote, but once you add your own freight and insurance, the gap often narrows or reverses — especially if the supplier has better shipping rates than you can get independently.
We've been in this industry long enough to see the pattern: a buyer picks the cheapest supplier, receives the carbon, and then discovers problems that cost far more than the savings.
Here are the most common traps:
Some suppliers test a select portion of the batch and report the best result, or use non-standard testing methods that give higher readings. When you retest the bulk delivery at an independent lab using ASTM D4607, the number comes in 50–150 mg/g lower than the certificate claims.
At that point, you've already paid, the carbon is in your warehouse, and your options are limited.
What to do: Request pre-shipment third-party testing (SGS, Bureau Veritas, Intertek) on a composite sample from the actual production batch. A reputable supplier will agree to this without hesitation.
This one hurts most in gold recovery. Low-hardness carbon breaks down in the CIL circuit, generating fines that pass through screens and carry gold out of the system. A 2% drop in hardness can translate to measurable gold loss over months of operation.
The math is simple: if your plant processes 500,000 tons of ore per year at 2 g/t gold, and poor carbon hardness causes 0.5% more gold loss, that's real money walking out the door — far more than whatever you saved per ton on carbon.
Ash doesn't adsorb anything. It's dead weight. High-ash carbon gives you less active surface area per kilogram, which means worse performance and more frequent carbon replacement. For applications like food-grade decolorization, high ash can also introduce unwanted minerals into your product.
A factory that gives you great specs on the first order and mediocre specs on the third is worse than a factory that's consistently mid-range. Process stability matters more than peak performance on one test report.
When you receive a quote, here's what to check beyond the price per ton:
The activated carbon supply chain from China typically has 2–3 layers: factory → trading company → distributor → end user. Each layer adds 10–15% markup without adding quality or accountability.
Buying direct from a manufacturer gives you:
Our factory in Fujian and Ningxia provinces produces coconut shell, coal-based, and wood-based activated carbon with monthly capacity over 700 tons. We ship directly to clients in 40+ countries — no middlemen, no markup layers. Every shipment includes SGS-testable documentation and full loading supervision with photos and video.
In 2026, FOB China pricing for coconut shell granular activated carbon ranges from $3,000 to $3,800 per ton for standard grades. Acid-washed grades range from $1,850 to $3,100 per ton. The exact price depends on your iodine requirement, mesh size, volume, and whether acid washing is needed.
Gold recovery carbon requires higher iodine (typically 1050+), higher hardness (98%+), and tighter particle size control — all of which reduce production yield. The activation process runs longer, burns off more material, and requires more precise kiln control. You're paying for performance that directly affects gold recovery rates and carbon lifespan in CIL/CIP circuits.
Only if your application requires it. Drinking water filtration meeting NSF/ANSI 61, food-grade decolorization, and pharmaceutical applications generally need acid-washed carbon for low ash and neutral pH. For industrial wastewater, gold recovery, and gas-phase applications, standard (non-acid-washed) grades work well.
Request pre-shipment composite sampling and independent lab testing. SGS, Bureau Veritas, and Intertek all offer activated carbon testing. A trustworthy supplier will welcome third-party verification — it removes doubt for both sides.
Most manufacturers have an MOQ of 10 tons, which fills one 20-foot container. Some suppliers offer smaller quantities at a premium, but for the best per-ton price, ordering at least one full container (26–28 tons in a 40GP) is recommended.
Looking for a coconut shell activated carbon quote? Tell us your application, target specs, and volume — we'll send you pricing with a full spec sheet within 24 hours. No middlemen, factory-direct.
If you're running a biogas upgrading plant or landfill gas treatment system, there's a good chance your carbon spec says "Jacobi" somewhere on it. The AddSorb and EcoSorb series have become default specifications for biogas purification across European and North American markets — covering everything from bulk H₂S removal to siloxane polishing.
That position is based on real performance. Jacobi's biogas carbons are engineered for the specific contaminant mix in biogas streams — hydrogen sulfide, ammonia, siloxanes, and VOCs that damage CHP engines and contaminate upgraded biomethane.
But "engineered for biogas" also means "priced through a distributor network." If you're consuming 20–100+ tons of carbon per year, the question worth asking is: does an equivalent carbon exist at factory-direct pricing — and does it actually perform the same?
This article breaks down Jacobi's current biogas product line, what each grade actually does, and how Huamei's HME-AC™ pellet carbon and custom-impregnated carbons compare on the parameters that determine whether your biogas meets pipeline or engine specifications.

Jacobi organizes its biogas carbons into three product families, each targeting different contaminants. Here's the current lineup:
| Jacobi Grade | Primary Target | Mechanism | Key Feature |
|---|---|---|---|
| AddSorb VA6-BG | H₂S | Catalytic oxidation
(impregnated) |
Standard biogas
H₂S grade |
| AddSorb VA12-BG | H₂S
(high concentration) |
Catalytic oxidation
(impregnated) |
Higher sulfur loading
capacity |
| AddSorb OX20 | H₂S | Catalytic oxidation | Non-impregnated,
oxygen-dependent |
| AddSorb OX30 | H₂S | Catalytic oxidation | Higher capacity
than OX20 |
| AddSorb VA10 | H₂S, mercaptans | Chemical + physical
adsorption |
Broader sulfur
compound spectrum |
| Jacobi Grade | Primary Target | Mechanism | Key Feature |
|---|---|---|---|
| AddSorb VB1-BG | NH₃, amines | Acid-impregnated
(chemical reaction) |
Purpose-built for alkaline
gas removal in biogas |
| Jacobi Grade | Primary Target | Mechanism | Key Feature |
|---|---|---|---|
| EcoSorb BS | Siloxanes (D4, D5, L2) | Physical adsorption | Optimized pore structure
for siloxane molecules |
| EcoSorb GXC | Siloxanes + VOCs | Physical adsorption | Broader spectrum,
multi-contaminant |
| ReSorb VT | VOCs + trace siloxanes | Physical adsorption | Regenerable grade
for thermal swing systems |
The key insight: Jacobi doesn't use one carbon for everything. They split the job into specialized grades — impregnated carbons for reactive gases (H₂S, NH₃), virgin carbons for physical adsorption tasks (siloxanes, VOCs), and regenerable grades for systems with thermal swing capability. Your replacement strategy needs to respect these distinctions.
Biogas purification isn't generic adsorption. The contaminant mix — H₂S, NH₃, siloxanes (D4, D5, L2), mercaptans, and halogenated compounds — demands specific carbon properties for each target:
H₂S removal operates through catalytic oxidation on the carbon surface. The carbon needs:
NH₃ removal requires the opposite chemistry — acid-impregnated carbon (typically phosphoric acid) that reacts with alkaline gases. Standard alkaline carbon does almost nothing for NH₃. This is why Jacobi has a separate grade (VB1-BG) rather than using their H₂S carbons for both.
Siloxane removal is primarily physical adsorption driven by:
The engineering reality: A single carbon grade cannot handle all three targets effectively. Most biogas plants run multi-stage systems with different carbons matched to each contaminant — and that's exactly what you should plan for when evaluating alternatives.
Replacing Jacobi biogas carbons isn't one product swap — it's matching the right Huamei grade to each Jacobi grade's function. Here's the mapping based on contaminant target and mechanism:
| Paramètres | Jacobi AddSorb H₂S Grades (typical) | Huamei KOH-Impregnated Pellet | Huamei HME-AC™60 (Virgin) |
|---|---|---|---|
| Form | Extruded pellet | Extruded pellet | Extruded pellet |
| Diamètre | 4mm | 3mm or 4mm | 4mm |
| Mechanism | Impregnated (VA6/VA12)
or catalytic (OX series) |
KOH-impregnated
(chemical + physical) |
Catalytic oxidation
(physical only) |
| H₂S capacity | Published per grade | 5–8× higher | Standard catalytic
capacity |
| CTC | 50–60% (typical) | Varies with impregnant
loading |
60% |
Replacement logic:
| Paramètres | Jacobi AddSorb VB1-BG | Huamei H₃PO₄-Impregnated Pellet |
|---|---|---|
| Raw material | Coal-based | Coal-based (Ningxia anthracite) |
| Form | Extruded pellet | Extruded pellet |
| Diamètre | 4mm | 3mm or 4mm |
| Mechanism | Acid-impregnated (reacts with NH₃) | Phosphoric acid-impregnated (reacts with NH₃) |
| Target | NH₃, amines | NH₃, amines |
Replacement logic: NH₃ removal requires acid-impregnated carbon — the chemistry is the opposite of H₂S removal. Do NOT use KOH-impregnated or standard alkaline carbon for NH₃; it won't work. Huamei produces phosphoric acid (H₃PO₄) impregnated pellet carbon specifically for alkaline gas treatment, which is the direct equivalent of VB1-BG.
| Paramètres | Jacobi EcoSorb/ReSorb (typical) | Huamei HME-AC™70 | Huamei HME-AC™80 |
|---|---|---|---|
| Raw material | Coal-based / coconut shell | Coal-based (anthracite) | Coal-based (anthracite) |
| Form | Pellet or granular | Extruded pellet | Extruded pellet |
| Diamètre | 4mm | 4mm | 4mm |
| Mechanism | Physical adsorption | Physical adsorption | Physical adsorption |
Replacement logic:

| Jacobi Grade | Target Contaminant | Huamei Equivalent | Key Matching Criteria |
|---|---|---|---|
| AddSorb VA6-BG | H₂S | KOH-impregnated pellet (custom) | Match impregnant
type + loading % |
| AddSorb VA12-BG | H₂S (high conc.) | KOH-impregnated pellet (high loading) | Higher KOH loading
for higher capacity |
| AddSorb OX20 | H₂S | HME-AC™60 | Virgin, alkaline pH,
CTC ≥60% |
| AddSorb VA10 | H₂S + mercaptans | KI-impregnated pellet (custom) | Discuss mercaptan
species with Huamei |
| AddSorb VB1-BG | NH₃, amines | H₃PO₄-impregnated pellet | Acid impregnation
required — NOT KOH |
| EcoSorb BS | Siloxanes | HME-AC™70 | CTC 70%, pore
structure for D4/D5 |
| EcoSorb GXC | Siloxanes + VOCs | HME-AC™80 | CTC 80%, broad-spectrum adsorption |
| ReSorb VT | VOCs (regenerable) | HME-AC™70 / HME-AC™80 | Confirm regen
temperature compatibility |
| Factor | Jacobi AddSorb / EcoSorb | Huamei HME-AC™ / Impregnated |
|---|---|---|
| Pricing model | Distributor network | Factory-direct |
| Distribution layers | Manufacturer → Distributor → End user | Manufacturer → End user |
| MOQ (virgin pellet) | Varies (typically 5–10 tons via distributor) | 3 tons |
| Échantillon | Through distributor | Free sample direct |
| COA | Yes | Yes (SGS available on request) |
| Custom impregnation | Limited to catalog grades | KOH, NaOH, H₃PO₄, KI — adjustable loading % |
The structural price difference is distribution economics: Jacobi passes through intermediaries between factory and end user; Huamei ships direct. For a biogas plant consuming 40–100 tons/year across multiple grades, the annual cost difference funds comprehensive pilot testing in Year 1 — and delivers ongoing savings every year after.
This deserves its own section because it's the most common mistake when switching biogas carbon suppliers.
You cannot replace impregnated carbon with virgin carbon. If your current Jacobi grade is AddSorb VA6-BG (KOH-impregnated for H₂S) or VB1-BG (acid-impregnated for NH₃), replacing it with a standard HME-AC™60 pellet will fail — the virgin carbon lacks the chemical reactivity needed for high-efficiency removal of reactive gases.
Conversely:
When requesting quotes from Huamei, always specify:
Huamei produces both KOH and H₃PO₄ impregnated carbons with adjustable loading — but they need your specific requirements to match the product correctly.
Jacobi offers several H₂S grades for biogas: AddSorb VA6-BG and VA12-BG (impregnated, high sulfur capacity), AddSorb OX20 and OX30 (non-impregnated catalytic), and AddSorb VA10 (H₂S plus mercaptans). The choice depends on H₂S inlet concentration, whether you need impregnated or catalytic removal, and bed design. For direct factory-sourced equivalents, Huamei's HME-AC™ pellet carbon (virgin catalytic) and custom KOH-impregnated pellets match these specifications.
Yes — if you match the mechanism, not just the format. For H₂S grades: impregnated Jacobi carbons (VA6-BG, VA12-BG) must be replaced with impregnated equivalents. For siloxane grades (EcoSorb BS, GXC): match CTC value and pore structure with high-CTC virgin pellet carbon like HME-AC™70 or HME-AC™80. Always run a pilot breakthrough test before committing to a full bed replacement.
AddSorb grades target reactive gases — H₂S (VA6-BG, VA12-BG, OX20, OX30, VA10) and NH₃ (VB1-BG) — using catalytic or chemical impregnation mechanisms. EcoSorb grades (BS, GXC) target siloxanes and VOCs using physical adsorption — they rely on pore structure rather than chemical treatment. ReSorb VT is the regenerable variant for thermal swing systems. They're different product families for different contaminant targets.
Typical consumption ranges from 10–100+ tons/year depending on plant capacity, contaminant levels, and number of treatment stages. A 500 Nm³/hr biogas upgrading plant with 2,000 ppm H₂S inlet typically consumes 20–40 tons/year of H₂S-grade carbon. Siloxane polishing stages consume less (5–15 tons/year) but require more frequent replacement due to faster saturation.
Yes. Huamei produces custom-impregnated pellet activated carbon including KOH-impregnated (for H₂S/acid gases), NaOH-impregnated, H₃PO₄-impregnated (for NH₃/alkaline gases), and KI-impregnated (for mercaptans). Impregnant loading percentage is adjustable to match your target contaminant concentration. MOQ is 10 tons per impregnation type, with 28-day lead time including impregnation, curing, and QC.
Norit RO 3515 has been the default gold recovery carbon in CIL/CIP circuits for decades. If you've worked in gold mining in South Africa, West Africa, or Australia, chances are RO 3515 was the first carbon your plant loaded — and possibly the only one your metallurgist ever approved.
That market position was earned. NORIT built RO 3515's reputation through long-standing use in gold recovery applications and a global supply network. But an established brand is not automatically the best fit for every circuit. Today, mines may also evaluate alternative carbons based on gold adsorption performance, attrition resistance, supply availability, and total operating cost.

This article compares RO 3515 against HMGOLD™7500 from Huamei Carbon — spec by spec, using Norit's published product data and Huamei's SGS test results (Report No. MSRCZ2500346-01A). Where the numbers speak, we let them. Where they don't, we say what's missing.
| Paramètres | Norit RO 3515 | Huamei HMGOLD™7500 | Notes |
|---|---|---|---|
| Raw material | Coconut shell | Coconut shell | Same |
| Activation | Steam | Steam | Same |
| Indice d'iode | ≥1050 mg/g | 1150 mg/g (spec) /
1208 mg/g (SGS actual) |
✅ HMGOLD higher |
| Teneur en cendres | ≤5% | 2.52% (SGS) | ✅ HMGOLD
significantly lower |
| Humidité | ≤5% | ≤5% | Match |
| Ball-pan hardness | ≥97% (ASTM D3802) | 98.2% (GB/T
method, SGS) |
⚠️ Different test methods |
| K value (gold loading) | Not typically published | 28 kg/t | HMGOLD published |
| R value (adsorption kinetics) | Not typically published | 58% | HMGOLD published |
| Densité apparente | 0.46–0.50 g/cm³ | 0.48–0.52 g/cm³ | Comparable range |
| Taille des mailles | 6×12 | 6×12, 8×16 | HMGOLD offers
more options |
| pH | Alkaline | 10.0 (SGS) | Both alkaline |
One thing jumps out immediately: The first thing to note is that RO 3515 and HMGOLD™7500 are not identical product forms. RO 3515 is an extruded activated carbon, while HMGOLD™7500 is a coconut-shell granular carbon. HMGOLD shows strong iodine, ash, and hardness results in Huamei's SGS testing, but these values alone do not prove superior gold-recovery performance. Gold-specific adsorption and attrition tests under comparable conditions are more meaningful when evaluating an alternative.Iodine is 100+ mg/g higher. Ash is half. The real question is whether those spec-sheet advantages translate to performance advantages in your specific circuit — and that requires testing, not assumptions.
Understanding why mines use RO 3515 helps you evaluate whether switching makes sense:
Track record: RO 3515 has a long history of use in gold recovery and is widely recognized in CIL/CIP applications. Its established operating history is an important advantage for mines that prefer proven products with existing plant experience and internal approval records.
Consistency: Norit's manufacturing process delivered batch-to-batch consistency that mines relied on. When you ordered RO 3515, you got RO 3515 — the carbon performed within predictable bounds every time.
Distribution reach: From Johannesburg to Perth to Accra, Norit distributors could deliver. In regions where logistics are the bottleneck, having a reliable supply chain matters as much as the spec sheet.
Inertia: This is the honest one. Many mines run RO 3515 because they've always run RO 3515. The metallurgist who approved it may have retired. The procurement team reorders on autopilot. Nobody has run a comparative trial in years — because why would you change something that works?
That last point is the opening for HMGOLD. "Works" and "optimal" are different things. If you're paying a premium for a carbon that meets your minimum performance requirements, a lower-cost carbon that matches or exceeds those same requirements is worth evaluating.
Iodine number isn't the primary metric for gold recovery carbon — K value matters more. But a higher iodine number indicates greater total micropore volume, which correlates with overall adsorption capacity. At 1208 mg/g (SGS verified), HMGOLD™7500 has roughly 15% more adsorptive capacity than RO 3515's minimum specification.
For operations where carbon also handles organic fouling alongside gold adsorption — common in high-organic ore bodies — that extra capacity provides a useful buffer before performance degrades.

This is the biggest measurable gap. HMGOLD's ash is roughly half of RO 3515's maximum specification.
Why this matters in your circuit:
Elution efficiency: Inorganic ash residues trap gold within the carbon structure during Zadra or AARL stripping. Lower ash = cleaner stripping = less residual gold left on carbon after each elution cycle. Over hundreds of cycles, that gold retention compounds into real losses.
Reactivation longevity: Ash doesn't burn off during thermal reactivation. It accumulates cycle after cycle. Carbon starting at 2.52% ash builds up contamination slower than carbon starting at 5%, maintaining its gold loading capacity through more reactivation cycles before requiring replacement.
Doré purity: Lower-ash carbon contributes fewer inorganic impurities to your final gold precipitate. If your refinery penalizes you for impurities in doré bars, your carbon's ash content directly affects your refining charges.
Here's where things get interesting. Norit/Cabot does not typically publish K value and R value for RO 3515 in the same format that Jacobi publishes for PICAGOLD G210AS.
HMGOLD™7500 publishes both:
These are competitive numbers. For context, Jacobi G210AS — another premium gold carbon — publishes K=28 kg/t and R=60%. HMGOLD™7500's K value matches G210AS exactly; the R value is 2 percentage points lower, which is within normal batch variation for most CIL circuits.
The fact that HMGOLD publishes K and R values while Norit does not is itself significant. If you're currently running RO 3515, you probably don't know its K and R values — unless you've tested it yourself. That means you're paying premium pricing for a carbon whose gold-specific performance metrics you may have never quantified.
RO 3515 comes in one size. HMGOLD offers three — which matters because mesh size selection directly affects circuit performance:
If you're running a CIP circuit on 6×12 carbon because that's all your supplier offers, you may be leaving performance on the table.
No amount of spec-sheet comparison replaces 40+ years of operational data. RO 3515 has been tested, approved, and documented in more CIL/CIP plant operating manuals than any other gold carbon. When your client requires a "proven carbon with established track record," RO 3515 checks that box without discussion.
HMGOLD™7500 is growing — Tanzania, Ghana, South Africa, Egypt, Azerbaijan — but it doesn't have decades of data yet.
Some mining companies have approved vendor lists. RO 3515 is on most of them. Getting HMGOLD approved requires a formal evaluation process — lab testing, plant trial, metallurgical report, management sign-off. That process takes 3–6 months and costs money.
If your company's procurement policy mandates approved-vendor-only purchasing, you'll need to run that approval process before HMGOLD becomes an option — regardless of how good the specs look.

Cabot's distributor network provides local technical support in major mining regions. If you have a carbon performance issue, your Cabot rep can visit your site. Huamei's support is primarily remote (WhatsApp, email, video calls) with periodic site visits for key accounts.
For operations in remote locations where on-site technical support matters, this is a real consideration — not a deal-breaker, but a factor.
| Factor | Norit RO 3515 | Huamei HMGOLD™7500 |
|---|---|---|
| Pricing model | Cabot distributor network | Factory-direct |
| Distribution layers | Manufacturer → Regional distributor → Local agent → Mine | Manufacturer → Mine |
| MOQ | Varies by distributor (typically 20+ tons) | 10 tons |
| Lead time | 2–6 weeks (dependent on distributor stock) | 2–3 weeks production + shipping |
| Échantillon | Through distributor | Free 1–2 kg sample direct |
| COA | Yes | Yes (SGS reports available) |
The structural price difference is distribution economics. RO 3515 passes through 2–3 intermediaries between Cabot's factory and your mine. Each adds margin. HMGOLD ships factory-direct from Fujian, China — one invoice, no intermediary markup.
On equivalent specifications, the price gap is significant. But "significant" varies by region, volume, and current market conditions. Get current quotes from both suppliers for your specific requirements before making assumptions based on list prices.
| Category | Norit RO 3515 | HMGOLD™7500 | Edge |
|---|---|---|---|
| Indice d'iode | ≥1050 mg/g | 1150 mg/g (spec) / 1208 (SGS) | HMGOLD |
| Teneur en cendres | ≤5% | 2.52% (SGS) | HMGOLD |
| Dureté | ≥97% (ball-pan, ASTM D3802) | 98.2% (GB/T, SGS) | Not directly comparable |
| K value (gold loading) | Not published | 28 kg/t | HMGOLD (data available) |
| R value (kinetics) | Not published | 58% | HMGOLD (data available) |
| Mesh options | 6×12 only | 6×12, 8×16, 5×10 | HMGOLD |
| Track record | 40+ years, global | Growing, Africa/Asia focus | Norit |
| Brand approvals | Industry standard | Requires evaluation | Norit |
| Pricing | Distributor markup | Factory-direct | HMGOLD |
| MOQ | 20+ tons | 10 tons | HMGOLD |
The bottom line: HMGOLD™7500 matches or exceeds Norit RO 3515 on every measurable specification — and publishes gold-specific metrics (K value, R value) that Norit doesn't. What HMGOLD lacks is the decades of operational track record and automatic brand-approval status that RO 3515 carries. If your procurement decision is based on specs and price, HMGOLD wins. If it's based on institutional history and approved-vendor lists, Norit wins. For most operations, the smart move is to run a parallel trial and let the data decide.
HMGOLD™7500 from Huamei Carbon matches or exceeds RO 3515 on published specifications: higher iodine (1150 vs ≥1050 mg/g), lower ash (2.52% vs ≤5%), and comparable hardness. Both are coconut shell, steam-activated carbons designed for CIL/CIP gold recovery. A bottle-roll test and plant trial with your specific ore is recommended to confirm equivalent performance in your circuit.
Yes. Norit RO 3515 is now manufactured by Cabot Corporation, which acquired Norit in 2012. The product continues to be available through Cabot's global distributor network. Some industry professionals report longer lead times and availability fluctuations since the acquisition, but the product specification remains unchanged.
Norit RO 3515 specifies a minimum iodine number of ≥1050 mg/g. This measures total micropore volume using the ASTM D4607 method. While useful as a general quality indicator, iodine number is not the primary metric for evaluating gold recovery carbon performance — K value (gold loading capacity) and R value (adsorption kinetics) are more relevant for CIL/CIP applications.
Three main drivers: (1) pricing — RO 3515 routes through Cabot's multi-layer distributor network, adding margin at each step; (2) alternatives have improved — Chinese manufacturers like Huamei now offer SGS-verified carbons with equivalent or superior specifications; (3) data transparency — newer brands publish gold-specific metrics (K value, R value) that help metallurgists make informed comparisons, while Norit relies on legacy reputation.
Exact pricing varies by volume, destination, and current market conditions. The structural difference comes from distribution: RO 3515 passes through 2–3 intermediaries (Cabot → regional distributor → local agent), while HMGOLD ships factory-direct. Request current quotes from both suppliers for your specific requirements — pricing from even 6 months ago may not reflect today's market.