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Sustainable Bio-Adsorbent Generated from Coffee Waste for Dual Application in Heavy Metal and Dye Removal

Lin et al.

Researched by
K. Pendergrass iD
Last updated: 2026-06-02
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Lin et al. 2025 - Coffee waste bio-adsorbent for metal and dye removal

Lin and colleagues used Coffee Powder Trimmings (CPT), including spent coffee grounds and dried coffee-processing residues, as a bio-adsorbent for copper and iron ions before converting the metal-loaded material into biochar composites for methylene blue removal. This is primary remediation/materials evidence, not coffee-ingredient occurrence evidence: the source reports engineered adsorption and biochar performance rather than metals measured in coffee as consumed.

Key numbers

Metal adsorption and biochar synthesis

The methods describe rinsed and dried CPT mixed with either FeCl3.6H2O at 0.05 g/L in 100 mL DI water or CuCl2.2H2O at 0.03 g/L in 100 mL DI water. Six grams of dried CPT were stirred with the metal solution at room temperature for 3 h, then dried and pyrolyzed at 750 degrees C for 3 h at a 5 degrees C/min ramp to generate Fe/CB or Cu/CB.

The abstract reports that CPT removed more than 95% of Cu2+ and Fe3+ through chelation. Section 3.2 and the Figure 4 captions then label the iron removal experiment as Fe2+ rather than Fe3+; see the verification notes for this source-internal inconsistency.

Kinetic fitting for the metal-removal step favored the pseudo-second-order model. The paper reports R2 = 0.998 for Cu2+ and R2 = 0.999 for iron in the PSO plots, while the PFO fit was weaker for Cu2+ (R2 = 0.883) and stronger for iron (R2 = 0.997). The authors state that both metals reached rapid removal within the first 20 min and approached equilibrium afterward.

Textural properties of CPT-derived biochars

Table 1 reports surface area, pore volume, and Raman ID/IG values:

MaterialBET surface area (m2/g)Pore volume (cc/g)ID/IG
CPT15.2300.015not reported
CB450.4930.0251.18
Cu/CB559.2130.0291.15
Fe/CB492.0970.0201.19

EDS results in the text report CPT as 51.58 wt% carbon and 47.56 wt% oxygen, with minor sulfur at 0.39 wt% and calcium at 0.47 wt%. After pyrolysis, CB carbon increased to 87.30 wt%. Cu/CB contained Cu at 0.02 wt%, and Fe/CB contained Fe at 0.10 wt%; after methylene blue adsorption, the used materials showed 0.12 wt% Cu and 2.34 wt% Fe.

Dye-removal performance after metal loading

Although dye removal is not HMTc occurrence evidence, it is part of the source’s primary dual-use remediation claim. Table 2 reports methylene blue kinetic parameters at 30 degrees C, initial dye concentration 10 mg/L, adsorbent dosage 6 g, and solution volume 0.1 L:

MaterialExperimental qe (mg/g)PFO qe (mg/g)PFO k1 (min^-1)PFO R2PSO qe (mg/g)PSO k2 (g/mg min)PSO R2
CB41.08647.050-0.0320.97344.3160.0020.948
Cu/CB52.52064.846-0.0460.97855.4310.0020.985
Fe/CB55.24246.610-0.0350.97657.6070.0030.990

Table 3 compares room-temperature methylene blue adsorption capacity and activation energy, reporting qe = 41.086 mg/g and Ea = 53.7 kJ/mol for CB, qe = 52.520 mg/g and Ea = 35.6 kJ/mol for Cu/CB, and qe = 55.242 mg/g and Ea = 48.4 kJ/mol for Fe/CB.

Fe/CB was the best-performing dye-removal material. Figure 6a reports a dose sweep of methylene blue removal at 30 mg = 34.5%, 50 mg = 39.5%, 80 mg = 65.0%, 100 mg = 85.0%, and 150 mg = 97.8%. Figure 6b reports a pH sweep at pH 3 = 90.2%, pH 5 = 86.9%, pH 6 = 91.0%, pH 7 = 80.6%, pH 7.5 = 86.2%, pH 8 = 87.8%, pH 9 = 79.3%, and pH 11 = 87.1%; the running text on page 12 also claims a maximum of 95.2% at pH 4, which is not directly shown in Figure 6b (see verification notes). Figure 6c reports 100% removal across lake, rain, tap, and seawater matrices, and Figure 6d reports recyclability of 100% for cycles 1-3, 97.98% in cycle 4, and 86.88% in cycle 5.

Methods (brief)

Coffee Powder Trimmings were supplied by CH Biotech in Nantou, Taiwan, rinsed with deionized water, dried, and used first as a metal adsorbent and then as a pyrolysis precursor. Metal ions were quantified by ICP-MS. Methylene blue was quantified by UV-Vis absorbance at 664 +/- 1 nm. Materials were characterized with SEM/EDS, TEM, XRD, BET gas adsorption, FTIR, XPS, Raman spectroscopy, and TGA/DTG.

The metal-removal step used metal chloride solutions under laboratory conditions, not environmental or food samples. The biochar step used the metal-loaded CPT after pyrolysis and evaluated dye removal across contact time, temperature, pH, dose, water body, and reuse cycles.

Implications

Certification: Do not use this source in coffee, coffee ingredient, coffee beverage, or product occurrence pools. It does not measure Cu or Fe in coffee for consumption; it uses coffee-processing waste as a remediation material.

App: Context for remediation and circular-material notes involving spent coffee grounds, coffee waste biochar, copper/iron adsorption, and dye removal.

Courses: Useful for teaching why a familiar food-derived material can be a remediation matrix without becoming food-contaminant occurrence evidence.

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Verification notes

This page was built from the full PDF, including the abstract, reagents and synthesis protocol, characterization methods, Table 1 textural properties, Figure 4 copper/iron removal kinetics, Table 2 methylene blue kinetic parameters, Table 3 dye-removal capacity and activation energy comparison, Figure 6 dose/pH/water/reuse results, XPS mechanism discussion, conclusions, and data-availability statement.

The paper has four internal inconsistencies that the source page records without resolving:

  1. Iron species: the abstract and the FeCl3.6H2O method identify Fe3+, while Section 3.2 and the Figure 4 captions refer to Fe2+. Frontmatter uses broad Fe.
  2. CB activation energy: Table 3 reports Ea = 53.7 kJ/mol for CB, while the body text on page 12 reports Ea = 39.8 kJ/mol (R2 = 0.839) for the same material. Figure 5f labels match the body text. The page reports Table 3 values in the body and flags the discrepancy here.
  3. Cu/CB activation energy: Table 3 reports Ea = 35.6 kJ/mol for Cu/CB, while the body text on page 12 reports Ea = 38.2 kJ/mol (R2 = 0.871). Figure 5f labels match the body text. The page reports Table 3 values in the body and flags the discrepancy here.
  4. Fe/CB maximum pH removal: the body text on page 12 states a maximum methylene blue removal of 95.2% at pH 4, but Figure 6b does not include a pH-4 condition and its highest value is 91.0% at pH 6.

Products and ingredients are intentionally empty in frontmatter because this is a coffee-waste remediation study (Coffee Powder Trimmings used as engineered adsorbent and biochar precursor), not a coffee-food occurrence study. The routing layer therefore records this source as advisory-malformed for missing products/ingredients, which is the expected behavior for remediation-only evidence and is not a defect to fix.

Matrices vocabulary: biochar, aqueous-sorption-test, and wastewater-remediation are precedented slugs already used by other remediation source pages. coffee-powder-trimmings and spent-coffee-grounds are descriptive kebab-case tokens introduced by this paper and should be confirmed against the matrices controlled vocabulary on the next Karen review. Fresh-context audit subagent (2026-06-02) raised this as an advisory vocabulary note; no fidelity defects were found.

Page history

The five most recent substantive edits to this page. The full version history lives in git; when DOI minting comes online (see schema docs), each entry below will also link to a version-pinned DataCite DOI.

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