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Chapter 06 of 14 · Part II · Draft web edition

Chemical cellulosic regeneration overcomes fibre shortening through controlled depolymerisation

When cotton fibres are too short for mechanical spinning, chemical recycling dissolves cellulose chains into high-purity pulp for viscose and lyocell filaments, provided degree of polymerisation and solvent recovery are tightly controlled.

Sections
7
Exhibits
5
Minutes
27
Sources
26
EX 26 · Dissolving pulp (DP 500-700; 98.8% pure). From Hydrated DES (30% H2O) or H2SO4 (60 C) (88.01% pulp yield). Leads to Wet-spinning (1.27 cN/dtex; 13.6% elong.) (Homogeneous dope).

The cloth is woven from this chapter's 5 exhibits: each weft is one exhibit's own data, normalised; each warp group is a section. The probe reads the exhibit's own value where it crosses. Procedural visualisation, not a measurement.

The chapter as a draft: 7 sections, 4 exhibit wefts, one shuttle.

Lead exhibit · 26FlowsourcedTargeted depolymerisation converts DP 2,409 cotton waste into DP 500 to 700 dissolving pulp for viscose and Lyocell wet-spinning
Sorted cotton waste(DP 2,409)Knife milling (2 mm)& finish strippingHydrated DES (30%H2O) or H2SO4 (60 C)Dissolving pulp (DP500-700; 98.8% pure)Solvent recovery(80.8% DES; >99%NMMO)Wet-spinning (1.27cN/dtex; 13.6%elong.)

Read-outSorted cotton waste (DP 2,409). Starting point. Leads to Knife milling (2 mm) & finish stripping (100% cotton clips/noils).

Method and source

Chemical process sequence synthesising hydrated choline chloride / lactic acid / water (30% H2O) deep eutectic solvent depolymerisation (S34), sequential acid/alkaline viscosity tuning (S36), and closed-loop solvent recovery and wet-spinning (S34, S35).

Unit: process stage. Status: sourced. Sources: S34, S35, S36.

The chapter's warpBar: share of the reading · square: an exhibit

Section 6.0 · Opening · 1 min · no exhibit of its own · one movement Go to section ↓

Overture · 1 min

Chemical cellulosic regeneration solves the physical limit of mechanical textile recycling by operating at the macromolecular scale rather than the staple-fibre scale.[S34][S35] When pre-consumer cotton offcuts, spinning comber noils, carding strips or ginning linters are too short to hold twist in an open-end rotor groove, chemical pre-treatment cleaves and purifies the underlying cellulose chains into dissolving pulp.[S36][S37] Dissolved into a homogenous spinning dope and extruded through precision spinnerets, regenerated man-made cellulosic fibres (MMCFs) such as viscose, modal and lyocell emerge as continuous filaments or uniform staple fibres with virgin-equivalent tenacity and lustre.[S34][S36] Yet chemical regeneration is a continuous process industry governed by strict polymer rheology, trace-metal tolerances below 20 parts per million, and capital thresholds exceeding US$140 million for standalone commercial mills.[S34][S0601] For a greenfield cotton-to-garment venture in Cameroon, the engineering decision is one of disciplined sequencing: use zero-capex shop-floor sorting to capture and grade pure cellulosic residues today, monetise non-spinnable linters and short waste as certified feedstock for existing viscose and lyocell producers in Phases 1 and 2, and defer domestic chemical reactor capital until regional cluster volumes cross commercial breakeven in Phase 3.[R06][R10][S36]

¶ 01 · 7 sources

trace-metal tolerances below 20 parts per millionS34, S0601

S34S35S36S37S0601R06R10

6.13 min · 2 sub-steps · read with a related exhibit

Chemical regeneration resets physical fibre length by dissolving cotton cellulose at the macromolecular level

Related · chapter 056 paragraphs step it

Related exhibit 21 · chapter 05Review bandsillustrativeMechanical tearing reduces cotton staple length from 27 to 30 mm virgin lint to 16 to 24 mm on pre-consumer clips and under 15 mm on post-consumer waste
0102030Virgin Cameroon lintPre-consumer knit clipsPre-consumer woven clipsPost-consumer worn cotton

Read-outVirgin Cameroon lint: low 27, central 28.5, high 30 (staple length in millimetres (mm))

Method and source

Illustrative engineering staple-length bounds across four cotton feedstock categories after five-cylinder mechanical tearing, grounded in Rieter recycling classifications (S0501) and University of Boras tearing mechanics (S0502). Values are not a measured GFT factory result.

Unit: staple length in millimetres (mm). Status: illustrative. Sources: S20, S24, S35, S0501, S0502. Illustrative figures are teaching examples, not measured factory results.

Read this exhibit in its chapter ↗
6.1 · Introduction · paragraph 1 of 6

Mechanical garnetting and carding treat the cotton fibre as an intact physical cylinder pulled apart from woven or knitted yarns by saw-tooth pins.[S20][S24] Because every pass over a pinned drum ruptures fibres, mechanical recycling shortens staple length and raises the short-fibre index, imposing a ceiling on yarn fineness and requiring carrier blends of 50 to 80 percent virgin cotton lint in apparel applications.[S20][S24] Chemical cellulosic regeneration bypasses this downcycling ceiling by dissolving the solid cotton fibre into individual poly-(beta-1,4-D-anhydroglucopyranose) chains in solution and precipitating them anew through wet or dry-jet wet spinning.[S34][S35][S36]

6.2 Dissolving cellulose converts shortened cotton waste into continuous filament dope

In a chemical regeneration line, physical staple length at the reactor inlet has zero bearing on the physical length of the extruded product.[S35][S36] Whether incoming cellulose originates from 28-millimetre virgin ginned lint, 18-millimetre mechanically torn cutting clips, 10-millimetre spinning comber noils, or 4-millimetre cottonseed linters, dissolution erases prior fibre morphology and mechanical surface fibrillation.[S34][S36][S0602] Once purified cellulose pulp is dissolved into an alkaline xanthate viscose dope or a direct solvent such as aqueous N-Methylmorpholine N-oxide (NMMO), ionic liquids, or deep eutectic solvents, metering pumps force the solution through spinneret capillaries measuring 40 to 60 micrometres in diameter.[S34][S35]

As the liquid jets enter the coagulation bath, mass transfer regenerates solid cellulose II crystal structures oriented along the filament axis by godet drawing.[S34][S35] The plant can wind the coagulated strands as continuous multifilament yarns or crimp and cut them to any commercial staple length (such as 38 millimetres for ring spinning).[S35][S36] Chemical regeneration is thus the only industrial route capable of converting zero-twist mill dust, comber noils, and multi-cycled mechanically shortened cotton back into fine shirtings and filament fabrics without sacrificing tenacity.[S20][S35][S36]

6.3 Cotton waste outperforms wood chips in alpha-cellulose purity while sparing forest land

Conventional commercial dissolving pulp is manufactured from hardwood and softwood chips using pre-hydrolysis kraft (PHK) or acid sulphite (AS) pulping.[S36][S0602] Because raw wood contains only 40 to 50 percent cellulose embedded in 20 to 30 percent lignin and 20 to 35 percent hemicelluloses, wood-pulp mills run energy-intensive digesters and bleaching towers merely to strip away half of the harvested tree mass.[S34][S36][S0602] Even after refining, reference acid sulphite dissolving wood pulp exhibits an alpha-cellulose purity of roughly 92.3 percent alongside residual pentosans.[S36]

By contrast, mature cotton lint, spinning waste, and unbleached pre-consumer cutting clips consist of 90 to over 99 percent alpha-cellulose.[S34][S36][S0602] Laboratory characterisation of three pre-consumer 100 percent cotton fabrics (Cot 1, Cot 7, and Cot 33) at Durban University of Technology confirmed untreated alpha-cellulose contents of 99.4 percent, 99.0 percent, and 99.1 percent respectively, beating the 92.3 percent wood dissolving pulp baseline by nearly 7 percentage points.[S36] Untreated cotton fabrics also showed 18 percent sodium hydroxide alkali solubility (S18, measuring degraded hemicellulose and gamma-cellulose) of only 0.28 to 1.14 percent and 10 percent alkali solubility (S10) of 0.80 to 1.24 percent, compared with 4.94 percent S18 and 10.50 percent S10 in reference wood pulp.[S36]

Substituting cotton textile waste and linters for wood dissolving pulp starts with a lignin-free feedstock rich in alpha-cellulose.[S34][S36] European Commission analyses establish that textiles rank fourth highest among European Union consumption categories for overall environmental and climate impact and third highest for water and land use.[S38] Diverting pre-consumer cotton clips and linters into dissolving pulp displaces forestry land use and reduces textile carbon dioxide emissions by up to 33 percent when circular recycling replaces virgin extraction.[S36][S38]

6.43 min · 2 sub-steps · 2 exhibits

Waste cotton's high degree of polymerisation must be tuned from above 2,000 down to the 500 to 700 window

Step 1 of 5Alpha-cellulose purity

Exhibit 27 · sourcedDeep eutectic solvent depolymerisation achieves 98.80 percent alpha-cellulose purity and 88.01 percent pulp yield from waste cotton

025507510098.8Alpha-cellulose purity88Pulp mass yield85.8Pulp whiteness80.8DES solvent recovery13.6Fibre elongation atbreak
025507510098.8Alpha-cellulosepurity88Pulp massyield85.8Pulpwhiteness80.8DESsolvent…13.6Fibreelongati…

Alpha-cellulose purity

Alpha-cellulose purity: 98.8 percent · sourced

If cotton waste has higher alpha-cellulose purity than wood pulp, why cannot a spinner feed shredded cotton clips directly into a viscose or Lyocell dissolver?

Pulp mass yield

Pulp mass yield: 88 percent · sourced

Pulp whiteness

Pulp whiteness: 85.8 percent · sourced

DES solvent recovery

DES solvent recovery: 80.8 percent · sourced

Fibre elongation at break

Fibre elongation at break: 13.6 percent · sourced

Method and source · Exhibit 27

Experimental performance metrics from hydrated choline chloride / lactic acid / water (30% water content) depolymerisation of waste cotton textiles from DP 2,409 to DP 500-700, followed by wet-spinning into regenerated cellulose fibres (breaking strength 1.27 cN/dtex, iron content 17.01 ppm) (S34).

Unit: percent. Status: sourced. Sources: S34.

6.4 · the bodyExhibit 27 above; its figures are illustrative where marked.

If cotton waste has higher alpha-cellulose purity than wood pulp, why cannot a spinner feed shredded cotton clips directly into a viscose or Lyocell dissolver?[S34][S36] The primary chemical obstacle is the excessively high Degree of Polymerisation (DP) and intrinsic viscosity of native and pre-consumer cotton cellulose.[S34][S36] Degree of polymerisation measures the average number of anhydroglucose monomer units linked inside a cellulose chain; scoured and dyed pre-consumer cotton textiles retain a DP above 2,000, such as the baseline DP of 2,409 measured in recent deep eutectic solvent trials.[S34]

¶ 01 · 2 sources

scoured and dyed pre-consumer cotton textiles retain a DP above 2,000S34

Related · Exhibit 23 · chapter 05

S34S36

6.5 Excessive macromolecular chain length causes hydrogen-bond entanglement and filter blockage

6.5

Commercial viscose and Lyocell lines are engineered around wood dissolving pulps whose DP has been lowered into a window of 500 to 900 (and aged down to 250 to 350 in alkali cellulose prior to xanthation).[S34][S36] Because every anhydroglucose ring carries three hydroxyl groups that form dense intramolecular and intermolecular hydrogen bonds, a polymer chain of 2,409 glucose units exhibits severe hydrodynamic entanglement in solution.[S34][S35]

¶ 02 · 3 sources

a polymer chain of 2,409 glucose units exhibits severe hydrodynamic entanglement in solutionS34, S35

S34S36S35

Size-exclusion chromatography (SEC) of untreated pre-consumer cotton fabrics quantifies this macromolecular gap.[S36] In the Durban University of Technology study, untreated cotton fabrics Cot 1 and Cot 7 recorded weight-average molecular masses (Mw) of 975,078 g/mol and 961,810 g/mol, and number-average molecular masses (Mn) of 448,006 g/mol and 566,816 g/mol.[S36] Commercial acid sulphite wood pulp (AS DWP) recorded an Mw of 204,865 g/mol and Mn of 113,041 g/mol, while pre-hydrolysis kraft (PHK) wood pulp recorded an Mw of 412,185 g/mol and Mn of 219,498 g/mol.[S36]

¶ 03 · 1 source

and number-average molecular masses (Mn) of 448,006 g/mol and 566,816 g/molS36

S36

With four times the molecular mass of acid sulphite wood pulp, untreated cotton fabrics exhibited cupriethylenediamine intrinsic viscosities between 1,313 and 1,415 mL/g (1,415 mL/g for Cot 1, 1,313 mL/g for Cot 7, and 1,397 mL/g for Cot 33), far above the 400 to 600 mL/g viscose window (502 mL/g for AS DWP).[S36] Attempting to dissolve DP 2,409 cotton waste directly produces an unpumpable gel that blinds candle filters, raises the Treiber filter-clogging value (Kw), and ruptures filaments at the spinneret.[S34][S36]

¶ 04 · 2 sources

1,313 mL/g for Cot 7S36

S36S34

6.6 Hydrated deep eutectic solvents achieve controlled depolymerisation at 30 percent water content

6.6

Overcoming the viscosity barrier requires controlled cleavage of glycosidic bonds without over-hydrolysing chains into sugars or collapsing pores through hornification.[S34][S35][S36] Peer-reviewed research published in 2026 demonstrated a solvent-mediated strategy using a hydrated deep eutectic solvent (DES) of choline chloride, lactic acid, and water to convert waste cotton textiles into dissolving pulp.[S34] By tuning the water content to 30 percent, researchers controllably reduced the DP of waste cotton pulp from 2,409 into the target 500 to 700 window while preserving chemical composition and cellulose I crystallinity.[S34] The process sequence from high-DP cotton waste to wet-spun filament is mapped in Exhibit 26.[S34][S35][S36]

¶ 05 · 3 sources

By tuning the water content to 30 percentS34

Exhibit 26

S34S35S36

As shown in Exhibit 26, controlling the depolymerisation window between DP 500 and 700 bridges the gap between raw textile waste and filament extrusion, though process-flow diagrams cannot establish continuous reactor heat-transfer performance.[S34][S35] Quantitative pulp and fibre metrics from the hydrated DES route are presented in Exhibit 27.[S34]

¶ 06 · 2 sources

…the depolymerisation window between DP 500 and 700 bridges the gap between raw textile…S34, S35

Exhibit 26Exhibit 27

S34S35

The benchmarks in Exhibit 27 confirm five engineering realities for waste-cotton pulping: 98.80 percent alpha-cellulose purity, 88.01 percent gravimetric pulp yield (nearly double wood-chip pulping), 85.80 percent whiteness with 17.01 ppm iron content, 80.80 percent DES recovery, and wet-spun fibre tenacity of 1.27 cN/dtex at 13.63 percent elongation.[S34] While these laboratory results validate the macromolecular mechanism, an 80.80 percent DES recovery rate remains below the 99-plus percent recovery of industrial NMMO Lyocell plants.[S34][S35]

¶ 07 · 2 sources

98.80 percent alpha-cellulose purityS34

Exhibit 27

S34S35

6.73 min · 2 sub-steps · 1 exhibit

Alkaline, acid and oxidative pre-treatments strip reactive dyes and adjust intrinsic viscosity for viscose integration

Exhibit 285 paragraphs step it

Exhibit 28RegistersourcedAcid hydrolysis and hypochlorite bleaching align pre-consumer cotton waste viscosity, molecular mass and metal ash with wood dissolving pulp
Property (Unit)
Intrinsic viscosity (mL/g)
AS DWP (Wood Ref)
502
UT Cot 1 (Raw)
1,415
TA Cot 1 (Acid)
419
TB Cot 1 (Bleach)
393
TA Cot 7 (Acid)
442

Read-outProperty (Unit): Intrinsic viscosity (mL/g). AS DWP (Wood Ref): 502. UT Cot 1 (Raw): 1,415. TA Cot 1 (Acid): 419. TB Cot 1 (Bleach): 393. TA Cot 7 (Acid): 442

Open the full register (9 rows)
Intrinsic viscosity (mL/g)5021,415419393442
Alpha-cellulose (%)92.399.498.597.996.7
ISO brightness (%)92.735.732.879.297.8
Alkali solubility S18 (%)4.90.30.91.21.8
Number-average Mn (g/mol)113,041448,006111,57498,290102,622
Weight-average Mw (g/mol)204,865975,078222,112250,971296,521
Polydispersity (Mw/Mn)2.82.22.12.62.9
Calcium Ca (mg/kg dry)194063623822
Magnesium Mg (mg/kg dry)41356748
Method and source

Experimental data from Shangase, Chetty and Wessels (2024), Chemical Engineering Transactions Vol. 113, Tables 1, 2 and 3 (S36). AS DWP = Acid Sulphite Dissolving Wood Pulp reference; UT = Untreated pre-consumer 100% cotton fabric; TA = Treatment A (5% H2SO4 at 60 C for 50-53 min); TB = Treatment B (hypochlorite bleaching at 60 C for 30 min).

Unit: laboratory characterisation (TAPPI / ISO / SEC). Status: sourced. Sources: S36.

6.7 · Introduction · paragraph 1 of 5

Existing commercial dissolving-pulp and viscose mills rely on aqueous acid hydrolysis, alkaline extraction, and oxidative bleaching to prepare cotton waste for regeneration.[S35][S36] Before dyed or finished cotton textiles enter a viscose reactor, covalent reactive dyes, vat pigments, optical brighteners, and crosslinking resins must be cleaved so they do not form insoluble gel particles during xanthation.[S35][S36]

6.8 Sulphuric acid hydrolysis and hypochlorite bleaching align intrinsic viscosity with wood dissolving pulp

In the 2024 Chemical Engineering Transactions study by Shangase, Chetty, and Wessels, researchers cut FTIR-verified 100 percent pre-consumer cotton waste into 2 to 3 square centimetre pieces, milled them through a 2-millimetre sieve, and evaluated two pre-treatments against Acid Sulphite Dissolving Wood Pulp (AS DWP).[S36] Treatment A applied sulphuric acid hydrolysis (5 percent H2SO4 at 60 degrees Celsius across 10 to 120 minutes), reaching ideal post-pretreatment viscosity in 53 minutes for Cot 1 (419 mL/g) and 50 minutes for Cot 7 (442 mL/g).[S36] Treatment B applied hypochlorite bleaching at 60 degrees Celsius for 30 minutes, reaching 393 mL/g for Cot 1 and 389 mL/g for Cot 7.[S36] The analytical results across TAPPI viscosity, alkali solubility, ISO brightness, SEC molecular mass, and heavy-metal ash are compiled in Exhibit 28.[S36]

Inspecting Exhibit 28 shows why pre-treatment must match the optical and mineral profile of incoming cotton waste.[S36] On dyed Cot 1 (35.7 percent brightness), acid hydrolysis (Treatment A) cut viscosity to 419 mL/g and calcium from 406 mg/kg to 36 mg/kg, but left dye chromophores intact at 32.8 percent brightness, whereas hypochlorite bleaching (Treatment B) cleaved the dye and raised brightness by 43.5 percentage points to 79.2 percent (and by 27.4 percentage points on dark Cot 33).[S36] On white Cot 7 (111.9 percent initial brightness due to optical brighteners), acid hydrolysis stripped brighteners to 97.8 percent brightness, reduced Mw from 961,810 g/mol to 296,521 g/mol, and stripped calcium from 478 mg/kg to 22 mg/kg and magnesium from 235 mg/kg to 8 mg/kg, matching reference wood pulp (19 mg/kg Ca and 4 mg/kg Mg) while retaining 96.7 percent alpha-cellulose.[S36] After alkali ageing into viscose dope, the treated cotton achieved final DPs between 267 and 324, inside the 250 to 350 viscose spinning window, though continuous filament tenacity was not measured.[S36]

6.9 Unbleached pre-consumer cutting clips and comber noils bypass aggressive dye stripping

Aggressive hypochlorite bleaching on dyed fabrics raised the TAPPI T 430 cm:2009 copper number (oxidative damage) from 0.21 to 9.70 on Cot 7 and from 0.162 to 4.95 on Cot 33 (over-depolymerising Cot 33 to 145 mL/g), whereas mild acid hydrolysis kept copper numbers at 1.00 to 2.10, matching the 1.27 wood-pulp reference.[S36] In Cameroon, four cellulosic streams arise in an unbleached or white state prior to dyeing: SODECOTON cottonseed linters (9,000 to 15,000 tonnes a year across a 340,000 tonne crop), spinning card strips and comber noils at Camtext SA or CICAM scale (960 to 2,160 tonnes a year on 12,000 tonnes of lint), greige selvedges, and unbleached CMT cutting clips.[R01][R03][R10][S37] Segregating unbleached clips at the cutting table allows pulp off-takers to use mild acid or hydrated DES viscosity tuning alone, preserving >98 percent alpha-cellulose and ~88 percent pulp yield.[S34][S36]

Key figures from chapter 01 · Exhibit 01Key figuressourcedGlobal circularity indicators describe different boundaries and cannot be added as one flow
  • 124 MtFibre productionGlobal annual output in 2023
  • 73%Landfilled or burnedClothing materials at end of life
  • <1%Old clothing into new clothingGlobal closed-loop estimate
  • >US$500bnAnnual value lost2017 estimate including underutilisation

Read-outFibre production: 124 Mt. Global annual output in 2023

Method and source

Annual fibre production is a supply measure. Landfill or burning and clothing-to-clothing recycling are end-of-life measures. The value-loss estimate also includes clothing underutilisation. No tonnage conversion or common denominator is inferred.

Unit: reported global measures, with source dates retained. Status: sourced. Sources: S02, S08, S09.

Read this exhibit in its chapter ↗

6.102 min · 2 sub-steps · 1 exhibit

Direct solvent spinning via NMMO (Lyocell) and ionic liquids avoids carbon disulphide emissions

Once waste cotton is depolymerised into dissolving pulp, its environmental footprint and capital threshold depend on the spinning chemistry: derivatising routes (viscose xanthate and cellulose carbamate) versus direct dissolution routes (NMMO Lyocell, ionic liquids, and deep eutectic solvents).[S34][S35][S36]

6.11 Xanthate derivatisation in conventional viscose requires carbon disulphide abatement

6.11

In conventional viscose production, dissolving pulp is steeped in 17 to 19 percent aqueous sodium hydroxide (NaOH), aged to DP 250 to 350, reacted with liquid carbon disulphide (CS2) into sodium cellulose xanthate, and extruded into an acidic bath containing sulphuric acid, sodium sulphate, and zinc sulphate.[S35][S36] While viscose has a massive global installed base for co-processing recycled pulps, carbon disulphide is a volatile neurotoxin and zinc sulphate requires strict effluent precipitation.[S35] Modern viscose plants require multi-stage gas-scrubbing units to recover 95 to 98 percent of sulphur emissions under Zero Discharge of Hazardous Chemicals (ZDHC) rules, making small greenfield viscose reactors inside emerging garment parks unsound.[S28][S35]

¶ 02 · 3 sources

dissolving pulp is steeped in 17 to 19 percent aqueous sodium hydroxide (NaOH)S35, S36

S35S36S28

6.12 Closed-loop NMMO Lyocell and emerging ionic-liquid or carbamate systems recover solvent directly

6.12

To avoid carbon disulphide, the Lyocell process dissolves cellulose directly in aqueous N-Methylmorpholine N-oxide (NMMO) at 90 to 120 degrees Celsius (around 13.3 percent water) and extrudes the dope across an air gap into an aqueous coagulation bath.[S35][S0602] VTT's July 2026 review identifies NMMO dissolution as the closest direct-solvent route to widespread industrial implementation because it builds on commercial Lyocell lines (such as REFIBRA, NuCycl, and SaXcell), achieves up to 95 percent cellulose recovery, and recycles over 99 percent of the NMMO solvent.[S35]

¶ 03 · 2 sources

…aqueous N-Methylmorpholine N-oxide (NMMO) at 90 to 120 degrees Celsius (around 13.3 percent water)…S35, S0602

S35S0602

Alongside NMMO, three next-generation platforms are advancing: (1) Ionic liquids (Ioncell, DBNH-OAc, AmimCl, BmimCl) dissolve cotton at 80 to 130 degrees Celsius for dry-jet wet spinning while keeping polyester purity at 92 to 96 percent, though solvent cost and recycling energy remain hurdles; (2) Cellulose carbamate (CCA) reacts activated pulp with urea at 120 to 180 degrees Celsius so the carbamate dissolves in cold aqueous sodium zincate (ZnO/NaOH) and spins on standard viscose machines without CS2; and (3) Hydrated zinc chloride and deep eutectic solvents depolymerise and dissolve cotton at 60 to 100 degrees Celsius once solvent recovery rises from 80.80 percent toward 98 percent.[S34][S35][S36] These routes are compared against mechanical tearing across six engineering axes in Exhibit 29.[S20][S34][S35][S36]

¶ 04 · 4 sourcesExhibit 29

S34S35S36S20

Exhibit 29ExhibitderivedMechanical tearing, Lyocell NMMO regeneration, viscose co-processing and DES depolymerisation trade off capex against fibre quality

Derived multi-criteria engineering comparison scored from 1 (lowest/poorest performance) to 5 (highest/best performance) across six operational dimensions: Capex efficiency (5 = lowest capital threshold), Energy efficiency (5 = lowest kWh/t), Solvent safety (5 = no toxic solvents), Staple restoration (5 = virgin-equivalent filament/staple), Short-fibre acceptance (5 = accepts <10 mm linters/dust), and Industrial readiness (5 = TRL 9 mature commercial scale) based on S20, S34, S35 and S36.

Read-outMechanical tearing, Lyocell NMMO regeneration, viscose co-processing and DES depolymerisation trade off capex against fibre quality

Method and source

Derived multi-criteria engineering comparison scored from 1 (lowest/poorest performance) to 5 (highest/best performance) across six operational dimensions: Capex efficiency (5 = lowest capital threshold), Energy efficiency (5 = lowest kWh/t), Solvent safety (5 = no toxic solvents), Staple restoration (5 = virgin-equivalent filament/staple), Short-fibre acceptance (5 = accepts <10 mm linters/dust), and Industrial readiness (5 = TRL 9 mature commercial scale) based on S20, S34, S35 and S36.

Unit: normalised engineering score (1 = worst, 5 = best). Status: derived. Sources: S20, S34, S35, S36.

As Exhibit 29 shows (noting that radar polygon area depends on axis ordering and is not a physical total), mechanical tearing scores 5 on capex, energy, solvent safety, and readiness (TRL 9), but 2 on staple restoration and 1 on short-fibre acceptance (<10 to 12 mm).[S20][S24] Lyocell NMMO and viscose co-processing score 4 to 5 on staple restoration and short-fibre acceptance, but require heavy chemical plants or CS2 abatement, while hydrated DES pulping remains at pilot readiness (score 2).[S34][S35][S36]

¶ 01 · 5 sources

mechanical tearing scores 5 on capexS20, S24

Exhibit 29

S20S24S34S35S36

6.132 min · 2 sub-steps · read with a related exhibit

Commercial lessons from first-generation chemical recyclers highlight feedstock cost and minimum scale

Chemical textile recycling is governed by plant minimum efficient scale, feedstock logistics, and pulp market pricing.[S10][S0601] Between 2020 and 2025, first-generation standalone chemical recyclers collided with linear commodity economics.[S0601]

6.14 Capital intensity and price premiums exposed standalone greenfield pulp mills to liquidity risk

6.14

Sweden's Renewcell, founded in 2012 to convert cotton-rich waste into Circulose dissolving pulp, operated a demonstration plant in 2019, listed on Nasdaq First North in November 2020, and invested about US$140 million to launch commercial production at a former paper mill in Ortviken in December 2022.[S0601] Despite proven chemistry, Renewcell filed for bankruptcy in February 2024 before Altor Equity Partners acquired its assets three months later.[S0601] A July 2024 analysis by Renewcell's former Chief Commercial Officer identifies four structural lessons: (1) projecting a 12-month breakeven against a 12-to-18-month apparel development cycle; (2) pricing Circulose above cyclical virgin wood-pulp troughs without binding mandates; (3) shipping waste from as far as Bangladesh to Sweden and shipping pulp back to Asian spinners; and (4) relying on non-binding brand pledges that stalled under margin pressure.[S10][S0601] As Reverse Resources notes, scaling chemical recycling from 12,000 tonnes toward 200,000 tonnes a year requires clean, pre-sorted pre-consumer waste close to spinning hubs.[S10]

¶ 02 · 2 sources

and invested about US$140 million to launch commercial production at a former paper mill…S0601

S0601S10

6.15 Co-processing 10 to 20 percent cotton-waste pulp inside existing viscose mills de-risks capital

6.15

The antidote to the US$140 million standalone greenfield mill trap is co-processing: depolymerising cotton waste in a modular pre-treatment unit and blending it at 10:90 (10 percent) or 20:80 (20 percent) with conventional wood dissolving pulp inside an existing viscose or Lyocell plant.[S36][S0601] In the Durban University of Technology trials, Treiber filterability tests (measuring filtration value Fw, filter-clogging value Kw, and 24 to 78 second falling-ball viscosity times) proved that raising the treated cotton share to 20 percent (the 20:80 blend) improved dope homogeneity, stability, and filterability (lower Kw) through stronger intermolecular cellulose connections.[S36] A 20:80 blend also meets the 20 percent minimum certified recycled content threshold for Global Recycled Standard (GRS v4) labelling under algorithmic mass balance.[S28][S36]

¶ 03 · 3 sources

The antidote to the US$140 million standalone greenfield mill trap is co-processingS36, S0601

S36S0601S28

6.162 min · 2 sub-steps · read with a related exhibit

Trace impurities of iron, calcium and synthetic polymers poison chemical spinning dopes

In a chemical dissolving reactor, trace inorganic cations and synthetic polymers act as catalyst poisons and filter blockers.[S34][S35][S36]

6.17 Transition metals catalyse exothermic NMMO decomposition while alkaline earth metals clog spinnerets

6.17

Three contaminant classes must remain below strict parts-per-million (ppm, or mg/kg) tolerances: (1) Transition metals (Fe, Cu, Mn, Cr, Ni) catalyse N-O bond cleavage and rapid exothermic runaway in hot NMMO, requiring iron below 15 to 20 ppm (achieved at 17.01 ppm Fe in S34, alongside 0.28 to 7.07 mg/kg Cu and 0.21 to 0.57 mg/kg acid-treated Cr in S36); (2) Alkaline earth metals (Ca, Mg) from hard water and floor dust measured 406 to 514 mg/kg Ca and 90 to 235 mg/kg Mg in untreated cotton (S36), blinding spinneret filters until dilute sulphuric acid hydrolysis stripped them to 22 to 36 mg/kg Ca and 6 to 8 mg/kg Mg (matching the 19 mg/kg Ca and 4 mg/kg Mg wood-pulp reference); and (3) Synthetic polymers (elastane, polyester) form deformable micro-gels or oligomers that plug spinneret orifices.[S26][S34][S35][S36]

¶ 02 · 4 sources

S26S34S35S36

6.18 Shop-floor segregation and analytical batch certificates guarantee reactor-grade purity

6.18

Unlike post-consumer municipal rags, pre-consumer 100 percent cotton clips segregated on GFT's cutting tables (never touching concrete floors) combined with SODECOTON linters and Camtext SA comber noils start with near-zero synthetic or metal contamination.[R03][R10][S10] Pairing table sorting with regional benchtop NIR verification (91.7 percent composition and 92.6 percent elastane accuracy across 900 to 1,700 nm, S26, as benchmarked in European sorting trials, S17) enables a Cameroon cluster to issue an analytical batch certificate with every export lot documenting polymer purity, intrinsic viscosity, and ash content.[S17][S26][S28][S36]

¶ 03 · 7 sources

pre-consumer 100 percent cotton clips segregated on GFT’s cutting tables (never touching concrete floors)…R03, R10, S10

R03R10S10S17S26S28S36

Method

6.19 Mass-balance and macromolecular calculation boundary for cotton-to-pulp conversion

GFT applies a four-step calculation boundary across ginning, spinning, and cutting-room streams:[R01][S34][S36]

  1. Polymer chain cleavage ratio ($R_{\text{DP}}$): Given initial cotton $\text{DP}_0$ and target pulp $\text{DP}_t \in [500, 700]$, average glycosidic scissions per chain are $N_s = (\text{DP}_0 / \text{DP}_t) - 1$ ($3.0$ scissions from $\text{DP}_0 = 2,409$ to $\text{DP}_t = 602$, reducing $M_w$ from $\approx 968,000\text{ g/mol}$ into the $205,000\text{ to }296,000\text{ g/mol}$ viscose window).[S34][S36]
  2. Bone-dry Dissolving Pulp Mass Yield ($M_{\text{pulp}}$): From bone-dry cotton input $M_{\text{in}}$, output is $M_{\text{pulp}} = M_{\text{in}} \times (1 - L_{\text{mech}}) \times Y_{\text{chem}}$, where $L_{\text{mech}} \in [0.02, 0.04]$ (illustrative milling loss) and $Y_{\text{chem}} = 0.8801$ (S34).[S34][S36]
  3. Solvent Makeup Requirement ($M_{\text{solv,make}}$): For liquor ratio $R_L$ and recovery $\eta_{\text{rec}}$, makeup per tonne of pulp is $M_{\text{solv,make}} = [R_L \times (1 - \eta_{\text{rec}})] / Y_{\text{chem}}$; raising $\eta_{\text{rec}}$ from $0.8080$ (S34) to $0.9950$ (S35) cuts makeup mass by a factor of 38.[S34][S35]
  4. GRS v4 Co-Processing Blend Balance ($B_{\text{GRS}}$): Recycled share $F_{\text{rec}} = M_{\text{pulp}} / (M_{\text{pulp}} + M_{\text{wood}}) \ge 0.20$ (the 20:80 blend in S36), reconciled against empirical wet-spinning loss rates under GRS v4.[S28][S36]

6.204 min · 2 sub-steps · 1 exhibit

Cameroon's chemical circularity role is exporting graded cellulosic feedstock or co-processing linters before building reactors

Step 1 of 7Unbleached CMT knit clips

Exhibit 30 · derivedFeedstock allocation matrix routes long clips to mechanical rotor spinning and short linters or noils to chemical dissolving pulp

Chemical dissolving pulpMechanical rotor spinningFractionation or biomassNon-woven insulationStaple length index (0 = 24 mm) →Cellulose purity index (0 = mixed, 10 = pure) →Unbleached CMT knit c…Colour-sorted CMT wov…Spinning comber noilsSODECOTON cotton lint…Mechanical tearing dr…Polycotton uniform tr…Post-consumer friperi…
Chemical dissolving pulpMechanical rotor spinningFractionation or biomassNon-woven insulationStaple length index (0 = 24 mm) →Cellulose purity index (0 = mixed, 10 =… →Unbleached CMT knit c…Colour-sorted CMT wov…Spinning comber noilsSODECOTON cotton lint…Mechanical tearing dr…Polycotton uniform tr…Post-consumer friperi…

Unbleached CMT knit clips

Unbleached CMT knit clips: Staple length index (0 = 24 mm) 8.2, Cellulose purity index (0 = mixed, 10 = pure) 9.5. Quadrant: Mechanical rotor spinning · derived

Containing Phase 1 capital to high-utilisation CMT operations while partnering upstream and downstream avoids premature chemical reactor capex.

Colour-sorted CMT woven clips

Colour-sorted CMT woven clips: Staple length index (0 = 24 mm) 6.8, Cellulose purity index (0 = mixed, 10 = pure) 8.4. Quadrant: Mechanical rotor spinning · derived

Spinning comber noils

Spinning comber noils: Staple length index (0 = 24 mm) 3.5, Cellulose purity index (0 = mixed, 10 = pure) 9.6. Quadrant: Chemical dissolving pulp · derived

SODECOTON cotton linters

SODECOTON cotton linters: Staple length index (0 = 24 mm) 1.8, Cellulose purity index (0 = mixed, 10 = pure) 9.2. Quadrant: Chemical dissolving pulp · derived

Mechanical tearing droppings

Mechanical tearing droppings: Staple length index (0 = 24 mm) 2.4, Cellulose purity index (0 = mixed, 10 = pure) 8. Quadrant: Chemical dissolving pulp · derived

Polycotton uniform trims

Polycotton uniform trims: Staple length index (0 = 24 mm) 6.2, Cellulose purity index (0 = mixed, 10 = pure) 3.5. Quadrant: Non-woven insulation · derived

Post-consumer friperie discards

Post-consumer friperie discards: Staple length index (0 = 24 mm) 2.5, Cellulose purity index (0 = mixed, 10 = pure) 1.8. Quadrant: Fractionation or biomass · derived

The method behind it: Worked example.

Method and source · Exhibit 30

Derived engineering allocation matrix plotting seven Cameroon textile and ginning waste fractions by recoverable staple length index (x-axis: 0 = 24 mm long staple) and alpha-cellulose / mono-material purity index (y-axis: 0 = mixed post-consumer synthetics, 5 = dyed/blended industrial scrap, 10 = >98% unbleached pure cotton) based on S24, S34, S35, S36 and S37.

Unit: fibre length and cellulose purity index (0 to 10). Status: derived. Sources: S24, S34, S35, S37.

6.20 · the bodyExhibit 30 above; its figures are illustrative where marked.

Containing Phase 1 capital to high-utilisation CMT operations while partnering upstream and downstream avoids premature chemical reactor capex.[R08][R09][R12][S0601]

¶ 01 · 4 sources

Containing Phase 1 capital to high-utilisation CMT operations while partnering upstream and downstream avoids…R08, R09, R12, S0601

Related · Exhibit 68 · chapter 14

R08R09R12S0601

6.21 Exporting purified linters, comber noils and card droppings monetises non-spinnable fractions immediately

6.21

Long, clean CMT cutting clips (18 to 24 mm after opening) belong in regional open-end rotor spinning blended at 20 to 35 percent with virgin SODECOTON lint (Chapter 5).[R03][S24][S25] Conversely, three Cameroon streams are physically too short (<12 mm) for mechanical apparel spinning and should be aggregated for chemical dissolving pulp: (1) SODECOTON cottonseed linters and gin motes (estimated at 9,000 to 15,000 tonnes a year across nine gins from a 314,455 to 350,000+ tonne seed-cotton crop); (2) Spinning comber noils and filter dust at Camtext SA's 12,000 tonne a year hub (US$300 million / 180 billion XAF) and SODECOTON-CICAM (estimated at 600 to 1,200 tonnes a year of <12 mm virgin fibers); and (3) Mechanical tearing droppings (<10 mm, 10 to 15 percent of torn clip mass) plus high-twist woven clips.[R01][R02][R03][R08][R09][R10][S20][S24][S37] This allocation is mapped in Exhibit 30.[S24][S34][S35][S37]

¶ 02 · 12 sources

clean CMT cutting clips (18 to 24 mm after opening) belong in regional open-end…R03, S24, S25

Exhibit 30

R03S24S25R01R02R08R09R10S20S37S34S35

As Exhibit 30 demonstrates, the upper-right quadrant (Mechanical rotor spinning) captures long CMT knit and woven clips, while the upper-left quadrant (Chemical dissolving pulp) captures short, high-purity SODECOTON linters, comber noils, and tearing droppings.[S24][S34][S36][S37] Polycotton uniform trims route to Non-woven insulation (lower-right), while post-consumer friperie discards sit in the lower-left quadrant where chemical fractionation is uneconomic.[S24][S29][S35]

6.23 Phase 3 conditions precedent gate regional depolymerisation investment behind proven cluster volume

6.23

Consistent with GFT's four-phase programme spine (Feasibility Study Section 12) and Renewcell's lessons, committing capital to a domestic pre-treatment and dissolving-pulp module in Phase 3 (post-2030) requires four conditions precedent: (1) Aggregated domestic feedstock above 15,000 tonnes a year verified in PMS and ISO 59020 logs across SODECOTON, Camtext SA, and CMT plants operating above 75 percent utilisation; (2) Binding multi-year take-or-pay offtake contracts with MMCF spinners indexed to wood dissolving pulp plus a GRS v4 premium; (3) Demonstrated >98 percent solvent recovery (for DES/ionic liquids) or industrial hub effluent integration (for dilute acid/alkaline hydrolysis at Dibamba or Garoua); and (4) Zero elastane and polyester carryover enforced by NIR spectroscopy (Chapter 4) and mono-material design (Chapter 7).[R07][R08][R10][S26][S28][S34][S35][S36][S40][S0601]

¶ 04 · 10 sources

and CMT plants operating above 75 percent utilisationR07, R08, R10, S26, S28, S34, S35, S36, S40, S0601

R07R08R10S26S28S34S35S36S40S0601

By respecting polymer physics and industrial scale thresholds, GFT's circularity blueprint captures the macromolecular value of Cameroon's cotton harvest without exposing the greenfield garment venture to premature chemical-plant capital risk.[R06][S34][S0601] Where Chapter 6 has established how pure cotton cellulose is depolymerised and regenerated when fibres become too short for mechanical spinning, Chapter 7 confronts the chemical and design challenge that arises when cotton is blended with synthetic polyester and elastane.[S35]

¶ 05 · 4 sources

R06S34S0601S35

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Every knot is a source this chapter cites; select one to read its record, or filter the register by grade. Publication dates and inherited-source limits stay explicit. Read the paper's full evidence summary.

26 sources · 249 citation marks on this pageMost cited: S36, 63 times

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R01 · Grade C · inherited record

Business in Cameroon

Inherited evidence R01

Cameroon seed-cotton production 2022-2024: 330,000 t (2022), 314,455 t (2023), about 340,000 t (2024).

Publication date unrecorded. Inherited source-text record. The original publication has not been independently reopened for this web edition.

Chapter source notes

S34 National Library of Medicine (PubMed). 2026.

S35 VTT Technical Research Centre of Finland and MDPI Textiles. 2026-07-31.

S36 Chemical Engineering Transactions (AIDIC). 2024-11-02.

S37 UNCTAD (UN Trade and Development). 2019-10.

S0601 Stanford Social Innovation Review. 2024-07-24.

R06 Cameroon Trade Hub. Publication date unrecorded; inherited source-text check.

R10 Ecofin Agency. Publication date unrecorded; inherited source-text check.

S20 European Commission and Refashion. 2021-11.

S24 United Nations Industrial Development Organization (UNIDO). 2023-11.

S0602 Chalmers University of Technology. 2016.

S38 European Commission Directorate-General for Environment. 2024.

R01 Business in Cameroon. Publication date unrecorded; inherited source-text check.

R03 SODECOTON. Publication date unrecorded; inherited source-text check.

S10 Fashion for Good and Reverse Resources. 2024-06.

S28 TraceWeave. 2026-07-27.

S26 University of Groningen. 2026-04-22.

S17 UNCTAD (UN Trade and Development). 2019-07-17.

R08 Business in Cameroon. Publication date unrecorded; inherited source-text check.

R09 Ecofin Agency. Publication date unrecorded; inherited source-text check.

R12 Business in Cameroon. Publication date unrecorded; inherited source-text check.

S25 Closed Loop Fashion and UNIDO SwitchMed. 2022.

R02 Fibre2Fashion; Business in Cameroon. Publication date unrecorded; inherited source-text check.

S29 Pan African Climate Justice Alliance (PACJA). 2025-03-30.

R32 Wise; XE. Publication date unrecorded; inherited source-text check.

R07 Ecofin Agency. Publication date unrecorded; inherited source-text check.

S40 International Organization for Standardization (ISO). 2024-05.

Keep the thread · chapter 06 of 14

Chapter 07 picks up the thread.

Move the shuttle along the rack to preview any chapter: its sections, exhibits and reading time. Draft web edition. This research is not investment, legal or tax advice; illustrative models are not measured factory results.

The paper's rack · 14 boltsBolt length: reading time

07Part II: Engineering the Recycling Routes

Elastane contamination and polycotton blends require design discipline before chemical fractionation

Separating polyester-cotton and elastane blends chemically demands selective solvents, careful energy and residue control, and proven outlets, so mono-material cotton design is the first recycling investment.

  • 7.1Synthetic fibres dominate global output, but blend architecture determines the recycling problem
  • 7.2Polycotton fractionation must preserve a usable fraction, not merely split a fabric
  • 7.3Fraction purity, cellulose damage and process scale defeat a simple recovery percentage
  • 7.4Two percent elastane creates a process problem far beyond its mass share
Reading time
23 min
Exhibits
4
Sections
7
Continue to chapter 07
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