Fiber Removal
Starch sizing liquor applied to flax warp yarns during preparatory sizing before weaving creates a protective film that must be extracted completely during finishing. The desizing washability index quantifies the rate at which residual amylose and polyvinyl alcohol detach from woven linen fabric during aqueous scouring ranges in Chinese textile mills. Mill technicians measure this performance metric by comparing residual iodine stain intensities on conditioned grey goods against rinsed cloth after a standardized hot water treatment.
Quantitative spectrophotometric analysis records the optical density of extracted carbohydrate residues suspended in bath liquor. Strict quality control protocols demand complete removal of sizing agents before alkaline boiling stages to prevent uneven dyeing defects in export shipments. Finishing supervisors consult internal laboratory worksheets to verify that washing efficiency meets export grade specifications for fine handkerchief linens and heavy canvas materials alike.
Scour Efficiency
Aqueous extraction kinetics depend heavily on bath temperature and mechanical agitation within commercial washing compartments. Water temperature maintained near ninety degrees Celsius swells residual starch molecules rapidly and lowers solution viscosity for faster diffusion through dense flax yarn intersections. Surfactant concentrations added to the rinse bath reduce interfacial tension between hydrophobic natural pectin layers and hydrophilic sizing fragments.
Residual sizing mass fractions exceeding baseline tolerances indicate inadequate dwell time in the washing trough or insufficient hydrodynamic shear across squeeze rollers. Chemical oxygen demand levels measured in wastewater effluent confirm the total quantity of removed size reaching the treatment plant.
Liquor Dynamics
Countercurrent washing layouts optimize thermal energy transfer while maximizing concentration gradients between fabric capillaries and surrounding wash water. Fresh water enters at the final rinsing station and flows opposite to the movement of the woven linen web through successive tanks. Solute transfer rates accelerate when fresh solvent continuously replaces saturated liquor in direct contact with the textile substrate.
Hydraulic pressure differentials across nip rollers force dissolved impurities out of yarn interstices before the cloth enters the next treatment zone. Process engineers adjust countercurrent flow rates continuously to maintain high extraction efficiency without consuming excessive water resources. Final laboratory audit reports archive these operational parameters alongside fabric tensile strength data to guarantee lot conformity.