Skip to content
Heavy Metal Index

Keratin hydrolysate as a chrome exhaust aid and keratin filler in

Source

This source page is a mechanical bulk-ingest record for a PDF in the research-pulls corpus.

Page snapshot
Cited by6 pages
Metals measured2
Evidence tierB
Year2024

Overview

This source page is a mechanical bulk-ingest record for a PDF in the research-pulls corpus. It preserves source-level identity, routeable product/analyte scope, and exact extracted numeric lines for later human or fresh-context audit. It does not derive HMTc thresholds, percentiles, or brand-by-brand comparisons.

Key numbers

The worker extracted the full PDF text with layout preservation twice and compared extraction hashes before commit. The following lines are copied from numeric/table-bearing regions of the PDF and retain the source units and wording where legible:

  • replace the commercial protein filler (Celatan F: 50, 75, and 100 %) with KH solution, with
  • concurrent processing of control leather using conventional chrome tanning agent at 6 % dosage
  • mechanical strength, organoleptic properties and thermal stability were obtained with 100 %
  • substitution of Celatan F at pH 6 and 10 % chromium dosage. It was also discovered that the
  • (aldehydes, vegetable tannins, and resins) (8) to fill the interfibrillar void space created due to the removal of unwanted protein
  • limited exhaustion rate that does not surpass 50–70 %, making chromium the major constituent of tannery effluent (11). Discharge
  • hydrolysis (19). The extracted keratin has been used for a wide range of applications, such as for fertilizer industries (27); for
  • oratory chemicals and reagents used for analysis are of analytical grade and includes sodium hydroxide (NaOH), 99.0 %; hydrochloric
  • acid (HCl), 37 % w/w; sulfuric acid (H2SO4), 98 %; nitric acid (HNO3), 65 %; perchloric acid, 70 %; sodium chloride (NaCl), 99.5 %;
  • boric acid, 99.5 %; and basic chrome sulfate (33 % basicity). All the laboratory chemicals and reagents including process chemicals for
  • solution was subsequently adjusted to the necessary pH of 4.2 using a 2 M HCl (37 %) solution. The precipitated KH solution was then
  • centrifuged at 10,000 rpm for 5 min to produce keratin powder. Table 1 shows the experimental variables considered and protein yield
  • %Ash = × 100 (1)
  • minimum values of COD (mg O2/L), TDS (g/L), and % Cr2O3 (g/L). The stainless-steel pilot reactor employed for the extraction
  • 3.2 before the application of keratin hydrolysate according to the methods in Tables 2 and 3. The tanning process was applied to both
  • the experimental and control samples, using 6 % basic chromium sulfate (33 % basicity). The percentage of the chromium’s primary
  • same proportion (20 %) of pH-adjusted KH extract solutions was applied one at a time. The temperature, drum revolution per minute in
  • ranges of 20–35 ◦ C, 6–8, 40–100 %, and 6 %, respectively. The seventy-five pieces of fresh sheep skin purchased from the Addis Ababa
  • Run No. Actual factors Absorbance at 540 nm Protein concentration (mg/mL) % protein yield
  • Based on the weight of fleshed pelt, a constant KH dose of 20 % in solution or 1.43 % in powder form based on the KH solution solid
  • matter of 0.0721 g/mL was utilized. For both the experimental and control processes, the same amount of chromium was used (6 %
  • which should be closer to the dose of commercially available chemicals for chrome exhaustion (1.5 % of MgO) (48). Therefore, 30
  • solution and 2.5 %, 2.2 %, 1.8 %, 1.08 %, 0.7 %, and 0.4 % in powder form, respectively based on the solid matter (0.0721 g/mL) of the
  • %Cr2 O3 = (2)
  • process based on the designed methods, as shown in Table 4A number of retanning processes were conducted at different pH values of
  • 5, 6, 7, and 8, substituting the commercial protein filler (Celatan F) with the produced keratin filler (50 %, 75 % and 100 %). This
  • ammonium was then treated with an alkaline solution (50 % sodium hydroxide) to convert it to ammonia, and the mixture was distilled
  • extraction time (3.5 h), and protein yield (88.6 %) were attained. The treated samples were taken in triplicate to determine the ash
  • content, and the results are depicted in Table 5. As the table shows, the average ash content from the analysis data was 12.73 % of the
  • sample weight, which is in consistent with the value reported by Ref. (27), slightly higher than the one reported by Ref. (18), 10 % and
  • falls in the range of 30–40 % w/w” (18). This indicates that the experimental extract has relatively less hazardous inorganic oxides and
  • stretching motions of the amide functional group and absorbed water account for the relatively broad peak in the range of 3250–3300
  • The effects of five pH values of KH solution (4.5, 5, 6, 7, and 8), the percentage of the applied KH solution (5 %, 10 %, 15 %, 20 %,
  • 25 %, 30 %, and 35 %), and the points of application (before or after tanning) were considered in the optimization study. Several runs
  • with KH solution at different pH values ranging from 4.5 to 8 and percentage dosages ranging from 5 % (0.4 % in powder form based on
  • when the KH solution was applied at pH (5) than at pH (4.5) as depicted in Table 6, which is due to precipitation of KH at pH (4.5) that
  • value of pH 5 and pH 6, as shown in Table 6. On the other hand, it was demonstrated in Table 9 that chromic oxide in the spent liquor
  • Trial No. 1 2 3 Mean ± SD
  • Effects of varying pH and points of application on the %Cr2O3 content of wet blue leather.
  • pH Dosage of KH solution (%) Points of application % Cr2O3 in the wet blue leather (Mean ±SD)
  • (6). Furthermore, there was an improvement in the leather mechanical strength and organoleptic properties. Table 6 demonstrate that
  • TDS and Cr2O3 analysis results for tanning spent liquors at a 20 % KH dosage.

Methods (brief)

  • provided 6 kg of sheep hair waste for extraction purpose. The composite method of sampling was used to obtain samples of sheep hair
  • Science and Technology University (ASTU) and Addis Ababa Science and Technology University (AASTU).
  • paint unhairing, the raw sheep hair sample was washed many times with enough warm water. The sample of washed sheep hair was
  • bicarbonate (1 g/L), ammonia (1 g/L), and an anionic degreasing agent (1 g/L). The treated hair sample was subsequently cut into
  • carry out the experiment. 20 g of the samples were soaked in 0.25 L of 0.4 N, 0.70 N, or 1 N NaOH solutions for 1.5, 2.5, or 3.5 h, at 65,
  • 80, and 95 ◦ C, respectively. The samples and solution of the hydrolyzing agent were placed in conical flasks, which were subsequently
  • prepare for dialysis, the KH solution was concentrated once more in a water bath. The samples were then subjected to membrane
  • The total ash content of the keratin powder sample was determined according to the Society of Leather Technologists and Chemists,
  • SLC6 (IUC 7; BS 1309:6) (46,47). 5 g of the KH sample were weighed and placed in a pre-weighed, clean, and dry crucible dish. It was
  • preheated to 750 ◦ C and heated at that temperature for 3 h. The total ash content of the hair samples was calculated using Equation (1).
  • weight of hair sample
  • for the pilot-scale extraction; however, the amount and concentration of the solution, including the sample of sheep hair, were scaled
  • process, the raw sheep hair used, the extracted product KH at pilot scale and sample 25 mL kH solution were as shown in Fig. 1a,b, 1c
  • the experimental and control samples, using 6 % basic chromium sulfate (33 % basicity). The percentage of the chromium’s primary
  • spent liquors from both the control and experimental operations were collected.
  • After aging for at least 48 h, wet blue samples were taken from both the experimental and control process drums for the shrinkage
  • Finally, chrome liquors from the control and experimental processes drums were collected for chromic oxide, COD, and TDS analysis.
  • sheepskin samples were employed for these experiments, considering various concentrations of 35, 30, 25, 15, 10, and 5 % KH in

Implications

This page makes the source discoverable for category-level evidence routing. Values remain source-native and should be used only with the stated matrix, species, basis, geography, and censoring context from the paper. The page does not convert total mercury to methylmercury or use total arsenic as inorganic arsenic.

Wiki pages this source may touch

Verification notes

  • Identity check: DOI, raw handle, candidate cite-key, and SHA-256 were compared against existing wiki/sources/ pages before creation.
  • Full-PDF read: pdftotext -layout was run on the full PDF twice; extracted text hashes matched before the page was written.
  • Numeric verification: numeric/table-bearing lines were selected mechanically from the verified extraction and preserved without unit conversion or rounding.
  • Brand firewall: the worker skips PDFs when extracted numeric lines appear brand/manufacturer-sensitive; this page contains category-level or species-level evidence only.
  • HMTc firewall: no threshold, percentile, pass/fail, clean/dirty, or certification math is stated.

Update history

The five most recent substantive edits to this page, classified major (evidence or structure moved), correction (a published value or statement was wrong and has been fixed), or minor (narrative rewritten without changing the underlying evidence). Each description is derived from what the edit did to this page; the linked commit is the authoritative record, routine regeneration passes are excluded, and 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.

CommitDateChangeDescription
b01ec52c2026-08-04major2 sections added
d49e450f2026-08-03major5 sections added; narrative text revised