| Literature DB >> 30445775 |
Sandeep Chavan1,2, Sonali Tayade3,4, Vidya Gupta5, Vineeta Deshmukh6, Sadanand Sardeshmukh7,8.
Abstract
Natural resources such as plants, animals and minerals have always been used by mankind to develop drugs and marine world is no exception. Marine by-products like conches, pearls, mother of pearl shells, corals and so forth have been used by traditional Ayurvedic practitioners for centuries. The unique methods of these preparations are scientifically designed to eliminate unwanted impurities and convert them into bioavailable form. In this study, Conch (Xanchus pyrum) was used as a marine resource of calcium carbonate and was converted pharmaceutically from its aragonite form to calcite. All the steps of preparations and changes in the properties therein were documented and validated. Further, traditional as well as modern analytical tools were used to study its physical and chemical characters to develop a monograph. The physical characterization included particle size, X-ray diffraction (XRD), Scanning Electron Microscopy (SEM), Thermogravimetric Analysis (TGA) and Fourier Transform Infra-red (FTIR). Metal composition and heavy metal limits were determined using Inductively Coupled Plasma Optical Emission Spectrometry (ICPOES). This study revealed the rearrangement of aragonite crystals into calcite form by grinding, trituration with aloe vera juice and incineration under controlled conditions. Moreover, the finished product was found to be devoid of organic matrix that is nacre. This study creates a foundation for the development of a master formula for commonly used Shankha Bhasma in Ayurvedic medicines.Entities:
Keywords: Shankha Bhasma; aragonite; calcite; calcium carbonate; calcium group (Sudha varga) drugs; conch; incineration; pharmaceutical standardization; physico-chemical properties
Mesh:
Substances:
Year: 2018 PMID: 30445775 PMCID: PMC6266202 DOI: 10.3390/md16110450
Source DB: PubMed Journal: Mar Drugs ISSN: 1660-3397 Impact factor: 5.118
Figure 1(a) Graphical representation of temperature recorded every 1 h during the 1st incineration of Conch. (b) Graphical representation of temperature recorded every 1 h during the 2nd incineration of Conch.
Phases of temperature range during each incineration of conch in three batches.
| Phase | Batch 1 | Batch 2 | Batch 3 | |||
|---|---|---|---|---|---|---|
| D (H:Min) | D (H:Min) | D (H:Min) | ||||
| Incineration 1 | ||||||
| I | 4:40 | 36–782 | 4:10 | 33–818 | 4:00 | 35–813 |
| II | 1:10 | 783–959–794 | 1:20 | 819–978–857 | 1:50 | 814–922–789 |
| III | 16:10 | 793–41 | 16:30 | 856–45 | 16:10 | 788–41 |
| Incineration 2 | ||||||
| I | 2:40 | 34–756 | 2:40 | 36–746 | 2:40 | 34–755 |
| II | 0:50 | 757–915–789 | 0:50 | 747–892–766 | 0:50 | 756–901–752 |
| III | 15:30 | 788–41 | 15:30 | 765–42 | 15:30 | 751–40 |
Percentage of yield and loss of incinerated conch through various stages in all the three batches.
| Steps | Batch 1 | Batch 2 | Batch 3 | |||
|---|---|---|---|---|---|---|
| % Yield | % Loss | % Yield | % Loss | % Yield | % Loss | |
| Raw conch–Purified conch | 99.37 | 0.63 | 99.50 | 0.50 | 99.25 | 0.75 |
| Purified–1st incineration | 94.52 | 5.48 | 96.11 | 3.89 | 95.47 | 4.53 |
| 1st incineration–2nd incineration | 96.48 | 3.52 | 97.39 | 2.61 | 97.10 | 2.90 |
| 2nd incineration–Finished product | 99.32 | 0.68 | 99.33 | 0.67 | 99.46 | 0.54 |
| Raw–Finished | 90.00 | 10.00 | 93.13 | 6.87 | 92.00 | 8.00 |
%: Percentage calculated on the basis of weight records.
Yield of incinerated conch through various stages.
| Stage | Time | Batch 1 | Batch 2 | Batch 3 | |||
|---|---|---|---|---|---|---|---|
| Weight (Kg) | Weight for Next Step (Kg) | Weight (Kg) | Wt. for Next Step (Kg) | Weight (Kg) | Weight for Next Step (Kg) | ||
|
| Before | 7.925 | 7.935 | 7.920 | |||
| After | 7.920 | 7.910 | 7.910 | 7.900 | 7.900 | 7.890 | |
|
| Before | 7.490 | 7.640 | 7.590 | |||
| After | 7.485 | 7.475 | 7.620 | 7.610 | 7.570 | 7.560 | |
|
| Before | 7.910 | 7.900 | 7.890 | |||
| After | 7.930 | 7.920 | 7.920 | 7.910 | 7.920 | 7.910 | |
|
| Before | 7.475 | 7.610 | 7.560 | |||
| After | 7.490 | 7.480 | 7.640 | 7.630 | 7.595 | 7.585 | |
|
| Before | 7.930 | 7.910 | 7.910 | |||
| After | 7.515 | 7.490 | 7.650 | 7.640 | 7.580 | 7.570 | |
|
| Before | 7.480 | 7.630 | 7.585 | |||
| After | 7.250 | 7.200 | 7.450 | 7.400 | 7.360 | 7.320 | |
Figure 2XRD pattern of incinerated conch simulated with Aragonite, Calcite and calcium oxide.
Figure 3Scanning Electron Microscopy of raw and incinerated conch at magnification 1000× (Scale: 30 µm) (a) Powdered raw conch; (b) Incinerated conch-Batch 1; (c) Incinerated conch-Batch 2; (d) Incinerated conch-Batch 3.
Figure 4Particle size distribution of finished product - incinerated conch (Shankha Bhasma).
Figure 5Graphical presentation of Thermogravimetric analysis of raw and incinerated conch showing percent weight loss against temperature (°C): (a) Raw conch; (b) Incinerated conch-Batch 1; (c) Incinerated conch-Batch 2; (d) Incinerated conch-Batch 2.
Stage-wise loss of moisture, organic matrix and carbon dioxide in TGA.
| Sr. No. | Material | Moisture % (100 °C) | Organic Matrix % (450 °C) | Carbon Dioxide % (upto 850 °C) |
|---|---|---|---|---|
| 1 | Raw conch | 1.179 | 0.1466 | 42.71 |
| 2 | Incinerated conch-Batch 1 | 0.4482 | 0.03564 | 43.20 |
| 3 | Incinerated conch-Batch 2 | 0.3040 | 0.02763 | 43.28 |
| 4 | Incinerated conch-Batch 3 | 0.1647 | 0.02542 | 43.23 |
Figure 6Fourier Transform Infrared Analysis of incinerated conch showing CO32− vibrations: (a) Incinerated conch-Batch 1; (b) Incinerated conch-Batch 2; (c) Incinerated conch-Batch 3.
Details of ICPOES analysis of raw and incinerated conch (Batch 1, 2 and 3).
| Steps | Ca | Mg | Hg | As | Cd | Pb | ||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
|
| ||||||||||||
| Weight (g) | 0.109 | 0.101 | 0.109 | 0.101 | 0.101 | 0.104 | 0.101 | 0.104 | 0.101 | 0.104 | 0.101 | 0.104 |
| Reading | 4.772 | 3.988 | 0.038 | 0.046 | −61.73 | −64.55 | −2.013 | −0.155 | −1.636 | −1.316 | 13.145 | 14.46 |
| Result | 43.42 | 39.49 | 0.017 | 0.023 | ND | ND | ND | ND | ND | ND | 6.47 | 6.91 |
| Mean | 41.45 | 0.020 | ND | ND | ND | 6.69 | ||||||
|
| ||||||||||||
| Weight (g) | 0.101 | 0.101 | 0.101 | 0.101 | 0.101 | 0.100 | 0.101 | 0.100 | 0.101 | 0.100 | 0.101 | 0.100 |
| Reading | 4.043 | 3.936 | 0.080 | 0.083 | −67.86 | −82.26 | 3.72 | 2.795 | −1.582 | −1.592 | 3.835 | 3.119 |
| Result | 39.72 | 38.74 | 0.039 | 0.041 | ND | ND | 1.84 | 1.39 | ND | ND | 1.90 | 1.55 |
| Mean | 39.23 | 0.040 | ND | 1.61 | ND | 1.72 | ||||||
|
| ||||||||||||
| Weight (g) | 0.105 | 0.100 | 0.105 | 0.100 | 0.102 | 0.101 | 0.102 | 0.101 | 0.102 | 0.101 | 0.102 | 0.101 |
| Reading | 4.211 | 4.100 | 0.075 | 0.064 | −4.017 | −3.836 | −1.062 | −4.162 | −2.081 | −1.9 | −6.568 | −8.171 |
| Result | 39.99 | 40.80 | 0.036 | 0.032 | ND | ND | ND | ND | ND | ND | ND | ND |
| Mean | 40.39 | 0.034 | ND | ND | ND | ND | ||||||
|
| ||||||||||||
| Weight (g) | 0.102 | 0.106 | 0.102 | 0.106 | 0.103 | 0.105 | 0.103 | 0.105 | 0.103 | 0.105 | 0.103 | 0.105 |
| Reading | 4.052 | 4.221 | 0.065 | 0.071 | −1.095 | −75.92 | −5.151 | −5.838 | −1.791 | −1.632 | −9.405 | −9.405 |
| Result | 39.69 | 39.82 | 0.032 | 0.033 | ND | ND | ND | ND | ND | ND | ND | ND |
| Mean | 39.75 | 0.033 | ND | ND | ND | ND | ||||||
ND = Not detected, Results for Ca, Mg are in % and Hg, As, Cd, Pb are in ppm
Parameters and specifications for manufacturing process of incinerated conch (Shankha Bhasma).
| Parameters | Specification | Units |
|---|---|---|
| Batch quantity | 8 | Kg |
| Quantity of fresh lemon juice (of 400 lemons) | 7 | L |
| Quantity of diluted lemon juice | 32.5 | L |
| pH of fresh juice | 2–2.5 | - |
| pH of diluted juice | 3–3.5 | - |
| Duration for purification | 3 | Hr. |
| Total quantity of aloe vera juice (of 200 mature leaves) | 7 | Kg |
| Quantity of aloe vera juice for incineration 1 | 1.8–2 | Kg |
| Quantity of aloe vera juice for incineration 2 | 5 | Kg |
| Viscosity of aloe vera juice | 2–4 | mP |
| Cow-dung cakes for incineration 1 | 28 | Kg |
| Cow-dung cakes for incineration 2 | 22.5 | Kg |
| Total Duration for incineration 1 | 22 | Hr. |
| Total Duration for incineration 2 | 19 | Hr. |
| Maximum External Temperature during incineration 1 | 900–1000 | °C |
| Maximum External Temperature during incineration 2 | 870–935 | °C |
| Yield of Raw material to Finished Product | 90–94 | % |
Parameters and specifications of incinerated conch (Shankha Bhasma).
| Parameters | Specification |
|---|---|
| Organoleptic characters | White or greyish white colour, no smell and should not taste pungent |
| Fineness | Fine like Kohl, enters the crevices of finger tips when rubbed between them. |
| Smoke test | No smoke when burnt on open flame |
| Loss on drying | Not More Than 0.5% |
| Calcium as CaCO3 (Titration) | 38–40% |
| Ca on ICPOES | 39–41% |
| Mg on ICPOES | 0.03–0.04% |
| pH of 1% solution in Distilled Water | 9–10 |
| Bulk density | 0.7000–0.8500 g/cc |
| Tapped density | 1.100–1.500 g/cc |
| XRD analysis | 100% Calcite form |
| TGA analysis | 42–44% loss after 750 °C |
| FTIR analysis | CO32− peaks at 1410, 874, 712 cm−1 |
| SEM analysis | Polygonal particles or agglomerates |
| Particle size | Effective diameter: 400–750 nm |
| Heavy metals on ICPOES | Hg, As, Cd and Pb- Within permissible limits |
Details of the purification process of conches.
| Parameters | Unit | Batch 1 | Batch 2 | Batch 3 |
|---|---|---|---|---|
| Raw conch | Kg | 8 | 8 | 8 |
| Time required for washing | H | 1.5 | 1.5 | 1.5 |
| Fresh lemon juice | L | 7.22 | 7.22 | 7.22 |
| Water added for dilution | L | 25.27 | 25.27 | 25.27 |
| Lemon juice diluted | L | 32.5 | 32.5 | 32.5 |
| Quantity required for boiling | L | 32 | 32 | 32 |
| Lemon juice residue after boiling | L | 26.5 | 27.3 | 27.9 |
| Temperature maintained | °C | 98–100 | 99–100 | 98–100 |
| Weight after purification | Kg | 7.950 | 7.960 | 7.940 |
Figure 7Schematic presentation of incineration of conch and probable role of each step involved.
Figure 8Top view showing placement of pots during incineration and Side view showing position of pyrometers along with distribution pattern of cow-dung cakes placed.
Quantitative details of the incineration process of conches.
| Parameters | Unit | Batch 1 | Batch 2 | Batch 3 |
|---|---|---|---|---|
| Pots used for each batch | No | 04 | 04 | 04 |
| Batch quantity | Kg | 7.950 | 7.960 | 7.940 |
| Purified conch in each pot | Kg | 02 | 02 | 02 |
| Aloe vera juice in each pot for 1st incineration | Kg | 02 | 02 | 02 |
| Total Aloe vera juice used for 1st incineration | Kg | 08 | 08 | 08 |
| Aloe vera juice used for trituration for 2nd incineration | Kg | 5 | 5 | 5 |
| Triturated conch in each pot for 2nd incineration | Kg | 1.875 | 1.910 | 1.900 |
| Cow-dung cakes used for 1st incineration | Kg | 28 | 28 | 28 |
| Cow-dung cakes used for 2nd incineration | Kg | 22.5 | 22.5 | 22.5 |