Process for producing high purity isoflavones
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example 2
Primary Chromatography
[0020] This experiment was the similar to that described in Example 1 with the following exceptions:
[0021] 1. Feed material was pH adjusted to 8.6.
[0022] 2. Feed volume was 20 bed volumes.
[0023] 3. Ethanol solution was of 70% concentration.
[0024] The results from this operation appear below:
2 Isoflavones Dry Solids Purity Yield SAMPLE (mg / Kg) (g / Kg) (%) (%) FEED 544.9 47.1 1.2 PRODUCT 857.4 1.4 63.0 78.7
example 3
Primary Chromatography
[0025] This experiment was the similar to that described in Example 2 with the following exceptions:
[0026] 1. Feed material was pH adjusted to 9.0.
[0027] 2. Resin used was ROHM & HAAS XAD4.
[0028] The effluent streams from this operation appear below:
3 Isoflavones Dry Solids Purity Yield SAMPLE (mg / Kg) (g / Kg) (%) (%) FEED 1773.7 203.7 0.9 PRODUCT 5476.7 10.8 50.9 77.2
example 4
Secondary Chromatography
[0029] Experiments were carried out in a jacketed glass column containing 100 mls of non-ionic adsorbent resin (in this case TULSION ADS 600). The temperature of the column is maintained at 60-65.degree. C. by circulating hot water through the jacket of the column. The resins were conditioned by running 3 bed volumes (300 mls) of a solution of 2.5% NaOH through the resin. The resins were then rinsed with 3 bed volumes of deionized water. The flow rate for all steps in this test was 12 mls / min. Ethanol from the product made by the primary chromatography was used as the starting feed in these tests. This feed was diluted with water and the pH was adjusted to 9.3. One liter of this feed material was then passed through the resin bed. Then 3 bed volumes of deionized water was passed through the column. After the rinse, 5 bed volumes (500 mls) of a solution of 35% ethanol was passed through the resin. The effluent was sampled and collected as PROD. FRAC1. Then 5 b...
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