Supercritical carbondioxide is very effective in removing oils from a variety of seed matrices, devoid of any appreciable amount of phospholipid content. However, the limited solubility of phosphalipids in supercritical carbondioxide leaves behind a potentially valuable by-product in spent seed matrix. Any phospholipid extraction process from the spent matrix must maintain the structure and the quality of phospholipids and must be compatible with the end use of the seed protein meal an animal feed or for human consumption. An initial supercritical carbondioxide extraction of soybean flakes was performed at 32 MPa and 80℃ to extract the oils, leaving the phospholipids in the deflatted soybean flakes, A second step was performed on the defatted soybean flake using Xeth=0.10, Varying the pressure from 175 MPa to 70.6 MPa and temperature from 60℃ to 80℃. For all supercritical carbon dioxide/ethanol mixture extractions, a fraction rich in phospholipids was obtained. The fractions extracted from defatted soybean flakes were dried and them redissolved in chloroform before HPLC-ELSD analysis. Quantitative and qualitative analysis of phospholipids on soybean seeds, defatted soybean flake, and different extracted phospholipid fractions was carried out, to ascertain the effect of extraction pressure and temperature.

본 연구는 nPr-BTP/nitrobenzene 추출 계에 의한 악티나이드(III)의 선택적 분리로, 우선 자연친화적 CHN 형 의 nPr-BTP (2.6-Bis-(5.6-n-propyl-1.2.4-triazin-3-yl)-pyridine)를 합성하고, 이의 희석제에 대한 용해성 및 질산에 대한 안정성 등을 평가하였다. 악티나이드(III)의 대표원소로는 Am을 선정하였으며, 0.1M nPr-BTP/nitrobenzene-1M , O/A=2의 조건에서 Am은 약 85%, RE 원소는 Eu가 8%, 기타 Nd, Ce, Y 등은 3% 이하가 추출되어 (이때 Am/Eu의 상호분리 계수 약 60정도) 악티나이드(III)의 선택적 추출에는 별 문제가 없을 것으로 판단되었다. 그러나 Am의 역추출의 경우 0.05M 질산용액으로 O/A=1 에서 약43%가 역추출 되었으며, O/A=0.3에서도 65% 정도만이 역추출 되어 질산 이외의 다른 역추출제의 개발이 요구되고 있다.