This paper deals with a procedure of purification of three classes of immunoglobulinfrom porcine serum and sows colostrum. The procedure was summarized as follows(Charts 1 to 3).I. For the purification of immunoglobulins IgG and IgM, pooled porcine serumwas treated with (NH4)2804 to a concentration of ? saturation. Then precipitation wascarried out with a DEAF, -cellulose column (anion-exchange chromatography). The step-wise elution entailed tlte use of seven buffers: (J) 0.01 M NaH:P0+ adjusted to pH 7.6with 0.01 M NaOII, (2) 0.02 M NaH.P0. adjusted to pH 6.3 with 0.02 M Na0H, (3) 0.05 MN1H204, (4) 0.1 M N3lH2PO4, (5) 0.15 M NlH2P04, (6) 0.3 M NlH2P04, and (7) 0.4 MNaH, .P0+. IgG was seen in an elution obtained with buffers (l) and (2). This IgG waspurified by chromatography on CM-cellulose (cation-exchange chromatography) and getfiltration on Sephadex G-200. IgM could be obtained with buffers (4) to (6). The proteincontaining IgM was also fractionated by repetition at get filtration three times onSpehadex G-200 using 0.2 M Tris-HCI and 0.15 M Nail buffer (pH 8.1) for purification, From 100 ml of pooled porcine serum, about 675 rug of IgG was collected, and IgMwas estimated to be 117 mg.2. Colostrum was collected from sows for the purification of IgA. Fat was removedfrom the colostrum, which was then subjected to decaseination and delipoproteinization.The whey was fractionated with Sephadex G-200 against 0.2 M Tris-HCI saline buffer(pH 8.1) which had been used for elution. The resultant fraction was then applied to acolumn of DEAF, -cellulose by stepwise elution. The protein that was assumed to be IgAwas eluted with 0.125 M and 0.15 M Tris-HCI buffer (pH 7.4). This crude IgA was fractionated by repetition of get filtration three times on Sephadex G-200 with Tris-HCIsaline buffer (pH 8.1).From TOO ml of colostrum, about 192 mg of IgA was finally collected.3. Antisera were prepared by injection of rabbits with the three classes of immuno-globulin in Freunds complete adjuvant. Alpha- or beta-globulin was seen in ant In recent years, some trials for separating the plasma protein components have beenput in practice by the author33=3) to explain the behavior of transaminases in fowl bloodplasma and their physicochemical properties. As a result, it was pointed out that several components obtained by subfractionationof albumin37) and beta-globulins36) were regarded satisfactorily as carriers of reverse (R)-aspartate aminotransferase (GOT), R-alanine aminotransferase (GPT), and reversibleGPT. Several physicochemical determinations laave already been performed to clarifythe properties of these components36?37).On the contrary, it is known that the fairly effective purification of ant active material?on1y for forward (F)-GOT substrate was accomplished as fraction IV-73?35). Moreover, aprotein component with an active fragment of F-GOT has frequently been found in acertain globulin group3?35). Notwithstanding, that fraction has not yet been subjectedto a highly effective purification, because the problem of how to separate and purify itremains unsettled. In order to obtain a basic solution for this problem, it is necessary to?devise a method for systematic separation of blood plasma globulins.The present report deals with a method developed and introduced into practical, application by the author.The results of experiments with this method are summarized as follows.I. On the basis of the relations among several quantities listed in some tables, acomponent distinguishable by disc electrophoresis that had migrated to position 5-b wasobtained by subfractionation from the original fraction, IV-4, as fraction IV-4(d). It wasfound to be F-GOT. Moreover, one of the R-GPT samples existed among the conjugatedprotein components with the relative position, 6-a to b. This conjugated component wasobtained from the original fraction, IV-l, as fraction IV-1(f).2. [the rest omitted]
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