TW200521136A - Method of purification for a lectin of marine microalgae - Google Patents

Method of purification for a lectin of marine microalgae Download PDF

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TW200521136A
TW200521136A TW92137344A TW92137344A TW200521136A TW 200521136 A TW200521136 A TW 200521136A TW 92137344 A TW92137344 A TW 92137344A TW 92137344 A TW92137344 A TW 92137344A TW 200521136 A TW200521136 A TW 200521136A
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protein
purifying
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TW92137344A
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Liang-Ping Lin
Wan-Ju Liao
Shi-Li Chen
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Liang-Ping Lin
Wan-Ju Liao
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Abstract

A method of purification for a lectin of marine microalgae that separates and purifies the agglutinins from Chlorella luteovirides with high activity. Firstly, an extract is obtained by a method of cytoclasis, which is glass bead with ultrasonication. Then, the extract is divided by a ammonium sulfate solution with 60-80% saturated concentration, and a protein is precipitated and collected. Next, the precipitable protein is dialyzed by phosphate buffer saline, moreover; a suppressor is collected by centrifugation. Subsequently, the suppressor is added to DEAE-C-52 ion exchange chromatography to separate and purify, and an active protein solution is collected. Following that, the protein solution is separated and purified again by CM-C-52 ion exchange chromatography. Finally, the purification is performed by Superdex 75 gel filtration, and the method of a lectin of marine microalgae is successively accomplished.

Description

200521136 五、發明說明(1) 一、【發明所屬技術領域】 本發明係有關於一種藻類之純化方法,特別是有關於 一種小球藻凝集素之純化方法。 二、【先前技術】 凝集素(a g g 1 u t i n i n s )是指能與紅血球或正常及其他 變形細胞結合造成凝集現象的一種活性物質,凝集素為一 種蛋白質,其中的親醣蛋白(lectin)能和碳水化合物結合 ,凝集素分佈在自然界各種生物中,例如植物、細菌、地 衣、真菌、蚯蚓、蝸牛、鰻、鮪魚、貝類、哺乳動物、昆 蟲。凝集素在海洋生物則有海藻、海參、珊瑚及海綿等, 他們在不同的生物之間結構差異很大,且凝集素的活性會 因生長部位不同而異,目前已分離出之植物凝集素已超過 2 0 0種,主要分佈在種子,而在根部、葉片及其他部位則 有較少量之分佈。 親醣蛋白具有與紅血球及其他細胞表面醣類結構結合 之能力,在雞母珠、靈芝、金針菇、草菇、蓖麻子等各種 生物種類中,可分離純化出具免疫調節功能之蛋白與溶血 毒蛋白,其能凝集人類之紅血球且具有良好的免疫抑制力 ,而在海洋藻類親蛋白的研究中也找到溶血毒蛋白與高凝200521136 V. Description of the invention (1) 1. [Technical field to which the invention belongs] The present invention relates to a method for purifying algae, and more particularly to a method for purifying chlorella lectin. 2. [Prior art] Lectin (agg 1 utinins) refers to an active substance that can bind to red blood cells or normal and other deformed cells to cause agglutination. Lectin is a protein, of which lectin and carbohydrate Compound binding, lectins are distributed in various organisms in nature, such as plants, bacteria, lichens, fungi, earthworms, snails, eels, catfish, shellfish, mammals, insects. Lectin in marine life includes seaweed, sea cucumber, coral and sponge, etc., their structure is very different between different organisms, and the activity of lectin will vary depending on the growth site. At present, the plant lectin has been isolated. More than 200 species are mainly distributed in seeds, but are distributed in smaller amounts in roots, leaves and other parts. Glycoproteins have the ability to combine with red blood cells and other cell surface carbohydrate structures. In various biological species such as chicken bead, Ganoderma lucidum, Flammulina velutipes, ricinus, and castor beans, proteins with immunomodulatory functions and hemolytic proteins can be separated and purified. It can agglutinate human red blood cells and has good immunosuppressive power. In the study of marine algae proteolysis, hemolytic proteins and high coagulation have also been found.

第5頁 200521136 "" '一 '~ --------— 五、發明說明(2) " -- 集價之特殊藻珠。 大部分的凝集素含2 - 5 0%之碳水化合物,有些凝集素 則不含酶類’凝集素可與特定的醣類反應,類似抗體特異 性(a n 11 b 〇 d y s p e c i f i c i t y )的結合性質,因此,一般係利 用此性吳來作為分離或分析親醣蛋白的指標。凝集素具有 免疫性與專一性,且對人類之紅血球細胞的凝集具有選擇 性’亦即可凝集某一種血型之細胞,但對另一種血型之細 胞不凝集’因此,可用來區分不同血型之紅血球。西元 1 986年利司(Lis)及薛倫(Sharon)、西元1 9 9 5年克拉伯 (Go 1 lob)等人指出一些屬於親醣蛋白的凝集素可應用在血 型分類、測定醣蛋白及醣脂肪、刺激脾臟細胞和淋巴有絲 分裂、偵測正常或惡性腫瘤細胞、誘導細胞壁產生分解酵 素、活化訊號傳導途徑及抗腫瘤之功用。西元丨9 9 8年斯巴 弗里(Sparvoli)等人發現青豆(iima —bean)凝集素會凝集a 型血球細胞,不凝集B型或〇型血球細胞。凝集素除S了對紅 血球有凝集作用,對其他細胞亦可發生凝集現象,例如淋 巴球細胞、細菌、真菌、精細胞等等。 西元1 9 9 3年南森(Nathan)等人將目前凝集素種類分為 (一)植物性來源:(A)穀類··其蛋白結合的醣類多為^ 乙醯葡萄胺(N-acetylglucosamine)、乙醯神經氨酸( acety lneuramic acid),而蛋白質由兩個單元體所組成, 每個單元體具有兩個結合位置,含雙硫鍵及不需金屬來與Page 5 200521136 " " '一' ~ ------------ V. Description of Invention (2) " Most lectins contain 2-50% carbohydrates, and some lectins do not contain enzymes. Lectins can react with specific sugars, similar to the binding properties of antibody specific (an 11 b 〇dyspecificity), so Generally, this property is used as an indicator for the isolation or analysis of glycoproteins. Lectins are immune and specific, and are selective for the agglutination of human red blood cells, that is, cells of one blood type, but not agglutinated cells of another blood type. Therefore, it can be used to distinguish red blood cells of different blood types . Lis and Sharon in 1986 AD and Go 1 lob in 1959 AD pointed out that some lectins belonging to glycoproteins can be used in blood group classification, determination of glycoproteins and sugars Fat, stimulation of spleen cells and lymphatic mitosis, detection of normal or malignant tumor cells, induction of cell wall production of degrading enzymes, activation of signal transduction pathways and anti-tumor functions. AD 丨 In 1998, Sparvoli and others found that green bean (iima-bean) lectin would agglutinate type A blood cells, but not type B or 0 blood cells. In addition to S, lectin has an agglutination effect on red blood cells, and agglutination can also occur on other cells, such as lymphocytes, bacteria, fungi, and sperm cells. In 1933, Nathan and others divided the current lectin types into (1) plant sources: (A) cereals. · The protein-bound sugars were mostly ^ N-acetylglucosamine And acety lneuramic acid, and the protein is composed of two units, each unit has two binding sites, contains disulfide bonds and does not require metals to communicate with

200521136 五、發明說明(3) ;(B)豆科:其結合的醣類較不具專一性,由2或4個單 元體所組成,單元體分子量為25-3 0千達(kDa),每一單元 體有一結合位置,沒有雙硫鍵,需正二價I弓離子(Ca 2+)及 正一彳貝纟孟離子(Μ η 2+)參與凝集反應,(二)動物性來源:(a ) C型態(C-type):並沒有專一性的醣類,其單元體構成數 目不一,但每一單元體分子量不大於15千達,每一單元體 具有1 - 8個結合位置,有雙硫鍵及需與正二價飼離子結合 ;(B ) S型態(S -1 y p e ):其結合的膽類為D -半乳糖(d -galactose)’構成單元體數目尚不清楚’每一單元體有一 結合位置,無雙硫鍵及不需金屬離子參與。 藻類凝集素之研究歷史可追溯至西元1 9 6 6年布伊 (Boyd)等人,他們檢測出24種波多黎各海藻的細胞液 (cel 1 sap)能凝集人類的紅血球,換言之,海藻萃取液内 含有凝集素之成分,另外,他們亦發現不同海藻的凝集活 性程度依血型而異,例如S p y r i d i a f i 1 a m e n t 〇 s a只凝集A 型紅血球,但 Codium isthmoclaclum,Turbinaria t urb i nata及 Sargassum natans能凝集 A、0及 B型紅血球, 但檢測時活性太弱,且不耐熱,因而對其應用性與價值產 生了疑問,並未進一步做生化特性之研究。西元1 9 7 0年布 拉登(B1 unde η)及羅覺斯(Rogers)陸續調查英國的海藻, 發現某些種類之海藻具高凝集活性,此時才引起許多學者 的興趣,開啟了研究海藻凝集素之領域。當時,他們利用 艮鹽水製成的紅血球懸浮液(s a 1丨n e s u s p e n s i ο η )來做生200521136 V. Description of the invention (3); (B) Leguminosae: the saccharides they bind are less specific, consisting of 2 or 4 units with a molecular weight of 25-30 kilodaltons (kDa), each A unit body has a binding site, without disulfide bonds, and requires a positive divalent I bow ion (Ca 2+) and a positive monopyridium ion (Μ η 2+) to participate in the agglutination reaction. (II) Animal source: (a ) C-type (C-type): there is no specific carbohydrates, the number of units is different, but the molecular weight of each unit is not more than 15 thousand, each unit has 1-8 binding positions, Has a disulfide bond and needs to be combined with a positive divalent feed ion; (B) S type (S -1 ype): its bound bile is D-galactose (d -galactose) 'The number of constituent units is unknown' Each unit has a binding site, no disulfide bonds and no metal ions. The research history of algae lectins can be traced back to Boyd et al. In 1966 AD. They have detected that the cell fluid (cel 1 sap) of 24 kinds of Puerto Rican algae can aggregate human red blood cells. In other words, the seaweed extract contains Contains lectin components. In addition, they also found that the degree of agglutination activity of different seaweeds varies according to blood type. For example, Spiridiafi 1 ament 〇sa only aggregates type A red blood cells, but Codium isthmoclaclum, Turbinaria t urb i nata, and Sargassum natans can aggregate A. , 0, and B type red blood cells, but the activity is too weak and heat-resistant during testing, so it has doubts about its applicability and value, and no further research on biochemical characteristics has been done. In 1970, B1 unde η and Rogers investigated British algae one after another, and found that some species of algae have high agglutination activity. At this time, many scholars were interested, and research on algae was started. The field of lectins. At that time, they used red blood cell suspensions (s a 1 丨 n e s u s p e n s i ο η) made of gen saline to make a living.

200521136 -------— 五、發明說明(4) ' "" --—- 物檢測,其中,i i 1 . a 紅澡Pt 1 lota plumosa含有抗B型紅血球的 凝ί Ϊ^較為特殊。他們檢測百餘種的海藻,得到的結 論是只=少數的海藻含有凝集素,且凝集活性很低,而同 ’種類澡的不同部位所檢測的凝集活性並沒有明顯的差異 。西,=81年後里(Hori)等人檢測日本沿岸43種海藻,其 、’々果疋/、有1 4種具/旋集大白鼠紅血球的活性,但& 8種對人 類紅血球具活性’其中U1 a r u s a k丨丨對Α型及〇型紅血球較具 親和性’已顯示該藻類具有少見之反(A + H)(anti — (A + H)) 專一性。 由於生物檢測顯示許多藻類萃取液對紅血球溶液之凝 集活性很低或不具活性,為了改善及增加檢測效果,許多 學者除了改變血液來源外,也利用不同酵素處理紅血球以 增強凝集素與紅血球表面結合之能力。在西元1 9 7 7年,羅 覺斯(Rogers)將紅血球除以食鹽水製備外,另設一組加入 清蛋白(albumins)或將紅血球先經木瓜蛋白酵素(papain) 的前處理再檢測海藻萃取液,結果是經後二者處理後,藻 類凝集活性明顯提升。之後,陸續有許多學者使用不同之 酵素,例如胰蛋白(trypsin)及神經氨酸(neuraminidase )等做前處理來檢測活性,結果發現藻類萃取液與經過酵 素處理後之紅血球溶液,相較於未經任何處理之紅血球溶 液,其凝集活性有明顯之提升。由於經酵素處理後,紅血 球細胞表面之部分蛋白被酵素破壞,因此,能被凝集素辨 識之醣基有更多機會裸露於細胞表面並被凝集素辨識及結200521136 --------- V. Description of the invention (4) '" " ---- Physical detection, in which ii 1. A red bath Pt 1 lota plumosa contains anti-type B red blood cell coagulation Ϊ ^^ More special. They tested more than a hundred kinds of seaweeds, and concluded that only a few seaweeds contain lectins, and the agglutination activity is very low, and there is no significant difference in the agglutination activity detected in different parts of the same type of bath. West, = 81 years later (Hori) et al. Detected 43 species of seaweed along the coast of Japan, and their 'capsules /' have 14 kinds of red blood cell activity in spinal mice, but & 8 kinds of human red blood cells have The activity 'where U1 arusak 丨 丨 has more affinity for type A and type 0 red blood cells' has shown that the algae has a rare anti- (A + H) (anti — (A + H)) specificity. As bioassays show that many algae extracts have low or no agglutination activity on red blood cell solutions, in order to improve and increase the detection effect, many scholars have used different enzymes to treat red blood cells in addition to changing the blood source to enhance the binding of lectin to the surface of red blood cells. ability. In 1977, Rogers prepared red blood cells in addition to saline, and set up another set of albumins or red blood cells that had been pretreated with papain before detecting seaweed. As a result of the extraction, the algae agglutination activity was significantly improved after the latter two treatments. Since then, many scholars have used different enzymes, such as trypsin and neuraminidase, to test the activity. As a result, it is found that the algae extract and the red blood cell solution after enzyme treatment are compared with After any treatment, the agglutination activity of the red blood cell solution is significantly improved. After enzyme treatment, some proteins on the surface of red blood cells are destroyed by enzymes. Therefore, the glycosyl groups that can be recognized by lectin have more opportunities to be exposed on the cell surface and be recognized and bound by lectin.

第8頁 200521136Page 8 200521136

五、發明說明(5) 合,凝集活性因而顯著加強 ’夕位學者開始錯者不同醣 類親和的專一性,也發現許 (lectin)的構造。 ,達到改善檢測之效果。自此 類處理來瞭解海藻凝集素的· 多海藻的凝集素為親醣蛋白 由 合產生 的特性 究者即 及分離 物凝集 他們利 鼠’發 成左右 腫瘤復V. Description of the invention (5) The agglutination activity was significantly enhanced, and the scholars began to mistake the specificity of the affinity of different sugars and found the structure of lectin. To achieve the effect of improving detection. From this kind of treatment, we have learned about the characteristics of algae agglutinin. The algae agglutinin is a kind of glycoprotein produced by glycoproteins. Researchers and isolates agglutinate them.

^凝集素會去辨識特定的醣基而與之結合,這種結 夕種生物力月b,因此可用它來探討細胞表面膽分子 細胞膜之化學構造以及細胞生物學作用。咛多研 ::用凝集素這種特殊結合性質,物田胞表面結榻 、、、化斗夕具有重要生物功能的含醣物質。此外,植 素中有y些曾被利用於醫學臨床上做為抗癌研究, 用蓖麻凝集素中的毒蛋白部分處理含有腹瘤的小白 現其腹腔内含腫瘤數在48小時就減少到對照組的一 ,且5個月内發現處理凝集素的小白鼠沒有死亡或 發。 間内即^ ^球澡具有容易培養、繁殖迅速的優點’在短時 物、蛋L ί得大量生質’小球藻除了含有豐富的碳水化合 的一半質及維生素外,其蛋白質含量幾乎佔小球藻細胞 細胞蛋白i(乾重量之40〜60%),是一種極具開發價值的單 水處理、球澡常用來生產健康食品、有機物及重金屬的廢 節酸性髀i保健用途亦相當廣泛,如提昇抗氧化能力、調 -貝、加強免疫功能及改善腸道功能等。小球藻除 SCp)。,處’即英文稱謂"single cell protein,,(簡稱^ Lectins will recognize specific glycosyl groups and bind them. This kind of biological force is b. Therefore, it can be used to explore the chemical structure of cell surface bile molecules and cell membranes and cell biological functions.咛 多 研 :: Using the special binding property of lectin, the surface of the object cells has sugar-containing substances with important biological functions. In addition, some of the phytochemicals have been used in clinical medicine as anti-cancer research. The toxic protein in ricin agglutinin has been used to treat small whites containing abdominal tumors. The number of tumors in the abdominal cavity has been reduced in 48 hours To the one in the control group, and found that the mice treated with lectin did not die or develop within 5 months. In the meantime, ^ ^ ball bath has the advantages of easy cultivation and rapid reproduction. 'In a short period of time, eggs have a lot of biomass.' Chlorella, in addition to rich carbohydrate and half of the quality and vitamins, its protein content almost accounts for Chlorella cell cell protein i (40 ~ 60% of dry weight) is a kind of highly valuable single water treatment and ball bath. It is commonly used to produce health food, organic matter and waste metals. It is also widely used in health care. , Such as improving antioxidant capacity, regulating shellfish, strengthening immune function and improving intestinal function. Chlorella except SCp). , 处 ’is the English title " single cell protein, (referred to as

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了可以做為生物性肥料外, 生素、藻膠、化妝品或藥品 氣體或液體的原料。另外小 及抗腫瘤活性。隨著醣生物 集素的研究。鑑於小球藻具 、生物醫學與生物製藥的新 供一種藻類之純化方法,以 發。 或做為天然色素、脂肪酸、維 之來源,也可做為生產可燁性 球藻萃取液中含有抗菌功能, 學的發展,更多人去注意到凝 有應用於血型鐘定、生物化學 藥開發之用途,因此生Γ需; 利應用於上述之各種研究及開 三、【發明内容】 /本發明之一目的係提供一種微藻親醣蛋白之純化方法 ’係利用陰離子交換層析、陽離子交換層析及膠體過濾層 析法得到一純化之小球藻凝集素,以利於各種生物醫學、 血型鑑定、保健食品及相關之研究與應用。It can be used as a raw material for bio-fertilizers, biotin, algin, cosmetics or pharmaceuticals as a gas or liquid. Also small and antitumor activity. With the study of sugar biotins. In view of the new chlorella, biomedical and biopharmaceutical, a new algae purification method was developed. Or as a source of natural pigments, fatty acids and vitamins, or as a source of antibacterial function in extractable chlorella extracts. As a result of scientific development, more people have noticed that it has been used in blood grouping and biochemical medicine. It can be used for various purposes as described above. It can be applied to the above-mentioned various research and development. [Summary of the Invention] / One of the purposes of the present invention is to provide a method for purifying microalgal glycoproteins. A purified chlorella agglutinin was obtained by exchange chromatography and colloidal filtration chromatography to facilitate various biomedical, blood group identification, health food, and related research and applications.

、 本發明之另一目的係提供一種微藻親醣蛋白之純化方 t ’係利用一具有適當濃度範圍之硫酸銨水溶液沈澱所欲 分析之小球藻凝集素,以開發出進行小球藻凝集素分離純 化之最適條件。 本發明之又一目的係提供一種微藻親醣蛋白之純化方 法’係利用一人類或動物之紅血球細胞進行凝集活性之檢2. Another object of the present invention is to provide a method for purifying microalgae glycoproteins. The method is to use a aqueous ammonium sulfate solution with an appropriate concentration range to precipitate the chlorella agglutinin for analysis to develop chlorella agglutination. Optimum conditions for the separation and purification of vegans. Another object of the present invention is to provide a method for purifying microalgal glycoproteins. The method is to detect the agglutination activity of a human or animal red blood cell.

第10頁 200521136 五、發明說明(7) 測,以作為判斷純化與否之一依據。 根據以上所述之目的,本發明係提供一種微藻親醣蛋 白之純化方法,其係將小球藻藻體細胞執行一萃取之步驟 ,其中係利用石粦酸鹽缓衝液(phosphate buffer saline) 將所欲分離純化之小球藻凝集素萃取出,所得之藻類萃取 液以硫酸銨水溶液(ammo n ium sul fate)進行蛋白質之沈殿 ,並收集0-80 %飽和濃度之硫酸銨水溶液所沈澱之蛋白質 ,以進行小球藻凝集素的分離及純化。將所得到之蛋白質 沈殿置於磷酸鹽緩衝液中進行透析去鹽,離心後取上層之 蛋白質澄清液,以DEAE-C-52(diethyl amin〇 ethyl_ ^ cellulose-52)管柱進行陰離子交換管柱分析,並利用一 濃度梯度之方式(由O.i莫爾濃度至〇.5莫爾濃度)來收集 具有活性之蛋白質’其中係收集自0.2莫爾濃度之氣化鈉、 (NaCU水溶液所沖提出具有活性之蛋白質,接著,經醋酸 鈉綾衝液(Sodlum Acetate Buffer)透析去鹽後,繼續以 CM-C-5 2(carb〇xymethyhcellulose-52)f 交換管柱分析,豆中俜 适4 丁丨两雕于 :二中係以乳化鈉水,谷液,並利用一濃度梯 度之方式(由0·1莫爾濃度至〇·5莫爾濃度)來收集具 性之蛋白質,接著,再利用 dex 技 …、4 瞢知厣挤古、、i八祕w 用P 75 &柱之膠體過濾 吕柱層析方法刀離純化此具有活性之蛋白質, 類或動物之紅 球溱凝集素。而上述之所有步驟係經由一、二、 血球細胞來判斷其凝集活性及純化與否。Page 10 200521136 V. Description of the invention (7) Test, as a basis for judging whether it is purified or not. According to the above-mentioned object, the present invention provides a method for purifying microalgae glycoprotein, which comprises performing an extraction step of chlorella somatic cells, wherein a phosphate buffer saline is used. The desired chlorella lectin is separated and purified, and the obtained algae extract is used for ammonium sulfate aqueous solution (ammo n ium sul fate) to immerse the protein, and the precipitated ammonium sulfate aqueous solution with a concentration of 0-80% is collected. Protein for chlorin lectin isolation and purification. The obtained protein Shen Dian was placed in a phosphate buffer solution for dialysis and desalting. After centrifugation, the upper protein clarified solution was taken, and a DEAE-C-52 (diethyl amin〇ethyl_ ^ cellulose-52) column was used for an anion exchange column. Analysis and use a concentration gradient method (from Oi Moore concentration to 0.5 Moore concentration) to collect the active protein 'which is collected from the 0.2 Moore concentration of sodium vapor, The active protein was then dialyzed through Sodlum Acetate Buffer to remove salts, and then analyzed by CM-C-5 2 (carb〇xymethyhcellulose-52) f exchange column. Carved in: the second middle school uses emulsified sodium water and valley liquid to collect a solid protein by using a concentration gradient method (from 0.1 Moore concentration to 0.5 Moore concentration), and then uses dex technology …, 4 瞢 know 厣, i, 八, 秘, 八, 八, 用, 75, 75, 75, 75, 用, 75, 用, 用, 75, 八, 八 ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, ,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, b, All steps go through one, two, and blood Cells to determine their hemagglutinating activity and purified or not.

200521136200521136

本發明另一方面提供一種微藻 係利用經酵素處理之人類或動物之紅,白之純化方法, 分離出蛋白質之凝集活性,作以在 砰:胞,判斷與所 貝純化與否之-依據,其中此酵素可為胰 :之蛋白 或鏈蛋白(papa i η )。 ypsin) 四、【實施方式】 本發明之微藻親醣蛋白之純化方法中,由於小球藻呈 有堅韌之細胞壁,此細胞壁係由纖維素、半纖維素等所= 成,因此,需利用一種破胞方法將小球藻藻體細胞壁擊破 丄j利於進行凝集素之萃取,其中不同的破胞方法對小球 藻萃取液之凝集活性並不相同。本發明所採用之破胞方法 包含(一)液態氮法(liquid nitrogen):係以液態氮將小 球藻藻體細胞在液態氮溫度下(攝氏零下一百九十六度)研 磨成粉狀;(二)玻璃珠法(g 1 a s s b e a d) ··以1 · 6克玻璃珠 ,其中玻璃珠之大小在1 50-220微米之間,加入〇· 2克之乾 燥澡體’每打一分鐘休息一分鐘,共打2 〇次;(三)超聲波 處理法(ul trasoni cat ion):係使用一細胞研磨機(cel 1 disrupter)在冰浴下將小球藻藻體細胞擊破,其中其破胞 條件係將超音波增強值(u 11 r a s ο n i c i n t e n s i f i e r v a 1 u e ) 設為5 0,而其破胞頻率為每破胞3分鐘休息2分鐘,共破胞 1 0次;(四)組織檮碎法(War i ng-b 1 ender ):係將調數器撥Another aspect of the present invention provides a method for purifying red or white of human or animal treated with enzyme by using microalgae to separate the agglutination activity of protein for judging whether it is purified or not-basis Wherein, the enzyme may be pancreatic protein or chain protein (papa i η). ypsin) 4. [Embodiment] In the method for purifying microalgae glycoprotein of the present invention, since chlorella has a tough cell wall, this cell wall is made of cellulose, hemicellulose, etc., so it needs to be used A method of cell disruption breaks the cell wall of the chlorella alga so as to facilitate the extraction of lectin. Among them, different cell disruption methods have different agglutination activities on the chlorella extract. The cell breaking method used in the present invention includes (1) liquid nitrogen method: the chlorella somatic cells are ground into liquid powder by liquid nitrogen at a temperature of liquid nitrogen (minus 196 degrees Celsius). (2) glass bead method (g 1 assbead) ····························································································································· of-bakes · Dry Bath · 0.2g One minute, hit 20 times in total; (3) Ultrasound treatment (ul trasoni cat ion): using a cell grinder (cel 1 disrupter) in the ice bath to destroy the chlorella algal somatic cells, in which the broken cells The condition is that the ultrasound enhancement value (u 11 ras ο nicintensifierva 1 ue) is set to 50, and the frequency of breaking cells is to rest for 2 minutes every 3 minutes, breaking cells 10 times in total; (4) Tissue fragmentation method (War i ng-b 1 ender): Set the dial

第12頁 200521136Page 12 200521136

至所需速度檔次,每次禱碎時間為5秒,纟⑽秒,4 碎6次五)第一研磨法:係將小球藻蒸體二 胞與氧化鋁(A!2%)以重量比(w/w)1 :3均勻混合之,利用 玻棒在冰浴下研磨10分鐘;(六)第二研磨法:係將小球筑 澡體細胞與海沙以重量比(w/w)1 : 3均勻混合之’利用玻* 棒在冰浴下研磨1〇分鐘;(七)酵素法:係分別將兩種酵 以體積比1 : 1在37 °C下混合兩小時使用,其中此兩酵素係 為生命小體(Macrozyme) R-10與蒸餾水之容積百分比為2 % (w/v)及尿甘酸鹽(giucuronidase)與蒸餾水之體積百分 比為 2% (v/v)。 本發明之微澡親醣蛋白之純化方法中,係利用人類之 A、B、0、AB型血液及動物之血液,例如豬、牛及羊,將 各分離純化步驟中所收集之蛋白質與一紅企球懸浮液之凝 集活性,來作為判斷蛋白質純化與否的一種依據,其中此 紅血球懸浮液之置備係利用以下之方法··將所採集之紅血 球加入pH值為7· 2、50毫莫爾濃度(mM)之磷酸鹽緩衝液( Phosphate Buffer Saline, PBS)中,以離心方式清洗三 次,其離心條件為每分鐘2 0 0 0轉速(2 0 0 0 r pm ),連續旋轉 1 0分鐘;取下層之紅血球濃縮液,再以磷酸鹽緩衝液(PBS )稀釋成一體積百分比為2% (v/v)之紅血球懸浮液,在4 °C 下備用以用來做生物檢測。 而凝集活性之測定係將一純化分離步驟中所取得之蛋To the required speed grade, the time of each crushing is 5 seconds, leap seconds, 4 crushing 6 times. 5) The first grinding method: the chlorella steamed body two cells and alumina (A! 2%) by weight Ratio (w / w) 1: 3, uniformly mix it, and use a glass rod to grind it in an ice bath for 10 minutes; (six) the second grinding method: a small ball bathing the body cells and the sea sand in a weight ratio (w / w ) 1: 3 uniformly mixed using a glass * rod in an ice bath for 10 minutes; (7) Enzyme method: the two yeasts were mixed at a volume ratio of 1: 1 for two hours at 37 ° C, where The two enzymes are a volume percentage of Macrozyme R-10 and distilled water of 2% (w / v) and a volume percentage of giucuronidase and distilled water of 2% (v / v). In the method for purifying glycoproteins of the microbath according to the present invention, human blood of type A, B, 0, AB and animal blood, such as pigs, cattle, and sheep, are used to separate the protein collected in each separation and purification step with one The agglutination activity of erythrocyte suspension was used as a basis for judging whether the protein was purified or not. The preparation of this erythrocyte suspension was made by the following methods: · The collected erythrocytes were added to the pH value of 7. 2, 50 mmol In mM phosphate buffer (Phosphate Buffer Saline, PBS), wash three times by centrifugation. The centrifugation condition is 20000 rotation speed (20000 r pm) per minute, continuous rotation for 10 minutes. ; Take down the red blood cell concentrated solution, and then dilute with phosphate buffered saline (PBS) to a 2% (v / v) red blood cell suspension, and reserve it at 4 ° C for biological detection. The agglutination activity is determined by separating eggs obtained in a purification and separation step.

第13頁 200521136 五、發明說明(10) 白質,以50微升(micro 1 iter, //L)置放於96孔穴血孔計 算盤(96-well micro-V-plates)的第一個孔洞上,另外, 係取50微升之磷酸鹽緩衝液(PBS)置放於96孔穴血孔計算 盤中之每一孔洞中,將第一孔洞中之蛋白質與磷酸鹽緩衝 液均勻混合之,之後,將第一孔洞中之混合溶液取5 〇微 升至第二孔洞中,做二分之一連續稀釋,亦即執行上述之 步驟後,其第二孔洞混合溶液之濃度係為第一孔洞中之一 半,之後,加入2 %紅血球懸浮液於各孔洞中,均勻混合 後’係在室溫下靜置2小時,並以肉眼觀察其凝集反應。 而凝集活性之大小係以凝集力價(t i ter)來表示,凝集力 饧的表示是在觀察到紅企球凝集時之最後稀釋稀釋倍數之 倒數,例如,蛋白質在稀釋丨/64倍數仍具有活性,因此, 此時之凝集力價為6 4,亦即26。 要說明的是,本發明之微藻親醣蛋白之純化方法中, 亦可使用一紅血球酵素懸浮液與在各純化分離步驟中所 集之蛋白質做一凝集活性測試,其中,為了提高檢測之結 果,係利用一經酵素别處理之紅血球細胞,例如鏈黴蛋白 酵素(pronase)、胰蛋白(trypsin)或鏈蛋白(papin)、,蛋 白酵素可增加紅血球表面之接受位置(recept〇r sit 以助於凝集活性之確立。而鈴a讨觖各辟、,…六士印 张、f ·脱一紐I 而紅血球酵素懸汙液之置備係如 ;L 酵素,例如鏈蛋白(papain),加入一石粦酸蜂 緩衝液中,並配置為體積百分比2% (v/v)之一酵素溶: 取一紅血球懸洋液加人此酵素溶液中,其中紅血球與酵素Page 13 200521136 V. Description of the invention (10) White matter, placed in the first hole of a 96-well micro-V-plates at 50 microliters (micro 1 iter, // L) In addition, 50 microliters of phosphate buffered saline (PBS) was placed in each well of a 96-well blood plate, and the protein in the first well was uniformly mixed with the phosphate buffered solution. Take 50 microliters of the mixed solution in the first hole into the second hole and make one-half continuous dilution, that is, after performing the above steps, the concentration of the second hole mixed solution is in the first hole One and a half, after that, 2% red blood cell suspension was added to each hole, and after homogeneous mixing, it was left at room temperature for 2 hours, and its agglutination reaction was observed with the naked eye. The size of agglutination activity is expressed by the agglutination valence (ti ter). The expression of agglutination 饧 is the reciprocal of the final dilution dilution when erythrocyte agglutination is observed. For example, the protein still has Activity, so the cohesive force valence at this time is 64, which is 26. It should be noted that in the method for purifying the microalgal glycophilic protein of the present invention, a erythrocyte enzyme suspension and the protein collected in each purification and separation step may be used to perform an agglutination activity test, in order to improve the detection result The use of enzyme-treated red blood cells, such as pronase, trypsin, or papin, proteinases can increase the red blood cell surface's acceptance position (receptor sit to help The establishment of agglutination activity. And boll a discusses each,… six seal sheets, f · take off a button I and the preparation of red blood cell enzyme suspension is as follows; L enzyme, such as papain, add monolithic acid In bee buffer and configured as one of 2% (v / v) by volume of enzyme solution: take a red blood cell suspension and add it to this enzyme solution, where red blood cells and enzymes

200521136 五、發明說明(11) 溶液之體積比為1 · 1 0 ’在3 7 C下反應1小時,以除去紅血 球表面之涎酸(si al ic acid)或醣蛋白,並置於4。〇下保存 而其凝集活性之測試係將一純化分離步驟中所取得之 蛋白質,以5 0微升置放於9 6孔穴血孔計算盤的第一個孔洞 上,另外,係取50微升之磷酸鹽緩衝液置放於96孔穴血 孔計算盤中之每一孔洞中,將第一孔洞中之蛋白質與磷酸 鹽緩衝液均勻混合之,之後,將第一孔洞中之混合溶液取 5 0微升至第二孔洞中,做二分之一連續稀釋,亦即執行 上述之步驟後,其第二孔洞混合溶液之濃度係為第一孔洞 中之一半,之後,加入2 %紅血球酵素懸浮液於各孔洞中 均勻混合後’係在室溫下靜置2小時,並以肉眼觀察1 凝集反應。 本發明之被澡親酶蛋白之純化方法十,係將小球藻萃 取液以一硫酸敍水溶液來沈殿一部份之蛋白質,並用以決 =進行小球藻凝集素分離純化之最適條件。其中不同飽= ^度之硫酸銨水溶液其所沈澱之蛋白質的凝集活性亦不相 =’如表一所示。其中,0_20%飽和濃度之硫酸銨水溶液 沈澱之蛋白質其凝集活性最高,係為π凝集力價(tt π ’而20-40 % 、40-60 %及60_8〇%飽和濃度之硫酸銨水溶 ^所沈澱之蛋白質亦有部分凝集活性,係在22至25凝集力 貝之間,而8 0 -1 0 0 %則無凝集活性。在硫酸銨水溶液中所200521136 V. Description of the invention (11) The volume ratio of the solution is 1 · 1 0 ′ and the reaction is performed at 37 ° C for 1 hour to remove the sialic acid or glycoprotein on the surface of red blood cells, and placed at 4. The test of its agglutination activity stored under 〇 is to place 50 microliters of the protein obtained in a purification and separation step on the first hole of a 96-well blood cell calculation disk, and in addition, take 50 microliters The phosphate buffer solution is placed in each hole in the 96-well blood well calculation plate, and the protein in the first hole is uniformly mixed with the phosphate buffer solution. After that, the mixed solution in the first hole is taken as 50. Slightly dilute to the second hole and make one-half serial dilution, that is, after performing the above steps, the concentration of the second hole mixed solution is half of that in the first hole, and then add 2% red blood cell enzyme suspension After being uniformly mixed in each hole, the system was left at room temperature for 2 hours, and the agglutination reaction was observed with the naked eye. The purification method 10 of the bathed pro-enzyme protein of the present invention is to extract a part of the protein from the chlorella extract with a sulfuric acid aqueous solution and use it to determine the optimal conditions for the separation and purification of chlorella agglutinin. Among them, the agglutination activity of the precipitated protein in different ammonium sulfate aqueous solutions of different degrees = ^ degrees is not the same as shown in Table 1. Among them, 0-20% saturated ammonium sulfate aqueous solution precipitates proteins with the highest agglutination activity, which are π agglutination valence (tt π 'and 20-40%, 40-60% and 60_80% saturated ammonium sulfate aqueous solution ^ The precipitated protein also has partial agglutination activity, which is between 22 and 25 agglutination force, while 8 0-100% has no agglutination activity.

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200521136 五、發明說明(12) 需添加之硫酸銨含量如表二所述,例如,欲配置一 0 - 2 0 % 飽和濃度之硫酸銨水溶液,係參照硫酸銨之起始飽和濃度 為0 % ,而最終硫酸銨飽和濃度為2 0 %時,此條件下在1公 升溶液中所需添加固態硫酸銨之含量為1 0 6公克,其他濃 度範圍所需的硫酸銨含量以此類推。 表一200521136 V. Description of the invention (12) The ammonium sulfate content to be added is as described in Table 2. For example, if you want to configure a 0-20% saturated ammonium sulfate aqueous solution, refer to the initial saturation concentration of ammonium sulfate as 0%, When the final saturated concentration of ammonium sulfate is 20%, under this condition, the content of solid ammonium sulfate required in a 1 liter solution is 106 grams, and the other ammonium sulfate content required in the other concentration ranges can be deduced by analogy. Table I

硫酸敍水溶液之 飽和濃度範圍(% ) 蛋白質濃度 (毫克/毫升) 凝集力價 (第特)(titer) 粗萃取 0.168 26 0-20 0.573 29 20-40 0.4 11 25 40-60 0.244 無凝集活性 60-80 0.266 22 80-100 0.2 1 無凝集活性 第16頁 200521136 五、發明說明(13) 表 最終硫酸銨飽和濃度(% ) 20 25 30 35 40 45 50 55 60 65 70 75 80 90 100 加入一公升溶液中之固態硫酸銨含量(克) 硫 酸 敍 起 始 飽 和 濃 度 % 0 106 134 164 194 226 258 291 326 361 398 436 476 516 603 697 0 20 0 27 55 83 113 143 175 207 241 276 312 349 387 469 557 20 25 0 27 56 84 115 146 179 211 245 280 317 355 436 522 25 30 0 28 56 86 117 148 181 214 249 285 323 402 488 30 35 0 28 57 87 118 151 184 218 254 291 369 453 35 40 0 29 58 89 120 153 187 222 258 335 418 40 45 0 29 59 90 123 156 190 226 302 383 45 50 0 30 60 92 125 159 194 268 348 50 55 0 31 61 93 127 161 235 313 55 60 0 31 62 95 129 201 279 60 65 0 31 63 97 168 244 65 70 0 32 65 134 209 70 75 0 32 101 174 75 80 0 34 139 80 90 0 70 90 100 0 100 本發明之微藻親醣蛋白之純化方法將以下述之具體實 施例做一詳細說明。 本發明微藻親醣蛋白之純化方法的一具體實施例中, iiii 第17頁 200521136 五、發明說明(14) 係將一小球藻藻珠,例如c. lute〇viridis luteoviridis),利用 (Ch1 ore 11 a 璃珠法,將此小球藻藻體卓:皮處理加玻 響凝集活性之關鍵,因此,破由於破胞時間係影 分鐘,休息兩分鐘之以機器震1三 條件将在、太、、又下婭从 以避免凝集活性喪失,且破胞 執行收隼一蛋白質、、六γ ^ t,將破胞後之小球藻藻體細胞 所欲分離純化之小球薄凝隹♦ 2 I +疋蛋白貝浴液L έ 係如下所述:#先,;〇 ΓΛν 質溶液的步驟 奸丄 取0·5克已破胞之小球藻藻體細胞, ,加入一 Μ中進行小球藻凝集素之萃$,例如5毫升之 Μ酸鹽缓衝液(PBS),此萃取條件係在4t下萃取24小時, 之後,以每分鐘20000轉速(rpm)、離心2〇分鐘之離心方式 j除殘渣。接著,取上層之上清液並加入不同濃度範圍之 一硫酸銨水溶液中,例如〇 一 20% 、2〇-4〇% 、4卜6〇% 、 6 〇〜8 0 %及8 0 - 1 〇 〇 %飽和濃度之硫酸銨水溶液,以將所欲 刀離之蛋白質溶液沈殿出,此蛋白質係包含所欲分離純化 之小球藻凝集素。 以不同濃度之硫酸銨水溶液來決定凝集素分離純化條 件之步驟係如下所述:以0-20 %飽和濃度之硫酸銨水溶夜 加入小球藻萃取液中,並在冰浴中平衡一小時,即沈澱出 所欲分離之蛋白質,於4 °C下以每分鐘1 5 00 0轉速(rpm)並 離心30分鐘,之後,取上層之上清液,加入20-40%飽和 濃度之硫酸錄水溶液,並得到以此濃度範圍所沈澱出之蛋Saturated concentration range of sulfuric acid aqueous solution (%) Protein concentration (mg / ml) Cohesion value (tite) Coarse extraction 0.168 26 0-20 0.573 29 20-40 0.4 11 25 40-60 0.244 No agglutination activity 60 -80 0.266 22 80-100 0.2 1 No agglutination activity Page 16 200521136 V. Description of the invention (13) Table final concentration of ammonium sulfate (%) 20 25 30 35 40 45 50 55 60 65 70 75 80 90 100 Add one liter Solid ammonium sulfate content in solution (g) Initial saturation concentration of sulfuric acid% 0 106 134 164 194 226 258 291 326 361 398 436 476 476 516 603 697 0 20 0 27 55 83 113 143 175 207 241 276 312 349 387 469 557 20 25 0 27 56 84 115 146 179 211 245 280 317 355 436 522 25 30 0 28 56 86 117 148 181 214 249 285 323 402 488 30 35 0 28 57 87 118 151 184 218 254 291 369 453 35 40 0 29 58 89 120 153 187 222 258 335 418 40 45 0 29 59 90 123 156 190 226 302 383 45 50 0 30 60 92 125 159 194 268 348 50 55 0 31 61 93 127 161 235 313 55 60 0 31 62 95 129 201 279 60 65 0 31 63 97 168 244 65 70 0 32 65 134 209 70 75 0 32 101 174 75 80 0 34 139 80 90 0 70 90 100 0 100 The purification method of the microalgal glycoprotein of the present invention will be described in the following specific examples Do a detailed explanation. In a specific embodiment of the method for purifying the microalgae glycoprotein of the present invention, iiii page 17 200521136 V. Description of the invention (14) A chlorella bead, such as c. Lute〇viridis luteoviridis, is used (Ch1 ore 11 a glass bead method, the key to this chlorella algae body: skin treatment plus glassy agglutination agglutination activity, so, because the cell-breaking time is a matter of minutes, take a two-minute rest with a machine shock To avoid the loss of agglutination activity, and break the cells to collect a protein, six γ ^ t, to separate and purify the small globules of the chlorella somatic cells after the break ♦ 2 I + 疋 protein shell bath L is as follows: # 先 , ; 〇ΓΛν The step of the quality solution is to take 0.5 grams of broken Chlorella alga cells, and add 1 M to the pellet. Extraction of algae agglutinin, such as 5 ml of M salt buffer (PBS). The extraction conditions are extraction at 4t for 24 hours, and then centrifugation at a speed of 20,000 rpm for 20 minutes. Remove the residue. Next, take the supernatant of the upper layer and add one sulfur of different concentration range In the ammonium aqueous solution, for example, -20%, 20-40%, 40%, 60%, 600 ~ 80%, and 80% -1000% saturated ammonium sulfate aqueous solution to cut off the desired A protein solution from Shen Dian, this protein contains the desired chlorella lectin. The steps for determining the lectin separation and purification conditions with different concentrations of ammonium sulfate aqueous solution are as follows: 0-20% saturated concentration Ammonium sulfate was dissolved in water and added to the chlorella extract, and equilibrated in an ice bath for one hour, and the protein to be separated was precipitated. At 4 ° C, it was centrifuged at 15,000 rpm for 30 minutes. After that, the supernatant of the upper layer was taken, and a 20-40% saturated aqueous solution of sulfuric acid was added to obtain eggs precipitated in this concentration range.

第18頁 200521136 五、發明說明(15) 白質,接著,以每2 〇 %之飽和濃度為一劃分,重複以上之 步驟及條件,因此,係得到五個分劃之蛋白質沈澱。完成 分劃後,每個分劃中所沈澱之蛋白質係以磷酸鹽緩衝液( PBS)溶解,並置入一透析袋中,在4它透析下48-72小時, 透析之目的係為去除填酸鹽等鹽類,其中,每四小時更換 一次透析溶液。接著,完成透析後,以每分鐘1 5 0 00轉迷、 (rpm)並離心3〇分鐘,以除去不溶物之雜質,然後取上層 澄清液並測定其凝集活性,其中,以0-20 %飽和濃度之^硫 酸銨水溶液所沈澱之蛋白質其凝集活性最高,而2〇-8()% 硫酸銨水溶液所沈澱之蛋白質亦有部分凝集活性,因此, 取0-80 %飽和濃度之硫酸銨水溶液所沈澱的蛋 接續㈣。 貝木進盯 接著’將0-80 %飽和濃度之硫酸銨水溶液所沈澱之蛋 白質通入一DEAE-C-52之陰離子交換層析管柱中分離純化 ,此純化分離之步驟係在4 t下進行。其中,此阶離子交 換層析管柱之尺寸大小係為2·6αηχ 18cm,而此$柱先以 一 pH值為8.0之磷酸緩衝液(ph〇sphate buffe ,28〇nm之吸收值為零,再將欲分離之蛋白質通入此管柱 中,其中,每分鐘流速為1.5毫升。首先,收 性之流出液(以與紅血球之凝集活性做判斷)〃,麩後,/以 容ίί利用?度梯度之方式,將所欲離之蛋 八中,此氣化鈉水溶液之濃度範圍传由〇 1 莫爾濃度⑻至0.5莫爾濃度(Μ),卩每以莫爾^^區Page 18 200521136 V. Description of the invention (15) White matter. Then, the above steps and conditions are repeated with a saturation concentration of 20% each. Therefore, five divided protein precipitates are obtained. After the division is completed, the protein precipitated in each division is dissolved in phosphate buffered saline (PBS) and placed in a dialysis bag. It is dialyzed for 48-72 hours. The purpose of dialysis is to remove Salts such as acid salts, in which the dialysis solution is changed every four hours. Next, after dialysis is completed, rotate at 15,000 rpm (rpm) and centrifuge for 30 minutes to remove impurities of insoluble matter, then take the upper clear solution and measure its agglutination activity, where 0-20% Saturated concentration of ^ ammonium sulfate aqueous solution has the highest agglutination activity of the protein, and 20-8 ()% ammonium sulfate aqueous solution of the protein precipitated also has some agglutination activity. Therefore, 0-80% saturated concentration of ammonium sulfate aqueous solution is taken The precipitated eggs continued to scramble. Beimujin followed by 'pass the 0-80% saturated concentration of ammonium sulfate aqueous solution of the protein precipitated into a DEAE-C-52 anion exchange chromatography column separation and purification, the purification and separation step is under 4 t get on. Among them, the size of this stage ion exchange chromatography column is 2. 6αηχ 18cm, and this $ column first uses a phosphate buffer solution (ph0sphate buffe with a pH value of 8.0, the absorption value of 28nm is zero, Then the protein to be separated is passed into the column, wherein the flow rate is 1.5 ml per minute. First, the recoverable effluent (based on the agglutination activity with red blood cells) is used. After the bran, is it used? The degree of gradient method is to transfer the concentration range of the gasified sodium hydroxide aqueous solution in the desired egg eight from 0 mol concentration to 0.5 mol concentration (M).

第19頁 200521136 五、發明說明(16) ^ 分,而所收集之蛋白質係以每分鐘丨· 5毫升,每3毫升一 分劃。將所收集之各分劃的蛋白質做其凝集活性之剛試, 以及在波長280nm下偵測其吸收值,其中,以〇· 2莫爾^ 之氣化納水溶液所沖提出之蛋白質同時具有最大之吸$ ^ 及凝集活性,而其他分劃所收集之蛋白質流出液則有二 之吸收度及凝集活性,如第一圖所示。因此,收集以〇 莫爾濃度之氯化鈉水溶液所沖提出之蛋白質流出液。· 將此濃度下所收集之蛋白質流出液濃縮後,以一醋酸 納緩衝液(Sodium Acetate Buffer)為一透析溶液,此透 析溶液之pH值為4.0,濃度為50毫莫爾濃度(mM),其體積 為所收集之蛋白質流出液體積的丨〇 〇倍,而其透析時間為貝 1 2小時以上。之後’利用1 50 0 〇轉速(rpm)離心以去除不溶 之沈澱物及雜質,以達到純化之目的及去除不具凝集活性 之蛋白質,並利於進行下一步之純化分離步驟。 將在DEAE-C-52之陰離子交換層析方法中,以〇·2莫爾 濃度氯化鈉水溶液沖提所得到之蛋白質溶液,通入一CM-C- 5 2陽離子交換層析管柱中,以進行下一步之分離純化步 驟。其中,此陽離子交換層析管柱之配置方法係如下所述 :首先,秤取適量之CM-cellulose-52之乾燥粉末,以50 倍體積之0.5當量氫氧化鈉(NaoH)水溶液浸泡30分鐘,再 以去離子水洗至中性(其pH值低於8. 0)後,再以50倍體積 之〇· 5當量氯化氫(HC1)水溶液浸泡30分鐘,再以去離子水Page 19 200521136 V. Description of the invention (16) ^ points, and the collected protein is divided into 5 ml per minute and 3 ml per minute. The collected proteins were tested for their agglutination activity, and their absorption values were detected at a wavelength of 280 nm. Among them, the protein extracted from the aqueous sodium carbonate solution of 0.2 Moore ^ had the largest value at the same time. The absorption of ^^ and agglutination activity, while the protein effluent collected by other divisions has two absorbance and agglutination activity, as shown in the first figure. Therefore, the protein effluent, which was extracted with an aqueous solution of sodium chloride at a concentration of 0 mole, was collected. · After concentrating the protein effluent collected at this concentration, a sodium acetate buffer (Sodium Acetate Buffer) is used as a dialysis solution. The pH of the dialysis solution is 4.0 and the concentration is 50 millimolar (mM). Its volume is 1000 times the volume of the collected protein effluent, and its dialysis time is more than 12 hours. After that, it is centrifuged at 15,000 rpm to remove insoluble precipitates and impurities to achieve the purpose of purification and to remove proteins without agglutination activity, which is beneficial to the next step of purification and separation. The DEAE-C-52 anion exchange chromatography method was used to extract the obtained protein solution with an aqueous sodium chloride solution at a concentration of 0.2 Moore, and passed through a CM-C-5 2 cation exchange chromatography column. For the next step of isolation and purification. Among them, the configuration method of the cation exchange chromatography column is as follows: First, weigh out an appropriate amount of dry powder of CM-cellulose-52, and soak it with 50 times the volume of 0.5 equivalent sodium hydroxide (NaoH) aqueous solution for 30 minutes. It was washed with deionized water to neutrality (its pH value was lower than 8.0), and then immersed in 50 times the volume of 0.5 equivalent hydrogen chloride (HC1) aqueous solution for 30 minutes, and then deionized water.

第20頁 200521136 五、發明說明(17) 洗至中性(其PH值高於4.(0,以一〇>1莫爾濃度之醋酸 緩衝液浸泡數小時後,緩緩倒去上層液,去除懸浮粒 並倒入管柱中,待沈澱至所需要之高度後,以一1〇 j 濃度值為4.0之醋酸鈉緩衝液充分平衡備用之爾 將DEAE-C-52之陰離子交換層析方法中所收集之且 性之蛋白質溶液通入此CM-C-52之陽離子交換層析管柱中 职t ΐ —圖所示,賓"先,係以—醋酸鈉緩衝溶液(1〇毫莫 :=,ΡΗ值為4·。)先沖提出未吸附之蛋白質 ^ 波長下之吸收值,此蛋白質流出液在此波長下 有吸收但以紅血球檢測卻無凝集活性,因此, 友 =水溶液’制用濃度梯度: 蛋白質沖提出。其中,此氯化納水溶液: 产、.莫爾遭度(Μ)至0.5莫爾濃度⑷’以每〇 ΐ 毫升為而所Λ集之… 紅血球之1升隹為刀剎,檢測所收集之各分劃的蛋白質與 白質产出^集活性’其中’每一濃度範圍下所沖提出之蛋 納水;=吸收性,但以°.2莫爾濃度之氯化 收集以0 ?替如/之蛋白質具有最大之凝集活性,因此, 蛋白質,·以進爾漢下度之氣化納水溶液所沖提出之具有活性 進灯下一步之純化分離步驟。 要說明的旱,i i 集之蛋白質、、容、凉#田;陰離子交換層析方法中,將所收 、夜使用一醋酸鈉緩衝液做透析,因此,其蛋 200521136 五、發明說明(18) 白貝溶液會帶有較多之負電性,所以,當通過CM-52 c e 1 1 u 1 〇 s e陽離子交換管柱時,其凝集素會吸附在此管柱 之纖維上’之後,再利用不同濃度之氯化鈉水溶液沖提, 則可達到分離之目的及去除不具凝集活性之蛋白質。 將在CM-C-52之陽離子交換層析方法中所收集之具有活 陵之蛋白質’以每分鐘⑽〇轉速(rpm)並離心20分鐘,以 ^除不溶之沈澱物。接著,以一Superdex 75膠體管柱進 !!更進一步之純化分離步驟,其中,此Superdex 75膠體 、官柱係先置於一〇· 莫爾濃度,pH值為7· 4之磷酸鹽緩衝 液中’ 4 c下以此緩衝液沖提,直至波長28〇ηιη之吸收值為 零。之後’利用在CM-C-52之陽離子交換層析管柱中所收 集到之具有活性之蛋白質流出液,將其體積濃縮至3 %以 ^例如由丨00毫升至3毫升,之後,通入此Superdex 75 ^體管柱中。其中,係以每分鐘〇· 3毫升,每丨毫升為一分 ^查收集所流出之蛋白質溶液。如第三圖所示,檢測每個 为劃之蛋白質流出液在波長28〇11111之吸收值及其凝集活性 其中,以此膠體層析方法分離純化後,可得到包含兩種 J =質之流出液,因此,將此蛋白質流出液與紅血球做一 中y活性之測試,並完成此小球藻凝集素之純化步驟。其 一之蛋白負與紅血球具有凝集性,但另一蛋白質則 藉由上述純化小球藻凝集素之過程可得知,本發明提Page 20 200521136 V. Description of the invention (17) Wash to neutral (its pH value is higher than 4. (0, acetic acid buffer solution with a concentration of 10 > 1 > Mohr), after several hours, slowly pour off the upper layer Remove the suspended particles and pour into the column. After precipitation to the required height, fully equilibrate with a 10j sodium acetate buffer solution with a concentration of 4.0, and use the anion exchange chromatography of DEAE-C-52. The neutral protein solution collected in the method was passed into the cation exchange chromatography column of this CM-C-52. Ϊ́ —As shown in the figure, Bin " First, it is-sodium acetate buffer solution (10 mM) Mo: =, PΗ value is 4 ·.) First put forward the absorption value of unadsorbed protein ^ at the wavelength. The protein effluent has absorption at this wavelength but has no agglutination activity when detected by red blood cells. Therefore, Friend = aqueous solution ' Concentration gradient for production: Protein is extracted. Among them, this aqueous solution of sodium chloride: produces, Moore (degrees) to 0.5 Moore concentration ⑷ 'set per ΐ milliliter ml ... 1 liter of red blood cells隹 is a knife brake, which detects the protein and white matter output of each division collected. Egg water absorbed at each concentration range; = Absorptive, but chlorinated at a concentration of ° .2 Mohr and collected at 0? Tir / has the highest agglutinating activity, so protein, The next step is the purification and separation step of the next step of purification of the gasified sodium aqueous solution, which has the activity to enter the lamp. To be explained, the protein,, capacity, and cold #field of the set II; the anion exchange chromatography method, the A sodium acetate buffer solution was used for dialysis at night. Therefore, its egg 200521136 V. Description of the invention (18) The white shell solution will have more negative electrical properties. Therefore, when passed CM-52 ce 1 1 u 1 〇se When a cation exchange column is used, its lectin will be adsorbed on the fibers of this column, and then it is extracted with different concentrations of sodium chloride aqueous solution to achieve the purpose of separation and remove proteins without agglutination activity. -C-52 cation-exchange chromatography-collected protein with active protein 'was centrifuged at rpm (rpm) for 20 minutes to remove insoluble precipitate. Then, a Superdex 75 colloid tube was used. Zhujin !! Purification and separation steps, in which the Superdex 75 colloid and the official column are first placed in a phosphate buffer solution with a concentration of 10 · Moore and a pH value of 7.4, and the buffer solution is extracted under 4 C until the wavelength The absorption value of 28〇ηιη is zero. Afterwards, the volume of the active protein effluent collected in the cation exchange chromatography column of CM-C-52 is used to concentrate the volume to 3%. Milliliter to 3 milliliter, and then passed into this Superdex 75 ^ body tube column, where 0.3 milliliter per minute, each milliliter is a minute to collect the effluent protein solution. As shown in the third figure, the absorption value and agglutination activity of each protein effluent at a wavelength of 28011111 are detected. After being separated and purified by the colloidal chromatography method, two kinds of effluents with J = mass can be obtained. Therefore, the protein effluent and red blood cells were tested for y activity, and the purification step of chlorella agglutinin was completed. One of the proteins has agglutination with red blood cells, but the other protein can be learned through the above-mentioned process of purifying chlorella lectin, and the present invention provides

第22頁 200521136Page 22 200521136

五、發明說明(19) 出之凝集素純化方法簡單明瞭且容易操作,且小球藻、t 素可應用在其他生化機能以及保健食品等等,榀集 益。 寸極具經濟效 以上所述僅為本發明之具體實施例,並非用以限— 發明之申請專利範圍,凡其他為脫離本發明所揭示疋本 下所完成之等效改變或修飾,均應包含在下述 主精神 範圍内。 T %專利V. Description of the invention (19) The lectin purification method is simple, straightforward, and easy to operate, and chlorella and t can be used in other biochemical functions and health foods, etc. Inch is highly economical. The above description is only a specific embodiment of the present invention, and is not intended to limit the scope of the patent application for the invention. Any other equivalent changes or modifications made outside the scope of the present disclosure should be applied. Contained within the scope of the main spirit described below. T% patent

200521136_ 圖式簡單說明 五、【圖示簡單說明】 第一圖係小球藻C. luteoviridis利用DEAE-C-52之陰 離子交換層析管柱方法純化分離小球藻凝集素之曲線圖 第二圖係小球藻C. luteoviridis利用CM-C-52之陽離 子交換層析管柱方法純化分離小球藻凝集素之曲線圖;及 第三圖係小球藻C. luteoviridis利用Superdex 75之 膠體層析過濾方法純化分離小球藻凝集素之曲線圖。200521136_ Brief description of the diagram V. [Simplified illustration of the diagram] The first diagram is a graph of the purification and separation of chlorella lectin by C. luteoviridis using anion exchange chromatography column method of DEAE-C-52. It is a graph of chlorella C. luteoviridis using CM-C-52 cation exchange chromatography column method to purify and isolate chlorella lectin; and the third graph is of chlorella C. luteoviridis using colloidal chromatography of Superdex 75 Graph of purification and separation of chlorella lectin by filtration method.

第24頁Page 24

Claims (1)

200521136 六、申請專利範圍 1. 一種微藻親醣蛋白之純化方法,包含: 提供一小球藻樣品,該小球藻樣品係包含複數個小球 藻藻體細胞; 對該小球藻樣品執行一破胞步驟,以擊破該複數個小 球藻無體細胞; 對該已擊破之複數個小球藻藻體細胞執行一收集之步 驟; 執行一陰離子交換管柱層析步驟; 執行一陽離子交換管柱層析步驟,其中該陽離子交換 管柱層析步驟係執行於該陰離子交換管柱層析步驟之後; 及 執行一膠體過濾層析步驟,以獲得一凝集素。 2. 如申請專利範圍第1項所述之微藻親醣蛋白之純化方法 ,其中於上述之破胞步驟後,更包含執行複數次紅血球凝 集活性之檢測。 3. 如申請專利範圍第1項所述之微藻親醣蛋白之純化方法 ,其中上述之破胞步驟係以一液態氮法達成。 4. 如申請專利範圍第1項所述之微藻親醣蛋白之純化方法 ,其中上述之破胞步驟係以一玻璃珠法達成。 5.如申請專利範圍第1項所述之微藻親醣蛋白之純化方法200521136 6. Application patent scope 1. A method for purifying microalgae glycoprotein, comprising: providing a chlorella sample, the chlorella sample system comprises a plurality of chlorella somatic cells; performing the chlorella sample A cell breaking step to break the plurality of chlorella somatic cells; perform a collection step on the broken plurality of chlorella somatic cells; perform an anion exchange column chromatography step; perform a cation exchange A column chromatography step, wherein the cation exchange column chromatography step is performed after the anion exchange column chromatography step; and a colloid filtration chromatography step is performed to obtain a lectin. 2. The method for purifying microalgal glycoproteins as described in item 1 of the scope of the patent application, wherein after the lysis step described above, the method further comprises performing a plurality of tests of red blood cell agglutination activity. 3. The method for purifying microalgal glycoproteins as described in item 1 of the scope of the patent application, wherein the step of breaking cells is achieved by a liquid nitrogen method. 4. The method for purifying microalgal glycoproteins as described in item 1 of the scope of the patent application, wherein the step of breaking cells is achieved by a glass bead method. 5. Purification method of microalgal glycoprotein as described in item 1 of the scope of patent application 200521136 六、申請專利範圍 成 ,其中上述之破胞步驟係以/超聲波處理法達 6·如申請專利範圍第1項所述之微藻親醣|占 裏曰之纟φ ,其中上述之破胞步驟係以/組織禱碎法達成、、化方法 7. 如申請專利範圍第1項所述之微藻親醣蛋白 其中上述之破胞步驟係以/研磨法達成。 之純化方法 8.如申請專利範圍第1項所述之微藻親醣蛋白夕紐&士 K曰 < 純化方法 ,其中上述之破胞步驟係以一酵素法達成。200521136 6. The scope of the patent application is completed, in which the above-mentioned cell-breaking step is performed by the ultrasonic treatment method 6. The microalgae sugar as described in item 1 of the scope of patent application | The steps are achieved by the / organization method. 7. The microalgae glycoprotein described in item 1 of the patent application scope, wherein the above-mentioned cytolytic step is achieved by the / mill method. Purification method 8. The microalgae glycoprotein Xi Nuo & K K < purification method as described in item 1 of the scope of the patent application, wherein the cell breaking step described above is achieved by an enzyme method. 9 ·如申請專利範圍第1項所述之微藻親醣蛋白之純化方法 ,其中上述之收集步驟係包含利用一磷酸鹽緩衝液 (Phosphate buffer saline)為一萃取溶液。 1 0 ·如申請專利範圍第1項所述之微藻親醣蛋白之純化方法 ,其中上述之收集步驟係包含加入一硫酸銨水溶液。 11·如申請專利範圍第1 0項所述之微藻親醣蛋白之純化方9. The method for purifying microalgal glycoproteins as described in item 1 of the scope of the patent application, wherein the above-mentioned collection step comprises using a phosphate buffer saline as an extraction solution. 10 · The method for purifying a microalgal glycoprotein as described in item 1 of the scope of the patent application, wherein the above-mentioned collection step includes adding an ammonium monosulfate aqueous solution. 11. Purification method of microalgal glycoprotein as described in item 10 of the scope of patent application 法’其中上述之硫酸銨水溶液之飽和濃度範圍係選自下列 任一者··重量百分比濃度為〇-2〇 % 、20-40 % 、40-60%及 6 0 - 8 0 % 〇 12·如申請專利範圍第1項所述之微藻親醣蛋白之純化方Method 'wherein the saturated concentration range of the above-mentioned ammonium sulfate aqueous solution is selected from any one of the following: · The weight percentage concentration is 0-20%, 20-40%, 40-60%, and 60-80%. 012. Purification method of microalgal glycoproteins as described in the first patent application scope 第26頁 200521136 六、申請專利範圍 法,其中上述之陰離子交換管柱層析方法係包含利用一氯 化鈉水溶液沖提一蛋白質物質。 13.如申請專利範圍第1項所述之微藻親醣蛋白之純化方 法,其中上述之陽離子交換管柱層析方法係包含利用一氯 化鈉水溶液沖提一蛋白質物質。 14·如申請專利範圍第1 2項所述之微蕩親醣蛋白之純化方 法,更包含以一濃度梯度之方法沖提該蛋白質物質。 15·如申請專利範圍第1 3項所述之微藻親醣蛋白之純化方 法,更包含以一濃度梯度之方法沖提該蛋白質物質。 16.如申請專利範圍第1 2項所述之微藻親醣蛋白之純化方 法,更包含利用一醋酸鈉缓衝液(Sodium Acetate Buffer) 為一透析溶液。 1 7 ·如申請專利範圍第1 3項所述之微藻親醣蛋白之純化方 法,更包含利用一碟酸鹽緩衝液為一透析溶液。 18· 一種微藻親醣蛋白之純化方法,包含: 提供一小球藻樣品,該小球藻樣品係包含複數個小球 無無體細胞; 執行一超聲波處理混合玻璃珠之破胞步驟,以擊破該Page 26 200521136 VI. Patent application method, wherein the above-mentioned anion exchange column chromatography method comprises extracting a protein substance with an aqueous solution of sodium chloride. 13. The method for purifying microalgal glycoproteins according to item 1 of the scope of the patent application, wherein the method of cation exchange column chromatography described above comprises eluting a protein substance with an aqueous solution of sodium chloride. 14. The method for purifying a slightly glycophilic protein as described in item 12 of the scope of the patent application, further comprising extracting the protein substance by a concentration gradient method. 15. The method for purifying a microalgal glycoprotein as described in item 13 of the scope of the patent application, further comprising extracting the protein substance by a concentration gradient method. 16. The method for purifying a microalgal glycoprotein according to item 12 of the patent application scope, further comprising using a sodium acetate buffer (Sodium Acetate Buffer) as a dialysis solution. 17 · The method for purifying a microalgal glycoprotein as described in item 13 of the scope of the patent application, further comprising using a dish buffer solution as a dialysis solution. 18. A method for purifying microalgae glycoproteins, comprising: providing a chlorella sample, the chlorella sample system comprising a plurality of globules without somatic cells; performing an sonication step of mixed glass beads, and Break that 第27頁 200521136 六、申請專利範圍 複數個小球藻藻體細胞; 對該已擊破之複數個小球藻藻體細胞執行一萃取之步 驟以得到一萃取液; 對該萃取液執行一沈澱之步驟,以得到一第一蛋白質 溶液,其中在該沈澱之步驟中係包含加入一硫酸銨水溶液 對該第一蛋白質溶液執行一透析之步驟,以得到一第 二蛋白質溶液,其中在該透析步驟中係包含加入一醋酸鈉 緩衝液; 執行一第一管柱層析步驟,以得到一第三蛋白質溶液 ,其中在該第一管柱層析步驟中係加入具有不同濃度之一 第一氯化鈉水溶液; 執行一第二管柱層析步驟,以得到一第四蛋白質溶液 ,其中在該第二管柱層析步驟中係加入具有不同濃度之一 第二氣化納水溶液;及 對該第四蛋白質溶液執行一膠體過濾層析步驟,以獲 得一凝集素。 19. 如申請專利範圍第1 8項所述之微藻親醣蛋白之純化方 法,其中上述之硫酸銨水溶液之重量百分比濃度為0-80 % 20. 如申請專利範圍第1 8項所述之微藻親醣蛋白之純化方 法,其中於上述之破胞步驟後,更包含執行複數次紅血球Page 27 200521136 VI. Application scope of a plurality of chlorella somatic cells; performing an extraction step on the broken chlorella somatic cells to obtain an extract; performing a precipitation of the extract Step to obtain a first protein solution, wherein the step of precipitating comprises adding a solution of ammonium sulfate to perform a dialysis on the first protein solution to obtain a second protein solution, wherein in the dialysis step It includes adding a sodium acetate buffer solution; performing a first column chromatography step to obtain a third protein solution, wherein a first sodium chloride having a different concentration is added in the first column chromatography step An aqueous solution; performing a second column chromatography step to obtain a fourth protein solution, wherein in the second column chromatography step, a second aqueous solution of sodium gasification having a different concentration is added; and The protein solution is subjected to a colloidal filtration chromatography step to obtain a lectin. 19. The method for purifying microalgal glycoproteins as described in item 18 of the scope of patent application, wherein the weight percentage concentration of the above ammonium sulfate aqueous solution is 0-80% 20. As described in item 18 of the scope of patent application A method for purifying microalgae glycoprotein, wherein after the cell breaking step described above, the method further comprises performing a plurality of red blood cells 200521136 六、申請專利範圍 凝集活性之檢測。 21. 如申請專利範圍第1 8項所述之微藻親醣蛋白之純化方 法,其中上述之萃取之步驟係包含加入一磷酸鹽緩衝液 (Phosphate buffer saline) 〇 22. 如申請專利範圍第1 8項所述之微藻親醣蛋白之純化方 法,其中上述之第一氯化鈉水溶液更包含以一濃度梯度之 方法沖提一蛋白質物質。200521136 6. Scope of patent application Testing of agglutination activity. 21. The method for purifying microalgal glycoproteins as described in item 18 of the scope of patent application, wherein the above-mentioned extraction step includes adding a phosphate buffer saline (Phosphate buffer saline) 〇 22. As the scope of patent application No. 1 The method for purifying a microalgal glycophilic protein according to item 8, wherein the first aqueous sodium chloride solution further comprises extracting a protein substance by a concentration gradient method. 23. 如申請專利範圍第18項所述之微藻親醣蛋白之純化方 法,其中上述之第二氯化鈉水溶液更包含以一濃度梯度之 方法沖提一蛋白質物質。23. The method for purifying a microalgal glycoprotein as described in claim 18, wherein the second aqueous sodium chloride solution further comprises extracting a protein substance by a concentration gradient method. 第29頁Page 29
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109797105A (en) * 2019-02-22 2019-05-24 中国科学院水生生物研究所 A kind of screening technique of microalgae cell wall mutant

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109797105A (en) * 2019-02-22 2019-05-24 中国科学院水生生物研究所 A kind of screening technique of microalgae cell wall mutant
CN109797105B (en) * 2019-02-22 2021-04-13 中国科学院水生生物研究所 Screening method of microalgae cell wall mutant

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