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TW581811B - Process for preparing lysozyme - Google Patents

Process for preparing lysozyme Download PDF

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Publication number
TW581811B
TW581811B TW86118081A TW86118081A TW581811B TW 581811 B TW581811 B TW 581811B TW 86118081 A TW86118081 A TW 86118081A TW 86118081 A TW86118081 A TW 86118081A TW 581811 B TW581811 B TW 581811B
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Taiwan
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lysozyme
protein
solution
kaolin
adsorption
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TW86118081A
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Chinese (zh)
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Min-Shiung Li
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Min-Shiung Li
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Abstract

The present invention provides a process for preparing lysozyme characterized by mixing the egg white or its diluted solution with diatomaceous earth, kaolin, zeolite or the mixtures thereof, and followed by eluting the adsorbed lysozyme with a salt solution. The diatomaceous earth, kaolin and zeolite can specifically adsorb the lysozyme in egg white, and the adsorbed lysozyme can be easily eluted with a salt solution.

Description

581811 欢、發明說明: 本發明係提供一種簡便而有效之製備溶菌酶的方 法。 溶菌酶在食品與醫療上有相當廣泛的用途。普遍應 用於,,保存及加工,常見者有牡蠣、蝦等水產品,豆 j、蔬菜、魚肉、水果等生鮮品、壽司、煮麵、魚丸、 貝丸、魚板等加工食品。此外,溶菌酶的添加也廣泛被 ,用在乳酪的製作上,溶菌酶具有如同凝乳酶之角色, 月b使牛乳中之赂蛋白不穩定而產生凝乳作用。 、、二過反復結晶精製、脫鹽、乾燥而得之純化溶菌 酉母二:製成錠狀、顆粒狀、舌片等形式而加以利用。例 如溶菌酶可作為慢性副鼻腔炎之傷口等之治療劑,以及 作為眼藥水等醫藥用品之保存劑。 ,581811 Description of the invention: The present invention provides a simple and effective method for preparing lysozyme. Lysozyme has a wide range of uses in food and medicine. It is generally used for, preservation and processing. Common products include aquatic products such as oysters, shrimps, fresh products such as beans, vegetables, fish, fruits, sushi, boiled noodles, fish balls, shell balls, and fish plates. In addition, the addition of lysozyme has also been widely used in the production of cheese, lysozyme has the role of rennet, and makes the protein in cow's milk unstable and produces rennet effect. The purified lysobacteria obtained through repeated crystallization, purification, desalting, and drying. 酉 Mother II: made into the form of ingots, granules, tongues, etc. and used. For example, lysozyme can be used as a therapeutic agent for wounds of chronic paranasal inflammation, and as a preservative for medical supplies such as eye drops. ,

雞蛋白中約含3·5%之溶gg|(乾重計),為製備溶 囷酉母之主要原料。目丽工業上生產溶菌酶之方法主要係 採用直接結晶法[Alderton, and Fev(Dld H LThe egg white contains about 3.5% soluble gg | (dry weight basis), which is the main raw material for the preparation of soluble gluten. The method of producing lysozyme in Muli industry is mainly by direct crystallization [Alderton, and Fev (Dld H L

Direct crystallization of lys〇zyme fr〇m egg white and some crystalline salts of lysozyme_ βι〇1_Direct crystallization of lys〇zyme fr〇m egg white and some crystalline salts of lysozyme_ βι〇1_

Chem. 1 04:1 ( 1 946 )]’此方法係於雞蛋白液中添加 氯化鈉,調整pH為9.5,加入少量晶種,然後置於4 °C結晶化,其溶菌酶回收率約60至8〇%。缺而,此方 法之回收率可能受原料量之影響甚鉅,張等之研究[張 珍田等。利用超過濾法純化雞蛋白溶菌酶之研究。中國 農業化學會該,24(0:86( 1 986),台北]使用7〇〇虬之 15564 5 雞蛋白液以同樣方本;隹并每 .„ , ^ , 進仃男、驗之結果顯示:第1次結晶 之回收率為4 3 · 〇 %,純化倍| & π ΙΛ- ^ 數為4. 9倍;兩次結晶時之 回收率降為1 2· 4%,純化彳立叙& 门从玄★, 數為7· 9倍;叁次結晶時之 回收率為11· 8%,純化倍數A Q, 旦々4。a 1σ歎為9· 1倍。此結果顯示較大 :之=可能顯著降低其回故率,純化倍數亦不甚理 m,/最大缺點為:分離溶菌酶後之大量蛋白液 、ι卜;,二之乳化鈉,因而無法再行有效之利用。為解 鹽量之問題,許多研究嘗試以超遽法進行溶 曰 苽寻之研九(冋上)顯示,一次超濾配合結 1二收率為47%,純化倍數為3.0; Chiang等人之研 hiang, B'H·' et Egg White lysozyme 7lflCatl〇n by ultl-afntrat1〇n and affxmty c romatography. J. Food Sci. 58(2):303(1993)]指 出以刀離分子篁3〇, 〇〇0之超濾膜處理後之溶菌酶回 收率為96%,但純化倍數僅6倍’顯示純化效果並不理 ,。此外’超遽'法之最大缺點為濾膜容易阻塞,有礙大 量生產。 - 此外’亦有利用吸附劑純化溶菌酶之研究,Chem. 1 04: 1 (1 946)] 'This method is to add sodium chloride to the chicken protein solution, adjust the pH to 9.5, add a small amount of seeds, and then crystallize at 4 ° C. The lysozyme recovery rate is about 60 to 80%. However, the recovery rate of this method may be greatly affected by the amount of raw materials. Zhang et al. [Zhang Zhentian et al. Study on Purification of Chicken Protein Lysozyme by Ultrafiltration. The Chinese Agricultural Chemical Society, 24 (0:86 (1 986), Taipei] uses 15564 chicken egg white solution in the same formula; and each .., ^, the results of the test are shown in male and male. : The recovery rate of the first crystallization is 43. 0%, the purification times | & π ΙΛ- ^ number is 4.9 times; the recovery rate during the two crystallizations is reduced to 12 · 4%, and the purification is performed. & Men Congxuan ★, the number is 7.9 times; the recovery rate during the three crystallizations is 11.8%, the purification factor is AQ, and the denier is 4. a 1σ sigh is 9.1 times. This result shows a larger: == It may significantly reduce its recovery rate, and the purification factor is not very reasonable. / The biggest disadvantage is: a large amount of protein solution and ιb after the lysozyme is separated; the second is the emulsified sodium, so it cannot be used effectively. To solve the problem of the amount of salt, many studies have attempted to dissolve the salt by the ultra-thin method (see above), which shows that the yield of a single ultrafiltration combined with 47 is 47%, and the purification factor is 3.0; the research by Chiang et al. hiang, B'H · 'et Egg White lysozyme 7lflCatl0n by ultl-afntrat10n and affxmty c romatography. J. Food Sci. 58 (2): 303 (1993)] pointed out that the molecule 篁 3 was removed by a knife. The recovery rate of lysozyme after 〇000 ultrafiltration membrane treatment is 96%, but the purification factor is only 6 times. It shows that the purification effect is irrelevant. In addition, the biggest disadvantage of the method is that the filter membrane is easily clogged. Hinder mass production.-In addition, there are also studies on the purification of lysozyme using adsorbents,

Alderton #[Alderton, etal. Isolation of lysozyme fr⑽ egg white. J. Bl0l· Chem· 1 57:43( 1 945)]發現 t 土(bentoni te)具有吸附溶菌酶之性質,但不易洗 出,必須以5%醋酸之吡啶溶液溶洗,不適合產業上之 生產。 本發明人為解決上述問題,經不斷深入研究之結 果,首先發現矽藻土、高嶺土及沸石等對溶菌酶具有優 異之選擇性吸附現象,而且吸附之溶菌酶很容易以離子 溶液洗出。此外,經吸附處理後之蛋白液具有與原蛋白 液相同之加工特性,且無任何添加劑之污染,能完全保 15564 6 持其利用性。本發明即基於上述發現而完成。 1式說明 第1圖示吸附劑用量對溶菌酶回收率之影塑。 第2圖示蛋白原液及經過三種吸附劑處理後之產 物的SDS-PAGE圖譜。Μ示標示蛋白質;i示蛋白原液; 2示蛋白原液經矽藻土處理者;3示蛋白原液經高嶺土 處理者;4示蛋白原液經沸石處理者。 第3圖示溶菌酶標準品(1)、蛋白原液(2)、經高嶺 土處理之產品(3 )、以及再經結晶處理(4)或再經陰離子 交換樹脂處理之產品的SDS-PAGE圖譜。 分析方法 1 ·蛋白質相對量之測定 將蛋白液經適當稀釋後以Hitachi公司製造之11- 1100 Spectrophotometer 測定 280nm 之吸光度(A280)., 並以此A28G之相對值計算蛋白質之吸附百分比。 2·蛋白質濃度之測定 採用Lowry法測定。 A 液:Na2C03 1 0g 與 NaHC03 2g 溶成 500mL。 B 液:1.6gCuS04.5H20 與 2.3g 檸檬酸納溶成 水溶液。 C液··取5 0mL A液與lmL B液,於使用前混合。Alderton # [Alderton, etal. Isolation of lysozyme fr⑽ egg white. J. Bl0l · Chem · 1 57:43 (1 945)] found that t soil (bentoni te) has the property of adsorbing lysozyme, but it is not easy to wash out. 5% acetic acid in pyridine solution is not suitable for industrial production. In order to solve the above-mentioned problems, the inventors have conducted in-depth research. First, they found that diatomite, kaolin, and zeolite have excellent selective adsorption of lysozyme, and the adsorbed lysozyme can be easily washed out with an ionic solution. In addition, the protein solution after adsorption treatment has the same processing characteristics as the original protein solution, without any contamination by additives, and can fully maintain its usability. The present invention has been completed based on the above findings. Explanation of Formula 1 The first figure shows the effect of the amount of adsorbent on the recovery of lysozyme. Figure 2 shows the SDS-PAGE spectra of the protein stock solution and the products treated with the three adsorbents. M shows labeled protein; i shows protein stock solution; 2 shows protein stock solution treated with diatomaceous earth; 3 shows protein stock solution treated with kaolin; 4 shows protein stock solution treated with zeolite. Figure 3 shows the SDS-PAGE spectra of lysozyme standard (1), protein stock solution (2), kaolin-treated product (3), and product recrystallized (4) or anion exchange resin. Analytical method 1 · Determination of relative amount of protein After proper dilution of the protein solution, the absorbance at 280 nm (A280) was measured with an 11-1100 Spectrophotometer manufactured by Hitachi, and the relative value of A28G was used to calculate the protein adsorption percentage. 2. Measurement of protein concentration The Lowry method was used for measurement. Solution A: Na2C03 1 0g and NaHC03 2g are dissolved into 500mL. Solution B: 1.6g of CuS04.5H20 and 2.3g of sodium citrate were dissolved into an aqueous solution. Liquid C ... Take 50 mL of liquid A and 1 mL of liquid B and mix before use.

Fol in-Ciocal teu’ s S分試劑:使用前加入2倍體積 洛鶴水稀釋之。 取經適當稀釋之樣品液〇. 2niL,加入C液lmL,混 15564 7 合均句後於室溫下反應30分鐘,再加入F〇lln,s溶液 0 · 1 m L ’於至溫下反應6 0分鐘,測6 5 0 n m之吸光值,與 標準曲線比對求出樣品中之蛋白質含量。 標準曲線是以50至400/zg/niL之牛血清白蛋白為 標準溶液作出。 3·溶菌酶活性之測定Fol in-Ciocal teu ’s S: Dilute it by adding 2 volumes of Luohe water before use. Take 0.2 niL of the appropriately diluted sample solution, add 1 mL of solution C, mix with 15564 7 and then react at room temperature for 30 minutes, then add Folln, s solution 0 · 1 ml L 'to react at room temperature 6 At 0 minutes, the absorbance at 650 nm was measured and compared with the standard curve to determine the protein content in the sample. The standard curve was prepared using bovine serum albumin at 50 to 400 / zg / niL as the standard solution. 3 · Determination of lysozyme activity

將 Micrococcus lysodeikticus 菌體懸浮於 〇. 〇67Μ 之磷酸緩衝液中(20mg/100niL,ρΗ6·3),取出菌液2. 97mL 置於石央中’加入3 # L酵素液,混合均勻後,於室 溫測定450ηπι波長之吸光變化值,每3〇秒記錄一次, 持績2 0分鐘。 * 一單位溶菌酶活性係指於上述條件下,每分鐘能水解 菌體使吸光值下降〇· 〇〇丨單位之酵素量。Micrococcus lysodeikticus cells were suspended in 0.067M phosphate buffer solution (20mg / 100niL, ρΗ6.3 · 3), and 2.97mL of the cell liquid was taken out and placed in Shiyang '. Add 3 # L enzyme solution, mix well, The change in absorbance at 450nm was measured at room temperature, recorded every 30 seconds, and held for 20 minutes. * One unit of lysozyme activity refers to the amount of enzyme that can hydrolyze bacteria to reduce the absorbance per minute under the above conditions.

0.001 OD/minx〇.03mL 4. SDS-PAGE電泳分析 分離膠體採用膠體濃度15%者,而焦集膠體之膠體 濃度為4%。取ΙΟ" !樣品溶液(濃度約4mg/mL),加1〇 // 1樣品緩衝液(註丨)及4 v丨之追蹤染料溶液(註2), 然後於1 0 0 C下加熱5分鐘後,冷卻至室溫,進行電泳 分析。膠體中蛋白質帶以CoomassieBrilliantBlueR 染色,並以醋酸-甲醇-水(1 〇 : 2 〇 : 7 〇)脫色至呈背景透 明’然後進行乾片並予以保存。 註1 : SDS-PAGE樣品緩衝溶液(2χ )0.001 OD / minx 0.03mL 4. SDS-PAGE electrophoresis analysis The colloid concentration of 15% is used for separating colloids, and the colloid concentration of coke colloid is 4%. Take ΙΟ "! sample solution (concentration of about 4mg / mL), add 1/10 sample buffer (Note 丨) and 4v 丨 trace dye solution (Note2), and then heat at 100 ° C for 5 minutes After that, it was cooled to room temperature and analyzed by electrophoresis. The protein bands in the colloid were stained with CoomassieBrilliantBlueR and decolorized with acetic acid-methanol-water (10: 20: 7) to have a transparent background ', then dried and stored. Note 1: SDS-PAGE sample buffer solution (2χ)

TrisCTrizma Base, 125mMx2) 3. Ogm 8 15564 581811 EDTA-2Na(2mMx2) 14·8mg SDS(2%x2) 4.0gm —2-巯基乙醇_i 〇_ 〇mi 加水80ml溶之,pH調到6. 8,加水至1 00ml稀釋2 倍後使用。 註2 :追蹤染料溶液: 溴酚藍大約1 mg (稱量不需十分準確) 溶於5m 1水,加5m 1甘油混合均勻。 5 ·吸附後廢蛋白功能性測定 (A)蛋白質發泡力及泡珠安定性測定 取50 ΐ:升吸附後之蛋白液置入毫升容量之量 筒内’用石壤紙封緊後以手搖方式垂直來回振盪1分鐘 (2次/秒),測定所得泡沫體積(mL)即為發泡力(f oam expansion)。靜置30分鐘後再測定殘留泡沫體積,π 殘留體積與原來體積之百分率比值表示其泡沫安定 性0 (Β)蛋白乳化安定性之測定 取25毫升吸附後之蛋白液置於50mL容量之量筒, 加入25毫升大豆油,於12,〇〇〇rpm均質1分鐘,立即 測定水層高度(Mo),然後於室溫下放置3 0分鐘,再測 定其水層高度(Mt),然後以下式計算其乳化安定性。 50 - Mt 乳化安定性(%)= '^ X 100% 50 - Mo 實施例及試驗例 9 15564 心以下11實施例及試驗例對本發明内容作進—步之具體 。兄月,但本發明並非限 明之每所 限制於k些貫施例。只要是利用本發 〜男'貝精神者,均應屬於本發明之範圍。 將雞蛋白液以基飽^接^罢 、居 …蝻水稀釋5倍,攪拌混合後以紗布過 率及被吸附蛋白質之溶菌酶比活性及理論上之純化倍數。 結果如表1所示。TrisCTrizma Base, 125mMx2) 3. Ogm 8 15564 581811 EDTA-2Na (2mMx2) 14.8mg SDS (2% x2) 4.0gm —2-mercaptoethanol_i 〇_ 〇mi dissolved in 80ml water, the pH was adjusted to 6.8 , Add water to 100ml and dilute it twice before use. Note 2: Trace dye solution: Bromophenol blue is about 1 mg (we don't need to be very accurate for weighing). Dissolve in 5m 1 of water, add 5m 1 of glycerin and mix well. 5 · Functional determination of waste protein after adsorption (A) Determination of protein foaming power and stability of vesicles Take 50ΐ: liter of protein solution after adsorption is placed in a milliliter volumetric cylinder, sealed with stone soil paper, and then shaken by hand The method oscillates vertically back and forth for 1 minute (2 times / second), and the obtained foam volume (mL) is the foam expansion (foam expansion). Measure the residual foam volume after standing for 30 minutes. The ratio of π residual volume to the original volume indicates its foam stability. 0 (B) Determination of protein emulsification stability. Take 25 ml of the adsorbed protein solution and place it in a 50 mL measuring cylinder. Add 25 ml of soybean oil, homogenize at 12,000 rpm for 1 minute, immediately measure the water layer height (Mo), then leave it at room temperature for 30 minutes, then measure the water layer height (Mt), and then calculate it by the following formula Its emulsification stability. 50-Mt Emulsification stability (%) = '^ X 100% 50-Mo Examples and test examples 9 15564 The following 11 examples and test examples make the content of the present invention further-specific. Brother, but the present invention is not limited to every embodiment. Anyone who uses the spirit of the present invention should fall within the scope of the present invention. Dilute the chicken protein solution with a base solution, dilute it 5 times with water, stir and mix with the gauze pass rate and the lysozyme specific activity of the adsorbed protein and the theoretical purification multiple. The results are shown in Table 1.

吸附劑 未吸附蛋白 質百分率(%) 未吸附溶菌 酶百分率(%) 蛋白質 吸附率(%) 溶菌酶活性 吸附率(%) :除黏性團塊物f,必要時可加以離心處理。取蛋白稀 _ 〇〇mL,分別添加5g不同之吸附劑(皂土、矽藻土、 、=及’弗石,均為Sl§me公司產品),於室溫下處理3〇 1麵其間偶而加以搖動混合。離心(丨,〇⑼以5— η)分離上 清液。測定上清液及原蛋白液之溶菌酶活性及28〇nm之吸 光度㉟據測疋值推异蛋白質之吸附率、;容菌酶活性吸附 純化 倍數 原液 皂土 矽蕩土 高嶺土 沸石 100 100 47.18 96.73 94.02 95.82 0 0 0 49 52.82 3.27 5.98 4.18Sorbent Unabsorbed protein Percentage (%) Unadsorbed lysozyme Percentage (%) Protein Adsorption rate (%) Lysozyme activity Adsorption rate (%): In addition to the sticky mass f, it can be centrifuged if necessary. Take protein dilute OOmL, add 5g of different adsorbents (bentonite, diatomaceous earth, and =, and "Fu Shi, all products of Sl§me company), and treat 301 side occasionally at room temperature. Shake to mix. The supernatant was separated by centrifugation (5, n). Measure the lysozyme activity and absorbance at 28nm of the supernatant and the original protein solution. According to the measured value, the adsorption rate of different proteins is deduced; the bacterial enzyme activity is adsorbed and purified. The original solution is bentonite siliceous soil kaolin zeolite 100 100 47.18 96.73 94.02 95.82 0 0 0 49 52.82 3.27 5.98 4.18

100 100 100 51 1.89 26.88 16.72 12.20 15564 10 581811 由表1結果可知,ο 、 但是,對於溶=菌酶之吸附性雖然报強, 性不佳,由計笞 貝的吸附性亦強,因此選擇 高至U9倍。:對:破吸附之蛋白質的溶菌酶比活性僅提 質則大部分為溶菌酶,’::、二高嶺土及彿石吸附之蛋白 倍、㈣倍及12.2。倍::::r:序㈣ 附具有優異之選擇性,亦g τ ★:種吸附劑對溶菌酶之。及 於溶菌酶之製備。’、P上述二種吸附劑可有效地應用 t施例2 各取lOOmL稀釋5仵走 怦)借之蛋白液,分別以 矽藻土、高嶺土及彿石依實施例 g… 授,廿、目丨丨令卜、主、六 ^方法進行吸附處 另:溶菌酶活性’藉此計算被吸附之溶菌 百分率。另外’將離心沈殿之各吸附劑分別: 1M NaCl洗提溶菌酶(室溫,7 ς ,e ,a 心坶(至/皿,75rpm振盪3〇分鐘)。離心集洗=1定其溶_活性。然後計算以各吸附劑處理 後之溶菌酶回收率及自吸附劑之洗提率。結果如表2所 示0 _表2初^純化溶^酶之吸附劑篩選試驗 吸附劑 溶菌酶吸附率(%) 皂土 矽藻土 南領土 沸石 100 100 100 50.88 溶菌酶回收率(%) 82.23 90.70 49.05 溶菌酶之 洗提率(%) 0 82.23 90.70 96.40 15564 11 上述表2之結果顯示,I 土 ^ 危、1、, f〉谷菌酶之吸附力極強, …、法以1M NaCl洗出。本發明所 一 一山 、波工μ 之用之石夕藻土、咼嶺土及 那石寺吸附劑所吸附之溶菌酶則 皮八^ 脚⑷很各易洗出,其洗提率依 序刀別為 82.23%、90·70〇/〇及 96·4〇% 0 實施例 3 取l〇〇mL稀釋5倍之蛋白液,八 # _ 、 分別添加1至5 g之矽 澡土或高嶺土,或2至12 ζ之洮r , g f石,然後依實施例1之相 同方法進行吸附處理。經離心分離上清液後,各吸附劑分 別以m社之1M NaC1洗提被吸附之溶菌酶(75_, …25 c )。離心收集洗提液,測定其溶菌酶活性之回 收率’結果如第i圖所示。帛i圖結果顯示,對每1〇〇社 5倍稀釋之蛋白液而言’矽藻土及高嶺土只要使用4g即可 回收幾乎1GG%之溶菌酶(亦即,蛋白原液對吸附劑之比例 :、 )'弗石則需使用8 g (亦即蛋白原液對吸附劑之比j列 為10 . 1)才可達到最高溶菌酶回收率,約為50%。 實施例4 取1 〇〇mL稀釋5倍之蛋白液,分別添加4g之矽藻土 或南嶺土’或之沸石,然後依實施例3之相同方法進行 吸附及洗提處理,但使用之洗提液分別改為不同濃度之 MaCl /谷;夜。然後測定洗提液中溶菌酶之回收率,結果如表 J所不。表3之結果顯示,使用1M之NaCl洗提可回收大 部分被吸附之溶菌酶,使用矽藻土、高嶺土及沸石之溶菌 酶/舌性回收率依序分別為86〇1%、90.12%及51.69%。 12 15564 581811 表3氣化納道庙 -一辰度對溶洗效果之影響100 100 100 51 1.89 26.88 16.72 12.20 15564 10 581811 From the results in Table 1, it can be seen that ο, but although the adsorption to lysozyme is reported to be strong, the performance is not good, and the adsorption of tadpoles is also strong, so choose high To U9 times. : Yes: The specific activity of the lysozyme that breaks the adsorbed protein is mostly lysozyme, and ‘::, double kaolin and fossil adsorbed protein times, times and 12.2. Times :::: r: Xuan Yu Fu has excellent selectivity, also g τ ★: a kind of adsorbent for lysozyme. And in the preparation of lysozyme. ', P The two adsorbents mentioned above can be effectively used. Example 2 Take 100mL each and dilute 5 仵 to remove the protein solution borrowed, using diatomaceous earth, kaolin, and Buddhist stones according to Example g ...丨 丨 Order, main, and six methods are used for adsorption: Lysozyme activity 'is used to calculate the percentage of lysobacteria adsorbed. In addition, each adsorbent of Shen Dian Centrifuge was centrifuged: 1M NaCl was used to elute lysozyme (room temperature, 7 d, e, a palpitate (to / dish, shake at 75 rpm for 30 minutes). Centrifugal wash = 1 to determine its dissolution_ Activity. Then calculate the recovery rate of lysozyme after treatment with each adsorbent and the elution rate of self-adsorbent. The results are shown in Table 2 _Table 2 Preliminary ^ purified lysozyme sorbent screening test sorbent lysozyme adsorption Rate (%) Bentonite diatomaceous earth zeolite 100 100 100 50.88 Recovery rate of lysozyme (%) 82.23 90.70 49.05 Extraction rate of lysozyme (%) 0 82.23 90.70 96.40 15564 11 The results in Table 2 above show that I soil ^ Wei, 1 ,, f> glutenase has a very strong adsorption force,…, and washed out with 1M NaCl. Shi Xi algae soil, Mo Ling soil and Na Shi Temple used in the present invention for a mountain, wave industry μ. The lysozyme adsorbed by the adsorbent is very easy to wash out. The elution rate is 82.23%, 90.70 // and 96.40% in order. Example 3 Take l. 〇mL diluted 5 times the protein solution, eight # _, add 1 to 5 g of silica bath or kaolin, or 2 to 12 洮 r, gf stone, and then according to Example 1 Adsorption treatment was performed in the same way. After the supernatant was separated by centrifugation, each adsorbent was used to extract the adsorbed lysozyme (75_,… 25 c) with 1M NaC1 of m company. The eluate was collected by centrifugation, and its lysozyme activity was measured. The results of the “recovery rate” are shown in FIG. I. The results of the “i” graph show that for each protein solution diluted 5 times, the diatomite and kaolin can recover almost 1GG% of lysozyme by using 4 g (That is, the ratio of protein stock solution to adsorbent :,) 'Fu Shi requires 8 g (that is, the ratio of protein stock solution to adsorbent j is 10.1) to achieve the highest lysozyme recovery, approximately 50% Example 4 Take 100 mL of a 5-fold diluted protein solution, add 4 g of diatomite or Nanling'or zeolite, and then perform adsorption and elution treatment in the same manner as in Example 3, but The eluent used was changed to different concentrations of MaCl / Valley. Then, the recovery of lysozyme in the eluent was measured, and the results are not as shown in Table J. The results in Table 3 show that the elution using 1M NaCl can be recovered. Most adsorbed lysozyme, using diatomite, kaolin and zeolite / Tongue of sequential recoveries were 86〇1%, 90.12% and 51.69% 1215564581811 Table 3 Road Temple gasification satisfied - Effect of an e-wash effect of lytic

NaCl濃度 (Μ) 0 0.25 2 7 0.50 4 0.75 43 1.00 86 f施例5 溶菌酶回收率(%)NaCl concentration (M) 0 0.25 2 7 0.50 4 0.75 43 1.00 86 f Example 5 Recovery rate of lysozyme (%)

0 0 高嶺土 29.18 58.10 78.96 90.12 34.27 42.13 41.57 51.69 取2 00mL經5倍稀雜+ a 稀釋之雞蛋白均質液’分別加入8 石夕藻土、8克高嶺土或16克彿石,置於水浴振盡器 勻反應(75rpmx30min,25〇r、雜 " ^C) ’ 離心(1,000gx 5min),水 沈殿,離心、,再以15G毫升1MNaa分三次反覆洗出蛋令 質,測定總蛋白質濃度與溶菌酶活性,並作電泳分析。 、一結果如表4所示,以矽藻土、高嶺土及海石為吸附劑 ^劑酶回收率依序分別為82%、98%及54%;纯化倍數 則为別為17.05倍、Μ.” 1〇及-乜。頒不此三種吸附 ^句具有優異之純化效果。 表4 以三種吸附劑分別 之比較 自五倍稀釋雞蛋液中分離溶菌酶 15564 13 須lj试樣品 比活性 (U/mg) 純化倍數 溶菌酶回' 率(%) >倍稀釋之 要白液 516 1 矽藻土 高嶺土 ;弗石 ^- 8798 10273 1 0757 17.05 19.91 20.85 82 98 54 使用上述三種吸著劑進行純化所得溶菌酶之SDS-pAGE〆分析口圖譜如第2圖所示。第2圖中i號為蛋白原液 厶圜譜,呈色帶以UKd附近之色帶為主成分,在l4.4Kd 附近=溶菌酶則幾乎不呈現可見之色帶,表示蛋白原液中 滚g酶=量相對地很少。2、3及4號樣品係分別經由矽藻 土 鬲袅土及沸石處理精製之產品的SDS-PAGE圖謂,二 耆均顯示以l4.4Kd附近之溶菌酶色帶為主成分,而原先 為主要成分之43 Kd附近的色帶則變為微量成分。此結涞 顯示上述三種吸附劑對溶菌酶具有優異之選擇性吸附作 用。 f施例6 使用高嶺土為吸附劑,依照實施例5之相同方法製備 溶菌酶。然後依下列方法分別進一步進行陰離子交換樹脂 處理或溶菌酶之結晶處理。 (1)以陰離子交換樹脂之純化處埋 取1克陰離子交換樹脂(Amberlyst A-207,〇H-型,曰 本Organo公司)’以蒸餾水洗至pH8至9左右,加入已經 吸附純化且透析過之酵素液1〇毫升’於室溫下處理1小二 15564 14 時。取上清液測總蛋白質量和溶菌酶活性,並作電泳分析。 (2)溶菌酶之結晶化 取經吸附純化、並絲和#、皆、曲W / 、、二超過濾)辰縮6倍之酵素液,調整 P值至9 · 5加入J终結晶性溶菌酶,放置於4下,待 結士…’離心收集溶菌酶之結晶,並測定蛋白質含量 及〉谷囷酶活性。 疋處:刖處理後之樣品的蛋白質含量及溶菌酶活 …後°十:其比活性、純化倍數及溶菌酶之回收率。結 果如表5所不。此結果顯示上述兩種處理均能進—步純化 溶菌酶,其純化倍數可提高至”至28倍。 將上述純化之溶菌酶進行SDS邛織分析,結果如第 圖匕、°果顯不上述經過陰離子交換樹脂處理或結晶化 處理之洛囷酶均呈單一色帶,與市售之純化溶菌酶 a司產扣)相同。此結果表示上述純化之兩種產品 溶菌酶。 & 比活性 辺/mg) 722 純化倍數 ---—-—_ 回收率 —_ 1 3 527 18.74 88.04 20375 28.22 80.98 1 9724 27.32 68.27 原液 南領土吸附 精製 高嶺土吸附 精製+0 0 Kaolin 29.18 58.10 78.96 90.12 34.27 42.13 41.57 51.69 Take 2OmL of chicken egg homogeneous solution diluted 5 times + a, and add 8 Shi Xi algae soil, 8 g kaolin clay or 16 g Buddha stone, put them in the water bath and shake them up Shake the reaction (75rpmx30min, 25 ° C, ^ C) 'Centrifuge (1,000gx 5min), water sink, centrifuge, and then wash the egg protein repeatedly with 15Gml 1MNaa three times to determine the total protein concentration and Lysozyme activity was analyzed by electrophoresis. 1. The results are shown in Table 4. Using diatomite, kaolin and sea stone as adsorbents, the enzyme recovery rates were 82%, 98%, and 54%, respectively; the purification multiples were 17.05 times, M, respectively. "10 and-乜. The three adsorptive sentences have excellent purification effect. Table 4 Isolation of lysozyme from a five-fold diluted egg solution by comparing three adsorbents respectively 15564 13 Specific activity of the test sample (U / mg) Purification factor lysozyme recovery rate (%) > Double dilution of the white liquor 516 1 diatomite kaolin clay; fusi ^-8798 10273 1 0757 17.05 19.91 20.85 82 98 54 Purified using the above three sorbents The SDS-pAGE〆 analysis profile of lysozyme is shown in Figure 2. Figure i shows the protein stock solution 厶 圜. The color band is mainly composed of the band near UKd, and is near l4.4Kd = lysozyme Enzymes hardly show a visible color band, indicating that the amount of enzyme in the protein stock solution is relatively small. Samples 2, 3, and 4 are SDS-PAGE of the refined products treated with diatomaceous earth and zeolite, respectively. The figure shows that the two stilbene shows that the lysozyme band near l4.4Kd is the main component, while the original The color band near 43 Kd of the component becomes a trace component. This result shows that the above three adsorbents have excellent selective adsorption of lysozyme. FExample 6 Using kaolin as an adsorbent, the same method as in Example 5 was used Preparation of lysozyme. Then proceed to anion exchange resin treatment or lysozyme crystallization treatment according to the following methods. (1) Embed 1 g of anion exchange resin (Amberlyst A-207, 0H-type, (Organo Co., Ltd.) 'washed with distilled water to a pH of about 8 to 9, and added 10 ml of the enzyme solution that has been purified, purified and dialyzed', and processed at room temperature for 15 hours at 14 pm 14. Take the supernatant and measure the total protein mass and The lysozyme activity was analyzed by electrophoresis. (2) Crystallization of lysozyme: Take the enzyme solution purified and adsorbed and bound, and #, Jie, Qu W /, and two ultrafiltration) to reduce the enzyme solution 6 times, adjust the P value to 9 5 Add J final crystalline lysozyme, place 4 times, and wait for the results ... 'Centrifuge to collect the lysozyme crystals, and determine the protein content and glutenase activity. Where: The protein of the treated sample Amount and lysozyme activity ... After ° 10: Its specific activity, purification factor and recovery of lysozyme. The results are shown in Table 5. This result shows that the above two treatments can further purify the lysozyme, and the purification factor can be further improved. Increase to "to 28 times. The purified lysozyme was subjected to SDS weaving analysis. As shown in the figure, the results showed that the above-mentioned locustases treated with anion exchange resin or crystallized all showed a single color band, and were commercially available with purified lysozyme a Division production deduction) same. This result indicates that the two products purified above were lysozyme. & Specific activity 辺 / mg) 722 Purification multiple --------_ Recovery rate --_ 1 3 527 18.74 88.04 20375 28.22 80.98 1 9724 27.32 68.27 Stock solution Southern Territories adsorption Refined Kaolin adsorption Refined +

Amberlyst A- 27(ΟΗ·)處理 高嶺土吸附 精製+ 結晶處理 15564 15 581811 試驗例 將經過本發明使用之三種吸附劑處理後之三種蛋白、夜 依刖述記載之方法測定其加工功能性,亦即發泡力、泡、、末 安疋性及乳化安定性,並與原蛋白液比較。結果如表6所 不。表6結果顯示,上述經吸附處理後之蛋白液均仍然具 有相當良好的加工功能性。 又’本發明使用之吸附劑均係食品加工上合 劑,經此類吸附劑處理後之蛋白液仍然可安全使用。由、 未添加鹽或其他任何添加劑,因此仍可廣泛作為人由於 使用。 , ”、、㊅品成分 表·…6 吸附前後功能性質的比較 ' ' ~--—-— 功能性 雞蛋白種類Amberlyst A- 27 (〇Η ·) treatment kaolin adsorption purification + crystallization treatment 15564 15 581811 Test example The processing functionality of the three proteins after the treatment with the three adsorbents used in the present invention and the method described in the following is described, that is, Foaming power, foam, foam stability and emulsification stability, and compared with the original protein solution. The results are shown in Table 6. The results in Table 6 show that the above-mentioned protein solutions after adsorption treatment still have fairly good processing functionality. Furthermore, the adsorbents used in the present invention are all food processing mixtures, and the protein solution treated by such adsorbents can still be used safely. Because it has no added salt or any other additives, it can still be widely used as a human. 、 、、, and counterfeit ingredients Table ·… 6 Comparison of functional properties before and after adsorption '' ~ --- --- Functional egg protein types

17.5 64 7 1-4317.5 64 7 1-43

蛋白原液 石夕藻土處理 者 高嶺土處理 者 72 〉弗石處理者 發明效^ 本發明使用之三種吸附劑斜 J主丁 /合囷酉母具有良好夕、技加 吸附能力,可簡便而有效地用 之·、擇 %衣備溶囷酶。以雞疋二 原料’使用上述三種吸附劑進 、 !及1打㈠運仃溶菌酶製 地提高比活性至17俾以卜,而 K衣爾^,可顯 ”。以上’而且溶菌酶之回收率高,分 15564 16 581811 約為80%以上(使用矽藻土時),90%以上(使用高嶺 及5 0%以上(使用沸石時)。進一步配合結晶化處理 子交換樹脂處理,則可製得在SDS-PAGE分析圖譜 一色帶之純化溶菌酶。 土時) 或陰離 中呈單 17 15564Protein solution liquid stone diatomaceous earth processor Kaolin clay processor 72〉 Effective effect of the stone processor ^ The three adsorbents used by the present invention, oblique J, main compound / combined mother, have good adsorption ability, and can be easily and effectively added Use ·, choose% clothing to prepare lysozyme. Use chicken gluten two raw materials' using the above three adsorbents to improve the specific activity to 17 仃 lysozyme to increase the specific activity to 17 俾, and K Yier ^, can be "above" and the recovery of lysozyme It has a high rate of 15564 16 581811, which is about 80% or more (when using diatomite), 90% or more (when using kaolin and 50% or more (when using zeolite). Further crystallization treatment and sub-exchange resin treatment can be prepared. The purified lysozyme can be obtained in a band of SDS-PAGE analysis map (in the case of soil) or in a shade of 17 15564

Claims (1)

5mii 附 公告本 m*m w ·ΡΙ II <1 丨· _5mii with bulletin m * m w · PI II < 1 丨 · _ 第86 1 1 808 1號專利申請案 .申請專利範圍修正本 (92年10月21曰) 1. 一種製備溶菌酶之方法,其特徵為_使用矽藻土、高嶺土、 沸石或其混合物選擇性地吸附蛋白中之溶議酶,及隨後 以中性鹽類溶液進行洗提。 2. 如申請專利範圍第1項所述之製備溶菌酶之方法,其 中,該鹽類之溶液係氯化鈉之溶液者。 3 .如申請專利範圍第1或2項所述之製備溶g酶之方法, 其中,係進一步以結晶方法純化者。 4.如申請專利範圍第1或2項所述之製備溶議酶之方法, 其中,係進一步以陰離子交換樹脂純化者。 15564Patent application No. 86 1 1 808 1. Amended version of patent application scope (October 21, 1992) 1. A method for preparing lysozyme, characterized by using diatomite, kaolin, zeolite or mixture thereof It adsorbs the lysozyme in the protein and then elutes it with a neutral salt solution. 2. The method for preparing a lysozyme as described in item 1 of the scope of the patent application, wherein the solution of the salt is a solution of sodium chloride. 3. The method for preparing lysozyme as described in item 1 or 2 of the scope of patent application, wherein it is further purified by crystallization. 4. The method for preparing a lysozyme as described in item 1 or 2 of the scope of patent application, wherein the method is further purified by an anion exchange resin. 15564
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