低pH孵放法灭活静注人免疫球蛋白中脂包膜病毒效果验证的研究

选用不同核酸类型的脂包膜病毒,其中RNA病毒为水疱性口炎病毒(VSV),DNA病毒为伪狂犬病毒(PRV),将两种指示病毒分别用于验证低pH孵放法对不同厂家生产的人血静脉注射用丙种球蛋白(IVIG)的病毒灭活效果。结果表明,液体IVIG的pH值为3.8～4.4,在23～25℃环境中,孵放21天可灭活VSV和PRV,两种指示病毒的灭活效果分别为≥5.50～6.62和≥5.38～6.62logTCID50/0.1ml。因此,低pH孵放法是一种安全、有效且简便实用的灭活脂包膜病毒的方法。     

S/D法灭活血液制剂中脂包膜病毒效果验证的研究

选用不同核酸的脂包膜病毒,其中RNA病毒为水疱性口炎病毒(VSV),DNA病毒为伪狂犬病毒(PRV),将两种指示病毒分别用于验证S/D法处理对纤维蛋白原、凝血酶原复合物、凝血因子Ⅷ、静注丙种球蛋白、免疫血浆等血液制剂的病毒灭活效果。结果该法对所有被处理的血液制剂中的PRV及VSV灭活能力分别为≥3.38~5.88和≥3.50~4.75logTCID50/0.1ml,表明S/D法对两种病毒核酸类型的脂包膜病毒有良好的灭活效果。     

S／D处理血浆过程中的脂包膜病毒灭活试验观察

通过有机溶剂/去污剂对血浆中指示病毒VSV灭活的观察评估有机溶剂/去污剂对脂包膜病毒死活的效果。血浆样品与VSV病毒按9:1混合,然后用1％TNBP/1％ Triton X-100在30℃处理4h,测定开始样品中的病毒总量和S/D处理后不同时间取样内的病毒总量。实验中样品内加入1％TNBP/1％ Triton X-10015min后VSV病毒已全部灭活,灭活效果≥6.0log。按所述S/D处理方法可以完全灭活血浆内所有的脂包膜病毒而没有主要血浆蛋白的损失。     

S／D法处理凝血因子浓缩物类制品的病毒灭活验证

以水泡性口炎病毒 (VSV)为指示病毒 ,验证应用有机溶剂 /去污剂 (简称S/D)法灭活血液制品中病毒的生产工艺 ,并对不同厂家不同批号的四种凝血因子浓缩物类制品 (中间品 )的病毒灭活效果进行了分析总结。结果表明当制品中TNBP和Tween80终浓度为 0 3%和 1 0 % ,在 2 5± 1℃处理 6小时后对于包膜病毒确有显著的灭活效果。     

低pH孵放法对马破伤风免疫球蛋白F(ab′)_2病毒灭活效果的验证

目的采用低pH孵放法对马破伤风免疫球蛋白F(ab′)_2样品中辛德毕斯病毒(sindbis virus, SINV)、水疱性口炎病毒(vesicular stomatitis virus, VSV)、脑心肌炎病毒(encephalomyocarditis virus, EMCV)的灭活效果进行验证。方法以SINV、VSV、EMCV作为指示病毒,将3批马破伤风免疫球蛋白F(ab′)_2的pH调至4.1±0.1,每批12瓶(3 mL/瓶),分别加入333μL指示病毒,25℃放置21 d灭活病毒,同时设置中性对照和阳性对照,并于0 d、1 d、3 d、7 d、14 d、21 d取样测定剩余病毒滴度,验证低pH孵放法的病毒灭活效果。结果马破伤风免疫球蛋白F(ab′)_2样品经低pH孵放处理21 d后,SINV、VSV和EMCV等3种指示病毒残余病毒滴度均≤0.5 lgTCID_(50)/0.1 mL,灭活效果分别达到5.50～5.83、5.70～6.00和6.00～6.17 lgTCID_(50)/0.1 mL。结论采用低pH孵放法处理马破伤风免疫球蛋白F(ab′)_2中SINV、VSV、EMCV,病毒滴度下降值均>4 lgTCID_(50)/0.1 mL,灭活效果较好。     

板层人工角膜辐照法病毒灭活验证方法的建立及灭活效果验证

目的建立板层人工角膜钴-60照射病毒灭活验证方法,用该方法对脂包膜病毒灭活效果进行验证。方法以伪狂犬病毒(pseudorabies virus,PRV)为指示病毒,将干燥的板层人工角膜浸泡在高滴度病毒液中,在2~8℃浸泡5 h,经剪碎、研磨等步骤后4℃放置12 h,确立角膜吸附和释放病毒的条件。之后,将吸附病毒并呈干燥状态的角膜以0、5、10、15、20、25 k Gy辐照剂量进行钴-60辐照,以确立的条件释放病毒并进行滴定,考察灭活效果。结果板层角膜在2~8℃浸泡5 h可吸附足量病毒;病毒滴度可达到4 lg值以上,满足病毒灭活验证的要求。样品经25 k Gy剂量钴-60照射后灭活PRV为2.75~3.25 lg TCID50/100μL,灭活后的样品在敏感细胞上盲传3代均未出现细胞病变。结论成功建立了板层人工角膜病毒灭活验证的方法,并验证采用钴-60辐照法对PRV有较好的灭活效果。     

S/D灭活血浆内脂包膜病毒及病毒灭活血浆的研究

研究磷酸三丁酯(TNBP)／Triton X-100对血浆内脂包膜病毒的灭活效果。用VSV病毒和Sindbis病毒作指示病毒,加入血浆后再加磷酸三丁酯／Triton X-100,观察病毒的滴度变化及对血浆蛋白的影响。结果发现终浓度各为1％的磷酸三丁酯／Triton X-100在60min内可以灭活血浆内的两种指示病毒,而血浆蛋白的组成和功能变化很小。经层折、超滤后血浆内磷酸三丁酯和Triton X-100的残余量分别低于5μg/ml,表明S／D处理血浆的安全性和治疗作用都很好,其制剂冰冻血浆或冻干血浆可用于临床治疗凝血因子缺乏症,或用作血容量扩张剂。     

重组乙型肝炎疫苗(CHO细胞)生产工艺病毒灭活验证

目的:验证重组乙型肝炎疫苗(CHO细胞)生产工艺灭活病毒能力,评价疫苗安全性。方法:将乙型肝炎疫苗原液按1∶9比例加入指示病毒(麻疹病毒、VSV病毒),混匀后加入甲醛溶液,使甲醛终浓度达到1/2000和1/4000,放置于37℃,分别于0h、24h、48h、72h取样,用亚硫酸氢钠中和,贮存于-70℃待检或立即检测病毒滴度,对病毒检测阴性的样品盲传3代,进一步检测。结果:疫苗原液加入1/2000和1/4000的甲醛溶液,37℃作用24h、48h、72h,麻疹病毒滴度下降4.0个Log值,VSV病毒滴度下降5.0个Log值,且细胞盲传三代,均未出现细胞病变。结论:乙型肝炎疫苗原液在1/2000和1/4000甲醛浓度37℃72h作用下,均能有效灭活麻疹病毒和VSV病毒。     

冻干加热处理凝血因子类制剂的病毒灭活验证

在病毒灭活验证过程中,比较了冻干后不同加热方法对凝血因子类制剂中伪狂犬病毒(PRV)的灭活效果,包括80℃干烤72h、100℃水浴加热30min以及100℃蒸汽加热30min方法。结果表明80℃干烤72h对制品中PRV灭活较彻底,另外两种方法对制品中PRV的灭活效果均不理想。     

注射用胸腺肽灭活/去除可能的污染病毒的工艺

目的制备注射用胸腺肽,并评价其病毒灭活/去除工艺的可行性和可信度。方法将麻疹病毒(MV)、水痘带状疱疹病毒(VZV)和甲肝病毒(HAV)作为指示病毒,分别在pH值3.2±0.3于-20℃冻存21 d、80℃加热5min灭活病毒、在进压0.15 MPa、回流压0.05 MPa下先后用截留相对分子质量10kD的中空纤维柱和膜包滤器循环超滤去除病毒,并于病毒灭活/去除前后分别取样感染宿主细胞,做病毒滴定,以病毒是否灭活/去除或病毒量下降是否大于4.0 Log作为病毒是否有效灭活/去除的标准。结果经过酸沉灭活后,3种指示病毒的滴度均有所降低;经过加热灭活后,MV和VZV均未检出,滴度下降大于4.0 Log;经超滤去除病毒后,3种指示病毒均未检出,滴度下降均大于4.0Log,且经盲传复壮后均未检出病毒。结论注射用胸腺肽生产工艺中的低pH孵放法、加热法、超滤法的联合运用可以有效地灭活/去除病毒。     

Enveloped virus inactivation by caprylate: a robust alternative to solvent-detergent treatment in plasma derived intermediates.

Solvent-detergent treatment, although used routinely in plasma product processing to inactivate enveloped viruses, substantially reduces product yield from the human plasma resource. To improve yields in plasma product manufacturing, a new viral reduction process has been developed using the fatty acid caprylate. As licensure of plasma products warrants thorough evaluation of pathogen reduction capabilities, the present study examined susceptibility of enveloped viruses to inactivation by caprylate in protein solutions with varied pH and temperature. In the immunoglobin-rich solutions from Cohn Fraction II+III, human immunodeficiency virus, Type-1, bovine viral diarrhea virus (BVDV), and pseudorabies virus were inactivated by caprylate concentrations of >/=9 mM, >/=12 mM, and >/=9 mM, respectively. Compared to solvent-detergent treatment, BVDV inactivation in Fraction II+III solution was significantly faster (20-60 fold) using 16 mM caprylate. Caprylate-mediated inactivation of BVDV was not noticeably affected by temperature within the range chosen manufacturing the immunoglobulin product. In Fraction II+III solutions, IgG solubility was unaffected by 相似文献   

Low pH, caprylate incubation as a second viral inactivation step in the manufacture of albumin. Parametric and validation studies.

Caprylate has long been used as a stabiliser for albumin solutions, as well as a precipitation agent for immunoglobulins, ceruloplasmin and more recently in removing contaminants during albumin purification. Its virucidal properties have been explored and it has been proposed that the non-ionised form of the caprylate acid disrupts the integrity of the lipid bilayer and membrane associated proteins of enveloped viruses. The studies reported here further explore the use of this fatty acid to inactivate lipid-enveloped viruses in albumin manufactured for therapeutic use.Caprylate concentrations considered above solubility limits were adopted. Acidic pH was used to maximise the percentage of non-ionised caprylate and elevated temperatures were used to enhance inactivation rates. Parameters were manipulated to determine the relationship between pH, temperature and caprylate: protein ratio.These studies demonstrated that elevated temperature and low pH were critical in achieving significant reduction in virus infectivity and that the rate and extent of inactivation was sensitive to changes in caprylate:protein ratio and to changes in pH. Final inactivation conditions of 10% w/v protein, 16 mM caprylate, pH 4.5 and 30 degrees C were chosen to minimise protein dimerisation and to achieve greater than 4 log(10)inactivation of the most resistant virus tested, bovine viral diarrhoea virus.Validation studies using both model and relevant blood borne viruses demonstrated this to be a robust and effective viral inactivation step and is complementary to the commonly used pasteurisation viral inactivation step, thus providing an additional margin of safety to this valuable therapeutic blood product.     

Assessment of viral inactivation during pH 3.3 pepsin digestion and caprylic acid treatment of antivenoms

Antivenoms are manufactured by the fractionation of animal plasma which may possibly be contaminated by infectious agents pathogenic to humans. This study was carried out to determine whether pre-existing antivenom production steps, as carried out by EgyVac in Egypt, may reduce viral risks. Two typical manufacturing steps were studied by performing down-scaled viral inactivation experiments: (a) a pH 3.3 pepsin digestion of diluted plasma at 30 degrees C for 1h, and (b) a caprylic acid treatment of a purified F(ab')2 fragment fraction at 18 degrees C for 1h. Three lipid-enveloped (LE) viruses [bovine viral diarrhoea virus (BVDV), pseudorabies virus (PRV), and vesicular stomatitis virus (VSV)] and one non-lipid-enveloped (NLE) virus [encephalomyocarditis virus (EMC)] were used as models. Kinetics of inactivation was determined by taking samples at 3 time-points during the treatments. The pH 3.3 pepsin digestion resulted in complete clearance of PRV (>7.0 log(10)) and in almost complete reduction of VSV (>4.5 but < or =6.4 log(10)), and in a limited inactivation of BVDV (1.7 log(10)). EMC inactivation was > or =2.5 but < or =5.7 log(10). The caprylic acid treatment resulted in complete inactivation of the 3 LE viruses tested: BVDV (>6.6 log(10)), PRV (>6.6 log(10)), and VSV (>7.0 log(10)). For EMC no significant reduction was obtained (0.7 log(10)). Cumulative reduction was >13.6, >11.5, >8.3 and > or =2.5 for PRV, VSV, BVDV and EMC, respectively. Therefore the current manufacturing processes of at least some animal antisera already include production steps that can ensure robust viral inactivation of LE viruses and moderate inactivation of a NLE virus.     

Virus Validation of PH 4-treated Human Immunoglobulin Produced by the Cohn Fractionation Process

To assess the virus reducing capacity of Cohn's cold ethanol fractionation process for the production of intravenous (IVIg) and intramuscular (IMIg) immunoglobulin products, and treatment of these products at pH 4, a validation study of virus removal and/or inactivation was performed using both lipid-enveloped viruses [human immunodeficiency virus (HIV), bovine viral diarrhoea virus (BVDV) and pseudorabies virus (PSR)], and non-lipid-enveloped viruses [(simian virus 40 (SV40) and encephalomyocarditis virus (EMC)]. For the cold ethanol fractionation process, overall reduction factors of 3.0 logs, > or = 2.6 (< 5.5) logs, 4.6 logs, 5.8 logs and > or = 2.6 (< 6.2) logs were found for HIV, BVDV, PSR, SV40 and EMC, respectively. For all tested viruses the precipitation of fraction III from fraction II + III was the most effective step. From the overall reduction factors it appears that cold ethanol fractionation, although capable of reducing viral infectivity to a significant extent, is not sufficient to meet the requirements of regulatory bodies for viral safety of immunoglobulin products. However, pH 4 treatment contributes effectively to the viral safety of the final products. Treatment at pH 4.05 and 37 degrees C for 16 h, as is applied to IVIg, yields reduction factors of > or = 8.4 logs, > or = 4.0 logs, > or = 7.1 logs, 4.8 logs and 1.4 logs for HIV, BVDV, PSR, SV40 and EMC, respectively. The effectiveness of this process step could be enhanced by extending incubation to 40 h at pH 4.25 compared to 16 h at pH 4.05. The extended incubation, as applied in the production of IMIg, yields a reduction of infectivity of SV40 by > or = 5.5 (< 8.0) logs and of EMC by > or = 4.1 (< 7.1) logs. Storage of IMIg, which is formulated as a solution, at 2-8 degrees C also contributes to virus safety. For storage periods of 8 weeks or longer, reduction factors of 2 to 6 logs were found for all viruses, except for BVDV which remained unaffected. These data indicate that the production processes for IVIg and IMIg as described here have sufficient virus reducing capacity to achieve a high margin of virus safety.     

Fusion and infection of influenza and Sendai viruses as modulated by dextran sulfate: a comparative study

We have directly compared the effect of two types of dextran sulfate with distinct molecular weights (500 kDa and 5 kDa) on the fusion activity and infectivity of both Sendai and influenza viruses, two lipid-enveloped viruses that differ in their routes of entry into target cells. To correlate membrane merging and infectivity MDCK cells were used as targets for the viruses in both approaches. In either case pronounced inhibition of virus–cell interactions by dextran sulfate was only observed at low pH, even though Sendai virus fuses maximally at pH 7.4. Although membrane merging could not be fully abolished, the inhibitory effect was always greater when the higher molecular weight dextran sulfate was used. The presence of this residual fusion activity, that could not be reduced even with high concentrations of agent, suggests that a limited number of binding sites for dextran sulfate may exist on the viral envelopes. The compounds also inhibited fusion of bound virions, and all results could be reproduced using erythrocyte ghosts as target membranes in the fusion assay, instead of MDCK cells. In agreement with these observations only the infectivity of influenza virus (which requires a low pH-dependent step to enter target cells) was affected by dextran sulfate, again the higher molecular weight compound showing a more pronounced inhibitory effect.     

静注丙球低pH孵放灭活病毒效果验证

以水泡性口炎病毒（ＶＳＶ）为指示病毒,考察了低ｐＨ孵放不同时间对低温乙醇法生产的静注丙球（ＩＶＩＧ）中ＶＳＶ的灭活效果,并对不同厂家及不同批号ＩＶＩＧ中病毒灭活情况进行了比较。结果表明,液体ＩＶＩＧ在ＰＨ４．１±０．３,２０－２５℃,孵放２１天可灭活ＶＳＶ达６Ｌｏｇｓ以上（即低于实验检测限）,但不同厂家及不同批号的ＩＶＩＧ在病毒灭活的发生上有所不同     

层析法从血浆分离静注人免疫球蛋白及其初步检定

目的：实验尝试采用多步柱层析的工艺取代乙醇低温沉淀的方法,能高效的从血浆中获得IVIG产品。方法：通过亲和层析、离子交换一套工艺纯化出IVIG产品,进而按照枟中华人民共和国药典枠对静注人免疫球蛋白（pH4）及其关键指标进行了检测。在此基础上还采用免疫浊度法等方法,对其纯度和非目的蛋白构成与国际产品进行比较。结果：工艺获得IVIG产品的关键性指标检测均达到枟中华人民共和国药典枠的要求,其质量不低于现有国际同类产品。结论：本工艺能以较高回收率获得高质量的IVIG产品。