Real time quantitative PCR as a method to evaluate xenotropic murine leukemia virus removal during pharmaceutical protein purification

Chinese hamster ovary cells used for pharmaceutical protein production express noninfectious retrovirus-like particles. To assure the safety of pharmaceutical proteins, validation of the ability of manufacturing processes to clear retrovirus-like particles is required for product registration. Xenotropic murine leukemia virus (X-MuLV) is often used as a model virus for clearance studies. Traditionally, cell-based infectivity assay has been the standard virus quantification method. In this article, a real time quantitative PCR (Q-PCR) method has been developed for X-MuLV detection/quantification. This method provides accurate and reproducible quantification of X-MuLV particle RNA (pRNA) over a linear dynamic range of at least 100,000-fold with a quantification limit of approximately 1.5 pRNA copies microL(-1). It is about 100-fold more sensitive than the cell-based infectivity assay. High concentrations of protein and cellular DNA present in test samples have been demonstrated to have no impact on X-MuLV quantification. The X-MuLV clearance during chromatography and filtration procedures determined by this method is highly comparable with that determined by the cell-based infectivity assay. X-MuLV clearance measured by both methods showed that anion exchange chromatography (QSFF) and DV50 viral filtration are robust retroviral removal steps. In addition, combination of the two methods was able to distinguish the viral removal from inactivation by the Protein A chromatography, and fully recognize the viral clearance capacity of this step. This new method offers significant advantages over cell-based infectivity assays. It could be used to substitute cell-based infectivity assays for process validation of viral removal procedures, but not inactivation steps. Its availability should greatly facilitate and reduce the cost of viral clearance evaluations for new biologic product development.     

Inactivation of viruses using novel protein A wash buffers

Low pH viral inactivation is typically performed in the eluate pool following the protein A capture step during the manufacturing of monoclonal antibodies and Fc‐fusion proteins. However, exposure to low pH has the potential to alter protein quality. To avoid these difficulties, novel wash buffers capable of inactivating viruses while antibodies or Fc‐fusion proteins were bound to protein A or mixed mode resins were developed. By equilibrating the column in high salt buffer (2 M ammonium sulfate or 3 M sodium chloride) after loading, the hydrophobic interactions between antibodies and protein A ligands were increased enough to prevent elution at pH 3. The ammonium sulfate was also found to cause binding of an antibody to a mixed mode cation exchange and a mixed mode anion exchange resin at pH values that caused elution in conventional cation and anion exchange resins (pH 3.5 for Capto Adhere and pH 8.0 for Capto MMC), indicating that retention was due to enhanced hydrophobic interactions. The potential of the 2 M ammonium sulfate pH 3 buffer, a 1 M arginine buffer, and a buffer containing the detergent LDAO to inactivate XMuLV virus when used as protein A wash buffers with a 1 hour contact time were studied. The high salt and detergent containing wash buffers provided about five logs of removal, determined using PCR, and complete combined removal and inactivation (> 6 logs), determined by measuring infectivity. The novel protein A washes could provide more rapid, automated viral inactivation steps with lower pool conductivities. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:406–413, 2015     

Real-time quantitative PCR for retrovirus-like particle quantification in CHO cell culture.

Chinese hamster ovary (CHO) cells have been widely used to manufacture recombinant proteins intended for human therapeutic uses. Retrovirus-like particles, which are apparently defective and non-infectious, have been detected in all CHO cells by electron microscopy (EM). To assure viral safety of CHO cell-derived biologicals, quantification of retrovirus-like particles in production cell culture and demonstration of sufficient elimination of such retrovirus-like particles by the down-stream purification process are required for product market registration worldwide. EM, with a detection limit of 1x10(6) particles/ml, is the standard retrovirus-like particle quantification method. The whole process, which requires a large amount of sample (3-6 litres), is labour intensive, time consuming, expensive, and subject to significant assay variability. In this paper, a novel real-time quantitative PCR assay (TaqMan assay) has been developed for the quantification of retrovirus-like particles. Each retrovirus particle contains two copies of the viral genomic particle RNA (pRNA) molecule. Therefore, quantification of retrovirus particles can be achieved by quantifying the pRNA copy number, i.e. every two copies of retroviral pRNA is equivalent to one retrovirus-like particle. The TaqMan assay takes advantage of the 5'-->3' exonuclease activity of Taq DNA polymerase and utilizes the PRISM 7700 Sequence Detection System of PE Applied Biosystems (Foster City, CA, U.S.A.) for automated pRNA quantification through a dual-labelled fluorogenic probe. The TaqMan quantification technique is highly comparable to the EM analysis. In addition, it offers significant advantages over the EM analysis, such as a higher sensitivity of less than 600 particles/ml, greater accuracy and reliability, higher sample throughput, more flexibility and lower cost. Therefore, the TaqMan assay should be used as a substitute for EM analysis for retrovirus-like particle quantification in CHO cell-based production system.     

Characterization of ionic strength for X-MuLV inactivation by low pH treatment for monoclonal antibody purification

In the production of monoclonal antibodies (mAbs) intended for use in humans, it is a global regulatory requirement that the manufacturing process includes unit operations that are proven to inactivate or remove adventitious agents to ensure viral safety. Viral inactivation by low pH hold (LPH) is typically used to ensure this viral safety in the purification process of mAbs and other biotherapeutics derived from mammalian cell lines. To ascertain the effectiveness of the LPH step, viral clearance studies have evaluated LPH under worst-case conditions of pH above the manufacturing set point and hold duration at or below the manufacturing minimum. Highly acidic conditions (i.e., pH < 3.60) provide robust and effective enveloped virus inactivation but may lead to reduced product quality of the therapeutic protein. However, when viral inactivation is operated above pH 3.60 to ensure product stability, effective (>4 log₁₀ reduction factor) viral inactivation may not be observed under these worst-case pH conditions in viral clearance studies. A multivariate design of experiments was conducted to further characterize the operating space for low pH viral inactivation of a model retrovirus, xenotropic murine leukemia virus (X-MuLV). The statistically designed experiment evaluated the effect of mAb isotype, pH, temperature, acid titrant, sodium chloride (NaCl) concentration, virus spike timing, and post-spike filtration on X-MuLV inactivation. Data from the characterization study were used to generate predictive models to identify conditions that reliably achieve effective viral inactivation at pH ≥ 3.60. Results of the study demonstrated that NaCl concentration has the greatest effect on virus inactivation in the range studied, and pH has a large effect when the load material has no additional NaCl. Overall, robust and effective inactivation of X-MuLV at pH 3.65–3.80 can be achieved by manipulating either the pH or the NaCl concentration of the load material. This study contributes to the understanding of ionic strength as an influential parameter in low pH viral inactivation studies.     

Real time quantitative PCR as a method to evaluate simian virus 40 removal during pharmaceutical protein purification.

Continuous cell lines used for pharmaceutical protein manufacturing have the potential to be contaminated by viruses. To ensure the safety of pharmaceutical proteins derived from continuous cell lines, validation of the ability of the manufacturing process to clear potential contaminating viruses is required for product registration. In this paper, a real time quantitative PCR method has been applied to the evaluation of simian virus 40 (SV40) removal during chromatography and filtration procedures. This method takes advantage of the 5'-3' exonuclease activity of Taq DNA polymerase and utilizes the PRISM 7700 sequence detection system of PE Applied Biosystems for automated SV40 DNA quantification through a dual-labeled fluorogenic probe. This method provides accurate and reproducible quantification of SV40 DNA. The SV40 clearance during chromatography and filtration procedures determined by this method is highly comparable with that determined by the cell-based infectivity assay. This method offers significant advantages over cell-based infectivity assays, such as higher sensitivity, greater reliability, higher sample throughput and lower cost. This method can be potentially used to evaluate the clearance of all model viruses during chromatography and filtration procedures. This method can be used to substitute cell-based infectivity assays for process validation of viral removal procedures and the availability of this method should greatly facilitate and reduce the cost of viral clearance evaluations required for new biologic product development.     

Virus inactivation by protein denaturants used in affinity chromatography

Virus inactivation by a number of protein denaturants commonly used in gel affinity chromatography for protein elution and gel recycling has been investigated. The enveloped viruses Sindbis, herpes simplex-1 and vaccinia, and the non-enveloped virus polio-1 were effectively inactivated by 0.5 M sodium hydroxide, 6 M guanidinium thiocyanate, 8 M urea and 70% ethanol. However, pH 2.6, 3 M sodium thiocyanate, 6 M guanidinium chloride and 20% ethanol, while effectively inactivating the enveloped viruses, did not inactivate polio-1. These studies demonstrate that protein denaturants are generally effective for virus inactivation but with the limitation that only some may inactivate non-enveloped viruses. The use of protein denaturants, together with virus reduction steps in the manufacturing process should ensure that viral cross contamination between manufacturing batches of therapeutic biological products is prevented and the safety of the product ensured.     

Virus clearance validation across continuous capture chromatography

Multicolumn capture chromatography is gaining increased attention lately due to the significant economic and process advantages it offers compared with traditional batch mode chromatography. However, for wide adoption of this technology in clinical and commercial space, it requires scalable models for executing viral validation studies. In this study, viral validation studies were conducted under cGLP guidelines to assess retro- (X-MuLV) and parvo-virus (MVM) clearance across twin-column continuous capture chromatography (CaptureSMB). A surrogate model was also developed using standard batch mode chromatography based on flow path modifications to mimic the loading strategy used in CaptureSMB. The results show that a steady state was achieved by the second cycle for both antibody binding and virus clearance and that the surrogate model using batch mode chromatography equipment provided impurity clearance that was comparable to that obtained during cyclical operation of CaptureSMB. Further, the log reduction values (LRVs) achieved during CaptureSMB were also comparable to the LRVs obtained using standard batch capture chromatography. This was expected since the mode of virus separation during protein A chromatography is primarily based on removal during the flow through and wash steps. Finally, this study also presents assessments on the resin cleaning strategy during continuous chromatography and how the duration of clean-in-place solution exposure impacts virus carryover.     

Manufacturing process of anti-thrombin III concentrate: viral safety validation studies and effect of column re-use on viral clearance.

A manufacturing process for the production of Anti-thrombin IIII concentrate is described, which is based primarily on Heparin Sepharose affinity chromatography. The process includes two sequential viral inactivation/removal procedures, applied to the fraction eluted from the column, the first by heating in aqueous solution at 60 degrees C for 10 h and the second by nanofiltration. Using viral validation on a scaled-down process both treatments proved to be effective steps; able to inactivate or remove more than 4 logs of virus, and their combined effect (>8 logs) assured the safety of the final product. Viral validation studies of the Heparin Sepharose chromatographic step demonstrated a consistency of the affinity of the resin for viruses over repeated use (16 runs), thus providing evidence of absence of cross-contamination from one batch to the next. It was concluded that the process of ATIII manufacturing provides a high level of confidence that the product will not transmit viruses.     

Pressure-induced formation of inactive triple-shelled rotavirus particles is associated with changes in the spike protein Vp4

Rotaviruses are non-enveloped, triple-shelled particles that cause enteritis in animals and humans. The interactions among the different viral proteins located in the three concentric layers make the rotavirus particle an excellent model for physico-chemical and biological studies of viral assemblage. SA11-4S rotaviruses subjected to high pressure were inactivated by more than five log units. After pressure treatment, the particles were recovered with slight structural changes when compared to the control. Electron microscopy suggested subtle changes in the viral outer layer in some pressurised particles. Fluorescence spectroscopy showed that much more dramatic changes were produced by urea denaturation than by pressure. Based on the fluorescence spectrum, the genome resistance to ribonuclease, and the absence of changes in hydrodynamic properties, there was little or no disruption of the capsid under pressure. On the other hand, hemagglutination assays indicated that the main component affected by pressure was the spike protein VP4, thus accounting for changes in interaction with host cells and greatly reduced infectivity. The changes leading to inactivation did not cause removal of VP4 from the outer capsid, as verified by size-exclusion chromatography. Antibodies raised against pressurised material were as effective as antibodies raised against the intact virus, based on their neutralisation titre in plaque reduction assays, enzyme-linked immunosorbent assays and direct interaction with the particle, as measured by gel-filtration chromatography. Therefore, the new conformation of the pressurised particle did not result in loss of immunogenicity. We propose that pressure alters the receptor-binding protein VP4 by triggering changes similar to those produced when the virus interacts with target cells. As the changes in VP4 conformation caused by pressure occur prior to virus exposure to target cells, it leads to non-infectious particles and may lead to the exposure of previously occult epitopes, important for vaccine development.     

Suitability of a generic virus safety evaluation for monoclonal antibody investigational new drug applications

Biologics produced from CHO cell lines with endogenous virus DNA can produce retrovirus-like particles in cell culture at high titers, and other adventitious viruses can find their way through raw materials into the process to make a product. Therefore, it is the industry standard to have controls to avoid introduction of viruses into the production process, to test for the presence of viral particles in unclarified cell culture, and to develop purification procedures to ensure that manufacturing processes are robust for viral clearance. Data have been accumulated over the past four decades on unit operations that can inactivate and clear adventitious virus and provide a high degree of assurance for patient safety. During clinical development, biological products are traditionally tested at process set points for viral clearance. However, the widespread implementation of platform production processes to produce highly similar IgG antibodies for many indications makes it possible to leverage historical data and knowledge from representative molecules to allow for better understanding and control of virus safety. More recently, individualized viral clearance studies are becoming the rate-limiting step in getting new antibody molecules to clinic, particularly in Phase 0 and eIND situations. Here, we explore considerations for application of a generic platform virus clearance strategy that can be applied for relevant investigational antibodies within defined operational parameters in order to increase speed to the clinic and reduce validation costs while providing a better understanding and assurance of process virus safety.     

Anion exchange chromatography provides a robust, predictable process to ensure viral safety of biotechnology products

The mammalian cell-lines used to produce biopharmaceutical products are known to produce endogenous retrovirus-like particles and have the potential to foster adventitious viruses as well. To ensure product safety and regulatory compliance, recovery processes must be capable of removing or inactivating any viral impurities or contaminants which may be present. Anion exchange chromatography (AEX) is a common process in the recovery of monoclonal antibody products and has been shown to be effective for viral removal. To further characterize the robustness of viral clearance by AEX with respect to process variations, we have investigated the ability of an AEX process to remove three model viruses using various combinations of mAb products, feedstock conductivities and compositions, equilibration buffers, and pooling criteria. Our data indicate that AEX provides complete or near-complete removal of all three model viruses over a wide range of process conditions, including those typically used in manufacturing processes. Furthermore, this process provides effective viral clearance for different mAb products, using a variety of feedstocks, equilibration buffers, and different pooling criteria. Viral clearance is observed to decrease when feedstocks with sufficiently high conductivities are used, and the limit at which the decrease occurs is dependent on the salt composition of the feedstock. These data illustrate the robust nature of the AEX recovery process for removal of viruses, and they indicate that proper design of AEX processes can ensure viral safety of mAb products.     

Generic/matrix evaluation of SV40 clearance by anion exchange chromatography in flow-through mode

The potential of viral contamination is a regulatory concern for continuous cell line-derived pharmaceutical proteins. Complementary and redundant safety steps, including an evaluation of the viral clearance capacity of unit operations in the purification process, are performed prior to registration and marketing of biotechnology pharmaceuticals. Because process refinement is frequently beneficial, CBER/FDA has published guidance facilitating process improvement by delineating specific instances where the bracketing and generic approaches are appropriate for virus removal validation. In this study, a generic/matrix study was performed using Q-Sepharose Fast Flow (QSFF) chromatography to determine if bracketing and generic validation can be applied to anion exchange chromatography. Key operational parameters were varied to upper and lower extreme values and the impact on viral clearance was assessed using simian virus 40 (SV40) as the model virus. Operational ranges for key chromatography parameters were identified where an SV40 log(10) reduction value (LRV) of >or=4.7 log(10) is consistently achieved. On the basis of the apparent robustness of SV40 removal by Q-anion exchange chromatography, we propose that the concept of "bracketed generic" validation can be applied to this and potentially other chromatography unit operations.     

Mechanistic insights into viral clearance during the chromatography steps in antibody processes by using virus surrogates

Viral safety is required for biological products to treat human diseases, and the burden of inactivation and or virus removal lies on the downstream purification process. Minute virus of mice (MVM) is a nonenveloped parvovirus commonly used as the worst-case model virus in validation studies because of its small size and high chemical stability. In this study, we investigated the use of MVM-mock virus particle (MVP) and bacteriophage ΦX174 as surrogates for MVM to mimic viral clearance studies, with a focus on chromatography operations. Based on structural models and comparison of log reduction value among MVM, MVP, and ΦX174, it was demonstrated that MVP can be used as a noninfectious surrogate to assess viral clearance during process development in multiple chromatography systems in a biosafety level one (BSL-1) laboratory. Protein A (ProA) chromatography was investigated to strategically assess the impact of the resin, impurities, and the monoclonal antibody product on virus removal.     

Densonucleosis virus purification by ion exchange membranes

Preparative chromatography is widely used in the downstream purification of biopharmaceutical products. Replacement of resins by membranes as chromatographic supports, overcomes many of the limitations associated with resin-based chromatography such as high-pressure drops, slow processing rates due to pore diffusion and channeling of the feed through the bed. In particular, adsorptive membranes may be ideally suited for virus capture. Virus capture is critical in a number of applications. In gene therapy and vaccine production, large-scale purification of virus vectors is often essential. In the manufacture of biopharmaceuticals, validation of virus clearance is critical.Here results for purification of Aedes aegypti densonucleosis virus (AeDNV) using anion and cation exchange membranes are presented. AeDNV is a non-enveloped, single-stranded mosquito-specific parvovirus. Virus particles are around 20 nm in size. AeDNV could find potential applications in integrated vector-borne disease control programs. In addition, capture of parvovirus for validation of virus clearance in the manufacture of biopharmaceuticals is of commercial importance.By adjusting the pH of the feed stream, AeDNV particles may be adsorbed by both anion and cation exchange membranes. However, strongly basic anion exchange membranes were the most effective in adsorbing AeDNV particles. Adsorption and subsequent elution of AeDNV by anion exchange membranes leads to significant virus concentration. Dynamic and static capacities for anion exchange membranes were similar. Further, a sharp elution curve was obtained suggesting that pore diffusional resistances are insignificant. The adsorption of AeDNV particles by anion exchange membranes may be described by a linear isotherm.     

Clearance of porcine circovirus and porcine parvovirus from porcine-derived pepsin by low pH inactivation and cation exchange chromatography

The contamination of oral rotavirus vaccines by porcine circovirus (PCV) raised questions about potential PCV contamination of other biological products when porcine trypsin or pepsin is used in production process. Several methods can be potentially implemented as a safety barrier when animal derived trypsin or pepsin is used. Removal of PCV is difficult by the commonly used viral filters with the pore size cutoff of approximately 20 nm because of the smaller size of PCV particles that are around 17 nm. It was speculated that operating the chromatography step at a pH higher than pepsin's low pI, but lower than pIs, of most viruses would allow the pepsin to flow through the resin and be recovered from the flow through pool whilst the viruses would be retained on the resin. In this study, we investigated low pH inactivation of viruses including PCV Type 1 (PCV1) and PCV1 removal by cation exchange chromatography (CEX) in the presence of pepsin. Both parvovirus and PCV1 could be effectively inactivated by low pH and PCV1 could be removed by POROS 50HS CEX. The POROS 50HS method presented in this article is helpful for designing other CEX methods for the same purpose and not much difference would be expected for similar product intermediates and same process parameters. While the effectiveness needs to be confirmed for specific applications, the results demonstrate that both low pH (pH 1.7) and CEX methods were successful in eliminating PCV1 and thus either can be considered as an effective virus barrier.     

正辛酸沉淀在单克隆抗体纯化中的工艺优化与应用

为应对治疗性抗体快速增长的市场需求,抗体上游细胞培养规模和表达量水平已显著提高,而下游纯化工艺的生产效率则相对落后,下游处理能力已成为限制抗体产能的瓶颈。本研究以单克隆抗体mab-X为实验材料,优化了细胞培养液、低pH病毒灭活收集液2种模式的正辛酸(caprylic acid,CA)沉淀工艺条件,并研究了CA处理去除聚体、CA处理灭活病毒等2种应用,在小试的基础上,采用低pH病毒灭活收集液CA沉淀的模式进行了500 L细胞培养规模生产放大研究,对沉淀前后的产品质量和收率进行了检测和对比。结果显示,两种模式的CA沉淀均可显著降低宿主细胞蛋白(host cell protein,HCP)残留和聚体含量,在聚体去除实验中CA沉淀可去除约15%的聚体,病毒灭活研究显示CA对逆转录模型病毒具有完全的病毒灭活能力。在放大生产规模中,下游依次进行了深层过滤收获、亲和层析、低pH病毒灭活、CA沉淀及深层过滤、阳离子交换层析,CA沉淀过程中混合时间和搅拌速度显著影响CA沉淀效果,CA沉淀处理后低pH病毒灭活液中的HCP残留量降低了895倍,沉淀后产品纯度和HCP残留均已控制在单克隆抗体质量要求范围内,CA沉淀可以减少传统纯化工艺中的一个精纯步骤。总之,下游工艺中采用CA沉淀,能够精简传统纯化工艺,并完全满足mab-X的纯化质量要求,而且能提高生产效率、降低生产成本。本研究结果将推动CA沉淀在单克隆抗体下游纯化生产中的应用,为解决目前传统纯化工艺的问题提供参考。     

TnBP?Triton X-45 Treatment of Plasma for Transfusion Efficiently Inactivates Hepatitis C Virus

Risk of transmission of hepatitis C virus (HCV) by clinical plasma remains high in countries with a high prevalence of hepatitis C, justifying the implementation of viral inactivation treatments. In this study, we assessed the extent of inactivation of HCV during minipool solvent/detergent (SD; 1% TnBP / 1% Triton X-45) treatment of human plasma. Luciferase-tagged infectious cell culture-derived HCV (HCVcc) particles were used to spike human plasma prior to treatment by SD at 31 ± 0.5°C for 30 min. Samples were taken before and after SD treatment and filtered on a Sep-Pak Plus C18 cartridge to remove the SD agents. Risk of cytotoxicity was assessed by XTT cell viability assay. Viral infectivity was analyzed based on the luciferase signals, 50% tissue culture infectious dose viral titer, and immunofluorescence staining for HCV NS5A protein. Total protein, cholesterol, and triglyceride contents were determined before and after SD treatment and C18 cartridge filtration. Binding analysis, using patient-derived HCV clinical isolates, was also examined to validate the efficacy of the inactivation by SD. SD treatment effectively inactivated HCVcc within 30 min, as demonstrated by the baseline level of reporter signals, total loss of viral infectivity, and absence of viral protein NS5A. SD specifically targeted HCV particles to render them inactive, with essentially no effect on plasma protein content and hemostatic function. More importantly, the efficacy of the SD inactivation method was confirmed against various genotypes of patient-derived HCV clinical isolates and against HCVcc infection of primary human hepatocytes. Therefore, treatment by 1% TnBP / 1% Triton X-45 at 31°C is highly efficient to inactivate HCV in plasma for transfusion, showing its capacity to enhance the safety of therapeutic plasma products. We propose that the methodology used here to study HCV infectivity can be valuable in the validation of viral inactivation and removal processes of human plasma-derived products.     

Application of multivirus spike approach for viral clearance evaluation

Viral contamination is a common risk to continuous cell line-derived biologics. Viral validation is thus required for license applications. Viral validation for chromatography procedures is routinely performed by spiking a model virus into the load material and performing the chromatography procedures at small scale under conditions equivalent to the commercial scale. With traditional cell-based infectivity assays, one can only spike one model virus at one time. Quantitative PCR methods (TaqMan) make it possible to spike multiple model viruses for a chromatography procedure simultaneously. TaqMan assays can quantify multiple types of viruses and other types of nucleic acid in a single sample without cross interference because of its extremely high specificity. Therefore, a multivirus spike approach was evaluated and compared to a single virus spike approach. The study was further extended to the evaluation of host cell DNA clearance. The data shows highly comparable viral and host cell DNA clearance between the single and multiple virus spike approaches. Application of a multivirus spike approach provides significant time, manpower, and cost savings for new drug development.     

Inactivation of retroviruses with preservation of structural integrity by targeting the hydrophobic domain of the viral envelope

We describe a new approach for the preparation of inactivated retroviruses for vaccine application. The lipid domain of the viral envelope was selectively targeted to inactivate proteins and lipids therein and block fusion of the virus with the target cell membrane. In this way, complete elimination of the infectivity of human immunodeficiency virus (HIV) and simian immunodeficiency virus (SIV) could be achieved with preservation of antigenic determinants on the surface of the viral envelope. Inactivation was accomplished by modification of proteins and lipids in the viral envelope using the hydrophobic photoinduced alkylating probe 1,5 iodonaphthylazide (INA). Treatment of HIV and SIV isolates with INA plus light completely blocked fusion of the viral envelope and abolished infectivity. The inactivated virus remained structurally unchanged, with no detectable loss of viral proteins. Modifications to envelope and nucleocapsid proteins were detected by changes in their elution pattern on reverse-phase high-performance liquid chromatography. These modifications had no effect on primary and secondary structure epitopes as determined by monoclonal antibodies. Likewise, the inactivated HIV reacted as well as the live virus with the conformation-sensitive and broadly neutralizing anti-HIV type 1 monoclonal antibodies 2G12, b12, and 4E10. Targeting the lipid domain of biological membranes with hydrophobic alkylating compounds could be used as a general approach for inactivation of enveloped viruses and other pathogenic microorganisms for vaccine application.