Добавил:
kiopkiopkiop18@yandex.ru t.me/Prokururor I Вовсе не секретарь, но почту проверяю Опубликованный материал нарушает ваши авторские права? Сообщите нам.
Вуз: Предмет: Файл:

Ординатура / Хирургия / Библиотека им академика М.И. Перельмана / Книга_5395_Библиотеки_им_академика_М_И_Перельмана

.pdf
Скачиваний:
0
Добавлен:
15.09.2026
Размер:
15 Мб
Скачать
☆
388 M. Karlberg et al.
https://t.me/medicina_free
12. Yamashita, T. 2018. Toward rational antibody design: recent advancements in molecular dynamics simulations. International Immunology, 30, 133-140.
13. Harms, J., Wang, X., Kim, T., Yang, X. & Rathore, A. S. 2008. Defining process design space for biotech products: case study of Pichia pastoris fermentation. Biotechnol Prog, 24, 655-62.
14. Zimmermann, H. F. & Hentschel, N. 2011. Proposal on how to conduct a biopharmaceutical process Failure Mode and Effect Analysis (FMEA) as a Risk Assessment Tool. PDA J Pharm Sci Technol, 65, 506-12.
15. Leardi, R. 2009. Experimental design in chemistry: A tutorial. Anal Chim Acta, 652, 161-72.
16. Rathore, A. S. 2016. Quality by design (QbD)-based process development for purification of a biotherapeutic. Trends in biotechnology, 34, 358-370.
17. Kumar, V., Bhalla, A. & Rathore, A. S. 2014. Design of experiments applications in bioprocessing: concepts and approach. Biotechnology Progress, 30, 86-99.
18. Tai, M., Ly, A., Leung, I. & Nayar, G. 2015. Efficient high-throughput biological process char­acterization: Definitive screening design with the Ambr250 bioreactor system. Biotechnology Progress, 31, 1388-1395.
19. Zurdo, J. 2013. Surviving the valley of death. Eur Biopharmaceutical Rev, 195, 50-4.
20. Dehmer, M., Varmuza, K., Bonchev, D. & Ebrary Academic Complete International Sub­scription Collection. 2012. Statistical modelling of molecular descriptors in QSAR/QSPR. Quantitative and network biology v 2. Weinheim: Wiley-Blackwell,.
21. Dudek, A. Z., Arodz, T. & Galvez, J. 2006. Computational methods in Developing quantitative structure-activity relationships (QSAR): A review. Combinatorial Chemistry & High Through- put Screening, 9, 213-228.
22. Du, Q. S., Huang, R. B. & Chou, K. C. 2008. Recent advances in QSAR and their applications in predicting the activities of chemical molecules, peptides and proteins for drug design. Current Protein & Peptide Science, 9, 248-259.
23. Zhou, P., Chen, X., Wu, Y. Q. & Shang, Z. C. 2010. Gaussian process: an alternative approach for QSAM modeling of peptides. Amino Acids, 38, 199-212.
24. Hechinger, M., Leonhard, K. & Marquardt, W. 2012. What is Wrong with Quantitative Structure-Property Relations Models Based on Three-Dimensional Descriptors? Journal of Chemical Information and Modeling, 52, 1984-1993.
25. Zhou, P., Tian, F. F., Wu, Y. Q., Li, Z. L. & Shang, Z. C. 2008. Quantitative Sequence-Activity Model (QSAM): Applying QSAR Strategy to Model and Predict Bioactivity and Function of Peptides, Proteins and Nucleic Acids. Current Computer-Aided Drug Design, 4, 311-321.
26. Sneath, P. H. 1966. Relations between chemical structure and biological activity in peptides. J Theor Biol, 12, 157-95.
27. Kidera, A., Konishi, Y., Oka, M., Ooi, T. & Scheraga, H. A. 1985. Statistical-analysis of the physical-properties of the 20 naturally-occurring amino-acids. Journal of Protein Chemistry, 4, 23-55.
28. Hellberg, S., Sjostrom, M., Skagerberg, B. & WOLD, S. 1987. Peptide Quantitative Structure­Activity-Relationships, a Multivariate Approach. Journal of Medicinal Chemistry, 30, 1126-
1135.
29. Hellberg, S., Sjostrom, M. & Wold, S. 1986. The prediction of bradykinin potentiating potency of pentapeptides. An example of a peptide quantitative structure-activity relationship. Acta Chem Scand B, 40, 135-40.
30. Sandberg, M., Eriksson, L., Jonsson, J., Sjostrom, M. & Wold, S. 1998. New chemical descrip­tors relevant for the design of biologically active peptides. A multivariate characterization of 87 amino acids. Journal of Medicinal Chemistry, 41, 2481-2491.
31. Tian, F. F., Zhou, P. & Li, Z. L. 2007. T-scale as a novel vector of topological descriptors for amino acids and its application in QSARs of peptides. Journal of Molecular Structure, 830, 106-115.
32. Collantes, E. R. & Dunn, W. J. 1995. Amino-Acid Side-Chain Descriptors for Quantitative Structure-Activity Relationship Studies of Peptide Analogs. Journal of Medicinal Chemistry, 38, 2705-2713.
33. van Westen, G. J. P., Swier, R. F., Cortes-Ciriano, I., Wegner, J. K., Overington, J. P., Ijzerman, A. P., Van Vlijmen, H. W. T. & Bender, A. 2013b. Benchmarking of protein descriptor sets in
Model-Based Risk Assessment of mAb Developability 389
https://t.me/medicina_free
proteochemometric modeling (part 2): modeling performance of 13 amino acid descriptor sets. Journal of Cheminformatics, 5.
34. Van Westen, G. J. P., Swier, R. F., Wegner, J. K., Ijzerman, A. P., Van Vlijmen, H. W. T. & Bender, A. 2013a. Benchmarking of protein descriptor sets in proteochemometric modeling (part 1): comparative study of 13 amino acid descriptor sets. Journal of Cheminformatics, 5.
35. Doytchinova, I. A., Walshe, V., Borrow, P. & Flower, D. R. 2005. Towards the chemometric dissection of peptide - HLA-A*0201 binding affinity: comparison of local and global QSAR models. Journal of Computer-Aided Molecular Design, 19, 203-212.
36. Gasteiger, E., Hoogland, C., Gattiker, A., Duvaud, S. E., Wilkins, M. R., Appel, R. D. & Bairoch, A. 2005. Protein identification and analysis tools on the ExPASy server, Springer.
37. Li, W., Cowley, A., Uludag, M., Gur, T., Mcwilliam, H., Squizzato, S., Park, Y. M., Buso, N. & Lopez, R. 2015. The EMBL-EBI bioinformatics web and programmatic tools framework. Nucleic Acids Research, 43, W580-W584.
38. Liao, C., Sitzmann, M., Pugliese, A. & Nicklaus, M. C. 2011. Software and resources for computational medicinal chemistry. Future Med Chem, 3, 1057-85.
39. Buyel, J. F., Woo, J. A., Cramer, S. M. & Fischer, R. 2013. The use of quantitative structure­activity relationshipmodels to develop optimized processes for the removalof tobacco hostcell proteins during biopharmaceutical production. Journal of Chromatography A, 1322, 18-28.
40. Sharma, V. K., Patapoff, T. W., Kabakoff, B., Pai, S., Hilario, E., Zhang, B., Li, C., Borisov, O., Kelley, R. F., Chorny, I., Zhou, J. Z., Dill, K. A. & Swartz, T. E. 2014. In silico selection of therapeutic antibodies for development: viscosity, clearance, and chemical stability. Proc Natl Acad Sci U S A, 111, 18601-6.
41. Sydow, J. F., Lipsmeier, F., Larraillet, V., Hilger, M., Mautz, B., Molhoj, M., Kuentzer, J., Klostermann, S., Schoch, J., Voelger, H. R., Regula, J. T., Cramer, P., Papadimitriou, A. & Kettenberger, H. 2014. Structure-based prediction of asparagine and aspartate degradation sites in antibody variable regions. PLoS One, 9, e100736.
42. Breneman, C. M., Thompson, T. R., Rhem, M. & Dung, M. 1995. Electron-density modeling of large systems using the transferable atom equivalent method. Computers & Chemistry, 19,
161.
43. Tugcu, N., Song, M. H., Breneman, C. M., Sukumar, N., Bennett, K. P. & Cramer, S. M. 2003. Prediction of the effect of mobile-phase salt type on protein retention and selectivity in anion exchange systems. Analytical Chemistry, 75, 3563-3572.
44. Robinson, J. R., Karkov, H. S., Woo, J. A., Krogh, B. O. & Cramer, S. M. 2017. QSAR models for prediction of chromatographic behavior of homologous Fab variants. Biotechnology and Bioengineering, 114, 1231-1240.
45. Brandt, J. P., Patapoff, T. W. & Aragon, S. R. 2010. Construction, MD simulation, and hydrodynamic validation of an all-atom model of a monoclonal IgG antibody. Biophys J, 99, 905-13.
46. Kortkhonjia, E., Brandman, R., Zhou, J. Z., VOELZ, V. A., Chorny, I., Kabakoff, B., Patapoff, T. W., Dill, K. A. & Swartz, T. E. 2013. Probing antibody internal dynamics with fluorescence anisotropy and molecular dynamics simulations. mAbs, 5, 306-22.
47. Kmiecik, S., Gront, D., Kolinski, M., Wieteska, L., Dawid, A. E. & Kolinski, A. 2016. Coarse­grained protein models and their applications. Chemical Reviews, 116, 7898-7936.
48. Ladiwala, A., Rege, K., Breneman, C. M. & Cramer, S. M. 2005. A priori prediction of adsorption isotherm parameters and chromatographic behavior in ion-exchange systems. Proceedings of the National Academy of Sciences of the United States of America, 102, 11710-
11715.
49. Yang, T., Breneman, C. M. & Cramer, S. M. 2007a. Investigation of multi-modal high­salt binding ion-exchange chromatography using quantitative structure-property relationship modeling. Journal of Chromatography A, 1175, 96-105.
50. Yang, T., Sundling, M. C., Freed, A. S., Breneman, C. M.& Cramer, S.M. 2007b. Prediction of pH-dependent chromatographic behavior in ion-exchange systems. Analytical Chemistry, 79 8927-8939.
,
390 M. Karlberg et al.
https://t.me/medicina_free
51. Insaidoo, F. K., Rauscher, M. A., Smithline, S. J., Kaarsholm, N. C., Feuston, B. P., Ortigosa, A. D., Linden, T. O. & Roush, D. J. 2015. Targeted purification development enabled by computational biophysical modeling. Biotechnology Progress, 31, 154-164.
52. Bishop, C. M. 2006. Introduction. Pattern recognition and machine learning. Springer.
53. Jiang, W. L., KIM, S., Zhang, X. Y., Lionberger, R. A., Davit, B. M., Conner, D. P. & Yu, L. X.
2011. The role of predictive biopharmaceutical modeling and simulation in drug development and regulatory evaluation. International Journal of Pharmaceutics, 418, 151-160.
54. Chen, J., Yang, T. & Cramer, S. M. 2008. Prediction of protein retention times in gradient hydrophobic interaction chromatographic systems. Journal of Chromatography A, 1177, 207-
214.
55. Hou, Y., Jiang, C. P., Shukla, A. A. & Cramer, S. M. 2011. Improved process analytical technology for protein A chromatography using predictive principal component analysis tools. Biotechnology and Bioengineering, 108, 59-68.
56. Karlberg, M., De Souza, J. V., Fan, L., Kizhedath, A., Bronowska, A. K. & Glassey, J. 2020. QSAR Implementation for HIC Retention Time Prediction of mAbs Using Fab Structure: A Comparison between Structural Representations. International Journal of Molecular Sciences, 21, 8037.
57. Woo, J., Parimal, S., Brown, M. R., Heden, R. & Cramer, S. M. 2015. The effect of geometrical presentation of multimodal cation-exchange ligands on selective recognition of hydrophobic regions on protein surfaces. Journal of Chromatography A, 1412, 33-42.
58. Farid, S. S. 2007. Process economics of industrial monoclonal antibody manufacture. Journal of Chromatography B-Analytical Technologies in the Biomedical and Life Sciences, 848, 8-18.
59. Hammerschmidt, N., Tscheliessnig, A., Sommer, R., Helk, B. & Jungbauer, A. 2014. Eco­nomics of recombinant antibody production processes at various scales: Industry-standard compared to continuous precipitation. Biotechnology Journal, 9, 766-775.
60. European Medicines Agency 2016. Guideline on development, production, characterisation and specification for monoclonal antibodies and related products. Committee for medicinal products for human use (CHMP).
61. Rodrigues de Azevedo, C., von Stosch, M., Costa, M. S., Ramos, A. M., Cardoso, M. M., Danhier, F., Preat, V. & Oliveira, R. 2017. Modeling of the burst release from PLGA micro­and nanoparticles as function of physicochemical parameters and formulation characteristics. Int J Pharm, 532, 229-240.
62. Jain, T., Sun, T., Durand, S., Hall, A., Houston, N. R., Nett, J. H., Sharkey, B., Bobrowicz, B., Caffry, I., Yu, Y., Cao, Y., Lynaugh, H., Brown, M., Baruah, H., Gray, L. T., Krauland, E. M., XU, Y., Vasquez, M. & Wittrup, K. D. 2017. Biophysical properties of the clinical-stage antibody landscape. Proc Natl Acad Sci U S A, 114, 944-949.
63. Kizhedath, A. 2019. QSAR model development for early stage screening of monoclonal antibody therapeutics to facilitate rapid developability. (Doctoral Dissertation, Newcastle University).
64. Chang, C.-C. & Lin, C.-J. 2011. LIBSVM: a library for support vector machines. ACM transactions on intelligent systems and technology (TIST), 2, 27.
65. Hebditch, M. & Warwicker, J. 2019. Charge and hydrophobicity are key features in sequence­trained machine learning models for predicting the biophysical properties of clinical-stage antibodies. PeerJ, 7, e8199.
66. Cortegiani, A., Ippolito, M., Greco, M., Granone, V., Protti, A., Gregoretti, C., Giarratano, A., Einav, S. & Cecconi, M.2021. Rationale and evidence on the use oftocilizumab in COVID-19: a systematic review, Pulmonology, 27, 52–6
67. US Food & Drug Administration. 2004. Guidance for Industry PAT — A Framework for Innovative Pharmaceutical Development, Manufacturing, and Quality Assurance https://
www.fda.gov/media/71012/download
68. Kizhedath, A., Wilkinson, S. & Glassey, J. 2017. Applicability of predictive toxicology methods for monoclonal antibody therapeutics: status Quo and scope, Arch Toxicol, 91, 1595– 1612
Model-Based Risk Assessment of mAb Developability 391
https://t.me/medicina_free
69. Zalai, D., Dietzsch C. & Herwig C. 2013. Risk-based process development of biosimilars as part of the Quality by Design paradigm, PDA Journal of Pharmaceutical Science and Technology, 67, 569–580
Design Framework and Tools for Solid
https://t.me/medicina_free
Drug Product Manufacturing Processes
Kensaku Matsunami, Sara Badr, and Hirokazu Sugiyama
1 Introduction
Solid drug products, e.g., tablets and capsules, represent a large fraction of drug product sales, with their sales accounting for more than 50% of the Japanese market [1]. Solid drug products are of different types, e.g., generic, orphan, and blockbuster drugs, which differ in physical properties, demand, and price of raw materials. With the rising pressure for cost reduction in the pharmaceutical industry, solid drug product manufacturing has gained increased attention. An example of a solid drug product manufacturing process, which produces tablets from an active pharmaceutical ingredient (API) in a powder state, is given in Fig. 1. This process is one of the typical manufacturing processes, but there are numerous solid drug product manufacturing process alternatives, e.g., wet granulation, dry granulation, and direct compression. Process alternatives are usually selected in conjunction with clinical trials,where many kinds of uncertainty still exist, e.g., undeterminedprocess parameters and success/failure of the clinical development.
Continuous manufacturing has attracted the attention of the pharmaceutical industry, regulatory authorities, and academia in and beyond solid drug product manufacturing. The pharmaceutical industry traditionally uses batchwise opera­tions, where all the materials are processed at once within each individual unit. Continuous technology enables all unit operations to be interconnected and the materials to be processed at a specific flow rate throughout the entire process. Unlike the chemical industry, continuous technology in the pharmaceutical industry normally has a defined running time, which can also be classified as semicontinuous manufacturing [2]. Continuous technology is expected to have merits regarding
K. Matsunami · S. Badr · H. Sugiyama () Department of Chemical System Engineering, The University of Tokyo, Tokyo, Japan e-mail: sugiyama@chemsys.t.u-tokyo.ac.jp
© The Author(s), under exclusive license to Springer Nature Switzerland AG 2022 A. Fytopoulos et al. (eds.), Optimization of Pharmaceutical Processes, Springer Optimization and Its Applications 189, https://doi.org/10.1007/978-3-030-90924-6_15
393
394 K. Matsunami et al.
https://t.me/medicina_free
Fig. 1 Typical example of a solid drug product manufacturing process
flexibility to change in demand, reduced efforts for scale-up, and fewer required operators. By contrast, there are concerns such as start-up operations, variability of the inputs, and the necessity of real-time quality control. Although continuous tech­nology has the potential to contribute to cost reduction, the benefits vary depending on the product and process characteristics. Thus, process design should reflect such characteristics to adequately evaluate the choice of continuous technology.
Numerous studies have dealt with further innovations, including implementation of continuous technology, development of process control [3, 4], and physical modeling of unit operations [5, 6]. Regarding comparative studies between batch and continuous technologies, case studies of economic assessment (e.g., [7]) and small-scale experimental investigations [8] have been conducted. However, there is still difficulty in applying these studies to practical decision-making in the pharmaceutical industry because previous studies have focused on specific unit operations, alternatives, and products. A pathway of process design needs to be established that has a broader scope covering newer technologies such as continuous manufacturing.
This chapter presents a design framework for solid drug product manufacturing, considering continuous technology as an alternative. First, the design framework is described in the form of an activity model, which defines two newly developed mechanisms as additional design elements. Next, the details of the introduced mechanisms are presented with applications in various case studies. The chapter combines and partly reproduces previous works from our research group published in collaboration with other industrial partners [9–13] and demonstrates their inte­gration into the proposed design framework.
2 Design Framework
The design framework was described by using the type zero method of integration definition for function modeling (IDEF0). The IDEF0 is a function model systemat­ically representing the functions, activities, or processes [14]. This method has been applied to describe various design frameworks, such as chemical process design
Design Framework and Tools for Solid Drug Product Manufacturing Processes 395
https://t.me/medicina_free
Fig. 2 Top activity A0: Design a solid drug product manufacturing process
[15, 16]. The model consists of boxes and arrows (Fig. 2). Each activity is shown in a box as a verb form, e.g., “design a process.” The arrows are classified into four types: input, output (e.g., promising alternatives), control (e.g., regulations), and mechanism (e.g., industrial knowledge) of the activity.
In this study, the IDEF0 viewpoint was set as designers and researchers of formulation and processes. The top activity was defined as “Design a solid drug product manufacturing process” (see Fig. 2). The activity is controlled by the constraints that are characteristic of the pharmaceutical industry, e.g., regulations and clinical trial results. Moreover, the mechanisms of the model define tools and knowledge, which are essential for the process design. Two mechanisms were newly developed by the authors’ research group, in collaboration with industrial experts. One is a tool that enables uncertainty-conscious economic assessment with superstructure-based comprehensive alternative generation (new mechanism 1). The other introduces practical knowledge of continuous technology obtained through experimental investigations (new mechanism 2). The top activity, A0, was divided into four sub-activities (Fig. 3). Sub-activities are managed in activity A1, and both simulations (A2) and experiments (A3) are performed interactively before evaluating alternatives (A4).
The developed design framework can be applied at any decision phase. Controls and mechanisms progressively evolve at each phase; for example, the regulatory constraints become more specific and detailed toward the implementation of the process. This chapter focuses on conceptual design in earlier decision phases, where the degree of uncertainty in product, process, and business is high. Thus, the examples given in this chapter will consider the establishment of conceptual process design during the clinical development phase. The controls and mechanisms
396 K. Matsunami et al.
https://t.me/medicina_free
Fig. 3 Sub-activities of the top activity A0 (activities A1 to A4)
will be adjusted for that purpose. The outputs of the framework in this phase are the promising alternatives regarding process and formulation strategy (to be explained in more detail later).
The application of the framework can be described as follows. After receiving a design request, a design case is defined in A1, which includes the API properties, e.g., solubility, and design phase, e.g., clinical phase. The candidate dosage forms, e.g., tablets or capsules, and types of potential excipients, e.g., mannitol or lactose, are also specified in the design case. The uncertainty regarding the new drug, e.g., expected market size, and the clinical trial results, e.g., drug efficacy, are also considered. Activity A1 manages the conducting and iteration of activities A2 to A4. The simulation (A2) can be further divided into three sub-activities: “generate alternatives” (A21), “analyze processes” (A22), and “assess processes” (A23). Alternatives regarding process and formulation strategy are generated in A21 based on the design case. For each alternative, the process is analyzed to clarify the process characteristics (A22), e.g., start-up time, product loss, required resources (person hours), and the impacts of process parameters on product quality. In activity A23, the economic performance of the alternative is assessed, where the results reflect the uncertainty in the phase concerned, e.g., undetermined process parameters, potential change of the market demand, and success or failure of the clinical development. The two new developed mechanisms are introduced for use in activity A2. New mechanism 1 (assessment tool) is for the systematic
Design Framework and Tools for Solid Drug Product Manufacturing Processes 397
https://t.me/medicina_free
generation, analysis, and assessment of alternatives, the application of which can be assisted by new mechanism 2 (practical knowledge of continuous technology). The details are discussed in the later sections. These simulation activities are conducted concurrently with experiments (A3). Experiments can provide missing but critical information in simulation (represented by the path from activity A3 to A2 through A4 and A1), and simulation can help conduct designed experiments (the path from activity A2 to A3 through A4 and A1). Finally, in activity A4, promising alternatives for processes and the formulation strategy are determined as an output based on the assessment results. During the process design activities, requests for other stakeholders, e.g., clinical developers and API designers, are produced in A1. New findings from the process and product design are integrated with the existing know-how, which is indicated as accumulated knowledge for new drug products in the output.
In the existing framework for bulk chemical process design [15, 16], nonexperi­mental activities, such as flowsheeting and steady-state simulation, were considered as the core of the process design. Because of the nature of the product and the pro­cess, our proposed framework highlights the collaboration between the experimental and simulation investigations. Heterogeneous characteristics of powder materials are, by their nature, difficult to simulate. Repetition of the start-up and shutdown operations for lot-based manufacturing (even for continuous manufacturing) could cause unforeseen phenomena such as clogging of powder materials or machine deterioration/malfunctions. Thus, the effective use of simulation techniques, in particular new mechanism 1 (the economic assessment tool), requires interaction with experiments. In our framework, this point is reflected in the presence of A3 as the main activity and as new mechanism 2 (practical knowledge obtained from experimental analyses) for activity A2.
3 New Mechanism 1: Superstructure-Based Economic
Assessment Tool
In activity A2, alternatives are generated, analyzed, and assessed according to the specifications in the design case, e.g., the potential dosage form or type of excipients. The choice of the processing technologies (wet and dry granulation, or continuous and batch) and formulation strategy (common and proportional, explained later) can be considered. The economic assessment is performed con­sidering the uncertainty in clinical development. New mechanism 1 (Fig. 3)was developed to support these activities and was implemented as an original software “SoliDecision” (the name is a combination of the words “solid” and “decision”). This section introduces this software, together with the implemented algorithm. The full details of the mechanism are presented elsewhere [9].
398 K. Matsunami et al.
https://t.me/medicina_free
Fig. 4 Developed superstructure for solid drug product manufacturing processes [9]
3.1 Generation of Alternatives
Process Alternatives Represented as a Superstructure
The superstructure of the solid drug product manufacturing processes was defined to comprehensively generate possible process alternatives. Figure 4 presents the superstructure, covering various units such as size reduction, spray drying, mixing, granulation, drying, tableting, coating, and encapsulation, from units 1 to 18. Super­scripts B and C represent batch and continuous operation in the unit. To describe the superstructure, the unit, port, conditioning stream (UPCS) representation [17] was adopted. Units are categorized as sources representing the provision of raw materials, sinks for the collection of final products, and general unit operations. Ports represent interfaces between units, e.g., materials transferred such as granules and tablets. The presence of the API in a stream is represented by a solid arrow, while streams with no API are represented as dotted arrows. One process alternative is defined as the connected options of streams, ports, and units starting from source to sink units, which represent the combination of raw materials, processing technologies, and dosage forms.
The superstructure in Fig. 4 was developed after conducting a thorough liter­ature survey and consulting the expert knowledge of the industrial collaborators [9]. In total, 9452 process alternatives were specified, some of which are well­known alternatives, e.g., wet granulation, dry granulation, and direct compression methods. Among these 9452 alternatives, process alternatives were counted under “continuous technology”if all interconnectedunit operations wererun in continuous operation mode with a single manufacturing rate for the entire process. If any of the units was operated in batch mode, then the alternative is counted under