Relevant bibliographies by topics / Batch process system

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers

Academic literature on the topic 'Batch process system'

Author: Grafiati
Published: 4 June 2021
Last updated: 14 February 2022

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Journal articles on the topic "Batch process system"

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E, Kanniga, and Akhil Varma. "History for Batch Process Simulation CM System." International Journal of Psychosocial Rehabilitation 23, no. 4 (July 20, 2019): 354–60. http://dx.doi.org/10.37200/ijpr/v23i4/pr190194.

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Hadiyanto, H., D. Ariyanti, A. P. Aini, and D. S. Pinundi. "Batch and Fed-Batch Fermentation System on Ethanol Production from Whey using Kluyveromyces marxianus." International Journal of Renewable Energy Development 2, no. 3 (October 30, 2013): 127–31. http://dx.doi.org/10.14710/ijred.2.3.127-131.

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Nowadays reserve of fossil fuel has gradually depleted. This condition forces many researchers to find energy alternatives which is renewable and sustainable in the future. Ethanol derived from cheese industrial waste (whey) using fermentation process can be a new perspective in order to secure both energy and environment. The aim of this study was to compare the operation modes (batch and fed-batch) of fermentation system on ethanol production from whey using Kluyveromyces marxianus. The result showed that the fermentation process for ethanol production by fed-batch system was higher at some point of parameters compared with batch system. Growth rate and ethanol yield (YP/S) of fed-batch fermentation were 0.122/h and 0.21 gP/gS respectively; growth rate and ethanol yield (YP/S) of batch fermentation were 0.107/h, and 0.12 g ethanol/g substrate, respectively. Based on the data of biomass and ethanol concentrations, the fermentation process for ethanol production by fed-batch system were higher at some point of parameters compared to batch system. Periodic substrate addition performed on fed-batch system leads the yeast growth in low substrate concentrations and consequently increasing their activity and ethanol productivity. Keywords: batch; ethanol; fed-batch; fermentation;Kluyveromyces marxianus, whey
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Yuan, Zhong Hu, Xiao Yu Qi, and Xiao Wei Han. "Design of Simulation System for Batch Process." Applied Mechanics and Materials 55-57 (May 2011): 1693–98. http://dx.doi.org/10.4028/www.scientific.net/amm.55-57.1693.

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Process monitoring and fault diagnosis of batch process is a research focus in the industrial control field. In this paper, penicillin fermentation is taken as the research background, a visual batch process simulation system is designed based on mathematical models of an actual production process. By introducing different fault signals to the penicillin fermentation simulation process, the designed system can be used to simulate the real penicillin fermentation production process clearly. In the end, an ideal experimental simulation data for batch process fault diagnosis is provided.
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Jamkar, R. G., R. H. Chile, and Y. S. Angal. "PLC based Sequential Batch Process Control System." IETE Technical Review 23, no. 3 (May 2006): 163–71. http://dx.doi.org/10.1080/02564602.2006.11657942.

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Ishii, N., and M. Muraki. "A process-variability-based online scheduling system in multiproduct batch process." Computers & Chemical Engineering 20, no. 2 (February 1996): 217–34. http://dx.doi.org/10.1016/0098-1354(95)00016-u.

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Damayanti, Astrilia, Sarto Sarto, and Wahyudi Budi Sediawan. "Biohydrogen Production by Reusing Immobilized Mixed Culture in Batch System." International Journal of Renewable Energy Development 9, no. 1 (January 16, 2020): 37–42. http://dx.doi.org/10.14710/ijred.9.1.37-42.

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Biohydrogen production via dark fermentation is a prospective renewable energy technology. In the process, reused of immobilized mixed culture is very important as their activities greatly influencehydrogen production. The aim of this work was to evaluate the reuse of alginate beads affecting the biohydrogen production for 45 days. This study in batch reactor were performed using glucose 10 M as substrate, alginate and activated carbon as immobilization matrix materials, chicken eggshell as buffer, and cow dung biodigester as mixed culture. Hydrogen and pH on fermentation product are investigated by gas chromatography (GC) technique and pH meter, respectively. The colony diameter on immobilized and co-immobilized mixed culture was observed using optical microscope and colony diameter was measured using Image-Pro Plus Software v4.5.0.29. The surface morphology of immobilization and co-immobilization beads were determined using scanning electron microscope (SEM). The results showed that the colonies growth observed using optical microscopy or SEM was apparent only in the immobilization of mixed culture. The average growth and diameter of colonies per day were 90 colonies and 0.025 mm, respectively. The weight of beads and pH during the 45-day fermentation process for bead immobilization of mixed culture were 1.32–1.95 g and 6.25–6.62, correspondingly, meanwhile, the co-immobilizations of the mixed culture were 1.735–2.21g and 6.25–6.61, respectively. In addition, the average hydrogen volume of glucose fermented using an eggshell buffer and reusing the immobilization and co-immobilization beads was 18.91 mL for 15 cycles.©2020. CBIORE-IJRED. All rights reserved
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Hashizume, Satoru, Susumu Hashizume, Tomoyuki Yajima, and Katsuaki Onogi. "Construction of Batch Process System Models for Fault Analysis." Journal of Chemical Engineering of Japan 49, no. 7 (2016): 689–97. http://dx.doi.org/10.1252/jcej.15we181.

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Rao, Ming, and Jean Corbin. "Intelligent operation support system for batch chemical pulping process." Engineering Applications of Artificial Intelligence 6, no. 4 (August 1993): 357–80. http://dx.doi.org/10.1016/0952-1976(93)90019-t.

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Cao, Zhixing, Jingyi Lu, Ridong Zhang, and Furong Gao. "Online average-based system modelling method for batch process." Computers & Chemical Engineering 108 (January 2018): 128–38. http://dx.doi.org/10.1016/j.compchemeng.2017.09.005.

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Peng, Chang, RuiWei Lu, Olivia Kang, and Wang Kai. "Batch process fault detection for multi-stage broad learning system." Neural Networks 129 (September 2020): 298–312. http://dx.doi.org/10.1016/j.neunet.2020.05.031.

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Dissertations / Theses on the topic "Batch process system"

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Mau, K. Y. "The development of a real-time process control batch/semi-batch expert advisory system." Thesis, London South Bank University, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.618636.

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MacRosty, R. D. M. "Optimal scheduling of an integrated batch and continuous process system." Master's thesis, University of Cape Town, 2000. http://hdl.handle.net/11427/7686.

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Bibliography: leaves 136-139.
An industrial problem has been posed involving the determination of the optimal scheduling and sequencing of a batch process system. The plant incorporates both batch and continuous units and is further complicated by the existence of a nonlinear relationship between the processing rate and the lot size in the continuous plant. The primary goal of this project is to investigate the application of a rigorous mathematical approach to determine the optimal operating policy of a complex processing system. In broad terms, scheduling involves the allocation of a limited number of resources to ensure the completion of a set of tasks, in an optimal way. The problem is formulated as a mathematical model through the use of mixed-integer programming. The difficulty associated with this type of work is in describing the plant using constraints to develop a mathematical model which both accurately reflects the plant and renders the problem solvable. The model must incorporate the connectivity of the plant and prevent resource-task allocation conflicts. A survey of the pertinent literature has been conducted and is reviewed in Chapter 2. Here the principles of batch scheduling are addressed. The focus of the literature review is on the formulation of such problems into a mathematical representation. A description of two fundamentally different approaches for the formulation of short-term scheduling problems is presented. Other aspects of the review include the commercially available software used in the solution of these problems, campaign planning and on-line scheduling. The work in this thesis initially focuses on the scheduling of a simplified version of the industrial plant. The simplified version consists exclusively of batch processing units. The motivation for this was to develop a formulation which incorporated the unique characteristics of the full problem but was computationally easier to solve. A number of scenarios were conducted which show both the flexibility of the formulation and the ability of the formulation to reschedule tasks when faced with different operating conditions. In the discussion of these scenarios, issues such as the computational efficiency and the implications of the results are addressed. The next step was to add a continuous plant upstream to the simplified batch process. The continuous plant exhibits a nonlinear relationship between the processing rate and the efficiency of operation. An approximation of the non-linearity is proposed and further scenario studies are carried out. Finally, the full problem is tackled but due to the great computational expense required to solve the problem an alternative method is proposed. This method is based on a series of random-type scenarios, which serve as an alternative as well as benchmark to the solutions obtained via rigorous optimization.
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Liu, Zhen Hai. "An advanced process manufacturing system : design and application to a food processing pilot plant." Thesis, Imperial College London, 1995. http://hdl.handle.net/10044/1/8694.

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ONOGI, Katsuaki, Tomoyuki YAJIMA, Susumu HASHIZUME, and Takashi ITO. "Integration between Scheduling and Design of Batch Systems Based on Petri Net Models." Institute of Electronics, Information and Communication Engineers, 2005. http://hdl.handle.net/2237/14964.

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Edreder, E. A. "Modelling and optimisation of batch distillation involving esterification and hydrolysis reaction systems. Modelling and optimisation of conventional and unconventional batch distillation process: Application to esterification of methanol and ethanol using acetic acid and hydrolysis of methyl lactate system." Thesis, University of Bradford, 2010. http://hdl.handle.net/10454/4296.

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Batch distillation with chemical reaction when takes place in the same unit is referred to as batch reactive distillation process. The combination reduces the capital and operating costs considerably. Among many different types of batch reactive distillation column configurations, (a) conventional (b) inverted (c) semi-batch columns are considered here. Three reaction schemes such as (a) esterification of methanol (b) esterification of ethanol (c) hydrolysis of methyl lactate are studied here. Four different types of dynamic optimisation problems such as (a) maximum conversion (b) maximum productivity (c) maximum profit and (d) minimum time are formulated in this work. Optimal design and or operation policies are obtained for all the reaction schemes. A detailed rigorous dynamic model consisting of mass, energy balances, chemical reaction and thermodynamic properties is considered for the process. The model was incorporated within the dynamic optimisation problems. Control Vector Parameterisation (CVP) technique was used to convert the dynamic optimisation problem into a nonlinear programming problem which was solved using efficient SQP (Successive Quadratic Programming) method available within the gPROMS (general PROcess Modelling System) software. It is observed that multi-reflux ratio or linear reflux operation always led to better performance in terms of conversion, productivity for all reaction schemes compared to that obtained using single reflux operation. Feed dilution (in the case of ethanol esterification) led to more profit even though productivity was found to be lower. This was due to reduction in feed price because of feed dilution. Semi-batch reactive distillation opertation (for ethanol esterification) led to better conversion compared to conventional batch distillation, however, the total amount of acetic acid (reactant) was greater in semi-batch operation. Optimisation of design and operation (for ethanol esterification) clearly showed that a single cloumn will not lead to profitable operation for all possible product demand profile. Also change in feed and /or product price may lead to adjust the production target to maximise the profitability. In batch distillation, total reflux operation is recommended or observed at the begining of the operation (as is the case for methnaol or ethanol esterification). However, in the case of hydrolysis, total reflux operation was obseved at the end of the operation. This was due to lactic acid (being the heaviest) was withrawn as the final bottom product.
Libyan Petroleum Institute
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Edreder, Elmahboub A. "Modelling and optimisation of batch distillation involving esterification and hydrolysis reaction systems : modelling and optimisation of conventional and unconventional batch distillation process : application to esterification of methanol and ethanol using acetic acid and hydrolysis of methyl lactate system." Thesis, University of Bradford, 2010. http://hdl.handle.net/10454/4296.

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Batch distillation with chemical reaction when takes place in the same unit is referred to as batch reactive distillation process. The combination reduces the capital and operating costs considerably. Among many different types of batch reactive distillation column configurations, (a) conventional (b) inverted (c) semi-batch columns are considered here. Three reaction schemes such as (a) esterification of methanol (b) esterification of ethanol (c) hydrolysis of methyl lactate are studied here. Four different types of dynamic optimisation problems such as (a) maximum conversion (b) maximum productivity (c) maximum profit and (d) minimum time are formulated in this work. Optimal design and or operation policies are obtained for all the reaction schemes. A detailed rigorous dynamic model consisting of mass, energy balances, chemical reaction and thermodynamic properties is considered for the process. The model was incorporated within the dynamic optimisation problems. Control Vector Parameterisation (CVP) technique was used to convert the dynamic optimisation problem into a nonlinear programming problem which was solved using efficient SQP (Successive Quadratic Programming) method available within the gPROMS (general PROcess Modelling System) software. It is observed that multi-reflux ratio or linear reflux operation always led to better performance in terms of conversion, productivity for all reaction schemes compared to that obtained using single reflux operation. Feed dilution (in the case of ethanol esterification) led to more profit even though productivity was found to be lower. This was due to reduction in feed price because of feed dilution. Semi-batch reactive distillation opertation (for ethanol esterification) led to better conversion compared to conventional batch distillation, however, the total amount of acetic acid (reactant) was greater in semi-batch operation. Optimisation of design and operation (for ethanol esterification) clearly showed that a single cloumn will not lead to profitable operation for all possible product demand profile. Also change in feed and /or product price may lead to adjust the production target to maximise the profitability. In batch distillation, total reflux operation is recommended or observed at the begining of the operation (as is the case for methnaol or ethanol esterification). However, in the case of hydrolysis, total reflux operation was obseved at the end of the operation. This was due to lactic acid (being the heaviest) was withrawn as the final bottom product.
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Ibrahim, W. H. B. W. "Dynamic Modelling and Optimization of Polymerization Processes in Batch and Semi-batch Reactors. Dynamic Modelling and Optimization of Bulk Polymerization of Styrene, Solution Polymerization of MMA and Emulsion Copolymerization of Styrene and MMA in Batch and Semi-batch Reactors using Control Vector Parameterization Techniques." Thesis, University of Bradford, 2011. http://hdl.handle.net/10454/5392.

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Dynamic modelling and optimization of three different processes namely (a) bulk polymerization of styrene, (b) solution polymerization of methyl methacrylate (MMA) and (c) emulsion copolymerization of Styrene and MMA in batch and semi-batch reactors are the focus of this work. In this work, models are presented as sets of differential-algebraic equations describing the process. Different optimization problems such as (a) maximum conversion (Xn), (b) maximum number average molecular weight (Mn) and (c) minimum time to achieve the desired polymer molecular properties (defined as pre-specified values of monomer conversion and number average molecular weight) are formulated. Reactor temperature, jacket temperature, initial initiator concentration, monomer feed rate, initiator feed rate and surfactant feed rate are used as optimization variables in the optimization formulations. The dynamic optimization problems were converted into nonlinear programming problem using the CVP techniques which were solved using efficient SQP (Successive Quadratic Programming) method available within the gPROMS (general PROcess Modelling System) software. The process model used for bulk polystyrene polymerization in batch reactors, using 2, 2 azobisisobutyronitrile catalyst (AIBN) as initiator was improved by including the gel and glass effects. The results obtained from this work when compared with the previous study by other researcher which disregarded the gel and glass effect in their study which show that the batch time operation are significantly reduced while the amount of the initial initiator concentration required increases. Also, the termination rate constant decreases as the concentration of the mixture increases, resulting rapid monomer conversion. The process model used for solution polymerization of methyl methacrylate (MMA) in batch reactors, using AIBN as the initiator and Toluene as the solvent was improved by including the free volume theory to calculate the initiator efficiency, f. The effects of different f was examined and compared with previous work which used a constant value of f 0.53. The results of these studies show that initiator efficiency, f is not constant but decreases with the increase of monomer conversion along the process. The determination of optimal control trajectories for emulsion copolymerization of Styrene and MMA with the objective of maximizing the number average molecular weight (Mn) and overall conversion (Xn) were carried out in batch and semi-batch reactors. The initiator used in this work is Persulfate K2S2O8 and the surfactant is Sodium Dodecyl Sulfate (SDS). Reduction of the pre-batch time increases the Mn but decreases the conversion (Xn). The sooner the addition of monomer into the reactor, the earlier the growth of the polymer chain leading to higher Mn. Besides that, Mn also can be increased by decreasing the initial initiator concentration (Ci0). Less oligomeric radicals will be produced with low Ci0, leading to reduced polymerization loci thus lowering the overall conversion. On the other hand, increases of reaction temperature (Tr) will decrease the Mn since transfer coefficient is increased at higher Tr leading to increase of the monomeric radicals resulting in an increase in termination reaction.
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Larsson, Johan. "High-throughput Fed-batch Production of Affibody® molecules in a novel Multi-fermentor system." Thesis, Linköping University, The Department of Physics, Chemistry and Biology, 2005. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-3490.

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The present Master thesis describes the development and optimization of a fed-batch process for production of recombinant proteins in Escherichia coli BL21(DE3) in a multi-fermentor system. The system consists of six 1-liter fermentors, capable of producing 500-1500 μg/mL with present protocol.

Response surface methodology (RSM) was used for multivariable optimization regarding cultivation time, pH, temperature and feed rate. Optimal protein expression conditions were found out to be 17.8 h cultivation time, 36.7 ºC, pH 6.8 and a feed rate corresponding to specific growth of 0.23 h-1, on glucose substrate. The aggregation of expressed proteins to inclusion bodies, could not be affected by the various growth conditions employed during cultivations.

A study was conducted regarding growth conditions effect on phosphogluconoylation of expressed proteins. In ten fed-batch cultivations on glucose, LC/MS analysis showed a gluconoylated fraction with additional 178 Da mass, but no correlation between growth conditions and gluconoylation could be found. In two fed-batch cultivations on glycerol-feed, a lower feed rate resulted in no gluconoylation, while a higher did. An explanation would be that the lower amount of available intra-cellular carbon limits formation of gluconoylation precursors.

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Walker, Helen R. "The design and development of a computer aided process planning decision support system within the small batch, discrete parts manufacturing environment." Thesis, Brunel University, 1990. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.277627.

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Fridman, Belinda. "Process development for the production of a therapeutic Affibody® Molecule." Thesis, Uppsala universitet, Institutionen för biologisk grundutbildning, 2014. http://urn.kb.se/resolve?urn=urn:nbn:se:uu:diva-218861.

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Recently HER3, member of the epidermal growth factor receptor family (EGFR), has been found to play a crucial role in the development of resistance towards inhibitors that are given to patients with HER1- and HER2-driven cancers. As HER3 is up-regulated or over-activated in several types of human cancers, it is of outmost importance that new innovative drugs target its oncologic activity. The Affibody® Molecule Z08698 inhibits the heregulin induced signalling of HER3 with high affinity (KD~50 pM). As the Affibody® Molecule is small, has high solubility and outstanding folding kinetics, an effective penetration of tumour tissue is suggested together with a rationalized manufacturing process. Further coupling to an albumin binding domain (ABD) expands the plasma half-life of the molecule, hence increasing the molecule's potential of serving as a therapeutic. A process development for production of Z08698-VDGS-ABD094 has been established, where the molecule is efficiently produced in the E. coli host strain BL21(DE3), through a T7 based expression system. Cultivations were performed with a fed-batch fermentation process and the conditions were further optimized in order to obtain highest expression, while avoiding undesirable modifications like gluconoylations. By employing Design of experiments in combination with multivariate data analysis, a production process resulting in ~3.5 g product/ l culture could be verified. Moreover, thermolysis was evaluated as a suitable method for cell disruption, enabling an easy and cost-effective manufacturing process of the ABD fused Affibody® Molecule.
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Books on the topic "Batch process system"

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Walker, Helen R. The design and development of a computer aided process planning decision support system within the small batch, discrete parts manufacturing environment. Uxbridge: Brunel University, 1990.

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Thomas, Fisher, and Fisher Thomas, eds. Batch control systems: Design, application, and implementation. 2nd ed. Research Triangle Park, NC: ISA, 2005.

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Fisher, Thomas G. Batch control systems: Design, application, and implementation. Research Triangle Park, N.C: Instrument Society of America, 1990.

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American Institute of Chemical Engineers. Center for Chemical Process Safety. Guidelines for process safety in batch reaction systems. New York: Center for Chemical Process Safety of the American Institute of Chemical Engineers, 1999.

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NATO Advanced Study Institute on Batch Processing Systems Engineering: Current Status and FutureDirections (1992 Antalya, Turkey). Batch processing systems engineering: Fundamentals and applications for chemical engineering. Berlin: Springer, 1996.

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Sadr-Kazemi, N. Design of energy storage-systems for batch process plants. Manchester: UMIST, 1995.

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Webb, Marcus Charles. Control system design for an analogue batch process simulator. Bradford, 1987.

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Hawkins, William M., and Thomas G. Fisher. Batch Control Systems: Design, Application, and Implementation. 2nd ed. ISA-Instrumentation, Systems, and Automation Society, 2006.

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CCPS (Center for Chemical Process Safety). Guidelines for Process Safety in Batch Reaction Systems. American Institute of Chemical Engineers, 2010.

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Center for Chemical Process Safety (CCPS). Guidelines for Process Safety in Batch Reaction Systems. Wiley-AIChE, 1999.

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Book chapters on the topic "Batch process system"

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Sakaki, Y., K. Matsunaga, and I. W. Hoekstra. "Batch Process Control and Recipe Management Using a Distributed Control System." In Fortschritte in der Meß- und Automatisierungstechnik durch Informationstechnik, 223–32. Berlin, Heidelberg: Springer Berlin Heidelberg, 1986. http://dx.doi.org/10.1007/978-3-642-95506-8_18.

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Rosenof, Howard P., and Asish Ghosh. "Automation Systems." In Batch Process Automation, 65–93. Boston, MA: Springer US, 1987. http://dx.doi.org/10.1007/978-1-4684-6641-6_6.

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Clark, Steven M., and Girish S. Joglekar. "Simulation Software for Batch Process Engineering." In Batch Processing Systems Engineering, 376–92. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_18.

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Shaik, Munawar A., and Christodoulos A. Floudas. "Short-Term Scheduling of Batch and Continuous Processes." In Process Systems Engineering, 173–217. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527631209.ch37.

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Shaik, Munawar A., and Christodoulos A. Floudas. "Short-Term Scheduling of Batch and Continuous Processes." In Process Systems Engineering, 173–217. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2011. http://dx.doi.org/10.1002/9783527631278.ch6.

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Ponton, Jack W. "Artificial Intelligence Techniques in Batch Process Systems Engineering." In Batch Processing Systems Engineering, 517–29. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_23.

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Reklaitis, G. V. "Overview of Scheduling and Planning of Batch Process Operations." In Batch Processing Systems Engineering, 660–705. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_27.

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Lucet, Michel, Andre Charamel, Alain Chapuis, Gilbert Guido, and Jean Loreau. "Role of Batch Processing in the Chemical Process Industry." In Batch Processing Systems Engineering, 43–48. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_3.

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Hasebe, Shinji, and Iori Hashimoto. "Present Status of Batch Process Systems Engineering in Japan." In Batch Processing Systems Engineering, 49–77. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_4.

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Sørenson, Eva, and Sigurd Skogestad. "Control Strategies for a Combined Batch Reactor/Batch Distillation Process." In Batch Processing Systems Engineering, 274–94. Berlin, Heidelberg: Springer Berlin Heidelberg, 1996. http://dx.doi.org/10.1007/978-3-642-60972-5_13.

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Conference papers on the topic "Batch process system"

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Rodler, M., Martin Melik-Merkumians, W. Lepuschitz, and M. Merdan. "Visualization of an agent-based batch process system." In 2013 IEEE International Conference on Industrial Technology (ICIT 2013). IEEE, 2013. http://dx.doi.org/10.1109/icit.2013.6505880.

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Kadam, Vivek, Sharad Jadhav, Mahesh Parihar, and Amit Karande. "Development of wireless embedded automation system for batch process." In 2015 5th Nirma University International Conference on Engineering (NUiCONE). IEEE, 2015. http://dx.doi.org/10.1109/nuicone.2015.7449593.

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Li, Wei, Rod J. Fretwell, and Demetres D. Kouvatsos. "Analysis of Correlated Traffic by Batch Renewal Process." In 2009 International Conference on E-Business and Information System Security (EBISS). IEEE, 2009. http://dx.doi.org/10.1109/ebiss.2009.5137930.

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Hamzah, Nuramalina, Sherif Abdulbari Ali, and Siti Fatma Abd Karim. "Improvement of Process Quality via Integration of Statistical Process Control and Engineering Process Control in Batch Process." In 2020 IEEE 10th International Conference on System Engineering and Technology (ICSET). IEEE, 2020. http://dx.doi.org/10.1109/icset51301.2020.9265367.

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Guo, Jinyu, Yuan Li, Guozhu Wang, and Jing Zeng. "Batch Process Monitoring Based on Multilinear Principal Component Analysis." In 2010 International Conference on Intelligent System Design and Engineering Application (ISDEA). IEEE, 2010. http://dx.doi.org/10.1109/isdea.2010.274.

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Wu, Zhihui, and Yu Qian. "A study on computer aided process integration system design for chemical batch process development." In 2010 2nd International Conference on Networking and Digital Society (ICNDS). IEEE, 2010. http://dx.doi.org/10.1109/icnds.2010.5479446.

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Song, J. R., H. W. Wang, H. B. Shi, and SH H. Zhang. "Iterative Learning Control and It's Application to Batch Process Optimization." In 2011 Third Pacific-Asia Conference on Circuits, Communications and System (PACCS). IEEE, 2011. http://dx.doi.org/10.1109/paccs.2011.5990241.

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Kadam, Vivek S., Sharad P. Jadhav, and Mahesh N. Parihar. "Development and analysis of wireless controlled batch process system using ARM." In 2015 International Conference on Communications and Signal Processing (ICCSP). IEEE, 2015. http://dx.doi.org/10.1109/iccsp.2015.7322744.

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9

George, Halim,. "Fuzzy Supervisory Control System for a Fed-Batch Baker's Yeast Fermentation Process." In Information Control Problems in Manufacturing, edited by Bakhtadze, Natalia, chair Dolgui, Alexandre and Bakhtadze, Natalia. Elsevier, 2009. http://dx.doi.org/10.3182/20090603-3-ru-2001.00171.

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Wang, Xuefeng, Na Li, Yaowei Liu, Mingzhu Sun, and Xin Zhao. "Pipelined batch-operation process of nuclear transplantation based on micro-manipulation system." In 2016 IEEE International Conference on Robotics and Biomimetics (ROBIO). IEEE, 2016. http://dx.doi.org/10.1109/robio.2016.7866518.

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