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Efficient MILP formulations for the optimal synthesis of chromatographic protein purification processes.

The use of recombinant proteins has increased greatly in recent years, as well as the techniques used for their purification. The selection of an efficient process to purify proteins is a major bottleneck found when trying to scale up results obtained in the laboratory to a large-scale industrial process. One of the main challenges in the synthesis of downstream purification stages in biotechnological processes is the appropriate selection and sequencing of chromatographic steps. The objective of this work is to develop mixed integer linear programming models for the synthesis of protein purification processes. Models for each chromatographic technique rely on physicochemical data of a protein mixture, which contains the desired product and provide information on its potential purification. Formulations that are based on convex hull representations are proposed to calculate the minimum number of steps from a set of chromatographic techniques that must achieve a specified purity level and alternatively to maximize purity for a given number of steps. The proposed models are tested in several examples with experimental data and present time reductions of up to three orders of magnitude when compared to big-M formulations.

Biotechnology↗

Sonication effect on cellular material in sedimentation and gravitational field flow fractionation.

Sonication procedures are generally used prior to field flow fractionation (FFF) separation in order to produce suspensions without aggregates. Yeast cells manufactured in active dry wine yeast (ADWY) were placed in an ultrasound water bath in order to disrupt possible clumps and to obtain a single-cell suspension to be used in optimal conditions during fermentation processes. In order to determine whether this sample preparation procedure meets absolute needs, different yeast samples before and after sonication were analysed by two field flow fractionation techniques. It is shown that 2 min of sonication in the sample preparation process is sufficient to obtain an optimal dispersion of the yeast cells, that is, without critical percentage of aggregates. To demonstrate this effect, photographs of the yeast cell suspensions were performed with non-sonicated and sonicated yeast sample dispersion. The resulting data are compared with the elution profiles obtained from the two different FFF techniques. It is demonstrated that fractogram profiles prove the effectiveness of sonication methodologies.

Fractionation, Field Flow↗

Fundamentals of the psoralen-based Helinx technology for inactivation of infectious pathogens and leukocytes in platelets and plasma.

Psoralens plus ultraviolet A (UVA) light inactivate viruses and bacteria as well as leukocytes. A system employing the synthetic psoralen compound amotosalen hydrochloride (S-59), in combination with UVA light, is being developed to decontaminate platelet concentrates and plasma in a blood-bank setting. S-59 is a heterocyclic psoralen compound that reacts by a three-step process with nucleic acids (NAs): (1) S-59 intercalates into the double helix; (2) upon illumination with long-wavelength ultraviolet light (UVA), it covalently attaches to a single strand, forming a monoadduct; and (3) additional illumination causes a photoreaction of the monoadduct with the second NA strand, resulting in an interstrand crosslink. The reaction occurs with the genomic material of DNA- and RNA-based viruses and occurs in genomes that are single stranded as well as double stranded. Inactivation rate is related to genome size. Large genomes such as those in leukocytes are far more susceptible to inactivation than are viruses such as hepatitis B virus (HBV), which is inactivated (>10(5) logs) under conditions being developed for blood-bank use. The efficiency of the process is affected by a number of practical considerations such as solution components and light source. The S-59 photochemical treatment process (PCT) has been optimized for platelet concentrates as currently processed for transfusion.

DNA↗

A hybrid artificial neural network as a software sensor for optimal control of a wastewater treatment process.

For control and automation of biological treatment processes, lack of reliable on-line sensors to measure water quality parameters is one of the most important problems to overcome. Many parameters cannot be measured directly with on-line sensors. The accuracy of existing hardware sensors is also not sufficient and maintenance problems such as electrode fouling often cause trouble. This paper deals with the development of software sensor techniques that estimate the target water quality parameter from other parameters using the correlation between water quality parameters. We focus our attention on the preprocessing of noisy data and the selection of the best model feasible to the situation. Problems of existing approaches are also discussed. We propose a hybrid neural network as a software sensor inferring wastewater quality parameter. Multivariate regression, artificial neural networks (ANN), and a hybrid technique that combines principal component analysis as a preprocessing stage are applied to data from industrial wastewater processes. The hybrid ANN technique shows an enhancement of prediction capability and reduces the overfitting problem of neural networks. The result shows that the hybrid ANN technique can be used to extract information from noisy data and to describe the nonlinearity of complex wastewater treatment processes.

Automation↗

Optimization of the solid state fermentation process to obtain tempeh from hardened chickpeas (Cicer arietinum L.).

Solid state fermentation (SSF) represents a technological alternative for a great variety of cereals and legumes, or combination of them, to improve their nutritional quality and to obtain edible products with palatable sensorial characteristics. The objective of this work was to find the best conditions of fermentation temperature and time to obtain tempeh from hardened chickpeas (Cicer arietinum L.) applying SSF. Response surface methodology (RSM) was applied over three response variables (phytic acid, in vitro protein digestibility and available lysine) to find best conditions of fermentation to carry out the process. A central composite experimental design with two factors [X1 = temperature (31-36 degrees C) and X2 = time (48-72 h)] in five levels (2 factorials, 2 axial, I central) was used. Spores from Rhizopus stolonifer were suspended in distilled water (1 x 10(6) spores/mL) and used as starter. According to regression models, minimum and maximum levels of the response variables were 1.24-2.66 mg phytic acid/g of sample DM, 77.6-83.5% in vitro protein digestibility and 2.18-4.63 g available lysine/16 g N. The superposition of contour plots of each one of the response variables allowed researchers to find, graphically, the best conditions for the SSF process: 35.8 degrees C for 42.7 h.

Fabaceae↗

Optimal Thermal Environments for Plant Metabolic Processes (Cucumis sativus L.) (Light-Harvesting Chlorophyll a/b Pigment-Protein Complex of Photosystem II and Seedling Establishment in Cucumber).

Analysis of the temperatures providing maximal photosystem II fluorescence reappearance following illumination and thermal kinetic windows (TKWs), obtained from the temperature characteristics of enzyme apparent Km values, have been proposed as indicators of the bounds of thermal stress in plants. In this study, we have evaluated the temperature optimum for the accumulation of the chlorophyll a/b light-harvesting complex of photosystem II (LHCP II), its mRNA, and the mRNA of the small subunit of ribulose-1,5-bisphosphate carboxylase/oxygenase (Rubisco) in cucumber (Cucumis sativus L. cv Ashley) as a broader measure of metabolism than that provided by either the fluorescence reappearance or TKWs. The TKW for cucumber is between 23.5 and 39[deg]C, with the minimum apparent Km occurring at 32.5[deg]C. The photosystem II variable fluorescence reappearance following illumination was maximal between 30 and 35[deg]C. Maximum synthesis of the LHCP II occurred at 30[deg] C. The light-induced accumulation of the LHCP II and the small subunit of Rubisco mRNAs showed similar temperature characteristics. Suboptimal temperatures delayed germination, altered cotyledonary soluble sugar content, and broadened the temperature range for chlorophyll accumulation. These results demonstrate an effect of seed reserve mobilization on the range of temperatures for chlorophyll accumulation, and suggest that metabolic temperature characteristics may be broadened by increasing available substrates for enzyme utilization. This study provides new information about the relationship between TKWs and cellular responses to temperature. In addition, the results suggest that the temperature range outside of which plants experience temperature stress is narrower than traditionally supposed.

Journal Article↗

Recruitment of MHC class I molecules by tapasin into the transporter associated with antigen processing-associated complex is essential for optimal peptide loading.

The ER protein tapasin (Tpn) forms a bridge between MHC class I H chain (HC)/beta(2)-microglobulin and the TAP peptide transporter. The function of this TAP-associated complex was unclear because it was reported that soluble Tpn that has lost TAP interaction would be fully competent in terms of peptide loading and Ag presentation. We found, however, that only wild-type human Tpn (hTpn), but not three soluble hTpn variants, a transmembrane domain point mutant of hTpn (L410-->F), wild-type mouse Tpn, nor a mouse-human Tpn hybrid, fully up-regulated peptide-dependent Bw4 epitopes when expressed in Tpn-deficient.220.B*4402 cells. Consistent with suboptimal peptide loading, the t(1/2) of class I molecules was considerably reduced in the presence of soluble hTpn, hTpn-L410F, and murine Tpn. Furthermore, eluted peptide spectra and the class I-mediated inhibition of NK clones showed distinct differences to the hTpn transfectant. Only wild-type hTpn efficiently recruited HC and calreticulin (Crt) into complexes with TAP and endoplasmic reticulum p57 (ERp57). The L410F mutant was defective in TAP association, but bound to class I molecules, Crt, and ERp57. Mouse Tpn associated with human TAP and ERp57 on the one hand, and with HC and Crt on the other, but failed to recruit normal amounts of HLA class I molecules into the TAP complex. We conclude that the loading with peptides conferring high stability requires the Tpn-mediated introduction of HC into the TAP complex, whereas the mere interaction with Tpn is not sufficient.

ATP Binding Cassette Transporter, Subfamily B, Mem↗

Open information systems and data security in medicine.

The realization of the German law for a new structure of health care delivery by the assurance of efficient structures and processes in hospitals calls for an optimal design of informational processes. To realize applications near to the users and just in time as well as to build up the complex functional relationships between departments and subsystems in big hospitals, a new design for Hospital Information Systems (HIS) is necessary. The features of modern HIS outlined in the paper can only be established by open systems, which guarantee portability, scalability and interoperability. This is also true in regionally distributed systems like the tumour register at Cancer Centres. In the paper the necessity and possibilities of open systems and different levels of application integration are discussed. The general statements are illustrated by practical realizations in the HIS of the Magdeburg University Hospital as well as in the tumour register at the Cancer Centre of Magdeburg/Sachsen-Anhalt. The creation of integrated structures for communications makes great demands on the assurance of data security and data protection, especially for the inclusion of external partners from the region. In the context of high sensitive data of cancer patients data protection is of top priority. The legal problems of data collection, data storage and exchange in medicine are discussed first. The paper presents some aspects of the concept for data security and data protection in the Magdeburg University HIS and of the related concept for data protection in the tumour register of the Cancer Centre Magdeburg/Sachsen-Anhalt. Appropriate steps of realization are demonstrated. The application of hardware based modern access control systems with integrated encryption of data follows. The statements are extended to the planned installation of hardware based network access control systems with integrated encryption of data in the LAN.

Computer Communication Networks↗

Optimization of the ethylene oxide sterilization process.

Hospitals and manufacturers of medical supplies use ethylene oxide (EO) gas almost exclusively to sterilize devices that are heat sensitive. However, the evidence relating the mutagenicity and cytogeneticity shows the desirability of reducing personal exposure to a practical minimum.

Central Supply, Hospital↗

Optimizing nitrogen removal in the BioDenitro process.

The potential and limits of different configurations of the BioDenitro-alternating process to suit the various design cases that can arise depending on the wastewater characteristics, space necessary and effluent nitrogen requirements were analysed through simulations of the activated sludge model No. 2. The first analysis involved the combination in one cycle of the main phase in the alternating reactors with an aerated phase having the two reactors in aerobic conditions and/or a hydraulic phase using the flow only in the anoxic reactor. This option has been found to have a very high potential for cases with strict requirements concerning effluent total nitrogen, but limited when the requirements are low effluent NH4-N, relatively high effluent total nitrogen and minimum solids and hydraulic retention times. When the latter conditions have to be fulfilled the incorporation of a post-aeration reactor to the alternating reactor was found to be very effective. In addition the configuration is very flexible because multiple combinations of post-aeration reactor volumes and in the duration of the different phases in the alternating reactors can be selected to achieve effluent nitrogen requirements. This flexibility is limited to the use of moderate values in the post-aeration reactor volumes and in the duration of the aerated phase. An experimental trial of the latter configuration was carried out and demonstrated its operational simplicity by achieving the desired nitrogen requirements in the effluent simply by changing the duration of the aerated phase for a given post-aeration reactor volume. From the experimental results an enhanced simultaneous nitrification-denitrification at the start of aeration in the alternating reactors was found and the ASM2 model was shown to have a satisfactory predictive capacity.

Bioreactors↗

Use of industrial wastewaters for the optimization and control of nitrogen removal processes.

In this experimental study the characterization of 2 industrial wastewaters, coming from an ice cream production industry (IW1) and a beet-sugar factory (IW2), with respect to their readily biodegradable fraction and denitrification potential, has been performed. To this end physical-chemical and biological characterization methods, both anoxic and aerobic, were used. Moreover a pilot scale SBR fed with municipal wastewater was started to verify the effect of the gradual addition of the concentrated organic wastewaters during the anoxic phase. The SBR was initially fed only with a primary municipal wastewater, then the organic load was increased by adding to the feed, during the anoxic phase, a small amount of the IW1 (second period). Once the initial conditions were restored the load was again raised using the second industrial wastewater (IW2) (third period). With those additions the nitrogen removal efficiency increased from 26% to 50%, in the case of the IW1 and from 23% to 53% in the case of the wastewater IW2, without any negative effect on the global performance of the system. In addition, periodical kinetic studies of denitrification and nitrification in the SBR, were performed.

Ammonia↗

[Optimization of the pertussis vaccine production process].

The production of Pertussis Vaccine was reevaluated at the Instituto Nacional de Higiene "Rafael Rangel" in order to optimise it in terms of vaccine yield, potency, specific toxicity and efficiency (cost per doses). Four different processes, using two culture media (Cohen-Wheeler and Fermentación Glutamato Prolina-1) and two types of bioreactors (25 L Fermentador Caracas and a 450 L industrial fermentor) were compared. Runs were started from freeze-dried strains (134 or 509) and continued until the obtention of the maximal yield. It was found that the combination Fermentación Glutamato Prolina-1/industrial fermentor, shortened the process to 40 hours while consistently yielding a vaccine of higher potency (7.91 +/- 2.56 IU/human dose) and lower specific toxicity in a mice bioassay. In addition, the physical aspect of the preparation was rather homogeneous and free of dark aggregates. Most importantly, the biomass yield more than doubled those of the Fermentador Caracas using the two different media and that in the industrial fermentor with the Cohen-Wheeler medium. Therefore, the cost per doses was substantially decreased.

Animals↗