I would like to acknowledge Dr. Thomas Rademacher for providing the transgenic tobacco seeds and Ibrahim Al Amedi for cultivating the tobacco plants. I wish to thank Dr. Richard M Twyman for editorial assistance and Prof. Dr. Rainer Fischer for fruitful discussions. This work was funded in part by the European Research Council Advanced Grant ''Future-Pharma'', proposal number 269110, the Fraunhofer-Zukunftsstiftung (Fraunhofer Future Foundation) and the Fraunhofer-Gesellschaft Internal Programs under Grant No. Attract 125-600164.

1. Develop an Adequate Experimental Strategy
<ol>
	<li>Identify the environmental and process parameters that are relevant for the flocculation procedure to be established or optimized, i.e. which factors have the strongest effect on flocculation. Typically, there are several such parameters so a DoE approach as recently described 20 is necessary due to the lack of mechanistic models.
	<ol>
		<li>Select parameters (factors) based on literature data 12, prior knowledge and experience with the system. Typical factors include buffer pH, buffer conductivity, incubation time and temperature as well as polymer type and concentration 15,16,27.</li>
		<li>Use the same references (see 1.1) to define meaningful ranges for each numeric factor and levels for categorical factors.</li>
		<li>Define the experimental outcomes (responses) to be monitored and used to evaluate the efficiency of flocculation. Depending on the system, this can be filtrate or supernatant turbidity, settling velocity, aggregate size or the capacity of a subsequent filter 16,23,28-30.</li>
		<li>Ensure the assays used to measure the responses are quantitative, robust and repeatable/reproducible so that the resulting high-quality data can be augmented with experiments performed later or by another operator.</li>
	</ol>
	</li>
	<li>Choose a DoE type suiting the number of factors to be investigated and the degree of knowledge already accumulated about the system. Use available literature to identify a suitable DoE type 20.
	<ol>
		<li>Select a screening design if there is little information about the flocculation system to be investigated, a large number of parameters must be screened or little is known about meaningful ranges for the parameters. Typical screening designs are full and fractional factorial designs. Include center points in the design if the parameters are expected to have a non-linear impact, e.g. saturation above a certain threshold 19.</li>
		<li>Select a response surface methodology (RSM), e.g. central composite design (CCD) 31 or optimal 32,33, if only a few factors with well-known ranges need to be characterized precisely.</li>
	</ol>
	</li>
	<li>Set up the DoE with appropriate software, ensuring a priori quality criteria such as the fraction of design space are met 20.</li>
</ol>
2. Prepare the Flocculation Experiments
<img alt="Figure 1" src="/files/ftp_upload/53940/53940fig1.jpg" /> 
Figure 1: Plant extract flocculation workflow: process scale (left) and benchtop scale (right). Following protein extraction with aqueous buffers, dispersed particles of cell debris are aggregated by the addition of flocculants. The aggregates are then removed by a cascade of bag and depth filtration and the capacity of these filters along with the filtrate turbidities can be used directly to measure the efficiency of flocculation.
<ol>
	<li>Develop a General Experimental Work Flow (Figure 1).
	<ol>
		<li>Use an extraction device that results in the same particle size distribution expected (or already observed) at the final application scale, e.g. a specialized homogenizer. If possible, design a scale-down model of the extractor as described for the homogenization of tobacco leaves 10.</li>
		<li>Define the extract volumes used during flocculation experiments (here 20 ml). Select a volume that allows a representative number of particles to be present in the reaction vessel, e.g. flocculation experiments in 20 ml aliquots yielded reproducible and scalable results for tobacco extracts containing ~7% [w/v] solids 34 and particle sizes of ~0.5 &#181;m to ~3 mm 16.</li>
		<li>Design all monitoring and post-flocculation operations so that they are representative of the final application scale, e.g. select filters with the same particle retention behavior as those used at the production scale.</li>
	</ol>
	</li>
	<li>Cultivate the Plants from Which the Extracts Will be Derived.
	<ol>
		<li>Use the same plant line, here Nicotiana tabacum cv. Petit Havana SR1, and cultivation conditions that will be used during production as previously described 33.</li>
		<li>If other feed stocks will be processed, prepare these feed stocks so that they are representative of the final application scale, e.g. use authentic buffers, take into account any dilution steps during the process and stick to the anticipated pH and conductivity, here pH 7.5 and conductivity 30 mS cm-1.</li>
	</ol>
	</li>
	<li>Prepare Filtration Utilities, Turbidity-Monitoring Devices and Sampling Vessels.
	<ol>
		<li>Cut the filter materials to the required sizes, here 15 x 15 cm2, if they are not ready-to-use modules. Ensure all monitoring and analysis devices are functional and label all sample tubes.</li>
		<li>Even though these are simple tasks, prepare these items in time to ensure that they will not cause interruptions during the actual flocculation experiments. Avoid delays because they can interfere with the results given that flocculation is a time-dependent process.</li>
	</ol>
	</li>
	<li>Prepare Flocculant Stock Solutions. CAUTION: Wear appropriate personal protection equipment when handling flocculants, e.g. gloves. The materials can be dangerous (hazard labels according to Europe UE 67/548/CEE, 1999/45/CE include N, Xi or Xn). Avoid dust and refer to the material safety data sheets. Work under a fume hood.
	<ol>
		<li>Choose a stock concentration for each flocculant, here 80.0 g L-1 for the two PEI flocculants that were used. Select concentrations as high as possible to avoid sample dilution when adding the flocculant, which would reduce particle concentration and thus affect flocculation efficiency.</li>
		<li>Account for any pre-dilution that reflects the manufacturer&#39;s formulation of the polymer, e.g. if the polymer is already supplied as an aqueous 50% [w/v] solution. Flocculant stock solutions of 4-8% [w/v] were found to be the most suitable so far.</li>
		<li>Bearing in mind the points discussed above, make sure the flocculant concentration does not generate a highly viscous solution that inhibits pipetting, potentially causing errors because the final flocculant concentration is not adjusted correctly.</li>
		<li>Use the same stock concentration for all flocculants if possible because this will facilitate the setup of a pipetting scheme (2.5) thus reducing the likelihood of errors.</li>
		<li>Adjust the pH and conductivity of each flocculant stock solution to match the conditions of the extracts, here pH 4&#8722;10 and conductivity 15&#8722;55 mS cm-1. Prepare individual stocks for a single flocculant if more than one set of pH and/or conductivity conditions is tested for that polymer.</li>
		<li>Prepare flocculant stock solutions freshly, no longer than 48 h before use. Even though flocculation can be induced with polymer stocks stored for more than 4 weeks, the efficiency may decline due to polymer hydrolysis at high or low pH values. See the manufacturer&#39;s documentation for further details.</li>
		<li>Make sure that the parameters selected for the DoE can be adjusted precisely for each sample during the experiment, e.g. ensure there are heating/cooling baths available to adjust incubation temperatures, here 4 &#176;C, 20 &#176;C and 37 &#176;C. If mixing during flocculation is part of the experiment, ensure that the mixing device is representative of the final application scale in terms of critical parameters such as power input.</li>
	</ol>
	</li>
	<li>Convert the DoE Schedule into a Pipetting Scheme.
	<ol>
		<li>Convert the different flocculant concentrations to be tested into volumes of stock solution that will be added to the extract samples: divide the final flocculant concentrations by the stock concentration and multiply by the sample volume used in the flocculation experiments. Identify the largest resulting final volume, e.g. if 20 ml of sample is mixed with a maximum of 2 ml flocculant stock solution this will be 22 ml.</li>
		<li>Calculate volumes of buffer required to maintain the same final volume in all flocculation aliquots based on the largest volume of flocculant stock to be added, e.g. if 0.75 ml of flocculant stock must be added to a sample then 1.25 ml of buffer is required to maintain the final sample volume of 22 ml (2.5.1).</li>
		<li>Sum up the volumes of flocculant stock solution for each polymer and flocculation condition to calculate the absolute volumes of stock solution that are required for the DoE.</li>
	</ol>
	</li>
	<li>Harvest Tobacco Leaves and Prepare the Extract.
	<ol>
		<li>Remove the top six leaves (or as many as indicated by in the process instructions) from tobacco plants of an appropriate age, e.g. 6 weeks old, and transfer to a suitable extraction device such as a homogenizer or screw press.</li>
		<li>Add three volumes of extraction buffer per gram biomass, e.g. 300 ml per 100 g, and blend for 8 min.</li>
		<li>Prepare individual extracts with the appropriate buffers if different pH and/or conductivities are being tested. Here, this involves homogenizing the plant material for 3 x 30 sec in a blender or a juicer 34.</li>
		<li>Alternatively, prepare the extract in a manner that is representative of the process under investigation.</li>
	</ol>
	</li>
	<li>Aliquot the Extract and Add the Buffer.
	<ol>
		<li>Manually and thoroughly stir the extract during the entire procedure to ensure the samples are homogeneous with an even distribution of particles.</li>
		<li>Precisely distribute the extract among the pre-labeled reaction tubes by decanting, here 20 ml in each vessel. Self-standing 50 ml tubes simplify handling and are ideal for 20 ml samples.</li>
		<li>Add the volume of each extraction buffer required to maintain the fixed final volume for each individual reaction tube using a suitable pipette.</li>
	</ol>
	</li>
</ol>
3. Flocculate the Plant Extracts with Different Polymers
<ol>
	<li>Pipette the required volume of flocculant stock solution, here 0.1&#8722;2.0 ml, to the samples sequentially as indicated by the randomized run order of the DoE. Thoroughly mix each sample immediately after the addition of flocculant by intense manual shaking for precisely 20 sec.
	<ol>
		<li>If required, adjust the shaking time for other feed stocks to ensure thorough mixing, but strictly ensure consistent mixing times for all samples. Bear in mind that prolonged mixing may cause the irreversible disruption of flocs and inconsistently applied force during shaking can distort the flocculation results.</li>
	</ol>
	</li>
	<li>Optional: Modify the procedure described above for the simultaneous application of two or more flocculants.
	<ol>
		<li>Option 1: Instead of a single polymer add a mixture of two or more flocculants, here PEI and chitosan. Use the flocculant combinations defined in the DoE. Incorporate the ratio and absolute concentrations of the polymers as individual parameters during the DoE setup (1.1).</li>
		<li>Option 2: Add two or more polymers sequentially to the extract.
		<ol>
			<li>Use the individual polymer concentrations, their type, and the incubation time between each addition to the extract, as additional factors during the DoE setup.</li>
			<li>Also use this approach to test whether the repeated addition of a single polymer can improve flocculation. Use a stepwise addition to simulate the slow addition of a flocculant, e.g. four steps, each adding 0.25 ml 80 g L-1 flocculant stock to a 20 ml volume over 4 min can mimic the addition of flocculant with a flow rate of 0.25 ml min-1.</li>
			<li>In all cases, identify a new maximum final sample volume for this setup by adding the maximum volumes of all flocculants to the sample volume, here still 22 ml, and recalculate the required volumes of flocculant stock solutions and buffers for volume adjustment if necessary.</li>
		</ol>
		</li>
	</ol>
	</li>
	<li>Incubate the samples for the times defined in the DoE, typically 3-30 min, to allow floc formation. Make sure all other incubation conditions, e.g. temperature, are set according to the DoE.</li>
	<li>Observe and document floc formation. Record the progress of floc formation as required, e.g. as mm of floc settling per min by measuring the height of the settled solids. If necessary, prolong flocculation for an extended time period such as overnight.</li>
	<li>Filter the Flocculated Extract.
	<ol>
		<li>Use the filter materials prepared earlier (2.3) to clarify the flocculated extract after the appropriate incubation time by decanting the flocculated samples through the filter material and into a clean vessel or reaction tube.
		<ol>
			<li>Do not re-suspend the settled flocs before filtration and apply the extract with at a rate of ~300 ml min-1 to the filter, corresponding to 3&#8722;4 sec for a 20 ml sample.</li>
			<li>Confirm the performance of the filtration step if a different material is used in the bench-top experiments compared to the final process in terms of particle retention, e.g. by measuring the particle size distribution in both sample types 11.</li>
		</ol>
		</li>
		<li>Analyze the filtrate in terms of turbidity and/or particle size distribution as required using appropriate devices, e.g. a turbidimeter.</li>
		<li>Optional: repeat the analysis after extended incubation times, e.g. 12&#8722;24 hr, to investigate the formation or reformation of unstable flocs.</li>
	</ol>
	</li>
	<li>Analyze the Samples in Terms of the Pre-defined Responses (1.1.3).
	<ol>
		<li>Take samples from the filtrates and analyze them for additional response parameters, e.g. the concentrations of different target proteins or valuable products.</li>
		<li>Optional: Analyze the retentate (mostly solids) for the same parameters to close the mass balance of the process. In particular, quantify the effect of flocculants on liquid recovery by comparing the solids mass remaining after samples are treated or not treated with flocculant.</li>
	</ol>
	</li>
	<li>Confirm the data quality and transfer the results to the DoE software.
	<ol>
		<li>Look for extreme values in the collected response data, e.g. unexpectedly high values.</li>
		<li>Ensure that all response data are correctly aligned with their corresponding experimental conditions.</li>
		<li>Transfer the results into the DoE software and make sure the standard and randomized run orders are not mixed up.</li>
	</ol>
	</li>
</ol>
4. Evaluate the DoE
<ol>
	<li>Use the built-in data analysis tools of the DoE software to develop a predictive model as previously described 20.
	<ol>
		<li>Select a proper data transformation mode if required to facilitate model building, here log10. A ratio larger than 10 for largest vs. smallest response value indicates that a data transformation may be required. Identify the most suitable transformation using the appropriate statistical tools, e.g. a Box-Cox plot 35.</li>
		<li>Chose a base model that (i) fits to the selected DoE (1.2) and (ii) agrees with previous knowledge about the system under investigation based on the analysis of variance (ANOVA) tools of the DoE software, e.g. a second-order polynomial often fits better to the observed effect of incubation time than a first-order polynomial.</li>
		<li>Remove insignificant model factors, e.g. p &#62;0.05, or factor interactions iteratively by deselecting them, thereby reducing the model complexity and increasing its predictive power.</li>
		<li>Confirm the model quality by comparing R2, adjusted R2 and predicted R2 along with the normal probability plot of the studentized residuals, residuals-vs-run, predicted-vs-actual and Box-Cox plots 36. All R2 values should be within a 0.2 range.</li>
		<li>Make sure that the final model agrees with basic assumptions of physics and thermodynamics, e.g. no negative concentrations are predicted.</li>
	</ol>
	</li>
	<li>Use the model to predict conditions that are most favorable for the system under investigation, here a low turbidity.
	<ol>
		<li>Select the most important responses and their preferred states, e.g. minimal turbidity. Combine these selections by maximizing a desirability function or similar tools, which are built-in features of several DoE software packages 36.</li>
		<li>Depending on the intended application of the model, select confirmation runs to verify the optimal conditions and/or the predictive power of the model in general, e.g. if the conditions predicted to be most favorable were not part of the initial DoE select them as follow-up experiments.</li>
	</ol>
	</li>
</ol>
5. Improve the Model and Verify the Predictive Power
<ol>
	<li>Narrow down the initial design space to the most desirable operation conditions, e.g. low turbidity in the 0&#8722;1,000 nephelometric turbidity units (NTU) range, based on the model predictions (4.2).</li>
	<li>Set up a new DoE within these ranges, including only those factors that have been identified as significant or relevant (4.1.2)). 
	NOTE: A factor can be significant in terms of model analysis but irrelevant for a process, i.e. its effect on a response is &#60;1% compared to that of other factors.</li>
	<li>Repeat steps 1-5.2 until the quality of the model predictions matches the requirements, e.g. the standard deviation of the model as indicated by the software is sufficient for the intended application. Modify the experimental strategy if required for these iterations, e.g. use only one flocculant in the refinement.</li>
	<li>Transfer and confirm the results from the scale-down model to the pilot scale or final production scale.</li>
</ol>

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S., Sofer, G. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Process Validation in Manufacturing of Biopharmaceuticals, 3rd edn, Vol. 1. , (2012).</li><li>Kang, Y., et al. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Development+of+a+Novel+and+Efficient+Cell+Culture+Flocculation+Process+Using+a+Stimulus+Responsive+Polymer+to+Streamline+Antibody+Purification+Processes.">Development of a Novel and Efficient Cell Culture Flocculation Process Using a Stimulus Responsive Polymer to Streamline Antibody Purification Processes.</a> Biotechnol. Bioeng. 110, 2928-2937 (2013).</li><li>Menkhaus, T. J., Eriksson, S. U., Whitson, P. B., Glatz, C. E. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Host+selection+as+a+downstream+strategy:+Polyelectrolyte+precipitation+of+beta-glucuronidase+from+plant+extracts.">Host selection as a downstream strategy: Polyelectrolyte precipitation of beta-glucuronidase from plant extracts.</a> Biotechnol. Bioeng. 77, 148-154 (2002).</li><li>Holler, C., Vaughan, D., Zhang, C. M. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Polyethyleneimine+precipitation+versus+anion+exchange+chromatography+in+fractionating+recombinant+beta-glucuronidase+from+transgenic+tobacco+extract.">Polyethyleneimine precipitation versus anion exchange chromatography in fractionating recombinant beta-glucuronidase from transgenic tobacco extract.</a> J. Chromatogr. A. 1142, 98-105 (2007).</li><li>Buyel, J. F., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Synthetic+polymers+are+more+effective+than+natural+flocculants+for+the+clarification+of+tobacco+leaf+extracts.">Synthetic polymers are more effective than natural flocculants for the clarification of tobacco leaf extracts.</a> J. Biotechnol. 195, 37-42 (2014).</li><li>Pearson, C. R., Heng, M., Gebert, M., Glatz, C. E. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Zeta+potential+as+a+measure+of+polyelectrolyte+flocculation+and+the+effect+of+polymer+dosing+conditions+on+cell+removal+from+fermentation+broth.">Zeta potential as a measure of polyelectrolyte flocculation and the effect of polymer dosing conditions on cell removal from fermentation broth.</a> Biotechnol. Bioeng. 87, 54-60 (2004).</li><li>Buyel, J. F., Gruchow, H. M., Boes, A., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Rational+design+of+a+host+cell+protein+heat+precipitation+step+simplifies+the+subsequent+purification+of+recombinant+proteins+from+tobacco.">Rational design of a host cell protein heat precipitation step simplifies the subsequent purification of recombinant proteins from tobacco.</a> Biochem. Eng. J. 88, 162-170 (2014).</li><li>Wang, S., Liu, C., Li, Q. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Impact+of+polymer+flocculants+on+coagulation-microfiltration+of+surface+water.">Impact of polymer flocculants on coagulation-microfiltration of surface water.</a> Water Res. 47, 4538-4546 (2013).</li><li>Menkhaus, T. J., Anderson, J., Lane, S., Waddell, E. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Polyelectrolyte+flocculation+of+grain+stillage+for+improved+clarification+and+water+recovery+within+bioethanol+production+facilities.">Polyelectrolyte flocculation of grain stillage for improved clarification and water recovery within bioethanol production facilities.</a> Bioresour. Technol. 101, 2280-2286 (2010).</li><li>Mune, M. A. M., Minka, S. R., Mbome, I. L. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Optimising+functional+properties+during+preparation+of+cowpea+protein+concentrate.">Optimising functional properties during preparation of cowpea protein concentrate.</a> Food Chem. 154, 32-37 (2014).</li><li>Buyel, J. F., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Predictive+models+for+transient+protein+expression+in+tobacco+(Nicotiana+tabacum+L.)+can+optimize+process+time,+yield,+and+downstream+costs.">Predictive models for transient protein expression in tobacco (Nicotiana tabacum L.) can optimize process time, yield, and downstream costs.</a> Biotechnol. Bioeng. 109, 2575-2588 (2012).</li><li>Buyel, J. F., Kaever, T., Buyel, J. J., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Predictive+models+for+the+accumulation+of+a+fluorescent+marker+protein+in+tobacco+leaves+according+to+the+promoter/5'UTR+combination.">Predictive models for the accumulation of a fluorescent marker protein in tobacco leaves according to the promoter/5'UTR combination.</a> Biotechnol. Bioeng. 110, 471-482 (2013).</li><li>Buyel, J. F., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=A+juice+extractor+can+simplify+the+downstream+processing+of+plant-derived+biopharmaceutical+proteins+compared+to+blade-based+homogenizers.">A juice extractor can simplify the downstream processing of plant-derived biopharmaceutical proteins compared to blade-based homogenizers.</a> Process Biochem. 50, 859-866 (2014).</li><li>Anderson, M. J., Whitcomb, P. J. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> DOE Simplified: Practical Tools for Effective Experimentation. Vol. 1. 1, (2000).</li><li>Anderson, M. J., Whitcomb, P. J. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Response Surface Methods Simplified. , (2005).</li><li>Buyel, J. F., Fischer, R. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=Generic+chromatography-based+purification+strategies+accelerate+the+development+of+downstream+processes+for+biopharmaceutical+proteins+produced+in+plants.">Generic chromatography-based purification strategies accelerate the development of downstream processes for biopharmaceutical proteins produced in plants.</a> Biotechnol. J. 9, 566-577 (2014).</li><li>Myers, R. H., Montgomery, D. C., Anderson-Cook, C. M. <a target="_blank" href="http://www.ncbi.nlm.nih.gov/entrez/query.fcgi?db=PubMed&cmd=Search&doptcmdl=Citation&defaultField=Title+Word&term=.">.</a> Response Surface Methodology: Process and Product Optimization Using Designed Experiments. , (2009).</li></ol>

The author has no conflicts of interest to disclose.

The most important aspect to consider when setting up a DoE to characterize particle flocculation is that the design must in principle be able to detect and describe the anticipated or possible effects 36,38, e.g. the influence of pH, polymer type and polymer concentration 16. Therefore, it is important to evaluate the fraction of design space (FDS) before starting the actual experiments. The FDS is the fraction of the multidimensional experimental space (covered by the design factors, ...

Plants are widely used to produce food commodities such as fruit juices, but they can also be developed as platforms for the manufacture of higher-value biopharmaceutical products 1-3. In both cases, downstream processing (DSP) often begins with the extraction of liquids from tissues such as leaves or fruits, followed by the clarification of particle-laden extracts 4,5. For the manufacture of biopharmaceuticals, the costs of DSP can account for up to 80% of the overall production costs 6,7 and this in part reflects the high particle burden present in extracts prepared by disruptive methods such as blade-based homogenization 8,9. Although the rational selection of filter layers to match the particle size distribution in the extract can increase filter capacity and reduce costs 10,11, the improvement can never exceed the ceiling of absolute capacity defined by the number of particles that must be retained per unit of filter area to achieve clarification.
The ceiling can be lifted if fewer particles reach the surface of the finest filters in the filtration train, and this can be achieved if dispersed particles are mixed with polymers known as flocculants that promote aggregation to form large flocs 12. Such flocs can be retained further upstream by coarser and less expensive bag filters, reducing the particle burden reaching the finer and more expensive depth filters. The polymers must have safety profiles suitable for their applications, e.g. for biopharmaceuticals they must be compliant with good manufacturing practice (GMP), and typically they must have a molar mass &#62;100 kDa and can either be neutral or charged 13. Whereas neutral flocculants generally act by cross-linking dispersed particles causing their aggregation and the formation of flocs with diameters &#62;1 mm 11, charged polymers neutralize the charge of dispersed particles, reducing their solubility and thus causing precipitation 14.
Flocculation can be improved by adjusting parameters such as buffer pH or conductivity, and the polymer type or concentration, to match the properties of the extract 15,16. For tobacco extracts pretreated with 0.5-5.0 g L-1 polyethylenimine (PEI), a greater than 2-fold increase in depth filter capacity was reported in a 100-L pilot-scale process. The cost of this polymer is less than &#8364;10 kg-1 so its introduction into the process resulted in cost savings of about &#8364;6,000 for filters and consumables per batch 16 or even more when combined with cellulose-based filter aids 17. Even so, predictive models are required to evaluate the a priori economic benefits of flocculants because their inclusion can require hold steps of 15-30 min 16,18, resulting in further investment costs for storage tanks. However, there are currently no mechanistic models available that can predict the outcome of such experiments due to the complex nature of flocculation. Therefore, a more appropriate design-of-experiments (DoE) approach 19 was developed as described in this article. A protocol for the general DoE procedure has recently been published 20.
Small-scale devices are now available for the high-throughput screening of flocculation conditions 21. However, these devices may not realistically simulate conditions during the flocculation of plant extracts because the dimensions of the reaction vessel (~7 mm for wells on a 96-well plate) and the particles or flocs can be less than an order of magnitude apart. This can affect mixing patterns and thus the predictive power of the model. Furthermore, it can be difficult to scale down processes involving precipitation due to non-linear changes in the mixing behavior and precipitate stability 22. Therefore, this article outlines a bench-top-scale screening system with a throughput of 50-75 samples per day, yielding results that are scalable from the initial 20 ml reaction volume to a 100 L pilot-scale process 16. When combined with a DoE approach, this allows the predictive models to be used for process optimization and documentation as part of a quality-by-design concept.
The method described below may also be adapted to biopharmaceuticals produced in cell culture-based processes, where flocculants are also being considered as a cost-saving tool 23. It can also be used to model the precipitation of target proteins from a crude extract as part of a purification strategy, as demonstrated for &#946;-glucuronidase produced in canola, maize and soybean 24,25. A detailed description of flocculant properties can be found elsewhere 16,26 and it is important to ensure that the polymer concentrations are either non-toxic or below harmful levels in the final product 11.

<table><tbody><tr><td>2100P Portable Turbidimeter</td><td>Hach</td><td>4650000</td><td>Turbidimeter</td></tr><tr><td>2G12 antibody</td><td>Polymun</td><td>AB002</td><td>Reference antibody</td></tr><tr><td>Biacore T200</td><td>GE Healthcare</td><td>28-9750-01</td><td>SPR device</td></tr><tr><td>BP-410</td><td>Furh</td><td>2632410001</td><td>Bag filter</td></tr><tr><td>Catiofast VSH</td><td>BASF</td><td>79002360</td><td>Flocculating agent</td></tr><tr><td>Centrifuge 5415D</td><td>Eppendorf</td><td>5424 000.410</td><td>Centrifuge</td></tr><tr><td>Centrifuge tube 15 ml</td><td>Labomedic</td><td>2017106</td><td>Reaction tube</td></tr><tr><td>Centrifuge tube 50 ml self-standing</td><td>Labomedic</td><td>1110504</td><td>Reaction tube</td></tr><tr><td>Chitosan</td><td>Carl Roth GmbH</td><td>5375.1</td><td>Flocculating agent</td></tr><tr><td>Design-Expert(R) 8</td><td>Stat-Ease, Inc.</td><td>n.a.</td><td>DoE software</td></tr><tr><td>Disodium phosphate</td><td>Carl Roth GmbH</td><td>&amp;nbsp;4984.3&amp;nbsp;</td><td>Media component</td></tr><tr><td>Ferty 2 Mega</td><td>Kammlott</td><td>5.220072</td><td>Fertilizer</td></tr><tr><td>Forma -86C ULT freezer</td><td>ThermoFisher</td><td>88400</td><td>Freezer</td></tr><tr><td>Greenhouse</td><td>n.a.</td><td>n.a.</td><td>For plant cultivation</td></tr><tr><td>Grodan Rockwool Cubes 10 x 10 cm</td><td>Grodan</td><td>102446</td><td>Rockwool block</td></tr><tr><td>HEPES</td><td>Carl Roth GmbH</td><td>9105.3</td><td>Media component</td></tr><tr><td>K700P 60D</td><td>Pall</td><td>5302305</td><td>Depth filter layer</td></tr><tr><td>KS50P 60D</td><td>Pall</td><td>B12486</td><td>Depth filter layer</td></tr><tr><td>Miracloth</td><td>Labomedic</td><td>475855-1R</td><td>Filter cloth</td></tr><tr><td>MultiLine Multi 3410 IDS</td><td>WTW</td><td>WTW_2020</td><td>pH meter / conductivity meter</td></tr><tr><td>Osram cool white 36 W</td><td>Osram</td><td>4930440</td><td>Light source</td></tr><tr><td>Phytotron</td><td>Ilka Zell</td><td>n.a.</td><td>For plant cultivation</td></tr><tr><td>Polymin P</td><td>BASF</td><td>79002360</td><td>Flocculating agent</td></tr><tr><td>POLYTRON PT 6100 D</td><td>Kinematica</td><td>11010110</td><td>Homogenization device with custom blade tool</td></tr><tr><td>Protein A</td><td>Life technologies</td><td>10-1006</td><td>Antibody binding protein</td></tr><tr><td>Sodium chloride</td><td>Carl Roth GmbH</td><td>P029.2</td><td>Media component</td></tr><tr><td>Synergy HT</td><td>BioTek</td><td>SIAFRT</td><td>Fluorescence plate reader</td></tr><tr><td>TRIS</td><td>Carl Roth GmbH</td><td>4855.3</td><td>Media component</td></tr><tr><td>Tween-20</td><td>Carl Roth GmbH</td><td>9127.3</td><td>Media component</td></tr><tr><td>VelaPad 60</td><td>Pall</td><td>VP60G03KNH4</td><td>Filter housing</td></tr><tr><td>Zetasizer Nano ZS</td><td>Malvern</td><td>ZEN3600</td><td>DLS particle size distribution measurement</td></tr></tbody></table>

procedure to evaluate the efficiency of flocculants for the removal of dispersed particles from plant extracts

Plants are important to humans not only because they provide commodities such as food, feed and raw materials, but increasingly because they can be used as manufacturing platforms for added-value products such as biopharmaceuticals. In both cases, liquid plant extracts may need to be clarified to remove particulates. Optimal clarification reduces the costs of filtration and centrifugation by increasing capacity and longevity. This can be achieved by introducing charged polymers known as flocculants, which cross-link dispersed particles to facilitate solid-liquid separation. There are no mechanistic flocculation models for complex mixtures such as plant extracts so empirical models are used instead. Here a design-of-experiments procedure is described that allows the rapid screening of different flocculants, optimizing the clarification of plant extracts and significantly reducing turbidity. The resulting predictive models allow the identification of robust process conditions and sets of polymers with complementary properties, e.g. effective flocculation in extracts with specific conductivities. The results presented for tobacco leaf extracts can easily be adapted to other plant species or tissues and will thus facilitate the development of more cost-effective downstream processes for commodities and plant-derived pharmaceuticals.

Flocculation of tobacco extract with different polymers
The method described above was successfully used to develop a process for the flocculation of tobacco extracts during the manufacture of a monoclonal antibody (the HIV-neutralizing antibody 2G12) and a fluorescent protein (DsRed) (Figure 1) 16, and has since been transferred to other proteins including lectins, malaria vaccine candidates and fusi...

Watch this Scientific Journal Video about Procedure to Evaluate the Efficiency of Flocculants for the Removal of Dispersed Particles from Plant Extracts at JoVE.com

Procedure to Evaluate the Efficiency of Flocculants for the Removal of Dispersed Particles from Plant Extracts

The design-of-experiments procedure presented here allows the evaluation of different flocculants in terms of their ability to aggregate dispersed particles in plant extracts, thus reducing turbidity and the costs of downstream processing.

Plants are important to humans not only because they provide commodities such as food, feed and raw materials, but increasingly because they can be used ...

procedure-to-evaluate-efficiency-flocculants-for-removal-dispersed

Universidad de Cartagena UDEC

Research

JoVE Journal

Biology

8.8K Views.  Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e. V.. The design-of-experiments procedure presented here allows the evaluation of different flocculants in terms of their ability to aggregate dispersed particles in plant extracts, thus reducing turbidity and the costs of downstream processing.

Video: Procedure to Evaluate the Efficiency of Flocculants for the Removal of Dispersed Particles from Plant Extracts

Extraction and Characterization of Surfactants from Atmospheric Aerosols

Surface-active compounds, or surfactants, present in atmospheric aerosols are expected to play important roles in the formation of liquid water clouds in the Earth&#39;s atmosphere, a central process in meteorology, hydrology, and for the climate system. But because specific extraction and characterization of these compounds have been lacking for decades, very little is known on their identity, properties, mode of action and origins, thus preventing the full understanding of cloud formation and its potential links with the Earth&#39;s ecosystems.
In this paper we present recently developed methods for 1) the targeted extraction of all the surfactants from atmospheric aerosol samples and for the determination of 2) their absolute concentrations in the aerosol phase and 3) their static surface tension curves in water, including their Critical Micelle Concentration (CMC). These methods have been validated with 9 references surfactants, including anionic, cationic and non-ionic ones. Examples of results are presented for surfactants found in fine aerosol particles (diameter &#60;1 &#956;m) collected at a coastal site in Croatia and suggestions for future improvements and other characterizations than those presented are discussed.

Methods are presented for the targeted extraction of surfactants present in atmospheric aerosols and the determination of their absolute concentrations and surface tension curves in water, including their Critical Micelle Concentration (CMC).

Surface-active compounds, or surfactants, present in atmospheric aerosols are expected to play important roles in the formation of liquid water clouds in ...

Environment

Determination of the Settling Rate of Clay/Cyanobacterial Floccules

The mechanisms underpinning the deposition of fine-grained, organic-rich sediments are still largely debated. Specifically, the impact of the interaction of clay particles with reactive, planktonic cyanobacterial cells to the sedimentary record is under studied. This interaction is a potentially major contributor to shale depositional models. Within a lab setting, the flocculation and sedimentation rates of these materials can be examined and measured in a controlled environment. Here, we detail a protocol for measuring the sedimentation rate of cyanobacterial/clay mixtures. This methodology is demonstrated through the description of two sample experiments: the first uses kaolin (a dehydrated form of kaolinite) and Synechococcus sp. PCC 7002 (a marine coccoid cyanobacteria), and the second uses kaolin and Synechocystis sp. PCC 6803 (a freshwater coccoid cyanobacteria). Cyanobacterial cultures are mixed with varying amounts of clay within a specially designed tank apparatus optimized to allow continuous, real-time video and photographic recording. The sampling procedures are detailed as well as a post-collection protocol for precise measurement of chlorophyll a from which the concentration of cyanobacterial cells remaining in suspension can be determined. Through experimental replication, a profile is constructed that displays sedimentation rate.

The interaction and sedimentation of the clay and bacterial cells within the marine realm, observed in natural environments, can be best investigated in a controlled lab environment. Here, we describe a detailed protocol, which outlines a novel method for measuring the sedimentation rate of clay and cyanobacterial floccules.

The mechanisms underpinning the deposition of fine-grained, organic-rich sediments are still largely debated. Specifically, the impact of the interaction ...

Combined Size and Density Fractionation of Soils for Investigations of Organo-Mineral Interactions

Combined size and density fractionation (CSDF) is a method used to physically separate soil into fractions differing in particle size and mineralogy. CSDF relies on sequential density separation and sedimentation steps to isolate (1) the free light fraction (uncomplexed organic matter), (2) the occluded light fraction (uncomplexed organic matter trapped in soil aggregates) and (3) a variable number of heavy fractions (soil minerals and their associated organic matter) differing in composition. Provided that the parameters of the CSDF (dispersion energy, density cut-offs, sedimentation time) are properly selected, the method yields heavy fractions of relatively homogeneous mineral composition. Each of these fractions is expected to have a different complexing ability towards organic matter, rendering this a useful method to isolate and study the nature of organo-mineral interactions. Combining density and particle size separation brings an improved resolution compared to simple size or density fractionation methods, allowing the separation of heavy components according to both mineralogy and size (related to surface area) criteria. As is the case for all physical fractionation methods, it may be considered as less disruptive or aggressive than chemically-based extraction methods. However, CSDF is a time-consuming method and furthermore, the quantity of material obtained in some fractions can be limiting for subsequent analysis. Following CSDF, the fractions may be analyzed for mineralogical composition, soil organic carbon concentration and organic matter chemistry. The method provides quantitative information about organic carbon distribution within a soil sample and brings light to the sorptive capacity of the different, naturally-occurring mineral phases, thus providing mechanistic information about the preferential nature of organo-mineral interactions in soils (i.e., which minerals, what type of organic matter).

Combined size and density fractionation (CSDF) is a method to physically separate soil into fractions differing in texture (particle size) and mineralogy (density). The purpose is to isolate fractions with different reactivities towards soil organic matter (SOM), in order to better understand organo-mineral interactions and SOM dynamics.

Combined size and density fractionation (CSDF) is a method used to physically separate soil into fractions differing in particle size and mineralogy. CSDF ...

Capture of Environmental DNA (eDNA) from Water Samples by Flocculation

The analysis of environmental DNA (eDNA) has become a widely used approach to problem solving in species management. The detection of cryptic species including invasive and (or) species at risk is the goal, typically accomplished by testing water and sediment for the presence of characteristic DNA signatures. Reliable and efficient procedures for the capture of eDNA are required, especially those that can be performed easily in the field by personnel with limited training and citizen scientists. The capture of eDNA using membrane filtration is widely used currently. This approach has inherent issues that include the choice of filter material and porosity, filter fouling, and time required on site for the process to be performed. Flocculation offers an alternative that can be easily implemented and applied to sampling regimes that strive to cover broad territories in limited time.

Capture of Environmental DNA eDNA from Water Samples by Flocculation

Environmental DNA (eDNA) is typically captured from water samples using alcohol precipitation, filtration, or flocculation. Presented here is an alternative protocol that uses lanthanum chloride to enable collection of dissolved and particulate-bound nucleic acids from water samples containing eukaryotic cells, prokaryotic cells, and virus.

The analysis of environmental DNA (eDNA) has become a widely used approach to problem solving in species management. The detection of cryptic species ...

Activated Cross-linked Agarose for the Rapid Development of Affinity Chromatography Resins - Antibody Capture as a Case Study

The purification of monoclonal antibodies (mAbs) is commonly achieved by Protein A affinity chromatography, which can account for up to 25% of the overall process costs. Alternative, cost-effective capture steps are therefore valuable for industrial-scale manufacturing, where large quantities of a single mAb are produced. Here we present a method for the immobilization of a DsRed-based epitope ligand to a cross-linked agarose resin allowing the selective capture of the HIV-neutralizing antibody 2F5 from crude plant extracts without using Protein A. The linear epitope ELDKWA was first genetically fused to the fluorescent protein DsRed and the fusion protein was expressed in transgenic tobacco (Nicotiana tabacum) plants before purification by immobilized metal-ion affinity chromatography. Furthermore, a method based on activated cross-linked agarose was optimized for high ligand density, efficient coupling and low costs. The pH and buffer composition and the soluble ligand concentration were the most important parameters during the coupling procedure, which was improved using a design-of-experiments approach. The resulting affinity resin was tested for its ability to selectively bind the target mAb in a crude plant extract and the elution buffer was optimized for high mAb recovery, product activity and affinity resin stability. The method can easily be adapted to other antibodies with linear epitopes. The new resins allow gentler elution conditions than Protein A and could also reduce the costs of an initial capture step for mAb production.

In this procedure, a DsRed-based epitope ligand is immobilized to produce a highly selective affinity resin for the capture of monoclonal antibodies from crude plant extracts or cell culture supernatants, as an alternative to Protein A.

The purification of monoclonal antibodies (mAbs) is commonly achieved by Protein A affinity chromatography, which can account for up to 25% of the overall ...

Biochemistry

Evaluation of Wild Peanut Species for Resistance to Aflatoxin Accumulation

Non-destructive SPE-UPLC-based Quantification of Aflatoxins and Stilbenoid Phytoalexins in Single Peanut (Arachis spp.) Seeds

Aflatoxins are highly carcinogenic secondary metabolites of some fungal species, particularly Aspergillus flavus. Aflatoxins often contaminate economically important agricultural commodities, including peanuts, posing a high risk to human and animal health. Due to the narrow genetic base, peanut cultivars demonstrate limited resistance to fungal pathogens. Therefore, numerous wild peanut species with tolerance to Aspergillus have received substantial consideration by scientists as sources of disease resistance.
Exploring plant germplasm for resistance to aflatoxins is difficult since aflatoxin accumulation does not follow a normal distribution, which dictates the need for the analyses of thousands of single peanut seeds. Sufficiently hydrated peanut (Arachis spp.) seeds, when infected by Aspergillus species, are capable of producing biologically active stilbenes&#160;(stilbenoids) that are considered defensive phytoalexins. Peanut stilbenes inhibit fungal development and aflatoxin production. Therefore, it is crucial to analyze the same seeds for peanut stilbenoids to explain the nature of seed resistance/susceptibility to the Aspergillus invasion. None of the published methods offer single-seed analyses for aflatoxins and/or stilbene phytoalexins.
We attempted to fulfill the demand for such a method that is environment-friendly, uses inexpensive consumables, and is sensitive and selective. In addition, the method is non-destructive since it uses only half of the seed and leaves the other half containing the embryonic axis intact. Such a technique allows germination and growth of the peanut plant to full maturity from the same seed used for the aflatoxin and stilbenoid analysis. The integrated part of this method, the manual challenging of the seeds with Aspergillus, is a limiting step that requires more time and labor compared to other steps in the method. The method has been used for the exploration of wild Arachis germplasm to identify species resistant to Aspergillus and to determine and characterize novel sources of genetic resistance to this fungal pathogen.

Author Spotlight: Quantification of Aflatoxins and Phytoalexins in Peanut Seeds to Identify Genetic Resistance Against Aspergillus

We demonstrate a medium-throughput method for quantification of aflatoxins and stilbenoid phytoalexins in single peanut seeds using ultra performance liquid chromatography. This method was specifically developed for the analyses of wild Arachis species challenged by the aflatoxigenic Aspergillus species.

Aflatoxins are highly carcinogenic secondary metabolites of some fungal species, particularly Aspergillus flavus. Aflatoxins often contaminate ...

Tangential Flow Ultrafiltration: A  &ldquo;Green&rdquo; Method for the Size Selection and Concentration of Colloidal Silver Nanoparticles

Nowadays, AgNPs are extensively used in the manufacture of consumer products,1 water disinfectants,2 therapeutics,1, 3 and biomedical devices4 due to their powerful antimicrobial properties.3-6 These nanoparticle applications are strongly influenced by the AgNP size and aggregation state. Many challenges exist in the controlled fabrication7 and size-based isolation4,8 of unfunctionalized, homogenous AgNPs that are free from chemically aggressive capping/stabilizing agents or organic solvents.7-13 Limitations emerge from the toxicity of reagents, high costs or reduced efficiency of the AgNP synthesis or isolation methods (e.g., centrifugation, size-dependent solubility, size-exclusion chromatography, etc.).10,14-18 To overcome this, we recently showed that TFU permits greater control over the size, concentration and aggregation state of Creighton AgNPs (300 ml of 15.3 &mu;g ml-1 down to 10 ml of 198.7 &mu;g ml-1) than conventional methods of isolation such as ultracentrifugation.19
TFU is a recirculation method commonly used for the weight-based isolation of proteins, viruses and cells.20,21 Briefly, the liquid sample is passed through a series of hollow fiber membranes with pore size ranging from 1,000 kD to 10 kD. Smaller suspended or dissolved constituents in the sample will pass through the porous barrier together with the solvent (filtrate), while the larger constituents are retained (retentate). TFU may be considered a "green" method as it neither damages the sample nor requires additional solvent to eliminate toxic excess reagents and byproducts. Furthermore, TFU may be applied to a large variety of nanoparticles as both hydrophobic and hydrophilic filters are available.
The two main objectives of this study were: 1) to illustrate the experimental aspects of the TFU approach through an invited video experience and 2) to demonstrate the feasibility of the TFU method for larger volumes of colloidal nanoparticles and smaller volumes of retentate. First, unfuctionalized AgNPs (4 L, 15.2 &mu;g ml-1) were synthesized using the well-established Creighton method22,23 by the reduction of AgNO3 with NaBH4. AgNP polydispersity was then minimized via a 3-step TFU using a 50-nm filter (460 cm2) to remove AgNPs and AgNP-aggregates larger than 50 nm, followed by two 100-kD (200 cm2 and 20 cm2) filters to concentrate the AgNPs. Representative samples were characterized using transmission electron microscopy, UV-Vis absorption spectrophotometry, Raman spectroscopy, and inductively coupled plasma optical emission spectroscopy. The final retentate consisted of highly concentrated (4 ml, 8,539.9 &mu;g ml-1) yet lowly aggregated and homogeneous AgNPs of 1-20 nm in diameter. This corresponds to a silver concentration yield of about 62%.

Tangential flow ultrafiltration (TFU) is a recirculation method used for the weight-based separation of biosamples. TFU was adapted to size-select (1-20 nm diameter) and highly concentrate a large volume of polydisperse silver nanoparticles (4 L of 15.2 &mu;g ml-1 down to 4 ml of 8,539.9 &mu;g ml-1) with minimal aggregation.

Nowadays, AgNPs are extensively used in the manufacture of consumer products,1 water disinfectants,2 therapeutics,1, 3 and biomedical devices4 due to ...

Sustainable MCFA Production via Chain Elongation and Liquid-Liquid Extraction

Continuous Liquid-Liquid Extraction of Medium-Chain Fatty Acids from Fermentation Broth Using Hollow-Fiber Membranes

Medium-chain fatty acids (MCFAs; carbon-lengths: C6-C12) are high-value platform chemicals that serve a variety of industrial applications, including green antimicrobials, food ingredients, animal feed additives, cosmetics, fragrances, pharmaceuticals, and structured lipids. Currently, most MCFAs are produced from palm and coconut oil originating from Southeast Asia and South America. The conventional approach to harvesting palm and coconut fruits causes considerable ecological damage in these regions. Therefore, researchers are developing biological approaches (e.g., precision and open-culture fermentations) to generate MCFAs more sustainably using low-value substrates (e.g., methanol, ethanol, lactate) or organic wastes as feedstock. Microbial chain-elongation (CE) is a rapidly maturing open-culture fermentation platform that converts short-chain fatty acids (SCFAs; carbon lengths: C1-C5) into a subset of these MCFAs at industrially relevant rates. However, continuous in situ extraction of MCFA products is necessary not only to avoid product inhibition but also to facilitate the recovery of MCFAs in a pure and usable form.&#160;Liquid-liquid extraction (LLE) using hollow-fiber membranes and targeted extractant mixtures has proven a robust approach to selectively extract MCFA products from fermentation broths containing SCFAs. Here, the application of LLE for continuous MCFA removal is demonstrated using CE as the reference fermentation system and 3% (w/v) trioctylphosphine oxide in mineral oil as the extractant system. Fatty acids ranging from valeric acid (C5) to caprylic acid (C8) are selectively removed from SCFA-containing broths and concentrated to high titers in a semi-batch alkaline stripping solution for downstream processing.

Author Spotlight: Optimizing Hollow-Fiber Membranes for Continuous Liquid-Liquid Extraction of Medium-Chain Fatty Acids

A liquid-liquid extraction (LLE) system involving hollow-fiber membranes was developed to continuously and selectively extract medium-chain fatty acids (MCFAs) from the fermentation broth. The LLE system achieves high MCFA specificities from broths containing short-chain fatty acids and alcohols. Also, MCFAs are concentrated in a stripping solution to facilitate product recovery.

Medium-chain fatty acids (MCFAs; carbon-lengths: C6-C12) are high-value platform chemicals that serve a variety of industrial applications, including ...

Bioengineering

Comparison of Tobacco Host Cell Protein Removal Methods by Blanching Intact Plants or by Heat Treatment of Extracts

Plants not only provide food, feed and raw materials for humans, but have also been developed as an economical production system for biopharmaceutical proteins, such as antibodies, vaccine candidates and enzymes. These must be purified from the plant biomass but chromatography steps are hindered by the high concentrations of host cell proteins (HCPs) in plant extracts. However, most HCPs irreversibly aggregate at temperatures above 60 &#176;C facilitating subsequent purification of the target protein. Here, three methods are presented to achieve the heat precipitation of tobacco HCPs in either intact leaves or extracts. The blanching of intact leaves can easily be incorporated into existing processes but may have a negative impact on subsequent filtration steps. The opposite is true for heat precipitation of leaf extracts in a stirred vessel, which can improve the performance of downstream operations albeit with major changes in process equipment design, such as homogenizer geometry. Finally, a heat exchanger setup is well characterized in terms of heat transfer conditions and easy to scale, but cleaning can be difficult and there may be a negative impact on filter capacity. The design-of-experiments approach can be used to identify the most relevant process parameters affecting HCP removal and product recovery. This facilitates the application of each method in other expression platforms and the identification of the most suitable method for a given purification strategy.

Three heat precipitation methods are presented that effectively remove more than 90% of host cell proteins (HCPs) from tobacco extracts prior to any other purification step. The plant HCPs irreversibly aggregate at temperatures above 60 &#176;C.

Plants not only provide food, feed and raw materials for humans, but have also been developed as an economical production system for biopharmaceutical ...

Efficiency of Liquid-liquid Extraction

Source: <a href="https://jove.unicartagenaproxy.elogim.com/author/Kerry+M._Dooley">Kerry M. Dooley</a> and Michael G. Benton, Department of Chemical Engineering, Louisiana State University, Baton Rouge, LA
Liquid-liquid extraction (LLE) is a separation technique used instead of distillation when either: (a) the relative volatilities of the compounds to be separated are very similar; (b) one or more of the mixture components are temperature sensitive even near ambient conditions; (c) the distillation would require a very low pressure or a very high distillate/feed ratio.1The driving force for mass transfer is the difference in solubility of one material (the solute) in two other immiscible or partially miscible streams (the feed and the solvent). The feed and solvent streams are mixed and then separated, allowing the solute to transfer from the feed to the solvent. Normally, this process is repeated in successive stages using counter-current flow. The solute-rich solvent is called the extract as it leaves, and the solute-depleted feed is the raffinate. When there is a reasonable density difference between the feed and solvent streams, extraction can be accomplished using a vertical column, although in other cases a series of mixing and settling tanks may be used.
In this experiment, the operational goal is to extract isopropanol (IPA, ~10 - 15 wt. %, the solute) from a mixture of C8-to-C10 hydrocarbons using pure water as solvent. A York-Scheibel type (vertical mixers and coalescers, one each per physical stage) extraction column is available. Like most extractors, the overall efficiency (number theoretical stages/physical stages) of this column is quite low, especially in comparison to many distillation columns. The low efficiencies arise from both slow mass transfer (two liquid resistances instead of one as in distillation) and often also from maldistribution of the phases. The effect of agitator speed on both the solute recovery in the extract and the overall column efficiency will be evaluated.

Liquid-liquid Extraction and York-Scheibel Column Operation

Source: Kerry M. Dooley and Michael G. Benton, Department of Chemical Engineering, Louisiana State University, Baton Rouge, LA
Liquid-liquid extraction ...