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1 erogeneous at different scales (molecular to bioreactor).
2 was observed as an important reaction in the bioreactor.
3 etc.) and results in their enrichment in the bioreactor.
4  (MF) membrane are operated in parallel in a bioreactor.
5 actone) 3D scaffolds within a flow perfusion bioreactor.
6 iscible extractant and aqueous phases of the bioreactor.
7 d by the FO membrane and enriched within the bioreactor.
8 t of the 10-m-long ( approximately 1.5 m(2)) bioreactor.
9  for ethanol production by yeast in the same bioreactor.
10 hese cell-seeded constructs in a whole-organ bioreactor.
11 hypoxia, and glucose deprivation in a custom bioreactor.
12  a microbial fuel cell (MFC) inside an algal bioreactor.
13 t to operations downstream of the production bioreactor.
14 posed to coronary artery flow in a perfusion bioreactor.
15 tly obtained by cultivation in a bench-scale bioreactor.
16 s using a magnetic resonance (MR) compatible bioreactor.
17  in response to cyclic strains imparted in a bioreactor.
18 fter treatment in a laboratory-scale aerobic bioreactor.
19 a novel hemodynamically-equivalent pulsatile bioreactor.
20 ibution of biochemical substances inside the bioreactor.
21 mical changes caused by MICP in a laboratory bioreactor.
22  mccartyi-containing consortium in an upflow bioreactor.
23 d endothelial cells, either on discs or in a bioreactor.
24 re analyzed in the gastight headspace of the bioreactor.
25 s but as components of an incompletely mixed bioreactor.
26 hic bacteria from a laboratory-scale anammox bioreactor.
27 taminated soil after treatment in an aerobic bioreactor.
28 without compromising the performances of the bioreactors.
29  freshwater ecosystems, and in the design of bioreactors.
30 are two main cell types used for large-scale bioreactors.
31 ld higher output than provided by industrial bioreactors.
32  when held in a steady metabolic state using bioreactors.
33  pH, and other variables were similar across bioreactors.
34 rn highly efficient miniature biosensors and bioreactors.
35  conditions, as well as in turbulently mixed bioreactors.
36 gh-temperature processing, drop dynamics and bioreactors.
37  UV radiation in specifically designed photo-bioreactors.
38 A extracted from activated sludge in the two bioreactors.
39 -scale and a full-scale wastewater treatment bioreactors.
40 ontaminated sites, extreme environments, and bioreactors.
41 uently oxidized to sulfate in oxygen-limited bioreactors.
42 rs and for culturing artificial cartilage in bioreactors.
43 ates under conditions encountered in typical bioreactors.
44 atidylcholine) vesicles for realizing porous bioreactors.
45  tests in shake flasks and 1 L spinner-flask bioreactors.
46 ve and not easily integrable with low-volume bioreactors.
47  sewage transport, can also be considered as bioreactors.
48                             Silica microbead bioreactors (0.5 microm diameter) coated with DNA and en
49  wastewater treatment using aerobic membrane bioreactors (1-2 kWh/m3).
50 tly removed PAHs from the contaminated soil (bioreactor 69% removal, column 84% removal), bioreactor
51   The inability to consistently develop such bioreactors affects the way growth approaches for Dehalo
52  earlier manual processing with nanoparticle bioreactors, allowing a range of significant enzyme reac
53              The distal colon functions as a bioreactor and harbors an enormous amount of bacteria in
54 namics for a continually operated mesophilic bioreactor and highlight the enormous potential of delta
55 eks of sequential culture in a rotating wall bioreactor and perfusion at 6.8 dynes/cm(2).
56 otential as advanced drug delivery vehicles, bioreactors and artificial cells.
57               Using continuous-flow sediment bioreactors and batch incubations, we characterized (i)
58 ort, electronics, energy production, optics, bioreactors and catalysis.
59 rs on osteoconductive scaffolds in perfusion bioreactors and confirmed their phenotype stability in a
60 er in high-aspect ratio rotating wall vessel bioreactors and examined throughout the early stages of
61 proximately 3 mm beads that were packed into bioreactors and fed ad libitum.
62  in cell cultures, 3D models of live tissue, bioreactors and fluidic chips; ex vivo and in vivo O2 me
63  ecosystems ranging from oceans and soils to bioreactors and humans.
64 te the rapid commissioning of iron-oxidizing bioreactors and illustrated how microbial communities wi
65 The results are not restricted to bubbles in bioreactors and may be relevant to a variety of applicat
66 creasing interest in developing microfluidic bioreactors and organs-on-a-chip platforms combined with
67 sments of cellular functions in microfluidic bioreactors and organs-on-chips.
68 ed equipment including large stainless steel bioreactors and tanks to hold product intermediates and
69          Both the low animal cell density of bioreactors and their ability to post-translationally pr
70 ics (in the MFC) and nutrients (in the algal bioreactor), and the production of bioenergy in electric
71  consisting of a primary clarifier, membrane bioreactor, and five post-treatment technologies includi
72 ineralization: zinc as ZnS in a sulfidogenic bioreactor, and iron as schwertmannite by microbial iron
73 such as waters, soils, extreme environments, bioreactors, and human microbiomes.
74 called an anaerobic electrochemical membrane bioreactor (AnEMBR).
75 thodes in anaerobic electrochemical membrane bioreactors (AnEMBRs) operated at different applied volt
76  was to evaluate emerging anaerobic membrane bioreactor (AnMBR) technology in comparison with convent
77 n of dissolved methane in anaerobic membrane bioreactors (AnMBRs) treating a synthetic dilute wastewa
78 s-cast Mg-Zn-Mn, and extruded Mg-Zn-Mn) in a bioreactor applying cyclical loading and simulated body
79 scopic mineral deposits that form within the bioreactor are consistent with bone hydroxyapatite.
80 peed, and the hydrodynamic conditions in the bioreactor are shown to affect not only the overall rate
81                                     In-field bioreactors are a powerful tool for capturing natural mi
82                                   Artificial bioreactors are desirable for in vitro biochemical studi
83                                        These bioreactors are implanted in an ectopic site in the body
84                                              Bioreactors are typically composed of billions of cells,
85 est that denitrification in an aged woodchip bioreactor at constant temperature can effectively be mo
86 unds into a microfluidic human primary liver bioreactor at desired time points while monitoring their
87 imilar Monod growth kinetics when grown in a bioreactor at varying H(2) concentrations.
88 e-treatment plant (sequencing batch membrane bioreactor) at two solids retention times (SRTs): 20 and
89  Porcine AV cusps were cultured in a stretch bioreactor, at 10% (physiological) or 15% (pathological)
90                                A specialized bioreactor based on the principle of simultaneous growth
91                                     In vitro bioreactor-based cultures are being extensively investig
92 vitro from mouse ESCs using either static or bioreactor-based cultures, with that of native LKS cells
93 ue-engineered cartilage as an alternative to bioreactor-based mechanical stimulation.
94 on for vascular tissue engineering are still bioreactor-based, extremely expensive, laborious and tim
95 ion of the yeast Saccharomyces cerevisiae in bioreactor batch cultures yielded variants that grow as
96                                          The bioreactors became rapidly colonized by this bacterium,
97 is bleed stream can be treated in a separate bioreactor by reducing thiosulfate to sulfide and recycl
98  short duration dose of NO3(-) to an anammox bioreactor can rapidly restore the activity of NO2(-)-st
99  h(-1), and microbial communities within the bioreactors changed over time, with Atx. ferrooxidans be
100 is study, seven pilot-scale sulfate-reducing bioreactor columns containing varying ratios of alfalfa
101               A null model demonstrated that bioreactor communities were driven in part not only by e
102 ore the need for more detailed assessment of bioreactor community ecology and justify pilot- and full
103 ictions suggest that a large portion of each bioreactor community is autotrophic, relying not on mola
104 uced in W and WH in a further scale-up to 5L bioreactors, confirming the suitability of the low-cost
105                             Laboratory-scale bioreactors containing bauxite residue (an alkaline, sal
106 al evidence toward the feasibility of upflow bioreactors containing D. mccartyi as high-density cultu
107  steps of unsaturated LCFA was studied in 10 bioreactors continuously operated with saturated or unsa
108             In the first stage, an anaerobic bioreactor converts mixtures of gases of CO2 and CO or H
109 crobial communities for wastewater treatment bioreactors, could inspire development of mechanistic ma
110 nterpreting acetate metabolite trends from a bioreactor cultivation of Chinese hamster ovary cells ex
111 accharomyces cerevisiae during two different bioreactor cultivations.
112                                           In bioreactor culture, when syngas flowrate increased from
113 affolds (templates for tissue formation) and bioreactors (culture systems providing environmental con
114                                    Perfusion bioreactor cultures of primary human hepatocyte spheroid
115 Further, when compared to cells derived from bioreactor cultures, static culture-derived LKS cells sh
116                                 In contrast, bioreactor-derived LKS cells, when differentiated under
117 e is to introduce the concept of the in vivo bioreactor, describe important preclinical models in the
118       The aim of this study was to develop a bioreactor design for continuous milk coagulation using
119 00 mL gdcw(-1) h(-1)) were achieved in a new bioreactor designed and optimized for H2 production.
120 eriments in a novel high-temporal-resolution bioreactor, DOC concentration decreased by an average of
121 cult to characterize samples pulled from the bioreactor due to the low levels of product during the e
122  the same excellent quality as with membrane bioreactors due to the much lager pore sizes of the mesh
123 d on a cross-flow continuous membrane enzyme bioreactor (EMR).
124 ltivation in a 5 L continuously stirred tank bioreactor enabled production of 0.8 g lactate/L, repres
125 % respectively) over a 7-day period in a CDC bioreactor environment.
126 technological and biomedical applications in bioreactors, environmental sensing, drug monitoring, con
127 ined thermodynamic geochemical modeling with bioreactor experiments using Shewanella oneidensis MR-1.
128 rlong monthly time series of nine full-scale bioreactor facilities treating brewery wastewater (>20,0
129                          Silica nanoparticle bioreactors featuring thin films of enzymes and polyions
130 e established and operated a continuous-flow bioreactor fed increasing loadings of SCN(-).
131  extents of pH neutralization were higher in bioreactors fed with simpler organic carbon substrates (
132 achate using four laboratory-scale anaerobic bioreactors filled with municipal solid waste (MSW) and
133 cate) (PGS) and cultured in a pulsatile flow bioreactor for 3 wk.
134 olumn for application as a biosensor or as a bioreactor for continuous destruction of DNAN.
135 e-emulsion (DE) droplets as pico-liter sized bioreactor for rapid cell assembly and well-controlled m
136 ked environmental samples and samples from a bioreactor for sulfate reduction to sulfide were measure
137 ved the operating conditions of an anaerobic bioreactor for the conversion of complex yeast-fermentat
138 ermit good results and can be used to make a bioreactor for various applications in food industries.
139 ignificance in the design of one-step, green bioreactors for stereoselective drug metabolite synthesi
140 ubstrates/inhibitors and fabrication of nano-bioreactors for synthesis of high value natural products
141 lastoid cells in a high aspect ratio vessel (bioreactor) for 72 h either in the rotating condition to
142 n fluorescent protein, which when grown in a bioreactor generated more than 20 L of supernatant with
143 ficiency based on operational parameters and bioreactor geometry, and we verified it with experimenta
144               NMR experiments using advanced bioreactors have advantages with respect to having full
145           To address these problems, in vivo bioreactors have been explored as an approach to generat
146 ) bioreactor operating conditions; and (iii) bioreactor history (after perturbations during the opera
147 e composition after biomass pretreatment and bioreactor history are also important.
148                A horizontal rotating tubular bioreactor (HRTB) is a combination of a thin layer and a
149 e body, where ossified tissue grows into the bioreactor in predefined geometries and local vessels ar
150 PHBV cell accumulation were observed in both bioreactors in excess of nitrogen.
151 ed values that would kill many cells used in bioreactors, including Chinese Hamster Ovary (CHO) cells
152 oprecipitation of the phosphate added to the bioreactor influent.
153     We carried out experiments with gas lift bioreactors inoculated with haloalkaliphilic sulfide-oxi
154                                  In sediment bioreactors, inorganic carbon stable isotope mass balanc
155 n the selectivity for sulfur production in a bioreactor integrated with a gas absorber.
156 t needed for the stimulations in a one-liter bioreactor is only one-tenth of a US penny.
157          The capacity to serve as microscale bioreactors is established by demonstrating a ribozyme c
158 batches of organic-rich sediments in a novel bioreactor (IsoCaRB) that permitted continuous observati
159 arable with efficient incineration, MBT, and bioreactor landfilling technologies.
160                 Samples were drawn along the bioreactor length for monitoring the metal contents on s
161 lactate oxidase were immobilized in ABS flow bioreactors (manufactured through low-cost three-dimensi
162 yngas fermentation, and its implication with bioreactor mass transfer.
163 robial product (SMP) extracted from membrane bioreactor (MBR) feedwater, backwashed membrane, and che
164  acid) was investigated employing a membrane bioreactor (MBR) integrated with either ozonation or UV/
165 s applying oxidation ditch (OD) and membrane bioreactor (MBR) processes harbored a majority of shared
166 this article, the current status of membrane bioreactor (MBR) technology for wastewater treatment is
167                       A pilot-scale membrane bioreactor (MBR) was installed and operated for one year
168                       A pilot-scale membrane bioreactor (MBR) was tested for bioremediation of 1,2-di
169         It is a modification of the membrane bioreactor (MBR), in which a membrane filtration process
170 embranes in a bench-scale submerged membrane bioreactor (MBR).
171 s were investigated in a full-scale membrane bioreactor (MBR; nominal pore size 0.04 mum): (i) attach
172 tions in batch reactors and membrane-coupled bioreactors (MBRs).
173 gging probe to monitor MICP in a sand-filled bioreactor, measuring NMR signal amplitude and T2 relaxa
174 be mitigated by lowering the salinity of the bioreactor medium.
175 rid microfiltration-forward osmosis membrane bioreactor (MF-FOMBR) for direct phosphorus recovery fro
176 ells and an anaerobic fluidized bed membrane bioreactor (MFC-AFMBR), was examined here to produce hig
177  air-biocathode microbial fuel cell-membrane bioreactor (MFC-MBR) system was developed to achieve sim
178 ng microbial community in a laboratory-scale bioreactor model that closely mimicked estuary or bracki
179            We review the state of the art in bioreactor modeling and current efforts in modeling the
180 umn (BCR) and an internal loop airlift (ALR) bioreactors of 2.3 L for the abatement of N2O from a nit
181 nfigurations, while also enabling the use of bioreactors of greater optical depth operating at lower
182                         The osmotic membrane bioreactor (OMBR) is an emerging technology that uses wa
183        In order to design a green microsomal bioreactor on suitably identified carbon electrodes, it
184 ulfate conversion to sulfide in a H2/CO2 fed bioreactor operated at haloalkaline conditions was inves
185                                   Continuous bioreactors operated at low hydraulic retention times ha
186  experiments in laboratory-scale chemostatic bioreactors operated through a series of pH values (2.1-
187 f the best-suited assays for each industrial bioreactor operating condition, discuss next-generation
188  the factors: (i) biomass pretreatment; (ii) bioreactor operating conditions; and (iii) bioreactor hi
189 biomass, it was possible to achieve a stable bioreactor operation at which 80% of the supplied H2S (6
190 itude and that new approaches might optimize bioreactor operation.
191                                Utilizing the bioreactor or immobilized human cells, the production of
192 s has led to the concept of using plants as "bioreactors" or "biofactories" for the production of pha
193                                    We report bioreactor performance and dehalogenation kinetics of a
194 uences for 112 samples) with function (i.e., bioreactor performance) and environment (i.e., operating
195    The impact of cadmium perturbation on the bioreactor performance, bacterial activity, bacterial co
196 are taxa likely play an unrecognized role in bioreactor performance.
197                                              Bioreactor perturbations were shown to create cell abund
198 e the toxicity of carboxylic acids at acidic bioreactor pH levels even more, and this can, for exampl
199         Advances in upstream processing (the bioreactor phase) have been successful in achieving high
200 resonance spectroscopy (MRS) combined with a bioreactor platform and interrogated the biochemical bas
201 (MGP) site was treated in a laboratory scale bioreactor (postbioremediation) and extracted using pres
202 adsorption unit and a periphyton-based photo-bioreactor (PPBR), was built and applied for the first t
203 ll model that could be used to develop novel bioreactors, primitive artificial cells and plausible pa
204 etic groundwater at 11-3.6 h HRT, the upflow bioreactor removed >99.7% of the influent trichloroethen
205  biotechnology industry, as production scale bioreactors require continuous injection of oxygen bubbl
206 d-up production of these strains in benchtop bioreactors resulted in almost ten- and fivefold increas
207 anner either using spinner flasks or cellbag bioreactors, resulting in a final purified yield of appr
208  maturation of bone substitutes in perfusion bioreactors results in global repression of cell prolife
209  wastewater, and its conversion in anaerobic bioreactors results in palmitate (C16:0) accumulation.
210 r performance in a trichloroethene-degrading bioreactor, revealing population structures as well as t
211  of a lab-scale submerged anaerobic membrane bioreactor (SAnMBR), and their role in membrane fouling,
212  heterologous host Pichia pastoris on the 5L bioreactor scale (reUmChlE; 45.9UL(-1)).
213 ation of these beads into a novel swirl flow bioreactor (SFB), of low capital and running costs and o
214 d and ventilated cell-seeded constructs in a bioreactor simulating the physiologic environment of dev
215                                          The bioreactor simultaneously consumed sulfide, methane and
216 omplished by extracting the product from the bioreactor solutions.
217   Here, we developed a miniaturized spinning bioreactor (SpinOmega) to generate forebrain-specific or
218 trategy is evaluated for use in microfluidic bioreactor studies specifically aimed at characterizing
219 rations including three-dimensional culture, bioreactor studies, as well as microfabricated co-cultur
220 bioremediation processes: a sequencing batch bioreactor system and a continuous-flow column system.
221 nate, and sulfate was treated in a fixed-bed bioreactor system consisting of two reactors (reactors A
222                            The simple to use bioreactor system provides an in vitro model that permit
223               We used a rotating wall vessel bioreactor system to create 3-dimensional (3-D) epitheli
224                                  An in-field bioreactor system was developed to assess oxic versus an
225 ltured for up to 21 days in a flow perfusion bioreactor system wherein alpha-MEM (supplemented with 1
226 ltured for up to 21 days in a flow perfusion bioreactor system wherein alpha-MEM (supplemented with 1
227 em cells (hMSCs) and a "biomimetic" scaffold-bioreactor system.
228 e continuously perfused with nutrients via a bioreactor system.
229 ies, such as fecal microbiota transplant and bioreactor systems' optimization, suggest a promising ro
230 edia formulations, and potentially different bioreactor systems.
231 jective of this work was to develop a tissue bioreactor (TBR) enabling modulation of the microenviron
232 icacy, and will enable future development of bioreactor technologies at full field scale.
233 hicles to regenerative medicine, inexpensive bioreactor technology and tissue engineering therapies.
234                             Now, advances in bioreactor technology, metabolic engineering, and analyt
235 cell line and the rotating wall vessel (RWV) bioreactor technology.
236 planted and maintained for 24 h ex vivo in a bioreactor that preserves EMB viability and function.
237 have developed a microfluidic human platelet bioreactor that recapitulates bone marrow stiffness, ext
238 ts for up to 28 d by coronary perfusion in a bioreactor that simulated cardiac physiology.
239 d paddy fields are efficient denitrification bioreactors that can achieve decontamination of nitrate-
240  refinements of the model, we also developed bioreactors that enable intravital nonlinear optical mic
241 rming make some aquatic ecosystems behave as bioreactors that trigger rapid and massive cyanobacteria
242 production rate of 0.47 g COD l(-1) d(-1) in bioreactors that were fed with dilute-acid pretreated co
243 hod for controlling the oxygen supply to the bioreactor, that is, by maintaining a redox potential se
244                          Compared to control bioreactors, those with 11-12 mM of toluene in the oil (
245 rom industrial off-gases in two-liquid phase bioreactors (TLPBs).
246 cellularize rat oesophagi inside a perfusion bioreactor to create biocompatible biological rat scaffo
247 rioallantoic membrane (CAM) can be used as a bioreactor to culture and study the regeneration of huma
248                               We then used a bioreactor to culture pulmonary epithelium and vascular
249     The use of bioengineered human skin as a bioreactor to deliver therapeutic factors has a number o
250                    We developed microfluidic bioreactors to enable the investigation of the effects o
251 mals have great potential to act as powerful bioreactors to produce human therapeutic proteins.
252 y plant-based systems have been developed as bioreactors to produce recombinant proteins.
253  We operated six thermophilic (55 degrees C) bioreactors to test how the factors: (i) biomass pretrea
254 n hydrogels rich in maturogens and placed in bioreactors to undergo the fusion process of self-assemb
255 dimensional organoids, using a fluidised bed bioreactor, together with single-use bioprocessing equip
256 om no-surfactant controls, incubation of the bioreactor-treated soil with all surfactants increased P
257 t genes (ARG) in anaerobic, aerobic, and AAS bioreactors treating domestic wastewater.
258 bioreactor 69% removal, column 84% removal), bioreactor treatment resulted in an increase in toxicity
259 gues were shown to accumulate as a result of bioreactor treatment, and the C15H8O2 compound purified
260 load of 125 mg/L of each metal underwent the bioreactor treatment.
261    A hybrid ultrafiltration-osmotic membrane bioreactor (UFO-MBR) was investigated for over 35 days f
262 spiratory pathway mutants in three-electrode bioreactors under controlled flavin concentrations.
263 ifying enrichment cultures from a continuous bioreactor, up to 59.89 +/- 1.12 mg COD/L of CH(3)OH was
264 trafiltration permeate (UFP) from a membrane bioreactor used to treat municipal wastewater.
265 nalysis of samples from two laboratory-scale bioreactors used to study SCN(-) and CN(-) degradation.
266       We have constructed a small intestinal bioreactor using 3-D printing and polymeric scaffolds th
267 butanol and 3-methyl-1-butanol in an electro-bioreactor using CO(2) as the sole carbon source and ele
268 nd biotrickling filters depends on three key bioreactor variables: the support medium; gas molecule s
269 on, and light delivery throughout the entire bioreactor volume by using light-directing waveguides.
270              The concentration of NCO in the bioreactor was 11 mug g(-1) dry soil, corresponding to 1
271                Stable co-culture in the same bioreactor was achieved by designing a mutualistic relat
272 as defined and a technically-friendly enzyme bioreactor was developed in order to carry out a continu
273                        An anaerobic membrane bioreactor was retrofitted with polyvinylidene fluoride
274 ocal N2O emissions of a wastewater treatment bioreactor was sampled by a dedicated mobile sampling de
275 ent in the effluent of an anaerobic membrane bioreactor was then carried out using these assay method
276         In this work, an automated perfusion bioreactor was used to obtain and maintain human hepatoc
277 lis (rAvPAL) and their ability to perform as bioreactors was assessed in vivo in adult BTBR-Pah(enu2)
278                       The performance of the bioreactors was monitored throughout and the speciation
279 nization into an ecosystem (activated sludge bioreactor) was measured through a disturbance gradient
280                                     Woodchip bioreactors (WBRs) are increasingly being applied to rem
281  with sulfide produced in a sulfate-reducing bioreactor were studied at pH 3, 5, and 7.
282 ch human primary hepatocytes cultured in the bioreactor were treated with acetaminophen.
283   Enzyme turnover rates using the microsomal bioreactors were 2-3 fold larger compared to using conve
284                              Continuous-flow bioreactors were commissioned and tested for their capac
285 id product is fed as a substrate to a second bioreactor, where it is converted aerobically into lipid
286                           However, the "best bioreactor", which would be able to achieve maximum prod
287 was achieved through suspension culture in a bioreactor, which enabled the preparation of >10 mg of m
288 t option is anaerobic-aerobic sequence (AAS) bioreactors, which use an anaerobic pretreatment step (e
289 in the nutrient-rich upstream portion of the bioreactor, while the lower part of the system, which la
290                                            A bioreactor with a chamber in the exact shape of a human
291  digestion (CAS+AD), and an aerobic membrane bioreactor with anaerobic digestion (AeMBR+AD).
292 In an acetate-fed anaerobic-aerobic membrane bioreactor with deteriorated enhanced biological phospho
293                      In the present study, a bioreactor with gas sparging was used, where we observed
294                 In this work, we developed a bioreactor with living cultures of human respiratory epi
295 n low- and high-pressure, water-wet sandpack bioreactors with 0.5 pore volumes of residual oil in pla
296      In this work, continuous experiments in bioreactors with anammox bacteria closely related to "Ca
297  We show that semipermeable, size-controlled bioreactors with aqueous, macromolecularly crowded inter
298 ogenitors on 3D osteoconductive scaffolds in bioreactors with medium perfusion leads to the formation
299                     In wastewater treatment, bioreactors with microbial biofilms are widely used.
300 good manufacturing practices (GMP)-compliant bioreactor yielded effector cells that in a neuroblastom

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