Summary

First some trials of shaking flask cultivations were made with different parameters to define the best conditions for production of the His tagged CotA from [http://www.dsmz.de/catalogues/details/culture/DSM-27.html Bacillus pumilus DSM 27 ( ATCC7061)] named BPUL. Due to inactivity of the enzyme in the cell lysate a purification method was established (using Ni-NTA-Histag resin and Syringe or ÄKTA method). The purified BPUL could be detected by SDS-PAGE (molecular weight of 58.6 kDa) as well as by MALDI-TOF. To improve the purification strategies the length of the linear elution gradient was increased up to 200 mL . The fractionated samples were also tested concerning their activity and revealed high activity. Optimal conditions for activity were identified. After measuring activity of BPUL a successful scale up was made up to 3 L and also up to 6 L that enables an intense screening afterwards. A further scale up to 12 L with a optimized medium (HSG) was implemented to enable additional experiments to characterize BPUL. Additional scale up experiments will be important for further real world applications.

Cultivation, Purification and SDS-PAGE

Shaking Flask Cultivation

3 L Fermentation E. coli KRX with <partinfo>BBa_K863000</partinfo>

Figure 1: Fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo> (BPUL) in a Braun Biostat B, scale: 3 L, autoinduction medium + 60 µg/mL chloramphenicol, 37 °C, pH 7, agitation on cascade to hold pO₂ at 50 %, OD₆₀₀ measured every 30 minutes.

After the measurement of BPUL activity we made a scale-up and fermented E. coli KRX with <partinfo>BBa_K863000</partinfo> in aBraun Biostat B fermenter with a total volume of 3 L. Agitation speed, pO₂ and OD₆₀₀ were determined and illustrated in Figure 1. We got a long lag phase of 2 hours due to a relatively old preculture. The cell growth caused a decrease in pO₂ and after 3 hours the value fell below 50 %, so that the agitation speed increased automatically. After 8.5 hours the deceleration phase started and therefore the agitation speed was decreased. The maximal OD₆₀₀ of 3.53 was reached after 10 hours, which means a decrease in comparison to the fermentation of E. coli KRX under the same conditions (OD_600,max =4.86 after 8.5 hours, time shift due to long lag phase). The cells were harvested after 11 hours.

Purification of BPUL

The harvested cells were resuspended in Ni-NTA-equilibrationbuffer, mechanically lysed by homogenization and cell debris were removed by centrifugation. The supernatant of the lysed cell paste was loaded on the Ni-NTA-column (15 mL Ni-NTA resin) with a flowrate of 1 mL min^-1 cm^-2. The column was washed with 10 column volumes (CV) Ni-NTA-equilibrationbuffer. The bound proteins were eluted by an increasing Ni-NTA-elutionbuffer gradient from 0 % to 100 % with a total volume of 100 mL and the elution was collected in 10 mL fractions. In Figure 2 only the UV-detection signal of the wash step and the elution are shown, this is because of the high UV-detection signal of the loaded samples and to simplify the illustration of the detected product peak.A typical chromatogram of purified laccases is illustrated here. The chromatogram of the BPUL-elution is shown in Figure 2:

Figure 2: Chromatogram of wash and elution from FLPC Ni-NTA-His tag purification of BPUL produced by 3 L fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo>. BPUL was eluted between a process volume of 460 mL to 480 mL with a maximal UV-detection signal of 69 mAU

The chromatogram shows a remarkable widespread peak between the process volume of 460 mL to 480 mL with the highest UV-detection signal of 69 mAU, which can be explained by the elution of bound proteins. The corresponding fractions were analyzed by SDS-PAGE analysis. During the elution, a steady increase of the UV-signal caused by the increasing imidazol concentration during the elution gradient. Between the process volume of 550 and 580 mL there are several peaks (up to a UV-detection-signal of 980 mAU) detectable. These results are caused by an accidental detachment in front of the UV-detector. Just to be on the safe side, the corresponding fractions were analyzed by SDS-PAGE analysis. The corresponding SDS-PAGE is shown in Figure 3.

SDS-PAGE of purified BPUL

Figure 3: SDS-PAGE of purified E. coli KRX lysate containing <partinfo>BBa_K863000</partinfo> (fermented in a 3 L Biostat Braun B fermenter). The flow-through, wash and the elution fractions 7 and 8 are shown. The arrow marks the BPUL band with a molecular weight of 58.6 kDa.

Figure 3 shows the purified ECOL including flow-through, wash and the elution fractions 7 and 8. These two fractions were chosen due to a high peak in the chromatogram. BPUL has a molecular weight of 58.6 kDA and was marked with a red arrow. The band appears in both fractions. There are also some other non-specific bands, which could not be identified. To improve the purification the elution gradient length should be longer and slower the next time.

The appearing bands were analyzed by MALDI-TOF and could be identified as CotA (BPUL).

6 L Fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo>

Figure 4: Fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo> (BPUL) in aBioengineering NFL22 fermenter, scale: 6 L, autoinduction medium + 60 µg mL^-1 chloramphenicol, 37 °C, pH 7, agitation increased when pO₂ was below 30 %, OD₆₀₀ measured every hour.

Another scale-up for E. coli KRX with <partinfo>BBa_K863000</partinfo> was made up to a final working volume of 6 L in a Bioengineering NFL22. Agitation speed, pO₂ and OD₆₀₀ were determined and illustrated in Figure 4. There was no noticeable lag phase. Agitation speed was increased up to 425 rpm after one hour due to problems caused by the control panel. The pO₂ decreased until a cultivation time of 4.75 hours. The increasing pO₂ level indicates the beginning of the deceleration phase. There is no visible break in cell growth caused by an induction of protein expression. A maximal OD₆₀₀ of 3.68 was reached after 8 hours of cultivation, which is similar to the 3 L fermentation (OD₆₀₀ = 3.58 after 10 hours, time shift due to long lag phase). The cells were harvested after 12 hours.

Purification of BPUL

The harvested cells were prepared in Ni-NTA-equilibrationbuffer, mechanically lysed by homogenization and cell debris were removed by centrifugation. The supernatant of the lysed cell paste was loaded on the Ni-NTA-column (15 mL Ni-NTA resin) with a flow rate of 1 mL min^-1 cm^-2. The column was washed with 5 column volumes (CV) Ni-NTA-equilibrationbuffer. The bound proteins were eluted by an increasing elutionbuffer gradient from 0 % (equates to 20 mM imidazol) to 100 % (equates to 500 mM imidazol) with a length of 200 mL. This strategy was chosen to improve the purification by a slower increase of Ni-NTA-elutionbuffer concentration. The elution was collected in 10 mL fractions. In Figure 5 only the UV-detection signal of the wash step and the elution are shown, this is because of the high UV-detection signal of the loaded samples and to simplify the illustration of the detected product peak. A typical chromatogram of purified laccases is illustrated here. The chromatogram of the BPUL elution is shown in Figure 5.

Figure 5: Chromatogram of wash and elution from FLPC Ni-NTA-Histag Purification of BPUL produced by 6 L fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo>. BPUL was eluted between a process volume of 832 mL and 900 mL with a maximal UV-detection signal of 115 mAU.

The chromatogram shows a peak at the beginning of the elution. This can be explained by pressure fluctuations upon starting the elution procedure. In between the processing volumes of 832 mL and 900 mL there is remarkable widespread peak with a UV-detection signal of 115 mAU. This peak corresponds to an elution of bound proteins at a Ni-NTA elution buffer concentration between 10 % and 20 % (equates to 50-100 mM imidazol). The corresponding fractions were analyzed by SDS-PAGE. The ensuing upwards trend of the UV-signal is caused by the increasing imidazol concentration during the elution gradient. Towards the end of the elution procedure there is a constant UV-detection signal, which shows, that most of the bound proteins was already eluted. Just to be on the safe side, all fractions were analyzed by SDS-PAGE to detect BPUL. The SDS-PAGE is shown in Figure 6.

SDS-PAGE of purified BPUL

Figure 6: SDS-PAGE of purified E. coli with <partinfo>BBa_K863000</partinfo> lysate (fermented in a Bioengineering NFL22 fermenter, 6 L). The flow-through, wash and elution fraction 1 to 9 are shown. The arrow marks the BPUL band with a molecular weight of 58.6 kDa.

In Figure 6 the SDS-PAGE of the Ni-NTA purification of the lysed E. coli KRX culture containing <partinfo>BBa_K863000</partinfo> is illustrated. It shows the flow-through, wash and elution fractions 1 to 9. The His-tagged BPUL has a molecular weight of 58.6 kDA and was marked with a red arrow. The band appears in all fractions from 2 to 9 with varying strength, the strongest ones in fractions 7 to 9. There are also some other non-specific bands, which could not be identified. Therefore the purification method could moreover be improved. In summary, the scale up was successful, improving protein production and purification method once again.

Furthermore the bands were analyzed by MALDI-TOF and identified as CotA (BPUL).

Since Regionals: 12 L Fermentation E. coli KRX with <partinfo>BBa_K863000</partinfo>

Figure 7: Fermentation of E. coli KRX with <partinfo>BBa_K863000</partinfo> (BPUL) in an Bioengineering NFL 22, scale: 12 L, HSG autoinduction medium + 60 µg/mL chloramphenicol, 37 °C, pH 7, agitation on cascade to hold pO₂ at 50 %, OD₆₀₀ measured every hour.

Finally another scale-up was made and E. coli KRX with <partinfo>BBa_K863000</partinfo> was fermented in a Bioengineering NLF 22 fermenter with a total volume of 12 L to produce a high amount of the enzyme for further characterizations. This time HSG autoinduction medium was used to get a higher biomass. Agitation speed, pO₂ and OD₆₀₀ were determined and the glycerin concentration of the samples analyzed. The data are illustrated in Figure 7. At the beginning of the cultivation, the cells were in lag phase, in which they adapt to the medium. During their growth the cells consumed glycerin as well as O₂, which leads to an increase of agitation speed to hold a minimal pO₂ of 50 %. After 11 hours, the glycerin was completely consumed and the pO₂ increased up to 100 %, which indicates that the cells entered the stationary phase. The maximal OD₆₀₀ of 12.6 was reached after 12 hours of cultivation. The cells were harvested after 19 hours of cultivation.

Since Regionals: Purification of BPUL

The harvested cells were resuspended in Ni-NTA- equilibration buffer, mechanically disrupted by homogenization and cell debris were removed by centrifugation, microfiltration as well as diafiltration to concentrate the protein concentration in the cell lysate solution. This solution of the cell lysate was loaded on the Ni-NTA column (15 mL Ni-NTA resin) with a flow rate of 1 mL min^-1 cm^-2. Then the column was washed with 10 column volumes (CV) Ni-NTA equilibration buffer. The bound proteins were eluted by an increasing Ni-NTA elution buffer step elution from 5 % (equates to 25 mM imidazol) with a length of 50 mL, to 50 % (equates to 250 mM imidazol) with a length of 70 mL, to 80 % (equates to 400 mM imidazol) and finally to 100 % (equates to 500 mM imidazol) with a length of 100 mL. This strategy was chosen to improve the purification caused by a step by step increasing Ni-NTA-elution buffer concentration. The elution was collected in 10 mL fractions. A typical chromatogram of purified laccases is illustrated here. Unfortunately, the data of this procedure are not available due to a computer crash after the purification step. All Fractions were analysed to detect BPUL.

Since Regionals: SDS-Page of protein purification

Figure 8: SDS-Page of purification from the 12 L fermentations from 10/11 ([http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BBa_K863000]). Purification of the supernatant via microfiltration, diafiltration and Ni-NTA column (step gradient with 5 %, 50 % and 100 % elution buffer).

In Figure 8 the SDS-Page of the Ni-NTA purification of the lysed E.coli KRX culture containing [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BBa_K863000] is illustrated. It shows the permeate and retentate of microfiltration and diafiltration respectively, several fractions of flow-through, wash and the elutions with different buffer concentrations respectively. The selected samples were taken where peaks were seen in the chromatogram. The HIS-tagged BPUL has a molecular weight of 58.6 kDa. BPUL could not be attributed exactly to any band. There are some other non-specific bands, wich could not be identified because the MALDI was broken-down for the last two weeks.

MALDI-TOF Analysis of BPUL

The E. coli laccase was identified using the following software

• FlexControl
• Flexanalysis and
• Biotools

from Brunker Daltronics. The in silico- tryspinated created peptide mass fingerprints were compared with the measured masses gotten from the MALDI. With a sequence coverage of 21,9% BPUL was identified. In Figure 7 and 8 the chromatogram of the peptide mass fingerprint and the single masses are shown.

Figure 7: MALDI-TOF spectrum

Figure 8: MALDI-TOF spectrum results of the analysis

Activity analysis of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL]

Initial activity tests of purified fractions

Initial tests were done with elution fractions 1 to 4 to determine the activity of the purified [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase. The fractions were rebuffered into deionized H₂O using [http://www.sigmaaldrich.com/content/dam/sigma-aldrich/docs/Supelco/Product_Information_Sheet/4774.pdf HiTrap Desalting Columns] and incubated with 0.4 mM CuCl₂. The reaction setup included 140 µL of a elution fraction, 0.1 mM ABTS and 100 mM sodium acetate buffer (pH 5) to a final volume of 200 µL and the absorption was measured at 420 nm to detect oxidization over a time period of 5 hours at 25°C. Each fraction did show contained active laccase able to oxidize ABTS (see Figure 9). After 15 minutes, saturation was observed with ~60 µM oxidized ABTS. After 5 hours ~5 µM ABTS got reduced again. This behavior has been observed in the activity plot of the positive control TVEL0 before, indicating, that the oxidation catalyzed by this laccase seems is reversible. Additionally, protein concentrations of each fraction were identified using the Bradford protocol. The four tested fractions showed approximately the same amount of protein after rebuffering, namely 0.5 mg mL^-1. Fraction 4, containing the most protein and also most of active laccase was chosen for subsequent activity tests of BPUL. The protein concentration was reduced to 0.03 mg mL^-1 for each measured sample to allow a comparison between TVEL0 measurements and [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] measurements.

Figure 9: [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase activity measured in 0.1 mM ABTS and 100 mM sodium acetate buffer (pH 5) to a final volume of 200 µL at 25°C over a time period of 3.5 hours. Each tested fraction reveals activity reaching the saturation after 15 minutes with ~60 µM ABTS_ox after 0.4 mM CuCl₂ incubation. (n=4)

[http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] pH optimum

To determine at which pH the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase has its optimum in activity, a gradient of sodium acetate buffer pHs was prepared. Starting with pH 1 to pH 9 [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity was tested using the described conditions above and 0.03 mg mL^-1 protein. The results are shown in Figure 11. A distinct pH optimum can be seen at pH 5. The saturation is reached after 3 hours with 50% oxidization of ABTS through the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase at pH 5 (55 µM oxidized ABTS). The other tested pHs only led to a oxidation of 18% of added ABTS. Figure 12 represents the negative control showing the oxidation of ABTS through 0.4 mM CuCl₂ at the chosen pHs. The highest increase in oxidized ABTS can be seen at a pH of 5. After 5 hours 15% ABTS are oxidized only through CuCl₂. Nevertheless this result does not have an impact on the reactivity of the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase at pH 5, which is still the optimal pH. Therefore it has the same pH optimum as TVEL0.

Figure 11: [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase activity measured in 100 mM sodium acetate buffer with a range of different pHs from pH 1 to pH 9, 0.1 mM ABTS to a final volume of 200 µL at 25°C over a time period of 5 hours. Before the measurements samples were incubated with CuCl₂. The optimal pH for [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] is pH 5 with the most ABTS_ox.

Figure 12: Negative control for pH activity Tests using 0.04 mM CuCl₂ H₂O instead of Laccase to determine the potential of ABTS getting oxidized through CuCl₂.

In regard to our project an optimal pH of 5 is a helpful result. Since waste water in waste water treatment plants has a average pH of 6.9 it has to be kept in mind, that a adjustment of the pH is necessary.

[http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] CuCl₂ concentration

Another test of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] was done to survey the best CuCl₂ concentration for the activity of the purified [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase. 0.03 mg mL^-1 of protein were incubated with different CuCl₂ concentrations ranging from 0 to 0.7 mM CuCl₂. Activity tests were performed with the incubated samples, 0.1 mM ABTS and 100 mM sodium actetate buffer (pH 5) to a final volume of 200 µL. The reactivity was measured at 420 nm, 25°C and over a time period of 5 hours. As expected the saturation takes place after 3 hours (see Figure 12). The differences in the activity of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccases incubated in different CuCl₂ differ minimal. The highest activity of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase is observed after incubation with 0.6 mM CuCl₂ (52% of added ABTS). With a higher concentration of 0.7 mM CuCl₂ the activity seems to be reduced (only 48% ABTS got oxidized). This leads to the assumption that CuCl₂ supports the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase reactivity but concentrations exceeding this value of CuCl₂ may have a negative impact on the ability of oxidizing ABTS. This fits the expectations as laccases are copper reliant enzymes and gain their activity through the incorporation of copper. Additionally negative controls were done using the tested concentrations of CuCl₂ without applying laccase to detect the oxidization of ABTS through copper (see Figure 13). The more CuCl₂ was present, the more ABTS was oxidzied after 5 hours. Still the maximal change accounts only for ~6% oxidized ABTS after 5 hours.

Figure 12: Activity measurement using 0.1 mM ABTS of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] incubated in different CuCl₂ concentrations. Without CuCl₂ incubation the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase shows half of the activit as after CuCl₂ incubation. Incubation with 0.1 mM CuCl₂ or higher concentrations leas to an increase in ABTS_ox.

Figure 13: Negative control for CuCl₂ activity Tests using different concentrations of CuCl₂ H₂O instead of Laccase to determine the potential of ABTS getting oxidized through CuCl₂.

In relation to apply the laccase in waste water treatment plants it is beneficial knowing, that small amounts of CuCl₂ are enough to activate the enzyme. Still it is expensive to be reliant on CuCl₂ and a potential risk using heavy metals for waste water purifcation.

[http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity at different temperatures

Figure 14: Standard activity test for [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] measured at 10°C and 25°C resulting in a decreased activity at 10°C. As a negative control the impact of 0.4 mM CuCl₂ in oxidizing ABTS at 10°C were analyzed.

To investigate the activity of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] at lower temperatures, activity tests as described above were performed at 10°C and 25°C. A small decrease in the activity can be observed upon reducing the temperature from 25°C to 10°C (see Fig. 14). After 3.5 hours when samples at 25°C reached the saturation samples at 10°C had not, but nonetheless the difference is minimal. After 3 hours 5% difference in oxidized ABTS is observable. The negative control without the [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase but 0.4 mM CuCl₂ at 10°C shows a negligible oxidation of ABTS. A a decrease in the reactivity of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase was expected. The observed small reduction in enzyme activity is excellent news for the possible application in waste water treatment plants where the temperature differs from 8.1°C to 20.8°C.

[http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity depending on different ABTS concentrations

Figure 15: Analysis of ABTS oxidation by [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccases incubated in 0.4 CuCl₂ tested with different amounts of ABTS. The higher the amount of ABTS the more oxidized ABTS can be detected.

Furthermore, [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase were tested using different amounts of ABTS to calculate K_M and K_cat values. The same measurement setup as described above was used only with different amounts of ABTS. As anticipated, the amount of oxidized ABTS increased in dependence of the amount of ABTS used (Figure 15). Especially using 16 µL showed an increase in the activity until 1 hour (reaching 50 µM ABTS_ox), but the amount of oxidized ABTS decreased afterward.

Impact of MeOH and acteonitrile on [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL]

For substrate analytic tests the influence of MeOH and acetonitrile on [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccases had to be determined, because substrates have to be dissolved in these reagents. The experiment setup included 0.03 mg mL^-1 [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase, different amounts of MeOH (Figure 16) or acteonitrile (Figure 17), 0.1 mM ABTS and 100 mM sodium actetate buffer to a final volume of 200 µL. The observed reactivity of [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] in regard of oxidizing ABTS did not reveal a huge decrease. The less MeOH or acetonitrile was used, the higher was the amount of oxidized ABTS after 3 hours. An application of 16 µL MeOH or acetonitrile led to a decrease of maximal 10% oxidized ABTS compared to 2 µL MeOH or acetonitrile. Negative controls are shown in Figure 17 and 18 of the ECOL laccase. MeOH and acetonitril are able to oxidize ABTS. After 5 hours at 25°C ~15 µM ABTS get oxidized through MeOH or acetonitrile, but samples with [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] laccase show a distinct higher activity of 50 µM ABTS_ox.

Figure 16: Standard [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity test applying different amounts of MeOH. No considerable impact on the activity can be detected.

Figure 17: Standard [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity test applying different amounts of acetonitrile. No considerable impact on the activity can be detected.

Since Regionals: Initial activity tests of purified fractions

After the Regional Jamboree in Amsterdam further BPUL was produced. The most comprising fractions of the purification were analyzed for protein content (10/16), re-buffered into deionized H₂O and incubated in 0.4 mM CuCl₂. Again, the protein content (10/17) of each fraction was determined because of the loss of proteins through re-buffering. Initial activity tests were done in Britton-Robinson buffer with 0.1 mM ABTS. The protein content of each fraction was adjusted for comparison of the resulting activity (see Fig. 18).

Figure 18: Activity assay of each purified fraction of recent produced BPUL. Samples were re-buffered into H₂O and the protein amount in each fraction was adjusted. The measurement was done using the standard activity assay protocol over night. The first number indicates the percentage of used elution buffer, whereas the second number stands for the fraction number of this elution.

Fraction 50% 2 showed the highest activity. The first number indicates the percentage of used elution buffer, whereas the second number stands for the fraction number of this elution. The saturation was reached at ~1 h. For comparison it was stated that this fraction contains 90 % laccase and therefore the BPUL concentration is 25,1 µg mL^-1.

Since Regionals: [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity depending on different ABTS concentrations

In order to find the substrate saturation, laccase activity was measured with ABTS concentrations ranging from 0.1 mM to 8 mM. 616 ng BPUL were used for measurements with ABTS concentrations of 0.1 mM to 5 mM, 308 ng BPUL were used for measurements with ABTS concentrations of 5 mM to 8 mM. Measurements were done in Britton-Robinson buffer (pH 5) at 25 °C for 30 minutes taking the OD₄₂₀ every 5 minutes. Comparing the graphs in Figure 19 and Figure 20, both show a comprising substrate saturation with 5 mM ABTS. Higher concentrations of ABTS than 5 mM did not show any other effects on the activity of BPUL. For all following BPUL activity measurements after the Regional Jamborees in Amsterdam a concentration of 5 mM ABTS was applied.

Figure 19: Activity assay to determine the substrate saturation with ABTS as a substrate. Measurements were done with 616 ng BPUL in Britton-Robinson buffer (pH 5) at 25 °C. ABTS concentrations ranged from 0.1 mM to 5 mM.

Figure 20: Activity assay to determine the substrate saturation with ABTS as a substrate. Measurements were done with 308 ng BPUL in Britton-Robinson buffer (pH 5) at 25 °C. ABTS concentrations ranged from 5 mM to 8 mM. An ABTS concentration of 5 mM was determined as substrate saturation.

Since Regionals: [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] pH optimum

Figure 21: Microtiter plate of the measurements for pH optimum determination. The more intensive the blue color the more ABTS got oxidized. At pH 5 and pH 4 the darkest colour has been reached.

The pH of the medium containing the enzyme is of high importance for its activity. The pH optima of BPUL are pH 4 and pH 5. This is the result of activity measurements using Britton-Robinson buffer with differently adjusted pHs. BPUL was re-buffered into H₂O and incubated with 0.4 mM CuCl₂. The range from pH 4 to pH 9 was tested under substrate saturation at 25 °C for 30 minutes. At pH 4 and pH 5 ABTS got oxidized the fastest (see Fig. 21 and Fig. 22). At higher pHs than pH 5, the activity of BPUL was decreased considerably. The resulting Units mg^-1 support the observed data (see Fig. 23). At pH 4 and pH 5 BPUL showed a specific enzyme activity of ~37 U mg^-1. The higher the pH, the less U mg^-1 could be calculated for BPUL. At pH 7 1/3 of the activity decreased, but still BPUL was active at this pH allowing an application of this laccase in a waste water treatment plant where the average pH is a pH of 6.9.

Figure 22: Oxidized ABTS by BPUL at different pH adjustments. The experimental setup included CuCl₂ incubated BPUL laccase (308 ng), Britton Robinson buffer adjusted to the tested pHs and 5 mM ABTS. Measurements were done at 25 °C for 30 minutes. The highest amount of oxidized ABTS was detected at pH 4 and pH 5.

Figure 23: Calculated specific enzyme activity of BPUL at different pH conditions. The highest specific enzyme activity for ABTS was under pH 4 and pH 5 conditions. The higher the pH, the less ABTS got oxidized. One unit is defined as the amount of laccase that oxidizes 1 μmol of ABTS substrate per minute.

Since Regionals: [http://partsregistry.org/wiki/index.php?title=Part:BBa_K863000 BPUL] activity at different temperatures

Figure 24: Standard activity test for BPUL measured at 10 °C and 25 °C resulting in a comparable activity at the tested temperatures. As a negative control the impact of 0.4 mM CuCl₂ in oxidizing ABTS at 10 °C and 25 °C was analyzed.

Figure 25: Deriving from the obtained values of oxidized ABTS in time at 10 °C and 25 °C the specific enzyme activity was calculated. For the temperatures only a difference of 1 U mg^-1 could be detected. One unit is defined as the amount of laccase that oxidizes 1 μmol of ABTS substrate per minute.

To investigate the activity of BPUL at temperatures that will apply at a waste water treatment plant throughout the year, activity tests were performed at 10 °C and 25 °C as described above. The obtained results reveal a comparable activity of BPUL at high and low temperatures (see Fig. 24). The measurements were conducted for 30 minutes until saturation initiated. Both samples reached saturation after 15-20 minutes. The obtained results were used to calculate the specific enzyme activity which was in both cases at about 37 U mg^-1 (see Fig. 25). The negative control without BPUL laccase but 0.4 mM CuCl₂ at 10 °C and 25 °C show a negligible oxidation of ABTS. The observed activity at both conditions was good news for the possible application in waste water treatment plants where the temperature differs from 8.1 °C to 20.8 °C.

Substrate Analysis

Figure 2: Degradation of estradiol (dark green) and ethinyl estradiol (light green) with the different laccases after 5 hours without ABTS. In the graph it is shown that the bought laccase TVEL0 which was used as positive control is able to degrade more than 90 percent of the used substrates. None of the bacterial laccases are able to degrade ethinyl estradiol without ABTS but estradiol is degraded in a range from 16 %(ECOL) to 55 % (TTHL). The original concentrations of substrates were 2 µg per approach. (n = 4)

The measurements were made to test if the produced laccases were able to degrade different hormones. Therefore the produced laccases were inserted in the same concentrations (3 µg mL^-1) to the different measurement approaches. To work with the correct pH value (which were measured by the Team Activity Test) Britton Robinson buffer at pH 5 was used for all measurements. The initial substrate concentration was 5 µg mL^-1. The results of the reactions without ABTS are shown in Figure 2. On the Y-axis the percentages of degraded estradiol (blue) and ethinyl estradiol (red) are indicated. The X-axis displays the different tested laccases. The degradation was measured at t₀ and after five hours of incubation at 30 °C. The negative control was the substrate in Britton Robinson buffer and showed no degradation of the substrates. The bought laccase TVEL0 which is used as positive control is able to degrade 94.7 % estradiol and 92.7 % ethinyl estradiol. The laccase BPUL (from Bacillus pumilus) degraded 35.9 % of used estradiol after five hours. ECOL was able to degrade 16.8 % estradiol. BHAL degraded 30.2 % estradiol. The best results were determined with TTHL (laccase from Thermus thermophilus). Here the percentage of degradation amounted 55.4 %.

Figure 3: Degradation of estradiol (blue) and ethinyl estradiol (red) with the different laccases after 10 minutes hours with ABTS added. The commercial laccase TVEL0 which was used as positive control is able to degrade all of the used substrates. The bacterial laccase BPUL degraded 100 % of ethinyl estradiol and estradiol. ECOL the laccase from E. coli degraded 6.7 % estradiol and none of the used ethinyl estradiol. BHAL degraded 46.9 % of estradiol but no ethinyl estradiol. The laccase TTHL from Thermus thermophilus degraded 29.5 % of estradiol and 9.8 % ethinyl estradiol. The original concentrations of substrates were 2 µg per approach. (n = 4)

The results of the reactions of the laccases with addition of ABTS are shown in Figure 3. The experimental set ups were the same as the reaction approach without ABTS described above. The X-axis displays the different tested laccases. On the Y-axis the percentages of degraded estradiol (blue) and ethinyl estradiol (red) are shown. The degradation was measured at t₀ and after five hours of incubation at 20 °C. The negative control showed no degradation of estradiol. 6.8 % of ethinyl estradiol was decayed. The positive control TVEL0 is able to degrade 100 % estradiol and ethinyl estradiol. The laccase BPUL (from Bacillus pumilus) degraded 46.9 % of used estradiol after ten minutes incubation. ECOL was able to degrade 6.7 % estradiol. BHAL degraded 46.9 % estradiol. With TTHL (laccase from Thermus thermophilus) a degradation 29.5 % were determined.

Immobilization

Figure 20: The percentage of laccases immobilized to CPC-Beads. 99 % of ECOL, 97 % of BPUL and 79 % of BHAL and TTHL laccases were bound to the beads.

Figure 21: Enzymatic activity of BPUL supernatant compared to the activity of nontreated laccases, measured using 0.1 mM ABTS at 25°C over a time period of 12hours. The results show a dramatic decrease of BPUL in the Supernatant.

Figure 22: Illustration of ABTS oxidation by BPUL with time compared to the negative control. The increase in ABTS oxidized proves laccase activity.