Engineering

Overview

Mycosporine-like Amino Acids (MAAs) are a family of UV-absorbing natural products found in diverse organisms, especially in those that are exposed to extensive solar radiation such as cyanobacteria in ocean. Demand for novel,natural sunscreens is growing due to the potential negative effects on human health (endocrine disruption et.) and environmental (coral reef bleaching et.) of synthetic sunscreens. The diversity of MAAs allows them to absorb different wavelengths of UV radiation. The current method to obtain MAAs is through extraction from MAA-containing organisms such as nori; however, this method is extremely inefficient and costly. This year, LINKS_China attempted and succeeded in establishing and optimizing a series of metabolic pathways in S. cerevisiae to produce four molecules as the novel sunscreen. We aimed our experiments at three aspects. Firstly, we increased the production of S7P and 4DG, the precursors of most MAAs, by deleting endogenous TAl1 and introdcing exogenous xylose-utilizing pathway . Secondly, we combined different AGL and Alal ligases from three organisms to produce shinorine and porphyra-334 from 4DG, then choose and optimize the most effective combination. Lastly, we produced palythine and gadusol based on our previous genetic circuit. All gene expression is ultimately performed in the S. cerevisiae genome, a more stable and efficient expression than plasmid expression. In order to provide a more secure protection for our skin, we produced hSOD-linker-catalase in order to break down reactive oxygen species(ROS) caused by UV radiation that bypasses the barrier of MAAs.

Figure 1: The designed metabolic pathways in S. cerevisiae in order to produce MAAs. We introduced the genes Xyl 1, Xyl 2, Xyl 3 into S. cerevisiae to increase the production of S7P. We knocked out the downstream genes TAL1 and Nqm1 to prevent turnover of S7P into undesired F6P. In order to convert S7P into 4-DG, we knocked in two copies of both DDGS-OMT to the genome. Then, by arranging and comparing various AG-L and ALA-L amino acid ligases, we finally produced shinorine and porphyra-334 with the highest efficient combination. After the addition of NlmysH to the genetic circuit of shinorine, we were also able to produce MysH. To produce gadusol, we inserted the gene EEVS-MTOX into S. cerevisiae’s genome.

Increase Production of S7P and 4DG

Sedoheptulose 7-phosphate(S7P) is an intermediate of the pentose phosphate pathway, one of the alternative biosynthetic pathways of MAAs. Naturally, S7P is converted into saccharides for the later glycolytic pathway in S. cerevisiae. For more S7P to be utilized by the MAAs pathway, we decided to block the flow to glycolytic pathway by removing the endogenous TAL1. We employ the gene editing methods studied by Apel et. al. to construct a new Cas9-sgRNA plasmid pCRCT-TAL1 for the deletion of gene TAL1 (Fig.2A). By performing colony PCR (Fig.2B) and sequencing(Fig.2C), we found that we successfully removed 32 bp in TAL1's coding sequence. The deletion of the fragments will result in a frameshift mutation that renders TAL1 non-functional. After the removal of pCRCT plasmids from the cell, we obtained our first engineered strain: SC.L1.

Figure 2: Knockout of gene TAL1 by causing a frameshift mutation. (A) By transforming CRISPR-cas9 plasmid pCRCT-TAL1 and upstream and downstream homologous arms of the TAL1 loci, 32 base pairs of TAL1’s coding sequence were deleted in the recombinant stain. We verified the knockout of the strain by performing colony PCR for 11 colonies (B) and sequencing results (C), at last obtaining L1 strain.

Another method to increase the S7P levels is the introduction of xylose-utilizing pathway that provides an alternative carbon source for the pentose phosphate pathway. Xyl1, Xyl2, and Xyl3 genes from Scheffersomyces stipitis proved to be successfully heterologous expressed for efficiently xylose-fermenting in S. Cerevisiae. We used yeast toolkit (Lee, 2015) to assemble the Level 1 plasmid concluding the promoter, coding sequence, and terminator. Xyl1, Xyl2, and Xyl3 are under the control of promoters pTDH3, pPGK1, and pTEF2 respectively which have a high and stable transcription efficiency (Apel, et. al, 2016).Then we used PCR amplification to obtain the DNA fragment Xyl1, Xly2, Xly3 from Level1 plasmid, and two homology arm(LA and RA)from yeast genome(Fig.3B). The five fragments are transformed into the SC.L1 strain along with a pCRCT-His3 plasmid that will cut open the yeast genome at the His 3 position. The recombinant strains were identified by pcr and sequencing(Fig.3C and D), and the pCRCT plasmid was discarded using URA nutrient deficient medium. We name the strain with Xyl 1, 2, 3 inserted at His3 position SC.L2.

Figure 3: Insertion of Xyl 1, Xyl 2, Xyl 3 to introduce a xylose-utilizing metabolic pathway. By transforming CRISPR-His3 plasmid pCRCT-His3, His3 Left Arm (LA), xyl1, xyl2, xyl3, and His3 Right Arm (RA), the three genes are inserted at His3 loci (A). We expanded the homogenous arms, xyl1, xyl2, and xyl3 genes through PCR and transformed them into L1 strains for it to be assembled in the genome. We performed colony PCR on the yeast colonies to determine the existence of LA-xyl1, xyl2, and xyl3-RA (C) and verified this result through the sequencing testing (D), obtaining the L2 strain.

The recombinant strains SC.L2 ensured that S7P was sufficient for subsequent production.The next engineering is to convert S7P to 4DG efficiently. We selected the two genes from cyanobacteria N. punctiforme encoding DDGS(NpR5600) and OMT(NpR5599) for homologous recombination into SC.L2 genome. We used the strong promoters pTDH3 for DDGS and pPGK1 for OMT and constructed Level 1 plasmids. We chosed position 308 from chromosome III (Apel et. al., 2016) for genome recombinant. Using similar methods, We transformed pCRCT-308 plasmid, the DNA fragments of homologous arms, DDGS, and OMT into SC.L2. The recombinant strains were identified by PCR and sequencing(Fig.4C and D) , SC.L3 was obtained.

Figure 4: Insertion of DDGS and OMT at 308 position. By transforming CRISPR-308 plasmid pCRCT-308, LA, DDGS, OMT and RA, the two genes should be inserted at 308 position (A). We expanded the homogenous arms, DDGS and OMT genes through PCR and transformed them into L2 strains for it to be assembled in the genome. We performed colony PCR on the yeast colonies to determine the existence of LA-DDGS and OMT (C) and verified this result through the sequencing testing (D), obtaining the L3 strain.

To verify the previous engineering on yeast strains works, four strains(Wild Type, SC.L1, SC.L2, and SC.L3) were cultivated in four different media containing a different ratio of glucose to xylose. We found that in the medium containing only glucose(2%, 20 g/L), the growth curves of the 4 strains are roughly identical(Fig.5A), implying that our modification had no impact on the ability of cells to use glucose for growth when glucose is abundant. In the medium containing 1% glucose and 1% xylose, SC. L2 and SC.L3 containing Xyl1/2/3 showed a slight growth advantage compared with WT and SC.L1, which suggests xylose may be used as a potential carbon source for cell growth in yeast. As the concentration of glucose decreased and xylose increased further, the cell growth of all four strains is inhibited, especially SC.L3 and SC.L4(Fig. 5C and D). This result indicates most xylose is converted into S7P for MAAs production instead of being used for growth when xylose is abound and the xylose-utilizing pathway is introduced. Furthermore, the conversion of xylose into S7P requires the usage of ATP and NADPH, which might also affect growth. Therefore, we concluded that we need to supply xylose to generate S7P and maintain certain levels of glucose as the carbon source for cell growth. We chose the media containing 1% glucose and 1% xylose for later yeast fermentation.

Figure 5: Growth curves of wild type S. cerevisiae, L1, L2, and L3 under 2% glucose + 0% xylose (A), 1% glucose + 1% xylose (B), 0.4% glucose + 1.6% xylose (C), 0% glucose + 2% xylose (D). WT represents wild type CEN.PK2 strain. L1 represents S. cerevisiae with TAL1 gene removed. L2 represents strains with Xyl 1, Xyl 2, Xyl 3 inserted into L1. L3 represents L2 strains with DDGS-OMT inserted.

Production and Optimization of Shinorine and Porphyra-334

Production

After S7P is converted to 4DG by DDGS and OMT, we set producing shinorine and porphyra-334 as our primary goal. These two substances are produced by ATP-grasp ligase (AGL) and D-Ala-D-Ala ligase (ALAL) by two enzymatic steps. First, 4DG is converted to mycosporine-glycine(MG) by conjugating glycine to 4DG under the action of AGL. And then, another amino acid is attached to MG by AGL to produce shinorine or porphyra-334, L-serine for shinorine and L-threonine for porphyra-334.

Due to the existence of multiple different types of AGL and ALAL with different efficiency and amino acid preference in nature, we selected ligases from three different marine organisms: Nostoc punctiform(Np5598 and Np5597), Nostoc linckia(NlmysC and NImysD) and Actinosynnema mirum(Am4257 and Am4256), and expected to create nine combinations of AGL-AlaL. We used the promoter pTDH3 for AGL and pPGK1 for AGL. We used Lee's yeast toolkit to produce Level1 plasmids containing only one gene, and used Golden Gate assembly on the basis of Level1 to construct Level2 plasmid containing both. Finally, we transformed nine Level2 plasmids containing AGL and AlaL into SCL3，respectively, yielding SC.L5 series.

Figure 6: Different combinations of AGL-ALAL genes found from different MAA-producing marine organisms. We used the strongest yeast constitutive promoter pTDH3 to express all AG-L genes, and the strong promoter pPGK1 to express all ALA-L genes, then inserted the 9 different combinations into 2μ plasmid vectors and transformed the plasmids into L3 to obtain L5 strain.

We cultivated the L5 yeast using a SC-Ura culture medium with 1% glucose and 1% xylose and tested the absorption spectrum of the supernatant of the fermentation broth. Other than the Am4257-Am4256 combination yeast which failed to grow, there is an obvious absorption peak of 334 nm for the other 8 combinations. We found that the absorption peak of AGL Np5598 series was significantly higher than that of NlmysC and Am4257. In ALAL series, NlmysD has the highest absorption peak, followed by Am4256 and Np5597. We selected the 6 samples with higher peak and lysed them to preform OD scanning on the lysate. The scanning results after lysis further performed that Np5598 is the most efficient AGL and NlmysD is the most efficient ALAL. We think we have found an optimal combination of these two enzymes and have successfully produced MAAs. However, the lysis method we used was not completely effective, which resulted in unstable yield per lysis. We use the supernatant as a preliminary yield assessment in subsequent experiments.

Figure 7: Absorption spectrum of the AGL-ALAL combinations of L5 strains that produces shinorine or porphyra-334. We scanned the OD of broth supernatant after 72 hours of fermentation of 8 groups of yeast (except for Am4257-Am4256 which failed to grow), which shows a clear absorption peak at 334nm (A). We compared of OD334 values of the samples, discovering that Np5598 seems to be the most efficient AGL, while NlmysD being the most efficient ALAL. We conducted the same experiment with the yeast lysate of the 6 most efficient combinations and found a even more significant absorption peak (C). The OD334 value of the lysate supernatant affirms our previous conclusion that Np5598 is the best AGL and NlmysD the best ALAL (D).

Moreover, because AlaL has a preference for different amino acids to produce shinorine and porphyra-334, we need to further confirm the type of MAA in the supernatant. To do so, we used HPLC and MS technology. Due to the lack of standard samples of these MAAs in the market, we extracted MAAs from nori samples using methods we learnt through our human practice activities and used the extractives as standard. We found that the metabolite of Np5598-NlmysD mainly has the absorption spectrum of porphyra-334 according to HPLC, and the resthe ult of MS also proved that mainly porphyra-334 exist in the metabolite (m/q = 347). This shows that NlmysD has a strong selective preference toward the amino acid Threonine, and thus will mainly produce porphyra-334 if both Threonine and Serine are present in the environment. This is the first successful case of producing mainly 334 only. Np5597, on the other hand, shows shinorine's absorption peak, meaning it has preference toward serine. Therefore, we decided to use Np5598-NlmysD for porphyra-334 production and Np5598-Np5597 for shinorine production.

Figure 8: High Performance Liquid Chromatography (HPLC) and Mass Spectrometry (MS) test of Np5598-NlmysD and Np5598-Np5597 compared with nori samples. Shinorine and Porphyra-334 lack a standard on the market, thus we decided to extract pure MAA from nori (Porphyra spp.) to use as standard. HPLC results (A) and MS results (B) show a peak in shinorine and porphyra-334, which proves that there is high concentration in nori extractives, making it a reliable standard. In Np5598-NlmysD’s fermentation broth, HPLC results (C) and MS results (D) show that mostly porphyra-334 exists. However, in Np5598-Np5597’s liquid, HPLC (E) and MS (F) results show mostly shinorine.

Optimization

In order to increase MAA production, we need to further optimize the SC.L3 strains. Nqm1 has similar functions as TAL1 in shunting S7P into glycolytic pathway. To increase the S7P pool futher, we decided to remove this gene and simultaneously insert an extra copy of DDGS-OMT. It's shown that gene expression can be enhanced by using multiple promoters for increasing maas production (Yang et. al., 2018). We used pTDH3 to express OMT and pPGK1 to express DDGS, making the total transcription rate of the two copie roughly equal. We inserted DNA fragments of LA, OMT, DDGS, RA and the pCRCT-Nqm1 plasmid into SC.L3, and after PCR, DNA sequencing, selection of recombinant colonies, we removed the pCRCT-Nqm1 plasmid, obtaining SC.L6.

Figure 9: Shinorine and porphyra-334 production after optimization. We transformed porphyra-334 producing plasmid Np5598-NlmysD and shinorine producing plasmid Np5598-Np5597 into the L3 and L6 strains (A) and compared the absorption spectrum after 72 hours of fermentation. The absorption peak at 334nm of L6 strains displayed significant improvement compared to L3 strains (B) . From OD334, we concluded that in comparison with the L3 assembly, porphyra-334 production in L6 yeast increased by 91.8%, and shinorine production increased by 70.9% (C).

To test the result of the optimization, we transformed the Level2 plasmid Np5598-Np5597 and Np5598-NlmysD into L3 or L6 and named the new strains SC.L5 series and SC.L7 series. After fermentation for 72 hours, we tested the OD absorption of broth's supernatant from the yeast before and after optimization (i.e., L5 and L7 respectively). We found that there is a significant increase in the production of MAA. For porphyra-334, output increased by 91.8% in L7-Np5598-NlmysD compared to L5-Np5598-NlmysD, while for shiorine L7-Np5598-Np5597 increased by 70.9% compared to L5-Np5598-Np5597.

Figure 10: Shinorine and porphyra-334 production after optimization. We transformed porphyra-334 producing plasmid Np5598-NlmysD and shinorine producing plasmid Np5598-Np5597 into the L3 and L6 strains (A) and compared the absorption spectrum after 72 hours of fermentation. The absorption peak at 334nm of L6 strains displayed significant improvement compared to L3 strains (B) . From OD334, we concluded that in comparison with the L3 assembly, porphyra-334 production in L6 yeast increased by 91.8%, and shinorine production increased by 70.9% (C).

Considering the instability and lower efficiency of using plasmid expresssion, we decided to insert Np5598-NlmysD and Np5598-Np5597, the most efficient combinations to produce porphyra-334 and shinorine respectively (Figure 9 & 10) into SC.L6's genome at chromosome I, position 106. We named the new strains SC.L8 series. After fermentation for 72 hours in YPD medium, we compared the OD 334 absorption of the broth's supernatant between SC.L7 series and SC.L8 series. We found that the OD value of L8 series(for both Np5598-NlmysD and Np5598-Np5597) with genome recombinant, showed a steady increase of approximately 20% compared with that of L7 series with plasmid expression. Finally, the nori extract with a higher purity of shinorine and porphyra-334 is used as the standard sample to obtain rough yield data of SC.L8 series: the shinorine’s yield reached 258.5mg/L in L8-Np5598-Np5597, the porphyra-334’s yield reached 270.7mg/L in L8-Np5598-NlmysD.

Figure11:Genome insertion of Np5598-NlmysD and Np5598-Np5597. To further increase and stabilize Shinorine and Porphyra-334 production, we inserted the genes Np5598-NlmysD and Np5598-Np5597 into the yeast’s genome at position 106 of chromosome I (Amanda R. et.al. 2017). After OD scanning, we found that the absorption peak of after genome insertion is higher than plasmid vector (A). We compared the OD334 value of plasmid transformation and genome insertion and found that there is about 20% increase in genome insertion expression.

These results reveal that we were able to increase the production of shinorine and porphyra-334 to a great extent by introducing another copy of DDGS-OMT at position Nqm1 and inserting the genes into S. cerevisiae's genome.

Production of Palythine and Gadusol

Production of palythine

After obtaining shinorine and porphyra-334, we could produce the MAA palythine by removing a carboxyl group from shinorine. Thus, we added pTEF2-NlmysH-tSSA1 to the Np5598-Np5597 combination to obtain the genetic circuit for producing palythine . We constructed the plasmid and transformed it into SC.L3 or SC.L6, obtaining L3:Np5598-Np5597-NlmysH and L6: Np5598-Np5597-NlmysH. Again, we fermented the two strains for 72 hours in SC-Ura culture medium with 1% glucose and 1% xylose. The absorption spectrum of the supernatant broth was tested, and results show that there is an obvious absorption peak at 320 nm. We also compared the production in L3:Np5598-Np5597-NlmysH and L6:Np5598-Np5597-NlmysH using OD 320 value, which shows that L6 strains are much more productive than L3 strains. The OD 320 value of L6 is 2.62 times of L3 strains, whereas L3 strains barely had any increase in UV absorption at 320 nm. This shows that we have achieved palythine production, and also shows that our previous optimization of L3 is successful.

Figure 12: Palythine production in L9 and L5 strains. We transferred palythine plasmid Np5598-Np5597-NlmysH into the L3 and L6 strains (A). After 72 hours of fermentation, OD scanning results show that an absorption peak at was clear, but only in L9 strains (C). OD 320 value shows that L6 strains were much more effective in absorbing UV at 320 nm compared to L5 strains, and the value of OD320 of L9 is 2.62 times the control, justifying the production and optimization of palythine.

Production of gadusol

Gadusol is a MAA-like molecule that is capable of absorbing UV radiation mostly in the form of UVB. To produce gadusol, we chose the genes EEVS and MTOX from Danio rerio, which converts 4DG into gadusol. We used promoters pTDH3 to express EEVS and pPGK1 to express MTOX and inserted these genes into L2 yeast at position 308 to obtain L4 strain. After testing the obtaining the absorption spectrum of the supernatant broth after 72 hours of fermentation, a slight absorption peak was observed at around 290 nm. To better observe the absorption spectrum to better determine the existance of the gadusol, we subtracted the curve of the negative control from L4's absorption curve (Figure 15B). The relative OD curve of L4 strain shows an obvious absorption peak at 290 nm, which suggests the production of gadusol.

Figure 13: Insertion of EEVS-OMT in order to produce MAA-like molecule gadusol. By transforming CRISPR-308 plasmid pCRCT-308, LA, EEVS, MTOx, and RA, EEVS should be inserted at 308 position after assembly in S. cerevisiae (A). We expanded the homogenous arms, and EEVS, MTOX genes through PCR and transformed them into L3. We performed colony PCR on the yeast colonies to determine the existence of LA-EEVS and MTOX (C) and verified this result through the sequencing testing (D), obtaining the L4 strain.

Figure 14: Gadusol production. Fermenting the L4 strain, using the L2 strain as a comparison. After 72 hours of culturing, the absorption curve became clear, and it can be seen that L4 has a peak at 290nm (A). We compared L4’s values to the control, obtaining a clear absorption peak for gadusol.

Collections of novel sunscreen

After producing all planned UV-absorbing molecules - shinorine, porphyra-334, palythine, and gadusol, we compared the production and capabilities of our molecules against UV radiation. We concluded the absorption curves of the molecules expressed on plasmid vectors and compared our absorption curve (Figure 16.B) with the absorption curve from researches (Figure 16.A). We found that the absorption curve of all molecules had the same shape and location of peak compared to results from papers. Moreover, our MAAs also have a much higher absorbance value than Figure 16.A.

Figure 15: Comparison of MAA production. Through reading documents, we discovered the molecules gadusol, palythine, shinorine, and porphyra-334, which are able to absorb UV light within a range of 275 to 360 nm, absorbing UVB and the majority of UVA (A). After the fermentation of our yeast strains, it can be seen there are significant absorption peaks from 280nm to 360nm, perfectly conforming to our designs.

This year, LINKS­_China successfully produced shinorine, porphyra-334, palythine, and gadusol at an efficient rate. We hope that these MAAs we produce could be implemented in sunscreens to better protect our environment and our skin. For more information, please see Proposed Implementation!

Table 1

Sunburn Repair

Considering the fact that not all UV radiation could be absorbed by MAAs and could still result in increased oxidative stress, we decided to break down ROS (Reactive Oxygen Species). Therefore, we decided to produce human Superoxide Dismutase 1 (hSOD1) and human catalase (hCatalase). hSOD1 possesses the ability to convert superoxide (O2-), the main form of ROS, into hydrogen peroxide. However, hydrogen peroxide is also harmful to our body, and catalase provides a perfect solution to this problem as it could break down hydrogen peroxide into water.

Thence, we decided to form a fusion protein, hSOD-linker-hCatalase (SHC) (Figure 16.A, B, C), in order to enhance the efficiency of the breakdown of ROS. We have successfully constructed the fusion protein by linking genes expressing the separate enzymes with a flexible linker and expressing them in E.Coli BL21. Successful production of hSOD1, hCatalase and SHC are achieved in concentrations of 270mg/L, 240mg/L and 400mg/L respectively. Furthermore, we discovered that the three proteins all possess high solubility (Figure 16.D), which suggests high efficiency to extract these proteins.

Figure 16: Design and expression of hSOD, hCatalase, and fusion protein hSOD-flexible linker-hCatalase (SHC). We use promoter pT7 and terminator pET28a to express hSOD, hCatalase and SHC and transformed these plasmids into E. coli (A). After we synthesize SOD and catalase vectors, we used PCR to amplify the plasmid fragments (B). We created SHC using Gibson assembly, and through colony PCR and sequencing, determined that construction was successful (C). We induced the expression of SHC, hSOD, and hCatalase and obtained purified protein samples.

Under the same conditions, we set up assessments for hSOD, hCatalase and fusion protein hSOD-linker-hCAT. Quantitatively, our results showed that separate hSOD and hCatalase had activities of 3.00U/mg and 128.85U/g, respectively. In comparison, hSOD1 and hCAT in our fusion protein SHC produced activity levels of 8.04U/mg and 313.04U/g (Figure 17 & 18). Thence, our results proved that both proteins had enhanced activity when expressed with the linker connection, thereby proving that the fusion protein has improved performance.

Figure 17：Effects of hSOD, catalase, and SHC fusion protein at removing ROS. In order to test the enzyme activity of hSOD, catalase and SHC in converting superoxide (O2-), we tested WST-8 formazan concentrations, which would be decreased if hSOD is present (A). The WST-8 operating fluid was tested after incubation for 30 minutes, and the color was recorded (B). A lighter color represents lower WST-8 formazan concentration. The value of WST-8 formazan was found and summarized into a bar graph, with SHC being lowest, indicating it was most efficient in removing ROS.

Figure 18： Effects of hSOD, hCatalase, and SHC fusion protein in removing H2O2. In order to test the enzyme activity of hSOD, catalase and SHC in converting hydrogen peroxide into water and hydrogen, we tested H2O2 concentrations. If catalase activity, peroxidase activity decreases, thus showing a less red color. The samples were tested after incubation for 30 minutes, and the color was recorded (B). A lighter color represents higher enzyme activity. The standard curve of H2O2 concentration to absorption was found (C). Using the standard curve, we calculated the remaining levels of H2O2 in the sample after catalase and SHC were added (D). SHC was shown to have greater enzyme activity.

Xantine Oxidase can catalyze the production of ROS by Xanthine (Figure 19.A), and by adding our fusion protein SHC into this system and reacting for 60 minutes, we discovered that the ROS and H2O2 produced by the reaction are all degraded (Figure 19.B). We discovered that SHC has enhanced activity to eliminate hydrogen peroxide compared to the single enzyme . By calculation, fusion protein SHC enhanced SOD activity by 168% and catalase activity by 143% compared with single protein. This confirmed our engineering hypothesis as the efficacy of the fusion protein is higher than the two enzymes working separately.

Figure 19： ROS produced via the oxidation of Xanthine breakdown by hSOD1, hCatalase and SHC. SOD converts the ROS into Hydrogen Peroxide, whereby hCatalase then breaks it down completely. SHC, possessing functions of both enzymes, is able to complete the whole chain of reaction (A). After 60 minutes of reaction, and the color was recorded (B). The hSOD1 group has little amount of H2O2 present, while the hCatalase and the SHC groups finished the H2O2 degradation completely (C).