- Original article
- Open Access
Strain and process development for poly(3HB-co-3HP) fermentation by engineered Shimwellia blattae from glycerol
© Sato et al.; licensee Springer. 2015
Received: 29 January 2015
Accepted: 17 February 2015
Published: 4 March 2015
Poly(3-hydroxybytyrate-co-3-hydroxypropionate), poly(3HB-co-3HP), is a possible alternative to synthetic polymers such as polypropylene, polystyrene and polyethylene due to its low crystallinity and fragility. We already reported that recombinant strains of Shimwellia blattae expressing 1,3-propanediol dehydrogenase DhaT as well as aldehyde dehydrogenase AldD of Pseudomonas putida KT2442, propionate-CoA transferase Pct of Clostridium propionicum X2 and PHA synthase PhaC1 of Ralstonia eutropha H16 are able to accumulate up to 14.5% (wtPHA/wtCDW) of poly(3-hydroxypropionate), poly(3HP), homopolymer from glycerol as a sole carbon source (Appl Microbiol Biotechnol 98:7409-7422, 2014a). However, the cell density was rather low. In this study, we optimized the medium aiming at a more efficient PHA synthesis, and we engineered a S. blattae strain accumulating poly(3HB-co-3HP) with varying contents of the constituent 3-hydroxypropionate (3HP) depending on the cultivation conditions. Consequently, 7.12, 0.77 and 0.32 gPHA/L of poly(3HB-co-3HP) containing 2.1, 8.3 and 18.1 mol% 3HP under anaerobic/aerobic (the first 24 hours under anaerobic condition, thereafter, aerobic condition), low aeration/agitation (the minimum stirring rate required in medium mixing and small amount of aeration) and anaerobic conditions (the minimum stirring rate required in medium mixing without aeration), respectively, were synthesized from glycerol by the genetically modified S. blattae ATCC33430 strains in optimized culture medium.
Polyhydroxyalkanoates (PHA) are polyesters synthesized by a wide range of microorganisms (Anderson et al., 1990). Most of PHA are produced from renewable resources like sugars, plant oils, glycerol, and carbon dioxide (CO2). As these polyesters are biodegradable, they have been expected to play an important role in environmental protection and in reduction of CO2 emissions, a cause of global warming (Steinbüchel and Füchtenbusch, 1998). There have been many attempts to investigate industrial production of such polymers to ascertain if they are environmently friendly or biocompatible materials (Lee, 1996; Steinbüchel, 2001). In nature, poly(3-hydroxybutyrate), poly(3HB), a homopolymer of (R)-3-hydroxybutyric acid (3HB), is the most abundant PHA. However, because poly(3HB) is highly crystalline, hard and brittle, its practical applications are limited. Many studies have been undertaken to improve these properties. For example, among other PHA, poly(3-hydroxybutyrate-co-3-hydroxyvalerate), poly(3HB-co-3HV), poly(3-hydroxybutyrate-co-3-hydroxyhexanoate), poly(3HB-co-3HH), and poly(3-hydroxybutyrate-co-3-hydroxypropionate), poly(3HB-co-3HP) are much more flexible and less crystalline than poly(3HB) (Andreeßen et al., 2014b; Chen et al., 2000; Doi et al., 1995; Shimamura et al., 1993; Shimamura et al., 1994). The flexibility depends on the ratio of the constituents in the copolymer. Therefore, these copolymers are accordingly expected to have a broader range of applications in packaging, agriculture and medical materials (Chen et al., 2000). Among these copolymers, poly(3HB-co-3HP) is considered to be very promising due to its benefiting material properties (Andreeßen and Steinbüchel, 2010).
The global glycerol production has increased rapidly during the last decade due to the increase of biodiesel production. Concomitant with the conversion of about 10 million tons of vegetable oil into biofuel, about 1 million tons of glycerol were produced as a by-product in 2011 (Quispe et al. 2013). Therefore, the aim of this study was the development of strains for poly(3HB-co-3HP) synthesis from glycerol as sole carbon source.
Some processes for synthesis of poly(3HB-co-3HP) have already been reported by Shimamura et al., 1994, Fukui et al., 2009, Wang and Inoue, 2001 and Wang et al., 2013. However, in these studies the use of expensive 3HP as precursor of 3HP-CoA (Shimamura et al., 1994; Wang and Inoue, 2001), insufficient 3HP contents to reduce the crystallinity (Fukui et al., 2009) and the requirement of high cost vitamin B12 are major drawbacks (Wang and Inoue, 2001; Wang et al., 2013).
Vitamin B12 is a cofactor of the glycerol dehydratase (Martens et al., 2002), which converts glycerol to 3-hyrdoxypropionaldehyde (3HPA), a precursor of 3HP-CoA (Wang et al., 2013), to produce 1,3-propanediol (1,3PD). However, only few bacteria are capable of synthesizing vitamin B12 (Sun et al., 2003). To solve this problem, we used the enteric bacterium Shimwellia blattae ATCC33430 (Burgess et al., 1973; Priest and Barker, 2010) which cannot naturally produce PHA but synthesizes vitamin B12 (Andres et al., 2004) and converts glycerol to 1,3PD.
However, the residual cell density was less than 6 g/L and therefore too low to produce much poly(3HB-co-3HP). Since PHA are accumulated inside the cells, low residual cell density result in only low PHA productivity. For example, even if 90 % (wtPHA/wtCDW) of poly(3HB-co-3HP) is accumulated in a cell, less than 54 g/L of polymer is produced under such conditions.
Therefore, an optimized culture medium was needed to overcome this problem. In this study, we report on a new strategy for synthesis of poly(3HB-co-3HP) using optimized cultivation medium and glycerol in genetically modified S. blattae without the addition of vitaminB12 and 3HP into the culture.
Materials and methods
Strain and plasmid
Bacterial strains and plasmids used in this study
Strains and plasmids
Origin or reference
F - mcrA Δ(mrr-hsdRMS-mcrBC) φ80lacZΔM15 ΔlacX74 mupG recA1 araD139 Δ(ara-leu)7697 galE15 galK16 rpsL(StrR) endA1λ
Life technologies (Darmstadt, D)
Wild type strain
pBBR1MCS-2 ::plac::aldD::dhaT:: pct::plac::phaC1AB in S. blattae ATCC33430
Cloning vector, Kmr
Kovach et al., 1995
Kmr; aldD Pp ; dhaT Pp ; pct Cp
Heinrich et al., 2013
Kmr; phaC1 Re ; phaA Re ; phaB1 Re
pBBR1MCS-2 ::plac::aldD::dhaT::pct ::plac::phaC1AB
Kmr; aldD Pp ; dhaT Pp ; pct Cp ; phaC1 Re ; phaA Re ; phaB1 Re
Growth of cells
250-mL Erlenmeyer flasks containing 50 mL MMB medium [3.56 g/L Na2PO4 • 2 H2O, 0.68 g/L KH2PO4, 0.63 g/L (NH4)2SO4, 2.47 g/L MgSO4 • 7 H2O, 1.0% (vol/vol) trace element solution (0.1 N HCl in 4.2 g/L FeSO4 • 7 H2O, 5.0 g/L CaCl2 • 2H2O, 2.4 g/L CoCl2 • 6 H2O, 0.58 g/L CuCl2 • 2 H2O, 2 mg/L NiCl2 • 6 H2O, 3 mg/L MnCl2 • 4 H2O, 0.03 g/L H3BO3, 4.3 g/L ZnSO4 • 7 H2O, 3 mg/L NaMoO4 • 2 H2O)] with 300 mM of glycerol was used for optimization of culture medium. Cells were cultivated in 250-mL Erlenmeyer flasks at an agitation of 125 rpm and at 30°C. High cell density fed-batch cultivation of S. blattae were conducted in a 2 L jar fermenter (Biostat B plus, Sartorius AG, Göttingen, Germany) containing 1.5 L of basal medium (BM) (Andreeßen et al. 2014a,b) or MMB medium with 300 mM of glycerol as carbon source.
Glycerol was intermittently added to the culture medium to maintain a concentration between 50 and 300 mM. 500-mL flasks containing 100 mL BM or MMB medium, 300 mM of glycerol and 50 μg/L of kanamycin were used for seed cultivations. Dissolved oxygen was monitored and pH was controlled in the range of 6.8 – 6.9 by using a 7.5% aqueous solution of ammonium hydroxide.
Plasmid construction and transfer into E. coli and S. blattae
All processing and manipulation of DNA was carried out as described by Sambrook et al., 1989. Plasmid pBHR68 (Spiekermann et al., 1999) was digested with Bsp119I and EcoRI to generate a 4.2-kbp fragment comprising the coding regions of phaC1, phaA and phaB1. This fragment was ligated to the ClaI and EcoRI restriction fragment of pBBR1MCS-2 (Kovach et al., 1995) to generate pBBR1MCS-2::p lac ::phaC1AB. Then, pBBR1MCS-2::p lac ::phaC1AB was digested with SspI to generate a 4.7-kbp expression cassette of the phaC1, phaA and phaB1 under control of the lac promoter and ligated with the EcoICRI linearized fragment of pBBR1MCS-2::aldD::dhaT::pct (Heinrich et al., 2013) to generate the expression vector pBBR1MCS-2::p lac ::aldD::dhaT::pct::p lac ::phaC1AB. In addition, S. blattae ATCC33430 was transformed with pBBR1MCS-2::p lac ::aldD::dhaT::pct::p lac ::phaC1AB to generate Sb6BP by electroporation as previously described (Heinrich et al., 2013).
Optimization of cultivation medium
When optimizing the medium, we thought yeast extract is not necessary, because cultivations in complete synthetic medium have been made for bacteria such as Klebsiella pneumonia (Brandl et al., 1998), E. coli (Enayati et al., 1999) or R. eutropha (Sato et al., 2013). Therefore, several different concentrations of yeast extract were tested as described below.
250-mL Erlenmeyer flasks containing 50 mL MMB medium with 0, 0.2 or 2.0 (g/L) of yeast extract, respectively were used to cultivate S. blattae ATCC33430. The optical density at 600 nm and the pH were measured in samples withdrawn from the culture. In order to decide which yeast extract concentration is favorable for high cell density cultivation, 2 L bioreactors containing 1.5 L of MMB medium with 300 mM of glycerol and 0.2, 0.67 or 6.7 g/L of yeast extract and Sb6BP were used. Cell densities (gCDW/L) and polymer contents (% wtPHA/wtCDW) were measured.
Synthesis and purification of poly(3HB-co-3HP)
PHA was synthesized in a 2 L bioreactors containing 1.5 L of BM or MMB medium for 72 or 48 h. Glycerol was used as sole carbon source. Generally, enteric bacteria also S. blattae synthesize 1,3PD only under anaerobic condition. Thus, 4 different cultivation conditions (aerobic, anaerobic, low aeration/agitation and two-step) were conducted to optimize poly(3HB-co-3HP) synthesize condition in recombinant S. blattae (SB6P).
The operating conditions were as follows: Aerobic condition means an agitation at 800 rpm and an aeration rate of 2.0 L/min. Anaerobic conditions were maintained at an agitation of 150 rpm without any aeration whereas low aeration/agitation conditions were provided at a stirring rate of 150 rpm and an aeration rate of 0.4 L/min. 150 rpm was the minimum stirring rate required in medium mixing. The two-step fermentation (the first 24 hours under anaerobic condition, thereafter, aerobic condition) was performed according to Heinrich et al., 2013.
Cell harvest and extraction of poly(3HB-co-3HP)
After separating the cells from the culture broth, cells were frozen at −30°C and freeze dried. Poly(3HB-co-3HP) or poly(3HB) was isolated from the pulverized dry cell matter by digestion of non-PHA biomass employing a 13% (vol/vol) sodium hypochlorite solution (Heinrich et al., 2013, Heinrich et al., 2012).
Determination of poly(3HB-co-3HP)
Determination of glycerol and 1,3PD
Concentrations of glycerol and 1,3PD in the media were monitored by HPLC analysis. For this, supernatants were assayed using a Lachrom Elite HPLC-System (VWR-Hitachi, Darmstadt, D) chromatograph with a RI-detector (Type 2490 VWR, Darmstadt, D) and a Metacarb 67H-column (300 × 6.5 mM, VWR-Varian, Darmstadt, D) at 75°C and at a flow rate of 0.8 ml/min for 20 min. The mobile phase was 4.5 mM sulfuric acid.
Synthesis of poly(3HB-co-3HP) influenced by cultivation conditions
In order to develop a process for poly(3HB-co-3HP) production by a newly engineered Sb6BP strain, cultivation was conducted under four different conditions (aerobic, two-step, low aeration/agitation and aerobic conditions). (i) Aerobic condition occurred at high aeration and agitation, (ii) the two-step condition occurred during the first 24 hours under anaerobic condition and thereafter under aerobic condition, (iii) for low aeration/agitation condition a minimum stirring rate was applied together with low rate of aeration and (iv) for anaerobic condition was a minimum stirring rate was applied without aeration.
The amount of 1,3PD that was converted into 3-hydroxypropionyl-CoA and polymerized into poly(3HB-co-3HP) was too small to affect the 1,3PD concentration of the culture medium in these studies. We already confirmed that 1,3PD supplemented to the culture medium was converted to 3-hydroxypropiony-CoA which is polymerized into poly(3HB-co-3HP) in the recombinant strain in which dhaT was heterologously expressed. However, efficiency was very low (data not shown). Therefore, most of the 3HP monomer in the accumulated polymer was provided directly from 3-hydroxypropionaldehyde via 3-hydroxypropionate and 3-hydroxyproionyl-CoA by AldD and Pct, respectively.
Results of fed-batch cultivation using Sb 6BP and glycerol as sole carbon source
Cell density (g CDW /L)
PHA content (wt%)
PHA (g PHA /L)
Monomer composition (mol%)
Cultivation time (h)
PHB(P) productivity (mg PHA /L/h)
The time courses of polymer synthesis for each cultivation condition in BM medium were as follows (Figure 3): (1) Anaerobic: cell growth and addition of ammonium hydroxide almost stopped after 48 h cultivation time. The highest 3HP composition (20.2 mol%), 1,3PD concentration (242 mM) and polymer production was recorded after about 40 h cultivation time. These data indicate that 3HP-CoA and 1,3PD synthesis occurred only during exponential cell growth. Moreover, it was indicated that both, (R)-3HB-CoA and 3HP-CoA are not supplied after the stop of cell growth, because the 3HP content was very stable after 40 h. (2) Low aeration/agitation: the time courses of every parameter except 3HP monomer fraction were very similar when compared to anaerobic conditions as explained above. The highest molar 3HP monomer fraction was recorded earlier than 12 hour of culture time. The residual cell mass was only marginally influenced by aeration, but the 3HP monomer content of the polyester was decreased to less than 50% in comparison to anaerobic condition. (3) Two-step: Interestingly, the highest molar 3HP fraction in the copolymer was recorded at the time when the cultivation conditions were just switched. After that, the fraction of 3HP moieties rapidly dropped but the cell dry weight (CDW) increased on the other hand. Formation of 1,3PD was maintained for some hours after the cultivation condition was changed from anaerobic to aerobic and then stopped. (4) Aerobic: only the poly(3HB) homopolymer was synthesized under aerobic conditions. Furthermore, the cell density (12.6 gCDW/L) and the PHA productivity (96.6 mgPHA/L/h) were the highest. Only a small amount of 1,3PD (10 to 15 mM) was synthesized after 24 h of cultivation, and the 3HP monomer was not detected by GC analysis at any period.
GPC analysis of the isolated poly(3HB-co-3HP) obtained in BM after two-step cultivation for 72 h revealed an average molecular weight of 765,293 Da with a polydispersity index (Mw/Mn) of 2.49.
Optimization of the medium for cultivation
Although cells of strain Sb6BP could be successfully cultivated, poly(3HB-co-3HP) productivity was still low due to a low residual cell mass. The cell density was only 12.6 gCDW/L under aerobic condition in BM medium. From these results it was suspected that some substances required for cell growth were missing or that at least a severe shortage had occurred in BM medium. Therefore, the medium was optimized.
Cultivation of Sb 6BP in MMB containing various concentrations of yeast extract
Yeast extract (g/L)
Cell density (g CDW /L)
PHA (g PHA /L)
PHA content (wt%)
Cultivation time (h)
With regard to the cost, we chose of 0.67 g/L to obtain 27.3 gCDW/L.
Synthesis of poly(3HB-co-3HP) in MMB medium
Improved productivities for PHA synthesis were between 1.9 and 5.8 times higher in MMB than in BM; the highest poly(3HB-co-3HP) productivity was obtained in two-step cultivation (25 mgPHA/L/h in BM medium in comparison to 148 mgPHA/L/h in MMB) (Table 2). The positive effect of MMB medium was highest in two-step cultivation experiments. This is explained by the fact that cell growth was very high after the culture conditions were changed (Figure 4).
Conversely, these effects were less under anaerobic and low aeration/agitation conditions. An explanation is most probably because the rate-limiting factor was oxygen and not one of the compounds included in yeast extract. These observations could not be confirmed in MMB under aerobic condition as there was no poly(3HB-co-3HP) accumulated. The polymer content and the 3HP fraction in the copolyester were not so much influenced under anaerobic and low aeration/agitation conditions whereas the 3HP fraction in two-step condition dropped rapidly from 8.6 to 2.1 mol% after the cultivation conditions were changed (Figure 4). These results indicate that the decrease of 3HP fraction might be due to a relative decrease of the monomer composition by additional accumulation of 3HB and/or poly(3HB), because, after switching the conditions, cell growth started again and 3HB-CoA provision via acetoacetyl-CoA was started as well. In addition, it was confirmed that the net 3HP amount increased until 30 h; thereafter no increase occurred in case of two-step cultivation when using the MMB medium. Therefore, there is a possibility that the resulting polymer was likely a blend of poly(3HB) and poly(3HB-co-3HP).
Poly(3HB-co-3HP) with the highest 3HP fraction (18.1 mol%) was obtained during anaerobic condition; however, the polymer productivity and cell density were only 6.6 mgPHA/L/h and 1.84 gCDW/L, respectively.
In this study we engineered a recombinant strain of S. blattae ATCC33430 (Sb6BP), which is able to synthesize poly(3HB) and poly(3HB-co-3HP). However, Sb6BP synthesized the copolymer only under oxygen limiting conditions because the cells produced only small amounts of 1,3-propanediol (1,3PD) as a precursor of 3-hydroxypropionyl-CoA (3HP-CoA) under aerobic condition. In any case, in comparison with the 1,3PD productivity under oxygen limiting conditions, a lower productivity of 1,3PD under aerobic condition causes non-accumulation of poly(3HB-co-3HP).
However, successful production of poly(3HB-co-3HP) in recombinant S. blattae was achieved, 3HP composition was rather low. The glass transition temperature of poly(3HB-co-3HP) decreases rapidly from −3°C to −15°C, and the melting temperature (Tm) decreases from 163°C to 73°C as the 3HP fraction in the copolymer increased from 25.6 to 36.3 mol% (Wang et al., 2013). In particular, the poly(3HB-co-3HP) with a 3HP content exceeding 30 mol% is therefore much more flexible and less crystalline and is expected to approach that of conventional plastics such as polypropylene, polystyrene, and polyethylene. The low 3HP fraction indicates that the strain cannot actively import 1,3PD from culture medium or that 3HP-CoA supply via 3-hydroxypropionaldehyde and 3-hydroxypropionate is insufficient.
This is the first report for the production of poly(3HB-co-3HP) without using vitamin B12 and expensive compounds such as 3-hydroxypropionate by recombinant S. blattae. We achieved a poly(3HB-co-3HP) productivity of 148 mgPHA/L/h in this study, which is the highest so far reported (Shimamura et al., 1994; Fukui et al., 2009; Wang and Inoue, 2001; Wang et al., 2013). S. blattae is therefore one of the promising bacterial strains for poly(3HB-co-3HP) production from glycerol.
However, the reported processes still require oxygen limitation. Therefore, the polymer productivity is still very low. In addition, the polymer produced by two-step cultivation method was likely a blend of poly(3HB) and poly(3HB-co-3HP) owing to the conditional change from anaerobic to aerobic condition. The remaining challenges are to achieve efficient utilization of 3HPA or 1,3PD and the expression of the genes regulated by dha regulon in aerobic conditions for aerobic production of poly(3HB-co-3HP). Moreover, an enhancement of the metabolite flow from 3-hydroxypropionaldehyde to 3HP-CoA will be necessary to increase the 3HP fraction in the copolymer. By using the pduP gene from Salmonella enterica (Andreeßen et al., 2010) or Salmonella typhimurium (Gao et al., 2014), the provision of 3HP-CoA provision might be improved.
We thank Rolf Daniel and his laboratory at the Department of Genomic and Applied Microbiology (Georg-August University Göttingen) for providing S. blattae ATCC 33430 and Kaneka Corporation, Japan, for GPC analysis. We acknowledge support by Deutsche Forschungsgemeinschaft and Open Access Publication Fund of University of Münster.
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