Production of Chemicals by Klebsiella pneumoniae Using Bamboo Hydrolysate as Feedstock

Summary

Bamboo powder was pretreated with NaOH and enzymatically hydrolyzed. The hydrolysate of bamboo was used as the feedstock for 2,3-butanediol, R-acetoin, 2-ketogluconic acid, and xylonic acid production by Klebsiella pneumoniae.

Abstract

Bamboo is an important biomass, and bamboo hydrolysate is used by Klebsiella pneumoniae as a feedstock for chemical production. Here, bamboo powder was pretreated with NaOH and washed to a neutral pH. Cellulase was added to the pretreated bamboo powder to generate the hydrolysate, which contained 30 g/L glucose and 15 g/L xylose and was used as the carbon source to prepare a medium for chemical production. When cultured in microaerobic conditions, 12.7 g/L 2,3-butanediol was produced by wildtype K. pneumoniae. In aerobic conditions, 13.0 g/L R-acetoin was produced by the budC mutant of K. pneumoniae. A mixture of 25.5 g/L 2-ketogluconic acid and 13.6 g/L xylonic acid was produced by the budA mutant of K. pneumoniae in a two-stage, pH-controlled fermentation with high air supplementation. In the first stage of fermentation, the culture was maintained at a neutral pH; after cell growth, the fermentation proceeded to the second stage, during which the culture was allowed to become acidic.

Introduction

Klebsiella pneumoniae is a bacterium that grows well under both aerobic and anaerobic conditions. K. pneumoniae is an important industrial microorganism used to produce many chemicals. 1,3-propanediol is a valuable chemical that is mainly used as a monomer to synthesize polytrimethylene terephthalate. Polytrimethylene terephthalate is a biodegradable polyester that exhibits better properties than those of 1,2-propanediol, butanediol, or ethylene glycol¹. 1,3-propanediol is produced by K. pneumoniae using glycerol as a substrate in oxygen-limited conditions². 2,3-butanediol and its derivatives have applications in the field of plastics, solvent production, and synthetic rubber and have the potential to be used as biofuel³. With glucose as the substrate, 2,3-butanediol is the main metabolite of the wildtype strain⁴. 2,3-butanediol is synthesized from pyruvate. First, two molecules of pyruvate condense to yield α-acetolactate; this reaction is catalyzed by α-acetolactate synthase. α-acetolactate is then converted to acetoin by α-acetolactate decarboxylase. R-acetoin can be further reduced to 2,3-butanediol when catalyzed by butanediol dehydrogenase. An efficient gene replacement method suitable for K. pneumoniae has been explored, and many mutants have been constructed^5,6,7. A budC mutant, which lost its 2,3-butanediol dehydrogenase activity, accumulates high levels of acetoin in culture broth. Acetoin is used as an additive to enhance the flavor of food⁸. When budA, which encodes α-acetolactate decarboxylase, is mutated, 2-ketogluconic acid accumulates in the broth. 2-ketogluconic acid is used for the synthesis of erythorbic acid (isoascorbic acid), an antioxidant used in the food industry⁹. 2-ketogluconic acid is an intermediate of the glucose oxidation pathway; in this pathway, located in the periplasmic space, glucose is oxidized to gluconic acid and then further oxidized to 2-ketogluconic acid. Gluconic acid and 2-ketogluconic acid produced in the periplasm can be transported to the cytoplasm for further metabolism. The accumulation of 2-ketogluconic acid is dependent upon acidic conditions, and higher air supplementation favors 2-ketogluconic acid production¹⁰. Gluconate dehydrogenase, encoded by gad, catalyzes the conversion of gluconic acid to 2-ketolguconic acid. The gad mutant of K. pneumoniae produced high levels of gluconic acid instead of 2-ketogluconic acid, and this process is also dependent upon acidic conditions. Gluconic acid is a bulk organic acid and is used as an additive to increase the properties of cement¹¹. Glucose oxidation to gluconic acid is catalyzed by glucose dehydrogenase. Xylose is also a suitable substrate of glucose dehydrogenase. When xylose is used as a substrate, K. pneumoniae produces xylonic acid¹².

Chemical production using biomass as a feedstock is a hot topic in biotechnology¹³. The main components of biomass are cellulose, hemicellulose, and lignin. However, these macromolecular compounds cannot be directly catabolized by most microorganisms (including K. pneumoniae). Cellulose and hemicelluloses in the biomass must be hydrolyzed to glucose and xylose and can then be used by microorganisms. The presence of lignin in lignocelluloses creates a protective barrier that prevents biomass hydrolyzation by enzymes. Thus, a pretreatment process that removes lignin and hemicelluloses and reduces the crystallinity of cellulose is always performed during biomass utilization by microorganisms. Many pretreatment methods have been developed: acid, alkaline, ammonia, and steam pretreatments are common.

Bamboo is abundant in tropical and subtropical regions and is an important biomass resource. Here, the preparation of bamboo hydrolysate and chemical production using bamboo hydrolysate are presented

Protocol

1. Preparation of Bamboo Hydrolysate

1. Add 5 g of bamboo powder to 40 mL of an NaOH solution to achieve a 10% (g/g) final concentration in a 250 mL flask. Use a series of NaOH solutions ranging from 0.05 M to 0.50 M in increments of 0.05 M.
   1. Incubate the mixture for 60 min at 60 °C or 100 °C in a water bath. Incubate at 121 °C in an autoclave.
2. After incubation, leave the mixture to stand for 4 h at room temperature. Then, remove the supernatant. Add 100 mL of fresh water and mix.
   1. Repeat this washing 5-6 times, until the pH of the supernatant reaches 6.8. Use the obtained solid for the next step of enzymatic hydrolysis.
3. For hydrolysis, adjust 50 mL of the above mixture to pH 5.0 using 98% H₂SO₄. Then, add 0.5 mL of 200 filter paper activity (FPU)/mL cellulase.
   NOTE: The final ratio of cellulase to bamboo should be 20 FPU per 1 g of bamboo.
4. Incubate the mixture at 50 °C for 36 h in a shaker.
   NOTE: After hydrolysis, some solid will remain in the mixture.
5. Obtain a clear hydrolysate by centrifuging at 7,690 x g for 5 min.
6. Quantify the glucose, xylose, and other chemicals with a high-pressure liquid chromatograph system equipped with a refractive index detector and a photodiode array detector. Use an HPX-87H column (300 mm x 7.8 mm) and a mobile phase of 5 mM H₂SO₄ solution at a 0.8 mL/min flow rate¹².
7. For a large volume of hydrolysate preparation, mix 2 kg of bamboo powder and 18 L of 0.25 M NaOH in a 30-L stainless-steel tank.
   1. Incubate the tank at 121 °C in an autoclave for 60 min. After incubation, wash the mixture with 40 L of water in a 60 L plastic tank. Repeat this washing 5 times.
   2. Use water to adjust the total washed bamboo to a volume of 20 L. Adjust the pH of the mixture to 5.0 using 98% H₂SO₄.
   3. Enzymatically hydrolyze the mixture in a modified shaking water bath, equipped with a mechanical agitator to ensure that the mixture is well distributed. Add 200 mL of 200 FPU/mL cellulase and incubate the mixture at 50 °C for 36 h.
   4. After hydrolysis, centrifuge the mixture at 4,700 x g for 10 min.

2. 2,3-Butanediol Production by Wildtype K. pneumoniae

1. Use 3 L of bamboo hydrolysate as the solvent for medium preparation.
2. Prepare a fermentation medium containing 4 g/L corn steep liquor, 2 g/L (NH₄)₂SO₄, 6 g/L K₂HPO₄, 3 g/L KH₂PO₄, and 0.2 g/L MgSO₄. Adjust the pH of the medium to neutral using 2.5 M NaOH. Use a 5-L bioreactor containing 3 L of autoclaved fermentation medium for fermentation.
3. Use K. pneumoniae cells stored in a -80 °C low-temperature refrigerator.
4. For the seed culture, incubate a 250 mL flask containing 50 mL of Luria-Bertani (LB) medium overnight at 37 °C, with shaking at 200 rpm. Use LB medium containing 10 g/L tryptone, 5 g/L yeast extract, and 10 g/L NaCl.
   NOTE: The cell density of the seed culture should reach OD 2 (optical density at 600 nm).
5. Inoculate one flask of 50 mL of the seed culture in the bioreactor. Maintain the culture at pH 6.0 and 37 °C. Use an air supplementation rate of 2 L/min and an agitation rate of 250 rpm, creating a microaerobic condition.
6. Collect 5 mL samples every 2 h during the fermentation and analyze them with high-pressure liquid chromatography to determine the chemical concentrations in the broth⁴.
   1. Monitor the alkali added to the bioreactor online using MFCS/DA.
      NOTE: Organic acids are produced in the fermentation process, and NaOH is added to keep the culture pH stable. The volume of alkali added represents the amount of acid produced. When the alkali-added line plateaus, the process is finished, either because of carbon source exhaustion or cell death.

3. R-acetoin Production by the budC Mutant of K. pneumoniae

1. Prepare a medium for acetoin production containing 4 g/L corn steep liquor, 2 g/L (NH₄)₂SO₄, 3 g/L sodium acetate, 0.4 g/L KCl, and 0.1 g/L MgSO₄.
2. Use K. pneumoniae-ΔbudC for R-acetoin production. Repeat steps 2.4-2.5.
   NOTE: budC encodes 2,3-butanediol dehydrogenase. K. pneumoniae-ΔbudC loses the 2,3-butanediol dehydrogenase activity and produces R-acetoin instead of 2,3-butanediol.
3. Maintain the culture at pH 6.0 and 37 °C. Use an air supplementation rate of 4 L/min and an agitation rate of 450 rpm, an aerobic condition.
   NOTE: The oxygen supplementation is higher than that of 2,3-butanediol production.
4. Assay the samples as in step 2.6.

4. 2-Ketogluconic Acid Production by the budA Mutant of K. pneumoniae

1. For 2-ketogluconic acid production, use the same medium as for R-acetoin production.
2. Use K. pneumoniae-ΔbudA for 2-ketogluconic acid production. Repeat steps 2.4-2.5.
   NOTE: budA encodes α-acetolactate decarboxylase. K. pneumoniae-ΔbudA loses the α-acetolactate decarboxylase activity and produces 2-ketogluconic acid, using glucose as a substrate.
   NOTE: 2-ketogluconic acid synthesis is an acidic condition-dependent process. A two-stage fermentation has been developed for 2-ketogluconic acid production¹⁰; in the first stage, the seed culture is inoculated in the bioreactor.
3. Maintain the culture at pH 7.0 and 37 °C. Use an air supplementation rate of 4 L/min and an agitation rate of 500 rpm.
   NOTE: In these conditions, cells grow very fast (the cell density reaches OD 7 in about 4 h). Then, the fermentation progresses to the second stage, during which the culture pH decreases to 5.0. No acid is added; the organic acids produced in the culture naturally lead to the pH decrease. In these acidic conditions, cell growth stops, but 2-ketogluconic acid is synthesized and accumulates in the broth.
4. Assay the samples as in step 2.6. Using the hydrolysate of bamboo as the carbon source.
   NOTE: The glucose in the medium is converted to 2-ketogluconic acid, and the xylose is converted to xylonic acid. Thus, a mixture of 2-ketogluconic acid and xylonic acid is obtained.

Results

In this protocol, the bamboo was pretreated using alkali. The optimal incubation parameters-a temperature of 121 °C and 0.25 M NaOH-were determined in Figures 1 and 2. The pretreated bamboo was enzymatically hydrolyzed, and the glucose and xylose concentrations obtained in the hydrolysate were measured. Higher temperatures favored sugar production, so 121 °C was selected as the optimal temperature. The glucose and xylose produced in the hydrolysate increa...

Discussion

K. pneumoniae belongs to the genus Klebsiella in the family Enterobacteriaceae. K. pneumoniae is distributed widely in natural environments such as soil, vegetation, and water¹⁴. The wildtype K. pneumoniae strain used in this research was isolated from soil and is used for 1,3-propanediol production¹⁵. K. pneumoniae and mutants of this species produce many chemicals under different conditions.

Materials

List of materials used in this article

Name	Company	Catalog Number	Comments
autoclave	SANYO	3780
bioreactor	Sartorius stedim biotech	Bostat Aplus
agitator	IKA	RW 20
water bath shaker	Zhicheng	ZWY-110X50
high performance liquid chromatograph system	Shimadzu Corp	20AVP
centrifuge	Hitachi	CR22G III
Bamboo powder	purchased from Zhejiang Province, China		mesh number, 50
cellulase	Youtell Biochemical, Shandong, China		200 PFU/mL