From scratch to value: engineering <Emphasis Type="Italic">Escherichia coli</Emphasis> wild type cells to the production of <Emphasis Type="SmallCaps">l</Emphasis>-phenylalanine and other fine chemicals derived from chorismate

Recombinant strains of Escherichia coli K-12 for the production of the three aromatic amino acids (l-phenylalanine, l-tryptophan, l-tyrosine) have been constructed. The largest demand is for l-phenylalanine (l-Phe), as it can be used as a building block for the low-calorie sweetener, aspartame. Besides l-Phe, an increasing number of shikimic acid pathway intermediates can be produced from appropriate E. coli mutants with blocks in this pathway. The last common intermediate, chorismate, in E. coli not only serves for production of aromatic amino acids but can also be used for high-titer production of non-aromatic compounds, e.g., cyclohexadiene-transdiols. In an approach to diversity-oriented metabolic engineering (metabolic grafting), platform strains with increased flux through the general aromatic pathway were created by suitable gene deletions, additions, or rearrangements. Examples for rational strain constructions for l-phenylalanine and chorismate derivatives are given with emphasis on genetic engineering. As a result, l-phenylalanine producers are available, which were derived through several defined steps from E. coli K-12 wild type. These mutant strains showed l-phenylalanine titers of up to 38 g/l of l-phenylalanine (and up to 45.5 g/l using in situ product recovery). Likewise, two cyclohexadiene-transdiols could be recovered.     

Carbohydrate metabolism in Corynebacterium glutamicum and applications for the metabolic engineering of l-lysine production strains

Carbohydrates exclusively serve as feedstock for industrial amino acid production with Corynebacterium glutamicum. Due to the industrial interest, knowledge about the pathways for carbohydrate metabolization in C. glutamicum steadily increases, enabling the rational design of optimized strains and production processes. In this review, we provide an overview of the metabolic pathways for utilization of hexoses (glucose, fructose), disaccharides (sucrose, maltose), pentoses (d-ribose, l-arabinose, d-xylose), gluconate, and β-glucosides present in C. glutamicum. Recent approaches of metabolic engineering of l-lysine production strains based on the known pathways are described and evaluated with respect to l-lysine yields.     

Eco-Efficiency Analysis of biotechnological processes

For almost 50 years now, biotechnological production processes have been used for industrial production of amino acids. Market development has been particularly dynamic for the flavor-enhancer glutamate and the animal feed amino acids l-lysine, l-threonine, and l-tryptophan, which are produced by fermentation processes using high-performance strains of Corynebacterium glutamicum and Escherichia coli from sugar sources such as molasses, sucrose, or glucose. But the market for amino acids in synthesis is also becoming increasingly important, with annual growth rates of 5–7%. The use of enzymes and whole cell biocatalysts has proven particularly valuable in production of both proteinogenic and nonproteinogenic l-amino acids, d-amino acids, and enantiomerically pure amino acid derivatives, which are of great interest as building blocks for active ingredients that are applied as pharmaceuticals, cosmetics, and agricultural products. Nutrition and health will continue to be the driving forces for exploiting the potential of microorganisms, and possibly also of suitable plants, to arrive at even more efficient processes for amino acid production.     

Improvement of l-valine production at high temperature in Brevibacterium flavum by overexpressing ilvEBNrC genes

Brevibacterium flavum ATCC14067 was engineered for l-valine production by overexpression of different ilv genes; the ilvEBN^rC genes from B. flavum NV128 provided the best candidate for l-valine production. In traditional fermentation, l-valine production reached 30.08 ± 0.92 g/L at 31°C in 72 h with a low conversion efficiency of 0.129 g/g. To further improve the l-valine production and conversion efficiency based on the optimum temperatures of l-valine biosynthesis enzymes (above 35°C) and the thermotolerance of B. flavum, the fermentation temperature was increased to 34, 37, and 40°C. As a result, higher metabolic rate and l-valine biosynthesis enzymes activity were obtained at high temperature, and the maximum l-valine production, conversion efficiency, and specific l-valine production rate reached 38.08 ± 1.32 g/L, 0.241 g/g, and 0.133 g g⁻¹ h⁻¹, respectively, at 37°C in 48 h fermentation. The strategy for enhancing l-valine production by overexpression of key enzymes in thermotolerant strains may provide an alternative approach to enhance branched-chain amino acids production with other strains.     

Metabolic engineering of <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> for the production of platform chemicals

Rhizopus oryzae is a filamentous fungus belonging to the Zygomycetes. It is among others known for its ability to produce the sustainable platform chemicals l-(+)-lactic acid, fumaric acid, and ethanol. During glycolysis, all fermentable carbon sources are metabolized to pyruvate and subsequently distributed over the pathways leading to the formation of these products. These platform chemicals are produced in high yields on a wide range of carbon sources. The yields are in excess of 85 % of the theoretical yield for l-(+)-lactic acid and ethanol and over 65 % for fumaric acid. The study and optimization of the metabolic pathways involved in the production of these compounds requires well-developed metabolic engineering tools and knowledge of the genetic makeup of this organism. This review focuses on the current metabolic engineering techniques available for R. oryzae and their application on the metabolic pathways of the main fermentation products.     

Formation of Phenolic and Indolic Compounds by Anaerobic Bacteria in the Human Large Intestine

Abstract Batch culture incubations were used to investigate the effects of pH (6.8 or 5.5) and carbohydrate (starch) availability on dissimilatory aromatic amino acid metabolism in human fecal bacteria. During growth on peptide mixtures, tyrosine and phenylalanine fermentations occurred optimally at pH 6.8, while individual metabolic reactions were inhibited by up to 80% in the presence of 10 g l⁻¹ starch. Tryptophan metabolites were not detected in these experiments. When free amino acids replaced peptides, phenol production was increased during carbohydrate fermentation, although formation of p-cresol, another tyrosine metabolite was strongly inhibited. Phenylpropionate, which is produced from phenylalanine, was unaffected by starch. Tryptophan was fermented in these studies, although indole production was reduced in the starch fermentors. The importance of different fermentation substrates (casein, peptide mixtures, free amino acids) on aromatic amino acid metabolism was investigated in incubations of material taken from the proximal bowel. The phenylalanine metabolites, phenylacetate and phenylpropionate, were the principal phenolic compounds formed from all three substrates. Phenol was the major tyrosine metabolite produced in casein and peptide fermentations, while hydroxyphenylpropionate was a more important tyrosine product from free amino acids. Indole was the sole product of tryptophan metabolism, but was formed only from the free amino acid. Bacterial metabolism of individual phenolic and indolic compounds was also investigated. Phenol, p-cresol, phenylacetate, phenylpropionate, 4-ethylphenol, indole, indoleacetate, and indolepropionate were not metabolized by colonic bacteria. However, hydroxyphenylacetate was hydrolyzed to p-cresol, while hydroxyphenylpropionate was transformed into phenylpropionate. Indolepyruvate was either converted to indoleacetate or metabolized into indole. Indolepropionate, and to a lesser degree indoleacetate were produced from indolelactate. These data show that human colonic anaerobes are able to extensively degrade either free or peptide-bound aromatic amino acids, with the concomitant formation of toxic metabolic products. These processes are controlled to a significant degree by environmental factors such as pH and carbohydrate availability, and this ultimately influences the types and amounts of fermentation products that can be formed in different regions of the large bowel. Received: 25 January 1996; Accepted: 8 May 1996     

Biosynthesis of aromatic amino acids in Nocardia sp. 239: effects of amino acid analogues on growth and regulatory enzymes

Summary Further steps required for overproduction of aromatic amino acids by a mutant strain of Nocardia sp. 239 (Noc 87-13), unable to grow on l-phenylalanine as a sole carbon and energy source, were investigated. A number of analogues of the aromatic amino acids displayed severe inhibitory effects on the activities of regulatory enzymes in the biosynthetic pathway and growth of the organism in glucose mineral medium. l-Tryptophane analogues strongly inhibited 3-deoxy-d-arabino-heptulosonate 7-phosphate (DAHP) synthase activity. l-Tyrosine analogues especially inhibited DAHP synthase and chorismate mutase, whereas l-phenylalanine analogues strongly inhibited chorismate mutase and prephenate dehydratase activity. Addition of the aromatic amino acids and their precursors chorismate, 4-hydroxyphenylpyruvate, phenylpyruvate and anthranilate, to the medium counteracted the growth inhibitory effect of specific analogues. The data indicate that ortho- (OFP) and para-fluoro-d,l-phenylalanine (PFP), and l-phenylalanine amide, are the most suitable analogues for the isolation of feedback-inhibition-insensitive prephenate dehydratase mutants. Attempts to isolate l-tyrosine and l-trytophane auxotrophic mutants were only successful in the latter case, resulting in the selection of a stable anthranilate synthase-negative mutant (Noc 87-13-14). Uptake of aromatic amino acids in Nocardia sp. 239 most likely involves a common transport system. This necessitates the use of anthranilate, rather than l-trytophane, as a supplement during the isolation of l-tyrosine auxotrophic and OFP- and/or PFP-resistant mutant derivative strains of Noc 87-13-14. Offprint requests to: L. Dijkhuizen     

Biotechnological production of polyamines by bacteria: recent achievements and future perspectives

In Bacteria, the pathways of polyamine biosynthesis start with the amino acids l-lysine, l-ornithine, l-arginine, or l-aspartic acid. Some of these polyamines are of special interest due to their use in the production of engineering plastics (e.g., polyamides) or as curing agents in polymer applications. At present, the polyamines for industrial use are mainly synthesized on chemical routes. However, since a commercial market for polyamines as well as an industry for the fermentative production of amino acid exist, and since bacterial strains overproducing the polyamine precursors l-lysine, l-ornithine, and l-arginine are known, it was envisioned to engineer these amino acid-producing strains for polyamine production. Only recently, researchers have investigated the potential of amino acid-producing strains of Corynebacterium glutamicum and Escherichia coli for polyamine production. This mini-review illustrates the current knowledge of polyamine metabolism in Bacteria, including anabolism, catabolism, uptake, and excretion. The recent advances in engineering the industrial model bacteria C. glutamicum and E. coli for efficient production of the most promising polyamines, putrescine (1,4-diaminobutane), and cadaverine (1,5-diaminopentane), are discussed in more detail.     

Metabolic pathways and biotechnological production of l-cysteine

l-Cysteine is an important amino acid both biologically and commercially. Although most amino acids are commercially produced by fermentation, cysteine is mainly produced by protein hydrolysis. However, synthetic or biotechnological products have been preferred in the market. Biotechnological processes for cysteine production, both enzymatic and fermentative processes, are discussed. Enzymatic process, the asymmetric hydrolysis of dl-2-amino-Δ²-thiazoline-4-carboxylic acid to l-cysteine, has been developed and industrialized. The l-cysteine biosynthetic pathways of Escherichia coli and Corynebacterium glutamicum, which are used in many amino acid production processes, are also described. These two bacteria have basically same l-cysteine biosynthetic pathways. l-Cysteine-degrading enzymes and l-cysteine-exporting proteins both in E. coli and C. glutamicum are also described. In conclusion, for the effective fermentative production of l-cysteine directly from glucose, the combination of enhancing biosynthetic activity, weakening the degradation pathway, and exploiting the export system seems to be effective.     

Alcoholic fermentation of carbon sources in biomass hydrolysates by Saccharomyces cerevisiae: current status

Fuel ethanol production from plant biomass hydrolysates by Saccharomyces cerevisiae is of great economic and environmental significance. This paper reviews the current status with respect to alcoholic fermentation of the main plant biomass-derived monosaccharides by this yeast. Wild-type S. cerevisiae strains readily ferment glucose, mannose and fructose via the Embden–Meyerhof pathway of glycolysis, while galactose is fermented via the Leloir pathway. Construction of yeast strains that efficiently convert other potentially fermentable substrates in plant biomass hydrolysates into ethanol is a major challenge in metabolic engineering. The most abundant of these compounds is xylose. Recent metabolic and evolutionary engineering studies on S. cerevisiae strains that express a fungal xylose isomerase have enabled the rapid and efficient␣anaerobic fermentation of this pentose. l-Arabinose fermentation, based on the expression of a prokaryotic pathway in S. cerevisiae, has also been established, but needs further optimization before it can be considered for industrial implementation. In addition to these already investigated strategies, possible approaches for metabolic engineering of galacturonic acid and rhamnose fermentation by S. cerevisiae are discussed. An emerging and major challenge is to achieve the rapid transition from proof-of-principle experiments under ‘academic’ conditions (synthetic media, single substrates or simple substrate mixtures, absence of toxic inhibitors) towards efficient conversion of complex industrial substrate mixtures that contain synergistically acting inhibitors.     

Regulation of pteridine biosynthesis and aromatic amino acid hydroxylation inDrosophila melanogaster

The relationship between high dietary levels of aromatic amino acid and regulation of pteridines inDrosophila eyes was examined by measuring changes in pool levels of six pterins in the wild type and mutants and amino acid pool levels in flies that carry mutations for pteridine biosynthesis. The effect upon relative viability and developmental times was also analyzed; relative viability was affected byl-phenylalanine,l-tryptophan, andl-tyrosine in decreasing order and thed-amino acids had little or no effect. The changes in concentration of biopterin, dihydrobiopterin, pterin, sepiapterin, drosopterins, and isoxanthopterin showed a characteristic pattern of increased and/or decreased amounts in response to each of the threel-amino acids. Pterin was regularly increased, and isoxanthopterin decreased.l-Tyrosine caused a 2.1-fold increase in dihydrobiopterin, the largest increase found in this study;l-tryptophan also caused dihydrobiopterin to increase butl-phenylalanine did not. Of 18 eye-color mutants examined, 2 were found to contain high levels of phenylalanine and/or tyrosine,Pu ² andHn ^r3. These two mutants, along withpr ^c4 cn/pr ^m2b cn, were shown to be very sensitive to dietaryl-phenylalanine, indicating that having low levels of certain pteridines makes them susceptible to toxic effects of these amino acids. Therefore, high levels of aromatic amino acids can perturb the balance among pteridine pools, and low levels of some pteridines in mutants are correlated with the inability to withstand the toxic effects of phenylalanine. From the patterns of change in the pteridines we suggest that tetrahydropterin may also be a cofactor for hydroxylation of phenylalanine, along with tetrahydrobiopterin.This work was sponsored in part by a grant from the U.S.-Spain Joint Committee for Scientific and Technological Cooperation.     

<Emphasis Type="SmallCaps">L</Emphasis>-Tyrosine production by deregulated strains of <Emphasis Type="Italic">Escherichia coli</Emphasis>

The excretion of the aromatic amino acid l-tyrosine was achieved by manipulating three gene targets in the wild-type Escherichia coli K12: The feedback-inhibition-resistant (fbr) derivatives of aroG and tyrA were expressed on a low-copy-number vector, and the TyrR-mediated regulation of the aromatic amino acid biosynthesis was eliminated by deleting the tyrR gene. The generation of this l-tyrosine producer, strain T1, was based only on the deregulation of the aromatic amino acid biosynthesis pathway, but no structural genes in the genome were affected. A second tyrosine over-producing strain, E. coli T2, was generated considering the possible limitation of precursor substrates. To enhance the availability of the two precursor substrates phosphoenolpyruvate and erythrose-4-phosphate, the ppsA and the tktA genes were over-expressed in the strain T1 background, increasing l-tyrosine production by 80% in 50-ml batch cultures. Fed-batch fermentations revealed that l-tyrosine production was tightly correlated with cell growth, exhibiting the maximum productivity at the end of the exponential growth phase. The final l-tyrosine concentrations were 3.8 g/l for E. coli T1 and 9.7 g/l for E. coli T2 with a yield of l-tyrosine per glucose of 0.037 g/g (T1) and 0.102 g/g (T2), respectively.     

New ubiquitous translocators: amino acid export by<Emphasis Type="Italic"> Corynebacterium glutamicum</Emphasis> and<Emphasis Type="Italic"> Escherichia coli</Emphasis>

Molecular access to amino acid excretion by Corynebacterium glutamicum and Escherichia coli led to the identification of structurally novel carriers and novel carrier functions. The exporters LysE, RhtB, ThrE and BrnFE each represent the protoype of new transporter families, which are in part distributed throughout all of the kingdoms of life. LysE of C. glutamicum catalytes the export of basic amino acids. The expression of the carrier gene is regulated by the cell-internal concentration of basic amino acids. This serves, for example, to maintain homoeostasis if an excess of l-lysine or l-arginine inside the cell should arise during growth on complex media. RhtB is one of five paralogous systems in E. coli, of which at least two are relevant for l-threonine production. A third system is relevant for l-cysteine production. It is speculated that the physiological function of these paralogues is related to quorum sensing. ThrE of C. glutamicum exports l-threonine and l-serine. However, a ThrE domain with a putative hydrolytic function points to an as yet unknown role of this exporter. BrnFE in C. glutamicum is a two-component permease exporting branched-chained amino acids from the cell, and an orthologue in B. subtilis exports 4-azaleucine.     

Genomic variations of <Emphasis Type="Italic">Oenococcus oeni</Emphasis> strains and the potential to impact on malolactic fermentation and aroma compounds in wine

Malolactic fermentation (MLF) is the bacterially driven decarboxylation of l-malic acid to l-lactic acid and carbon dioxide, and brings about deacidification, flavour modification and microbial stability of wine. The main objective of MLF is to decrease wine sourness by a small increase in wine pH via the metabolism of l-malic acid. Oenococcus oeni is the main lactic acid bacterium to conduct MLF in virtually all red wine and an increasing number of white and sparkling wine bases. Over the last decade, it is becoming increasingly recognized that O. oeni exhibits a diverse array of secondary metabolic activities during MLF which can modify the sensory properties of wine. These secondary activities include the metabolism of organic acids, carbohydrates, polysaccharides and amino acids, and numerous enzymes such as glycosidases, esterases and proteases, which generate volatile compounds well above their odour detection threshold. Phenotypic variation between O. oeni strains is central for producing different wine styles. Recent studies using array-based comparative genome hybridization and genome sequencing of three O. oeni strains have revealed the large genomic diversity within this species. This review will explore the links between O. oeni metabolism, genomic diversity and wine sensory attributes.     

Intermediate metabolism inTrypanosoma cruzi

Epimastigotes ofTrypanosoma cruzi, the causative agent of Chagas disease, catabolize proteins and amino acids with production of NH₃, and glucose with production of reduced catabolites, chiefly succinate andl-alanine, even under aerobic conditions. This aerobic fermentation of glucose is probably due to both the presence of low levels of some cytochromes, causing a relative inefficiency of the respiratory chain for NADH reoxidation during active glucose catabolism, and the lack of NADH dehydrogenase and phosphorylation site I, resulting in the entry of reduction equivalents into the chain mostly as succinate. Phosphoenol pyruvate carboxykinase and pyruvate kinase may play an essential role in diverting glucose carbon to succinate orl-alanine, andl-malate seems to be the major metabolite for the transport of glucose carbon and reduction equivalents between glycosome and mitochondrion. The parasite contains proteinase and peptidase activities. The major lysosomal cysteine proteinase, cruzipain, has been characterized in considerable detail, and might be involved in the host/parasite relationship, in addition to its obvious role in parasite nutrition. Among the enzymes of amino acid catabolism, two glutamate dehydrogenases (one NADP- and the other NAD-linked), alanine aminotransferase, and the major enzymes of aromatic amino acid catabolism (tyrosine aminotransferase and aromatic -hydroxy acid dehydrogenase), have been characterized and proposed to be involved in the reoxidation of glycolytic NADH.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-Lysine from starch by <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> displaying α-amylase on its cell surface

We engineered a Corynebacterium glutamicum strain displaying α-amylase from Streptococcus bovis 148 (AmyA) on its cell surface to produce amino acids directly from starch. We used PgsA from Bacillus subtilis as an anchor protein, and the N-terminus of α-amylase was fused to the PgsA. The genes of the fusion protein were integrated into the homoserine dehydrogenase gene locus on the chromosome by homologous recombination. l-Lysine fermentation was carried out using C. glutamicum displaying AmyA in the growth medium containing 50 g/l soluble starch as the sole carbon source. We performed l-lysine fermentation at various temperatures (30–40°C) and pHs (6.0–7.0), as the optimal temperatures and pHs of AmyA and C. glutamicum differ significantly. The highest l-lysine yield was recorded at 30°C and pH 7.0. The amount of soluble starch was reduced to 18.29 g/l, and 6.04 g/l l-lysine was produced in 24 h. The l-lysine yield obtained using soluble starch as the sole carbon source was higher than that using glucose as the sole carbon source after 24 h when the same amount of substrates was added. The results shown in the current study demonstrate that C. glutamicum displaying α-amylase has a potential to directly convert soluble starch to amino acids.     

Inhibitory action of serine on growth of bacteria of the genusBacillus on mineral synthetic media

l-Serine added to minimal synthetic media stops the growth ofBacillus subtilis, B. megaterium, B. mycoides andB. pantothenticus. All tested subspecies ofBacillus thuringiensis appear resistant to this amino acid. Serine acts bacteriostatically onB. subtilis strain B 003 and this effect depends on the concentrations of both the amino acid and the plated bacterium. Growth of serine-sensitiveBacillus strains can be restored by simultaneous addition of some other amino acids (e.g. l-threonine,l-arginine,l-aspartate orl-alanine) to the minimal media. This alleviating effect depends on the kind of amino acid. Some amino acids (e.g. l-threonine,l-tyrosine orl-tryptophan) are only effective when the serine concentration is not higher than 125 μmol/L, others (l-arginine,l-proline,l-alanine,l-aspartate orl-glutamate) are effective even when the serine concentration is as high as 500 μmol/L.     

Chemoreception in the green algaDunaliella tertiolecta

A capillary assay was employed to quantify positive chemotactic responses in the motile, unicellular, marine algaDunaliella tertiolecta. Among a wide range of inorganic and organic compounds tested, only ammonium ion,l-tyrosine,l-tryptophan, andl-phenylalanine were found to be major atractants for the chlorophyte.l-Methionine andl-cysteine weakly attracted the alga at 10⁻³ M. The minimum concentration of the major attractants needed to elicit an observable chemotactic response was approximately 10⁻⁶ M. The maximum response occurred when the capillaries contained 10⁻⁵ Ml-tyrosine orl-tryptophan, 10⁻⁴ Ml-phenylalanine, and 10⁻³ M ammonium chloride. The other amino acids, carbohydrates, B-vitamins, urea, and nitrate were among the chemicals that failed to attractD. tertiolecta. The alga apparently possesses one chemoreceptor that binds ammonium ion only, and another chemoreceptor that binds the three aromatic amino acids.     

Enhanced production of GDP-<Emphasis Type="SmallCaps">l</Emphasis>-fucose by overexpression of NADPH regenerator in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Biosynthesis of guanosine 5′-diphosphate-l-fucose (GDP-l-fucose) requires NADPH as a reducing cofactor. In this study, endogenous NADPH regenerating enzymes such as glucose-6-phosphate dehydrogenase (G6PDH), isocitrate dehydrogenase (Icd), and NADP⁺-dependent malate dehydrogenase (MaeB) were overexpressed to increase GDP-l-fucose production in recombinant Escherichia coli. The effects of overexpression of each NADPH regenerating enzyme on GDP-l-fucose production were investigated in a series of batch and fed-batch fermentations. Batch fermentations showed that overexpression of G6PDH was the most effective for GDP-l-fucose production. However, GDP-l-fucose production was not enhanced by overexpression of G6PDH in the glucose-limited fed-batch fermentation. Hence, a glucose feeding strategy was optimized to enhance GDP-l-fucose production. Fed-batch fermentation with a pH-stat feeding mode for sufficient supply of glucose significantly enhanced GDP-l-fucose production compared with glucose-limited fed-batch fermentation. A maximum GDP-l-fucose concentration of 235.2 ± 3.3 mg l⁻¹, corresponding to a 21% enhancement in the GDP-l-fucose production compared with the control strain overexpressing GDP-l-fucose biosynthetic enzymes only, was achieved in the pH-stat fed-batch fermentation of the recombinant E. coli overexpressing G6PDH. It was concluded that sufficient glucose supply and efficient NADPH regeneration are crucial for NADPH-dependent GDP-l-fucose production in recombinant E. coli.     

Fermentation of seaweed sugars by Lactobacillus species and the potential of seaweed as a biomass feedstock

It is known that seaweeds differ greatly from land plants in their sugar composition. The current research on the L-lactic acid fermentation process focuses on land plant sugars as a carbon source, with the potential of seaweed sugars being largely ignored. This study examined the feasibility of seaweed biomass as a possible carbon source for the production of l-lactic acid, by comparing the fermentation of seaweed sugars (d-galactose, d-mannitol, l-rhamnose, d-glucuronic acid, and l-fucose) and land plant sugars (d-glucose, d-xylose, d-mannose, and l-arabinose). The experiments were repeated with 2 sugar acids (d-gluconic acid, d-glucaric acid) in order to investigate the effect of the degree of reduction of carbon source on the fermentation yield. This research also examined the effect of bacterial strain on the characteristics of fermentation reactions, by conducting l-lactic acid fermentation with 7 different Lactobacillus species. Taking into account the sugar composition of seaweed and the levels of lactic acid production from each pure sugar, it was possible to predict the lactic acid production yield of various seaweeds and land plants. From comparative analysis of the predicted lactic acid production yield, it was found that seaweeds are already comparable to lignocellulosics at the current stage of technology. If new technologies for the utilization of non-fermentable seaweed sugars are developed, seaweeds show promise as an even more useful biomass feedstock than lignocellulosics.