Lactic acid production from xylose by the fungus Rhizopus oryzae

Lignocellulosic biomass is considered nowadays to be an economically attractive carbohydrate feedstock for large-scale fermentation of bulk chemicals such as lactic acid. The filamentous fungus Rhizopus oryzae is able to grow in mineral medium with glucose as sole carbon source and to produce optically pure l(+)-lactic acid. Less is known about the conversion by R. oryzae of pentose sugars such as xylose, which is abundantly present in lignocellulosic hydrolysates. This paper describes the conversion of xylose in synthetic media into lactic acid by ten R. oryzae strains resulting in yields between 0.41 and 0.71 g g⁻¹. By-products were fungal biomass, xylitol, glycerol, ethanol and carbon dioxide. The growth of R. oryzae CBS 112.07 in media with initial xylose concentrations above 40 g l⁻¹ showed inhibition of substrate consumption and lactic acid production rates. In case of mixed substrates, diauxic growth was observed where consumption of glucose and xylose occurred subsequently. Sugar consumption rate and lactic acid production rate were significantly higher during glucose consumption phase compared to xylose consumption phase. Available xylose (10.3 g l⁻¹) and glucose (19.2 g l⁻¹) present in a mild-temperature alkaline treated wheat straw hydrolysate was converted subsequently by R. oryzae with rates of 2.2 g glucose l⁻¹ h⁻¹ and 0.5 g xylose l⁻¹ h⁻¹. This resulted mainly into the product lactic acid (6.8 g l⁻¹) and ethanol (5.7 g l⁻¹).     

Production of L(+)-lactic acid with Rhizopus oryzae immobilized in polyurethane foam cubes

Summary Polyurethane foam cubes were employed as carriers to immobilize Rhizopus oryzae for L(+)-lactic acid production. The immobilizing capacity reached 450 g-fresh cell/l-cube. The production rate of L(+)-lactic acid could be threefold increased by using the immobilized R. oryzae. The immobilized cells could be steadily used in repetitive fermentations for more than 10 batches.     

L(+) Lactate production from carbohydrates and lignocellulosic materials by Rhizopus oryzae UMIP 4.77

The lactate excretion by Rhizopus oryzae on various carbohydrates was studied in order to assess the potential of lactate production from raw materials. Six collection strains were tested on ten commercial carbohydrates i.e. glucose, xylose, glycerol, sucrose, lactose, cellobiose, inulin, starch, cellulose and fructose in flask or stirred-tank bioreactor. On glucose and xylose, lactate was produced by R. oryzae UMIP 4.77 at 73 and 8 gL^?1 respectively, indicating that lignocellulosic materials could be used as possible raw substrates. Two lignocellulosic substrates were therefore experimented in stirred-tank bioreactor with R. oryzae UMIP 4.77. The first one was hemicellulosic material, which is a concentrated C6 and C5 sugar solution resulting from washing of a steamed wheat straw sample. The second was cellulosic material, which is a partially-hydrolyzed unbleached pulp paper. In a simultaneous saccharification fermentation process, a final production of 24.1 gL^?1 of lactate was obtained from cellulosic material.     

Effects of Cultivation Parameters on the Morphology of Rhizopus arrhizus and the Lactic Acid Production in a Bubble Column Reactor

The use of filamentous Rhizopus for lactic acid production is facing a challenge due to its low yield mainly caused by the difficulty to control its morphology in submerged fermentation processes. This study was aimed at investigating the impacts of cultivation parameters on the morphology of Rhizopus arrhizus DAR 36017 and lactic acid production using waste potato starch in a laboratory scale bubble column reactor (BCR). The fungal morphology was significantly influenced by carbon sources, process pH, starch concentrations, sparger designs and aeration rates. The favorable morphology for lactic acid production was a freely dispersed small pellet, which was achieved under operation conditions at pH 5.0–6.0, starch concentrations of 60–120 g/L and aeration rates of 0.2–0.8 vvm using a sintered stainless steel disc sparger. Optimal cultivation conditions at pH 6.0 and an aeration rate of 0.4 vvm resulted in the formation of freely dispersed small pellets and 103.8 g/L lactic acid with a yield of 87 % from 120 g/L liquefied potato starch in 48 h. The overall results in terms of lactic acid yield and productivity are comparable to those reported in previous studies using immobilized Rhizopus cells in batch fermentations.     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

Production of L(+)-lactic acid from glucose and starch by immobilized cells of Rhizopus oryzae in a rotating fibrous bed bioreactor

A rotating fibrous-bed bioreactor (RFB) was developed for fermentation to produce L(+)-lactic acid from glucose and cornstarch by Rhizopus oryzae. Fungal mycelia were immobilized on cotton cloth in the RFB for a prolonged period to study the fermentation kinetics and process stability. The pH and dissolved oxygen concentration (DO) were found to have significant effects on lactic acid productivity and yield, with pH 6 and 90% DO being the optimal conditions. A high lactic acid yield of 90% (w/w) and productivity of 2.5 g/L.h (467 g/h.m(2)) was obtained from glucose in fed-batch fermentation. When cornstarch was used as the substrate, the lactic acid yield was close to 100% (w/w) and the productivity was 1.65 g/L.h (300 g/h.m(2)). The highest concentration of lactic acid achieved in these fed-batch fermentations was 127 g/L. The immobilized-cells fermentation in the RFB gave a virtually cell-free fermentation broth and provided many advantages over conventional fermentation processes, especially those with freely suspended fungal cells. Without immobilization with the cotton cloth, mycelia grew everywhere in the fermentor and caused serious problems in reactor control and operation and consequently the fermentation was poor in lactic acid production. Oxygen transfer in the RFB was also studied and the volumetric oxygen transfer coefficients under various aeration and agitation conditions were determined and then used to estimate the oxygen transfer rate and uptake rate during the fermentation. The results showed that the oxygen uptake rate increased with increasing DO, indicating that oxygen transfer was limited by the diffusion inside the mycelial layer.     

Lactic acid fermentation of potato pulp by the fungus Rhizopus oryzae

Production of molecules with toxic activity by genetically transformed symbiotic bacteria of pest insects may serve as a powerful approach to biological control. The symbiont, Enterobacter gergoviae, isolated from the gut of the pink bollworm (PBW), has been transformed to express Cyt1A, a cytolytic protein toxin lethal to mosquito and black fly larvae, as a model system. These transgenic bacteria might be used to spread genes encoding insecticidal proteins to populations of agricultural insects or as replacement for chemical insecticides such as malathion used in bait formulation to control specific insect pests, because of extreme public pressure against organophosphate pesticide spraying. Received: 27 November 2000 / Accepted: 29 December 2000     

Optimization of Citric Acid Production from Glucose by Yarrowia lipolytica

Citric acid (CA) is mainly produced in a biotechnological process using Aspergillus niger. In this process, large amounts of wastes have to be removed. Since the use of Yarrowia lipolytica for CA production is an environmental compatible alternative method, the CA production was optimized in regard to growth temperature and pH as well as substrate and product inhibition. The highest value of the maximum specific growth rate at pH 6.5 was found to be μ_max = 0.192 h^–1, whereas the largest amount of CA of 24.91 g/L as well as the highest selectivity of the bioprocess (89.9 % CA) and the maximum yield (0.22 g_CA/g_Glucose) were obtained at pH 6.0. During the growth phase, the temperature optimum was found to be in the range of 30–34 °C (μ_max = 0.132 h^–1). Nevertheless, the highest concentration of CA during the production phase was obtained at 30 °C (41 g/L CA, 93.1 % CA, 0.55 g_CA/g_glucose). In studying the substrate inhibition of the process, a clear tendency of decrease in the maximum specific growth rate was detected when the initial glucose concentration was increased from 50 g/L (μ_max = 0.17 h^–1) to 200 g/L (μ_max = 0.055 h^–1). The addition of 120 g/L CA to the culture broth at the start of the production phase reduced the production of CA from 32.1 g/L to 7.4 g/L.     

Bioconversion of waste office paper to L(+)-lactic acid by the filamentous fungus Rhizopus oryzae

L(+)-lactic acid production was investigated using an enzymatic hydrolysate of waste office automation (OA) paper in a culture of the filamentous fungus Rhizopus oryzae. In 4 d culture, 82.8 g/l glucose, 7 g/l xylose, and 3.4 g/l cellobiose contained in the hydrolysate were consumed to produce 49.1 g/l of lactic acid. The lactic acid yield and production rate were only 0.59 g/g and 16.3 g/l/d, respectively, only 75% and 61% of the results from the glucose medium. The low production rate from waste OA hydrolysate was elucidated by trials using xylose as the sole carbon source; in those trials, the lactic acid production rate was 7.3 g/l/d, only 28% that of glucose or cellobiose. The low lactic acid yield from waste OA hydrolysate was clarified by trials using artificial hydrolysates comprised of 7:2:1 or 7:1:2 ratios of glucose:cellobiose:xylose. For both, the lactic acid production rate of 17.4 g/l/d matched that of waste OA paper, while the lactic acid yield was similar to that of the glucose medium. This indicates that the production rate may be inhibited by xylose derived from hemicellulose, and the yield may be inhibited by unknown compounds derived from paper pulp.     

Direct fermentation of potato starch wastewater to lactic acid by Rhizopus oryzae and Rhizopus arrhizus

The biochemical kinetic of direct fermentation for lactic acid production by fungal species of Rhizopus arrhizus 3,6017 and Rhizopus oryzae 2,062 was studied with respect to growth pH, temperature and substrate. The direct fermentation was characterized by starch hydrolysis, accumulation of reducing sugar, and production of lactic acid and fungal biomass. Starch hydrolysis, reducing sugar accumulation, biomass formation and lactic acid production were affected with the variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/l at pH 6.0 and 30°C was favourable for both starch saccharification and lactic acid fermentation, resulting in lactic acid yield of 0.87–0.97 g/g starch associated with 1.5–2.0 g/l fungal biomass produced in 36 h fermentation. R. arrhizus 3,6017 had a higher capacity to produce lactic acid, while R. oryzae 2,062 produced more fungal biomass under similar conditions.     

Optimization of Xylanase Production by Sporotrichum thermophile Using Corn Cobs and Response Surface Methodology

A 3² central composite experimental design was performed with the aim of optimizing the production of xylanase by Sporotrichum thermophile grown on corn cobs in submerged cultures. Various carbon and nitrogen sources were consecutively optimized, and corn cobs and ammonium phosphate concentrations were selected as substrates to test the effect of two variables, i.e., both substrate concentrations, on xylanase production. A second‐order quadratic model and a response surface method showed that the optimum conditions for xylanase production were 2.7 % [w/v] corn cobs and 0.7 % [w/v] ammonium phosphate. These optimum conditions were transferred to 7 L bioreactors, where activities as high as 56 U/mL were obtained.     

Lactic acid and animal feeds production from Sophora flavescens residues by Rhizopus oryzae fermentation

In this study, the feasibility of producing lactic acid and animal feeds from Sophora flavescens residues (SFR) by Rhizopus oryzae was explored. Results showed that the simultaneous saccharification and fermentation (SSF) is the optimal fermentation mode, which was simple and high-efficiency. When the inoculation volume of R. oryzae was 10 % and the pH value was adjusted by adding CaCO₃ in stages during SSF, the maximum concentration of lactic acid was 46.78 g/L, and the maximum lactic acid productivity reached 0.97 g/L/h. Results also showed that the protein content of the solid residues after fermentation of R. oryzae reached 12.15 %. This content was 46 times higher than that by the original SFRs and nearly 4.3 times the protein content of the solid residues after fermentation by Enterococcus faecium. In addition, the solid residues after fermentation rich in Fe and Zn could be used as animal feeds or feed additives. Thus, it is expected that this study may provide a novel approach for Chinese medicine residues treatment towards full resource recovery.     

Immobilization of Rhizopus oryzae in a modified polyvinyl alcohol gel for L(+)-lactic acid production

The production of L(+)-lactic acid (LA) by Rhizopus oryzae immobilized in polyvinyl alcohol (PVA) was investigated. To decrease diffusional resistance, we modified the PVA gel through the addition of sodium alginate and phosphate esterification. The production of L(+)-LA improved notably in the immobilized Rhizopus oryzae. Maximum L(+)-LA production (106.27 g/L), with a yield of 73.1 % and rate of 2.95 g/L·h, was obtained at a temperature of 38 °C, 6 % PVA, and 0.8 % sodium alginate. The immobilized R. oryzae was stable in 14 serial-batch cultures using non-growth medium. The immobilized beads also displayed good tolerance to low temperature and long-term storage at 4 °C with the preservation of biochemical properties.     

Production of mycelium biomass and ethanol from paper pulp sulfite liquor by Rhizopus oryzae

The cultivation conditions for Rhizopus oryzae grown in synthetic medium and paper pulp spent sulfite liquor (SSL) were investigated to achieve high biomass and ethanol yields using shake flasks and bioreactors. The fungus assimilated the hexoses glucose, mannose and galactose, and the pentoses xylose and arabinose as well as acetic acid which are present in SSL. The assimilation of hexoses was faster than pentoses during cultivation in a synthetic medium. However, all sugars were assimilated concomitantly during growth in SSL supplemented with ammonium, magnesium, calcium, phosphate, sulfate and trace amounts of some other metal ions (SSL-S). The medium composition had an important influence on biomass yield. The highest biomass yields, viz. 0.18 and 0.43 g biomass/g sugar were obtained, when the cells were cultivated in shake flasks with a synthetic medium containing glucose as carbon and energy source and SSL-S, respectively. The corresponding yields in a bioreactor with more efficient aeration were 0.22 and 0.55 g/g. In addition to the biomass, ethanol, lactic acid, and glycerol were important extracellular metabolites of the cultivation with maximum yields of 0.37, 0.30 and 0.09 g/g, respectively. When the source of sugars in the medium was exhausted, the fungus consumed the metabolites produced, such that the liquid medium was depleted of potential oxidizable nutrients. In general, there was a direct competition between lactic acid and ethanol among the metabolites. Poor medium compositions and cultivation conditions resulted in higher yields of lactic acid, whereas the ethanol and biomass yields were higher in rich media. SSL-S supported good growth of mycelium and a high ethanol yield.     

代谢甘油高产乳酸的菌种选育及培养基优化

分离出一株可高效利用甘油生产乳酸的菌株, 经过生理生化和16S rDNA分子鉴定, 确定其属于大肠埃希氏菌, 命名为Escherichia coli AC-521。通过五因素四水平正交试验, 优化了其最佳发酵培养基成分为初始甘油70 g/L, 酵母粉4 g/L, 蛋白胨7 g/L, (NH4)2SO4 10 g/L, K2HPO4 2.5 g/L。利用该最佳条件的5 L发酵罐批式补料发酵实验表明: 该菌株发酵80 h后, 乳酸产量可达到74.5 g/L, 得率为0.87 mol/mol甘油。     

Direct fermentation of l(+)-lactic acid from cassava pulp by solid state culture of Rhizopus oryzae

This study shows that Rhizopus oryzae is capable of directly utilizing cassava pulp alone to L: -lactic acid in solid state fermentation (SSF). pH control at 6.0 helped prevent end product inhibition. Increasing lactate titer was observed at the higher initial moistened water due to the higher degree of substrate swelling and hydrolysis. With shaking, limited ethanol production but no change in lactate titer was observed. Rigorous shaking gave better oxygen transfer but presumably caused cell damage leading to substrate utilization through the biosynthesis route. Supplementing cassava pulp with nitrogen enhanced growth but not lactate production. Under the optimal conditions, R. oryzae converted the sole cassava pulp into lactic acid at the titer of 206.20?mg per g initial dry pulp. With the help of commercial cellulase and glucoamylase, the dramatically increasing lactate titer of 463.18?mg per g initial dry pulp was achieved via SSF.     

根霉菌利用木质纤维素发酵生产有机酸的研究进展*

木质纤维素是世界上储量最丰富、最廉价的可再生生物质资源,利用木质纤维素发酵生产有机酸具有重大的经济效益及社会效益。为发掘影响木质纤维素利用的关键因素,对根霉菌的木糖代谢途径以及利用木质纤维素发酵生产乳酸、富马酸等重要有机酸的生产方式、发酵策略等进行了阐述,指出针对木糖的转化率是制约木质纤维素高效利用的瓶颈。     

猪源乳酸菌产乳酸及其抑菌特性研究

研究了5株(L1、12、L3、L5和L7)分离自仔猪肠道的乳酸菌的产乳酸能力及抑菌特性。结果表明：L5菌株产乳酸的速度最快,培养液中乳酸含量最高,L5菌株培养液pH值的下降速度最快,终末pH值最低,而L1菌株产乳酸的速度最慢,培养液乳酸含量最低。5株乳酸菌对大肠杆菌K88、K99、987P、O141和大肠杆菌E1及金黄色葡萄球菌均有不同程度的抑制作用;排除酸的影响后仍有22％～53％抑菌效果;经热处理后保持有92％以上的抑菌效果;蛋白酶处理后保持85％以上的抑菌效果。     

一组鸡源乳酸菌产乳酸及其耐受特性研究*

研究了12株（K9、D17、C1、C12、D11、D14、C2、D9、K6、C21、D1和D7）分离自肉鸡肠道的乳酸菌的产乳酸能力及其中3株产酸能力强的菌株的耐受特性。12株乳酸菌产乳酸结果表明：12h内,K6产乳酸速度最快,其次为K9和C1,24h时,D17乳酸浓度最高,48h时C1终乳酸浓度最高。K9、D17和C1的耐受试验结果表明：C1菌株耐酸能力最强,pH2时,C1菌株培养3h后还能检测到活菌,D17和K9菌株培养1h后就已经检测不到活菌。在胆盐浓度0．08％-0．40％范围内,C1、D17和K9均有一定的耐受能力,随着胆盐浓度的升高,C1、D17和K9的存活数呈现缓慢的下降趋势。3株菌中D17耐热能力最强,经80％处理后仍有10^4.9／mL存活数,而K9和C1已检测不到活菌;C1对热最敏感,65℃处理后存活数由10^8／mL降为10^3／mL。     

Dehalogenation Activity of Selected Fungi Toward δ‐Iodo‐γ‐Lactone Derived from trans,trans‐Farnesol

Time‐course of biotransformation of racemic trans‐4‐((E)‐4′,8′‐dimethylnona‐3′,7′‐dien‐1‐yl)‐5‐iodomethyl‐4‐methyldihydrofuran‐2‐one ( 1 ) in fungal and yeast cultures was investigated. In these conditions, the substrate 1 was enantioselectively dehalogenated yielding 4‐((E)‐4′,8′‐dimethylnona‐3′,7′‐dien‐1‐yl)‐4‐methyl‐5‐methylenedihydrofuran‐2‐one ( 2 ) and its structure was established based on the spectroscopic data. The most effective biocatalyst used was Didymosphaeria igniaria, which catalyzed the process with highest rate and enantioselectivity (ee of product = 76%). The antiproliferative activity of δ‐iodo‐γ‐lactone 1 , product of its biotransformation 2 , and starting substrate (farnesol) were evaluated toward two cancer cell lines: A549 (human lung adenocarcinoma) and HL‐60 (human promyelocytic leukemia).