The mechanism of rock phosphate solubilization in the rhizosphere

Summary A simple model is described, and experimentally tested, for predicting the rate of dissolution of rock phosphates in soil, including the effect of solubilization by plant roots. The sensitivity of the model to its input parameters is assessed and it is seen that plants may significantly increase their P uptake by acid secretion. The model provides a rational basis for the selection of P solubilizing crops and inter-crops.     

Sugarcane bagasse derivative-based superabsorbent containing phosphate rock with water-fertilizer integration

To improve the water-fertilizer utilization ratio and mitigate the environmental contamination, an eco-friendly superabsorbent polymer (SPA), modified sugarcane bagasse/poly (acrylic acid) embedding phosphate rock (MSB/PAA/PHR), was prepared. Ammonia, phosphate rock (PHR) and KOH were admixed in the presence of acrylic acid to provide nitrogen (N), phosphorus (P) and potassium (K) nutrients, respectively. Impacts on water absorption capacity of the superabsorbent polymer (SAP) were investigated. The maximum swelling capacity in distilled water and 0.9wt.% (weight percent) NaCl solution reached 414gg(-1) and 55gg(-1) (water/prepared SAP), respectively. The available NPK contents of the combination system were 15.13mgg(-1), 6.93mgg(-1) and 52.05mgg(-1), respectively. Moreover, the release behaviors of NPK in the MSB/PAA/PHR were also studied. The results showed that the MSB/PAA/PHR has outstanding sustained-release plant nutrients property.     

Factors determining rock phosphate solubilization by microorganisms isolated from soil

Forty two soil isolates (31 bacteria and 11 fungi) were studied for their ability to solubilize rock phosphate and calcium phosphate in culture medium. Eight bacteria and 8 fungi possessed solubilizing ability. Pseudomonas cepacia and Penicillium purpurogenum showed the highest activity. There was a correlation between final pH value and titratable acidity (r=–0.29 to –0.87) and between titratable acidity and soluble phosphate (r=0.22 to 0.99). Correlation values were functions of insoluble phosphate and of the group of microorganisms considered. A high correlation was observed between final pH and soluble phosphate only for the rock phosphates inoculated with the highest concentration of solubilizing bacteria (r=–0.73 to –0.98).     

The solubilization of low-grade rock phosphate with anaerobic digester slurry

The effects of biogas slurry on the solubilization of low-grade rock phosphate was studied by digestion in compost pits. Biogas slurry had solubilizing power for up to 60 days while molasses addition prolonged it throughout a digestion period of 120 days. In this case solubilization reached a maximum of 42.6% of added rock phosphate. Pyrite incorporation depressed drastically the rate of solubilization in spite of decreasing the pH and increasing the citrate-soluble P of the digesting biogas slurry.The concentration of total P increased with increase the loss of organic matter during digestion. The maximum weight loss was recorded in rock phosphate-containing treatment, where release of water-soluble P increased continuously with time and organic P decreased after 30 days of incubation. On the other hand, incorporation of molasses both in presence and absence of pyrite, decreased the water-soluble P but increased the organic P content of the digesting material.     

Biotechnological solubilization of rock phosphate on media containing agro-industrial wastes

Rock phosphate (RP) is an important natural material traditionally used for the production of phosphorus (P) fertilizers. Compared with chemical treatment, microbial solubilization of RP is an alternative environmentally mild approach. An overview of biotechnological techniques, mainly based on solubilization processes involving agro-industrial residues, is presented. Potential advantages of composting, solid-state fermentation, and liquid submerged fermentation employing free and immobilized microorganisms that produce organic acids and simultaneously solubilize RP are discussed. Subsequent introduction of the final fermented products into soil-plant systems promotes plant growth and P acquisition.     

Citric acid production by solid state fermentation using sugarcane bagasse

A solid state fermentation (SSF) method was used to produce citric acid by Aspergillus niger DS 1 using sugarcane bagasse as a carrier and sucrose or molasses based medium as a moistening agent. Initially bagasse and wheat bran were compared as carrier. Bagasse was the most suitable carrier, as it did not show agglomeration after moistening with medium, resulting in better heat and mass transfer during fermentation and higher product yield. Different parameters such as moisture content, particle size, sugar level and methanol concentration of the medium were optimised and 75% moisture level, 31.8 g sugar/100 g dry solid, 4% (v/w) methanol and particles of the size between 1.2 and 1.6 mm were found to be optimal. Sucrose and clarified and non-clarified molasses medium were also tested as moistening agents for SSF and under optimised conditions, 20.2, 19.8 and 17.9 g citric acid /100 g of dry solid with yield of 69.6, 64.5 and 62.4% (based on sugar consumed) was obtained in sucrose, clarified and non-clarified molasses medium respectively, after 9 days of fermentation.     

Preparation of sugarcane bagasse hemicellulosic succinates using NBS as a catalyst

The chemical modification of native sugarcane bagasse hemicelluloses with succinic anhydride using N-bromosuccinimide as a catalyst and N,N-dimethylacetamide/lithium chloride system as solvent was studied. The parameters optimised included succinic anhydride concentration by the molar ratio of succinic anhydride/anhydroxylose units in native hemicelluloses from 1:1 to 9:1, reaction time 0.5–6 h, NBS concentration 0.5–3.0%, and reaction temperature 25–85 °C required in the process. Results were also compared with other catalysts such as pyridine, DMAP, H₂SO₄, and other two tertiary amine catalysts, N-methyl pyrrolidine, and N-methyl pyrrolidinone. The degree of substitution of succinylated hemicelluloses ranged between 0.19 and 1.39, depending on the experimental conditions. FT-IR and ¹H and ¹³C NMR spectroscopic characterization of the esterified polymers indicated a monoester substitution. The thermal stability of the succinylated hemicelluloses decreased upon chemical modification.     

Enhanced solubilization of rock phosphate by Penicillium bilaiae in pH-buffered solution culture

Little is known about how pH-buffering capacity affects phosphorus (P) solubilization by Penicillium bilaiae. This study compared solubilization of rock phosphate (RP) by P. bilaiae in nonbuffered (pH 5.0) and buffered (pH 7.0) media. Fungal growth reached the stationary phase around day 12 and was slightly enhanced in the buffered medium. The fungus reduced solution pH from 5.0 to 4.1 in the nonbuffered medium and from 7.0 to 4.9 in the buffered medium by day 12. Phosphorus concentrations increased after day 9 more in the buffered than in the nonbuffered media (53 and 5 mg P x L(-1), respectively, on day 12). On day 12, higher concentrations of citric and oxalic acids were detected in the buffered (2.0 and 1.2 g x L(-1), respectively) than nonbuffered media (0.5 and 0.04 g x L(-1), respectively). Solubilization of RP was simulated without P. bilaiae in solutions equivalent to the nonbuffered and buffered cultures of P. bilaiae grown with RP. After a 24 h incubation, the P concentrations were of similar magnitudes to those observed in the P. bilaiae culture (18 and 47 mg P x L(-1), respectively, in the nonbuffered and buffered media). Under increased pH-buffering conditions, the enhanced production of citric and oxalic acids led to significant RP solubilization.     

Extraction and characterization of wax from sugarcane bagasse and the enzymatic hydrolysis of dewaxed sugarcane bagasse

Extraction of high-value products from agricultural wastes is an important component for sustainable bioeconomy development. In this study, wax extraction from sugarcane bagasse was performed and the beneficial effect of dewaxing pretreatment on the enzymatic hydrolysis was investigated. About 1.2% (w/w) of crude sugarcane wax was obtained from the sugarcane bagasse using the mixture of petroleum ether and ethanol (mass ratio of 1:1) as the extraction agent. Results of Fourier-transform infrared characterization and gas chromatography–mass spectrometry qualitative analysis showed that the crude sugarcane wax consisted of fatty fractions (fatty acids, fatty aldehydes, hydrocarbons, and esters) and small amount of lignin derivatives. In addition, the effect of dewaxing pretreatment on the enzymatic hydrolysis of sugarcane bagasse was also investigated. The digestibilities of cellulose and xylan in dewaxed sugarcane bagasse were 18.7 and 10.3%, respectively, compared with those of 13.1 and 8.9% obtained from native sugarcane bagasse. The dewaxed sugarcane bagasse became more accessible to enzyme due to the disruption of the outermost layer of the waxy materials.     

Xylan extraction from pretreated sugarcane bagasse using alkaline and enzymatic approaches

Background

New biorefinery concepts are necessary to drive industrial use of lignocellulose biomass components. Xylan recovery before enzymatic hydrolysis of the glucan component is a way to add value to the hemicellulose fraction, which can be used in papermaking, pharmaceutical, and food industries. Hemicellulose removal can also facilitate subsequent cellulolytic glucan hydrolysis.

Results

Sugarcane bagasse was pretreated with an alkaline-sulfite chemithermomechanical process to facilitate subsequent extraction of xylan by enzymatic or alkaline procedures. Alkaline extraction methods yielded 53% (w/w) xylan recovery. The enzymatic approach provided a limited yield of 22% (w/w) but produced the xylan with the lowest contamination with lignin and glucan components. All extracted xylans presented arabinosyl side groups and absence of acetylation. 2D-NMR data suggested the presence of O-methyl-glucuronic acid and p-coumarates only in enzymatically extracted xylan. Xylans isolated using the enzymatic approach resulted in products with molecular weights (Mw) lower than 6 kDa. Higher Mw values were detected in the alkali-isolated xylans. Alkaline extraction of xylan provided a glucan-enriched solid readily hydrolysable with low cellulase loads, generating hydrolysates with a high glucose/xylose ratio.

Conclusions

Hemicellulose removal before enzymatic hydrolysis of the cellulosic fraction proved to be an efficient manner to add value to sugarcane bagasse biorefining. Xylans with varied yield, purity, and structure can be obtained according to the extraction method. Enzymatic extraction procedures produce high-purity xylans at low yield, whereas alkaline extraction methods provided higher xylan yields with more lignin and glucan contamination. When xylan extraction is performed with alkaline methods, the residual glucan-enriched solid seems suitable for glucose production employing low cellulase loadings.

     

Delignification of sugarcane bagasse using glycerol-water mixtures to produce pulps for saccharification

This paper describes the organosolv delignification of depithed bagasse using glycerol–water mixtures without a catalyst. The experiments were performed using two separate experimental designs. In the first experiment, two temperatures (150 and 190 °C), two time periods (60 and 240 min) and two glycerol contents (20% and 80%, v/v) were used. In the second experiment, which was a central composite design, the glycerol content was maintained at 80%, and a range of temperatures (141.7–198.3 °C) and time (23–277 min) was used. The best result, obtained with a glycerol content of 80%, a reaction time of 150 min and a temperature of 198.3 °C, produced pulps with 54.4% pulp yield, 7.75% residual lignin, 81.4% delignification and 13.7% polyose content. The results showed that high contents of glycerol tend to produce pulps with higher delignification and higher polyoses content in relation to the pulps obtained from low glycerol content reactions. In addition, the proposed method shows potential as a pretreatment for cellulose saccharification.     

Succinoylation of sugarcane bagasse under ultrasound irradiation

The chemical modification of sugarcane bagasse with succinic anhydride using pyridine as solvent after ultrasound irradiation was studied. The optimized parameters included ultrasound irradiating time 0-50 min, reaction time 30-120 min, succinic anhydride concentration by the ratio of dried sugarcane bagasse to succinic anhydride from 1:0.25 to 1:1.50, and reaction temperature 75-115 degrees C are required in the process. The extent of succinoylation was measured by the weight percent gain (WPG), which increased with increments of reaction time, succinic anhydride concentration, and reaction temperature. The ultrasound irradiation has a positive effect on bagasse succinoylation process. On the other hand, the ultrasonic pre-treatment application broke down the cell wall polymers, resulting in, therefore, a negative effect on the WPG. Evidences of succinoylation were also provided by FT-IR and CP MAS (13)C NMR and the results showed that the succinoylation at C-2 and C-3 occurred. The thermal stability of the succinylated bagasse decreased upon chemical modification.     

Fractionation of sugarcane bagasse by hydrothermal treatment

Hydrothermal treatment of sugarcane bagasse was conducted using a semi-batch reactor to develop a new biomass fractionation method that has low impact in the environment. A continuously increasing temperature was used in this treatment. It was found that hemicellulose and lignin could be mainly extracted as a water-soluble fraction at 200-230 degrees C, while the cellulose fraction was hydrolyzed at higher temperatures (230-280 degrees C) or recovered as solid residue from this treatment. Detailed analyses of the solid residue indicated that the crystal structure and the chemical composition of the residue were in good accordance with those of untreated crystalline cellulose. These experimental and analytical findings show that this method is promising for removal of hemicellulose and lignin from woody biomass without any catalyst and organic solvent.     

Growth of cellulolytic bacteria on sugarcane bagasse

The growth behavior of Cellulomonas has been examined in fermentation system using alkali pretreated sugarcane bagasse. During the batch operation diauxic growth was found which would not seem to be explained by catabolic repression. The relative variation of cellulose and hemicellulose during the fermentation process suggests the initial utilization of easily degradable substrate, i.e., hemicellulose and amorphous cellulose, until their concentration becomes limiting, followed by utilization of the crystalline cellulose. The conversion of substrate was 70% with a yield of 0.355 g of biomass per gram of bagasse feed.     

Extracellular L-asparaginase production in solid-state fermentation by using sugarcane bagasse as support material

Abstract

L-asparaginase is an important enzyme used in the pharmaceutical and food industry, which can be produced by different microorganisms using low cost feedstocks. In this work, sugarcane bagasse (SCB) was used as support for enzyme production in solid-state fermentation (SSF) by A. terreus. Initially, the influence of the variables carbon and nitrogen sources on the enzyme production was studied following an experimental design carried out in Erlenmeyer flasks. Statistical analysis indicated the use of 0.54% of starch, 0% of maltose, 0.44% of asparagine, and 1.14% of glutamine in the medium, resulting in enzyme activity per volume of produced extract of 120.723?U/L. Then, these conditions were applied in a horizontal column reactor filled with SCB, producing 105.3?U/L of enzyme activity. Therefore, the potential of extracellular L-asparaginase enzyme production in the column reactor using sugarcane bagasse as support was demonstrated and it represents a system that can favor large scale production.     

Xylanase production by endophytic Aspergillus niger using pentose-rich hydrothermal liquor from sugarcane bagasse

Fungal xylanases have been widely studied and various production methods have been proposed using submerged and solid-state fermentation. This class of enzyme is used to supplement cellulolytic enzyme cocktails in order to enhance the enzymatic hydrolysis of plant cell walls. The present work investigates the production of xylanase and other accessory enzymes by a recently isolated endophytic Aspergillus niger DR02 strain, using the pentose-rich liquor from hydrothermal pretreatment of sugarcane bagasse as carbon source. Batch and fed-batch submerged cultivation approaches were developed in order to minimize the toxicity of the liquor and increase enzyme production. Maximum xylanase activities obtained were 458.1 U/mL for constant fed-batch, 428.1 U/mL for exponential fed-batch, and 264.37 U/mL for pulsed fed-batch modes. The results indicated that carbon-limited fed-batch cultivation can reduce fungal catabolite repression, as well as overcome possible negative effects of toxic compounds present in the pentose-rich liquor. Enzymatic panel and mass spectrometric analyses of the fed-batch A. niger secretome showed high levels of xylanolytic enzymes (GH10, GH11, and GH62 Cazy families), together with cellobiohydrolase (G6 and GH7), β-glucosidase, β-xylosidase (GH3), and feruloyl esterase (CE1) accessory enzyme activities. The yields of glucose and xylose from enzymatic hydrolysis of hydrothermally pretreated sugarcane bagasse increased by 43.7 and 65.3%, respectively, when a commercial cellulase preparation was supplemented with the A. niger DR02 constant fed-batch enzyme complex.     

溶磷菌和固氮菌溶解磷矿粉时的互作效应

采用4株溶磷菌（Lx81、Dm84、Jm92、Lx191）、和3株固氮菌（ChW5、ChW6、ChO6）单独和混合接种后测定培养液有效磷含量、pH值及总有机酸含量的方法,研究溶磷菌和固氮菌溶解磷矿粉时的互作效应。结果表明,相对于单独接种溶磷菌：Lx81与3株固氮菌分别混合培养能提高磷矿粉的溶解能力,4株溶磷菌与ChW6,Lx81、Dm84、Lx191与Ch06分别混合培养及Jm92＋ChW5组合溶磷量极显著增加（P〈0．01）;Dm84＋ChW5、Lxl91＋ChW5、Jm92＋Ch06组合的溶磷量下降（P〈0．01）。除Lx81＋ChW6、Lx81＋Ch06培养液pH值降低外,混合培养的其它组合培养液pH值均较单独接种溶磷菌时升高。有机酸测定结果表明,Lx81、Jm92与ChW5、Ch06分别混合培养、ChW6＋Lx81组合有机酸含量升高（P〈0．01）,其它7种组合的有机酸含量均较单独接种溶磷菌的值下降（P〈0．01）。溶磷菌和固氮菌单菌培养时溶磷量与pH值、溶磷量与总有机酸含量及pH值与总有机酸含量之间呈现线性相关;Dm84、Lx191与3株固氮菌分别混合培养溶磷量与pH值之间、Lx81与3株固氮菌分别混合培养溶磷量与总有机酸含量之间呈现线性相关,其它组合的溶磷量与pH值、总有机酸含量间没有相关性。溶磷菌和固氮菌混合培养对溶解磷矿粉既有协同作用也有拮抗作用。     

不同碳源对三种溶磷真菌溶解磷矿粉能力的影响

通过液体培养法 ,对 3种溶磷真菌利用葡萄糖、果糖、蔗糖、麦芽糖、淀粉和纤维素等碳源溶解宜昌产磷矿粉的试验 ,结果表明 ,菌株P2 3在供给葡萄糖时的溶磷能力最高 ,并在一定程度上能够利用长链碳源淀粉和纤维素为营养而溶磷 ;而高效溶磷菌株P6 6和P39溶磷的最佳碳源是果糖和麦芽糖 ,该两菌株利用淀粉和纤维素的溶磷效果很小 ,甚至不溶磷。 3种溶磷真菌培养滤液 pH值、可滴定酸含量与其溶磷量之间的相关性因菌株而异 ,差别很大。菌株P2 3培养滤液pH值、可滴定酸含量与其溶磷量之间相关性很低 ,但菌株P6 6和P39培养滤液pH值、可滴定酸含量与其溶磷量之间相关性却达到极显著水平 (P <0 0 1)。结果表明 ,不同碳源对溶磷菌溶解磷矿粉能力影响很大 ,分析推断 3种菌株产生的有机酸活化磷矿粉能力为P6 6>P39>P2 3。     

Isolation of a gastroprotective arabinoxylan from sugarcane bagasse

After industrial processing, one-third of sugarcane culms is converted into residual bagasse. The xylan-rich hemicellulose components of the bagasse were extracted with hot aqueous alkali (AX-CRUDE). Approximately 82% of the extracted hemicelluloses was precipitated with ethanol (AX-PET). Both AX-CRUDE and AX-PET contained an arabinoxylan as confirmed by 13C NMR and methylation analysis. Fraction AX-PET was fed to female Wistar rats with ethanol-induced gastric lesions. Oral administrations of 30, 100, and 300 mg/kg reduced the gastric lesion area by over 50%, and replenished ethanol-induced depletion of glutathione. The polysaccharide also increased mucus production by over 70%, indicating its cytoprotective action on experimentally induced gastric ulcers. These findings are significant, since a biologically active compound can be extracted in high yields from an abundant, readily available residue.     

Fed-batch cultivation of Cellulomonas on sugarcane bagasse pith

A high biomass concentration (19.9 g/L) was obtained with the fed-batch cultivation of Cellulomonas on pretreated sugarcane bagasse pith. Similar results in biomass concentration, yield, and substrated consumption were obtained with the discontinuous feed of bagasses as with discontinuous feed supplemented with a partial continuous addition of salts. Two or more growth phases were detected, probably caused by the differential utilization of bagasse components. An acceptably low content of bagasse components remained in the biomass after separation.