Reduced formation of byproduct component C in acarbose fermentation by Actinoplanes sp. CKD485-16

Acarbose fermentation was conducted by cultivation of Actinoplanes sp. CKD485-16. Approximately 2,300 mg/L of acarbose was produced at the end of cultivation along with 600 mg/L of the acarbose byproduct component C. Maltose, a known moiety of acarbose, should be maintained at high concentration levels in culture broths for efficient acarbose production. The acarbose yield increased with an increasing osmolality of the culture medium, with a maximum value of 3,200 mg/L obtained at 500 mOsm/kg. Component C was also produced in proportion to the osmolality. Conversion of acarbose to component C was accomplished with resting whole cells. Inhibitors of the conversion of acarbose to component C were sought since component C is probably derived from acarbose. Valienamine was found to be a potent inhibitor, resulting in a more than 90% reduction in component C formation at a 10 microM concentration. Effects were similar in a 1,500-L pilot fermentor with acarbose and component C yields of 3,490 and 43 mg/L at 500 mOsm/kg, respectively.     

A new RNASeq-based reference transcriptome for sugar beet and its application in transcriptome-scale analysis of vernalization and gibberellin responses

Background

Actinoplanes sp. SE50/110 is known as the wild type producer of the alpha-glucosidase inhibitor acarbose, a potent drug used worldwide in the treatment of type-2 diabetes mellitus. As the incidence of diabetes is rapidly rising worldwide, an ever increasing demand for diabetes drugs, such as acarbose, needs to be anticipated. Consequently, derived Actinoplanes strains with increased acarbose yields are being used in large scale industrial batch fermentation since 1990 and were continuously optimized by conventional mutagenesis and screening experiments. This strategy reached its limits and is generally superseded by modern genetic engineering approaches. As a prerequisite for targeted genetic modifications, the complete genome sequence of the organism has to be known.

Results

Here, we present the complete genome sequence of Actinoplanes sp. SE50/110 [GenBank:CP003170], the first publicly available genome of the genus Actinoplanes, comprising various producers of pharmaceutically and economically important secondary metabolites. The genome features a high mean G + C content of 71.32% and consists of one circular chromosome with a size of 9,239,851 bp hosting 8,270 predicted protein coding sequences. Phylogenetic analysis of the core genome revealed a rather distant relation to other sequenced species of the family Micromonosporaceae whereas Actinoplanes utahensis was found to be the closest species based on 16S rRNA gene sequence comparison. Besides the already published acarbose biosynthetic gene cluster sequence, several new non-ribosomal peptide synthetase-, polyketide synthase- and hybrid-clusters were identified on the Actinoplanes genome. Another key feature of the genome represents the discovery of a functional actinomycete integrative and conjugative element.

Conclusions

The complete genome sequence of Actinoplanes sp. SE50/110 marks an important step towards the rational genetic optimization of the acarbose production. In this regard, the identified actinomycete integrative and conjugative element could play a central role by providing the basis for the development of a genetic transformation system for Actinoplanes sp. SE50/110 and other Actinoplanes spp. Furthermore, the identified non-ribosomal peptide synthetase- and polyketide synthase-clusters potentially encode new antibiotics and/or other bioactive compounds, which might be of pharmacologic interest.     

An effective and simplified scale-up strategy for acarbose fermentation based on the carbon source control

The scale-up strategy for acarbose fermentation by Actinoplanes sp. A56 was explored in this paper. The results obtained in shake-flask cultivation demonstrated that the ratio of maltose and glucose had significant effects on the biosynthesis of acarbose, and the feeding medium containing 3:1 (mass ratio) of maltose and glucose was favorable for acarbose production. Then the correlation of the carbon source concentration with acarbose production was further investigated in 100-l fermenter, and the results showed that 7.5–8.0 g of total sugar/100 ml and 4.0–4.5 g of reducing sugar/100 ml were optimal for acarbose production. Based on the results in 100-l fermenter, an effective and simplified scale-up strategy was successfully established for acarbose fermentation in a 30-m³ fermenter, by using total sugar and reducing sugar as the scale-up parameter. As a result, 4,327 mg of acarbose/l was obtained at 168 h of fermentation.     

Effects of elevated pCO2 and osmolality on growth of CHO cells and production of antibody-fusion protein B1: a case study

Partial pressure of CO2 (pCO2) and osmolality as high as 150 mmHg and 440 mOsm/kg, respectively, were observed in large-scale CHO cell culture producing an antibody-fusion protein, B1. pCO2 and osmolality, when elevated to high levels in bioreactors, can adversely affect cell culture and recombinant protein production. To understand the sole impact of pCO2 or osmolality on CHO cell growth, experiments were performed in bench-scale bioreactors allowing one variable to change while controlling the other. Elevating pCO2 from 50 to 150 mmHg under controlled osmolality (about 350 mOsm/kg) resulted in a 9% reduction in specific cell growth rate. In contrast, increasing osmolality resulted in a linear reduction in specific cell growth rate (0.008 h(-1)/100 mOsm/kg) and led to a 60% decrease at 450 mOsm/kg as compared to the control at 316 mOsm/kg. This osmolality shift from 316 to 445 mOsm/kg resulted in an increase in specific production rates of lactate and ammonia by 43% and 48%, respectively. To elucidate the effect of high osmolality and/or pCO2 on the production phase, experiments were conducted in bench-scale bioreactors to more closely reflect the pCO2 and osmolality levels observed at large scale. Increasing osmolality to 400-450 mOsm/kg did not result in an obvious change in viable cell density and product titer. However, a further increase in osmolality to 460-500 mOsm/kg led to a 5% reduction in viable cell density and a 8% decrease in cell viability as compared to the control. Final titer was not affected as a result of an apparent increase in specific production rate under this increased osmolality. Furthermore, the combined effects from high pCO2 (140-160 mmHg) and osmolality (400-450 mOsm/kg) caused a 20% drop in viable cell density, a more prominent decrease as compared to elevated osmolality alone. Results obtained here illustrate the sole effect of high pCO2 (or osmolality) on CHO cell growth and demonstrate a distinct impact of high osmolality and/or pCO2 on production phase as compared to that on growth phase. These results are useful to understand the response of the CHO cells to elevated pCO2 (and/or osmolality) at a different stage of cultivation in bioreactors and thus are valuable in guiding bioreactor optimization toward improving protein production.     

In vivo and in vitro decolorization of synthetic dyes by laccase from solid state fermentation with Trametes sp. SYBC-L4

Synthetic decolorization of dyes through solid cassava residue substrate fermentation with Trametes sp. SYBC-L4 via in vivo and in vitro processes was investigated in this study. Effects of pH and mediator (1-hydroxybenzotriazole, HBT) concentration on dyes decolorization were evaluated. In vitro, decolorization ratios of dyes differed considerably in pH and increased with the increasing of HBT concentration. Crude laccase (50 U/L) derived from Trametes sp. SYBC-L4 decolorized 67.91 ± 1.25 % Congo red (100 mg/L), 94.58 ± 1.05 % aniline blue (100 mg/L) and 99.02 ± 0.54 % indigo carmine (100 mg/L) with 2.5 mM HBT at pH 4.5 in 36 h of incubation. In vivo, decolorization ratios of dyes were not enhanced by usage of the mediator. After 10 days of fermentation, decolorization ratio of Congo red (1,000 mg/kg), aniline blue (1,000 mg/kg) and indigo carmine (1,000 mg/kg) was 57.82 ± 0.84, 92.53 ± 1.12 and 97.26 ± 1.92 % without the usage of mediator at pH 4.5, respectively. Moreover, there was no obvious difference between the in vivo decolorization of aniline blue and indigo carmine in the pH range of 3.0–9.0. Results showed that Trametes sp. SYBC-L4 had great potential to be used for dyes decolorization via in vivo and in vitro processes. Moreover, in terms of pH range and mediator, in vivo decolorization with Trametes sp. SYBC-L4 was more advantageous since laccase mediator was needless and the applicable range of pH was broader.     

Effect of osmolality of skim-milk diluents and thawing rate on cryosurvival of ram spermatozoa

The effect of osmolality of skim-milk diluents (200, 320, 450, 600, and 750 mOsm/kg water) on the survival of ram spermatozoa frozen in straws were investigated after thawing in 39 °C water or in 20 °C air.Spermatozoa motility improved with increasing osmolality of the freezing diluent, irrespective of thawing rate. Diluents of 600 and 750 mOsm resulted in highest motility immediately after thawing and after 60 min incubation at 39 °C. A significant decrease in spermatozoa motility was observed when straws were thawed at 20 °C air with the magnitude of decrease inversely related to osmolality of the freezing diluent. Fertility of progestagen synchronized ewes inseminated with semen frozen in the 600 mOsm hypertonic skim-milk diluent was comparable to that obtained with fresh semen.     

Survival,haemolymph osmolality and tissue water of Penaeus chinensis juveniles acclimated to different salinity and temperature levels

Survival, growth, haemolymph osmolality and tissue water of Penaeus chinensis (Osbeck) juveniles (0.11 ± 0.04 g) were investigated, after they were acclimated to 10, 20, 30 and 40 ppt from 33 ppt for 14 days at 24°C, and then acclimated to 12, 18, 24 and 30°C at each salinity for 14 days. The survival of shrimp was the lowest at 10 ppt and 12°C. Growth of shrimp increased with increased temperature in the range 12–24°C, with no significant difference among four salinity levels at 18, 24 and 30°C. Haemolymph osmolality increased with increased salinity, and decreased with increased temperature. The isosmotic point computed from the linear relationship between haemolymph osmolality and medium osmolality was 664, 632, 629 and 602 mOsm/kg which is equivalent to 25.2, 24.1, 24.0 and 23.1 ppt at 12, 18, 24 and 30°C, respectively. Tissue water decreased with increased medium osmolality and haemolymph osmolality. The slope obtained from the relationship between haemolymph osmolality and medium osmolality indicated that there is an impairment of osmoregulatory ability for the P. chinensis juveniles at 12°C.     

Three trehalose synthetic pathways in the acarbose-producing Actinoplanes sp. SN223/29 and evidence for the TreY role in biosynthesis of component C

In this study, three trehalose gene clusters, treX-Y-Z, tpS1, and treS, of the acarbose-producing strain, Actinoplanes sp. SN223/29, have been identified. In particular, five trehalose synthetic genes were sequenced and characterized in detail. They were cloned and expressed in Escherichia coli BL21(DE3)pLysS using the His-tag vector pET19b. The recombinant proteins were purified by Ni²⁺-nitrilotriacetic acid agarose affinity chromatography, and their functions were characterized biochemically. Both the maltooligosyltrehalose synthase (TreY–TreZ) pathway and the trehalose synthase (TreS) pathway have maximum activity at 40°C and at pH 7.5 and 7.0, respectively, in 100-mM phosphate buffer. Meanwhile, the trehalose-6-phosphate synthase (TpS1) showed maximum activity at 35°C and at pH 7.5 in 100 mM Tris–HCl. As a cofactor candidate, Mg²⁺ enhanced the activities of all three trehalose synthetic reactions significantly. TreY produced component C from acarbose by its proposed isomerase activity, but TreS did not. This study suggests that the mutation of treY can improve acarbose production by repressing component C production. Based on the data obtained in this study, a model for component C production in Actinoplanes sp. SN 223/29 is proposed.     

Sperm motility initiation and duration in a euryhaline fish, medaka (Oryzias latipes)

The medaka, Oryzias latipes, is a well-recognized fish model for biomedical research. An understanding of gamete characteristics is necessary for experimental manipulations such as artificial fertilization and sperm cryopreservation. The goal of this study was to investigate sperm characteristics of motility initiation, duration, and retention in medaka. First, motility was initiated by osmolality values ranging from 25 to 686 mOsm/kg, which included deionized water and hypotonic, isotonic, and hypertonic Hanks’ balanced salt solution. The percentage of motile sperm was >80% when osmolality was <315 mOsm/kg and decreased as osmolality increased. This is different from most fish with external fertilization in which sperm motility can be initiated by hypotonic (for freshwater fish) or hypertonic (for marine fish) solutions or by altering the concentration of specific ions such as potassium (e.g., in salmonids). Second, upon activation, the sperm remained continuously motile, with reserve capacity, for as long as 1 wk during storage at 4 °C. This was also different from other externally fertilizing fish, in which motility is typically maintained for seconds to several minutes. Third, after changing the osmolality to 46 to 68 mOsm/kg by adding deionized water, the motility of sperm held at 274 to 500 mOsm/kg was higher than the original motility (P ≤ 0.035) after 24, 48, and 72 h of storage at 4 °C. Fourth, the addition of glucose had no effect on maintaining sperm motility during refrigerated storage. To our knowledge, this combination of sperm motility characteristics is reported for the first time in fish and may be unique to medaka or may represent an undescribed modality of sperm behavior within euryhaline fish.     

Use of NaCl prevents aggregation of recombinant COMP–Angiopoietin-1 in Chinese hamster ovary cells

To investigate the effect of hyperosmotic medium on production and aggregation of the variant of Angiopoietin-1 (Ang1), cartilage oligomeric matrix protein (COMP)–Ang1, in recombinant Chinese hamster ovary (CHO) cells, CHO cells were cultivated in shaking flasks. NaCl and/or sorbitol were used to raise medium osmolality in the range of 300–450 mOsm/kg. The specific productivity of COMP–Ang1, q_COMP–Ang1, increased as medium osmolality increased. At NaCl-450 mOsm/kg, the q_COMP–Ang1 was 7.7-fold higher than that at NaCl-300 mOsm/kg, while, at sorbitol-450 mOsm/kg, it was 2.9-fold higher than that at sorbitol-300 mOsm/kg. This can be attributed to the increased relative mRNA level of COMP–Ang1 at NaCl-450 mOsm/kg which was approximately 2.4-fold higher than that at sorbitol-450 mOsm/kg. Western blot analysis showed that COMP–Ang1 aggregates started to occur in the late-exponential phase of cell growth. When sorbitol was used to raise the medium osmolality, a severe aggregation of COMP–Ang1 was observed. On the other hand, when NaCl was used, the aggregation of COMP–Ang1 was drastically reduced at NaCl-400 mOsm/kg. At NaCl-450 mOsm/kg, the aggregation of COMP–Ang1 was hardly observed. This suggests that environmental conditions are critical for the aggregation of COMP–Ang1. Taken together, the use of NaCl-induced hyperosmotic medium to cell culture process turns out to be an efficient strategy for enhancing COMP–Ang1 production and reducing COMP–Ang1 aggregation.     

l-Lactic acid production benefits from reduction of environmental osmotic stress through neutralizing agent combination

This paper hinged on the combination effect of two different neutralizing agents Ca(OH)₂ and NH₄OH on the production of l-lactic acid by Lactobacillus paracasei. Present study quantitatively indicated that environmental osmotic pressure (844–1,772 mOsm/kg) exerted minor influence on l-lactic acid production, but a critical level fell on approximately 3,000 mOsm/kg which restricted l-lactic acid production significantly. Once osmotic pressure exceeded 3,600 mOsm/kg, l-lactic acid production ran aground. A new and efficient neutralizing agent-adding strategy was established in this study to procure 2.21-fold enhancement (5.94 g/l/h) relative to previous productivity of l-lactic acid with NH₄OH as neutralizing agent via batch cultivation. It was, therefore, speculated that inhibition effect in the late phase of the fermentation might be in large part attributed to the dramatic increase of environmental osmotic stress, other than cumulative effect of lactate concentration itself.     

Overproduction of poly(β-malic acid) (PMA) from glucose by a novel Aureobasidium sp. P6 strain isolated from mangrove system

After over 100 strains of Aureobasidium spp isolated from mangrove system were screened for their ability to produce poly(β-malic acid) (PMA), it was found that Aureobasidium sp. P6 strain among them could produce high level of Ca²⁺-PMA. Fourteen percent glucose and 6.5 % CaCO₃ in the medium were the most suitable for Ca²⁺-PMA production. Then, 100.7 g/l of Ca²⁺-PMA was produced using Aureobasidium sp. P6 strain within 168 h at flask level. During 10-l batch fermentation, when the medium contained 12.0 % glucose, 98.7 g/l of Ca²⁺-PMA in the culture and 14.7 g/l of cell dry weight were obtained within 156 h, leaving 0.34 % reducing sugar in the fermented medium. When glucose concentration in the fermentation medium was 14.0 %, 118.3 g/l of Ca²⁺-PMA in the culture and 16.4 g/l of cell dry weight were obtained within 168 h, leaving 0.4 % reducing sugar in the fermented medium. After purification of Ca²⁺-PMA from the culture and acid hydrolysis of the pure Ca²⁺-PMA, analysis of HPLC showed that Aureobasidium sp. P6 strain only produced two main components of Ca²⁺-PMA and minor amount of calcium malate and that the hydrolysate of PMA was mainly composed of calcium malate. This is the first time to report that the novel yeast strain Aureobasidium sp. P6 strain isolated from the mangrove systems can produce such high amount of Ca²⁺-PMA.     

Enhancement of electricity production in a mediatorless air–cathode microbial fuel cell using <Emphasis Type="Italic">Klebsiella</Emphasis> sp. IR21

A novel dissimilatory iron-reducing bacteria, Klebsiella sp. IR21, was isolated from the anode biofilm of an MFC reactor. Klebsiella sp. IR21 reduced 27.8 % of ferric iron to ferrous iron demonstrating that Klebsiella sp. IR21 has electron transfer ability. Additionally, Klebsiella sp. IR21 generated electricity forming a biofilm on the anode surface. When a pure culture of Klebsiella sp. IR21 was supplied into a single chamber, air–cathode MFC fed with a mixture of glucose and acetate (500 mg L^?1 COD), 40–60 mV of voltage (17–26 mA m^?2 of current density) was produced. Klebsiella sp. IR21 was also utilized as a biocatalyst to improve the electrical performance of a conventional MFC reactor. A single chamber, air–cathode MFC was fed with reject wastewater (10,000 mg L^?1 COD) from a H₂ fermentation reactor. The average voltage, current density, and power density were 142.9 ± 25.74 mV, 60.5 ± 11.61 mA m^?2, and 8.9 ± 3.65 mW m^?2, respectively, in the MFC without inoculation of Klebsiella sp. IR21. However, these electrical performances of the MFC were significantly increased to 204.7 ± 40.24 mV, 87.5 ± 17.20 mA m^?2, and 18.6 ± 7.23 mW m^?2, respectively, with inoculation of Klebsiella sp. IR21. The results indicate that Klebsiella sp. IR21 can be utilized as a biocatalyst for enhancement of electrical performance in MFC systems.     

Effect of polyphenols extracted from tamarind (Tamarindus indica L.) seed coat on pathophysiological changes and red blood cell glutathione peroxidase activity in heat-stressed broilers

The purpose of this study was to determine the effect of polyphenols extracted from the tamarind seed coat (PETSC) on glutathione peroxidase (GPx) activity, red blood cell parameters and bilirubin in heat-stressed broilers. One hundred forty-seven broilers, 18-days old were divided into two groups. In group 1, broilers were maintained at an environmental temperature of 26?±?2 °C throughout the experimental period. In group 2, the broilers were maintained at 38?±?2 °C (cyclic temperature: 26?±?2 °C; ?38?±?2 °C; and ?26?±?2 °C, and broilers were maintained at 38?±?2 °C for 6 h/ day) and received PETSC at a concentration of 0, 100, 200, 300, 400 or 500 mg/kg in their diet ad libitum. Parameters were investigated on days 1, 7, 14 and 21 of the experimental period. Results showed that GPx activity of heat-stressed broilers that received 100 mg/kg of PETSC in their diet was lower (P?<?0.05) than that in broilers fed the other concentrations. The mean total red blood cell count and hemoglobin concentration of heat-stressed broilers that received 100 mg/kg PETSC was higher (P?<?0.05) than those in broilers in group 1 and those fed the other concentrations. The mean bilirubin level in the excreta of heat-stressed broilers that received 100 mg/kg of PETSC was lower (P?<?0.05) than that in broilers that received 0, 300, 400 and 500 mg/kg of PETSC. This showed that PETSC could reduce GPx activity and bilirubin in feces, and increase red blood cell parameters in heat-stressed broilers.     

Production of novel alkalitolerant and thermostable inulinase from marine actinomycete Nocardiopsis sp. DN-K15 and inulin hydrolysis by the enzyme

An actinomycete strain Nocardiopsis sp. DN-K15 showing high inulinolytic activity was isolated from marine sediment of Jiaozhou Bay in China. Under optimal conditions, Nocardiopsis sp. DN-K15 produced 25.1 U/ml of inulinase within 60 h of fermentation at shake flask level, which was 2.7-fold higher than the level in the basal medium. The optimal pH and temperature of the inulinase from strain DN-K15 were determined to be 60 °C and pH 8.0, respectively. The inulinase was highly active over a wide pH range (5.0–11.0) and retained more than 81 % of residual activity after incubation at 60 °C for 1 h, indicating its alkali-tolerant and thermostable nature. Thin layer chromatography analysis revealed that fructose was the main product of inulin hydrolysis, indicating its exoinulinase activity. The high yield of extracellular inulinase combined with its novel enzymatic property made Nocardiopsis sp. DN-K15 a potential candidate in biotechnological and industrial applications.     

Bioprospecting of thermo- and osmo-tolerant fungi from mango pulp–peel compost for bioethanol production

The persistent edaphic stress on microbial succession due to dynamic changes during composting was explored for selection of multi-stress tolerant microbe(s) desirable for ethanol production. A total of 23 strains were isolated from mango compost using four successive enrichments in YP broth (g l^?1): glucose, 100; 150; 250 with ethanol (40) and cycloheximide (0.4) at 40 °C, pH 6.0. Based on multi-gene ribotyping, 14 yeasts (61 %) of Saccharomycetaceae, 2 filamentous fungi (8.6 %) and 7 bacteria (30.4 %) were obtained. Phenetic and phylogenetic analysis of the 14 yeasts revealed 64.3 % tolerant to 500 g l^?1 glucose, growth at 45 °C and resemblance to Candida sp. (14.3 %), Kluyveromyces marxianus (35.7 %), Pichia kudriavzevii (21.4 %) and Saccharomyces cerevisiae (28.6 %). Assessment of the 14 yeasts in glucose fermentation medium (pH 4.5 at 40 °C) showed ethanol productivity of ≥92 % by 12 yeasts with theoretical yields of 90–97 %. Fermentation of molasses (150 g l^?1 glucose equivalent) by P. kudriavzevii D1C at 40 °C resulted in 73.70 ± 0.02 g l^?1 ethanol and productivity of 4.91 ± 0.01 g l^?1 h^?1. Assessment of P. kudriavzevii D1C revealed multi-stress tolerance towards 5-hydroxymethyl furfural, ethanol (20 %, v/v), high gravity and H₂O₂ (0.3 M) indicating suitability for ethanol production using high gravity molasses and pre-treated lignocellulosic biomass fermentation.     

A novel structured bioreactor for solid-state fermentation

A novel patented solid-state bioreactor (251 L) with honeycomb loading device was designed and its performance was tested. First, this apparatus gave a 66.87 % of calculated loading coefficient (volume ratio), which was almost twofold compared with conventional fermenters. Next, considering the crucial effect of heat transfer on bed loading and microbial growth, the performance was validated by temperature variance during fermentation and spore viability of Bacillus cereus DM423. Air pressure pulsation or external water jacket was used to control temperature; the maximal temperature variation was 7.7 versus 19.8 °C, respectively during fermentation. The difference was mainly due to the continuous gas phase characterized by solid-state fermentation (SSF). The average living spores of (1.50 ± 0.07) × 10¹¹ cfu/g at 40 h obtained from the device was higher than (0.70 ± 0.03) × 10¹¹ cfu/g from flask at 48 h. The results indicated that this new loading bioreactor with air pressure pulsation could be a good prospect for industrialization of SSF employing bacterial cultures.     

Production, statistical optimization and application of endoglucanase from Rhizopus stolonifer utilizing coffee husk

Coffee cherry husk (CH) is one of the major by-products obtained from coffee processing industry and accounts to 43 ± 5.9 % of cellulose. Screening of fungal organism for cellulase production was carried out and the potential organism was identified as Rhizopus stolonifer by internal transcribed spacer’s (ITS)—5.8S rDNA analysis. A systematic study with response surface methodology (RSM) based on CCRD was used to study the interactions among the variables such as pH (3–7), moisture (40–80 %) and progression duration (72–168 h) of the fermentation process to maximize the enzyme production. Under the optimized cultivation condition, R. stolonifer synthesized 22,109 U/gds. Model validations at optimum operating conditions showed excellent agreement between the experimental results and the predicted responses with a confidence level of 95 %. Endoglucanase thus produced was utilized for ethanol production by simultaneous saccharification and fermentation and maximum of 65.5 g/L of ethanol was obtained. This fungal cellulase has also reported to be efficient detergent additives and promising for commercial use. The present study demonstrates coffee husk as a significant bioprocess substrate. Statistical optimization with major parameters for cellulase production can be highly applicable for industrial scale. Furthermore, value addition to coffee husk with sustainable waste management leading to environment conservation can be achieved.