Increased intracellular levels of Ca²⁺ are generally thought to negatively regulate lipolysis in mature adipocytes, whereas store-operated Ca²⁺ entry was recently reported to facilitate lipolysis and attenuate lipotoxicity by inducing lipophagy. Transient receptor potential mucolipin1 (TRPML1), a Ca²⁺-permeable non-selective cation channel, is mainly expressed on the lysosomal membrane and plays key roles in lysosomal homeostasis and membrane trafficking. However, the roles of TRPML1 in lipolysis remains unclear. In this study, we examined whether the channel function of TRPML1 induces lipolysis in mature adipocytes. We found that treatment of mature adipocytes with ML-SA1, a specific agonist of TRPML1, solely upregulated extracellular glycerol release, but not to the same extent as isoproterenol. In addition, knockdown of TRPML1 in mature adipocytes significantly reduced autophagic flux, regardless of ML-SA1 treatment. Our findings demonstrate that the channel function of TRPML1 partially contributes to lipid metabolism and autophagic membrane trafficking, suggesting that TRPML1, particularly the channel function of TRPML1, is as therapeutic target molecule for treating obesity.
Adipocytes ; Glycerol ; Homeostasis ; Isoproterenol ; Lipid Metabolism ; Lipolysis ; Membranes ; Obesity

Aquaporin-9 (AQP9) is a membrane-span transport protein expressed in the liver. It is located in the cytoplasm membrane of hepatic cells. In addition to water, it is also permeable to glycerol, urea, and other small solutes. Several evidences have revealed that AQP9 is involved in multiple physiological and pathological process of the liver. This paper summarized the expression of AQP9 in the liver and the effect on the physiological and pathological processes of the liver. AQP9 may be defined as a novel target for diagnosis and treatment of hepatic diseases.
Aquaporins ; metabolism ; Cell Membrane ; metabolism ; Glycerol ; Hepatocytes ; metabolism ; Humans ; Liver ; metabolism ; Urea

By using some intermediate metabolites in EMP pathway and TCA cycle as the control, the effects of amino acid supplements on glycerol production by Candida glycerinogenes in shake-flask fermentations with urea as nitrogen resource were investigated. The results showed that ten kinds of amino acids, including L-glutamic acid, L-glutamine, L-aspartic acid, L-asparagine, L-glycin, L-lysine, L-tyrosine, L-proline, L-histidine, and L-serine, had strong promotional effects on glycerol production; The optimal concentrations of these amino acids were 0.40, 0.45, 0.36, 0.35, 0.39, 0.36, 0.35, 0.45, 0.26, and 0.45 g/L, respectively. Accordingly the optimum contents of pyruvic acid, a-oxoglutarate, oxaloacetic acid, citrate, and succinate were 0.24, 0.42, 0.40, 0.37, and 0.38 g/L, respectively. The advantageous opportunities of supplement were as follows: L-lysine at the beginning of fermentation; pyruvic acid and oxaloacetic acid at the fourteenth hour; L-glutamic acid, L-glutamine, L-histidine, L-proline, L-aspartic acid, L-tyrosine, L-glycin, alpha-oxoglutarate, and succinate at the thirtieth hour; and L-asparagine, L-serine, and citrate at the forty-eighth hour. The addition of each stimulant at the optimal conditions could significantly promote glycerol production, with the glycerol yield on initial glucose and its increased speed exceeding 60% and 16%, respectively. The possible stimulatory mechanism due to the amino acid supplements is that the increased intermediate metabolites levels from amino acids degradation may have enhanced the flux through TCA cycle, which improve cell energetics. Meanwhile, the shift of carbon metabolism flux at the glyceraldhyde-3-phosphate node can result in the incremental flux through glycerol biosynthesis pathway.
Amino Acids ; metabolism ; Candida ; growth & development ; metabolism ; Culture Media ; Dose-Response Relationship, Drug ; Fermentation ; Glycerol ; metabolism

Enzymatic esterification by reacting caparic acid with glycerol in solvent-free system was studied. Lipases from Pseudomonas fluoresces(PFL), Mucor miehei(MML) and Candida antarictica(CAL) possessed good catalytic activity. The optimal reaction conditions to convert capric acid with CAL are: 60 degrees C, 20-100 u of CAL per gram capric acid, 12% (W/W) of initial water content in glycerol. CAL does not express its 1,3-specificity in final product. Mechanical fraying denatured CAL partly. 96.4% of catalytic activity of CAL recovered after 5 batches of reaction. Extraction with sodium carbonate solution can decrease acid value of product from 9.8 mg KOH/g to 0.68 mg KOH/g. Applying the enzymatic esterification in open system, under vacuum or dehydrating with molecular sieves all dehydrate effectively. Molar ratio of reactants does not influence the total conversion of capric acid but influences the yield of monoglyceride. With certain protocols, the reaction period could be shortened dramatically; conversion of capric acid reached 96.9% in 5 h.
Catalysis ; Decanoic Acids ; isolation & purification ; metabolism ; Glycerol ; isolation & purification ; metabolism ; Lipase ; metabolism

1,3-propanediol is an important raw material in chemical industry. Microbial conversion of glycerol or glucose into 1,3-propanediol has been given much attention due to its renewable resource, mild reaction conditions, and other advantages. It is a challenge to efficiently separate 1,3-propanediol from a mixture of multiple components, such as 1,3-propanediol, 2,3-butanediol, water, residual glycerol, ethanol, macromolecules and salts, for the reason that 1,3-propanediol, glycerol and 2,3-butanediol are all very hydrophilic and have intense polarity. The conventional evaporation and distillation techniques used in the purification of 1,3-propanediol suffer from the problem of high energy consumption and low recovery. It makes the recovery of 1,3-propanediol from a fermentation broth become a bottleneck in industrial production. The down-stream processing of biologically produced 1,3-propanediol mainly includes the removal of protein, salts, water and other impurities. This paper analyze the research progress of these separation technologies and point out the developing direction worth further investigation.
Fermentation ; Glucose ; metabolism ; Glycerol ; metabolism ; Industrial Microbiology ; methods ; Propylene Glycols ; isolation & purification ; metabolism

Glucose oxidase (GOD) is an important industrial enzyme with many potential applications. In order to increase the production and productivity of GOD by recombinant Pichia pastoris GS115, we investigated the feeding strategies of mixed carbon sources during induction phase, based on results of the optimization of initial cell and methanol concentration on GOD production. The optimal initial cell and methanol concentration were 100 g/L and 18 g/L. During induction phase, the mixed-carbon-sources strategies showed that glycerol, sorbitol or mannitol co-feeding with methanol could enhance GOD production. With mannitol co-feeding (20:1(W/W)), the maximum GOD production and maximum GOD productivity reached 711.3 U/mL and 4.60 U/(mL x h) after an induction period of 156 h. Compared to the control, the enhancements of GOD production and productivity were 66.3% and 67.9%, respectively. Meanwhile, we found an appropriate mannitol co-feeding strategy that would not inhibit the expression of promote. The activity of alcohol oxidase was 8.8 U/g, which was enhanced by 69.2% compared to the control (5.2 U/g). We can use the same optimization process to improve the production of other proteins from recombinant Pichia pastoris by changing the fermentation parameters.
Carbon ; metabolism ; Fermentation ; Glucose Oxidase ; biosynthesis ; Glycerol ; metabolism ; Industrial Microbiology ; Mannitol ; metabolism ; Methanol ; metabolism ; Pichia ; metabolism ; Sorbitol ; metabolism

A recombinant strain of Pichia pastoris with a phenotype of Muts was used to produce angiostatin in a 5-L fermentor. The methanol utilization ability of the present strain was weak, which resulted in extremely low growth rate and angiostatin productivity during the expression phase with methanol as the sole carbon source. To enhance the cell density and angiostatin expression level, mixed-carbon-source of glycerol-methanol was used in the expression phase. The methanol concentration was well controlled at 5 g/L by a methanol sensor and control system, and glycerol was continuously fed into the fermentor to achieve a higher cell density. 120 g/L of cells and 39 mg/L of angiostatin were reached at the end of fermentation which lasted 110 h. The mean specific cell growth rate in the expression phase was 0.01 h(-1), and the mean specific angiostatin productivity was 0.006 mg/(g x h). According to the data obtained in several runs of fermentation in which glycerol was fed at different rates, a higher mean specific angiostatin productivity was reached at the mean specific cell growth rate of 0.012 h(-1). To avoid the repression of angiostatin expression caused by residual glycerol and ethanol accumulation due to overfeeding of glycerol, glycerol addition was controlled to produce continuous oscillations in dissolved oxygen, because the change of dissolved oxygen concentration could deliver the information of available carbon source in the fermentation broth. Controlled glycerol feeding also avoided the problem of oxygen limitation brought by high cell density, and thus decreased the cooling requirement of the fermentor. Cell density reached 150 g/L at the end of fermentation, and angiostatin level reached 108 mg/L after an expression period of 96 h when the mean specific growth rate was maintained at 0.012 h(-1) by using the glycerol feeding strategy to result in the oscillations in dissolved oxygen. The mean specific angiostatin productivity was improved to 0.02 mg/(g x h). The apparent cell yield on glycerol and methanol were respectively 0.69 g/g and 0.93 g/g, higher than those in the fermentation without using the feeding strategy with dissolved oxygen as the indicator of metabolism.
Angiostatins ; genetics ; metabolism ; physiology ; Biotechnology ; methods ; Carbon ; metabolism ; Fermentation ; physiology ; Glycerol ; metabolism ; Methanol ; metabolism ; Oxygen ; metabolism ; Pichia ; genetics ; metabolism

To study the roles of glucosylglycerol phosphate synthase (Ggps) in glucosylglycerol (GG) and glycerol biosynthesis, we over-expressed Ggps from either Synechocystis sp. PCC 6803 or Synechococcus sp. PCC 7002 in a Synechocystis strain with a high GG titer, and determined the GG and glycerol accumulation in the resultant mutants grown under different NaCl-stress conditions. Ion chromatography results revealed that GG yield was not improved, but glycerol production was significantly enhanced by over-expression of Ggps from Synechocystis sp. PCC 6803 (6803ggpS). In addition, increasing the NaCl concentration of medium from 600 to 900 mmol/L led to a further 75% increase of glycerol accumulation in the mutant strain with 6803ggpS over-expression. These findings show the role of ggpS in driving the carbon flux to the glycerol biosynthesis pathway, and will be helpful for further improvement of GG and glycerol production in Synechocystis.
Bacterial Proteins ; metabolism ; Culture Media ; Glucosides ; biosynthesis ; Glucosyltransferases ; metabolism ; Glycerol ; metabolism ; Industrial Microbiology ; Sodium Chloride ; Synechococcus ; enzymology ; Synechocystis ; enzymology ; metabolism

Enzymatic synthesis of monoglycerides by glycerolysis of oil and fats in microaqueous solvent-free media was investigated by using lipase from pseudomonus fluorescens (PFL). Initial eutectic point(IEP) was substituted for melt point of oil and fats in Critical Temperature Theory. By investigating the glycerolysis under different IEP, it is showed that there is a relationship between composition of the oils and the yield of monoglycerides: Y = -0.0006 X3 + 0.0592 X2 - 0.8909 X + 26.753(13% < X < 76.5%), here X is the contents(W/W) of saturated fatty acid residue (C16 + C18) in the oils, Y is the yield of monoglycerides at 40 degrees C. The optimum isothermal reaction conditions for a system which IEP is 40 degrees C are: 40 degrees C, 3%-4.5% (W/W) water in glycerol, dosage of lipase is 500 u/g oil when the mole ratio of glycerol to oil is 2.5:1. The highest yield of monoglycerides is 81.4% in 48 h by means of programming temperature reaction.
Glycerides ; metabolism ; Glycerol ; metabolism ; Kinetics ; Lipase ; metabolism ; Palm Oil ; Plant Oils ; metabolism ; Pseudomonas fluorescens ; enzymology ; Substrate Specificity ; Temperature

1,3-propanediol is an important chemical used as building block for the synthesis of highly promising polyesters such as polytrimethylene terephthalate. A genetically modified Klebsiella pneumoniae LDH526 can use glycerol as sole carbon source and produce 1,3-propanediol with the titer above 90 g/L. A key factor affecting the production of 1,3-propanediol by the mutant K. pneumoniae is the accurate control of the feeding of glycerol. To generate a robust and reproducible fermentation process of 1,3-propanediol, we designed and optimized an automatically feeding strategy of glycerol based on fermentation kinetics. By coupling the substrate feeding rate with easily observed variables -pH and fermentation time, we have achieved self-starting glycerol feeding and dynamic control of the glycerol concentration during the fermentation process. This automated system allowed us to generate a reproducible, consistent and operator-independent process from lab-scale to production scale. The final concentration of 1,3-propanediol was above 95 g/L after 72 h.
Culture Media ; Fermentation ; Glycerol ; Industrial Microbiology ; methods ; Klebsiella pneumoniae ; growth & development ; Propylene Glycol ; Propylene Glycols ; metabolism