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Engineering aspects of the production of sugar alcohols with the osmophilic yeast Moniliella tomentosa var pollinis. Part Ⅰ. Batch and fed-batch operation in stirred tank

机译:渗透性酵母莫尼利氏菌(Moniliella tomentosa var pollinis)生产糖醇的工程方面。第一部分。搅拌釜中的分批和补料分批操作

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Moniliella tomentosa var pollinis was cultivated on complex medium consisting of glucose as carbon source, urea, (NH_4)_2SO_4, corn steep liquor and yeast extract as nitrogen sources, respectively. The pH and the concentrations of (dry) cell mass, glucose, erythritol, ribitol, glycerol, disaccharides, trisaccharides, polysaccharides, amino acids in medium, oxygen and carbon dioxide in off-gas were monitored during cultivation. Rates of growth, substrate uptake and production, yields and yield coefficients as well as OUR, CPR and RQ were evaluated with different medium composition and operating conditions in a 30 1 stirred tank by batch and fed-batch operation. At high substrate concentrations in batch operation high (dry) cell mass concentrations (65 g l~(-1)), high erythritol concentrations (90 g l~(-1)) erythritol yield (36%) and yield coefficients (0.35 g g~(-1)) as well as polyol concentrations (150 g l~(-1)) polyol yield (62%) and yield coefficients (0.65 g g~(-1)) were obtained under optimal conditions. With fed-batch operation better results were obtained: high (dry) cell mass concentrations (up to 116 g l~(-1)), high erythritol concentrations (up to 170 g l~(-1)), polyol concentrations (up to 188 g l~(-1)) were obtained under optimal conditions. Under oxygen limitation ethanol was formed, and under nitrogen limitation foam formation impaired the production process. By suitable aeration and a fed-batch process using a mixture of glucose and nitrogen source for feeding, ethanol and foam formation could be reduced and eliminated, respectively.
机译:在复合培养基上分别培养了毛白粉虫(Moniliella tomentosa var pollinis),该复合培养基由葡萄糖为碳源,尿素,(NH_4)_2SO_4,玉米浆和酵母提取物为氮源组成。在培养过程中监测pH值和(干)细胞团,葡萄糖,赤藓糖醇,核糖醇,甘油,二糖,三糖,多糖,培养基中的氨基酸,废气中的氧气和二氧化碳的浓度。在30 1搅拌釜中,通过分批和补料分批操作,在不同的培养基组成和操作条件下,评估了生长速率,底物吸收和产量,产量和产量系数以及OUR,CPR和RQ。在分批操作中高底物浓度下,干细胞质量浓度高(65 gl〜(-1)),赤藓糖醇浓度高(90 gl〜(-1))赤藓糖醇收率(36%)和产量系数(0.35 gg〜( -1))和多元醇浓度(150 gl〜(-1))在最佳条件下可获得多元醇收率(62%)和收率系数(0.65 gg〜(-1))。使用分批补料操作可获得更好的结果:高(干)细胞质量浓度(高达116 gl〜(-1)),高赤藓糖醇浓度(高达170 gl〜(-1)),多元醇浓度(高达188)在最佳条件下获得了gl〜(-1))。在氧限制下形成乙醇,而在氮限制下形成泡沫损害了生产过程。通过适当的曝气和使用葡萄糖和氮源的混合物进行补料分批进料的工艺,可以分别减少和消除乙醇和泡沫的形成。

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