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Eng Life Sci. 2017 Aug 21;17(12):1234-1243. doi: 10.1002/elsc.201700099. eCollection 2017 Dec.
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本文引用的文献

1
Microbial high cell density fermentations in a stirred single-use bioreactor.搅拌式一次性生物反应器中的微生物高密度发酵。
Adv Biochem Eng Biotechnol. 2014;138:127-47. doi: 10.1007/10_2013_189.
2
Comparison of two methods for designing calorimeters using stirred tank reactors.两种利用搅拌槽式反应器设计量热器的方法比较。
Biotechnol Bioeng. 2013 Jan;110(1):180-90. doi: 10.1002/bit.24601. Epub 2012 Jul 25.
3
Calorimetric control for high cell density cultivation of a recombinant Escherichia coli strain.热计量控制用于重组大肠杆菌菌株的高密度培养。
J Biotechnol. 2010 Mar;146(1-2):45-53. doi: 10.1016/j.jbiotec.2010.01.004. Epub 2010 Jan 18.
4
Calorimetric bioprocess monitoring by small modifications to a standard bench-scale bioreactor.通过对标准台式生物反应器进行微小改动实现量热法生物过程监测。
J Biotechnol. 2007 May 31;130(1):24-31. doi: 10.1016/j.jbiotec.2007.02.013. Epub 2007 Feb 25.
5
Development of a large-scale biocalorimeter to monitor and control bioprocesses.用于监测和控制生物过程的大型生物量热计的开发。
Biotechnol Bioeng. 2002 Oct 20;80(2):125-38. doi: 10.1002/bit.10351.
6
Aeration without air: oxygen supply by hydrogen peroxide.无空气曝气:过氧化氢供氧
Biotechnol Bioeng. 1977 Mar;19(3):413-24. doi: 10.1002/bit.260190311.

通过过氧化氢的衰减测量搅拌式一次性生物反应器中的传热系数。

Measurement of heat transfer coefficients in stirred single-use bioreactors by the decay of hydrogen peroxide.

作者信息

Müller Matthias, Meusel Wolfram, Husemann Ute, Greller Gerhard, Kraume Matthias

机构信息

Hochschule Anhalt Köthen Germany.

Sartorius Stedim Biotech GmbH Göttingen Germany.

出版信息

Eng Life Sci. 2017 Aug 21;17(12):1234-1243. doi: 10.1002/elsc.201700099. eCollection 2017 Dec.

DOI:10.1002/elsc.201700099
PMID:32624751
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC6999534/
Abstract

Single-use bioreactors are barely described by means of their heat transfer characteristics, although some of their properties might affect this process. Steady-state methods that use external heat sources enable precise investigations. One option, commonly present in stirred, stainless steel tanks, is to use adjustable electrical heaters. An alternative are exothermic chemical reactions that offer a higher flexibility and scalability. Here, the catalytic decay of hydrogen peroxide was considered a possible reaction, because of the high reaction enthalpy of -98.2 kJ/mole and its uncritical reaction products. To establish the reaction, a proper catalyst needed to be determined upfront. Three candidates were screened: catalase, iron(III)-nitrate and manganese(IV)-oxide. Whilst catalase showed strong inactivation kinetic and general instability and iron(III)-nitrate solution has a pH of 2, it was decided to use manganese(IV)-oxide for the bioreactor studies. First, a comparison between electrical and chemical power input in a benchtop glass bioreactor of 3.5 L showed good agreement. Afterwards the method was transferred to a 50 L stirred single-use bioreactor. The deviation in the final results was acceptable. The heat transfer coefficient for the electrical method was 242 W/m/K, while the value achieved with the chemical differed by less than 5%. Finally, experiments were carried out in a 200 L single-use bioreactor proving the applicability of the chemical power input at technical relevant scales.

摘要

一次性生物反应器很少通过其传热特性来描述,尽管它们的一些特性可能会影响这一过程。使用外部热源的稳态方法能够进行精确研究。一种常见于搅拌不锈钢罐中的选择是使用可调电加热器。另一种选择是放热化学反应,其具有更高的灵活性和可扩展性。在此,过氧化氢的催化分解被认为是一种可能的反应,因为其反应焓高达-98.2千焦/摩尔,且反应产物无害。为了实现该反应,需要预先确定合适的催化剂。筛选了三种候选催化剂:过氧化氢酶、硝酸铁(III)和二氧化锰(IV)。由于过氧化氢酶表现出强烈的失活动力学和普遍的不稳定性,且硝酸铁(III)溶液的pH值为2,因此决定在生物反应器研究中使用二氧化锰(IV)。首先,对一个3.5升的台式玻璃生物反应器中电输入功率和化学输入功率进行的比较显示出良好的一致性。之后,该方法被应用于一个50升的搅拌式一次性生物反应器。最终结果的偏差是可以接受的。电加热方法的传热系数为242瓦/米/开尔文,而化学方法获得的值与之相差不到5%。最后,在一个200升的一次性生物反应器中进行了实验,证明了化学输入功率在技术相关规模下的适用性。