Institute of Biochemical Engineering, Technische Universität Braunschweig, 38106 Braunschweig, Germany.
Biotechnol Prog. 2010 Sep-Oct;26(5):1259-70. doi: 10.1002/btpr.449.
A diffusion-based microreactor system operated with a reaction volume of 8 μL is presented and characterized to intensify the process understanding in microscale cultivations. Its potential as screening tool for biological processes is evaluated. The advantage of the designed microbioreactor is the use for the continuous cultivation mode by integrating online measurement technique for dissolved oxygen (DO) and optical density (OD). A further advantage is the broaden application for biological systems. The bioreactor geometry was chosen to achieve homogeneous flow during continuous process operation. The device consisted of a microstructured top layer made of poly(dimethylsiloxane) (PDMS), which was designed and fabricated using UV-depth and soft lithography assembled with a glass bottom. CFD simulation data used for geometry design were verified via microparticle-image-velocimetry (μPIV). In the used microreactor geometry no concentration gradients occurred along the entire reaction volume because of rapid diffusive mixing, the homogeneous medium flow inside the growth chamber of the microreactor could be realized. Undesirable bubble formation before and during operation was reduced by using degassed medium as well as moistened and moderate incident air flow above the gas permeable PDMS membrane. Because of this a passive oxygen supply of the culture medium in the device is ensured by diffusion through the PDMS membrane. The oxygen supply itself was monitored online via integrated DO sensors based on a fluorescent dye complex. An adequate overall volumetric oxygen transfer coefficient K(L)a as well as mechanical stability of the device were accomplished for a membrane thickness of 300 μm. Experimental investigations considering measurements of OD (online) and several metabolite concentrations (offline) in a modified Verduyn medium. The used model organism Saccharomyces cerevisiae DSM 2155 tended to strong reactor wall growth resembling a biofilm.
本文提出并描述了一种基于扩散的微反应器系统,其工作体积为 8 μL,用于强化微尺度培养过程中的工艺理解。评估了其作为生物过程筛选工具的潜力。该设计的微生物反应器的优点是通过集成在线溶解氧(DO)和光密度(OD)测量技术,实现连续培养模式。另一个优点是更广泛地适用于生物系统。生物反应器的几何形状选择是为了在连续过程操作中实现均匀的流动。该装置由聚二甲基硅氧烷(PDMS)制成的微结构顶层组成,该顶层是使用 UV 深度和软光刻技术设计和制造的,与玻璃底层组装在一起。用于几何设计的 CFD 模拟数据通过微粒子图像测速(μPIV)进行了验证。在使用的微反应器几何形状中,由于快速扩散混合,整个反应体积中没有发生浓度梯度,因此可以在微反应器的生长室内部实现均匀的介质流动。通过使用脱气介质以及在透气 PDMS 膜上方润湿和适度的入射空气流,可以减少操作前后的不良气泡形成。因此,通过 PDMS 膜的扩散确保了装置中培养基的被动供氧。氧气供应本身通过基于荧光染料复合物的集成 DO 传感器在线监测。对于 300 μm 厚的膜,实现了足够的总体体积氧传递系数 K(L)a 和装置的机械稳定性。在改良的 Verduyn 培养基中进行了考虑在线 OD(在线)和几种代谢物浓度(离线)测量的实验研究。所用的模式生物酿酒酵母 DSM 2155倾向于强烈的反应器壁生长,类似于生物膜。