Batch process method for kinematics data of mass population based on MATLAB / 医用生物力学

Objective To develop a batch process method for kinematics data of mass population based on MATLAB. Methods Based on MATLAB, the original coordinate data of markers from motion capture system were first batch-read with interpolation processing for eliminating the error points. The body-fixed base of contiguous rigid body attached on human body was then constructed as the reference base and body-fixed base of relative joint kinematics computing. The flexion/extension, abduction/adduction, internal and external rotation angular displacement, angular velocity and angular acceleration of joints were obtained based on the rigid body kinematics, the basic description of rigid body posture and the direction cosine matrix. Results Taking climbing upstairs and squatting as samples, the joint kinematics of lower extremity were analyzed and calculated by the batch process method for kinematics data of mass population based on MATLAB to prove the effectiveness and accuracy of the method. Conclusions The batch process method for kinematics data of mass population based on MATLAB was proved to be effective and accurate, and can be provided as a statistical analysis tool for anthropometry, human engineering, etc.

Production of 2,3-Butanediol from Sucrose by Klebsiella pneumoniae NRRL B199 in Batch and Fed-Batch Reactors

In batch mode, Klebsiella pneumoniae growth and 2,3-butanediol/acetoin formation are increasingly inhibited by initial sucrose concentrations (S0) over 60 g/L. At non inhibitory conditions, a maximum sucrose consumption rate of 1,5 g/L/h was measured. With S0=204 g/L however, this rate decreased to 0.15 g/L/h. K. pneumoniae fermented 204 g/L sucrose to produce 84.3 g/L of a mixture 2,3-butanediol/acetoin with a yield of 0.41 g/g and a productivity of 1.06 g/L/h. Higher oxygen transfer rates improved the overall process rate but the product yield was reduced. Avoiding substrate inhibition, by performing the fermentation in fed-batch mode, a final 2,3-butanediol/acetoin concentration of 80.0 g/L was achieved. In this case, a productivity of 2.63 g/L/h and a product yield of 0.37 g/g were calculated.

Em regime descontínuo, o crescimento celular e a formação de 2,3-butanodiol/acetoína por Klebsiella pneumoniae sofrem inibição por concentrações iniciais de sacarose (S0) acima de 60 g/L. Sob condições não inibidoras, uma velocidade máxima de consumo de sacarose de 1,5 g/L/h foi observada. Entretanto, com S0 = 204 g/L, esta velocidade decresceu para 0,15 g/L/h. A fermentação de 204 g/L de sacarose por K. pneumoniae levou à formação de 84,3 g/L de mistura 2,3-butanodiol/acetoína, com uma conversão de 0,41 g/g e uma produtividade de 1,06 g/L/h. Um maior suprimento de oxigênio aumentou a velocidade global do processo mas reduziu a conversão em produto. Em regime descontínuo alimentado, a inibição foi evitada, tendo sido atingida uma concentração final de produtos de 80,0 g/L, com uma produtividade de 2,63 g/L/h e uma conversão de 0,37 g/g.