TLS Online TPP Program

#Question id: 5703


Robertsonian translocation is reciprocal exchange of genetic segment between two acrocentric chromosomes. Which of the following is incorrect statement?

#Part-B Specialized Branches in Biotechnology
  1. Translocation resulting karyotype in humans leaves only 45 chromosomes

  2. Robertsonian translocations carrier individuals are not associated with any phenotypic abnormalities

  3. All gamete of Robertsonian translocations carrier are unbalanced gametes that lead to miscarriages or abnormal offspring

  4. Carriers of Robertsonian translocations involving chromosome 21 have a higher risk of having a child with Down syndrome

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TLS Online TPP Program

#Question id: 15596

#Part-B Specialized Branches in Biotechnology

To solve the equation 2 sin x = x by Newton-Raphson method, the initial guess was chosen to be x = 2.0. Consider x in radian only. The value of x (in radian) obtained after one iteration will be closest to 

TLS Online TPP Program

#Question id: 15597

#Part-B Specialized Branches in Biotechnology

The iteration formula of Newton-Raphson method for finding roots of the equation f(x) = 0 is 


TLS Online TPP Program

#Question id: 15601

#Part-B Specialized Branches in Biotechnology

In Newton Raphson method if the curve f f(x) is constant then

TLS Online TPP Program

#Question id: 15623

#Part-B Specialized Branches in Biotechnology

Under unaerated condition in a fermentor, the power consumed by a single impeller was 10,000 W. The diameter of the impeller D is 1m and the density of the medium is 1000 kg/m3 and the stirrer speed is 1s-1. If one more impeller is added to the fermentor, power consumption would be approximately

TLS Online TPP Program

#Question id: 15624

#Part-B Specialized Branches in Biotechnology

In heat transfer through a heat exchanger in co- current or counter-current flow, which of the assumptions is not correct ?

TLS Online TPP Program

#Question id: 15625

#Part-B Specialized Branches in Biotechnology

A stagnant liquid film of 0.4 mm thickness is held between two parallel plates. The top plate is maintained at 400C and the bottom plate is maintained at 300C. If
the thermal conductivity of the liquid is 0.14 W/(m K), then the steady state heat flux ( W/m2) assuming one-dimensional heat transfer is