By: Ashley and Christine Phy 200 Professor Newman 4/13/12

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Transcription:

By: Ashley and Christine Phy 200 Professor Newman 4/13/12

What is it? Technique used to settle particles in solution against the barrier using centrifugal acceleration

Two Types of Centrifuges Analytical Non Analytical

History 1913 - Dumansky proposed the use of ultracentrifugation to determine dimensions of particles 1923 - The first centrifuge is constructed by Svedberg and Nichols. 1929 - Lamm deduces a general equation that describes the movement within the ultracentrifuge field 1940s - Spinco Model E centrifuge becomes commercially available 1950s - Sedimentation becomes a widely used method. 1960s - First scanning photoelectric absorption optical system developed 1980s - Sedimentation loses popularity due to data treatment being slow and the creation of gel electrophoresis and chromatography 1990s - Newer versions of centrifuge gains popularity again 2000s - It is now recognized as a necessary technique for most laboratories

How Does It Work? Everything has a sedimentation coefficient Ratio of measured velocity of the particle to its centrifugal acceleration Can be calculated from the forces acting on a particle in the cell

Sedimentation Coefficient Usually, determine mass by observing movement of particles due to known forced Use Gravity normally For molecules, force is too small Avoid this by increasing PE by putting paricles in a cell rotating at a high speed Get Sedimentation Coefficient

How does it work? Rotors must be capable of withstanding large gravitational stress Two types of cells: double sector (accounts for absorbing components in solvent) and boundary forming (allows for layering of solvent over the solution) Optical detection systems: Rayleigh optical system (displays boundaries in terms of refractive index as a function of radius), Schlieren optical system (refractive index gradient as a function of radius), and absorption optical system (optical density as a function of radius) Data acquisition is computer automated due to the Beckman Instruments Optima XL analytical centrifuge

Deriving the Lamm Equation Describes the transport process in the ultracentrifuge Fick s first equation: Jx = -D[dC/dx] If all particles in the cell drift in a +x direction at speed, u: Jx = -D[dC/dx] + uc(x) u = sω2x Therefore, Jx = -D[dC/dx] + sω2xc(x) For ideal infinite cell lacking walls.

Lamm Equation For real experimental conditions: Cross-section of a sector cell is proportional to r Continuity equation: (dc/dt)r= -(1/r)(drJ/dr)t Combine ideal equation with continuity equation to obtain: (dc/dt)r = -(1/r){(d/dr)[ω2r2sC Dr(dc/dr)t]}t Describes diffusion with drift in an AUC sector cell under real experimental conditions.

http://www.nibib.nih.gov/research/intramural/lbps/pbr/auc/lammeqsoluti ons

Lamm Equation: Different Boundary Conditions Exact Solutions Exist in 2 limiting cases: 1. NO DIFFUSION Homogeneous macromolecular solution C2(x,t) = {0 if xm<x<xavg {C0exp(-2sω2t) if xavg<x<xb 2. NO SEDIMENTATION Lamm Equation: (dc/dt)r = -D(d2C/dt2)t Concentration Gradient: (dc/dt)r = -Co(πDt)1/2exp(-x2/4Dt) Diffusion coefficient determined by measuring the standard deviation of Gaussian curve Used for small globular proteins, at low speed, with synthetic boundary cell.

Technology Enabling Analytical Analysis Two computer modeling methods enable simultaneous determination of sedimentation, diffusion coefficients, and molecular mass. 1. vanholde-weischet Method: http://www.aapsj.org/view.asp?art=aa psj080368 Extrapolation to infinite time must eliminate the contribution of diffusion to the boundary shape. ULTRASCAN software 2.Stafford Method: Sedimentation coefficient distribution is computed from the time derivate of the sedimentation velocity concentration profile

http://www.ultrascan2.uthscsa.edu/tutorial/basics_5.html

Specific Boundary Conditions Faxen-type solutions: Centrifugation cell considered infinite sector Diffusion is small Only consider early sedimentation times Archibald solutions: S and D considered constant Fujita-type solutions: D is constant S depends on concentration

Sedimentation Sedimentation Velocity and Velocity Equilibrium Sedimentation Equilibrium Angular Velocity Large (according to sedimentation properties) Small Analysis As a function of time At equilibrium Measurement Forming a Boundary Particle distribution in cell Calculated Parameters Shape, mass composition Mass composition

Sedimentation Velocity How we measure the results: Determine the Sedimentation and Diffusion Coefficients from a moving boundary

It takes a While to Run an Experiment! Speed (rpm) Time at each speed (s) Svedbergs 0-6000 15 500 6000 600 4220 9000 600 1330 13000 600 550 18000 600 250 25000 600 125 50000 3600 31

Correcting to Standard Value Allows for standardization of sedimentation coefficients

Concentration Dependence Sedimentation coefficients of biological macromolecules are normally obtained at finite concentration and should be extrapolated to zero concentration

Determining Macromolecular Mass First Svedberg equation: M = srt/d(1-υ avg ρ o ) Assumptions: Frictional coefficients affecting diffusion and sedimentation are identical

Sedimentation Equilibrium Even if centrifuged for an extended period of time, macromolecules will not join pellet because of gravitational and diffusion force equilibrium. Molecular mass determination is independent of shape. Shape only affects rate equilibrium is reached, not distribution. No changes in concentration with time at equilibrium Total flux = 0

Binding Constants Can measure concentration dependence of an effective average molecular mass. Can be used to describe different kinds of phenomenon. Dissociation equilibrium constant can be directly determined from the equilibrium sedimentation data C(r) = CA(r)σA + CB(r)σB + CAB(r)σAB

Partial Specific Volume Needed when determining molecular mass through sedimentation Measurement of the density of the particle using its calculated volume and mass Very difficult to make precise density measurements needed

Density Gradient Sedimentation Velocity Zonal Method Layered density gradient Sucrose, glycerol Particles separate into zones based on sedimentation velocity, according to sedimentation coefficients Determined by size, shape, and buoyant density Estimation of molecular masses Potential Problem: Molecular crowding effect due to high sucrose concentration Density Gradient Sedimentation Equilibrium Density gradient itself formed by centrifugal field Used in experiment by Messelson and Stahl

http://www.mun.ca/biology/scarr/gr10-23.html

Molecular Shape Sedimentation coefficient dependent on particle volume and shape Molecules having the same shape, but different molecular mass form a homologous series. http://web.virginia.edu/heidi/chapter30 /chp30.htm