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Astandard solution containing 6.310-8Miodoacetone and 2.010-7Mp-dichlorobenzene (an internal standard) gave peak areas of 395 and 787, respectively, in a gas chromatogram. A 3.00-mlunknown solution of iodoacetone was treated with 0.100mLof 1.610-5Mp-dichlorobenzene and the mixture was diluted to. Gas chromatography gave peak areas of 633 and 520 for iodoacetone and p-dichlorobenzene, respectively. Find the concentration of iodoacetone in the 3.00mLof original unknown.

Short Answer

Expert verified

In3.00mloftheoriginalsolution,theconcentrationoflodoacetoneis0.41渭惭.

Step by step solution

01

Definition of iodoacetone

C3H5IOisthechemicalformulaforiodoacetone,anorganoiodinecompound. Undernormalcircumstances,thematerialisawhiteliquidthatissolubleinethanol.

02

Step 2: Determine the concentration of iodoacetone in the 3.00 mL of originalunknown

It is necessary to calculate the concentration of lodoacetone in 3.00ml of the original solution.

The formula for quantitative analysis with internal standard can be found here,

AxX=FAsS

Here Ax=signal region of analyte

As=area of internal standard

[X] = analyte's concentration

[S]= concentration of internal standard

F= response factor

To figure out how much lodoacetone is in 3.00ml of the original solution

Given,

Lodoacetone molarity =6.310-8M

P-dichlorobenzene molarity =2.010-7MPeakareas=395&787

Unknown volume of lodoacetone solutionrole="math" localid="1654853858008" =3.00ml

p-dichlorobenzene Volume and Molarity=0.100ml&1.610-5M

Lodoacetone has a peak area of 633 square metres.

p-dichlorobenzene has a peak area of =520.

The response factor is determined as follows,

39563nM=F787200nMF=1.59

When an internal standard is coupled with an unknown, the concentration is determined as,

0.100ml10.00ml1.610-5M=0.16渭惭Lodoacetoneconcentrationisdeterminedas,633iodoacentone=1.595200.16渭惭iodoacentone=0.122渭惭Intheoriginalunknownsolution,theconcentrationoflodoacetoneisdeterminedas,iodoacentone=10.003.00-0.122渭惭iodoacentone=0.41渭惭In3.00mloftheoriginalsolution,theconcentrationoflodoactone=0.41渭惭The3.00mloftheoriginalsolution,theconcentrationoflodoacetonewasdeterminedandfoundtobe0.41渭惭

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Most popular questions from this chapter

Where would an unknown with a retention index of 936 be eluted in Figure 23-7?

(a) Use Trouton's rule, Hvap(88Jmol-1K-1)Tbp, to estimate the enthalpy of vaporization of octane (b.p. 126).

(b) Use the form of the Clausius-Clapeyron equation below to estimate the vapor pressure of octane at the column temperature in Figure 24-9(70C)

In(P1P2)=-(HvapR)(1T1-1T2)

(c) Calculate the vapor pressure for hexane (b.p. 69C) at70C

(d) What is the relationship between solute vapor pressure and retention?

(e) Why is the technique called "gas chromatography鈥 if retained analytes are only partially vaporized?

This problem reviews concepts from Chapter 23 using

Figure 24-15.

(a) Calculate the retention factor for peak 11 given tm 5 6.7 min.

(b) Calculate the number of theoretical plates (N in Equation 23-31)

and the plate height (H) for peak 11.

(c) Find the resolution (Equation 23-23) between peaks 16 and 17.

Describe how retention time of butanol on a poly (ethylene glycol) column will change with increasing temperature. Use the retention time for butanol in Figure 24-9b as the starting point.

The graph shows van Deemter curves for n-nonane at . in the 3.0-m-long microfabricated column in Box 24-2 with a -thick stationary phase.

van Deemter curves. [Data from G. Lambertus, A. Elstro, K. Sensenig, J. Potkay, M. Agah, S. Scheuening, K. Wise, F. Dorman, and R. Sacks, "Design, Fabrication, and Evaluation of Microfabricated Columns for Gas Chromatography," Anal. Chem. 2004, 76, 2629.]

(a) Why would air be chosen as the carrier gas? What is the danger of using

air as carrier gas?

(b) Measure the optimum velocity and plate height for air and for carrier

gases.

(c) How many plates are there in the 3 -m-long column for each carrier gas at

optimum flow rate?

(d) How long does unretained gas take to travel through the column at

optimum velocity for each carrier gas?

(e) If stationary phase is sufficiently thin with respect to column diameter, which of the two mass transfer terms (23-40 or 23-41) becomes negligible?

Why?

(f) Why is the loss of column efficiency at high flow rates less severe for

than for air carrier gas?

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