/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 99 Methanol is produced by reacting... [FREE SOLUTION] | 91Ó°ÊÓ

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Methanol is produced by reacting carbon monoxide and hydrogen at \(644 \mathrm{K}\) over a \(\mathrm{ZnO}-\mathrm{Cr}_{2} \mathrm{O}_{3}\) catalyst. A mixture of \(\mathrm{CO}\) and \(\mathrm{H}_{2}\) in a ratio \(2 \mathrm{mol} \mathrm{H}_{2} / \mathrm{mol}\) CO is compressed and fed to the catalyst bed at \(644 \mathrm{K}\) and 34.5 MPa absolute. A single-pass conversion of 25\% is obtained. The space velocity, or ratio of the volumetric flow rate of the feed gas to the volume of the catalyst bed, is The product gases are passed through a condenser, in which the methanol is liquefied. (a) You are designing a reactor to produce \(54.5 \mathrm{kmol} \mathrm{CH}_{3} \mathrm{OH} / \mathrm{h}\). Estimate (i) the volumetric flow rate that the compressor must be capable of delivering if no gases are recycled, and (ii) the required volume of the catalyst bed. (Use Kay's rule for pressure-volume calculations.) (b) If (as is done in practice) the gases from the condenser are recycled to the reactor, the compressor is then required to deliver only the fresh feed. What volumetric flow rate must it deliver assuming that the methanol produced is completely recovered in the condenser? (In practice it is not; moreover, a purge stream must be taken off to prevent the buildup of impurities in the system.)

Short Answer

Expert verified
For a reactor to produce 54.5 kmol/h methanol, the required volumetric flow rate for the compressor would be 44.95 m^3/h without gas recycling, and the volume of the catalyst bed required would be 22.475 m^3. If the gases are recycled, the fresh feed volumetric flow rate would be 11.18 m^3/h.

Step by step solution

01

(a) (i) Calculate the required feed of CO and H2

Using the stoichiometry of the reaction, for 54.5 kmol/h of CH3OH, the required feed of CO is also 54.5 kmol/h. As the ratio of H2:CO given is 2:1, the required feed of H2 is 2 * 54.5 = 109 kmol/h. The total molar flow rate of gases will be 54.5 (CO) + 109 (H2) = 163.5 kmol/h.
02

(a) (ii) Apply Kay's rule to find the volumetric flow rate

Applying Kay's rule, assuming unit volume at 0°C and 1 atm (1.013 bar), the total volume of feed gases at that condition will be 163.5 * 22.414 (molar volume at NTP) = 3664.3 m^3/h. Using the Ideal Gas Law, the volumetric flow rate for the feed gases can be found by correcting for actual temperature and pressure. At 644K (371°C) and 34.5 MPa (345 bar), this becomes 3664.3 * (273.15 + 371) / 273.15 * 1.013 / 345 = 44.95 m^3/h.
03

(a) (iii) Calculate the required volume of the catalyst bed

The space velocity (SV) given as ratio of volumetric flow rate to the volume of the catalyst bed, is defined as SV = V_feed/V_catalyst. The catalyst bed volume then can be expressed as V_catalyst = V_feed/SV. Given that SV is 2 h-1 and V_feed is 44.95 m^3/h, the volume of the catalyst bed required is V_catalyst = 44.95 / 2 = 22.475 m^3.
04

(b) Determine the fresh feed volumetric flow rate.

The fresh feed which is required to produce the methanol and is not recycled, includes the amount of gas which actually reacted in the reactor, which is 25% of the initial feed entering the reactor. Therefore, the fresh flow rate will be 0.25 * 163.5 (total molar flow rate as calculated earlier) = 40.875 kmol/h. Following the same procedure as before, the volumetric flow rate is 40.875 * 22.414 * (273.15 + 371) / 273.15 * 1.013 / 345 = 11.18 m^3/h.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Methanol Synthesis
Methanol (CH3OH) is a chemical with a wide array of uses, from fuel to feedstock for various chemical syntheses. To understand how methanol is made, one should look at the basic chemical reaction involving carbon monoxide (CO) and hydrogen (H2), generally over a catalyst like zinc oxide-chromium oxide (ZnO-Cr2O3). The reaction proceeds at elevated temperatures and pressures, yielding methanol through the following balanced equation:
CO + 2 H2 → CH3OH
For students grappling with the synthesis of methanol, remember it’s crucial to consider the molar ratios of reactants and the conditions required to favor the reaction, such as the 644 K temperature and 34.5 MPa pressure outlined in your textbook exercise.
Stoichiometry
Stoichiometry is the math behind chemistry. It's all about proportions and balancing act. When assessing the methanol synthesis, you may refer to the stoichiometric coefficients in the balanced reaction to understand the molar relationships between reactants and products. For the production of methanol, a 1:2 molar ratio of CO to H2 is needed, reflecting how many moles of each gas are necessary to form a mole of methanol. In practice, like in the textbook problem, we calculate the required feeds of CO and H2 based on the desired output of methanol—1 mole of CH3OH requires 1 mole of CO and 2 moles of H2. Thus, it's the stoichiometry that guides us in determining how much of each reactant we need to feed into the reactor to get our desired methanol output.
Catalyst Bed Design
In chemical engineering, the catalyst bed is where the magic happens. This is where reactant molecules meet and transform, with the help of a catalyst—our middleman. For a successful methanol synthesis process, the design of this catalyst bed is paramount. It needs to accommodate the correct volume of reactants and provide enough contact time for the reaction to occur. The space velocity, mentioned in the textbook problem, is a measure of how fast the gas flows through the bed relative to the catalyst's volume. It affects conversion rate, pressure drop, and ultimately the reactor's efficiency. Engineers must design the catalyst bed to ensure the right balance between size and flow rates to optimize production while minimizing costs and maximizing safety.
Kay's Rule
When dealing with gases under various conditions of temperature and pressure, one useful shortcut is Kay's rule. It's a thumb rule employed to quickly estimate the volume of a gas mixture at high pressures assuming ideal behavior. It asserts that the molar volume of a gas mixture can be approximated by the sum of the molar contributions of each individual gas, each adjusted for its mole fraction. This rule is applied, as demonstrated in the textbook solution, to estimate the volumetric flow rate of gases fed to the catalyst bed for methanol synthesis. Given the high-pressure conditions used in the methanol process, Kay's rule simplifies the step from knowing the molar flow rates to determining the actual gas volumes needed.
Ideal Gas Law
The Ideal Gas Law is a cornerstone of chemical engineering and broader physical science, encapsulating the relationship between a gas's pressure (P), volume (V), temperature (T), and the amount of substance (n). The law is expressed in the equation PV=nRT, where R is the universal gas constant. This equation allows engineers to calculate any one of the variables if the others are known and is crucial for designing processes like methanol synthesis. In our textbook exercise, the Ideal Gas Law is used alongside Kay's rule to correct the volumetric flow rate for actual operating conditions of the process—after all, real-life systems rarely operate at standard conditions of temperature and pressure.

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Most popular questions from this chapter

Determining the value of newly located natural gas sites involves estimating the gas composition. quantity, and ease of access. For example, one report described a find of 2 trillion cubic feet of natural gas that is significantly offshore, in 20 feet of water, and at a drilled depth of 25,000 ft. (In North America and the OPEC countries, reported volumes are determined at 14.73 psia and \(60^{\circ} \mathrm{F}\).) The pressure in this find is estimated to be 750 atm, and the gas is 94 mole \(\%\) methane, \(3.5 \%\) ethane, and the balance \(\mathrm{CO}_{2}\) (a) Estimate the total Ib-moles of gas in the find. (b) Use the compressibility-factor equation of state to estimate the specific volume (ft \(^{3} /\) /b-mole) in the well. The temperature of such wells can vary depending upon a number of factors; for the purposes of this problem, assume that it is \(200^{\circ} \mathrm{C}\).

Terephthalic acid (TPA), a raw material in the manufacture of polyester fiber, film, and soft drink bottles, is synthesized from \(p\) -xylene (PX) in the process shown below. A fresh feed of pure liquid \(\mathrm{PX}\) combines with a recycle stream containing \(\mathrm{PX}\) and a solution (S) of a catalyst (a cobalt salt) in a solvent (methanol). The combined stream, which contains \(S\) and \(P X\) in a 3: 1 mass ratio, is fed to a reactor in which \(90 \%\) of the \(\mathrm{PX}\) is converted to TPA. A stream of air at \(25^{\circ} \mathrm{C}\) and 6.0 atm absolute is also fed to the reactor. The air bubbles through the liquid and the reaction given above takes place under the influence of the catalyst. A liquid stream containing unreacted \(\mathrm{PX}\), dissolved TPA, and all the S that entered the reactor goes to a separator in which solid TPA crystals are formed and filtered out of the solution. The filtrate, which contains all the \(S\) and \(P X\) leaving the reactor, is the recycle stream. A gas stream containing unreacted oxygen, nitrogen, and the water formed in the reaction leaves the reactor at \(105^{\circ} \mathrm{C}\) and 5.5 atm absolute and goes through a condenser in which essentially all the water is condensed. The uncondensed gas contains 4.0 mole \(\%\) O. (a) Taking \(100 \mathrm{kmol}\) TPA produced/h as a basis of calculation, draw and label a flowchart for the process. (b) What is the required fresh feed rate (kmol PX/h)? (c) What are the volumetric flow rates \(\left(\mathrm{m}^{3} / \mathrm{h}\right)\) of the air fed to the reactor, the gas leaving the reactor, and the liquid water leaving the condenser? Assume ideal-gas behavior for the two gas streams. (d) What is the mass flow rate ( \(\mathrm{kg} / \mathrm{h}\) ) of the recycle stream? (e) Briefly explain in your own words the functions of the oxygen, nitrogen, catalyst, and solvent in the process. (f) In the actual process, the liquid condensate stream contains both water and PX. Speculate on what might be done with the latter stream to improve the economics of the process. [Hint: Note that PX is expensive, and recall what is said about oil (hydrocarbons) and water.]

Most of the concrete used in the construction of buildings, roads, dams, and bridges is made from Portland cement, a substance obtained by pulverizing the hard, granular residue (clinker) from the roasting of a mixture of clay and limestone and adding other materials to modify the setting properties of the cement and the mechanical properties of the concrete. The charge to a Portland cement rotary kiln contains \(17 \%\) of a dried building clay \(\left(72 \mathrm{wt} \% \mathrm{SiO}_{2}\right.\) \(\left.16 \% \mathrm{Al}_{2} \mathrm{O}_{3}, 7 \% \mathrm{Fe}_{2} \mathrm{O}_{3}, 1.7 \% \mathrm{K}_{2} \mathrm{O}, 3.3 \% \mathrm{Na}_{2} \mathrm{O}\right)\) and \(83 \%\) limestone \(\left(95 \mathrm{wt} \% \mathrm{CaCO}_{3}, 5 \% \text { impuritics }\right)\) When the solid temperature reaches about \(900^{\circ} \mathrm{C},\) calcination of the limestone to lime (CaO) and carbon dioxide occurs. As the temperature continues to rise to about \(1450^{\circ} \mathrm{C},\) the lime reacts with the minerals in the clay to form such compounds as \(3 \mathrm{CaO} \cdot \mathrm{SiO}_{2}, 3 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3},\) and \(4 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3} \cdot \mathrm{Fe}_{2} \mathrm{O}_{3} .\) The flow rate of \(\mathrm{CO}_{2}\) from the kiln is \(1350 \mathrm{m}^{3} / \mathrm{h}\) at \(1000^{\circ} \mathrm{C}\) and 1 atm. Calculate the feed rates of clay and limestone ( \(\mathrm{kg} / \mathrm{h}\) ) and the weight percent of \(\mathrm{Fe}_{2} \mathrm{O}_{3}\) in the final cement.

A nitrogen rotameter is calibrated by feeding \(\mathrm{N}_{2}\) from a compressor through a pressure regulator, a needle valve, the rotameter, and a dry test meter, a device that measures the total volume of gas that passes through it. A water manometer is used to measure the gas pressure at the rotameter outlet. A flow rate is set using the needle valve, the rotameter reading, \(\phi\), is noted, and the change in the dry gas meter reading \((\Delta V)\) for a measured running time \((\Delta t)\) is recorded. The following calibration data are taken on a day when the temperature is \(23^{\circ} \mathrm{C}\) and barometric pressure is \(763 \mathrm{mm} \mathrm{Hg} .\) $$\begin{array}{rrr} \hline \phi & \Delta t(\min ) & \Delta V(\mathrm{L}) \\ \hline 5.0 & 10.0 & 1.50 \\ 9.0 & 10.0 & 2.90 \\ 12.0 & 5.0 & 2.00 \\ \hline \end{array}$$ (a) Prepare a calibration chart of \(\phi\) versus \(\dot{V}_{\text {sid }}\), the flow rate in standard \(\mathrm{cm}^{3} / \mathrm{min}\) equivalent to the actual flow rate at the measurement conditions. (b) Suppose the rotameter-valve combination is to be used to set the flow rate to 0.010 mol \(\mathrm{N}_{2} / \mathrm{min}\). What rotameter reading must be maintained by adjusting the valve?

An ideal-gas mixture contains \(35 \%\) helium, \(20 \%\) methane, and \(45 \%\) nitrogen by volume at 2.00 atm absolute and \(90^{\circ} \mathrm{C}\). Calculate (a) the partial pressure of each component, (b) the mass fraction of methane, (c) the average molecular weight of the gas, and (d) the density of the gas in \(\mathrm{kg} / \mathrm{m}^{3}\).

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