Comprehension # 8
`A` factory, producing methanol, is based on the reaction:
`CO+2H_(2)hArrCH_(3)OH`
Hydrogen `&` carbon monoxide are obtained by the reaction
`CH_(4)+H_(2)OhArrCO+3H_(2)`
Three units of factory namely, the "reformer" for the `H_(2)` and `CO` production, the "methanol reactor" for production of methanol and a "separator" to separate `CH_(3)OH` from `CO` and `H_(2)` are schematically shown in figure.
four positions are indicated as `alpha,beta,gamma` and `delta`. The flow of methanol at position `gamma` is `10^(3)mol//sec`. The factory is so designed that `(2)/(3)` of the `CO` is converted to `CH_(3)OH`. Excess of `CO` and `H_(2)` at position `delta` are used to heat the first reaction. Assume that the reformer reaction goes to completion. At the position `(beta)` mole ratio of `CO` to `H_(2)` is `(1)/(3)`
`CO+2H_(2)hArrCH_(3)OH " "DeltaH_(r)=-100 R`
What is the flow of `CO` and `H_(2)` at position `(beta)` ?
Comprehension # 8
`A` factory, producing methanol, is based on the reaction:
`CO+2H_(2)hArrCH_(3)OH`
Hydrogen `&` carbon monoxide are obtained by the reaction
`CH_(4)+H_(2)OhArrCO+3H_(2)`
Three units of factory namely, the "reformer" for the `H_(2)` and `CO` production, the "methanol reactor" for production of methanol and a "separator" to separate `CH_(3)OH` from `CO` and `H_(2)` are schematically shown in figure.
four positions are indicated as `alpha,beta,gamma` and `delta`. The flow of methanol at position `gamma` is `10^(3)mol//sec`. The factory is so designed that `(2)/(3)` of the `CO` is converted to `CH_(3)OH`. Excess of `CO` and `H_(2)` at position `delta` are used to heat the first reaction. Assume that the reformer reaction goes to completion. At the position `(beta)` mole ratio of `CO` to `H_(2)` is `(1)/(3)`
`CO+2H_(2)hArrCH_(3)OH " "DeltaH_(r)=-100 R`
What is the flow of `CO` and `H_(2)` at position `(beta)` ?
`A` factory, producing methanol, is based on the reaction:
`CO+2H_(2)hArrCH_(3)OH`
Hydrogen `&` carbon monoxide are obtained by the reaction
`CH_(4)+H_(2)OhArrCO+3H_(2)`
Three units of factory namely, the "reformer" for the `H_(2)` and `CO` production, the "methanol reactor" for production of methanol and a "separator" to separate `CH_(3)OH` from `CO` and `H_(2)` are schematically shown in figure.
four positions are indicated as `alpha,beta,gamma` and `delta`. The flow of methanol at position `gamma` is `10^(3)mol//sec`. The factory is so designed that `(2)/(3)` of the `CO` is converted to `CH_(3)OH`. Excess of `CO` and `H_(2)` at position `delta` are used to heat the first reaction. Assume that the reformer reaction goes to completion. At the position `(beta)` mole ratio of `CO` to `H_(2)` is `(1)/(3)`
`CO+2H_(2)hArrCH_(3)OH " "DeltaH_(r)=-100 R`
What is the flow of `CO` and `H_(2)` at position `(beta)` ?
A
`CO : 1500mol//sec., H_(2) : 2000 mol//sec`.
B
`CO : 1500mol//sec., H_(2) : 3000 mol//sec`.
C
`CO : 1000mol//sec., H_(2) : 2000 mol//sec`.
D
`CO : 1500mol//sec., H_(2) : 4500 mol//sec`.
Text Solution
Verified by Experts
The correct Answer is:
D
`{:(,CH_(4)+H_(2)OrarrCO,+,3H_(2)),(," "(3)/(2)xx10^(3),,3):}`
`CO+2H_(2) rarr CH_(3)OH`
`10^(3)" "2xx10^(3)" "10^(3)("moles/sec")`
`("total" CO = (3)/(2) xx 10^(3))`
`CO+2H_(2) rarr CH_(3)OH`
`10^(3)" "2xx10^(3)" "10^(3)("moles/sec")`
`("total" CO = (3)/(2) xx 10^(3))`
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Which catalyst is used in the preparation of CH_(3)OH by the reaction of CO(g) & H_(2)(g) ?
A factory, producing methanol, is based on the reaction : CO+2H_(2)rarr CH_(3)OH ltBRgt Hydrogen and carbon monoxide are obtained by the reaction CH_(4)+H_(2)Orarr CO+3H_(2) Three units of factory namely, the "reformer" for the H_(2) and CO production, the "methanol reactor" for production of methonol adn a "separator" to separate CH_(3)OH form CO and H_(2) are schematically shown in figure. The flow of methonal from valve-3 is 10^(3)mol//sec. The factory is so designed that (2)/(3) of the CO is converted to CH_(3)OH. Assume that the feromer reaction goes to completion. CO+2H_(2)rarrCH_(3)OH Delta_(r) H=-100 R What is the flow of CO and H_(2) at valve-2 ?
Knowledge Check
Comprehension # 8 A factory, producing methanol, is based on the reaction: CO+2H_(2)hArrCH_(3)OH Hydrogen & carbon monoxide are obtained by the reaction CH_(4)+H_(2)OhArrCO+3H_(2) Three units of factory namely, the "reformer" for the H_(2) and CO production, the "methanol reactor" for production of methanol and a "separator" to separate CH_(3)OH from CO and H_(2) are schematically shown in figure. four positions are indicated as alpha,beta,gamma and delta . The flow of methanol at position gamma is 10^(3)mol//sec . The factory is so designed that (2)/(3) of the CO is converted to CH_(3)OH . Excess of CO and H_(2) at position delta are used to heat the first reaction. Assume that the reformer reaction goes to completion. At the position (beta) mole ratio of CO to H_(2) is (1)/(3) CO+2H_(2)hArrCH_(3)OH " "DeltaH_(r)=-100 R Amount of energy released in methanol reactor in 1 minute ?
Comprehension # 8 A factory, producing methanol, is based on the reaction: CO+2H_(2)hArrCH_(3)OH Hydrogen & carbon monoxide are obtained by the reaction CH_(4)+H_(2)OhArrCO+3H_(2) Three units of factory namely, the "reformer" for the H_(2) and CO production, the "methanol reactor" for production of methanol and a "separator" to separate CH_(3)OH from CO and H_(2) are schematically shown in figure. four positions are indicated as alpha,beta,gamma and delta . The flow of methanol at position gamma is 10^(3)mol//sec . The factory is so designed that (2)/(3) of the CO is converted to CH_(3)OH . Excess of CO and H_(2) at position delta are used to heat the first reaction. Assume that the reformer reaction goes to completion. At the position (beta) mole ratio of CO to H_(2) is (1)/(3) CO+2H_(2)hArrCH_(3)OH " "DeltaH_(r)=-100 R Amount of energy released in methanol reactor in 1 minute ?
A
`1200 kcal`
B
`12000 kcal`
C
`6000 kcal`
D
None of these
A factory, producing methanol, is based on the reaction : CO+2H_(2)rarr CH_(3)OH Hydrogen and carbon monoxide are obtained by the reaction CH_(4)+H_(2)Orarr CO+3H_(2) Three units of factory namely, the "reformer" for the H_(2) and CO production, the "methanol reactor" for production of methonol adn a "separator" to separate CH_(3)OH form CO and H_(2) are schematically shown in figure. The flow of methonal from valve-3 is 10^(3)mol//sec. The factory is so designed that (2)/(3) of the CO is converted to CH_(3)OH. Assume that the feromer reaction goes to completion. CO+2H_(2)rarrCH_(3)OH Delta_(r) H=-100 R What is the flow of CO and H_(2) at valve-1?
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A
`CO:1500 mol//sec, H_(2):2000 mol//sec`
B
`CO:1500 mol//sec,` `H_(2):3000 mol//sec`
C
`CO:1000 mol//sec,` `H_(2):2000 mol//sec`
D
`CO:1500 mol//sec,` `H_(2):4500 mol//sec`
A factory, producing methanol, is based on the reaction : CO+2H_(2)rarr CH_(3)OH ltBRgt Hydrogen and carbon monoxide are obtained by the reaction CH_(4)+H_(2)Orarr CO+3H_(2) Three units of factory namely, the "reformer" for the H_(2) and CO production, the "methanol reactor" for production of methonol adn a "separator" to separate CH_(3)OH form CO and H_(2) are schematically shown in figure. The flow of methonal from valve-3 is 10^(3)mol//sec. The factory is so designed that (2)/(3) of the CO is converted to CH_(3)OH. Assume that the feromer reaction goes to completion. CO+2H_(2)rarrCH_(3)OH Delta_(r) H=-100 R Amount of energy released in methanol reactor in1 minute :
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A
1200 kcal
B
12000 kcal
C
6000 kcal
D
none of these
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