![Propane is catalytically dehydrogenated to produce propylene by passing it over a granuar solid catalyst. In parallel with the main gas-phase reaction of propane dehydrogenation, side reaction to methane and carbon occurs: C,H,C,H +H A single-pass conversion of propane of 80%Is achieved in the reactor. Out of the propane reacting, 20% reacts according to the side reaction. The reactor effluent gases undergo a two-stage separation. In the first stage all hydrogen and 90% of the methane is separated, in the second stage the effluent from Separator 1 is divided into a product stream, containing also the rest of the methane and a waste stream, containing propane (98 wt%)and propylene (2 wt%) that is recycled to the reactor inlet. The requirement for the propylene content of the product stream is for a minimum of 98.8% by weight. (a) Draw the Process Flow Diagram (PFD) of the system and annotate it with the components for each of the streams. [15 marks) (b) Using a basis of 100 kmol/h fresh feed of pure propane for the system without the recycle stream - Calculate the reactor outlet composition and flows [5 marks - Calculate the waste stream Determine whether the product stream meets the specification for propylene content 5 marks) - [10 marks] - Calculate the overall conversion of propane - Write the overall atomic balance for carbon For the system with the recycle, assume the following: 1) Same single-pass conversion of propane in the reactor, 2) Same percentage propane for the side reaction; 3) Recycled propylene does not react 5 marks] [10 marks] (c) 120 marks) Calculate the Separator 1 outlet streams and compositions 15 marks Comment on the composition of the product stream. Do you expect it to differ from that of the system without a recycle? Explain your answer. [5 marks] - Calculate the overall conversion of propane. Compare it with the onie for the Calculate the recycle stream [5 marks) system without a recycle Give the main reason why the process has to be stopped periodically. d) [5 marks](http://img.homeworklib.com/questions/c6ddb720-bfc6-11ea-a53f-515a501b4603.png?x-oss-process=image/resize,w_560)
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Propane is catalytically dehydrogenated to produce propylene by passing it over a granuar solid catalyst. In...
0 One method of producing propylene is the dehydrogenation of propane (C3Hs) to propylene (CsHs) according...
0
One method of producing propylene is the dehydrogenation of propane (C3Hs) to propylene (CsHs) according to the reaction: A schematic of the reaction is shown below. The fresh feed (Stream 1) has a total flow rate of 100. mol/min and is composed of 96 mol% propane and 4.0 mol% propylene. The single pass conversion of propane across the reactor is 40% and all of the hydrogen is separated in the flash drum. Stream 5 exiting the flash drum is...
The final answers are: a) overall conversion= 0.578(57.8%) B) SP=12% C) V=233.1 L/h Please show me...
The final answers are:
a) overall conversion= 0.578(57.8%)
B) SP=12%
C) V=233.1 L/h
Please show me steps
Propylene is hydrogenated to produce propane via the gas phase reaction: C3H6 + H2 ? C3H8 A fresh feed (48 mole% C3H6, 48 mole% H2, and 4 mole% Inert) is mixed with a recycle stream in a ratio of 4 mole recycle/1 mole fresh feed to produce the feed to a reactor (8 mole% inert). The reactor output is fed to a separator...
D Question 9 1 pts C3H6 + CO + H2 C4H80 . In an existing process,...
D Question 9 1 pts C3H6 + CO + H2 C4H80 . In an existing process, 180 kgmol/h of C,H, (P) is mixed with 420 kgmol/h of a mixture containing 50% CO (C) and 50% H, (H) and with a recycle stream containing propylene and then fed to a reactor, 30% of the propylene fed to the reactor is consumed. The reactor effluent is sent to a separator. The desired product butanal (B) is removed in one stream, unreacted CO...
5) The most conventional method for producing propylene oxide is by the reaction of propylene with...
5) The most conventional method for producing propylene oxide is by the reaction of propylene with Hz and O2. However, propane is also produced from a competing reaction of propylene with Hz. If you mix a stream contains propylene, hydrogen and air (6, 18.6 and 27 mol/h, respectively) with an inert carbon dioxide (3000 mol/h) stream and fed them to a continuous reactor. The reactor effluents introduced to a condenser where the condensate liquids consisting propylene oxide, propylene and propane...
6.1. Propylene oxide (C,H,O is produced by reacting propylene (C,H) with oxygen and hydrogen. A side...
6.1. Propylene oxide (C,H,O is produced by reacting propylene (C,H) with oxygen and hydrogen. A side reaction resulted in reacting propylene with hydrogen and produces propane. A mixture of 35 mol/h Air, 4 mol/h propylene, and 12.6 mol/h hydrogen (H2) along with 5000 mol/h carbon dioxide (CO, is used as inert solvent) are fed to a continuous reactor. The percent single-pass conversion of limiting reactant is 10%. The fractional yield of C3Hs to C,H,O is 0.80 (i.e., fraction of moles...
7. A process takes hydrogen and nitrogen to make ammonia. It consists of a feed stream...
7. A process takes hydrogen and nitrogen to make ammonia. It consists of a feed stream (Hz: 330 kmol/h and N2: 110 kmol/h), a mixer in which the feed stream is mixed with the recycle stream, and a reactor (25% conversion), followed by a separator where the product is removed and the reactants are recycled. The recycle stream takes 95% of the unreacted H2 and N, and 2% of the produced ammonia. Draw the BFD for the process and number...
Problem Statement #3: Methane (CH) reacts with Cl; to produce methyl chloride (CH,CI) and HCI. However some of th...
Problem Statement #3: Methane (CH) reacts with Cl; to produce methyl chloride (CH,CI) and HCI. However some of the CH,CI undergoes further chlorination to form CH Cl; and HCI. The balanced reactions are shown below: CH,+C CHCI+ HCI CH CI CICH CI,+ HCI A fresh feed consisting of 200 mol/h of methane with 150% excess Cl, is joined by a recycle stream and the mixture is fed to a reactor where it reacts to produce CHCI, CH CI and HCL...
1. Acrylonitrile is produced by the reaction of propylene, ammonia, and oxygen C3H6 + NH3 +...
1. Acrylonitrile is produced by the reaction of propylene, ammonia, and oxygen C3H6 + NH3 + O2 C3H3N + 3H2O The feed contains 10 mole% propylene, 12% ammonia, and 78% air. A fractional conversion of 30% of the limiting reactant is achieved. Determine which reactant is limiting, the percentage by which each of the other reactants is in excess, and the molar flow rates of all product gas constituents for a 30% conversion of the limiting reactant, taking 100...
Purge CO Makupreactor Onygen SEM. Il 2018-19 The pertinent chemical reactions involved are: CH, +2H20 CH+H20 CO +3H2 CO2 4H2 (main reformer reaction) (reformer side reaction) (CO converter reacti...
Purge CO Makupreactor Onygen SEM. Il 2018-19 The pertinent chemical reactions involved are: CH, +2H20 CH+H20 CO +3H2 CO2 4H2 (main reformer reaction) (reformer side reaction) (CO converter reaction) (methanol synthesis reaction) 2co +02 2C02 (d) co2 + 3H, CH,OH + H20 Ten percent excess steam, based on Reaction (a), is fed to the reformer, and conversion of methane is 10%, with a 90% yield of CO2-A stoichiometric quantity of oxygen is fed to the CO converter, and the CO...
Problem #1: Haber-Bosch process. The Haber-Bosch process is an equilibrium-limited catalyzed reaction that converts nitrogen (N2)...
Problem #1: Haber-Bosch process. The Haber-Bosch process is an equilibrium-limited catalyzed reaction that converts nitrogen (N2) and hydrogen (H2) into ammonia (NH3). The process won Haber a Nobel Prize since it provided a way to produce fertilizer for millions of people at the beginning of the 20th century. However, this process typically has very low single pass conversion due to a low equilibrium at the prevailing temperature and therefore a recycle stream is required to achieve a high overall conversion....
0
One method of producing propylene is the dehydrogenation of propane (C3Hs) to propylene (CsHs) according to the reaction: A schematic of the reaction is shown below. The fresh feed (Stream 1) has a total flow rate of 100. mol/min and is composed of 96 mol% propane and 4.0 mol% propylene. The single pass conversion of propane across the reactor is 40% and all of the hydrogen is separated in the flash drum. Stream 5 exiting the flash drum is...
The final answers are:
a) overall conversion= 0.578(57.8%)
B) SP=12%
C) V=233.1 L/h
Please show me steps
Propylene is hydrogenated to produce propane via the gas phase reaction: C3H6 + H2 ? C3H8 A fresh feed (48 mole% C3H6, 48 mole% H2, and 4 mole% Inert) is mixed with a recycle stream in a ratio of 4 mole recycle/1 mole fresh feed to produce the feed to a reactor (8 mole% inert). The reactor output is fed to a separator...
D Question 9 1 pts C3H6 + CO + H2 C4H80 . In an existing process, 180 kgmol/h of C,H, (P) is mixed with 420 kgmol/h of a mixture containing 50% CO (C) and 50% H, (H) and with a recycle stream containing propylene and then fed to a reactor, 30% of the propylene fed to the reactor is consumed. The reactor effluent is sent to a separator. The desired product butanal (B) is removed in one stream, unreacted CO...
5) The most conventional method for producing propylene oxide is by the reaction of propylene with Hz and O2. However, propane is also produced from a competing reaction of propylene with Hz. If you mix a stream contains propylene, hydrogen and air (6, 18.6 and 27 mol/h, respectively) with an inert carbon dioxide (3000 mol/h) stream and fed them to a continuous reactor. The reactor effluents introduced to a condenser where the condensate liquids consisting propylene oxide, propylene and propane...
6.1. Propylene oxide (C,H,O is produced by reacting propylene (C,H) with oxygen and hydrogen. A side reaction resulted in reacting propylene with hydrogen and produces propane. A mixture of 35 mol/h Air, 4 mol/h propylene, and 12.6 mol/h hydrogen (H2) along with 5000 mol/h carbon dioxide (CO, is used as inert solvent) are fed to a continuous reactor. The percent single-pass conversion of limiting reactant is 10%. The fractional yield of C3Hs to C,H,O is 0.80 (i.e., fraction of moles...
7. A process takes hydrogen and nitrogen to make ammonia. It consists of a feed stream (Hz: 330 kmol/h and N2: 110 kmol/h), a mixer in which the feed stream is mixed with the recycle stream, and a reactor (25% conversion), followed by a separator where the product is removed and the reactants are recycled. The recycle stream takes 95% of the unreacted H2 and N, and 2% of the produced ammonia. Draw the BFD for the process and number...
Problem Statement #3: Methane (CH) reacts with Cl; to produce methyl chloride (CH,CI) and HCI. However some of the CH,CI undergoes further chlorination to form CH Cl; and HCI. The balanced reactions are shown below: CH,+C CHCI+ HCI CH CI CICH CI,+ HCI A fresh feed consisting of 200 mol/h of methane with 150% excess Cl, is joined by a recycle stream and the mixture is fed to a reactor where it reacts to produce CHCI, CH CI and HCL...
Purge CO Makupreactor Onygen SEM. Il 2018-19 The pertinent chemical reactions involved are: CH, +2H20 CH+H20 CO +3H2 CO2 4H2 (main reformer reaction) (reformer side reaction) (CO converter reaction) (methanol synthesis reaction) 2co +02 2C02 (d) co2 + 3H, CH,OH + H20 Ten percent excess steam, based on Reaction (a), is fed to the reformer, and conversion of methane is 10%, with a 90% yield of CO2-A stoichiometric quantity of oxygen is fed to the CO converter, and the CO...
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