tutorbin

chemical process calculations homework help

Boost your journey with 24/7 access to skilled experts, offering unmatched chemical process calculations homework help

tutorbin

Trusted by 1.1 M+ Happy Students

Place An Orderand save time
man
phone
  • United States+1
  • United Kingdom+44
  • Afghanistan (‫افغانستان‬‎)+93
  • Albania (Shqipëri)+355
  • Algeria (‫الجزائر‬‎)+213
  • American Samoa+1
  • Andorra+376
  • Angola+244
  • Anguilla+1
  • Antigua and Barbuda+1
  • Argentina+54
  • Armenia (Հայաստան)+374
  • Aruba+297
  • Ascension Island+247
  • Australia+61
  • Austria (Österreich)+43
  • Azerbaijan (Azərbaycan)+994
  • Bahamas+1
  • Bahrain (‫البحرين‬‎)+973
  • Barbados+1
  • Belarus (Беларусь)+375
  • Belgium (België)+32
  • Belize+501
  • Benin (Bénin)+229
  • Bermuda+1
  • Bhutan (འབྲུག)+975
  • Bolivia+591
  • Bosnia and Herzegovina (Босна и Херцеговина)+387
  • Botswana+267
  • Brazil (Brasil)+55
  • British Indian Ocean Territory+246
  • British Virgin Islands+1
  • Brunei+673
  • Bulgaria (България)+359
  • Burkina Faso+226
  • Burundi (Uburundi)+257
  • Cambodia (កម្ពុជា)+855
  • Cameroon (Cameroun)+237
  • Canada+1
  • Cape Verde (Kabu Verdi)+238
  • Caribbean Netherlands+599
  • Cayman Islands+1
  • Central African Republic (République centrafricaine)+236
  • Chad (Tchad)+235
  • Chile+56
  • China (中国)+86
  • Christmas Island+61
  • Cocos (Keeling) Islands+61
  • Colombia+57
  • Comoros (‫جزر القمر‬‎)+269
  • Congo (DRC) (Jamhuri ya Kidemokrasia ya Kongo)+243
  • Congo (Republic) (Congo-Brazzaville)+242
  • Cook Islands+682
  • Costa Rica+506
  • Côte d’Ivoire+225
  • Croatia (Hrvatska)+385
  • Cuba+53
  • Curaçao+599
  • Cyprus (Κύπρος)+357
  • Czech Republic (Česká republika)+420
  • Denmark (Danmark)+45
  • Djibouti+253
  • Dominica+1
  • Dominican Republic (República Dominicana)+1
  • Ecuador+593
  • Egypt (‫مصر‬‎)+20
  • El Salvador+503
  • Equatorial Guinea (Guinea Ecuatorial)+240
  • Eritrea+291
  • Estonia (Eesti)+372
  • Eswatini+268
  • Ethiopia+251
  • Falkland Islands (Islas Malvinas)+500
  • Faroe Islands (Føroyar)+298
  • Fiji+679
  • Finland (Suomi)+358
  • France+33
  • French Guiana (Guyane française)+594
  • French Polynesia (Polynésie française)+689
  • Gabon+241
  • Gambia+220
  • Georgia (საქართველო)+995
  • Germany (Deutschland)+49
  • Ghana (Gaana)+233
  • Gibraltar+350
  • Greece (Ελλάδα)+30
  • Greenland (Kalaallit Nunaat)+299
  • Grenada+1
  • Guadeloupe+590
  • Guam+1
  • Guatemala+502
  • Guernsey+44
  • Guinea (Guinée)+224
  • Guinea-Bissau (Guiné Bissau)+245
  • Guyana+592
  • Haiti+509
  • Honduras+504
  • Hong Kong (香港)+852
  • Hungary (Magyarország)+36
  • Iceland (Ísland)+354
  • India (भारत)+91
  • Indonesia+62
  • Iran (‫ایران‬‎)+98
  • Iraq (‫العراق‬‎)+964
  • Ireland+353
  • Isle of Man+44
  • Israel (‫ישראל‬‎)+972
  • Italy (Italia)+39
  • Jamaica+1
  • Japan (日本)+81
  • Jersey+44
  • Jordan (‫الأردن‬‎)+962
  • Kazakhstan (Казахстан)+7
  • Kenya+254
  • Kiribati+686
  • Kosovo+383
  • Kuwait (‫الكويت‬‎)+965
  • Kyrgyzstan (Кыргызстан)+996
  • Laos (ລາວ)+856
  • Latvia (Latvija)+371
  • Lebanon (‫لبنان‬‎)+961
  • Lesotho+266
  • Liberia+231
  • Libya (‫ليبيا‬‎)+218
  • Liechtenstein+423
  • Lithuania (Lietuva)+370
  • Luxembourg+352
  • Macau (澳門)+853
  • North Macedonia (Македонија)+389
  • Madagascar (Madagasikara)+261
  • Malawi+265
  • Malaysia+60
  • Maldives+960
  • Mali+223
  • Malta+356
  • Marshall Islands+692
  • Martinique+596
  • Mauritania (‫موريتانيا‬‎)+222
  • Mauritius (Moris)+230
  • Mayotte+262
  • Mexico (México)+52
  • Micronesia+691
  • Moldova (Republica Moldova)+373
  • Monaco+377
  • Mongolia (Монгол)+976
  • Montenegro (Crna Gora)+382
  • Montserrat+1
  • Morocco (‫المغرب‬‎)+212
  • Mozambique (Moçambique)+258
  • Myanmar (Burma) (မြန်မာ)+95
  • Namibia (Namibië)+264
  • Nauru+674
  • Nepal (नेपाल)+977
  • Netherlands (Nederland)+31
  • New Caledonia (Nouvelle-Calédonie)+687
  • New Zealand+64
  • Nicaragua+505
  • Niger (Nijar)+227
  • Nigeria+234
  • Niue+683
  • Norfolk Island+672
  • North Korea (조선 민주주의 인민 공화국)+850
  • Northern Mariana Islands+1
  • Norway (Norge)+47
  • Oman (‫عُمان‬‎)+968
  • Palau+680
  • Palestine (‫فلسطين‬‎)+970
  • Panama (Panamá)+507
  • Papua New Guinea+675
  • Paraguay+595
  • Peru (Perú)+51
  • Philippines+63
  • Poland (Polska)+48
  • Portugal+351
  • Puerto Rico+1
  • Qatar (‫قطر‬‎)+974
  • Réunion (La Réunion)+262
  • Romania (România)+40
  • Russia (Россия)+7
  • Rwanda+250
  • Saint Barthélemy+590
  • Saint Helena+290
  • Saint Kitts and Nevis+1
  • Saint Lucia+1
  • Saint Martin (Saint-Martin (partie française))+590
  • Saint Pierre and Miquelon (Saint-Pierre-et-Miquelon)+508
  • Saint Vincent and the Grenadines+1
  • Samoa+685
  • San Marino+378
  • São Tomé and Príncipe (São Tomé e Príncipe)+239
  • Saudi Arabia (‫المملكة العربية السعودية‬‎)+966
  • Senegal (Sénégal)+221
  • Serbia (Србија)+381
  • Seychelles+248
  • Sierra Leone+232
  • Singapore+65
  • Sint Maarten+1
  • Slovakia (Slovensko)+421
  • Slovenia (Slovenija)+386
  • Solomon Islands+677
  • Somalia (Soomaaliya)+252
  • South Africa+27
  • South Korea (대한민국)+82
  • South Sudan (‫جنوب السودان‬‎)+211
  • Spain (España)+34
  • Sri Lanka (ශ්‍රී ලංකාව)+94
  • Sudan (‫السودان‬‎)+249
  • Suriname+597
  • Svalbard and Jan Mayen+47
  • Sweden (Sverige)+46
  • Switzerland (Schweiz)+41
  • Syria (‫سوريا‬‎)+963
  • Taiwan (台灣)+886
  • Tajikistan+992
  • Tanzania+255
  • Thailand (ไทย)+66
  • Timor-Leste+670
  • Togo+228
  • Tokelau+690
  • Tonga+676
  • Trinidad and Tobago+1
  • Tunisia (‫تونس‬‎)+216
  • Turkey (Türkiye)+90
  • Turkmenistan+993
  • Turks and Caicos Islands+1
  • Tuvalu+688
  • U.S. Virgin Islands+1
  • Uganda+256
  • Ukraine (Україна)+380
  • United Arab Emirates (‫الإمارات العربية المتحدة‬‎)+971
  • United Kingdom+44
  • United States+1
  • Uruguay+598
  • Uzbekistan (Oʻzbekiston)+998
  • Vanuatu+678
  • Vatican City (Città del Vaticano)+39
  • Venezuela+58
  • Vietnam (Việt Nam)+84
  • Wallis and Futuna (Wallis-et-Futuna)+681
  • Western Sahara (‫الصحراء الغربية‬‎)+212
  • Yemen (‫اليمن‬‎)+967
  • Zambia+260
  • Zimbabwe+263
  • Åland Islands+358
*Get instant homework help from top tutors—just a WhatsApp message away. 24/7 support for all your academic needs!

Recently Asked chemical process calculations Questions

Expert help when you need it
  • Q1: Problem 2. Consider the spherical reboiler problem examined in EPAs 2 and 3. Using the linearized model from EPA No. 3, Problem 2, obtain the transfer functions that re-late changes in the inlet and outlet flow rates to changes in level. Draw a block diagram representation for the linearized model that incorporates these transfer functions.See Answer
  • Q2: 1-9. Codes, standards, and regulations: Go to the www.osha.gov web site and look up the OSHA regulation CFR 1910.119: Process Safety Management of Highly Hazardous Chemicals. Use Appendix A to determine the threshold quantities for the following chemicals. If your plant site exceeds this threshold quantity, then this standard applies. a. Ammonia, anhydrous b. Chlorine c. Hydrogen fluoride d. Propylene oxideSee Answer
  • Q3: A process description for a reagent mixing and delivery system is provided below. NaHS (a dry powder) is delivered by truck to the mine site in 25 kg bags. The dry NaHS powder is mixed with water in a mixing tank to 5% strength. The resultant NaHS solution is then sent to a storage tank, which is large enough to store one week's supply of 5% strength reagent solution.The fumes from the solutions are hazardous, and need to be sent to a scrubber before release to the atmosphere. Therefore, there is a connection for vapour discharge from both the mixing tank and the storage tank to the scrubber to treat vapour from the tanks before release to the atmosphere. Another reagent, SMBS, is similarly mixed with water and stored in another parallel reagent mixing and delivery system. Similarly, the vapour from SMBS solution is hazardous, and is sent to a scrubber for treatment before release to the atmosphere. There are therefore two parallel reagent mixing and storage systems. The two reagent mixing and storage systems are similar, so in order to allow for plant flexibility, it is proposed to connect each mixing tank with both storage tanks in the parallel trains. This would allow for storage of excess reagent from one train in the second train if required during the operation. Draw a PFD for the two interconnected reagent and mixing systems. Below is a copy of icons that may be useful to use in your PFD: marks)The vapours from SMBS solutions and NaHS solutions are not compatible and can aggressively react producing heat and corrosive liquids when they come into contact. Conduct a HAZOP for the vapour feed lines from the mixing tank and storage tank to one of the scrubbers. Conduct the HAZOP for the process variable "Flow" only. A risk matrix is provided below for use when conducting the HAZOP. Are there any design changes that you would propose to this system as a result of conducting the HAZOP? Discuss.See Answer
  • Q4: Question 3. A pumping station is used to pump water from a nearby river to a covered storage tank for use on a farm. The tank should be kept full so that water is available for the irrigation system on the farm. Another pump is then required to pressurise the irrigation system using water from the tank when required. (a) (10 marks) On the next page, sketch a P&ID for a feedback controller that willmaintain a high level in the tank and allow for water to be used for irrigation ondemand. The following icons may be useful to use when drawing the P&ID: (b) (8 marks) There are two situations on the farm that could cause damage to the pumps.If the pressure on the suction side of either pump is too low, cavitation in the pump can occur. In addition, if the irrigation system is blocked, the pressure can build in the pipework and cause damage and leakage in the irrigation pipework. On the next page,draw a P&ID showing a system to protect the pumps and irrigation system from damage due to these two events. (c) (5 marks) A PID controller is used for the level controller on the tank. Discuss what can happen to the integral action of the controller if override control in implemented.What can be done to avoid problems with integral control in an override control situation?See Answer
  • Q5: The response of the liquid level in a tank is given by the first-order differential equation: A \frac{d h(t)}{d t}=q_{0}(t) where h(t) is the level in the tank in m, gdt) is the flow of the liquid into the tank in m/s, and A =0.5 m is the constant area of the tank in m2. \text { Obtain the transfer function for the tank, } G(s)=\frac{H(s)}{Q_{0}(s)} Assume that initially the valve of the inlet stream was completely closed and the level in thetank was h(0) = 0.25 m. At t = 0, the valve was opened, and the flowrate was maintained atgo(0) = 0.25 m/min. Knowing that the height of the tank is 3.5 m, after which the tank willoverflow. Determine the time needed to fill up the tank. O Simulate and plot the responses obtained in parts (b) and (c). \text { Obtain the response of the level to a unit step in flow, } q_{o}(t)=u(t) .See Answer
  • Q6:P4.36 100 gmol/min of a solution of 70 mol % ethanol/30 mol % water is fed to a reactor operating at steady state, along with 80 gmol/min of air (79 mol % N₂, 21 mol % O₂). Ethanol (C₂H5OH) reacts with oxygen to make acetaldehyde (CH,CHO). Acetaldehyde is further oxidized to acetic acid (CH₂COOH). Write the two stoichiometrically balanced chemical equations. What is the byproduct of the reactions? What is the limiting reactant? If there is 100% conversion of the limiting reactant and the production rate of acetaldehyde is 25 gmol/min, calculate the fractional conversion of the excess reactant, the yield of acetaldehyde from ethanol, and the composition and flow rate of the reactor effluent stream. See Answer
  • Q7:P4.41 Hydrogen reacts with iron oxide (Fe₂O3) to produce metallic iron (Fe), with water vapor as a byproduct. 100% conversion of Fe₂O3 is achieved, and the metallic iron is easily separated from the hydrogen-water vapor mixture. The water is condensed, and the hydrogen is recycled. The hydrogen source is contaminated with 1 mol % CO. The recycle:fresh feed ratio is 4:1, and the maximum allowable CO in the gas fed to the reactor is 2.5 mol %. Draw a flow diagram, and complete a DOF analysis. Then calculate the single-pass and overall conversion of H₂ as well as all process flows, for a production rate of 1 ton/day metallic iron. (Hint: Consider changing basis to the gas feed.)See Answer
  • Q8:Problem 4-1-Butanol reactor variations The dehydration of 1-butanol to isobutene is run as an equilibrium-limited reaction with Keq = 2.4 atm at T = 323 K. The gas-phase reactor is operated at 1atm total pressure, and the feed is to contain 10 mole/min 1-butanol. (CH3)3COH -- (CH3)2C=CH2 + H₂O a) Calculate the equilibrium conversion expected when the feed is pure 1-butanol vapor. Also report the outlet composition and total molar flow rate. b) Calculate the equilibrium conversion expected if this reactor is operated at a total pressure of 0.2 atm. Also report the outlet composition and total molar flow rate. c) It is common to add nitrogen or another inert gas to the feed stream to increase the butanol conversion. Calculate the fractional conversion of butanol expected when the feed is 20 mole% 1-butanol and 80 mole% nitrogen, at the same total pressure and butanol flow rate as before. Also report the outlet composition and total molar flow rate. d) Comment briefly on the difference between the conversions expected for these conditions. Give advantages and disadvantages of each plan.See Answer
  • Q9:Question 1 [20 points] Propane (C3H8) is stored in a tank at a temperature of 400°C and a pressure of 2 atm. a) Show if the ideal gas law can be used for this calculation. [10 pts] b) Calculate the specific volume of the tank. [10 pts]See Answer
  • Q10:Question 2 [20 points] Consider a mixture of methanol (55%), formaldehyde (23%) and a variety of other solvents. If the other solvents have an average density of 0.831 g/cm3, estimate the density of the mixture a) Assuming volume additivity [10 pts] b) Assuming average of the pure-component density [10 pts] The density of methanol and formaldehyde are 798 kg/m3 and 815 kg/m3, respectively.See Answer
  • Q11:Question 3 [40 points] Heptane (C6H₁4) at 250 °C and 12 MPa absolute flows into a reactor at a rate of 200 kg/h. a) Calculate the volumetric flow rate of this stream using conversion from standard conditions. [20 pts] b) Calculate the volumetric flow rate of this stream using ideal gas EOS. [10 pts] c) Which method is accurate? Explain. [10 pts]See Answer
  • Q12:Question 4 [20 points] A gas occupies a volume of 10 liters at standard temperature and pressure (STP). If the gas is suddenly compressed to half its initial volume while maintaining the same temperature, what will be the new pressure of the gas. Show all calculation steps.See Answer
  • Q13:Name: Rawon Sanad Problem 1: [20% ] Show complete steps of your solution بیگی 1) [10% ] Determine the enthalpy change and the entropy change of CO2 per unit mass as it undergoes a change of state from 365 K and 14.78 MPa to 380 K and 22.17 MPa, by accounting for the deviation from ideal-gas behavior. Using Zn Name: Te/nit undergoes deviation Rawan Sanad Name: 2) [10% ] A mixture of gases consists of 30 kg of oxygen, 60 kg of carbon dioxide, and 10 kg of This mixture is maintained at 120 kPa and 37°C. Determine the following a) The mole fraction of oxygen b) The mole fraction of carbon dioxide c) The partial pressure of helium d) The apparent molecular weight of this mixture e) The volume of the mixtureSee Answer
  • Q14:Psych ormal dic Pr ric ir Name: Pawan Sanad Problem 2: (20% ] Show complete steps of your solution 1) [10% ] A room is filled with 120 kg of air at 75 kPa, 30°C dry-bulb temperature and 28.92% relativ humidity. Determine the following: a) The partial pressure of water vapor b) The partial pressure of dry air c) The humidity ratio d) The enthalpy of the mixture per unit mass of dry air e) The dew-point temperature f) The volume of the room anal //////nRawam Sanad Name: 2) [10%] Butane (C4H10) is burned with 180 percent theoretical air. Write the balanced combustion equation and determine the air-fuel mass ratio. F C4H10 + (02 +3.76N₂) → CO₂ + _H₂O + OLD MA _0₂+ N₂See Answer
  • Q15:# V=320 P=latin Air flowing at 320 m/min is to be conditioned in a constant pressure process at 1 atm from 43°C& and 40 percent relative humidity to 25°C dry bulb and 18.5°C wet bulb. The air is first passed ove T= 43°C coils to remove all the moisture necessary to achieve the final moisture content and then is heating coils to achieve the final state. Fill in the properties table [8%) and determine the following: =40% passed T₁=25°C Twbs=18.5°C 1 2 3 Name: Problem 3: [30%] Tab (°C) 43 -Y = Pv 8.71 25 Pu 117057 P- sat _=W3 Pu = Pesat Heating coils teleeeeeeeeeeeee W₂ =W₂ from then ermine $ (%) 40 too 2 chart (0 2 state 2 $/2=100%. 0.0714 1.635 1.635 a) [3%] Sketch the process on the provided psychrometric chart. b) [2%] The mass flow rate of air in "kg/s" →Pv₁ = 3.484 kpa Cooling coils P=1₁7057 15°C h (kJ/kga) llllllle 1 atm Condensate Condensate removal (m³/kga) T=43 Pat= 8.71 kpap W 0.622 Pu P-PU = 0.622 (3.484) 8.71 (3,484) = 0.0714 T₁=43°C ₁-40% State Twb (°C) اسپنسه 18.5 |Tz=15°C1 Sot = 1.7057 Ⓒ 0,622(1.7057) 1.50 1176037-(1.1257) التي 1/2 = 1.639 8=. 12 2 1.55 T=25°C =316= 0.60 065 03/nName: c) [5%] The rate of condensation in cooling section in "kg/s" d) [7%] The rate of heat removal in the cooling section in "kW" e) [5%] The rate of heat input in the heating section in "kW"See Answer
  • Q16:Name: Problem 4: [30%] percent excess air that also enters at 25°C. The products leave the combustion chamber at 1200 A special n-Dodecane fuel (C12H26) at 25°C is burned in a steady-flow combustion chamber with Assuming combustion is complete, write the balanced equation [5%] and determine the following: C12H26+. a) 5%] Fill in the following table: Substance hº, kJ/kmol C12H26 0₂ N₂ H₂O (g) CO₂ _H₂0+0₂ +_______N₂ (0₂ +3.76N₂)→CO₂+H₂0+. C12H26 25°C Air 80% excess air 25°C h298K kJ/kmol 3500 kJ/s Combustion chamber P= 1 atm KTE ZON h1200K kJ/kmol Products 1200K Nas/nName: 2 b) [10% ] Calculate the heat transfer per kmol of the fuel c) 5% determine the required mass flow rate of the fuel to supply heat at a rate of 3500 kJ/s. d) [5%] determine the required mass flow rate of air in “kg/s”.See Answer
  • Q17:Assignment 1 (Mass Balances) Part 1.A 26 Marks In the first assignment (Mass Balances) you will conduct "hand-calculation" of feedstock preparation and methanol synthesis route. Biomass (sugarcane bagasse) is gasified in a novel Reactive Flash Volatilisation (RFV) process to produce synthesis gas, along with biochar and water-soluble tar as by- products. In a pilot plant RFV process, pulverised biomass is feed to catalytic gasifier at a rate of 10.0 kg/h, along with 4.2 L(STP)/h of O₂ and 6.4 kg/h of steam as the gasifying agents. The biomass and oxygen are supplied at room temperature, whereas the steam is fed at 150°C and the gasifier operates at 800°C. The steam is supplied in excess; therefore, the unreacted water vapour exiting the gasifier with the synthesis gas is condensed at room temperature before the synthesis gas is sent for further processing. The condensed water can be assumed to contain all of the water-soluble tar produced in the gasifier. The biochar is periodically drawn from the gasifier and sent for analysis. Table 1 provides the ultimate and proximate analysis of sugarcane bagasse, whereas Table 2 shows the raw data for synthesis gas flow rate (wet basis) and composition (nitrogen and water free basis) measured at the outlet of the condenser. Table 3 provides the ultimate analysis of char and tar collected from the gasifier and condenser, respectively. 1. Conduct an atom species balance for C, N, H and O for the duration of the given measurement and estimate the average carbon conversion efficiency (percentage of carbon conversion into gas phase). (18 Marks) 2. Report the errors in mass balance analysis and reflect upon the reasons for those errors. What could be the reasons behind mass balances not closing properly? (8 Marks) Table 1 - Proximate and Ultimate Analysis of Sugarcane Bagasse Ultimate Analysis (% db) Carbon (C) Hydrogen (H) Nitrogen (N) Sulphur (S) Oxygen (0)" Proximate Analysis Moisture Ash Volatile Matter Fixed Carbon * Calculated by difference. 46.40 6.19 0.44 0.05 44.42 (% as received, db except moisture) 10.0 2.5 79.16 18.13/nSample Yield name (kg/h) Biochar Tar 0.262 1.552 N 0.472 0.794 Composition (wt% ) H 0.419 7.458 с 50.833 0.243 S N.D. N.D. Part 1.B The synthesis gas produced from the RFV process is pretreated to make the feed for methanol synthesis process. The pretreated synthesis gas feed enters the methanol synthesis plant at a flow rate of 100.0 kmol/h and contains 1.0% methane (inert) with the remainder being a stoichiometric mixture of CO and H₂. This stream is mixed with a recycle stream to produce a stream which is fed to the reactor. The product of the reactor is at equilibrium conversion based on reaction (2) and enters a condenser which condenses some of the methanol. The overhead gas product contains 5.0 mol% methane, 5.0% methanol, 30.0% CO and the remaining H₂. 5.0% of the overhead gas is purged to 26 Marks prevent build-up of the methane and the rest is recycled. The liquid product from the condenser contains pure methanol. A. Draw and clearly label the block flow diagram. Calculate the following- B. The molar flow rate of the purge stream. C. The molar flow rate of the liquid methanol stream. D. The equilibrium constant K based on the mole fractions. E. The composition of the recycle stream on a mass basis. F. The overall and single pass fractional conversion of CO in the reactor. (4 Marks) (3 Marks) (3 Marks) (10 Marks) (3 Marks) (3 Marks)See Answer
  • Q18:Discuss a typical refrigeration cycle. Next, describe how the cycle would be altered to operate as a high temperature heat pump to produce low pressure steam. Waste heat from hot exhaust is available at 75°C and a suitable working fluid is available for heat transfer from the hot exhaust to the steam. Explain the trade-offs in the system, the most expensive component of the system, and how compression ratio impacts heat exchanger design. You must include a technical drawing of the physical system, as well as the vapor compression cycle on a pressure-enthalpy diagram. Drawings and figures cannot be prepared by hand, but must be prepared inSee Answer
  • Q19:1. Solve Example 4.10 using the mole ratios. EXAMPLE 4.10 Absorption of SO, with Water. 200 kmol/h of feed gas, F, containing 2 mol% SO, and 98 molair is contacted in a single equilibrium stage with 1,000 kmol/h of pure water, W, at 25°C and 10 atm to absorb SO,. The total flow rates of equilibrium products are G and L. Determine the fraction of So, absorbed. Neglect the absorption of air and the vaporization of water. Assume the applicability of Henry's lawSee Answer
  • Q20:2. Solve Example 4.11 using the total mole of the gas feed = 15 mol (air + ammonia) while the liquid feed - 10 mol (water + ammonia)See Answer

TutorBin Testimonials

I found TutorBin Chemical Process Calculations homework help when I was struggling with complex concepts. Experts provided step-wise explanations and examples to help me understand concepts clearly.

Rick Jordon

5

TutorBin experts resolve your doubts without making you wait for long. Their experts are responsive & available 24/7 whenever you need Chemical Process Calculations subject guidance.

Andrea Jacobs

5

I trust TutorBin for assisting me in completing Chemical Process Calculations assignments with quality and 100% accuracy. Experts are polite, listen to my problems, and have extensive experience in their domain.

Lilian King

5

I got my Chemical Process Calculations homework done on time. My assignment is proofread and edited by professionals. Got zero plagiarism as experts developed my assignment from scratch. Feel relieved and super excited.

Joey Dip

5

TutorBin helping students around the globe

TutorBin believes that distance should never be a barrier to learning. Over 500000+ orders and 100000+ happy customers explain TutorBin has become the name that keeps learning fun in the UK, USA, Canada, Australia, Singapore, and UAE.