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Cornell - BLF - 2
THE JOURNAL OF COMPARATIVE NEUROLOGY 204:318-324 (1982)Cell Death i the Mammalian Visual n System During Normal Development: 11. Superior colliculusB.L. FINLAY, A.T. BERG, AND D.R. SENGELAUB Department of Psychology, Cornell University, Lthaca, Ne
Cornell - BLF - 2
CURRICULUM VITAE Barbara L. Finlay Office address: Department of Psychology Uris Hall Cornell University Ithaca, New York 14853 Phone: (607) 255-6394 FAX (607) 255-8433 blf2@cornell.edu March 31, 2007Website: http:/people.psych.cornell.edu/~blf2/ B
Cornell - CHEM - 112
3. (15 pts) Consider the temperature-composition phase diagrams for A-B mixtures and A-C mixtures.AB mixtures (no C) 240 220 200 T (C) 180 160liq+vap liquid+vaporAC mixtures (no B) 240 220 200 T (C) 180 160 140 120 100liquid+liquid liquid liquid
Cornell - CHEM - 481
Chemical and Biomolecular Engineering 481 Spring 2008Drug Delivery: Engineering Principles for Drug Therapy by W.M. Saltzman (Oxford University Press, 2001) Basic Transport Phenomena in Biomedical Engineering by R.L. Fournier (Taylor & Francis, 199
Cornell - CHEM - 112
4. Solution(A) The number of stages is given by the number of times the McCabe-Thiele steps contact the equilibrium line. There are 12 stages in this column. The feed stage is the step that changes from the lower (stripping) operating line to the mi
Cornell - CHEM - 112
3. SolutionOur goal is to synthesize P. We need to first synthesize intermediates H and M from A. The numbers in parentheses are flow rates, in mol/min. Note that the 50% of the A is converted in the reactor.A (1) H (0.5) M (0.5) H (0.5) M (0.5) li
Cornell - CHEM - 112
1. Solution(A) Begin with a mass balance around the entire process. Because we are given the compositions of all streams entering and leaving the process, and we are given the flow rate of one stream, we can calculate the flow rates of all streams.
Cornell - CHEM - 112
5. Solution(A) Stream 1 is at T = 20C, such that the partial pressure of H2O is 33% of the partial pressure at the dew point - the partial pressure at the border to the liquid+vapor region. At 20C, the dew point is 0.023 atm, so 33% humidity is 0.00
Cornell - TMD - 10
5. Solution(A) Stream 1 is at T = 20C, such that the partial pressure of H2O is 33% of the partial pressure at the dew point - the partial pressure at the border to the liquid+vapor region. At 20C, the dew point is 0.023 atm, so 33% humidity is 0.00
Cornell - TMD - 10
Last Update: August 9, 2007Page viii. The table of contents at the top of the page should read "3.2 The Conservation Principles" Pages 21-22. The last paragraph on page 21. The comment about recycling the heptane/propanol output from the washer is w
Cornell - CHEM - 112
2. Solution(A) Nomenclature: Total flow rate of stream i FT,i H2O flow rate of stream i FW,i Vegetable flow rate of stream i Fveg,i Note that water enters by stream 3 only and leaves by stream 2 only. Draw system borders around the entire process
Cornell - TMD - 10
2. Solution(A) Nomenclature: Total flow rate of stream i FT,i H2O flow rate of stream i FW,i Vegetable flow rate of stream i Fveg,i Note that water enters by stream 3 only and leaves by stream 2 only. Draw system borders around the entire process
Cornell - CHEM - 112
4. (30 pts) The feed to a distillation column is split: the two streams are heated and fed to a distillation column. The McCabe-Thiele analysis is shown on the next page.condenser 4 liquid at its bubble point heater 1 2 7 598. mol% methanol 2.0 m
Cornell - TMD - 10
4. (30 pts) The feed to a distillation column is split: the two streams are heated and fed to a distillation column. The McCabe-Thiele analysis is shown on the next page.condenser 4 liquid at its bubble point heater 1 2 7 598. mol% methanol 2.0 m
Cornell - CHEM - 112
Design Competition OverviewProduce P by the reaction A P, which is accompanied by a parallel reaction, A B. Both reactions are irreversible. Both reactions are incomplete; the reactor effluent contains reactant A, product P and worthless by-produc
Cornell - TMD - 10
Design Competition OverviewProduce P by the reaction A P, which is accompanied by a parallel reaction, A B. Both reactions are irreversible. Both reactions are incomplete; the reactor effluent contains reactant A, product P and worthless by-produc
Cornell - CHEM - 112
3. (50 pts) Design a process to produce P from reactants A and B. The reaction sequence begins with the reaction ofA to two intermediates: H and M. 2A H + M 50% of A reacts. The reaction is irreversible.Both intermediates H and M react with B to
Cornell - TMD - 10
3. (50 pts) Design a process to produce P from reactants A and B. The reaction sequence begins with the reaction ofA to two intermediates: H and M. 2A H + M 50% of A reacts. The reaction is irreversible.Both intermediates H and M react with B to
Cornell - CHEM - 112
2.(25 pts) Consider the following process to separate a mixture of hexane (H) and chlorobenzene (CB). The pressure in each flash drum is 1 atm. Heaters, coolers and pumps are not shown.4 vapor 2 50. mol% H 50. mol% CB 1 20C liquid 3 6 flash drum 3 l
Cornell - TMD - 10
2.(25 pts) Consider the following process to separate a mixture of hexane (H) and chlorobenzene (CB). The pressure in each flash drum is 1 atm. Heaters, coolers and pumps are not shown.4 vapor 2 50. mol% H 50. mol% CB 1 20C liquid 3 6 flash drum 3 l
Cornell - TMD - 112
2.(25 pts) Consider the following process to separate a mixture of hexane (H) and chlorobenzene (CB). The pressure in each flash drum is 1 atm. Heaters, coolers and pumps are not shown.4 vapor 2 50. mol% H 50. mol% CB 1 20C liquid 3 6 flash drum 3 l
Cornell - CHEM - 112
1. SolutionThe key parameter for judging a design is Return on Investment, or ROI. To compare the ROI for Scheme I to the ROI for Scheme II, we need to compare the profit and capital cost of each scheme, because ROI = profit/(capital cost). To compa
Cornell - TMD - 10
1. SolutionThe key parameter for judging a design is Return on Investment, or ROI. To compare the ROI for Scheme I to the ROI for Scheme II, we need to compare the profit and capital cost of each scheme, because ROI = profit/(capital cost). To compa
Cornell - TMD - 112
1. SolutionThe key parameter for judging a design is Return on Investment, or ROI. To compare the ROI for Scheme I to the ROI for Scheme II, we need to compare the profit and capital cost of each scheme, because ROI = profit/(capital cost). To compa
Cornell - CHEM - 112
2. Consider this continuous process for steaming dry vegetables taken directly from a refrigerator.dry vegetables 0.0C 43.5 kg/min 1 steam 100.C 5 cooker wet vegetables 7.0 wt% water (liquid) 75.C 2water 20.C 34 boilersteam 150.Cqin(A) Cal
Cornell - TMD - 10
2. Consider this continuous process for steaming dry vegetables taken directly from a refrigerator.dry vegetables 0.0C 43.5 kg/min 1 steam 100.C 5 cooker wet vegetables 7.0 wt% water (liquid) 75.C 2water 20.C 34 boilersteam 150.Cqin(A) Cal
Cornell - TMD - 112
2. Consider this continuous process for steaming dry vegetables taken directly from a refrigerator.dry vegetables 0.0C 43.5 kg/min 1 steam 100.C 5 cooker wet vegetables 7.0 wt% water (liquid) 75.C 2water 20.C 34 boilersteam 150.Cqin(A) Cal
Cornell - CHEM - 112
1. In lecture we considered three schemes for producing 100. kg/min of 1-phenyl propene (Propylbenzene, designated P) from 3-phenyl propene (Allyl benzene, designated A). A is dissolved in solvent 1-heptanol (designated S). The reactor effluent is e
Cornell - TMD - 112
1. In lecture we considered three schemes for producing 100. kg/min of 1-phenyl propene (Propylbenzene, designated P) from 3-phenyl propene (Allyl benzene, designated A). A is dissolved in solvent 1-heptanol (designated S). The reactor effluent is e
Cornell - TMD - 10
ChemE 390 - Chemical Kinetics & Reactor Design Second Preliminary Examination April 17, 2007Name1 _ / 25 2 _ / 15 3 _ / 15 4 _ / 20 5 _ / 25Total _ / 100Your exam should have 8 pages. Allotted Time: 90 minutes.Show all work.Academic integr
Cornell - TMD - 10
ChemE 3900 - Chemical Kinetics & Reactor Design Templates for graphical analysis of CSTRs and PFRs 1st Order Reaction, k = 1/min, [A]0 = 1 mol/L108 reciprocal rate, 1/r (Lmin)/mol6420 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 fractional conv
Cornell - CHEM - 112
2.17 A common error is to assume that I (impurity) can be separated from the aqueous solution of Fbecause I is a solid at temperatures below 62C. This assumption is wrong. Consider salt water. Although salt is a solid at room temperature, it is not
Cornell - TMD - 10
2.17 A common error is to assume that I (impurity) can be separated from the aqueous solution of Fbecause I is a solid at temperatures below 62C. This assumption is wrong. Consider salt water. Although salt is a solid at room temperature, it is not
Cornell - TMD - 112
2.17 A common error is to assume that I (impurity) can be separated from the aqueous solution of Fbecause I is a solid at temperatures below 62C. This assumption is wrong. Consider salt water. Although salt is a solid at room temperature, it is not
Cornell - CHEM - 112
3.4 Nomenclature:Total flow rate of stream i FT,i Water flow rate of stream i FW,i Solids flow rate of stream i FS,i(A) Strategy: The flow rates of streams 1 and 2 are known. Write a mass balance to calculate FT,3. Because stream 2 is 100% wat
Cornell - TMD - 10
3.4 Nomenclature:Total flow rate of stream i FT,i Water flow rate of stream i FW,i Solids flow rate of stream i FS,i(A) Strategy: The flow rates of streams 1 and 2 are known. Write a mass balance to calculate FT,3. Because stream 2 is 100% wat
Cornell - TMD - 112
3.4 Nomenclature:Total flow rate of stream i FT,i Water flow rate of stream i FW,i Solids flow rate of stream i FS,i(A) Strategy: The flow rates of streams 1 and 2 are known. Write a mass balance to calculate FT,3. Because stream 2 is 100% wat
Cornell - CHEM - 112
2.16 Some recommended criteria for grading:General rules for process flow sheets: 1. One operation per unit. 2 Matter is neither created nor destroyed. Rules specific to this design: 1. Facts given in the exercise statement should not be violated. F
Cornell - TMD - 10
2.16 Some recommended criteria for grading:General rules for process flow sheets: 1. One operation per unit. 2 Matter is neither created nor destroyed. Rules specific to this design: 1. Facts given in the exercise statement should not be violated. F
Cornell - TMD - 112
2.16 Some recommended criteria for grading:General rules for process flow sheets: 1. One operation per unit. 2 Matter is neither created nor destroyed. Rules specific to this design: 1. Facts given in the exercise statement should not be violated. F
Cornell - CHEM - 112
3.8(A) Divide orange juice into two components: water and non-water ingredientsNomenclature: Total flow rate of stream i FT,i Water flow rate of stream i FW,i Nonwater (others) flow rate of stream i FO,iFW ,1 FT ,1 FW ,3 FT ,3 = FW ,1 FW ,1 + FO
Cornell - TMD - 10
3.8(A) Divide orange juice into two components: water and non-water ingredientsNomenclature: Total flow rate of stream i FT,i Water flow rate of stream i FW,i Nonwater (others) flow rate of stream i FO,iFW ,1 FT ,1 FW ,3 FT ,3 = FW ,1 FW ,1 + FO
Cornell - TMD - 112
3.8(A) Divide orange juice into two components: water and non-water ingredientsNomenclature: Total flow rate of stream i FT,i Water flow rate of stream i FW,i Nonwater (others) flow rate of stream i FO,iFW ,1 FT ,1 FW ,3 FT ,3 = FW ,1 FW ,1 + FO
Cornell - CHEM - 112
3.9 Nomenclature:Total flow rate of stream i FT,i Protein flow rate of stream i FP,i Fiber flow rate of stream i FF,i Hexane flow rate of stream i FH,i(A) Strategy: Calculate the total flow rate of stream 2 from the flow rates of protein, fib
Cornell - TMD - 10
3.9 Nomenclature:Total flow rate of stream i FT,i Protein flow rate of stream i FP,i Fiber flow rate of stream i FF,i Hexane flow rate of stream i FH,i(A) Strategy: Calculate the total flow rate of stream 2 from the flow rates of protein, fib
Cornell - TMD - 112
3.9 Nomenclature:Total flow rate of stream i FT,i Protein flow rate of stream i FP,i Fiber flow rate of stream i FF,i Hexane flow rate of stream i FH,i(A) Strategy: Calculate the total flow rate of stream 2 from the flow rates of protein, fib
Cornell - TMD - 10
3.13 Nomenclature:Total flow rate of stream i FT,i Water flow rate of stream i FW,i Nitric Acid flow rate of stream i FNA,i (A) Draw system borders around the entire process and write a mass balance on nitric acid (HNO3).rate in = rate out FNA,
Cornell - TMD - 112
3.13 Nomenclature:Total flow rate of stream i FT,i Water flow rate of stream i FW,i Nitric Acid flow rate of stream i FNA,i (A) Draw system borders around the entire process and write a mass balance on nitric acid (HNO3).rate in = rate out FNA,
Cornell - TMD - 10
5.8 Prepare a table of the parameters, their symbols, and dimensions.parameter length fluid velocity specific heat fluid density thermal conductivity symbol dimensions l v CP k L L/TM L2 /T 2 joules L2 [ =] [ =] kg K M T2M/L3joules ML2 /T 2 ML
Cornell - CHEM - 112
3.21 For parts (A) and (B) it is useful to focus on the overall schemes, as diagrammed below, ignoring theflows out the purge streams.C2H2 (1 mol/min) HCl (1.2 mol/min) 13 C2H3Cl (0.8 mol/min) C2H4Cl2 (0.2 mol/min) scheme I 4C2H2 (1 mol/min) H
Cornell - TMD - 112
3.21 For parts (A) and (B) it is useful to focus on the overall schemes, as diagrammed below, ignoring theflows out the purge streams.C2H2 (1 mol/min) HCl (1.2 mol/min) 13 C2H3Cl (0.8 mol/min) C2H4Cl2 (0.2 mol/min) scheme I 4C2H2 (1 mol/min) H
Cornell - CHEM - 112
EngrI 112 - Introduction to Chemical Engineering4.lever.4 Draw a lever from ice at 12C (355 kJ/kg) to steam at 215C (2920 kJ/kg) and add masses corresponding to the flow rates of streams 1, 2, and 3.(Water at 16C is at 65 kJ/kg.)4 10 6solid -200
Cornell - TMD - 10
EngrI 112 - Introduction to Chemical Engineering4.lever.4 Draw a lever from ice at 12C (355 kJ/kg) to steam at 215C (2920 kJ/kg) and add masses corresponding to the flow rates of streams 1, 2, and 3.(Water at 16C is at 65 kJ/kg.)4 10 6solid -200
Cornell - TMD - 112
EngrI 112 - Introduction to Chemical Engineering4.lever.4 Draw a lever from ice at 12C (355 kJ/kg) to steam at 215C (2920 kJ/kg) and add masses corresponding to the flow rates of streams 1, 2, and 3.(Water at 16C is at 65 kJ/kg.)4 10 6solid -200
Cornell - CHEM - 112
4.di.1 Solution(A) The number of stages is given by the number of times the McCabe-Thiele steps contact the equilibrium line. There are 11 stages in this column. The feed stage is the step that changes from the lower (stripping) operating line to th
Cornell - TMD - 10
4.di.1 Solution(A) The number of stages is given by the number of times the McCabe-Thiele steps contact the equilibrium line. There are 11 stages in this column. The feed stage is the step that changes from the lower (stripping) operating line to th
Cornell - TMD - 112
4.di.1 Solution(A) The number of stages is given by the number of times the McCabe-Thiele steps contact the equilibrium line. There are 11 stages in this column. The feed stage is the step that changes from the lower (stripping) operating line to th
Cornell - CHEM - 112
4.de.16 Solution(A) It is useful to label some more landmarks on the ternary diagram: pure water, pure sugar, and pure I. Streams 4 and 5 are in equilibrium. Therefore, streams 4 and 5 lie at the ends of a tie line that spans the two phase: solution