aqueous solution of H-SO, (Solution A) is to be mixed with a H;SO, (Solution B) to produce a 75.0 wt% solution (Solution C).- Solution A Flowmeter A Analyzer Solution C 75% H2S0, Solution B 90% H,SO, Flowmeter B MIXER The flow rate and concentration of Solution A change periodically, so that it is necessary to adjust the flow rate of Solution B to keep the product H,SO, concentration constant. Flowmeters A and B have linear calibration plots of mass flow rate (mn) versus meter reading
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- Ex7; An aqueous solution of sodium hydroxide contains 20.0% NaOH by mass. It is desired to produce an 8.0% NaOH solution by diluting a stream of the 20% solution with a stream of pure water. Calculate the ratios (liters H20/kg feed solution) and (kg product solution/kg feed solution). F =? kg = 0.2 XNaOH P =? kg XH,0 = 0.8 F2 =? kg F2 = 0.08 kg Na0H/kg xH,0 = 0.92 kg H20/kg %3D 16.4 y la Q1. The distribution coefficient, KD (Cether/Cwater), for an organic substance X at roon temperature is 10.what relative volumes of ether to water should be used for the extraction of 90 percent of X from a water solution in a single extraction? KD - Celtier C wieher as there is 90yof cachion o solute rome water in ether. 90g of solute is in elher log of salue will be in wafer %3D 1o - 1o 3/vether lo 90XV water -> log/v water loxV ether loxvelther axV waher Velher V waher Q2.Achieving better liquid-liquid phase extraction and 100% separation with one single extraction, what you must to do? Organic Chemistry Ome_ap.50 A too kmal/h stream that is 97 msle % Carbon tetrachlorice Ccc4) and 3 % Carbon disullide ccs) is to be recovered Prom the bottom of a distillation column. The feed to the column is 16 mole % CS, and 84 % Cc4, and 2 % of the cc4 enterirg the column is contained in the overhead stream leaving H top of 'the column- O a flow charf of the pocess and do the degree-of- Drae and label freedom analysis- Clculate the mass and mle fracklons of Ccl4 in the overhend stranm, and determine He malar Piow rates of cc4 & CS, in the overhend and feel streams
- Tirofiban (C22H36N2O5S MWt = 440.6) is present as tirofiban HCI monohydrate (C22H36N2O5S.HCI.H₂O MWt=495.1) at 0.281 mg/mL in a concentrated solution. A solution for infusion is prepared by extracting 50 mL from a 250 mL bag of 5% glucose solution and adding 50 mL of concentrated solution. Sofia who weighs weighs 87 kg requires a tirofiban dose of 0.1 mcg/kg/min for 12 to 24 hours. What would the infusion rate be (mL/h)? (Answer to 1 decimal place.) Answer: 125.28 X令 。 B/s 因 1:Y9 404 2_543841247.. Use of the Normal Law Normality (N) = Wt /Eq.wt 1000/V(ml) Wt (gm) =Weight of sodium carbonate V (ml) = solution volume N= Normality Discussion: 1. What is the equivalent weight of the vehicle? primary standard? 2. Why is sodium carbonate 3- Attend naciN 3.3 solution in a 253 mi volume bottle. 4- Calculate the caliber of sodium carbonate if the weight of sodium carbonate gm 2 and the size of the bottle volume is 100ml Results Sheet Name: Group: Date: Signature 1-Calculations: 2-Aim of experiment: 3-Theoretical results M(Na2Co3).. .. Weight required= 4-Observations: 个Two aqueous sulfuric acid solutions are available at a processing facility: 20.0 wt% H2SO4 (sg = 1.139) 60.0 wt% H2SO4 (sg = 1.498) It is desired to mix the two solutions such that the final product has a concentration of 4.00 M (sg-1.213). There is 100 kg of the 20% solution available. If all of this is to be used, calculate: The mass of 60% solution needed The mass and composition of the final product
- In a process producing KNO3 salt, 1000 kg/h of a feed solution containing 10 wt% KNO3 is fed to an evaporator, which evaporates some water at 422 K to produce a 50 wt% KNO3 solution. This is then fed to a crystallizer at 311 K, where crystals containing 98 wt% KNO3 are removed. The saturated solution containing 37.5 wt% KNO3 is recycled to the evaporator. Calculate the amount of the recycle stream R in kg/h and the product stream of crystals P in kg/h.Mganga is doing a routine analysis in a copper plating factory. He is regularly making up solutions of verypure CuSO4.5H2O. He suspect that a batch of a reagent used to make up a stock solution of CuSO4.5H2Ois impure and it may contains some CuCl2. He asked you to determine the percentage impurity as follows:Dissolve1.500g of a mixture and make up to 1.00L mark.150mL of this solution was treated with 20.00mLof 0.100M AgNO3 to remove 98.6% of chloride as AgCl precipitate.10.11/ A 1.5-kg specimen of a 90 wt% Pb-10 wt% Sn alloy is heated to 250°C (480°F), at which temperature it is entirely an a-phase solid solution . The alloy is to be melted to the extent that 50% of the speci- men is liquid, the remainder being the a phase. This may be accomplished either by heating the alloy or changing its composi- tion while holding the temperature con- stant. (a) To what temperature must the speci- men be heated? (b) How much tin must be added to the 1.5-kg specimen at 250°C to achieve this state? 10.15) A magnesium-lead alloy of mass 5.5 ka consists of a solid a phase that has a compo- sition that is just slightly below the solubility limit at 200°C (390°F). (a) What mass of lead is in the alloy? (b) If the alloy is heated to 350°C (660°F). how much more lead may be dissolved in the a phase without exceeding the solubility limit of this phase? 10.27 A hypothetical A-B alloy of composition 55 wt% B-45 wt% A at some temperature is found to consist of mass…
- A 4.0 molar sulphuric acid solution (SG = 1.2) is prepared by mixing two aqueous sulphuric acid solutions A and B together: Sulphuric acid solution A: 20 wt% H₂SO4 (SG = 1.1) Sulphuric acid solution B: 60 wt% H₂SO4 (SG = 1.5) Assume the density of pure water is 1,000 kg/m³. Atomic weight of H, S and O are 1, 32, 16 g/mol, respectively. a) Calculate the mass fraction of sulphuric acid in the product solution. b) Use 100 kg of Solution A as a basis, draw a flowchart of this process and perform the degree-of-freedom analysis. c) Calculate the volumetric feed ratio (i.e., litres of Solution A/litres of Solution B).A liquid mixture containing 40.0% benzene (B) and 60% toluene (T) by mass to the distillation column. The upper product stream contains 90 mol% B, and the lower product stream contains 6% of the benzene fed into the column (meaning that 94% of the benzene is left with the upper product). The volumetric flow rate of the feed is 2500 1/ hr and the specific gravity of .the feed mixture is 0.870 A- Rate of mass accumulation B- Component balance equation . The accumulation terms (d/ dt), can also be diminished to zero by assuming steady stateA water containing 50 mg/L of phosphate (PO,") is flowing in an open channel at a volumetric flow rate (Q) of 2 MGD (million gallons per day). (a) What is the concentration of phosphate expressed in (i) mg/L as PO, --P, (ii) mM as PO., and (iii) mM as PO, P. (b) Find the mass flow rate (S) of phosphate through any section perpendicular to the direction of flow in the open channel expressed in lb/day? Given: Atomic weights: P= 31 g/mole, O = 16 g/mole, 1 gallon = 3.785 L, 1 kg = 2.204 Ib. %3D