Concept explainers
(a)
Interpretation:
The density of the methane and nitrogen needs to be determined.
Concept introduction:
The ideal-gas equation (also called as ideal-gas law) gives a decent estimate of numerous gases under certain conditions. The ideal-gas law is displayed below:
Here,
(b)
Interpretation:
The volume of the nitrogen required to displace all the methane from the tank should be calculated.
Concept introduction:
Density is defined as the ratio of Mass of a substance to its volume. A high-density liquid can displace a low-density liquid in a container as the high-density liquid moves down upon mixing it with a low-density liquidand the low-density liquid will move to the top and in this way high density liquid displaces the low-density liquid.
(c)
Interpretation:
The volume of the air needs to increase the oxygen concentration by 20% should be calculated.
Concept introduction:
In general, air consists of 79 mole% Nitrogen and 21 mole% Oxygen.
(d)
Interpretation:
The reason behind using nitrogen for purging instead of air should be explained.
Concept introduction:
Purging is the method of removing moisture content within the equipment to produce dry environment. Mostly the nitrogen is used for the purpose of purging and blanketing.

Want to see the full answer?
Check out a sample textbook solution
Chapter 10 Solutions
EBK ELEMENTARY PRINCIPLES OF CHEMICAL P
- Solve this questionarrow_forwardthe answer is shown but i dont know how to get to itarrow_forward1. (20 points) Steam (6000 kg/h, 10 bar, 400°C) is passed through an adiabatic turbine that drives a shaft to generate power. The steam leaving the turbine is at 0.5 bar and passes to a chiller where heat is removed at the rate of 1.25 x 107 kJ/h. Saturated liquid leaves the chiller at 0.5 bar. (a) How much work (kW) is produced in the turbine? (b) What is the quality of steam leaving the turbine? Sometimes, steam produced is 'wet' in nature, and is composed of saturated water vapor and entrained water droplets. In such cases, quality is defined as the fraction of steam that is vapor.arrow_forward
- WLV2 | Online teaching and × + w.com/ilrn/takeAssignment/takeCovalentActivity.do?locator-assignment-take A १ eq eq eq [Review Topics] [Referen Draw the structure of 3,3-dimethylbutanal in the window below. • In cases where there is more than one answer, just draw one. 985 + / $ Sn [ ] ChemDoodle ? req Submit Answer Retry Entire Group 8 more group attempts remaining req req Cengage Learning Cengage Technical Supportarrow_forwardA flat-sheet membrane of thickness, L, and surface area, S, separates two fluids (see figure). The concentration on the upstream side is maintained at C_A0 while that on the downstream side is maintained at zero. The membrane is loaded with an immobilized enzyme that converts substrate A to product B according to a zero order reaction mechanism given by:R_A=-k_0"' (d) What is the flux, N_A, at the downstream surface (z=L)? (e) Under what condition will the flux at z=L be equal to zero? (f) At the condition in (e), what can you say about the diffusion time relative to the reaction time?arrow_forwardDevelop a purification train for a facility where first process is a perfusion upstream bioreactors 500L producing low cell culture titer of approx. 0.5 g/L perfusing at 2 VVD over 30 days. The current facility has a secondary clarification process for the perfusate coming from the bioreactor. Secondary depth filtration clarification capacity of 200 L/m2. Identify the correct filter area, and system (pump) requirements for the process scale. Also identify optimal flowrates for flushing and processing, total process time, buffer volumes required. Assume 10 L/m2 holdup of the depth filters identify the size of the tank required to collect the filtrate. Average yield of overall clarification is 80% estimate the titer in the clarified pool.arrow_forward
- Bioprocessing/ Protein isolation and purification. Develop a purification train for a facility where first process is a perfusion upstream bioreactors 500L producing low cell culture titer of approx. 0.5 g/L perfusing at 2 VVD over 30 days. The current facility has a secondary clarification process for the perfusate coming from the bioreactor. Secondary depth filtration clarification capacity of 200 L/m2. Identify the correct filter area, and system (pump) requirements for the process scale. Also identify optimal flowrates for flushing and processing, total process time, buffer volumes required. Assume 10 L/m2 holdup of the depth filters identify the size of the tank required to collect the filtrate. Average yield of overall clarification is 80% estimate the titer in the clarified pool.arrow_forwardsolve for both a stripper and absorber. take the equilibrium data given to just be a y=x linearrow_forwardsolve all parts plsarrow_forward
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The





