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Question:
a) List, with appropriate justifications, the most significant design parameters while constructing a landfill
b) Draw the pattern of gas generation in a typical landfill and indicate the different phases.
c) Using the Landgem model of Q =∑ 2KMLoe-kt where Q yearly methane generation rate at time t after solid waste placement in m3 per yr M Solid waste placed t years before present in landfill
k First order rate constant in yr-1
Lo Potential methane generation capacity of the msw in m3 per ton
t Time since start of gas generation
Determine the peak gas production during the first year for a landfill receiving 167000 tons per year. The landfill gas constant is 0.0307 yr-1 and the methane generation potential is 140 m3/tonne.
Beginning in the early nineteenth century, scientists developed models to explain the structure of the atom. As more information was discovered about the nature of the subatomic pa
INTRODUCTION : In this exercise you will learn various steps and procedures adopted while purchasing lab-related items. This exercise will acquaint you with practices of preparing
Q. Show the d-orbital energy level splitting? Let us consider one of the consequences of the d-orbital energy level splitting. [Ti (H2o 6 ) 3+ is a d 1 system meaning that t
define ostwals dilution law
Acetic Acid or Ethanoic Acid Acetic acid is the oldest termed as fatty acid. It is the major constituent of vinegar and therefore its name (Latin acetum = vinegar)
Q. What do you know about Chemical Equilibrium Many chemical changes are reversible and will proceed towards an equilibrium instead of going to completion. The products react w
Borazole is very stable because it is aromatic; each nitrogen contributes two p electrons and each boron contributes zero electrons, for a total of six p electrons in the aromatic
Another way to show that water pressure increases with depth Search a tall tin can. Punch holes up the side of the can about 3 cm apart. Put a strip of adhesive or plastic tape
zinc+copper(ll) chloride
A single-effect evaporator is used to concentrate 60000 kg h-1 of a 40 wt % NaOH solution which is fed to the evaporator at 40°C. The concentrated liquid is a 55 wt % NaOH solut
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