Title: ENV 3001 Introduction to Environmental Engineering
1ENV 3001 Introduction to Environmental Engineering
Lecture III (b) Review Session Instructor Dr.
Ni-Bin Chang Spring, 2006
2HW 3.1
Five million kilograms per day of coal are
burned in an electric power plant. The coal
has an ash content of 12 by mass. Forty percent
of the ash falls out the bottom of the furnace.
The rest of the ash is carried out of the
furnace with the hot gases into an electrostatic
precipitator (ESP). The ESP is 99.5 efficient
in removing the ash that comes into it. Draw a
diagram representing this process and calculate
the mass emissions rate of ash into the
atmosphere from this plant.
3HW 3.1
4HW 3.1
Solution
5HW 3.3
clarifier
thickener
The above is a clarifier-thickener system to
separate solids and liquids. Ignore the effect of
solids content on density of the streams (i.e.,
assume density of solids density water).
6HW 3.3
- Complete the following material balance table.
- Stream Flow rate, L/s Solids, mg/L
- A 100 3000
- B 95 15
- C 6000
- D 50
- E
- A
7HW 3.3
8HW 3.3
9HW 3.3
10HW 3.4
- A 600 MW coal burning power plant is burning
Illinois bituminous coal with 8 ash content. - The plant is 39 efficient.
- 35 of the ash drops out in the furnace
- The electrostatic precipitator is 99.0
efficient. - A simplified sketch appears below
11HW 3.4
- a. Draw an energy balance diagram for the plant
and calculate the rate of heat emitted to the
environment, in J/s. - b. Calculate the rate of coal input to the
furnace, in kg/day. - c. Calculate the rate of ash emissions to the
atmosphere, in kg/s.
12HW 3.4
13HW 3.4
- Energy Balance
- Waste heat1579-600979MW
Heat in
14HW 3.4
- Coal input
- Ash to atmosphere
15HW 3.7
- An electrostatic precipitator removes 1000 kg of
particulates per day. - The stack gas from a process contains 4.0 g
particulates per m3 of gas. - The gas flow rate is 5 m3/s.
- What is the emission rate of particulates? Give
answer in kg/day.
16HW 3.7
INOUT or ABC CA-B
17HW 3.9
- A mining processes a silty water into a clean
brook at the rate of 5 m3/min - The silt content is 200 mg/L.
- The brook flows at 50 m3/min in rainy season and
5 m3/min in dry season. - What is the concentration in the brook during the
rainy and dry seasons?
18HW 3.9
In rainy season 50m3/min5 m3/min55 m3/min 50
(0)5(200)55(Ccs) Ccs18.2 mg/L In dry season
5m3/min5 m3/min10 m3/min 5 (0)5(200)10(Ccs) Cc
s100 mg/L
19HW 3.10
- The efficiently of a 800 MW nuclear power plant
is 32 percent. - Assume no heat is lost to the atmosphere directly
from the system. - Calculate the minimum rate at which cooling water
must be pumped through the condensers of the
plant if the maximum cooling water temperature
rise is 15 0F. - Assuming the plant is designed with five
identical pipes in parallel to carry this cooling
water, calculate the diameter of each pipe if the
water velocity is 6.0 ft/sec. - Give your answer in pounds/hr, and ft3/sec.
20HW 3.10
- Coal input
- heat in800/0.32 2500MW
- heat out 2500-8001700MW
21HW 3.11
- A new regulation requires that the wastewater
from a tannery be routed to a municipal
wastewater treatment plant for final treatment. - The tannery wastewater must be pretreated to
remove certain organic pollutants. - The pretreatment process is a biological
anaerobic process that has a limit on total
dissolved solids (TDS) of no more than 20,000
mg/L.
22HW 3.11
23HW 3.11
Rearrange the schematics as below
QM
24HW 3.11
25HW 3.11
Point I balance
QM
26HW 3.11
27HW 3.13
G1
G2
Straight-run gasoline
High-Octane gasoline
G3
Overall balance ?G1 ?G2 ?G3 10,000 gal
28HW 3.13
- Iso-Octane balance
- 0.92 G1 0.63 G2 0.83 (10,000)
- G2 900/0.29 3,103 gal of straight run
- G1 10,000 3,103 6,897 gal of Iso-Octane
29HW 3.15
(a)
- (b) 2A?B, so for each B created , 2A are
destroyed - Destruction rate of A is difference between input
of A its output. - 100(0.10)-100(0.05)5moles A/min being destroyed