absorption Flashcards

(68 cards)

1
Q

When the two contacting phases are a gas and a liquid, the unit operation is called ?

A

Absorption

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2
Q

are absorbed from the gas phase into a liquid phase in absorption.

A

Solute

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3
Q

This process involves molecular and turbulent diffusion or mass transfer of solute A through a stagnant non-diffusing gas B into a stagnant liquid C.

A

Absorption

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4
Q

General Types of Gas Absorption Equipment (3)

A

-Plate Towers
-Structure Packing
-Random Packing

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5
Q

To efficiently bring the vapor and liquid intro contact in the absorption tower

A

Plate Towers

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6
Q

Organized and geometrically designed elements, often stacked in a uniform way.

A

Structure Packing

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7
Q

Loose filling of a container with shapes like rings, spheres, or saddles. Installation involves simply pouring the packing material into the column.

A

Random Packing

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8
Q

Examples include mesh pads or specific shapes like discs with honeycombs.

A

Structure Packing

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9
Q

Plate Towers is also called?

A

Tray Towers

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10
Q

are designed to provide liquid holdup in order to achieve the proper vapor-liquid mass transfer that the distillation process requires for separation.

A

Tray Towers

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11
Q

Holdup is accomplished using a ——————– on each tray?

A

weir

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12
Q

flow across the trays allows ———– moving vapors and ————– moving liquids to have intimate contact in strategically placed passages in the tray.

A

upward and downward

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13
Q

Types of Tray (Plate) Towers (3)

A

-valve trays
-bubble cap trays
-sieve trays

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14
Q

are perforated plates with holes or slots that allow vapor to pass through. They typically have a larger open area compared to bubble cap trays, which allows for more vapor to pass through and interact with the liquid on the tray.

A

Sieve trays

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15
Q

feature perforated plates with movable valves or caps that open and close in response to the vapor flow. This movement helps to control the flow of vapor and liquid, promoting better contact and separation efficiency.

A

valve tray

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16
Q

consist of perforated plates with cylindrical caps that allow vapor to pass through the liquid on the tray. The caps help to evenly distribute the vapor and create bubbles, which enhances the contact between the vapor and liquid for efficient separation.

A

bubble cap tray

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17
Q

are more suitable for low capacity operations

A

packed columns

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18
Q

are particularly useful in the field of vacuum distillation

A

packed columns

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19
Q

For separating heat sensitive materials ——————- are useful because the liquid hold up is low

A

packed columns

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20
Q

when corrosion is a problem, the only solution is?

A

packing

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21
Q

Pressure drop per unit length is less.

A

packed columns

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22
Q

Types of Structure Packing (3)

A

-knitted Wire STructured Packing
-gauze
-corrugated structured packing

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23
Q

multitude of small wires, offer a large surface area and efficient mass transfer.

A

Knitted Wire Structured Packing

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24
Q

can be formed into other shapes, such as rolled into cylinders or wrapped to form a solid block.

A

KNitted wire structured packing

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25
is used for applications that require the low
gauze
26
It is ideal for processing pharmaceuticals and other chemicals that require a specific temperature range.
gauze
27
a type of tray tower that are high in capacity, turndown ratio, and efficiency
valve tray
28
a type of tray tower that are high in pressure drop and entrainment.
bubble cap tray
29
a type of tray tower that are high in efficiency alone and cheapest.
sieve tray
30
Sheet metal is often used in applications such as vacuum distillation and high-pressure absorption. Because it is stronger and more durable than knitted packing and gauze.
corrugated structured packing
31
it can process much higher volumes of liquid and vapor.
corugted structured packing
32
its smooth, open surface has some resistance to chemical fouling. This quality makes these types of packing ideal for wastewater and other fouling-prone environments.
corrugated structured packing
33
is used to increase surface area for vapor/liquid contact so that chemical separation is more efficient.
random packing
34
The small pieces of random packing in an absorption column are designed to form a ?
large surface area
35
is designed to maximize the surface-to-volume ratio and minimize pressure drop.
random packing
36
The efficacy of random packaging depends upon a few factors (3)
-efficiency -pressure drop -capacity
37
in random packing, ------------------- pressure drop is ideal because high pressure drop diminishes both performance and efficiency.
low
38
random packing materials were made of ?
ceramic
39
today, random packing are made of?
metal and plastic, with some other used in specialized applications
40
types of Random Packing (5)
-Raschig Rings -Pall Rings -saddle rings -lessing rings -tri-packs
41
makes use of small pieces of tube to make a packing bed. These small tubes are usually about as long as they are wide.
raschig rings
42
belong to an earlier, less sophisticated generation of packing material. They are smooth, without holes, grooves, ribbing or other textured elements. They have low capacity and low efficiency, and they tend to cost more than other types of random packing.
raschig rings
43
have such high cost in comparison to their efficacy, applications for this type of packing are limited.
raschig rings
44
In situations where corrosive material is being separated, however, ceramic material for this type of rings are effective thanks to their high corrosion-resistance.
raschig rings
45
46
are similar to Raschig rings but come with added sophistication.
pall rings
47
include added internal support structures and external surfacing. The texture within the ring walls allows for points of internal dripping that significantly increase the capacity and the efficiency of the packing.
pall rings
48
work particularly well for distillation and absorption applications.
pall rings
49
come in two primary types — Berl saddles and Intalox® saddles.
saddle rings
50
As their name suggests, they’re shaped like tiny saddles. They differ from Raschig and Pall rings in that their length exceeds their diameter.
saddle rings
51
are often shorter, with a more traditional saddle shape.
smooth berl saddles
52
are significantly longer, shaped much like pieces of macaroni halved lengthwise into long, open curved pieces. They also offer small holes and grooves for increased surface area and contact opportunity.
intalox saddles
53
with their increased surface area for liquid and vapor contact, offer increased capacity and efficiency. They are ideal for chemical distillation, stripping and absorption.
saddle rings
54
are made of ceramic. They have internal partitions to increase surface area and enhance efficiency. Like all ceramic packing pieces, they are highly resistant to heat and corrosion. These qualities make them ideal for applications such as regenerative oxide systems.
lessing rings
55
were first developed in the late 70s and are now broadly used. 
tri-packs
56
offer many advantages over older types of packings.
tri-packs
57
Thanks to their spherical shape, they are not prone to nesting and settling. The interior ribs also maximize surface area and wetting qualities. To achieve low pressure drop and high-mass transfer rates.
tri-packs
58
are commonly offered in a range of plastics, providing corrosion and temperature resistance.
tri-packs
59
a type of column which is high in capacity, large in diameter, less expensive, easier to maintain, less vapor liquid contact, available sie stream.
tray column
60
a type of column which is low in capacity, small in diameter, expensive, difficult to maintain, and have more vapor liquid contact.
packed column
61
a type of column who have high pressure drop and can handle high temperature, not safe for toxic and flammable liquids, appropriate for fouling liquids, and not reccomended for foaming systems.
tray column
62
a type of column who have lower pressure drop and cannot handle high temperature, safe for toxic and flammable liquids, not appropriate for fouling liquids, and reccomended for foaming systems.
packed column
63
no liquid flow
dry packing
64
the pressure drop is similar to that of dry packings.
at low to moderate velocity
65
the gas starts to hinder the liquid downflow, and local accumulations or pools of liquid start to appear in the packing
loading point
66
Upper limit to the rate of gas flow
flooding point
67
the liquid flows downward through the packing
low gas velocity
68
For optimum design, the recommended gas velocity is --------------% of the gas flooding velocity
50-70%