6 Flashcards

(28 cards)

1
Q

Acid gas removal

A

We want to reduce the contents of CO2 and H2S gases to meet the quality standards for natural gas distributors

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2
Q

Standards for CO2 and H2S

A
  • CO2 : 2mol%
  • H2S : 4ppm
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3
Q

How do we go about removing the acid gases?

A

Via absorption and stripping columns
And when we have a downstream dehydration process via absorption using glycols or MEA

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4
Q

Which fluid package do we use for absorption?

A

We use Acid Gas Chemical solvents as these are very high non ideal system

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5
Q

Absorption process

A
  • Gas enters bottom with contaminants and a liquid stream also enters from top
  • Separation occurs by gas mixture contact with liquid
  • Clean gas stream top and liquid with contaminant stream leaves bottom
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6
Q

Stripping process

A
  • Gas (steam) enters bottom and a liquid stream (amine) with contaminants also enters from top
  • Separation occurs by liquid mixture contact with gas
  • Gas stream with contaminants top and clean liquid (lean amine) stream leaves bottom
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7
Q

Types of amine solvents

A

MEA/ DEA

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8
Q

How is a stripper modelled on HYSYS?

A

With a distillation column

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9
Q

What is the operating pressure and temperature like for absorbers?

A

Typically low
If operating temperature is too high, the solvent can evaporate. More solvent needed for better separation

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10
Q

What does it mean if the concentration of contaminant in the gas is high?

A

The separation becomes more difficult to carry out

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11
Q

What type of columns are commonly modelled for absorption columns in HYSYS?

A

Packed columns
Could also use tray columns

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12
Q

When do we use physical absorption?

A

Usually in high pressures and when the concentration of the contaminant in the gas is high

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13
Q

When do we use chemical absorption?

A

When the concentration of contaminant in the gas is low

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14
Q

What is the tray efficiency like in absorbers?

A

Low (20-30%)
The tray efficiency set is a combination of operating experience, predictive correlations using height of liquids on the tray and residence time of gas in the liquid.

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15
Q

When do we use Acid Gas- Chemcial Solvents?

A

Removal of CO2 and H2S via amines

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16
Q

When do we use Acid Gas - Physical Solvents?

A

Removal of CO2 and H2S via DEPG, selexol solvent or , methanol

17
Q

When do we use Acid Gas - Liquid Treating?

A

Removal of CO2 and H2S via amines from natural gas liquid or liquified petroleum gas

18
Q

When do we use Acid Gas - Caustic Wash?

A
  • Caustic NaOH
  • treating liquid streams only like the previous one
19
Q

Acid Gas - Chemical Solvents

A

Addresses highly non-ideal absorption systems
Ensure to add heat stable salts

20
Q

What is the number of degrees of freedom for absorption columns?

A

0 ; no reboiler or condenser

21
Q

Calculation type for absorption columns

A
  • Efficiency : commonly used (default) for H2S and CO2
  • Advanced Modelling : assumes rigorous rate-based model to relate mercaptans, COS, CS
22
Q

Efficiencies calculated for each tray

A

CO2 ones tends to be lower than H2S
Easier to remove H2S than CO2

23
Q

Rich amine stream

A

Bottom of the absorber out

24
Q

Lean amine stream

A

Feed liquid stream into the absorber

25
What is the amine solvent Makeup unit?
This calculates how much makeup flow rate of amine we need. This third stream is to replenish the amine and water lost via oxidation/ entrainment/ vaporisation etc
26
Acid gas parameters
Need to enter these related mainly to tray geometry
27
Wier height
This is the wall on your plate where the liquid comes in The higher the wier height, the higher the mass transfer
28
Section diameter
Also known as column diameter