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Core Adsorbent plant with molecular sieve and activated alumina products

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Adsorbents for Natural Gas & Energy

Core Adsorbent supplies molecular sieves, activated alumina and inert ceramic balls for natural gas dehydration, LNG pretreatment, NGL drying and gas treating.

< 0.1 ppmv

Outlet water before LNG

4A · 3A · 13X

Molecular sieve grades

Complete bed

Sieve, alumina, ceramic balls

15–35 days

Delivery time

01 Overview

What does natural gas processing need from adsorbents?

Natural gas must be dried to very low water levels before cryogenic recovery, liquefaction or pipeline delivery, and often needs sulphur compounds removed. Molecular sieve dehydrators do this by temperature swing adsorption, protected by an activated alumina guard layer and supported on inert ceramic balls.

02 Product solutions

Adsorbent solutions for natural gas and energy

Every solution page tagged to this application appears here automatically.

03 Challenges

What goes wrong in natural gas drying?

Four problems decide whether a dehydration unit meets spec and how long its bed lasts.

Hydrate plug in a gas pipeline

Hydrates and ice

Water left in the gas forms hydrates in pipelines and freezes in cryogenic exchangers.

Sour gas treating unit

COS formation

When H₂S and CO₂ are co-adsorbed, a standard 4A bed can form carbonyl sulphide.

Broken molecular sieve beads

Bed damage

Liquid carry-over and condensation during regeneration break beads and form fines.

LPG storage spheres

Sulphur specs

NGL, LPG and LNG products carry mercaptan and H₂S limits that drying alone does not meet.

04 How it works

A typical molecular sieve dehydration unit

Two-tower molecular sieve dehydration unit for natural gas, showing ceramic ball, activated alumina and molecular sieve layers

< 0.1 ppmv

Outlet water ahead of cryogenic and LNG sections

−100 °C

Water dew point achievable

230–290 °C

Typical regeneration gas temperature for 4A

2 + 1

Common tower arrangement for LNG and NGL plants

Typical industry values; your design depends on feed composition, flow and cycle. Reference: molecular sieve dehydration technology profile.

05 Selection guide

Natural gas adsorbent selection table

Full specifications are on each product page.

ProductUse in natural gasKey figure
4A Molecular SieveMain drying layer for gas, NGL and LNG feedStatic H₂O ≥ 22.5 % (RH 75 %, 25 °C)
3A Molecular SieveGas with methanol upstream; low COS formation3 Å pore, static H₂O ≥ 21.5 %
13X Molecular SieveMercaptan, H₂S and CO₂ removalStatic CO₂ ≥ 18.5 %
5A Molecular SieveH₂S and light mercaptan removal5 Å pore
Activated Alumina DesiccantGuard layer for free water and acidsRegenerable desiccant
Inert Alumina Ceramic BallSupport and hold-down17–99 % Al₂O₃, Ø 3–50 mm

07 Case studies

Proven in plants like yours

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Case studies for this application will be published here.

08 From our plant

What you receive

The adsorbent, the packing and the plant it ships from.

4A molecular sieve beads, close-up
Molecular sieve packed in steel drums
Adsorbent packed in jumbo bags
Adsorbent forming line at the Core Adsorbent plant
Container loading of adsorbent for export

09 FAQ

Natural gas & energy FAQ

Can’t find your answer? Ask our sales engineer.

Which molecular sieve is used for natural gas dehydration?

4A is the usual choice. 3A is preferred where methanol is injected upstream or where co-adsorption of H₂S and CO₂ should be limited.

Why add activated alumina to a molecular sieve dryer?

A layer of Activated Alumina Desiccant at the feed end takes free water and liquid carry-over first, protecting the sieve and extending bed life.

Can you supply the complete dryer bed?

Yes. We supply the molecular sieve, the alumina guard layer and the ceramic ball support together, sized to your vessel.

How do you limit COS formation in the dryer?

Use 3A Molecular Sieve or a low-COS 4A grade where the gas contains both H₂S and CO₂, and keep regeneration within the recommended range.

What regeneration temperature is used?

Regeneration gas for 4A is typically heated to about 230–290 °C; the exact value depends on grade, bed design and cycle.