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Rethinking Aromatics Recovery Low-cost raw material for PX manufacture production GT-TolAlk SM Engineered to Innovate ®

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Rethinking Aromatics Recovery Low-cost raw material for PX manufacture production

GT-TolAlkSM

Engineered to Innovate®

GT-TolAlkRethinking Aromatics Recovery

Engineered to Innovate

As the growth of the paraxylene (PX) market continues to be driven by increasing global demand, PX prices and margins remain strong and are expected to remain healthy over the next several years. Toluene methylation is an e� ective and economical solution to maximize PX yields by adding the methyl group from low-cost methanol to the aromatic ring. GTC’s expanding technology portfolio introduces GT-TolAlk, a new way to derive PX while eliminating benzene production.

Process Overview� e feedstock, consisting of methanol and toluene, is processed in the toluene methylation reaction section where the toluene is alkylated into xylenes. � e reactor e� uent is processed in the fractionation section to produce the mixed xylene product. Unconverted toluene is separated and recycled back to the reaction section. C9+ aromatics fraction is also produced and separated, and is available as feedstock to the transalkylation unit, as the C9+ cut is rich in tri-methyl benzene.

Concept of Toluene MethylationTraditional toluene-based PX technologies involve re-arrangement of the alkyl groups though various methods. Benzene is the typical by-product due to insu� cient methyl groups compared to phenyl groups. By adding methyl groups to the aromatic ring, GT-TolAlk replenishes the methyl group shortage to yield more xylene over benzene. Figure 1 shows the chemistry of the toluene methylation reaction.

Process Advantages• Simple � xed-bed, low-pressure process

• No hydrogen needed

• High production capacity

• E� ective addition of methyl group to aromatic ring

• Very low EB in C8 aromatics; higher PX content compared to reformate xylenes

• Potential for zero benzene by-product

EconomicsFor a feed rate of 400 KTA, the estimated investment cost is $40MM USD for the reaction section and post fractionation units. Net operating pro� t is projected to be $37MM/yr.

Simple return on investment (ROI) is around 13 months.

� e GT-TolAlk process yields 389 KTA xylenes and 469 KTA methylated aromatics from 400 KTA toluene.

Figure 1 – Reaction Chemistry.

SM

Toluene Methanol Xylenes+ Water+

GTC Technology 900 Threadneedle St., Suite 800 Houston, Texas 77079 Main +1-281-597-4800 Toll Free [email protected] | www.gtctech.com

GTC Technology

Engineered to InnovateTo learn more about GTC Technology’s leading-edge technology solutions and the many ways we can help improve your operations and pro� tability, call us today at +1-281-597-4800, e-mail us at [email protected] or visit our Web site at http://www.gtctech.com.

GT-TolAlkSM is a service mark of GTC Technology US, LLC.

Figure 2 – Simpli� ed Process Scheme.

O� Gas

Light Ends

Waste Water

Mixed Xylenes toParaxylene Unit

C9+ Aromatics toTransalkylation

Separator

Stabilizer

Post-fractionation

Recycle Toluene

Toluene

Methanol

Reactor

Simple, �xed-bed design with no hydrogen compressor or circulation

Engineered to Innovate

GTC Technology 900 Threadneedle St., Suite 800 Houston, Texas 77079 Main +1-281-597-4800 Toll Free [email protected] | www.gtctech.com

©2016 GTC Technology - All rights reserved.

+1-281-597-4800 [email protected]

GTC Technology is a global licensor of process technologies and mass transfer solutions with the mission of creating value for our clients. Re� ning, petrochemical and chemical companies around the world rely on GTC’s advanced processes to optimize production capacity and e� ciency. With insightful industry expertise, research capabilities and innovative thinking, GTC solves complex processing problems and has earned a reputation of excellence in designing and delivering high-quality, strategic solutions for clients worldwide. We’re engineered to innovate.

Engineered to Innovate®