IHS CHEMICAL Toluene Methylation Process by GT-TolAlk SM Technology

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` IHS CHEMICAL Toluene Methylation Process by GT-TolAlk SM Technology March 2016 ihs.com Toluene Methylation Process by GT-TolAlk SM Technology Anshuman Agrawal Principal Analyst

Toluene Methylation Process by GT-TolAlk SM Technology Anshuman Agrawal, Principal Analyst Abstract Mixed xylenes are the second-most-important aromatic product in terms of world consumption for chemicals manufacture, ranking behind benzene and ahead of toluene. Global demand for xylene isomers has been continuously increasing, with para-xylene leading the way. During 2010 15, consumption of mixed xylenes increased by about 18% (3.4% average annual growth). The high demand for xylene isomers has created incentives for technology researchers to continue advancement work on various aspects and areas of the technologies. Improvements in catalyst performance are one of the prominent features of that work. Catalyst innovations have significantly improved the processes for on-purpose production of xylenes. Examples of those innovations include processes such as toluene disproportionation, toluene transalkylation, and xylene isomerization. A relatively new commercial development is the toluene alkylation process, in which mixed xylene is produced by reacting toluene and methanol in the presence of a ZSM-5 catalyst. This review presents a technoeconomic evaluation of the above-mentioned technology, branded as GT- TolAlk SM, which was developed by GTC Technology US, LLC, a US company headquartered in Houston, Texas. The production of mixed xylene using a toluene methylation process is one of the advanced methods developed by GTC via a toluene alkylation route. Sinopec Yangzi Petrochemical (China) has also independently developed and constructed that country s first toluene methanol alkylation plant, with the capacity to produce 200,000 metric tons per annum (MTPA) of para-xylene. That plant was successfully commissioned in December 2012. GTC won the first global application of toluene alkylation technology for a 280,000 MTPA toluene alkylation unit in China in January 2015. The technoeconomic evaluation in this review includes estimated capital and production cost estimates, showing the details of important process cost parameters such as battery limits and off-sites costs, variable cost, plant cash cost, plant gate cost, production cost, etc. A brief market overview summarizes the global producing companies, as well as consumption and price details of mixed xylenes. We prepared this review using information derived from public domain information sources (mainly patents). We also received some data of nonconfidential nature from the licensor (GTC Technology US, LLC) through private communications. Process design was done primarily through Aspen Plus simulations. Plant and process economics (capex and opex) were worked out using IHS proprietary PEPCOST software, using in places our own design judgments based on operational experience. 2016 IHS 1 March 2016

Contents 1 Introduction 5 2 Summary 6 3 Industry status 8 Producing companies 9 Consumption 11 Price 12 4 Technology review 13 Aromatic alkylation technologies 13 SABIC para-xylene technology 13 Sinopec Yangzi Petrochemical toluene methanol alkylation 13 ExxonMobil para-xylene by methylation 13 Johnson Matthey catalyst contact time 14 Background of GTC GT-TolAlk SM 14 5 Technology overview 16 GT-TolAlk SM technology 16 Catalyst specification 16 Catalyst cycle length and total life 16 Chemistry 16 Process chemistry 16 Process advantages 17 Process description 18 Process discussion 19 6 Cost estimates 24 Capital cost 24 Production cost 25 Appendix A References 31 Appendix B Process flow diagrams 33 Tables Table 1 Toluene methylation process by GT-TolAlk SM technology Production cost 6 Table 2 World supply/demand for mixed xylenes 8 Table 3 Major world producers of mixed xylenes 2015 10 Table 4 World consumption of mixed xylenes by region 2015 11 Table 5 World prices of mixed xylenes 12 Table 6 GT-TolAlk SM technology zeolite-based catalyst composition 16 Table 7 Chemical reaction involved in toluene methylation reactor 17 Table 8 Toluene methylation process by GT-TolAlk SM technology Design bases and assumptions 18 Table 9 Toluene methylation process by GT-TolAlk SM technology Major stream flows 20 IHS TM CHEMICAL COPYRIGHT NOTICE AND DISCLAIMER 2016 IHS. For internal use of IHS clients only. No portion of this report may be reproduced, reused, or otherwise distributed in any form without prior written consent, with the exception of any internal client distribution as may be permitted in the license agreement between client and IHS. Content reproduced or redistributed with IHS permission must display IHS legal notices and attributions of authorship. The information contained herein is from sources 2016 considered IHS reliable, but its accuracy and completeness are not warranted, nor are the opinions and 2 analyses that are based on it, and to the extent permitted by law, IHS March 2016 shall not be liable for any errors or omissions or any loss, damage, or expense incurred by reliance on information or any statement contained herein. In particular, please note that no representation or warranty is given as to the achievement or reasonableness of, and no reliance should be placed on, any projections, forecasts, estimates, or assumptions, and, due to various risks and uncertainties, actual events and results may differ materially from forecasts and statements of belief noted herein. This report is not to be construed as legal or financial advice, and use of or reliance on any information in this publication is entirely at client s own risk. IHS and the IHS logo are trademarks of IHS.

Table 10 Toluene methylation process by GT-TolAlk SM technology Major equipment 22 Table 11 Toluene methylation process by GT-TolAlk SM technology Utility summary 23 Table 12 Toluene methylation process by GT-TolAlk SM technology Total capital investment 25 Table 13 Toluene methylation process by GT-TolAlk SM technology Production cost 26 Figures Figure 1 World producers of mixed xylenes 2015 9 Figure 2 World consumption of mixed xylenes 2015 11 Figure 3 SABIC para-xylene block flow diagram 13 Figure 4 Block flow diagram of aromatic complex 14 Figure 5 Block flow diagram of GT-TolAlk SM technology 15 Figure 6 Toluene methylation process by GT-TolAlk SM technology Effect of plant capacity on investment cost 28 Figure 7 Toluene methylation process by GT-TolAlk SM technology Effect of net production cost and product value of mixed xylene as a function of toluene feed price 28 Figure 8 Toluene methylation process by GT-TolAlk SM technology Net production cost and product value of mixed xylene as a function of methanol feed price 29 Figure 9 Toluene methylation process by GT-TolAlk SM technology Net production cost of Figure 10 mixed xylene as a function of operating level and plant capacity 29 Toluene methylation process by GT-TolAlk SM technology Product value of mixed xylene as a function of operating level and plant capacity 30 Figure 11 Toluene methylation process by GT-TolAlk SM technology (1 of 2) 34 Figure 12 Toluene methylation process by GT-TolAlk SM technology (2 of 2) 35 2016 IHS 3 March 2016

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