Pygas Hydrotreating Process by GTC Technology

GTC offers an optimized technology for two-stage pyrolysis gasoline (pygas) hydrotreating (HDT), where di-olefins, olefins and styrene in the raw pygas feed are saturated. The technology is simple and easy to implement into existing plant requirements. The process is applied to the C5+ fraction of raw pyrolysis gasoline.

Pygas Hydrotreating Process by GTC Technology

In GTC’s pyrolysis hydrotreating technology process, raw pygas is first fed to the first-stage hydrotreating section. The pygas feed stream along with hydrogen is preheated by the recycle liquid stream to the desired temperature and sent to the first-stage hydrotreating (HDT) reactor where most di-olefins in the feed are selectively saturated to olefins only, preserving the octane value of the hydrotreated stream.

The reactor effluent is sent to the first-stage product separator. Part of the liquid from the bottom of the product separator is recycled back to the front section of the first-stage hydrogenator to control the reactor temperature rise. Excess hydrogen and light hydrocarbons are removed at the top of the separator and sent to the recycle gas compressor. The separator liquid is fed to a first-stage stabilizer column. In the receiver, H2 and light hydrocarbons are separated and drawn as a vapor product, which is sent as offgas to the battery limit (BL). The liquid from the receiver is fully returned as reflux to the column. The liquid stream from the stabilizer bottoms is C5+ gasoline fraction and can be sent to the gasoline pool. To produce benzene, toluene and xylene (BTX), this C5+ stream is sent to a fractionation section to obtain a C6–C8 heat cut, which will be further hydrotreated to saturate mono-olefins in the second-stage hydrotreating section.

In the second-stage hydrotreating section, the C6–C8 heart cut, combined with a recycle vapor stream and makeup hydrogen, is preheated in the second stage feed/effluent heat exchanger before being heated further to the desirable reaction temperature by a charge heater. The feed mixture passes through the fixed catalyst beds in the secondstage HDT reactor where olefin species are saturated and sulfur species are converted to H2S.

The reactor effluent is then cooled in the second-stage feed/effluent heat exchanger and subsequently in an after-cooler before being routed to a second-stage product separator. In the product separator, the unreacted hydrogen and other light components are separated from the hydrotreated liquid products and recycled to the HDT reactor using a recycle gas compressor. A small vapor stream is purged as offgas to control the level of impurities in the recycle gas. The hydrotreated liquid stream is fed to the second-stage stabilizer column. The column vapors are partially condensed in the overhead condenser and sent to an overhead receiver. In the receiver, H2 and light hydrocarbons are separated and drawn as a vapor product, which is sent as offgas to the BL. The liquid from the receiver is fully returned as reflux to the column. The bottoms product from the stabilizer, which is the hydrotreated C6–C8 cut, is cooled further and sent to BL for further processing for aromatics extraction.

Process advantages:
• Flexibility in prefractionator cut point and a proprietary vaporizer allows control of polymerization potential in the hydrotreaters.
• Reactor operates at high liquid content with mixed phases to minimize polymer byproduct plugging.
• Optimized recycle scheme minimizes hydrocarbon vaporization and thereby extends reactor run length.
• Catalyst exhibits high activity, stability, mechanical strength and poison resistance.
• Aromatics saturation in second-stage reactor is less than 1%.
• Efficient heat integration scheme reduces energy consumption.
• Turnkey package for high-purity benzene, toluene and paraxylene production is available from licensor.

Licensor: GTC Technology

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