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H₂ SO₄ Alkylation Unit

Ensure your Alkylation unit operates reliably, with minimum corrosion, low acid consumption, and on spec products.

H₂ SO₄ Alkylation

Process Description

Olefins (C3-C4) from the FCC unit are combined with isobutane (i-C4). Concentrated Sulfuric Acid (H₂ SO₄) is then mixed in and fed to the reactor that is operated with refrigeration to minimize formation of by-products. The alkylation reaction takes place combining the olefins with the isobutane to form the alkylate product which consists of high octane value products that are later blended into the gasoline pool. The hydrocarbons leaving the reactor mostly consist of alkylate, unreacted isobutane, n-butane, and propane.

 

The acid and alkylate product are separated by a settler and the acid is recovered for re-use in the reactor. The reactor hydrocarbons are separated by the main fractionator where the isobutane is recycled to the reactor, alkylate is drawn of the bottom and an n-butane product stream is separated from a side stream.

 

The light ends of the process fluids are used in the refrigeration loop and a side stream is passed through a propane stripper to recover propane. Effective separation is a critical component of an efficient, reliable and safe H₂ SO₄ alkylation process.

 

Refinery Needs

 

  • Equipment reliability/minimized corrosion to meet 4-6 year refinery turn around schedule
  • Meet product specs for high octane value alkylate and caustic free propane
  • Low acid makeup costs by minimizing acid dilution from wet feedstocks
  • Maintain high levels of safety by avoiding any equipment failures that could lead to fugitive acid emissions

 

Production Challenge/Pall Solution

 

 

Challenge

 

Meet product specifications.

Solution

 

Improve refinery productivity and product specifications by removal of water from the olefin and isobutane hydrocarbon reactor feed streams and by removing any carryover caustic in the propane.

 

 

 

Challenge

 

Protect fractionator towers from corrosion & plugging.

Solution

 

Improve protection of main fractionator/isobutane stripper and propane stripper.

 

  • High efficiency PhaseSep liquid/liquid coalescers reliably remove caustic from the feed to the main fractionator / isobutane stripper and to the propane stripper tower to prevent corrosion and fouling of the internal trays.

 

 

Challenge

Control acid makeup costs.

Solution

 

Ensure the high sulfuric acid strength is maintained.

 

 

 

 

h2so4 alkylation process diagram

 

Key Application/Filter Recommendations (other applications not shown)

 

Application

1, 3, 5.

Pre-filtration prior to liquid/liquid coalescer

Customer Benefits

 

Lower operating costs by improving the life of the liquid/ liquid coalescer

2.

Feed/isobutane recycle stream water removal

 

AquaSep XS (or PhaseSep) liquid/liquid coalescer 

 

Prevent dilution of acid catalyst and potential for corrosion and poor product yields

4.

Caustic removal from feed to propane stripper

 

Reduce corrosion in propane stripper and meet propane quality spec

6.

Caustic removal from feed to main fractionator/isobutane stripper

 

Reduce corrosion in main fractionator and meet butane and alkylate purity specs

 

 

For fast track upgrades, NO CAPEX:

 

Pall-Fit filter and coalescer retrofits enable a move to Pall quality without change to your existing filter housing

 

Pall filter and coalescer housing rentals enable a technology upgrade for rapid problem resolution

PDF version of this page

 

 

As the industry leader in innovative filtration technology, We offer premium filtration solutions for refining applications that maximize contaminant removal.

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