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Tight Oil Condensate Processing Design

Location of Project:Midwest

Project Cost :$5 million

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Create a center for collection and dispersal of shale oil

C&I was tasked with designing receiving facilities and tankage at the refinery to receive and distribute product streams distilled out of the condensate stream produced from tight oil. The scope called for a 35,000 BPD case which, apart from reusing the existing aliphatic unit towers, would replace essentially all other equipment.

This large project included barge unloading facilities at the light oil dock for tight oil condensate; four new tanks located in a new tank farm area; charge pumps and LSR pumps, piping, and controls; steam, steam condensate, HPBFW (for wash water) and cooling water supply and return piping between ISBL Battery Limits and

the utility source/destination; and piping to route tight oil condensate from the barge through the tanks and charge pumps to the ISBL battery limits and propane, butane, LSR, HSR, and Naphtha splitter bottoms from the battery limits to other storage units.

We also designed a propane H2S Scrubber facility for propane routed to the propane caverns. This facility would re-pipe and convert the existing out-of-service Cumene propane sulfur treaters to use a non-regenerable absorbent for H2S and mercaptan removal.

We handled process and detailed design for receiving and distribution.

Process Technical Solutions

The team created a way to receive and distribute product streams, designing facilities that would replace existing equipment.

Engineering Services

Once the process team finalized the roadmap for the project, mechanical, civil/structural and plant design provided detailed design for the extensive list of equipment including, among other items, piping, pumps, tanks and Scrubber facility.

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To learn about similar work C&I has handled for our client partners, or to find out what we can do for your operation, call us today at (502) 451-4977.
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