(140c) A Solution for the Increasing Amine Cycle in Refinery Operations
AIChE Spring Meeting and Global Congress on Process Safety
2016
2016 AIChE Spring Meeting and 12th Global Congress on Process Safety
19th Topical Conference on Refinery Processing
Refinery Margins and Operations
Tuesday, April 12, 2016 - 4:30pm to 5:00pm
Desalting problems begin with an increase in the aqueous phase pH driven by the tramp amines. The higher pH results in increased amine partitioning to the oil phase. It also stabilizes the emulsion at the oil/water interface and extends the rag layer. Water carryover increases to the crude which results in increased chlorides in the crude tower overhead. Oil under carry is also increased which impacts the wastewater treatment plant. Increased corrosion of overheads is due to more than the higher chlorides from water carryover. Excess amine carryover buffers the overhead and makes it more difficult to control and maintain desired pH targets and thereby negating the effectiveness of neutralizers. Also the excess amines combined with the reduction of operational flexibility creates very high salt points. Salt deposition problems can result when the Salting Point exceeds the tower top temperature.
Lowering levels of tramp amines is very difficult because there are multiple sources of amines. In addition to H2S scavengers and corrosion inhibitors in the incoming crude oil, amines are introduced through the sour water stripper, amine scrubber and from corrosion inhibitors used in steam production and refinery corrosion management. And with increased water recycling, amines and ammonia levels in the stripped sour water will tend to increase over time. This process can be described as the tramp amine cycle.
Conclusion
This paper will present a detailed overview of the cost of the amine cycle in the refinery, the solutions to break the amine cycle and provide supporting test and case study data.
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2016 AIChE Spring Meeting and 12th Global Congress on Process Safety
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