Honeywell International Inc.

Uop Lcc

Richard Huang

Christophe Romatier

Lamar A Davis

Ronald Klecka

Xin X Zhu

William J Lechnick

Bryan Anderson

Junfeng Pan

A simulation system includes at least one processor configured to execute a computer program product, stored upon a storage medium. The computer program product includes a database application, a process simulation application, and an integration tool, where the database application and the process simulation application are discrete, stand alone products. The process simulation application can simulate industry processes using at least one flowsheet, which models a general flow of industry processes. The integration tool can map process simulation application objects and properties to database application objects, can convey information between mapped objects, can perform case management functions, and can perform orchestrated calculation functions.

Database user interfaces with flowsheets of a simulation system

A simulation system includes at least one processor configured to execute a computer program product, stored upon a storage medium. The computer program product includes a spreadsheet application, a process simulation application, and an integration tool (e.g., eSim), where the spreadsheet application and the process simulation application are discrete, stand alone products. The process simulation application can simulate chemical processes using at least one flowsheet, which models a general flow of chemical plant processes and equipment. The integration tool can map process simulation application objects and properties to spreadsheet application objects, can convey information between mapped objects, can perform case management functions, and can perform orchestrated calculation functions.

Utilizing spreadsheet user interfaces with flowsheets of a CPI simulation system

Systems and processes disclosed herein relate to the utilization of direct contact condensing to provide heat to a solvent regeneration loop in an acid gas removal process. A first direct contact condenser can be included in the upper section of a concentrator that removes acid gas from a rich solvent stream. A first slip stream can be heated in the first direct contact condenser and can be combined with the rich solvent stream in the lower section of the stripper. A second direct contact condenser can be included in the lower section of an absorber that removes acid gas from a feed gas. A second slip stream can be heated in the second direct contact condenser, and can be combined with the rich solvent stream before the rich solvent stream is provided to the concentrator.

Direct contact cooling in an acid gas removal process

Systems and processes utilize one or more methods of providing overhead waste process heat to increase the feed temperature of the hot solvent stripping regeneration loop in an acid gas removal process. A heated rich solvent stream can be the primary feed for the hot solvent stripping regeneration loop, and one or more slip streams can be heated and then combined with the heated rich solvent stream to form a combined rich solvent stream prior to further processing in downstream units to remove acid gas from the solvent. A first slip stream can be heated in a stripper gas heat exchanger by heat exchange with a stripped gas stream. A second slip stream can be heated in a regenerator exchanger by heat exchange with an acid gas stream. A third slip stream can be heated in a recycle gas exchanger by heat exchange with a compressed recycle gas stream.

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Vernon Hills, IL, United States of America

Richard Huang