Abstract: The communication bridge enables trading partner customers to mass customize their interactions with their affiliated trading partners by controlling workflow and data presentation. A method and system allows the integration of standard and proprietary content, such as data and “look-and-feel” elements, from trading partners to be presented via a standard interface for the purpose of conducting mass customized interactions (transactions, communications). There is a high degree of variability in screen and workflow presentation. A particular Application Programming Interface (API) facilitates the dynamic exchange of information between disparate trading partners and end users.

Abstract: An apparatus for treating hydrocarbon gas containing carbonyl sulfide with hot aqueous absorbent at hydrolysis gas containing carbonyl sulfide hydrolysis of carbonyl sulfide to carbon dioxide and hydrogen sulfide and formation of hydrolysis product gas, and for cooling the hydrolysis product gas with cool absorbent at cooling temperature, comprising (a) a hydrolysis section, (b) a cooling section; (c) a chimney tray positioned between the cooling section and the hydrolysis section; (d) a heater to heat the absorbent to form hot aqueous absorbent at hydrolysis reaction temperature; and, (e) a cooler to cool the absorbent withdrawn from the hydrolysis section to cool absorbent at cooling temperature.

Abstract: An improved method of reducing the concentration of carbonyl sulfide in a hydrocarbon gas containing carbonyl sulfide, which method comprises (a) feeding the hydrocarbon gas containing carbonyl sulfide to a hydrolysis section to contact the hydrocarbon gas with hot aqueous absorbent to heat the hydrocarbon gas to form hydrolysis section effluent absorbent and hydrolysis section effluent gas containing carbon dioxide and hydrogen sulfide and having a lower concentration of carbonyl sulfide than the hydrocarbon gas; (b) withdrawing and cooling the hydrolysis section effluent absorbent to form a cool aqueous absorbent; (c) cooling the hydrolysis section effluent gas in a cooling section by contacting the hydrolysis section effluent gas with the cool aqueous absorbent to form warm aqueous absorbent and a cooling section effluent gas containing hydrogen sulfide and carbon dioxide; (d) heating the warm aqueous absorbent to form hot aqueous absorbent; (e) feeding the hot aqueous absorbent to the hydrolysis section;