Method and Apparatus for Separating One or More Components from a Composition
a technology of composition and one or more components, applied in the direction of separation process, liquid degasification, membranes, etc., can solve the problems of time-consuming and expensive separation process, and achieve the effects of less toxic, less corrosive, and less flammability
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Benefits of technology
Problems solved by technology
Method used
Examples
example 1
Water Vapor Absorption and Desorption
[0108]A gas / vapor mixture of nitrogen and water vapor at 23° C. and 60% RH was bubbled at a flow rate of 120 sccm at 1.01 atm pressure in a hydroxyl-terminated polydimethylsiloxane oligomer diol having a zero shear kinematic viscosity of about 40 cSt at 25° C. (Absorbent Fluid 1), at 20° C. By gravimetric analysis, 0.55 g of water vapor absorbed in the fluid after 23 h. Nitrogen at 23° C. and 0% RH was then bubbled in the fluid / water vapor mixture to desorb water vapor from the fluid / water vapor mixture. The initial desorption rate constant of water vapor from the fluid was 1.82×10−2 g water vapor desorbed / hr / g water vapor in solution. The interfacial area for mass transfer of water vapor to and from Absorbent Fluid 1 was comparable to the interfacial area for mass transfer of water vapor to and from TEG in Comparative Example 1.
example 2
Water Vapor Absorption and Desorption
[0109]A gas / vapor mixture of nitrogen and water vapor at 23° C. and 60% RH was bubbled at a flow rate of 120 sccm at 1.01 atm pressure in a hydroxyl-terminated oligomeric trifluoropropyl methylsiloxane having a zero shear kinematic viscosity of about 100 cSt at 25° C., (Absorbent Fluid 2) at 20° C. By gravimetric analysis, 2.08 g of water vapor absorbed in the fluid after 79 h. Nitrogen at 23° C. and 0% RH was then bubbled in the fluid / water vapor mixture to desorb water vapor from the fluid / water vapor mixture. The initial desorption rate constant of water vapor from fluid was 3.85×10−2 g water vapor desorbed / hr / g water vapor in solution. The interfacial area for mass transfer of water vapor to and from Absorbent Fluid 2 was comparable to the interfacial area for mass transfer of water vapor to and from Absorbent Fluid 1 in Example 1 and TEG in Comparative Example 1.
example 3
Water Vapor Absorption
[0110]A gas / vapor mixture of nitrogen and water vapor at 23° C. and 20%, 40%, 60%, and 80% RH was bubbled at a flow rate of 120 sccm at 1.01 atm pressure in Absorbent Fluid 1 at 20° C. until steady states were reached. By gravimetric analysis at steady state conditions, 4.2×10−8 mol H2O / Pa·g of Absorbent Fluid 1 absorbed in Absorbent Fluid 1 when the ratio moles H2O absorbed / (moles H2O absorbed+moles Absorbent Fluid 1) was between 0 and 0.05. A gas / vapor mixture of nitrogen and water vapor at 23° C. and 20%, 40%, 60%, and 80% RH was bubbled at a flow rate of 120 sccm at 1.01 atm pressure in Absorbent Fluid 1 at 30° C. until steady states were reached. By gravimetric analysis at steady state conditions, 3.0×10−9 mol H2O / Pa·g of Absorbent Fluid 1 absorbed in Absorbent Fluid 1 when the ratio moles H2O absorbed / (moles H2O absorbed+moles Absorbent Fluid 1) was between 0 and 0.05. The percent decrease in the mol H2O / Pa·g of Absorbent Fluid 1 absorbed in Absorbent Flu...
PUM
Property | Measurement | Unit |
---|---|---|
near wavelengths | aaaaa | aaaaa |
temperature | aaaaa | aaaaa |
surface area | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com