Electrode material for electrochemical capacitor, electrode coating solution for electrochemical capacitor, electrode for electrochemical capacitor, and electrochemical capacitor
US-2017323737-A1 · Nov 9, 2017 · US
US10159943B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10159943-B2 |
| Application number | US-201515328363-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 24, 2015 |
| Priority date | Jul 24, 2014 |
| Publication date | Dec 25, 2018 |
| Grant date | Dec 25, 2018 |
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The present invention provides a carbon membrane for fluid separation with which a high-pressure fluid can be separated and purified and which has excellent pressure resistance and is less apt to be damaged. The present invention relates to a carbon membrane for fluid separation, including: a core layer which has a co-continuous porous structure; and a skin layer which has substantially no co-continuous porous structure and is formed around the core layer.
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The invention claimed is: 1. A carbon membrane for fluid separation, comprising: a core layer which has a co-continuous porous structure; and a skin layer which has substantially no co-continuous porous structure and is formed around the core layer, wherein the co-continuous porous structure of the core layer has a structural period of 0.002 to 10 μm. 2. The carbon membrane for fluid separation according to claim 1 , wherein a central part of the core layer has an average porosity of 10 to 80%. 3. The carbon membrane for fluid separation according to claim 1 , which is a core/sheath fiber comprising a core part as the core layer and a sheath part as the skin layer. 4. The carbon membrane for fluid separation according to claim 3 , which is a fiber having a round cross-section. 5. A hollow-fiber carbon membrane for fluid separation comprising: a core layer which has a co-continuous porous structure; a skin layer which has substantially no co-continuous porous structure and is formed around the core layer; and a hollow part formed inside the core layer, wherein the co-continuous porous structure of the core layer has a structural period of 0.002 to 10 μm. 6. The hollow-fiber carbon membrane for fluid separation according to claim 5 , wherein an area ratio A/B of a cross-sectional area A of the hollow part to a cross-sectional area B of the hollow-fiber carbon membrane is 0.001 to 0.7. 7. The hollow-fiber carbon membrane for fluid separation according to claim 5 , wherein the core layer has a structural period of 0.05 to 3 μm. 8. The hollow-fiber carbon membrane for fluid separation according to claim 5 , wherein pores in the co-continuous porous structure of the core layer have an average diameter of 30 to 1,500 nm. 9. The hollow-fiber carbon membrane for fluid separation according to claim 5 , wherein the skin layer has a thickness of 5 μm or less. 10. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being either the carbon membrane for fluid separation according to claim 3 . 11. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the carbon membrane for fluid separation according to claim 4 . 12. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the hollow-fiber carbon membrane for fluid separation according to claim 5 . 13. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the hollow-fiber carbon membrane for fluid separation according to claim 6 . 14. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the hollow-fiber carbon membrane for fluid separation according to claim 7 . 15. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the hollow-fiber carbon membrane for fluid separation according to claim 8 . 16. A fluid separation membrane module produced by fabricating a plurality of membranes into a module, each of the membranes being the hollow-fiber carbon membrane for fluid separation according to claim 9 . 17. A process for producing a carbon membrane for fluid separation, the process comprising: step 1: a step in which 10 to 90% by weight of a carbonizable resin and 90 to 10% by weight of an eliminable resin are brought into a compatibly mixed state to obtain a resin mixture; step 2: a step in which the resin mixture obtained in the step 1 is caused to undergo phase separation to form a co-continuous phase separation structure and the separated phases are fixed to obtain a precursor for the carbon membrane for fluid separation; and step 3: a step in which the precursor for the carbon membrane for fluid separation obtained in the step 2 is carbonized by pyrolysis. 18. A process for producing a hollow-fiber carbon membrane for fluid separation, the process comprising: step 1: a step in which 10 to 90% by weight of a carbonizable resin and 90 to 10% by weight of an eliminable resin are brought into a compatibly mixed state to obtain a resin mixture; step 2: a step in which the resin mixture that has been brought into the compatibly mixed state in the step 1 is spun into a hollow fiber and caused to undergo phase separation to form a co continuous phase separation structure to obtain a precursor for the hollow-fiber carbon membrane for fluid separation; and step 3: a step in which the precursor for the hollow-fiber carbon membrane for fluid separation obtained in the step 2 is carbonized by pyrolysis.
characterised by a particular shape of the outline of the cross-section of a continuous layer; characterised by a layer with cavities or internal voids {(foam layer B32B5/18; layer of synthetic resin characterised by fillers that create voids or cavities B32B27/205); characterised by an apertured layer} · CPC title
Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30 · CPC title
by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00) · CPC title
Pore-control agents or pore formers · CPC title
with a hollow structure; Spinnerette packs therefor (D01D5/38 takes precedence; producing tubes of plastic material B29D; addition of agents forming hollow filaments D01F1/08) · CPC title
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