A fluid circuit defining a flow path for a fluid from a fluid supply toward a process stage. The fluid circuit may include a plurality of operative components including a body portion and a plurality of tubing connector fittings. The operative components may be connected by a plurality of tubing segments. Each body portion may include a non-conductive fluoropolymer portion and an outer conductor that extends between each of the plurality of tubing connector fittings and that is unitary with the non-conductive fluoropolymer portion. The plurality of tubing segments may include a non-conductive fluoropolymer tubing portion and an axial strip of conductive polymer. The outer conductor of each body portion conductively connected with tubing segments connected thereto. Each of the connectors may include a bridging component for conductively connecting the respective outer conductor of the body portion to the strip of conductive polymer of the connecting tubing segments.

A fluid circuit defining a flow path for a fluid from a fluid supply toward a process stage. The fluid circuit may include a plurality of operative components including a body portion and a plurality of tubing connector fittings. The operative components may be connected by a plurality of tubing segments. Each body portion may include a non-conductive fluoropolymer portion and an outer conductor that extends between each of the plurality of tubing connector fittings and that is unitary with the non-conductive fluoropolymer portion. The plurality of tubing segments may include a non-conductive fluoropolymer tubing portion and an axial strip of conductive polymer. The outer conductor of each body portion conductively connected with tubing segments connected thereto. Each of the connectors may include a bridging component for conductively connecting the respective outer conductor of the body portion to the strip of conductive polymer of the connecting tubing segments.

The present invention provides a composition for a CO.sub.2 gas separation membrane containing: at least one compound selected from the group consisting of an alkali metal carbonate, an alkali metal bicarbonate, and an alkali metal hydroxide; a crosslinked polymer in which a polymer having a carboxyl group has been crosslinked; and a non-crosslinked polymer obtained by polymerization of one or more monomers selected from the group consisting of vinyl acetate, acrylic acid, methacrylic acid, and a derivative thereof.

A to-be-treated liquid containing oil that is obtained from oil-containing discharged water is treated with an oil-resistant separation membrane to remove the oil.

A to-be-treated liquid containing oil that is obtained from oil-containing discharged water is treated with an oil-resistant separation membrane to remove the oil.

Disclosed are copolymers which are useful in hydrophilically modifying porous fluoropolymer supports. An example of the copolymers is: ##STR00001##
Also disclosed are a method of preparing such copolymers, a method of modifying porous fluoropolymer surfaces, and hydrophilic fluoropolymer porous membranes prepared therefrom. Also disclosed is a method of filtering fluids by the use of the hydrophilic fluoropolymer porous membranes.

Hollow fiber membranes having improved toughness and durability are prepared using a vinylidene fluoride polymer-containing component, such as Kynaro resins, having relatively low crystallinity. One aspect of the invention provides a membrane in the form of a fiber, wherein i) the fiber has a porous wall of a polymeric component enclosing a central hollow space extending the length of the fiber, ii) the polymeric component has a crystallinity as determined by wide angle x-ray diffraction of less than about 35%, iii) the polymeric component is comprised of at least one homopolymer or copolymer of vinylidene fluoride and iv) the membrane has an energy to break of at least about 0.5 J per square mm of membrane cross section.

To provide an ion exchange membrane for alkali chloride electrolysis for which membrane strength is increased while membrane resistance is reduced to reduce electrolysis voltage during alkali chloride electrolysis and which prevents peeling between layers (S) and a layer (C). The ion exchange membrane for alkali chloride electrolysis comprises a layer (C) which comprises a fluorinated polymer having carboxylic acid functional groups, at least two layers (S) which comprise a fluorinated polymer having sulfonic acid functional groups, and a reinforcing material, wherein the layers (S) include a layer (Sa) and a layer (Sb), the layer (Sa) is a layer which is adjacent to the layer (C), the layer (Sb) is a layer which is not adjacent to the layer (C), the reinforcing material is disposed in the layer (Sb) substantially in parallel to the layer (Sb) in a state not in contact with the layer (Sa), and the ion exchange capacity of the layer (Sa) is lower than the ion exchange capacity of the layer (Sb).

The present invention relates to a separation membrane including an organic polymer resin, in which a volume V1 of fine pores having a pore diameter of 100 nm or more is 0.3 cm.sup.3/g or more and 0.5 cm.sup.3/g or less, a volume V2 of fine pores having a pore diameter of less than 100 nm is 0.02 cm.sup.3/g or more and less than 0.1 cm.sup.3/g, and a ratio V1/V2 of the fine pore volume V1 to the fine pore volume V2 is 3 or more and 60 or less.

The present invention relates to a separation membrane including an organic polymer resin, in which a volume V1 of fine pores having a pore diameter of 100 nm or more is 0.3 cm.sup.3/g or more and 0.5 cm.sup.3/g or less, a volume V2 of fine pores having a pore diameter of less than 100 nm is 0.02 cm.sup.3/g or more and less than 0.1 cm.sup.3/g, and a ratio V1/V2 of the fine pore volume V1 to the fine pore volume V2 is 3 or more and 60 or less.