Hollow fiber membrane module
A hollow fiber membrane module 100 includes: a plurality of hollow fiber membranes 10 ; a container 20 storing the plurality of hollow fiber membranes 10 ; and a feed water inlet 201 provided at one end portion of the container 20 such that a direction in which feed water flows into the container 20 is parallel to a longitudinal direction of the plurality of hollow fiber membranes 10 . A permeation flux of the hollow fiber membranes 10 at a transmembrane pressure difference of 0.1 MPa is higher than or equal to 850 liter/m 2 /h.
1. A hollow fiber membrane module comprising:
a plurality of hollow fiber membranes;
a container storing the plurality of hollow fiber membranes;
a feed water inlet provided at one end portion of the container such that a direction in which feed water flows into the container is parallel to a longitudinal direction of the plurality of hollow fiber membranes;
a first binding portion provided at one end portion of the plurality of hollow fiber membranes;
a second binding portion provided at the other end portion of the plurality of hollow fiber membranes, and
a baffle disposed between the feed water inlet and one end portion of the plurality of hollow fiber membranes, wherein
the hollow fiber membrane module is configured as an external-pressure type in which the feed water flows outside the plurality of hollow fiber membranes and permeate water flows inside the plurality of hollow fiber membranes,
the feed water inlet is provided such that the feed water does not directly collide with the plurality of hollow fiber membranes in the direction perpendicular to the longitudinal direction of the plurality of hollow fiber membranes,
a gap is present between the baffle and the first binding portion,
a plurality of through holes are provided in an outer circumferential portion of the baffle along the circumferential direction,
the baffle prevents flow of the feed water from directly colliding with the hollow fiber membranes and the first binding portion when the feed water is introduced through the feed water inlet into the container,
a permeation flux of the hollow fiber membranes at a transmembrane pressure difference of 0.1 MPa is higher than or equal to 850 liter/m 2 /h,
the container comprises a container body, a first cap attached to one end portion of the container body, and a second cap attached to the other end portion of the container body,
the second binding portion is fixed to the second cap by using an adhesive,
the plurality of hollow fiber membranes, the second binding portion, and the second cap form a unit that is separable from each other only in a destructive manner, and
the unit is detachable from the container body in a non-destructive manner,
the plurality of hollow fiber membranes are sealed at the one end portion by the first binding portion,
the other end portion of the plurality of hollow fiber membranes are opened at an end face of the second binding portion,
the second binding portion separates a feed water flow path and a permeate water flow path from each other in the container,
the first binding portion has no through hole that penetrates the first binding portion in the direction parallel to the longitudinal direction of the plurality of hollow fiber membranes,
in the container, internal spaces SP 1 , SP 2 , and SP 3 that act as flow paths are present, the internal space SP 1 is an internal space of the container body and acts as the feed water flow path, the internal space SP 2 is an internal space of the first cap and acts as the feed water flow path, the internal space SP 3 is an internal space of the second cap and acts as the permeate water flow path,
the feed water flows from the internal space SP 2 through the plurality of through holes of the baffle toward the internal space SP 1 , and
the permeate water is sent through the internal space SP 3 from the plurality of hollow fiber membranes to the outside of the hollow fiber membrane module.
2. The hollow fiber membrane module according to claim 1 , wherein a tensile strength of each hollow fiber membrane is higher than or equal to 0.20 kgf.
3. The hollow fiber membrane module according to claim 1 , further comprising:
a plurality of inner nets binding the plurality of hollow fiber membranes such that the plurality of hollow fiber membranes are separated into a plurality of bundles; and
an outer net binding the plurality of inner nets.
4. The hollow fiber membrane module according to claim 1 , further comprising a concentrated water outlet provided at the other end portion of the container such that a direction in which the feed water flows from the container to outside of the container is perpendicular to the longitudinal direction.
5. The hollow fiber membrane module according to claim 1 , wherein the hollow fiber membrane module is used for producing ultrapure water.
6. The hollow fiber membrane module according to claim 1 , wherein
the baffle is plate-like,
the plurality of the through holes are provided only in the outer circumferential portion of the baffle along the circumferential direction, and
the first binding portion is located inside an outer edge of the baffle in a radial direction of the baffle.
7. The hollow fiber membrane module according to claim 1 , wherein an outer edge of a projected view obtained by projecting the first binding portion onto the second binding portion in the direction parallel to the longitudinal direction of the plurality of hollow fiber membranes is located inside an outer edge of the second binding portion.