Humidifier for fuel cell
US-9160015-B2 · Oct 13, 2015 · US
US2016240870A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016240870-A1 |
| Application number | US-201415025089-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 29, 2014 |
| Priority date | Sep 30, 2013 |
| Publication date | Aug 18, 2016 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A fluid exchange membrane module includes a case including at least two pairs of fluid inlets and fluid outlets, and a fluid exchange membrane installed within the case and disposed so that a dry fluid flowing between one pair of a fluid inlet and a fluid outlet does not directly contact a high-humidity fluid flowing between another pair of a fluid inlet and a fluid outlet in the operating state of the module. The fluid inlet for the high-humidity fluid includes a diffuser. The fluid exchange membrane module may adiabatically expand a fluid flowing toward one side of a fluid exchange membrane and thus increase the relative humidity of the high-temperature and high-humidity fluid so as to maximize fluid transmission through the fluid exchange membrane, and may decrease the pressure of the fluid so as to uniform pressure distribution of a fluid flow.
Opening claim text (preview).
1 . A fluid exchange membrane module comprising a case including at least two pairs of fluid inlets and fluid outlets, and a fluid exchange membrane installed within the case and disposed so that a dry fluid flowing between one pair of a fluid inlet and a fluid outlet does not directly contact a high-humidity fluid flowing between another pair of a fluid inlet and a fluid outlet in the operating state of the fluid exchange membrane module, wherein the fluid inlet to introduce the high-humidity fluid into the fluid exchange membrane module therethrough includes a diffuser. 2 . The fluid exchange membrane module according to claim 1 , wherein the diffuser is installed at pipes connected to the fluid inlets. 3 . The fluid exchange membrane module according to claim 1 , wherein the diffuser includes a first inner diameter part and a second inner diameter part having different inner diameters. 4 . The fluid exchange membrane module according to claim 3 , wherein the inner diameter of the second inner diameter part is greater than the inner diameter of the first inner diameter part. 5 . The fluid exchange membrane module according to claim 3 , wherein the first inner diameter part is disposed at an upstream region of a fluid flow and the second inner diameter part is disposed at a downstream region of the fluid flow. 6 . The fluid exchange membrane module according to claim 3 , wherein the ratio of the inner diameter of the second inner diameter part to the inner diameter of the first inner diameter part is 2:1 to 20:1. 7 . The fluid exchange membrane module according to claim 3 , wherein the diffuser further includes an inner diameter extension part located between the first inner diameter part and the second inner diameter part. 8 . The fluid exchange membrane module according to claim 7 , wherein the inner diameter of the inner diameter extension part is gradually increased from the inner diameter of the first inner diameter part to the inner diameter of the second inner diameter part. 9 . The fluid exchange membrane module according to claim 8 , wherein the diffuser has a Venturi tube shape. 10 . The fluid exchange membrane module according to claim 9 , wherein the inner diameter of the first inner diameter part is gradually decreased. 11 . The fluid exchange membrane module according to claim 10 , wherein the ratio of a length at which the inner diameter of the inner diameter extension part is gradually increased to a length at which the inner diameter of the first inner diameter part is gradually decreased is 1:1 to 10:1. 12 . The fluid exchange membrane module according to claim 3 , wherein the first inner diameter part is an orifice plate. 13 . The fluid exchange membrane module according to claim 12 , wherein: the orifice plate includes a plate including at least one opening; and the ratio of the inner diameter of the second inner diameter part to the diameter of the opening is 3:1 to 30:1. 14 . The fluid exchange membrane module according to claim 3 , wherein the first inner diameter part is a nozzle. 15 . The fluid exchange membrane module according to claim 14 , wherein the inner diameter of the first inner diameter part is gradually decreased. 16 . The fluid exchange membrane module according to claim 1 , further comprising an adiabatic member configured to thermally insulate the diffuser. 17 . The fluid exchange membrane module according to claim 1 , wherein the fluid exchange membrane is formed as a hollow fiber membrane, and the case and the fluid exchange membrane are disposed such that the dry fluid flows through hollows of the hollow fiber membrane and the high-humidity fluid flows outside the hollow fiber membrane. 18 . The fluid exchange membrane module according to claim 17 , wherein: the case includes an inlet case provided with a first fluid inlet, an outlet case provided with a first outlet, and a connection case provided with a second fluid inlet and a second fluid outlet; the case has a connection structure in which the inlet case and the outlet case are connected by the connection case; and hollow fibers are disposed within the case such that one end of each of the hollow fibers in the length direction is located at the inlet case and the other end of each of the hollow fibers is located at the outlet case. 19 . The fluid exchange membrane module according to claim 18 , in which potting parts to fix the hollow fibers are installed at both ends of the connection case. 20 . The fluid exchange membrane module according to claim 1 , wherein the fluid exchange membrane is formed as a flat sheet membrane, and the case and the fluid exchange membrane are disposed such that the dry fluid flows along one surface of the flat sheet membrane and the high-humidity fluid flows along the other surface of the flat sheet membrane. 21 . The fluid exchange membrane module according to claim 20 , wherein: the case has an inner space formed therein and is provided with two pairs of fluid inlets and fluid outlets so that fluids are supplied from the outside of the case to the inner space and the fluids are discharged from the inner space to the outside of the case; and the fluid exchange membrane is disposed within the case such that the circumference of the flat sheet membrane contacts the inner wall of the case so as to divide the inner space of the case into two sub-spaces, one sub-space of the two sub-spaces is connected to one pair of a fluid inlet and a fluid outlet and the other sub-space is connected to another pair of a fluid inlet and a fluid outlet. 22 . The fluid exchange membrane module according to claim 1 , wherein the fluid exchange membrane module is any one of selected from the group consisting of a moisture supply module, a heat exchange module, a gas separation module and a water treatment module.
by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title
Hollow fibre modules · CPC title
by diffusion, e.g. making use of membranes · CPC title
Operations & Transport · mapped topic
Polysulfones; Polyethersulfones · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.