Method of membrane separating property of variable pitch, membrane module apparatus and usage
A technology of variable pitch and separation membrane, used in semi-permeable membrane separation, chemical instruments and methods, membrane technology, etc., can solve the problem of small membrane filling area, no further consideration of the permeate flow performance and energy consumption of the membrane tube flow channel flow rate change system Influence, not considering the flow rate change system infiltration flow performance and energy consumption and other issues
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Embodiment 1
[0035] Accompanying drawing 6 is a structural schematic diagram of a Dean vortex spiral flow channel tubular microfiltration membrane module. It can be seen from the figure that the Dean vortex spiral flow channel tubular microfiltration membrane structure assembly includes a separation membrane 1, a membrane housing 3, and a raw material inlet 5 , permeate outlet 6, concentrated solution outlet 7, several parts, wherein: the membrane module raw material inlet 5 and the concentrated solution outlet 7 are respectively located at the inlet end of the tubular membrane module and the end of the pipe relative to the inlet direction, inside the membrane shell 3 It is a separation liquid separation chamber, and the lower end of the membrane shell 3 is provided with a concentrated liquid outlet 7; the separation membrane 1 is a tubular membrane, placed in the membrane shell 3, and is a microfiltration (MF), ultrafiltration (UF) with different opening sizes. ) structure of a hollow filt...
Embodiment 2
[0037] Accompanying drawing 6 is the structure schematic diagram of another embodiment of Dean vortex spiral flow channel tubular microfiltration membrane module, the other parts of this embodiment are the same as the embodiment, the difference is that the spiral circulation channel of the spiral flow channel guide device 2 The section shape is triangular, and it is a variable-pitch helical flow channel, and the pitch ratio of the inlet section and the outlet section is 8-15. According to Embodiments 1 and 2, it can be deduced that the cross-sectional shape of the spiral circulation channel of the spiral flow channel guide device 2 may also be square or semicircular.
Embodiment 3
[0039] Accompanying drawings 7-9 are schematic diagrams of a braided hollow fiber pipe thread connection tubular membrane module. It can be seen from the figure that the braided hollow fiber membrane module includes a braided hollow fiber membrane 18, a membrane casing thread 17, and a separation plate 19. Raw material inlet 20, permeate outlet 21, concentrate outlet 22 and membrane shell 23. Wherein: the separation liquid enters from the raw material inlet 20, and after being separated by the braided hollow fiber membrane 18, the permeate is discharged into the casing 23, and then discharged from the permeate outlet 21, and the separated concentrated liquid is discharged out of the tube through the concentrated liquid outlet 22 , which is characterized in that the braiding pitch of the braided hollow fiber membrane 18 is a variable-pitch helical channel, and the pitch ratio of the inlet section to the outlet section is 3-4.
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