Method for operating membrane separation device with halt process

Patent metadata

Field	Value
Publication number	US-11452971-B2
Application number	US-201816203311-A
Country	US
Kind code	B2
Filing date	Nov 28, 2018
Priority date	Aug 29, 2016
Publication date	Sep 27, 2022
Grant date	Sep 27, 2022

Abstract

A method for operating a membrane separation device includes (a) setting a flow amount M(t) of permeated water and extracting the permeated water from the membrane separation device by the set flow amount M(t), and (b) temporarily stopping the extracting the permeated water, when a water level of a first water tank in which the membrane separation device is immersed, a water level of a second water tank in communication with the first tank, or a water level of a third water tank receiving overflowing water from the first water tank becomes lower than a predetermined halt water level. M(t), which is the flow amount of the permeated water during a time period t, satisfies a equation M(t)=KQ(t−1), where K is a gain (K>1), and Q(t−1) is an amount of inflow of the water-to-be-treated during a time period t−1 immediately prior to the time period t.

First claim

What is claimed is:

1. A method for operating a membrane separation device for performing solid-liquid separation of water to be treated via a separation membrane, the method comprising:
a membrane filtration process including:
setting a flow amount M(t) of permeated water from the membrane separation device so as to satisfy a relationship expressed by the following equation: M(t)=KQ(t−1), where M(t) is the flow amount s f the permeated water during a time period t having a predetermined length, K is a gain (>1), and Q(t−1) is an amount of inflow of the water to be treated during a time period t−1 immediately prior to the time period t; and
extracting the permeated water from the membrane separation device by the set flow amount M(t) of the permeated water; and

a halt process including:
temporarily stopping extracting the permeated water from the membrane separation device when a water level of a first water tank in which the membrane separation device is immersed, a water level of a second water tank which is in communication with the first water tank such that the water level thereof is the same as that of the first water tank, or a water level of a third water tank into which overflowing water from the first water tank is flowing, becomes lower than a predetermined halt water level.

2. The method for operating the met brane separation device according to claim 1 , wherein the halt process further includes:
temporarily stopping extracting the permeated water from the membrane separation device when a transmembrane pressure of the separation membrane becomes equal to or greater than a predetermined upper limit of a range of allowable values, even before the water level of any one of the first, second, and third water tanks drops to the predetermined halt water level.

3. The method for operating the membrane separation device according to claim 2 , wherein, after performing the halt process, the membrane filtration process resumed when one of the following conditions is met:
the water level of the first, second, or third tank which was detected in the halt process returns to a predetermined water level higher than the predetermined halt water level;
a predetermined time has elapsed; and
the transmembrane pressure of the separation membrane drops to a reference value lower than the predetermined upper limit of the range of allowable values.

4. The method for operating the membrane separation device according to claim 1 , wherein the halt process further includes:
performing a relaxation step for cleaning the separation membrane with an upward flow of the water to be treated by aerating the membrane separation device.

5. The method for operating the membrane separation device according to claim 1 , wherein the halt process further includes:
performing a chemical liquid cleaning step for cleaning the membrane separation device with a chemical solution.

6. The method for operating the membrane separation device according to claim 1 , wherein, after performing the halt process, the membrane filtration process is resumed when one of the following conditions is met:
the water level of the first, second, or third tank which was detected in the halt process returns to a predetermined water level higher than the halt water level; and
a predetermined time has elapsed.

7. The method for operating the membrane separation device according to claim 1 , wherein the gain K is set in a range of 1.01<K<1.10.

8. The method for operating the membrane separation device according to claim 1 , wherein extracting the permeated water from the membrane separation device by the set flow amount M(t)=KQ(t−1) gradually decreases contents of the third water tank during execution of the membrane filtration process.

9. The method for operating the membrane separation device according to claim 1 , wherein extracting the permeated water from the membrane separation device by the set flow amount M(t)=KQ(t−1) provides a delayed response of the flow amount of the permeated water to the amount of inflow of the water to be treated.

10. A method for operating a membrane separation device for performing solid-liquid separation of water to be treated via a separation membrane, the method comprising:
a membrane filtration process including:
setting a flow amount M(t) of permeated water from the membrane separation device so as to satisfy a relationship expressed by the following equation: M(t)=KQ(t−1), where M(t) is the flow amount of the permeated water during a time period t having a predetermined length, K is a gain (>1), and Q(t−1) is an amount of inflow of the water to be treated during a time period t−1 immediately prior to the time period t; and
extracting the permeated water from the membrane separation device by the set flow amount M(t) of the permeated water, the membrane separation device being immersed in a first water tank; and

a halt process including:
temporarily stopping extracting the permeated water from the membrane separation device when a water level of a tank into which overflowing water from the first water tank is flowing becomes lower than a predetermined halt water level.

Assignees

• Kubota Kk

Inventors

• Okajima Yasunobu
• Ishikawa Kimihiro

Classifications

• B01D2315/06

  Submerged-type; Immersion type · CPC title

• B01D65/02 Primary

  Membrane cleaning or sterilisation {; Membrane regeneration} · CPC title

• C02F2303/16

  Regeneration of sorbents, filters · CPC title

• C02F3/12

  Activated sludge processes · CPC title

• B01D65/06 Primary

  with special washing compositions · CPC title