欧美亚洲精品SUV,国产精品视频在线观看,花蝴蝶日本视频免费高清,色狠狠一区二区三区香蕉

Location:Home > News Center > Industry News
Causes of ultrafiltration membrane fouling and its harm to the system
Time:2022-04-12

Membrane fouling is the biggest problem during the operation of ultrafiltration device, and it is also one of the most common problems of ultrafiltration device. The pollution is mainly manifested in the reduction of water yield and the deterioration of water quality. At the same time, with the increase of water inlet pressure, the transmembrane pressure difference increases, and there is a certain phenomenon of wire breakage. The greater the transmembrane pressure difference, the more serious the wire breakage phenomenon will be.

Causes of fouling in ultrafiltration system:

(1) The inlet water temperature of ultrafiltration is too low, resulting in the increase of operation resistance;

(2) Ultrafiltration membrane fouling is caused by raw water pollution, too many bacteria and algae, that is, the SDI of influent is too high, resulting in ultrafiltration fouling;

(3) The influent flow of ultrafiltration increases, which exceeds the water production capacity of the filter membrane;

(4) The inlet pressure is too high. In order to increase the water production, artificially increase the inlet pressure of ultrafiltration.

When ultrafiltration is polluted, it will have a great impact on RO system and increase pollution blockage, mainly in the following aspects:

(1) The water quality deteriorates, the SDI value becomes higher or exceeds the standard, and the color of the SDI value test diaphragm becomes darker;

(2) The reverse osmosis membrane is polluted and blocked, resulting in the rapid decline of water production rate of the reverse osmosis system;

(3) When the UF is seriously polluted, a layer of "sponge" will be generated in the UF. During chemical cleaning, the residual NaOH or sodium hypochlorite can not be washed in time, which will be released slowly, which will bring serious harm to the subsequent RO system.

Therefore, in ultrafiltration operation, it is generally designed with forward flushing, backflushing and conventional on-line automatic pH adjustment immersion cleaning. Generally, it is backwashed once from 20min to 1H; Conduct a low pH or high pH cleaning for more than 8h. When adjusting the pH, generally soak for 10min, and then conduct physical flushing. When soaking with alkaline solution, a certain amount of NaClO is often added to enhance the cleaning effect.

The filtration mode of membrane is divided into dead end and cross flow. Dead end filtration, also known as full flow filtration, means that the flow direction of the liquid is perpendicular to the membrane surface. After the filtered liquid passes through the membrane, all the intercepts are deposited on the membrane surface. This filtration mode has a high probability of blockage and is generally suitable for water quality with low turbidity and low suspended solids content. Cross flow filtration can realize the continuous operation of ultrafiltration device and meet the scale requirements of large flow. In cross flow filtration, the water flow is parallel to the surface of the filter membrane, which can form a large shear force on the surface of the filter membrane, resulting in the membrane pollutants always in a suspended state, reducing the impact of concentration polarization, reducing the deposition of particles and solutes on the membrane surface and reducing membrane pollution. Therefore, the cross flow mode has strong adaptability to the water quality of feed water. In addition, increasing the cross flow velocity can also improve the critical flux.

When the TMP increases to a certain level and cannot be recovered through cross flow and backwashing, chemical cleaning can be used to recover the membrane flux. Through contact with a certain dose of chemicals and under the action of large flow cleaning, the pollutants on the membrane surface and membrane pores can be removed, so as to restore the flux of the membrane.

Most ultrafiltration equipment adopts hollow fiber membrane wire. It is a common phenomenon that a small amount of wire breakage occurs during operation. Wire breakage is generally caused by membrane wire fouling, back impact and other reasons. Tens of thousands of membrane wires are installed in one element, and a small amount of broken wires will not immediately affect the water quality. Therefore, it is not easy to detect during operation. However, once the change of water production quality is found, the accurate position of broken wire should be determined quickly in order to take corresponding measures.

The treatment of broken wire is generally to find out the damaged membrane wire and block it. If the amount of broken wire or blocked membrane wire increases to a certain extent (more than 10%), the whole element needs to be replaced.


Weclome
Sichuan sidaneng Environmental Protection Technology Co., Ltd
MORE
Service Tel:
+86 189-8175-1540
Join Us
日韩毛片| 久久精品人妻中文系列| 久草视频新免费| 无码人妻久久一区二区三区免费| 三人性FREE欧美| 亚洲国产成人精品无码区99| 成人区人妻精品一区二区不卡网站| 中文字幕乱码一区二区欧美| 免费无码av一区二区三区| 亚洲午夜无码久久久久软件| 丰满熟女人妻大乳波多野吉衣| 香蕉AV久久一区二区三区| 国产在线拍揄自揄拍免费下载 | 亚洲天天做日日做天天爽| 婷婷亚洲五月色综合久久| 亚洲日韩av在线观看| 国产在线拍揄自揄视精品| 日本精品人妻无码免费大全| 99久久国产精品人妻无码| 亚洲AV午夜成人片精品网站| 成 人 A V免费视频在线观看| 欧美巨大乳bbwvideos| 国产精品久久久久久久小说| 亚洲国产精品无码专区网站| 凹凸国产熟女精品视频app| 国产99视频精品免视看9| 88国产精品视频一区二区三区| 亚洲AV无码一区二区三区DV| 熟妇人妻系列AV无码一区二区| 無码一区中文字幕少妇熟女| 国产精品欧美一区二区三区不卡| 久久精品国产亚洲AV无码麻豆| 国产精品久久久久久久久久直播 | 日韩精品人妻中文字幕有码| 国产精品久久人妻互换| 国产伦精品一区二区三区| 少妇特黄A片一区二区三区蜜桃 | 精品丰满人妻无套内射| 久久久久国产精品嫩草影院欧洲| 色欲精品人妻AV一区二区三区| 花火视频影视大全免费观看|