CN101088924A - High manganese water purifying process - Google Patents

High manganese water purifying process Download PDF

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Publication number
CN101088924A
CN101088924A CN 200710011856 CN200710011856A CN101088924A CN 101088924 A CN101088924 A CN 101088924A CN 200710011856 CN200710011856 CN 200710011856 CN 200710011856 A CN200710011856 A CN 200710011856A CN 101088924 A CN101088924 A CN 101088924A
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CN
China
Prior art keywords
high manganese
filtrate
water
filter screen
diatomite
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 200710011856
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Chinese (zh)
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CN100509646C (en
Inventor
周楠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenyang Jianzhu University
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Shenyang Jianzhu University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenyang Jianzhu University filed Critical Shenyang Jianzhu University
Priority to CNB2007100118569A priority Critical patent/CN100509646C/en
Publication of CN101088924A publication Critical patent/CN101088924A/en
Application granted granted Critical
Publication of CN100509646C publication Critical patent/CN100509646C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Water Treatment By Sorption (AREA)

Abstract

The present invention is high manganese water purifying process, and relates to water treatment. The high manganese water purifying process includes the following steps: 1. adopting nickel net as filtering net; 2. adopting filtering material comprising diatomite and active carbon in the volume ratio of 2 to 1; and 3. accumulating the filtering material onto the filtering net to the thickness of 5-10 cm, applying positive voltage of 220 V to the filtering net and filtering underground water in the speed of 0.3-1.0 cu m/sq m.s, so as to eliminate manganese dioxide effectively. The process has low purifying cost and high manganese dioxide eliminating efficiency.

Description

A kind of high manganese water purifying process
Technical field
The present invention relates to a kind of water treatment method, particularly relate to a kind of high manganese water purifying process.
Background technology
Manganse Dioxide content is higher in the underground water of the northern area of China, it has been generally acknowledged that in the past it is harmless to human body, but it is a kind of potential carcinogens that Recent study is found Manganse Dioxide, therefore must find the low and effective purifying method of a kind of cost to handle high manganese water.
Summary of the invention
The objective of the invention is to overcome the existing inefficient shortcoming of high manganese water technology, improve by test, providing a kind of is filter screen with the nickel screen, and diatomite and gac are the low cost of filtrate, high efficiency high manganese water treatment method.
The objective of the invention is to be achieved through the following technical solutions:
A kind of high manganese water purifying process, this method may further comprise the steps:
(1) selecting nickel screen for use is filter screen;
(2) selecting diatomite and gac for use is filtrate, and diatomite and gac volume ratio are 2: 1;
(3) at first filtrate is deposited on the filter screen, thickness is 5~10cm, and nickel filter net is loaded 220V positive electricity, again with the underground water that extracts with the speed of 0.3~1.0 cubic metre of/square metre second by filtrate and filter screen, can effectively remove the Manganse Dioxide in the water.
Advantage of the present invention and effect are:
The present invention is filter screen with the nickel screen, and diatomite and gac are filtrate, and it is low that it purifies cost, Manganse Dioxide clearance rate height.
Embodiment
Embodiment 1
Selecting nickel screen for use is filter screen, and selecting diatomite and gac for use is filtrate, and diatomite and gac volume ratio are 2: 1; At first filtrate is deposited on the filter screen, thickness is 10cm, and nickel filter net is loaded 220V positive electricity, again with the underground water that extracts with the speed of 0.3 cubic metre of/square metre second by filtrate and filter screen, can effectively remove the Manganse Dioxide in the water, clearance rate is 99%.
Embodiment 2
Selecting nickel screen for use is filter screen, and selecting diatomite and gac for use is filtrate, and diatomite and gac volume ratio are 2: 1; At first filtrate is deposited on the filter screen, thickness is 7cm, and nickel filter net is loaded 220V positive electricity, again with the underground water that extracts with the speed of 0.5 cubic metre of/square metre second by filtrate and filter screen, can effectively remove the Manganse Dioxide in the water, clearance rate is 94%.
Embodiment 3
Selecting nickel screen for use is filter screen, and selecting diatomite and gac for use is filtrate, and diatomite and gac volume ratio are 2: 1; At first filtrate is deposited on the filter screen, thickness is 5cm, and nickel filter net is loaded 220V positive electricity, again with the underground water that extracts with the speed of 1.0 cubic metres of/square metre seconds by filtrate and filter screen, can effectively remove the Manganse Dioxide in the water, clearance rate is 91%.

Claims (1)

1. a high manganese water purifying process is characterized in that, this method may further comprise the steps:
(1) selecting nickel screen for use is filter screen;
(2) selecting diatomite and gac for use is filtrate, and diatomite and gac volume ratio are 2: 1;
(3) at first filtrate is deposited on the filter screen, thickness is 5~10cm, and nickel filter net is loaded 220V positive electricity, again with the underground water that extracts with the speed of 0.3~1.0 cubic metre of/square metre second by filtrate and filter screen, can effectively remove the Manganse Dioxide in the water.
CNB2007100118569A 2007-06-25 2007-06-25 High manganese water purifying process Expired - Fee Related CN100509646C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2007100118569A CN100509646C (en) 2007-06-25 2007-06-25 High manganese water purifying process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2007100118569A CN100509646C (en) 2007-06-25 2007-06-25 High manganese water purifying process

Publications (2)

Publication Number Publication Date
CN101088924A true CN101088924A (en) 2007-12-19
CN100509646C CN100509646C (en) 2009-07-08

Family

ID=38942449

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2007100118569A Expired - Fee Related CN100509646C (en) 2007-06-25 2007-06-25 High manganese water purifying process

Country Status (1)

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CN (1) CN100509646C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MD4142C1 (en) * 2010-10-12 2012-07-31 Inst De Chimie Al Academiei De Stiinte A Moldovei Process for water purification from hydrogen sulfide and sulfides
CN106040175A (en) * 2016-06-30 2016-10-26 安徽建筑大学 Carbonization straw/kieselguhr molecular sieve manganese-removing filtering material doped with nanometer hydroxy manganese oxide

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MD4142C1 (en) * 2010-10-12 2012-07-31 Inst De Chimie Al Academiei De Stiinte A Moldovei Process for water purification from hydrogen sulfide and sulfides
CN106040175A (en) * 2016-06-30 2016-10-26 安徽建筑大学 Carbonization straw/kieselguhr molecular sieve manganese-removing filtering material doped with nanometer hydroxy manganese oxide

Also Published As

Publication number Publication date
CN100509646C (en) 2009-07-08

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Granted publication date: 20090708

Termination date: 20100625