CN103145263B - Method for removing trace manganese in aqueous solution - Google Patents

Method for removing trace manganese in aqueous solution Download PDF

Info

Publication number
CN103145263B
CN103145263B CN201310060173.8A CN201310060173A CN103145263B CN 103145263 B CN103145263 B CN 103145263B CN 201310060173 A CN201310060173 A CN 201310060173A CN 103145263 B CN103145263 B CN 103145263B
Authority
CN
China
Prior art keywords
manganese
aqueous solution
carbonate
industry
calcium
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.)
Expired - Fee Related
Application number
CN201310060173.8A
Other languages
Chinese (zh)
Other versions
CN103145263A (en
Inventor
孙波
杜倩
安钢
吴新世
张春雪
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.)
Tianjin University of Technology
Original Assignee
Tianjin University of Technology
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 Tianjin University of Technology filed Critical Tianjin University of Technology
Priority to CN201310060173.8A priority Critical patent/CN103145263B/en
Publication of CN103145263A publication Critical patent/CN103145263A/en
Application granted granted Critical
Publication of CN103145263B publication Critical patent/CN103145263B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Removal Of Specific Substances (AREA)

Abstract

The invention discloses a method for removing trace manganese in aqueous solution. By cultivating and analyzing a plant which grows in a manganese environment, acid or alkali is used for adjusting the pH value of a manganese-contained aqueous solution, calcium reagent, phosphate and carbonate are respectively added into the manganese-contained aqueous solution, then the manganese-contained aqueous solution stands and deposits to separate water containing manganese residues, and the content of the manganese in the water is detected to be less than 0.01mg/L. The method is characterized in that by controlling the addition quantity of the calcium reagent, the phosphate and the carbonate as well as the pH value of the solution, trace manganese in the aqueous solution can be removed; and moreover, the water treatment time is short, raw materials used in the method are economical and easily gotten, and no harmful element is added to the system, so that the method is an environment-friendly and economical treatment process. The process can be widely used for treating manganese-contained waste water discharged in the fields such as the metal machining industry, the electroplating industry, the machine building industry, the catalyzing industry, the tannery industry and the textile industry.

Description

A kind of method that removes trace manganese in the aqueous solution
[technical field]
The present invention relates to the field of waste water treatment in environmental technology, particularly a kind of method that removes trace manganese in industrial wastewater.
[background technology]
Along with increasing sharply of trade waste, the heavy metal in water pollution by manganese causing is more and more serious.In trade effluent, usually find manganese, maximum pollution by manganese is from the exploitation of manganese ore and smelting, metal processing, machinofacture, Iron and Steel Production, battery, dyestuff, catalyzer etc.In these industrial effluent liquid, usually contain the poisonous manganese compound of a great deal of.
Traditional method that removes manganese is suitable for processing the waste liquid that manganese content is higher, but for liquid waste disposal that manganese content is lower, removal effect is undesirable, when processing, agents useful for same consumption is large, produces thus a large amount of waste residues, but also may in water body, introduce undesirable ion.
[summary of the invention]
The object of the invention is, for protection of the environment, to meet the needs of economical and efficient simultaneously, and a kind of method that removes micro-Trace Amount Manganese in the aqueous solution is provided.The method comprises by acid or the pending pH value containing manganese waste liquid of alkali adjusting, adds containing calcon, phosphoric acid salt, carbonate, through leaving standstill, after precipitation, isolates containing manganese and precipitates.
The invention discloses a kind of method that removes trace manganese in the aqueous solution, it is characterized in that: in the pending aqueous solution that contains bivalent manganese, intersect or add as follows reagent simultaneously and regulate pH Value Operations: adding containing calcon, add phosphoric acid salt, add carbonate, regulate the pH value of the pending aqueous solution with acid or alkali; Then leave standstill solution, separate out precipitation, finally separate containing manganese precipitation; Described adjusting pH value is 6-8, and calcic reagent dosage is that the mol ratio of calcium and manganese is 0.1-10:1, and phosphoric acid salt consumption is that the mol ratio of phosphorus and manganese is 0.1-10:1, and carbonate consumption is that the mol ratio of carbon and manganese is 0.1-10:1.
The method that removes trace manganese in the aqueous solution of the present invention, can be used for administering trade effluent, takes into account economy and environment protection simultaneously.It can cut the waste, and improves the decreasing ratio of lower concentration manganese, reduces costs, and reduces environmental pollution simultaneously.Be characterized in by cultivation and anatomy to growing plant under manganese environment, by controlling pH, and add containing calcon, phosphoric acid salt, carbonate etc., substantially remove the manganese containing manganese waste liquid completely.The raw materials used economy of the present invention is easy to get, and in system, does not add any harmful element, and the wastewater treatment time is short, reagent dosage water, and waste residue generation is few, and in the aqueous solution after treatment, manganese content is less than 0.01mg/L, can enter secondary network.Therefore be a kind of environmentally friendly treatment process.This technique can be widely used in the processing of the Mn-bearing waste water discharging in the fields such as metal-processing industry, Electroplating Operations, machinery manufacturing industry, curriery and textile industry.
[embodiment]
The method that removes aqueous solution trace manganese of the present invention, in the pending aqueous solution that contains bivalent manganese, to add as follows reagent first, afterwards or simultaneously and regulate pH Value Operations: add containing calcon, add phosphoric acid salt, add carbonate, regulate the pH value of the pending aqueous solution with acid or alkali; Then leave standstill solution, separate out precipitation, finally separate containing manganese precipitation; Described adjusting pH value is 6-8, and calcic reagent dosage is that the mol ratio of calcium and manganese is 0.1-10:1, and phosphoric acid salt consumption is that the mol ratio of phosphorus and manganese is 0.1-10:1, and carbonate consumption is that the mol ratio of carbon and manganese is 0.1-10:1.
In described method treating processes, the temperature of the pending aqueous solution is 0~80 ℃.The better temperature of described method treating processes is 10~45 ℃.
Described is calcium chloride containing calcon, nitrocalcite, the mixture of one or more in calcium sulfate or calcium acetate.
Described phosphoric acid salt is sodium phosphate, SODIUM PHOSPHATE, MONOBASIC, Sodium phosphate dibasic, ammonium phosphate, the mixture of one or more in primary ammonium phosphate or ammonium hydrogen phosphate.
Described carbonate is sodium carbonate, sodium bicarbonate, salt of wormwood, saleratus, volatile salt, the mixture of one or more in bicarbonate of ammonia or calcium carbonate.
Embodiment 1: measuring manganese content is the aqueous solution 1L of 13mg/L, adds 30mg calcium chloride, and 0.6g Sodium phosphate dibasic, controlling aqueous temperature is 20 ℃.Under the condition of violent stirring hierarchy of control pH7-7.2, (while needs, regulate with sodium hydroxide and hydrochloric acid), drip 50mL containing 20mg sodium bicarbonate aqueous solution.After dropwising, continue to stir 1 hour.Afterwards, be cooled to room temperature, leave standstill, sedimentation also removes by filter containing manganese throw out.Through ICP(inductively coupled plasma emmission spectrum, lower with) analyze the manganese content of filtrate and be less than 0.01mg/L.
Embodiment 2: measuring manganese content is the aqueous solution 1L of 13mg/L, adds 4mg calcium sulfate, and 60mg Sodium phosphate dibasic, controlling aqueous temperature is 30 ℃.Under the condition of violent stirring hierarchy of control pH7-7.2, (while needs, regulate with sodium hydroxide and hydrochloric acid), drip 30mL containing 20mg ammonium bicarbonate aqueous solution.After dropwising, continue to stir 1 hour.Afterwards, be cooled to room temperature, leave standstill, sedimentation also removes by filter containing manganese throw out.Through ICP(inductively coupled plasma emmission spectrum, lower with) analyze the manganese content of filtrate and be less than 0.01mg/L.
Embodiment 3: measuring manganese content is the aqueous solution 1L of 13mg/L, under 40 ℃ and violent stirring, adds 20mg ammonium hydrogen phosphate and 0.2g nitrocalcite, then will be under the condition of control system pH6-6.5, drip the aqueous solution of 20mL containing 0.3g volatile salt.After dropwising, continue to stir 1 hour.Afterwards, be cooled to room temperature, leave standstill, sedimentation centrifugal removing containing manganese throw out.Manganese content through icp analysis filtrate is less than 0.01mg/L.
Embodiment 4: measuring manganese content is the aqueous solution 1L of 13mg/L, by its with hcl acidifying to pH~6, under violent stirring, add 0.4g calcium acetate, 20mg sodium bicarbonate and 3mg sodium phosphate, then pH value of solution is adjusted to 7.5~8, and to control aqueous temperature be 45 ℃.Continue to stir 2 hours.Afterwards, leave standstill, sedimentation also removes by filter containing manganese throw out.Manganese content through icp analysis filtrate is less than 0.01mg/L.
Embodiment 5: measuring manganese content is the aqueous solution 1L of 13mg/L, under violent stirring, adds 30mg ammonium phosphate, 40mg calcium sulfate and 10mg salt of wormwood, then pH value of solution is adjusted to 7~7.5, and to control aqueous temperature be 10 ℃.Continue to stir 2 hours.Afterwards, leave standstill, sedimentation also filters out containing manganese throw out.Manganese content through icp analysis filtrate is less than 0.01mg/L.
Embodiment 6: measuring manganese content is the aqueous solution 1L of 13mg/L, pH~7 of the adjusting aqueous solution.Under 30 ℃ and violent stirring, add 30mg ammonium hydrogen phosphate and 40mg calcium carbonate.Controlling solution~7(can add sodium hydroxide or hydrochloric acid to regulate), continue to stir 1 hour.Afterwards, leave standstill sedimentation centrifugal removing containing manganese throw out.Manganese content through icp analysis filtrate is less than 0.01mg/L.
Embodiment 7: measuring manganese content is the aqueous solution 1L of 13mg/L, adds 0.6g four water-calcium nitrate and 80mg primary ammonium phosphate, then uses pH~7 of sodium hydroxide solution regulator solution, and to control aqueous temperature be 10 ℃.Under the condition of violent stirring control system pH7.2-7.5, drip the aqueous solution of 6mL containing 3mg sodium carbonate.After dropwising, continue to stir 1 hour.Afterwards, be cooled to room temperature, leave standstill, sedimentation centrifugal removing containing manganese throw out.Manganese content through icp analysis filtrate is less than 0.01mg/L.

Claims (3)

1. one kind removes the method for trace manganese in the aqueous solution, it is characterized in that: in the pending aqueous solution that contains bivalent manganese, intersect or add as follows reagent simultaneously and regulate pH Value Operations: adding containing calcon, add phosphoric acid salt, add carbonate, regulate the pH value of the pending aqueous solution with acid or alkali; Then leave standstill solution, separate out precipitation, finally separate containing manganese precipitation; Described is calcium chloride containing calcon, nitrocalcite, the mixture of one or more in calcium sulfate or calcium acetate; Described phosphoric acid salt is sodium phosphate, SODIUM PHOSPHATE, MONOBASIC, Sodium phosphate dibasic, ammonium phosphate, the mixture of one or more in primary ammonium phosphate or ammonium hydrogen phosphate; Described carbonate is sodium carbonate, sodium bicarbonate, salt of wormwood, saleratus, volatile salt, the mixture of one or more in bicarbonate of ammonia or calcium carbonate; Described adjusting pH value is 6-8; Calcic reagent dosage is that the mol ratio of calcium and manganese is 0.1-10:1; Phosphoric acid salt consumption is that the mol ratio of phosphorus and manganese is 0.1-10:1; Carbonate consumption is that the mol ratio of carbon and manganese is 0.1-10:1.
2. the pending aqueous temperature that in accordance with the method for claim 1, it is characterized in that described method treating processes is 0~80 ℃.
3. according to the method described in claim 1 or 2, the pending aqueous temperature that it is characterized in that described method treating processes is 10~45 ℃.
CN201310060173.8A 2013-02-26 2013-02-26 Method for removing trace manganese in aqueous solution Expired - Fee Related CN103145263B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310060173.8A CN103145263B (en) 2013-02-26 2013-02-26 Method for removing trace manganese in aqueous solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310060173.8A CN103145263B (en) 2013-02-26 2013-02-26 Method for removing trace manganese in aqueous solution

Publications (2)

Publication Number Publication Date
CN103145263A CN103145263A (en) 2013-06-12
CN103145263B true CN103145263B (en) 2014-06-25

Family

ID=48543651

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310060173.8A Expired - Fee Related CN103145263B (en) 2013-02-26 2013-02-26 Method for removing trace manganese in aqueous solution

Country Status (1)

Country Link
CN (1) CN103145263B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104690080B (en) * 2015-03-28 2016-08-24 重庆大学 The directly method of harmless treatment electrolytic manganese residues in filtrating-pressing plate frame
CN114457241B (en) * 2022-01-05 2024-01-30 重庆大学 Method for reducing soluble manganese and water content of electrolytic manganese slag
CN114457240A (en) * 2022-01-05 2022-05-10 重庆大学 Method for harmlessly treating electrolytic manganese slag leachate
CN115583740A (en) * 2022-09-09 2023-01-10 昆山三一环保科技有限公司 Manganese removal method and system for iron phosphate wastewater

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87106661A (en) * 1987-09-28 1988-04-06 湖北工业建筑设计院 A kind of underground water deferrization and demanganization equipment
JP3659383B2 (en) * 1998-03-30 2005-06-15 株式会社荏原製作所 Method and apparatus for treating manganese-containing water
CN102139973A (en) * 2011-02-18 2011-08-03 南京大学 Method for treating micro-polluted and eutrophicated water body by utilizing coprecipitation method
CN102153187A (en) * 2011-05-11 2011-08-17 天津理工大学 Method for removing trace chromium in aqueous solution

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87106661A (en) * 1987-09-28 1988-04-06 湖北工业建筑设计院 A kind of underground water deferrization and demanganization equipment
JP3659383B2 (en) * 1998-03-30 2005-06-15 株式会社荏原製作所 Method and apparatus for treating manganese-containing water
CN102139973A (en) * 2011-02-18 2011-08-03 南京大学 Method for treating micro-polluted and eutrophicated water body by utilizing coprecipitation method
CN102153187A (en) * 2011-05-11 2011-08-17 天津理工大学 Method for removing trace chromium in aqueous solution

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
仿骨盐吸附剂的合成及其在脱除重金属方面的应用;田惠芸等;《天津理工大学学报》;20110430;第27卷(第2期);第76-81页 *
田惠芸等.仿骨盐吸附剂的合成及其在脱除重金属方面的应用.《天津理工大学学报》.2011,第27卷(第2期),

Also Published As

Publication number Publication date
CN103145263A (en) 2013-06-12

Similar Documents

Publication Publication Date Title
Booker et al. Struvite formation in wastewater treatment plants: opportunities for nutrient recovery
US9102555B2 (en) Method for removing phosphorus and nitrogen contained in sewage or wastewater using iron ore wastewater
TWI551549B (en) Method for removing phosphorus from wastewater and method for preparing ferrous phosphate
CN106315535B (en) A kind of method that pure ferric phosphate is prepared from iron content zinc waste phosphorized slag
CN102887535A (en) Method for recycling high-purity fluorine and phosphorus from wastewater of phosphogypsum residue field
CN104761114A (en) Enhanced wastewater phosphorus removal method
CN102249450B (en) Method for removing trace cadmium from aqueous solution
CN103145263B (en) Method for removing trace manganese in aqueous solution
CN106892415B (en) A kind of method that byproduct ferrous sulfate of titanium dioxide prepares ferric phosphate
CN102126738A (en) Method for producing nitrophosphate fertilizer and co-producing gypsum through decomposing phosphorite with nitric acid
Huang et al. Removal of ammonium as struvite using magnesite as a source of magnesium ions
CN107056388B (en) Chemical polishing waste phosphoric acid treatment method and fertilizer preparation method
CN103951113A (en) Method for removing tetracycline antibiotics in wastewater phosphorus recovery product
CN107055495A (en) A kind of acid phosphorus-containing wastewater is used for the method for phosphorus ore de-magging
Zhang et al. Obtaining high-purity struvite from anaerobically digested wastewater: effects of pH, Mg/P, and Ca2+ interactions
CN105272441A (en) Process for production of liquid compound fertilizer by combination of decomposition of phosphate ore by use of nitric acid and removal of calcium by use of potassium salt
CN104944561A (en) Wastewater nitrogen and phosphorus removing method based on magnesite
CN102583685B (en) Method for removing trace mercury in water solution
CN102153187B (en) Method for removing trace chromium in aqueous solution
CN103951112A (en) Method for removing heavy metals in wastewater phosphorus recovery product
CN102765834A (en) Method for treating industrial nitrogenous waste water through chemical precipitation method
CN106745631B (en) Method for removing fluorine and arsenic in tungsten smelting wastewater
CN115321736A (en) Treatment method of glyphosate production wastewater and high-value recycling of phosphorus-containing waste
CN104163486A (en) Method for treating glyphosate waste water by using calcium hypochlorite waste water
CN104401956A (en) Method for producing magnesium ammonium phosphate from high-magnesium phosphorite powder extraction waste liquid

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140625

Termination date: 20160226