CN2114658U - Oxidation reacting tower for water treatment - Google Patents

Oxidation reacting tower for water treatment Download PDF

Info

Publication number
CN2114658U
CN2114658U CN 92215175 CN92215175U CN2114658U CN 2114658 U CN2114658 U CN 2114658U CN 92215175 CN92215175 CN 92215175 CN 92215175 U CN92215175 U CN 92215175U CN 2114658 U CN2114658 U CN 2114658U
Authority
CN
China
Prior art keywords
pipe
water
reactive center
center pipe
tower body
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 92215175
Other languages
Chinese (zh)
Inventor
吴克中
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 92215175 priority Critical patent/CN2114658U/en
Publication of CN2114658U publication Critical patent/CN2114658U/en
Granted legal-status Critical Current

Links

Images

Abstract

The utility model relates to an oxidation reaction tower for water treatment used for removing soluble heavy metal ion in raw water or industrial waste water, comprising a tower body, a reaction center pipe, etc. The utility model is characterized in that the lower part of the reaction center pipe is communicated with a neutralizing agent juice filling pipe, a raw water or waste water inlet pipe and an air lance. The utility model has the advantages that the consumption of the neutralizing agent is reduced, the removal ratio of the soluble heavy metal ion in water is enhanced, iron and manganese ion contents in the water are lower than 1 and 0.1 mg / l after treatment, and removal ratio is 98-100%.

Description

Oxidation reacting tower for water treatment
The utility model relates to the water treating equipment of heavy metal ion in former water of a kind of water treating equipment, particularly oxidation removal or the trade effluent.
Contain soluble iron, manganese plasma in the former water, influence civilian or the industrial production use.Contain a large amount of these type of heavy metal ion in non-ferrous metal metallurgy, iron and steel, titanium dioxide, the detergent factory's trade effluent.Must can discharge or reuse through handling.Adopt present general equipment such as flow lifting type expansion neutralizing tower, drum-type filtration neutralizer to remove soluble heavy metal ions in former water or the waste water, its common shortcoming is that clearance is low, removal of heavy metal ions rate as trade effluent has only about 50%, is difficult to reach the basic demand of water treatment.
The purpose of this utility model provides the water treating equipment of soluble heavy metal ions in former water of a kind of efficient removal or the waste water.
Task of the present utility model is finished like this.Inject the neutralizing agent juice in former water or the trade effluent, regulate pH value, make water transfer alkali to by acidity, spray into air simultaneously, the assurance oxidizing reaction is fully carried out in vigorous stirring, at a low price becomes after oxidation can settled high-valency metal compound for soluble metal ion, through promptly be purified water behind settling tank eliminating settling.The utility model of principle design one-tenth is made up of tower body and reactive center pipe etc. in view of the above.The reactive center pipe is positioned at tower body central authorities, is communicated with neutralizing agent juice filler pipe, former water or waste water in reactive center pipe bottom and enters pipe, air lance, also can only be communicated with back two kinds of pipelines.Neutralizing agent juice filler pipe, former water or waste water enter pipe can be radially or tangentially be communicated with the reactive center pipe.The tower body bottom has scum pipe, top that effluent trough, rising pipe are arranged.There is the reflection flow deflector reactive center pipe upper end, also has extraction hood.Between tower body and extraction hood, form the particle separation chamber.Between reactive center pipe outer wall and tower body inwall, form reaction chamber.Because feed the effect of reactive center pipe airflow, oxidizing reaction from bottom to top, is carried out again in reactive center pipe and reaction chamber from top to bottom repeatedly.Discharge from scum pipe after the inert substance sedimentation.Generate and to be gathered in tower body top by settled high volence metal ion compound through oxidation, flow out from rising pipe through effluent trough, after neutralizing treatment enters settling tank, be excluded, be purified water immediately with current.
Fig. 1 is the utility model water treatment oxidizing reaction tower sectional view
Now the utility model is described in further detail in conjunction with the accompanying drawings.
The utility model is made up of tower body (12), reactive center pipe (7) etc.Reactive center pipe (7) is positioned at tower body (12) central authorities, supports (5) by means of pipe core and fuses with tower body (12).Reactive center pipe (7) both ends open, bottom are communicated with neutralizing agent juice filler pipe (8), former water or waste water and enter pipe (11), air lance (9), also can only be communicated with back two kinds of pipelines.It can be radially or tangentially to be communicated with reactive center pipe (7) that neutralizing agent juice filler pipe (8), former water or waste water enter pipe (11).The tower body bottom has scum pipe (10), top that effluent trough (14), rising pipe (2) are arranged.There is reflection flow deflector (4) reactive center pipe (7) upper end, also has extraction hood (1).Between tower body (12) and extraction hood (1), form particle separation chamber (3).Between reactive center pipe (7) and tower body (12) inner chamber, form reaction chamber (6).Tower body (12) is provided with maintenance open holes (13).
The neutralizing agent of using is lime or carbide slag, can also can directly add in the tower body reaction chamber (6) through neutralizing agent juice filler pipe (8) input reactive center pipe (7).PH value generally is adjusted into 8-10.Because the effect of airflow, oxidizing reaction is fully carried out in the reactive center pipe He in the tower body reaction chamber, both saved the consumption of neutralizing agent, improve the clearance of former water or trade effluent soluble heavy metal ions again, through the utility model handle and after settling tank is handled water outlet iron, mn ion content be lower than 1,0.1 mg/litre, clearance is at 98-100%.

Claims (4)

1, a kind of water treatment oxidizing reaction tower comprises tower body (12), reactive center pipe (7) etc., it is characterized in that: reactive center pipe (7) bottom is communicated with former water or wastewater inlet pipe (11), air lance (9).
2, by the described reaction tower of claim 1, it is characterized in that: reactive center pipe (7) bottom also is communicated with neutralizing agent juice filler pipe (8).
3, by claim 1 or 2 described reaction towers, it is characterized in that: neutralizing agent juice filler pipe (8), former water or wastewater inlet pipe (11) tangentially are communicated with reactive center pipe (7).
4, by the described reaction tower of claim 3, it is characterized in that: extraction hood (1), effluent trough (14), rising pipe (2) are arranged at tower body top, there is reflection flow deflector (4) reactive center pipe (7) upper end, constitutes particle separation chamber (3) between tower body (12) top and extraction hood (1).
CN 92215175 1992-02-25 1992-02-25 Oxidation reacting tower for water treatment Granted CN2114658U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 92215175 CN2114658U (en) 1992-02-25 1992-02-25 Oxidation reacting tower for water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 92215175 CN2114658U (en) 1992-02-25 1992-02-25 Oxidation reacting tower for water treatment

Publications (1)

Publication Number Publication Date
CN2114658U true CN2114658U (en) 1992-09-02

Family

ID=4959609

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 92215175 Granted CN2114658U (en) 1992-02-25 1992-02-25 Oxidation reacting tower for water treatment

Country Status (1)

Country Link
CN (1) CN2114658U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439276A (en) * 2015-12-28 2016-03-30 徐州市城区水资源管理处 Device and processing method for removing high-concentration ferro-manganese in mine water with oxidation and catalysis column

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439276A (en) * 2015-12-28 2016-03-30 徐州市城区水资源管理处 Device and processing method for removing high-concentration ferro-manganese in mine water with oxidation and catalysis column
CN105439276B (en) * 2015-12-28 2017-11-24 徐州市城区水资源管理处 A kind of oxidation catalysis post removes mine water middle and high concentration ferrimanganic device and its processing method

Similar Documents

Publication Publication Date Title
CN101875518B (en) Treatment method of stainless steel pickling waste water
US4565633A (en) Removal of dissolved heavy metals from aqueous waste effluents
CN107188339A (en) A kind of composite ozone air-floating integral unit
CN106242185B (en) Banana pulp producing wastewater treatment
CN106630370B (en) Sewage disposal system, the method for Hydrodynamic cavitation dephosphorization apparatus and the application device
US5647996A (en) Groundwater total cyanide treatment method
CN102153216B (en) Method and equipment for removing heavy metal from rubbish hydrolysate
CN210974194U (en) Comprehensive utilization system for phosphogypsum backwater
CN2114658U (en) Oxidation reacting tower for water treatment
CN202881027U (en) Device for removing organophosphorus from wastewater produced in rare earth extraction process
CN213171877U (en) Device for treating arsenic-containing waste acid
CN210945128U (en) Desulfurization wastewater treatment device
CN101314087A (en) High-efficiency steel-smelting wet-process dedusting sewage water and refining sewage processor
CN204918228U (en) Acid copper -containing effluent disposal system in metal mine
CN208577561U (en) A kind of mining smelting wastewater exception water quality emergency treatment device
CN113880318A (en) Two-stage advanced oxidation process, system and application for treating chemical wastewater
CN208087423U (en) Painting wastewater processing equipment
CN113209781A (en) System and method for removing fluorine in pyrometallurgical flue gas
CN112777801A (en) Integrated form sludge water processing system
CN100412000C (en) Treatment method for ash water of heating and power plant
CN2511382Y (en) Special apparatus for treating flute containing sulfur dioxide
CN2151113Y (en) Vertical container with spiral discharge to a fixed ration
CN215161278U (en) Smelting wastewater treatment device
CN209468238U (en) Waste acid sewage treatment and intermediate water reuse system in lead smelting process
CN216191595U (en) Advanced oxidation equipment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee