CN202898094U - System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel - Google Patents

System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel Download PDF

Info

Publication number
CN202898094U
CN202898094U CN 201220498472 CN201220498472U CN202898094U CN 202898094 U CN202898094 U CN 202898094U CN 201220498472 CN201220498472 CN 201220498472 CN 201220498472 U CN201220498472 U CN 201220498472U CN 202898094 U CN202898094 U CN 202898094U
Authority
CN
China
Prior art keywords
pas
molten steel
aminosailcylic
para
acid
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
CN 201220498472
Other languages
Chinese (zh)
Inventor
赵锡斌
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 Sunlong Xingye Technology Co., Ltd.
Original Assignee
TIANJIN SHENLONG WATER TREATMENT ENGINEERING TECHNOLOGY Co Ltd
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 SHENLONG WATER TREATMENT ENGINEERING TECHNOLOGY Co Ltd filed Critical TIANJIN SHENLONG WATER TREATMENT ENGINEERING TECHNOLOGY Co Ltd
Priority to CN 201220498472 priority Critical patent/CN202898094U/en
Application granted granted Critical
Publication of CN202898094U publication Critical patent/CN202898094U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The utility model provides a system for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel, which comprises a waste liquid tank, a catalytic polymerization tank and a sedimentation and slagging removal tank. Wastewater flows from the waste liquid tank into the catalytic polymerization tank to react with an oxidizing agent; and a reaction product enters the sedimentation and slagging removal tank. The system has the beneficial effects that due to adoption of the technical scheme, the reaction product obtained after the waste molten steel is processed is the flocculant PAS and can be industrially utilized; and the system has the advantages of simple structure, reduction of cost, environmental protection, effectiveness, high production efficiency and the like.

Description

The system of flocculation agent PAS is produced in the catalysis of a kind of steel scrap liquid
Technical field
The utility model relates to the system that flocculation agent PAS is produced in the catalysis of a kind of steel scrap liquid.
Background technology
Steel work manufacturer, the pickle solution of generation contains a large amount of metallic irons, the general about 10-20% of iron-holder, directly discharging can pollute, and just is badly in need of a kind of method or system that can process steel scrap liquid, protection of the environment now.
The utility model content
The system of flocculation agent PAS is produced in the steel scrap liquid catalysis that the purpose of this utility model provides a kind of protection of the environment, utilization of waste material.
The technical solution of the utility model is: the system of flocculation agent PAS is produced in the catalysis of a kind of steel scrap liquid, comprise that waste liquid pool, catalyzed polymerization pond and sedimentation are except slag bath, waste water flows to the described catalyzed polymerization pond and oxidant reaction from described waste liquid pool, and reaction product enters described falling except slag bath.
Preferably, described oxygenant is hydrogen peroxide or sodium chlorate.
Advantage and the positively effect that the utlity model has are:
Owing to adopt technique scheme, having processed the reaction product that obtains after the steel scrap liquid is flocculation agent PAS, can industrialized utilization; Have simple in structure, reduce cost, environmental protection effectively, the production efficiency advantages of higher.
Description of drawings
Fig. 1 is process flow sheet of the present utility model;
Fig. 2 is structural representation of the present utility model.
Among the figure:
1, waste liquid pool 2, catalyzed polymerization pond 3, catalyzed polymerization pond
Embodiment
The utility model is described in further detail below in conjunction with the drawings and the specific embodiments.
As depicted in figs. 1 and 2, the utility model comprises waste liquid pool 1, catalyzed polymerization pond 2 and catalyzed polymerization pond 3, waste water flows to the described catalyzed polymerization pond 2 from described waste liquid pool 1 and reacts with oxidant hydrogen peroxide, reaction product enters described falling except slag bath 3, directly just can carry out the packing of polymerization iron sulfate water-purifying agent product.
The utility model adds oxygenant two valency iron in the waste liquid is oxidized to ferric iron, makes it to become polymerization iron sulfate water-purifying agent by polyreaction again, reacts as follows:
Fe 2+q+M+H 2O→〔Fe 2(OH) n(SO 4) 3-n/2m
With the utilization of waste material of steel scrap liquid, can reduce well cost, protection of the environment.
Above embodiment has been described in detail the utility model, but described content only is preferred embodiment of the present utility model, can not be considered to be used to limiting practical range of the present utility model.All equalizations of doing according to the utility model application range change and improve etc., all should still belong within the patent covering scope of the present utility model.

Claims (2)

1. the system of flocculation agent PAS is produced in steel scrap liquid catalysis, it is characterized in that: comprise that waste liquid pool (1), catalyzed polymerization pond (2) and sedimentation are except slag bath (3), waste water flows to the described catalyzed polymerization pond (2) and oxidant reaction from described waste liquid pool (1), and reaction product enters described falling except slag bath (3).
2. the system of flocculation agent PAS is produced in steel scrap liquid according to claim 1 catalysis, it is characterized in that: described oxygenant is hydrogen peroxide or sodium chlorate.
CN 201220498472 2012-09-26 2012-09-26 System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel Expired - Fee Related CN202898094U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220498472 CN202898094U (en) 2012-09-26 2012-09-26 System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220498472 CN202898094U (en) 2012-09-26 2012-09-26 System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel

Publications (1)

Publication Number Publication Date
CN202898094U true CN202898094U (en) 2013-04-24

Family

ID=48118787

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220498472 Expired - Fee Related CN202898094U (en) 2012-09-26 2012-09-26 System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel

Country Status (1)

Country Link
CN (1) CN202898094U (en)

Similar Documents

Publication Publication Date Title
CN103739039B (en) A kind of multi-dimensional electro-catalytic equipment
CN105461043B (en) A kind of advanced catalytic oxidation method for handling phthalic acid ester waste water
CN103449527A (en) Method for preparing ferrate through hydraulic power cavitation and activation
CN105461103A (en) Fenton fluidized bed wastewater treatment method using iron oxide red as carrier
CN102659290A (en) Method for advanced treatment of high-concentration chemi-mechanical pulp effluent by catalytic oxidation
CN102295389A (en) Industrial waste water treating technology
CN102942243A (en) Wastewater treatment method combining three-dimensional electrode and electric Fenton
CN204529549U (en) A kind of acid fracturing Waste Water Treatment
CN113171881B (en) Method for recycling metal ions in sulfuric acid process titanium dioxide waste acid
CN202898094U (en) System for preparing flocculant PAS (Para-Aminosailcylic Acid) by catalyzing waste molten steel
CN103924082A (en) Method for removing iron from laterite-nickel ore high-pressure leaching solution
CN103755066A (en) Waste regenerating production process after hot galvanizing
CN203307147U (en) Fluidized bed reactor for advanced treatment of pulping and papermaking wastewater by Fenton method
CN102897880A (en) System for preparing poly aluminum sulfate (PAS) flocculant through catalysis of waste molten steel
CN206927636U (en) A kind of dehydrogenation of isobutane device waste water reclaiming device
CN103304113A (en) Sludge treatment method
CN204644045U (en) A kind for the treatment of system of epoxy resin production waste-water
CN204727647U (en) A kind of micro-electrolysis reactor
CN204111472U (en) A kind of branch inlet type Fenton reagent oxidizing treater
CN103936113B (en) A kind of iron charcoal reactor apparatus and treatment process processing high concentrated organic wastewater
CN203389528U (en) Tailing slurry type flue gas desulfurization treatment equipment
CN1101011A (en) Production method for polymerization iron sulfate water-purifying agent
CN201990574U (en) Beer production waste water treatment system
CN202729944U (en) Treatment device of printing and dyeing wastewater
CN204211568U (en) The Fenton treatment unit of waste water

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20150914

Address after: 300384 Tianjin City Huayuan Industrial Zone Rong Yuan Road No. 15 1-C-1405

Patentee after: Tianjin Sunlong Xingye Technology Co., Ltd.

Address before: Three road 300000 Tianjin Haitai Huayuan Industrial Zone No. 1 Building No. 1 -1-409 branch

Patentee before: TIANJIN SHENLONG WATER TREATMENT ENGINEERING TECHNOLOGY CO., LTD.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130424

Termination date: 20150926

EXPY Termination of patent right or utility model