CN101311331A - On-line processing system for nickel-plating rinsing waste water - Google Patents

On-line processing system for nickel-plating rinsing waste water Download PDF

Info

Publication number
CN101311331A
CN101311331A CNA2008100263548A CN200810026354A CN101311331A CN 101311331 A CN101311331 A CN 101311331A CN A2008100263548 A CNA2008100263548 A CN A2008100263548A CN 200810026354 A CN200810026354 A CN 200810026354A CN 101311331 A CN101311331 A CN 101311331A
Authority
CN
China
Prior art keywords
nickel
waste water
processing system
plating
water
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
CNA2008100263548A
Other languages
Chinese (zh)
Other versions
CN101311331B (en
Inventor
古晓雁
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.)
GUANGDONG REAL FAITH LIGHTING TECHNOLOGY CO., LTD.
Original Assignee
FOSHAN ZHAOXIN METAL PRODUCTS 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 FOSHAN ZHAOXIN METAL PRODUCTS Co Ltd filed Critical FOSHAN ZHAOXIN METAL PRODUCTS Co Ltd
Priority to CN2008100263548A priority Critical patent/CN101311331B/en
Publication of CN101311331A publication Critical patent/CN101311331A/en
Application granted granted Critical
Publication of CN101311331B publication Critical patent/CN101311331B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses an on-line processing system of the rinse waste water of nickel plating, comprising the corresponding equipment of rinsing treatment connected with a nickel plating wastewater discharge port, which is characterized in that the processing system of the rinse waste water of nickel plating is connected with a nickel plating production line to form an integrated on-line processing system of circulation recovery. The on-line processing system comprises the following parts which are mutually communicated by pipes: a pre-filter, a fine-filter, a buffer tank, a clean-in-place tank, a secondary fine-filter and a nanofiltration membrane or a reverse osmosis membrane. A pressure feeding pump is also correspondingly arranged in the pipes. The dialysate treated by the nanofiltration membrane or the reverse osmosis membrane is communicated with a water using spot of the nickel plating production line by pipes while the concentrated solution treated by the nanofiltration membrane or the reverse osmosis membrane is communicated with a nickel plating groove of the nickel plating production line by a recovery groove. The pipes of the dialysate treated by the nanofiltration membrane or the reverse osmosis membrane can also be connected with a water inlet which is provided with a multilevel countercurrent rinsing device, so as to from an airtight circulation system. The on-line processing system has the advantages of high treatment efficiency, environmental protection and good water treating quality.

Description

The Online Processing System of nickel-plating rinsing waste water
Technical field
The present invention relates to a kind of treatment system of electroplate rinsing wastewater, but specifically be a kind of online treatment nickel-plating rinsing waste water process system.
Background technology
Waste water rinsing after traditional nickel plating generally is with the waste water after the nickel plating, by pipeline it is collected in together, adopts chemical method to concentrate then and handles, by regulating pH value with Ni 2+Transfer Ni (OH) to 2, flocculation agents such as adding polyacrylamide are handled, and then by precipitation mode, by the strainer filtering separation it are removed again; Nickeliferous mud is sent to professional factory again and refines in the precipitation, and nickel is reclaimed, and the water after will handling simultaneously discharges, and as shown in Figure 1, is the treatment system skeleton diagram of prior art.
Yet, this mode that focuses on, be subjected to reason sedimentations such as discharge to filter bad control, treatment effect is not remarkable, and processing efficiency is lower, its system's cost of investment height, land occupation area are big, working cost is also high, can't realize the reuse immediately of waste water, send associated companies to refine recovery again though the nickel metal in the waste water can be collected by coprecipitation mode, but resource utilization is low, the cost height.
Summary of the invention
The objective of the invention is to overcome traditional treatment technology, provide a kind of processing cost low, recycle the efficient height, can carry out the nickel-plating rinsing waste water treatment system of online treatment waste water.
A kind of Online Processing System of nickel-plating rinsing waste water, the relevant device that comprises the rinsing processing that connects the nickel-plating waste water discharge outlet, it is characterized in that, this nickel-plating rinsing waste water treatment system and nickel plating production line connect and compose looping back of an integral body and are received in the line treatment system, it specifically comprises the following part that is interconnected by pipeline: prefilter, accurate filter, buffer tank, clean-in-place CIP water tank, secondary accurate filter and nanofiltration/reverse osmosis (NF/RO) film, the corresponding pressurization charging pump that also is provided with in the pipeline, the dialyzate of handling through nanofiltration/reverse osmosis (NF/RO) film is by the water spot of use of pipeline connection nickel plating production line, can directly be communicated with the nickel bath of nickel plating production line or be communicated with by the nickel bath of accumulator tank with the nickel plating production line through the concentrated solution of NF/RO film processing.
As further specifying of such scheme, the described former water that enters treatment system also can be provided with the multi-stage countercurrent rinsing device and connect water-in again; Described multi-stage countercurrent rinsing device is generally three grades.
Be provided with charging pump between described buffer tank and the secondary accurate filter; Secondary accurate filter and NF/RO film are handled between the pipeline and are provided with topping-up pump.
Described buffer tank also can be connected with clean-in-place CIP water tank with pipeline between the charging pump, can clean whole piping system as required.
Meanwhile, also be connected with former water filler pipe road and raw water pump on the described prefilter.
The beneficial effect that the present invention adopts the solution of above-mentioned technology to reach is:
One, this treatment system adopts the circular treatment closed loop system that connects and composes an integral body with the nickel plating production line, directly nickel poaching wastewater on the line is handled, and is in time reclaimed useful nickel metal ingredient, and nickel metal recovery rate excellence can be controlled in more than 98%; Simultaneously by purifying treatment to nickel poaching wastewater on the line, with the waste water recycling rinsing on line after handling, a large amount of dischargings of poaching wastewater have been avoided, the water reclamation rate reaches more than 80%, substantially can be outside waste discharge, and waste the nickel plating post rinsing again and handle water, its water quality excellence of treated water has been avoided the waste of resource to greatest extent.
Two, technical scheme floor space of the present invention is little, cost is low, and flow process is short, pipeline is economized, the level of automation height, and the processing efficiency height, processing cost is controlled, helps promoting; And identical thinking can be applied to the processing of waste water after the rinsing of other coating baths.
Description of drawings
Fig. 1 is the process flow sheet of prior art;
Fig. 2 is the equipment flowsheet synoptic diagram of system of the present invention;
Fig. 3 is a process flow sheet of the present invention.
Description of reference numerals: 1 nickel bath, 2 three stage countercurrent rinsing devices, 3 raw water pumps, 4 charging pumps, 5 prefilters, 6 accurate filters, 7 buffer tanks, 8 clean-in-place CIP water tanks, 9 secondary accurate filters, 10 topping-up pumps, 11NF/RO film, accumulator tank 12, former water A, dialyzate B, concentrated solution C.
Embodiment
As Fig. 2, shown in Figure 3, nickel-plating rinsing waste water Online Processing System of the present invention, the relevant device that comprises the rinsing processing that connects the nickel-plating waste water discharge outlet, this nickel-plating rinsing waste water treatment system and nickel plating production line connect and compose looping back of an integral body and are received in the line treatment system, it specifically comprises the following part that is interconnected by pipeline: prefilter 5, accurate filter 6, buffer tank 7, clean-in-place CIP water tank 8, secondary accurate filter 9 and nanofiltration/reverse osmosis (NF/RO) film 11, the corresponding pressurization charging pump that also is provided with in the pipeline, the dialyzate B that handles through nanofiltration/reverse osmosis (NF/RO) film is by the water spot of use of pipeline connection nickel plating production line, and the concentrated solution C that handles through NF/RO film 11 can directly be communicated with the nickel bath 1 of nickel plating production line or pass through accumulator tank 12 and be communicated with the nickel bath 1 of nickel plating production line.The described former water A that enters treatment system also can be provided with three stage countercurrent rinsing devices 2 and connect water-in again; Be provided with charging pump 4 between described buffer tank 7 and the secondary accurate filter 9; Secondary accurate filter 9 and NF/RO film are handled between the pipeline and are provided with topping-up pump 10.Described buffer tank 7 also can be connected with clean-in-place CIP water tank 8 with pipeline between the charging pump 4, can clean whole piping system as required; Also be connected with former water filler pipe road and raw water pump 3 on the described prefilter 5.Its concrete processing technological flow may further comprise the steps:
At first, the workpiece poaching wastewater after the nickel plating is introduced treatment system by pipeline; This poaching wastewater pumps into prefilter through pressurization and carries out prefiltration, bigger granule foreign and absorbed portion organism in the filtering waste water; Waste water with above-mentioned prefiltration carries out fine filtering more again, by accurate filter granule foreign in the water and the component substances of not wanting is further removed, and enters charging pump through buffer tank; Then above-mentioned filtering waste water is pumped into fine filter and carry out the secondary fine filtering again, improve hydraulic pressure by high-pressure pump again,, be divided into the dialysis stillness of night and concentrated solution and recycle respectively again by nanofiltration/reverse osmosis (NF/RO) concentration; Described dialysis clear liquid can be back to three stage countercurrent rinsings and be used for the rinsing processing, and nickel salt and nickel sulfate solution after concentrating can be used for accumulator tank to nickel coating bath or other coating baths.
The present invention adopts nickel plating after the waste water that discharges after the multi-stage countercurrent rinsing is handled as former water, has related parameter to determine by the water-quality guideline of factory's plating shop waste discharge after 3 stage countercurrent rinsings.Specific as follows:
Flooding quantity (tap water quality): 360-400L/H;
Nickel bath steam output (amount of makeup water): 15-20L/H;
Nickel plating post rinsing waste discharge composition: Ni 2+: 353-520mg/L
H 3BO 3:117-173mg/L
PH value: 7.3-7.8
F:0.058%
Fe:0.021%
SiO 2:6.78%
K:1.83%
Na:12.14%
COD:34%
HCO 3 -:0.14g/L
CO 3 2-: less than 0.5mg/L
SO 4 2-:0.37g/L
The mensuration of quality of reused water parameter of the present invention, nickel plating accumulator tank (replenishing back the nickel groove): nickel content 12620-13630mg/L, nickel rinsing quality of reused water: allow to contain Ni 2+Be less than 50mg/L, H 3BO 3Be less than 10mg/L, promptly be about 10% before handling, pH value 5-8.
In the treating processes, nickel plating post rinsing waste water enters filtering system by pipeline, raw water pump supercharging or the mode by gravity flow, and wherein pre-filtered effect mainly is granule foreign and an absorbed portion organism bigger in the filtering water; The effect of secondary filter is that the granule foreign in the water is further removed; Water after the smart filter can enter buffer tank or directly enter filtering system by charging pump, by high-pressure pump feed pressure is brought up to 10 kilograms per centimeter then 2More than, enter nanofiltration/reverse osmosis (NF/RO) system, by the physics chemical action of nanofiltration membrane and reverse osmosis membrane that the material of macromolecule is concentrated, allow the material of moisture and small molecular weight pass through; The effect of NF/RO system is with the Ni in the water 2+Concentrate with sulfate ion, enrichment factor is not less than 40 times, can allow the monovalent metallic ion such as the K of small molecular weight simultaneously +, Na +By.Thereby with the poaching wastewater separated into two parts after the nickel plating, a part is that the nickel sulfate solution after concentrating can be back to the nickel coating bath, and a part is that the reuse water of having removed single nickel salt can be back in the rinsing process; The CIP water tank of simultaneity factor contains the clean-in-place function, can effectively keep the unimpeded of pipeline and avoid microbiological contamination such as bacterium.

Claims (5)

1, a kind of Online Processing System of nickel-plating rinsing waste water, the relevant device that comprises the rinsing processing that the nickel-plating waste water discharge outlet connects, it is characterized in that, this nickel-plating rinsing waste water treatment system and nickel plating production line connect and compose looping back of an integral body and are received in the line treatment system, it specifically comprises the following part that is interconnected by pipeline: prefilter, fine filter, buffer tank, clean-in-place (CIP) water tank, secondary fine filter and nanofiltration/reverse osmosis membrane, the corresponding pressurization charging pump that also is provided with in the pipeline, through the dialyzate of nanofiltration/reverse osmosis membrane processing the water spot of using, be communicated with by the nickel bath of accumulator tank with the nickel plating production line through the concentrated solution of nanofiltration/reverse osmosis membrane processing by pipeline connection nickel plating production line.
2, the Online Processing System of nickel-plating rinsing waste water according to claim 1, it is characterized in that, describedly on the dialyzate pipeline of nanofiltration/reverse osmosis membrane processing, also can connect, form an airtight recycle system with the water-in that the multi-stage countercurrent rinsing device is set.
3, the Online Processing System of nickel-plating rinsing waste water according to claim 2 is characterized in that, described multi-stage countercurrent rinsing device is three grades.
4, the Online Processing System of nickel-plating rinsing waste water according to claim 1 and 2 is characterized in that, is provided with charging pump between described clean-in-place (CIP) water tank and the secondary fine filter; Be provided with topping-up pump between secondary fine filter and nanofiltration/reverse osmosis membrane processing pipeline.
5, the Online Processing System of nickel-plating rinsing waste water according to claim 1 and 2 is characterized in that, also is connected with former water suction culvert and raw water pump on the described prefilter.
CN2008100263548A 2008-02-18 2008-02-18 On-line processing system for nickel-plating rinsing waste water Expired - Fee Related CN101311331B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2008100263548A CN101311331B (en) 2008-02-18 2008-02-18 On-line processing system for nickel-plating rinsing waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2008100263548A CN101311331B (en) 2008-02-18 2008-02-18 On-line processing system for nickel-plating rinsing waste water

Publications (2)

Publication Number Publication Date
CN101311331A true CN101311331A (en) 2008-11-26
CN101311331B CN101311331B (en) 2012-05-02

Family

ID=40100161

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2008100263548A Expired - Fee Related CN101311331B (en) 2008-02-18 2008-02-18 On-line processing system for nickel-plating rinsing waste water

Country Status (1)

Country Link
CN (1) CN101311331B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101875515A (en) * 2009-04-28 2010-11-03 株式会社大宇建设 A kind of water purification apparatus and method
CN106242148A (en) * 2016-08-31 2016-12-21 上海交通大学 The method improving nickel-plating rinsing waste water online resource embrane method closed-system efficiency
CN107445319A (en) * 2017-08-10 2017-12-08 国网河南省电力公司电力科学研究院 A kind of retired composite insulator cleaning sullage processing system and method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0060091A3 (en) * 1981-03-06 1983-06-29 Innova, Inc. Apparatus and method for electrolytically treating an ion containing liquid such as chromium plating rinse water
US4680126A (en) * 1986-02-18 1987-07-14 Frankard James M Separation and recovery of reusable heavy metal hydroxides from metal finishing wastewaters
CN100386475C (en) * 2005-10-17 2008-05-07 海宁市海整整流器有限公司 Water comprehensive utilization technology for cleaning electroplating nickel
CN2903097Y (en) * 2005-12-13 2007-05-23 上海瑞勇实业有限公司 Electroplating rinsing water on line recovering equipment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101875515A (en) * 2009-04-28 2010-11-03 株式会社大宇建设 A kind of water purification apparatus and method
CN106242148A (en) * 2016-08-31 2016-12-21 上海交通大学 The method improving nickel-plating rinsing waste water online resource embrane method closed-system efficiency
CN107445319A (en) * 2017-08-10 2017-12-08 国网河南省电力公司电力科学研究院 A kind of retired composite insulator cleaning sullage processing system and method

Also Published As

Publication number Publication date
CN101311331B (en) 2012-05-02

Similar Documents

Publication Publication Date Title
CN104787938B (en) It is a kind of effectively to remove the electrolyzed water machines of removing heavy metals
CN100513334C (en) Deep treatment process of metallurgical sewage
CN107840511A (en) Coal chemical industry method for treating strong brine and system
CN111285531A (en) Method and system for concentrating high-salinity mine water
CN102627364A (en) Process flow for recycling and treating reverse osmosis concentrated water
CN103539295A (en) Method and device for deeply treating heavy metal wastewater
CN201427903Y (en) Nickel electroplating rinse water cleaning system
CN205838739U (en) A kind of fluorine-contained wastewater treatment system
CN101863570B (en) Heavy metal-containing wastewater treatment and reuse method and device
CN201610402U (en) Recycling and deep treatment device for electronic electroplating wastewater
CN101311331B (en) On-line processing system for nickel-plating rinsing waste water
CN205347081U (en) Cyanogen chemical plating cadmium waste water zero release processing system
CN202279743U (en) On-line purifying device for EDRO
CN212640193U (en) High-low salt wastewater separation system
CN100522826C (en) Water treatment method capable of reusing concentrated water wholly
CN208762364U (en) Dyeing waste water advanced treatment system
CN106746130A (en) A kind of high-salt concentrated water zero-discharge treatment system and process
CN208561983U (en) A kind of heavy metal waste water treatment system
CN204454775U (en) A kind of trivalent chromium passivation Wastewater zero-discharge treatment system
CN201395536Y (en) Electroplating comprehensive cleaning wastewater treatment and recovery system
CN207685046U (en) Sewage treatment equipment with tubular membrane filter device
CN2910907Y (en) Water treatment equipment able to recover total concentration water
CN215906017U (en) Silver cyanide wastewater treatment system
CN213295051U (en) Contain salt waste water resourceful treatment device
CN106145457A (en) A kind of waste water resource recycles processing method entirely

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
ASS Succession or assignment of patent right

Owner name: GUANGDONG REAL FAITH LIGHTING CO., LTD.

Free format text: FORMER OWNER: FOSHAN ZHAOXIN METAL PRODUCTS CO., LTD.

Effective date: 20121224

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 528100 FOSHAN, GUANGDONG PROVINCE TO: 528200 FOSHAN, GUANGDONG PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20121224

Address after: One of the 528200 Guangdong Province Nanhai District of Foshan city Guicheng street, No. 1 Yongan Road, valley optoelectronics industry community A block sixth layer

Patentee after: Guangdong Real Faith Lighting Co., Ltd.

Address before: 528100 Guangdong city of Foshan province Baini town Sanshui District West Kau large sand

Patentee before: Foshan Zhaoxin Metal Products Co., Ltd.

C56 Change in the name or address of the patentee

Owner name: GUANGDONG REAL FAITH LIGHTING TECHNOLOGY CO., LTD.

Free format text: FORMER NAME: GUANGDONG REAL FAITH LIGHTING CO., LTD.

CP03 Change of name, title or address

Address after: One of the 528251 Guangdong Province Nanhai District of Foshan city Guicheng street, No. 1 Yongan Road, valley optoelectronics industry community A block sixth layer

Patentee after: GUANGDONG REAL FAITH LIGHTING TECHNOLOGY CO., LTD.

Address before: One of the 528200 Guangdong Province Nanhai District of Foshan city Guicheng street, No. 1 Yongan Road, valley optoelectronics industry community A block sixth layer

Patentee before: Guangdong Real Faith Lighting Co., Ltd.

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

Granted publication date: 20120502

Termination date: 20180218

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