CN110016660A - A kind of galvanizing inactivating liquid generating apparatus again - Google Patents
A kind of galvanizing inactivating liquid generating apparatus again Download PDFInfo
- Publication number
- CN110016660A CN110016660A CN201910462957.0A CN201910462957A CN110016660A CN 110016660 A CN110016660 A CN 110016660A CN 201910462957 A CN201910462957 A CN 201910462957A CN 110016660 A CN110016660 A CN 110016660A
- Authority
- CN
- China
- Prior art keywords
- regulating tank
- value
- liquid
- water pump
- ion
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 48
- 238000005246 galvanizing Methods 0.000 title claims abstract description 14
- 230000000415 inactivating effect Effects 0.000 title claims abstract description 14
- 230000001105 regulatory effect Effects 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 230000009849 deactivation Effects 0.000 claims abstract description 24
- 239000000523 sample Substances 0.000 claims abstract description 13
- 238000002161 passivation Methods 0.000 claims abstract description 4
- 238000004140 cleaning Methods 0.000 claims description 8
- 239000006210 lotion Substances 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 6
- 238000005342 ion exchange Methods 0.000 claims description 4
- 230000003139 buffering effect Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000243 solution Substances 0.000 description 29
- 238000006243 chemical reaction Methods 0.000 description 12
- 150000002500 ions Chemical class 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/04—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the coating material
- C23C2/06—Zinc or cadmium or alloys based thereon
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/26—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/86—Regeneration of coating baths
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The invention discloses a kind of galvanizing inactivating liquid generating apparatus again, including ion-exchanger and PH regulating tank, the liquid inlet of ion-exchanger is connected to deactivation slot liquid outlet, liquid outlet is connected to PH regulating tank, PH regulating tank is also equipped with the container of pH value adjustment liquid by water pump connection, pH value probe is provided in PH regulating tank, pH value adjustment controller is provided with outside PH regulating tank, the signal input part of pH value adjustment controller connects PH probe, the control signal output of pH value adjustment controller connects water pump on off controller, water pump on off controller connects water pump, the liquid outlet of the PH regulating tank is also connected to deactivation slot liquid inlet.The foreign ion removal of passivating solution can be achieved in the present invention, reduces passivating solution discharge, the on-line automatic pH value for adjusting processing post-passivation liquid, without manually adjusting, treated, and passivating solution be can be used directly, and not affected the normal production.
Description
Technical field
The present invention relates to passivating solution foreign ion processing technology fields, and in particular to a kind of galvanizing inactivating liquid generating apparatus again.
Background technique
In galvanizing inactivating liquid, is increased for a long time using Zn2+ the and Fe2+ impurity that can make in tank liquor, influence the anti-corrosion of product
Performance, so needing the metal impurities ion in periodically effective removal passivating solution.Common practice be precentagewise replacement or
Person all replaces passivating solution, it is serious to cause passivating solution waste in this way, while increasing sewage treatment expense, cost is also high.Portion
Although point enterprise leads to treatment effeciency occur because pH value changes rapid problem using simple ion-exchange treatment
Lowly, it the situation that influences normally produce such as can not handle in time.
Summary of the invention
Based on the deficiencies of the prior art, the present invention provides a kind of galvanizing inactivating liquid generating apparatus again, in process of production
Passivating solution carry out foreign ion exchange, while promoting passivating solution treatment effeciency, reduce the discharge of passivating solution, reduce passivating solution
Cost and cost of sewage disposal.
The technical solution of the present invention is as follows:
A kind of galvanizing inactivating liquid generating apparatus again, it is characterised in that: including ion-exchanger and PH regulating tank, the ion is handed over
The liquid inlet of parallel operation is connected to deactivation slot liquid outlet, and liquid outlet is connected to PH regulating tank, and the PH regulating tank is also connected by water pump
The logical container equipped with pH value adjustment liquid, wherein be provided with pH value probe in the PH regulating tank, pH value is provided with outside PH regulating tank
The signal input part of adjusting controller, pH value adjustment controller connects the PH probe, the control signal of pH value adjustment controller
Output end connects water pump on off controller, and water pump on off controller connects water pump, and the pH value adjustment controller is for working as pH value
The exceeded backward water pump on off controller of the pH value of probe collection issues the signal of starting water pump, and the Xiang Shui after pH value complies with standard
Pump on off controller issues the signal to switch off the pump, and the liquid outlet of such loop control, the PH regulating tank also enters with deactivation slot
The connection of liquid mouth passes through deactivation slot liquid inlet circulation by the solution that the purification of PH regulating tank regulates pH value again and flows into deactivation slot.
Further, the PH regulating tank is also communicated with dashpot, and the purification of PH regulating tank is regulated PH by dashpot
The solution of value is flowed into deactivation slot by dashpot liquid outlet circulation.
Further, on the connecting pipe of the deactivation slot and the ion-exchanger, the ion-exchanger with it is described
On the connecting pipe of PH regulating tank, flow control valve is provided on the connecting pipe of the dashpot and the deactivation slot.
Further, the ion-exchanger is also respectively communicated with the washing lotion bucket for holding ion-exchanger cleaning solution and holds
The pure water cylinder of pure water.
Further, the connecting pipe of the ion-exchanger and washing lotion bucket and pure water cylinder is respectively arranged with flow adjusting
Valve.
The invention has the benefit that the foreign ion removal of passivating solution can be realized, passivating solution discharge is reduced, it is on-line automatic
The pH value of processing post-passivation liquid is adjusted, without manually adjusting, treated, and passivating solution be can be used directly, and not affected the normal production.
Detailed description of the invention
Fig. 1 is structural block diagram of the invention.
Specific embodiment
Below with reference to the accompanying drawings and in conjunction with the embodiments the present invention is described in detail.It should be noted that in the feelings not conflicted
Under condition, the feature in following embodiment and embodiment can be combined with each other.
As shown in Figure 1, a kind of galvanizing inactivating liquid generating apparatus, including ion-exchanger and PH regulating tank again, the ion is handed over
The liquid inlet of parallel operation is connected to deactivation slot liquid outlet, and liquid outlet is connected to PH regulating tank, and the PH regulating tank is also connected by water pump
The logical container equipped with pH value adjustment liquid, wherein be provided with pH value probe in the PH regulating tank, pH value is provided with outside PH regulating tank
The signal input part of adjusting controller, pH value adjustment controller connects the PH probe, the control signal of pH value adjustment controller
Output end connects water pump on off controller, and water pump on off controller connects water pump, and the pH value adjustment controller is for working as pH value
The exceeded backward water pump on off controller of the pH value of probe collection issues the signal of starting water pump, and the Xiang Shui after pH value complies with standard
Pump on off controller issues the signal to switch off the pump, and the liquid outlet of such loop control, the PH regulating tank also enters with deactivation slot
The connection of liquid mouth passes through deactivation slot liquid inlet circulation by the solution that the purification of PH regulating tank regulates pH value again and flows into deactivation slot.
Wherein, the shell of pH value adjustment controller is mounted on outside PH regulating tank, and control circuit board is provided in shell, control
Control chip is provided on circuit board, if select control chip without AD conversion or D/A conversion module, by pH value probe
The PH analog electrical signal of output is transferred to after AD conversion module is AD converted, with the preset PH stored in control chip
Value is compared, when the pH value of pH value probe collection is bigger than preset value, the control signal of control chip output starting water pump
To the D/A conversion module, control digital signal is converted into control analog electrical signal feed pump on off controller, and in pH value
The signal to switch off the pump is issued after complying with standard to water pump on off controller, relay can be used in water pump on off controller, connects
The settable fracture of the power supply of water pump, the movable contact of one end connection relay of fracture, the output end of D/A conversion module connect relay
The coil of device, and obtain electric late contact in coil and be attracted, the both ends of supply lines fracture are connected to by movable contact, and water pump is opened in realization
Open control.Certainly, it is contemplated that the signal exported from D/A conversion module is minimum, can amplify in the output connection signal of D/A conversion module
Device, the coil after signal amplifier amplifies again with relay are connect.If, can also be in the lesser situation of received pH value
In the front end matched signal amplifier of AD conversion module, if the control chip used carries AD conversion and DA conversion function, then
AD conversion module and D/A conversion module can be omitted.
Since the solution in deactivation slot is in acidity, and wherein most foreign ion is Zn2+And Zn2+Ion, by from
Sub- exchanger removes major part Zn therein2+And Zn2+Ion carries out contamination precipitation by precipitating reagent, flows from ion-exchanger
The solution entered in PH regulating tank has had been removed Zn substantially2+And Zn2+Equal foreign ions, ion-exchanger can be used on the market often
Ion-exchanger.
Holding in the container of water pump connection is the alkaline solutions such as sodium hydroxide.
The PH regulating tank is also communicated with dashpot, is led to the solution that the purification of PH regulating tank regulates pH value by dashpot
Dashpot liquid outlet circulation is crossed to flow into deactivation slot.Dashpot can be such that the passivating solution after adjusting pH value more fully stirs
It is even, influence of the passivating solution to deactivation slot that be further reduced that treated.
On the connecting pipe of the deactivation slot and the ion-exchanger, the ion-exchanger and the PH regulating tank
On connecting pipe, flow control valve is provided on the connecting pipe of the dashpot and the deactivation slot.It is adjusted by flow
The flow of valve regulation liquid, or when needing thorough drain or cleaning corresponding groove body, flow control valve can be closed.
The ion-exchanger is also respectively communicated with the washing lotion bucket for holding ion-exchanger cleaning solution and holds the pure of pure water
Bucket.The connecting pipe of ion-exchanger and washing lotion bucket and pure water cylinder is respectively arranged with flow control valve.When ion-exchanger needs
When cleaning, cleaning solution and water can be evacuated to respectively by water pump after being cleaned in ion-exchanger and be discharged, wherein cleaning solution
Hydrochloric acid can be selected because passivating solution be it is acid, cleaning solution also must be it is acid, the cost of hydrochloric acid is low and liquid waste processing
It is easy.
Generating apparatus, the foreign ion for realizing passivating solution remove the galvanizing inactivating liquid of the present embodiment again, reduce passivating solution
Discharge, the on-line automatic pH value for adjusting processing post-passivation liquid, without manually adjusting, treated, and passivating solution be can be used directly, no
Influence normal production.
Embodiment belonging to above only expresses concentration embodiment of the invention, and the description thereof is more specific and detailed, but simultaneously
Limitations on the scope of the patent of the present invention therefore cannot be interpreted as, it is noted that for those of ordinary skill in the art
For, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to guarantor of the invention
Protect range.Therefore the scope of protection of the patent of the invention shall be subject to the appended claims.
Claims (5)
1. a kind of galvanizing inactivating liquid generating apparatus again, it is characterised in that: including ion-exchanger and PH regulating tank, the ion exchange
The liquid inlet of device is connected to deactivation slot liquid outlet, and liquid outlet is connected to PH regulating tank, and the PH regulating tank is also connected to by water pump
Container equipped with pH value adjustment liquid, wherein be provided with pH value probe in the PH regulating tank, pH value tune is provided with outside PH regulating tank
Controller is saved, the signal input part of pH value adjustment controller connects the PH probe, and the control signal of pH value adjustment controller is defeated
Outlet connects water pump on off controller, and water pump on off controller connects water pump, and the pH value adjustment controller is used for according to pH value
The exceeded backward water pump on off controller of the pH value of probe collection issues the signal of starting water pump, and the Xiang Shui after pH value complies with standard
Pump on off controller issues the signal to switch off the pump, and the liquid outlet of such loop control, the PH regulating tank also enters with deactivation slot
The connection of liquid mouth passes through deactivation slot liquid inlet circulation by the solution that the purification of PH regulating tank regulates pH value again and flows into deactivation slot.
2. galvanizing inactivating liquid as described in claim 1 generating apparatus again, it is characterised in that: the PH regulating tank is also communicated with buffering
Slot is flowed into the solution that the purification of PH regulating tank regulates pH value in deactivation slot by dashpot liquid outlet circulation by dashpot.
3. galvanizing inactivating liquid as described in claim 1 generating apparatus again, it is characterised in that: the deactivation slot and the ion exchange
On the connecting pipe of device, on the connecting pipe of the ion-exchanger and the PH regulating tank, the dashpot and the passivation
Flow control valve is provided on the connecting pipe of slot.
4. galvanizing inactivating liquid as described in claim 1 generating apparatus again, it is characterised in that: the ion-exchanger is also respectively communicated with
There is the washing lotion bucket for holding ion-exchanger cleaning solution and holds the pure water cylinder of pure water.
5. galvanizing inactivating liquid as claimed in claim 3 generating apparatus again, it is characterised in that: ion-exchanger and washing lotion bucket and pure water
Flow control valve is respectively arranged in the connecting pipe of bucket.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2019102528221 | 2019-03-29 | ||
CN201910252822.1A CN109797386A (en) | 2019-03-29 | 2019-03-29 | A kind of galvanizing inactivating liquid generating apparatus again |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110016660A true CN110016660A (en) | 2019-07-16 |
CN110016660B CN110016660B (en) | 2023-11-24 |
Family
ID=66564377
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910252822.1A Withdrawn CN109797386A (en) | 2019-03-29 | 2019-03-29 | A kind of galvanizing inactivating liquid generating apparatus again |
CN201910462957.0A Active CN110016660B (en) | 2019-03-29 | 2019-05-30 | Zinc-plating passivation solution regeneration facility |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910252822.1A Withdrawn CN109797386A (en) | 2019-03-29 | 2019-03-29 | A kind of galvanizing inactivating liquid generating apparatus again |
Country Status (1)
Country | Link |
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CN (2) | CN109797386A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112813429A (en) * | 2020-12-30 | 2021-05-18 | 苏州碧清源环保技术有限公司 | Passivating agent regeneration and reuse equipment and method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3973987A (en) * | 1974-03-18 | 1976-08-10 | Data General Corporation | Water recycle treatment system for use in metal processing |
FR2721326A1 (en) * | 1994-06-20 | 1995-12-22 | Yves Bardin | Continuous regeneration of surface treatment bath for passivation of metal components |
CN2927144Y (en) * | 2006-06-06 | 2007-07-25 | 杜文蔚 | pH-value automatic controlling system |
CN207537571U (en) * | 2017-11-28 | 2018-06-26 | 江门市高信科技有限公司 | A kind of passivator de-burring machine |
CN210314487U (en) * | 2019-03-29 | 2020-04-14 | 珠海市玛斯特五金塑胶制品有限公司 | Regeneration equipment for galvanized passivation solution |
-
2019
- 2019-03-29 CN CN201910252822.1A patent/CN109797386A/en not_active Withdrawn
- 2019-05-30 CN CN201910462957.0A patent/CN110016660B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3973987A (en) * | 1974-03-18 | 1976-08-10 | Data General Corporation | Water recycle treatment system for use in metal processing |
FR2721326A1 (en) * | 1994-06-20 | 1995-12-22 | Yves Bardin | Continuous regeneration of surface treatment bath for passivation of metal components |
CN2927144Y (en) * | 2006-06-06 | 2007-07-25 | 杜文蔚 | pH-value automatic controlling system |
CN207537571U (en) * | 2017-11-28 | 2018-06-26 | 江门市高信科技有限公司 | A kind of passivator de-burring machine |
CN210314487U (en) * | 2019-03-29 | 2020-04-14 | 珠海市玛斯特五金塑胶制品有限公司 | Regeneration equipment for galvanized passivation solution |
Also Published As
Publication number | Publication date |
---|---|
CN110016660B (en) | 2023-11-24 |
CN109797386A (en) | 2019-05-24 |
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