CN102285704B - Ion exchange resin arsenic removal method for acidic etching liquid, resin regeneration method and treatment system thereof - Google Patents
Ion exchange resin arsenic removal method for acidic etching liquid, resin regeneration method and treatment system thereof Download PDFInfo
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- CN102285704B CN102285704B CN 201010242923 CN201010242923A CN102285704B CN 102285704 B CN102285704 B CN 102285704B CN 201010242923 CN201010242923 CN 201010242923 CN 201010242923 A CN201010242923 A CN 201010242923A CN 102285704 B CN102285704 B CN 102285704B
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Abstract
The invention relates to an ion exchange resin arsenic removal method for acidic etching liquid, which comprises the steps of: A) placing extraction resin in an ion exchanger; B) pumping acidic etching liquid waste into the ion exchanger, controlling the flow rate of the acidic etching liquid waste in the ion exchanger and then letting the acidic etching liquid waste flow out of the ion exchanger to obtain arsenic-removed printed circuit board acidic etching liquid waste; and C) when the adsorbing capacity of the extraction resin is saturated, conducting regeneration treatment to the extraction resin, and after the treatment is completed, using the extraction resin to continuously treat the acidic etching liquid waste; and when the removal rate of arsenic in the acidic etching liquid waste after the arsenic is removed through the ion exchanger is lower than 60 percent, replacing the extraction resin, emptying the ion exchanger at the moment and repeating the step A. Since the resin used by the ion exchange resin arsenic removal method is the extraction resin, the extraction resin is simple to regenerate, the operation is convenient, the cost is low and the ion exchange resin arsenic removal method is suitable for the arsenic removal of large-scale printed circuit board acidic etching liquid waste.
Description
[technical field]
The present invention relates to remove in the waste water multiple-stage treatment of specific solute, particularly waste printed circuit board etching liquid is removed the method for arsenic, relates in particular to the ion exchange resin dearsenicating method for the production of the printed circuit board acidic etching waste liquor of basic copper chloride; The invention still further relates to the method for resin regeneration in the ion exchange resin arsenic removal process of printed circuit board acidic etching waste liquor, and the treatment system of arsenic removal and resin regeneration.
[background technology]
Waste printed circuit board etching liquid (also claiming the PCB etching waste liquor) comprises alkaline etching waste liquid for producing and acidic etching waste liquid, and wherein copper and chloride ion content height in the printed circuit board acidic etching waste liquor belong to acidity, contain impurity such as arsenic; The basic copper chloride of being produced by printed circuit board acidic etching waste liquor has strict demand to the content of arsenic, arsenic content is more low more good, generally before producing basic copper chloride with printed circuit board acidic etching waste liquor, need carry out the processing in early stage of arsenic removal to printed circuit board acidic etching waste liquor.
Prior art method of arsenic removal from printed circuit board acidic etching waste liquor comprises neutralization precipitation method, sulphide precipitation, the ferrite precipitator method and flocculent precipitation, and the effect of removing arsenic that these methods have is bad, and the meeting that has causes secondary pollution, and the cost that has is higher; The method of prior art arsenic removal from printed circuit board acidic etching waste liquor also comprises ion-exchange resin, this method treatment capacity is big, simple to operate and good separating effect, be conducive to the recycling of various materials in the acidic etching waste liquid, it is a kind of good dearsenicating method, but the used resin of this method comprises the gac exchange resin, the regenerating resin of sulfide, mineral ion exchange resin and selective chelating resin, after the acidic etching waste liquid arsenic removal is handled, these resin regenerations are difficulty, and the resin regeneration processing cost is higher, the cost that causes adopting ion-exchange resin to handle arsenic removal in the printed circuit board acidic etching waste liquor increases, and the popularization of this ion exchange resin dearsenicating method also is restricted.
[summary of the invention]
The technical problem to be solved in the present invention is to avoid above-mentioned the deficiencies in the prior art part and proposes a kind of ion exchange resin dearsenicating method for acidic etching waste liquid, the resin of this ion exchange resin dearsenicating method adopts extration resin 941 types, this extration resin 941 types regeneration is simple, easy to operate and cost is lower, is fit to the arsenic removal of printed circuit board acidic etching waste liquor in enormous quantities is handled.The invention allows for the method for the used ion exchange resin regeneration of a kind of acidic etching liquid arsenic removal.The present invention has also proposed a kind of ion exchange resin arsenic removal treatment system for acidic etching liquid.
The technical scheme that the present invention solve the technical problem employing is:
A kind of ion exchange resin dearsenicating method for acidic etching liquid is for the treating processes in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprises the steps:
A, fresh extration resin 941 types are packed in the ion-exchanger;
B, pending printed circuit board acidic etching waste liquor pumped into from the entrance of described ion-exchanger carry out arsenic removal in this ion-exchanger and handle, control the velocity of flow of described acidic etching waste liquid in described ion-exchanger, being allowed to condition at the time of flowing in this ion-exchanger remained on 20～40 minutes, flow out from the outlet of described ion-exchanger then, obtain the printed circuit board acidic etching waste liquor after the arsenic removal;
When the volume of C, the acidic etching waste liquid handled when described extration resin 941 types is 390～410 times of volume of these extration resin 941 types, the adsorptive power of these extration resin 941 types reaches capacity, then described extration resin 941 types need carry out manipulation of regeneration, and its steps in sequence is as follows:
C
1The entrance of hydrochloric acid from described ion-exchanger pumped in this ion-exchanger, make this hydrochloric acid by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
2After described hydrochloric acid has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
3After described tap water has cleaned described extration resin 941 types, the entrance of sodium hydroxide solution from described ion-exchanger pumped in this ion-exchanger, make this sodium hydroxide solution by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
4After described sodium hydroxide solution has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger again, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
Through above C
1～C
4Each step, described extration resin 941 type manipulation of regeneration finish, and available its continues to handle printed circuit board acidic etching waste liquor;
Repeating step B, after extremely the adsorptive power of described extration resin 941 types reaches capacity, operation steps C again, and then alternately repeating step B, C, acidic etching waste liquid after handling through described ion-exchanger arsenic removal, after the clearance of arsenic was lower than 60%, described extration resin 941 types needed to change, should empty described ion-exchanger this moment, repeats implementation step A.
The invention allows for the method for the used ion exchange resin regeneration of a kind of acidic etching liquid arsenic removal, used resin is extration resin 941 types, when the volume of the acidic etching waste liquid of handling when described extration resin 941 types is 390～410 times of volume of these extration resin 941 types, the adsorptive power of these extration resin 941 types reaches capacity, then described extration resin 941 types need carry out manipulation of regeneration, comprise the steps: according to this
C
1The entrance of hydrochloric acid from described ion-exchanger pumped in this ion-exchanger, make this hydrochloric acid by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
2After described hydrochloric acid has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
3After described tap water has cleaned described extration resin 941 types, the entrance of sodium hydroxide solution from described ion-exchanger pumped in this ion-exchanger, make this sodium hydroxide solution by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
4After described sodium hydroxide solution has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger again, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
Through above C
1～C
4Each step, described extration resin 941 type manipulation of regeneration finish, and can be reused for the processing printed circuit board acidic etching waste liquor.
Above-mentioned steps C
1In, the concentration of described hydrochloric acid is 7～10%, and the consumption of this hydrochloric acid is 1.5～2.5 times of described extration resin 941 type volumes, and this hydrochloric acid is 1.5～2.5 hours by the time of described ion-exchanger.
Above-mentioned steps C
2In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.
Above-mentioned steps C
3In, the concentration of described sodium hydroxide solution is 7～10%, and the consumption of this sodium hydroxide is 1.5～2.5 times of described extration resin 941 type volumes, and this sodium hydroxide is 1.5～2.5 hours by the time of described ion-exchanger.
Above-mentioned steps C
4In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.
The present invention has proposed a kind of ion exchange resin arsenic removal treatment system for acidic etching liquid again, be for the treatment system in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprise ion-exchanger and liquid absorbing pump that resin is housed, and be arranged on the entrance of described ion-exchanger and the feed valve between the drawing liquid pump outlet; Described liquid absorbing pump pumps into pending acidic etching liquid and carries out arsenic removal in this ion-exchanger and handle from the entrance of described ion-exchanger, the acidic etching liquid after arsenic removal is handled flows out through bleeder valve from the outlet of described ion-exchanger.
Described resin is extration resin 941 types; Described ion exchange resin arsenic removal treatment system also comprises the extration resin regenerating unit, and this extration resin regenerating unit comprises the hydrochloric acid pond, takes out the hydrochloric acid pump, hydrochloric acid feed valve, hydrochloric acid pond for recovering, hydrochloric acid bleeder valve, sodium hydroxide pond, take out hydroxide sodium pump, sodium hydroxide feed valve, sodium hydroxide pond for recovering, sodium hydroxide bleeder valve, tap water feed valve, tap water pond for recovering and tap water bleeder valve.
The outlet in described hydrochloric acid pond is connected with the entrance of described ion-exchanger after taking out hydrochloric acid pump and hydrochloric acid feed valve through described, the outlet of described ion-exchanger is connected with the entrance of described hydrochloric acid pond for recovering behind described hydrochloric acid bleeder valve, the described hydrochloric acid pump of taking out pumps into described ion-exchanger with the hydrochloric acid in the described hydrochloric acid pond and flows through behind described extration resin 941 types, from the outlet of described ion-exchanger in described hydrochloric acid bleeder valve flow into described hydrochloric acid pond for recovering.
The outlet in described sodium hydroxide pond is connected with the entrance of described ion-exchanger after taking out hydroxide sodium pump and sodium hydroxide feed valve through described, the outlet of described ion-exchanger is connected with the entrance of described sodium hydroxide pond for recovering behind described sodium hydroxide bleeder valve, the described hydroxide sodium pump of taking out pumps into described ion-exchanger with the sodium hydroxide solution in the described sodium hydroxide pond and flows through behind described extration resin 941 types, from the outlet of described ion-exchanger in described sodium hydroxide bleeder valve flow into described sodium hydroxide pond for recovering.
Described tap water feed valve is arranged on the entrance of described ion-exchanger and from the beginning between the water source, the outlet of described ion-exchanger is connected with the entrance of described tap water pond for recovering behind described tap water bleeder valve, after described tap water flows into extration resin 941 types of described ion-exchanger through described tap water feed valve, from the outlet of described ion-exchanger in described tap water bleeder valve flow into described tap water pond for recovering.
Compare with prior art, ion exchange resin dearsenicating method, the method for resin regeneration and the beneficial effect for the treatment of system thereof that the present invention is used for acidic etching liquid are:
1, the required material of arsenic removal adopts extration resin 941 types, and this extration resin 941 types regeneration is simple, easy to operate and cost is lower, is fit to the arsenic removal of printed circuit board acidic etching waste liquor in enormous quantities is handled;
2, whole arsenic removal operating process is simple, and good separating effect is easy to control, is conducive to keep the various valuable components in the acidic etching waste liquid;
3, hydrochloric acid and the sodium hydroxide solution cost for extration resin 941 type manipulation of regeneration is low;
4, arsenic removal treatment system is cleaned easily, and cost is low.
[description of drawings]
Fig. 1 is the rough schematic view that the present invention is used for the ion exchange resin arsenic removal treatment system of acidic etching liquid.
[embodiment]
Below in conjunction with each accompanying drawing the present invention is described in further detail.
A kind of ion exchange resin dearsenicating method for acidic etching liquid is for the treating processes in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprises the steps:
A, fresh extration resin 941 types are packed in the ion-exchanger, the chemical name classification of this extration resin is strongly acidic styrene type cation exchange resin;
B, referring to Fig. 1, pending printed circuit board acidic etching waste liquor pumped into from the entrance of described ion-exchanger carry out arsenic removal in this ion-exchanger and handle, control the velocity of flow of described acidic etching waste liquid in described ion-exchanger, being allowed to condition at the time of flowing in this ion-exchanger remained on 20～40 minutes, flow out from the outlet of described ion-exchanger then, obtain the printed circuit board acidic etching waste liquor after the arsenic removal; Flow when the feed valve 30 among Fig. 1 can be controlled described acidic etching waste liquid and pumps into, just can control the velocity of flow of described acidic etching waste liquid in described ion-exchanger, usually described acidic etching waste liquid mobile time in described ion-exchanger remained on 30 minutes;
When the volume of C, the acidic etching waste liquid handled when described extration resin 941 types is 390～410 times of volume of these extration resin 941 types, the adsorptive power of these extration resin 941 types reaches capacity, then described extration resin 941 types need carry out manipulation of regeneration, and its steps in sequence is as follows:
C
1Referring to Fig. 1, the entrance of hydrochloric acid from described ion-exchanger pumped in this ion-exchanger, make this hydrochloric acid by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger; Washing with hydrochloric acid mainly is that impurity such as the arsenic that will stay described extration resin 941 type surfaces, copper rinse out; Flow when the flow when the hydrochloric acid feed valve 43 among Fig. 1 can be controlled hydrochloric acid and pumps into, hydrochloric acid bleeder valve 45 then can be controlled hydrochloric acid and flow out;
C
2After described hydrochloric acid has washed described extration resin 941 types, referring to Fig. 1, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger; Washing with tap water mainly is further described extration resin 941 types to be rinsed well; Flow when the flow when the tap water feed valve 51 among Fig. 1 can be controlled the tap water inflow, tap water bleeder valve 53 then can be controlled the tap water outflow;
C
3After described tap water has cleaned described extration resin 941 types, referring to Fig. 1, the entrance of sodium hydroxide solution from described ion-exchanger pumped in this ion-exchanger, make this sodium hydroxide solution by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger; Washing with sodium hydroxide solution mainly is to stay the hydrochloric acid neutralization on described extration resin 941 type surfaces, makes described extration resin 941 types be neutral; Flow when the flow when the sodium hydroxide feed valve 48 among Fig. 1 can be controlled sodium hydroxide solution and pumps into, sodium hydroxide bleeder valve 50 then can be controlled sodium hydroxide solution and flow out;
C
4After described sodium hydroxide solution has washed described extration resin 941 types, referring to Fig. 1, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger again, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger; Washing with tap water again mainly is further described extration resin 941 types to be rinsed well; Flow when the flow when the tap water feed valve 51 among Fig. 1 can be controlled the tap water inflow, tap water bleeder valve 53 then can be controlled the tap water outflow;
Through above C
1～C
4Each step, described extration resin 941 type manipulation of regeneration finish, and available its continues to handle printed circuit board acidic etching waste liquor;
Repeating step B, after the adsorptive power of described extration resin 941 types reaches capacity, operation steps C again, and then alternately repeating step B, C, acidic etching waste liquid after handling through described ion-exchanger arsenic removal, after the clearance of arsenic was lower than 60%, described extration resin 941 types needed to change, should empty described ion-exchanger this moment, repeats implementation step A.Experience according to the applicant's long-term disposal, when the volume of the acidic etching waste liquid of handling when described extration resin 941 types is 1900～2100 times of volume of these extration resin 941 types, this moment the acidic etching waste liquid after described ion-exchanger arsenic removal is handled, the clearance of arsenic generally can be lower than 60%, just needs to have changed extration resin 941 types.
Above-mentioned steps C
1In, the concentration of described hydrochloric acid is 7～10%, and the consumption of this hydrochloric acid is 1.5～2.5 times of described extration resin 941 type volumes, and this hydrochloric acid is 1.5～2.5 hours by the time of described ion-exchanger.As the concentration that adopts hydrochloric acid is 8%, and the consumption of hydrochloric acid is 2 times of described extration resin 941 type volumes, and hydrochloric acid is 2 hours by the time of described ion-exchanger.
Above-mentioned steps C
2In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.As described in as the consumption of tap water being 2 times of extration resin 941 type volumes, tap water is 30 minutes by the time of described ion-exchanger.
Above-mentioned steps C
3In, the concentration of described sodium hydroxide solution is 7～10%, and the consumption of this sodium hydroxide is 1.5～2.5 times of described extration resin 941 type volumes, and this sodium hydroxide is 1.5～2.5 hours by the time of described ion-exchanger.As the concentration that adopts sodium hydroxide solution is 8%, and the consumption of sodium hydroxide is 2 times of described extration resin 941 type volumes, and sodium hydroxide is 2 hours by the time of described ion-exchanger.
Above-mentioned steps C
4In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.As described in as the consumption of tap water being 2 times of extration resin 941 type volumes, tap water is 30 minutes by the time of described ion-exchanger.
Referring to Fig. 1, a kind of ion exchange resin arsenic removal treatment system for acidic etching liquid, be for the treatment system in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprise ion-exchanger 10 and liquid absorbing pump 20 that resin is housed, and be arranged on the feed valve 30 between the outlet of the entrance 11 of described ion-exchanger 10 and liquid absorbing pump 20; Described liquid absorbing pump 20 pumps into the pending acidic etching liquid in the treating pond and carries out arsenic removal in this ion-exchanger 10 and handle from the entrance 11 of described ion-exchanger 10, the acidic etching liquid after arsenic removal is handled is from outlet 12 pond in the middle of bleeder valve 31 flows out to of described ion-exchanger 10; Described resin is extration resin 941 types, and the chemical name classification of this extration resin is strongly acidic styrene type cation exchange resin; Described arsenic removal treatment system also comprises the extration resin regenerating unit, and this extration resin regenerating unit comprises hydrochloric acid pond 41, takes out hydrochloric acid pump 42, hydrochloric acid feed valve 43, hydrochloric acid pond for recovering 44, hydrochloric acid bleeder valve 45, sodium hydroxide pond 46, take out hydroxide sodium pump 47, sodium hydroxide feed valve 48, sodium hydroxide pond for recovering 49, sodium hydroxide bleeder valve 50, tap water feed valve 51, tap water pond for recovering 52 and tap water bleeder valve 53.
The outlet in described hydrochloric acid pond 41 is connected with the entrance 11 of described ion-exchanger 10 after taking out hydrochloric acid pump 42 and hydrochloric acid feed valve 43 through described, the outlet 12 of described ion-exchanger 10 is connected with the entrance of described hydrochloric acid pond for recovering 44 behind described hydrochloric acid bleeder valve 45, the described hydrochloric acid pump 42 of taking out pumps into described ion-exchanger 10 with the hydrochloric acid in the described hydrochloric acid pond 41 and flows through behind described extration resin 941 types, from the outlet 12 of described ion-exchanger 10 in described hydrochloric acid bleeder valve 45 flow into described hydrochloric acid pond for recovering 44.
The outlet in described sodium hydroxide pond 46 is connected with the entrance 11 of described ion-exchanger 10 after taking out hydroxide sodium pump 47 and sodium hydroxide feed valve 48 through described, the outlet 12 of described ion-exchanger 10 is connected with the entrance of described sodium hydroxide pond for recovering 49 behind described sodium hydroxide bleeder valve 50, the described hydroxide sodium pump 47 of taking out pumps into described ion-exchanger 10 with the sodium hydroxide solutions in the described sodium hydroxide pond 46 and flows through behind described extration resin 941 types, from the outlet 12 of described ion-exchanger 10 in described sodium hydroxide bleeder valve 50 flow into described sodium hydroxide pond for recovering 49.
Described tap water feed valve 51 is arranged on the entrance 11 of described ion-exchanger 10 and from the beginning between the water source, the outlet 12 of described ion-exchanger 10 is connected with the entrance of described tap water pond for recovering 52 behind described tap water bleeder valve 53, described tap water after described tap water feed valve 51 flows into extration resin 941 types of described ion-exchanger 10, from the outlet 12 of described ion-exchanger 10 in described tap water bleeder valve 53 flow into described tap water pond for recovering 52.
One of preferred embodiment:
A kind of pending printed circuit board acidic etching waste liquor, its arsenic content is 4ppm, i.e. 4 mg/litre, make its present invention that flows through be used for the ion exchange resin arsenic removal treatment system of acidic etching liquid, the ion exchange resin dearsenicating method that adopts the present invention to be used for acidic etching liquid is handled, and obtains the printed circuit board acidic etching waste liquor after the arsenic removal, and its arsenic content is reduced to 1.2ppm, i.e. 1.2 mg/litre, the clearance of arsenic is 70%; The model of used extration resin is extration resin 941 types; In the arsenic removal treating processes, the feed valve of regulating among Fig. 1 30 is controlled the velocity of flow of described acidic etching waste liquid in described ion-exchanger, the time that described acidic etching waste liquid flows in described ion-exchanger was remained on 30 minutes, and the volume of the acidic etching waste liquid of handling when described extration resin 941 types just need carry out manipulation of regeneration to described extration resin 941 types when being 400 times of volume of these extration resin 941 types; Usually, when the volume of the acidic etching waste liquid of handling when described extration resin 941 types is 2000 times of volume of these extration resin 941 types, this moment the acidic etching waste liquid after described ion-exchanger arsenic removal is handled, the clearance of arsenic generally can be lower than 60%, just needs to have changed extration resin 941 types.
Printed circuit board acidic etching waste liquor after handling through arsenic removal of the present invention is for the production of basic copper chloride, very low, the up to specification technological standard of arsenic content of products obtained therefrom basic copper chloride.
The above embodiment has only expressed preferred implementation of the present invention, and it describes comparatively concrete and detailed, but can not therefore be interpreted as the restriction to claim of the present invention; Should be pointed out that for the person of ordinary skill of the art without departing from the inventive concept of the premise, can also make some distortion and improvement, these all belong to protection scope of the present invention; Therefore, all equivalents and modifications of doing with claim scope of the present invention all should belong to the covering scope of claim of the present invention.
Claims (10)
1. an ion exchange resin dearsenicating method that is used for acidic etching liquid is for the treating processes in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprises the steps:
A, fresh extration resin 941 types are packed in the ion-exchanger;
B, pending printed circuit board acidic etching waste liquor pumped into from the entrance of described ion-exchanger carry out arsenic removal in this ion-exchanger and handle, control the velocity of flow of described acidic etching waste liquid in described ion-exchanger, being allowed to condition at the time of flowing in this ion-exchanger remained on 20～40 minutes, flow out from the outlet of described ion-exchanger then, obtain the printed circuit board acidic etching waste liquor after the arsenic removal;
When the volume of C, the acidic etching waste liquid handled when described extration resin 941 types is 390～410 times of volume of these extration resin 941 types, the adsorptive power of these extration resin 941 types reaches capacity, then described extration resin 941 types need carry out manipulation of regeneration, and its steps in sequence is as follows:
C
1The entrance of hydrochloric acid from described ion-exchanger pumped in this ion-exchanger, make this hydrochloric acid by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
2After described hydrochloric acid has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
3After described tap water has cleaned described extration resin 941 types, the entrance of sodium hydroxide solution from described ion-exchanger pumped in this ion-exchanger, make this sodium hydroxide solution by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
4After described sodium hydroxide solution has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger again, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
Through above C
1～C
4Each step, described extration resin 941 type manipulation of regeneration finish, and available its continues to handle printed circuit board acidic etching waste liquor;
Repeating step B, after extremely the adsorptive power of described extration resin 941 types reaches capacity, operation steps C again, and then alternately repeating step B, C, acidic etching waste liquid after handling through described ion-exchanger arsenic removal, after the clearance of arsenic was lower than 60%, described extration resin 941 types needed to change, should empty described ion-exchanger this moment, repeats implementation step A.
2. the ion exchange resin dearsenicating method for acidic etching liquid according to claim 1 is characterized in that:
Step C
1In, the concentration of described hydrochloric acid is 7～10%, and the consumption of this hydrochloric acid is 1.5～2.5 times of described extration resin 941 type volumes, and this hydrochloric acid is 1.5～2.5 hours by the time of described ion-exchanger.
3. the ion exchange resin dearsenicating method for acidic etching liquid according to claim 1 is characterized in that:
Step C
2In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.
4. the ion exchange resin dearsenicating method for acidic etching liquid according to claim 1 is characterized in that:
Step C
3In, the concentration of described sodium hydroxide solution is 7～10%, and the consumption of this sodium hydroxide is 1.5～2.5 times of described extration resin 941 type volumes, and this sodium hydroxide is 1.5～2.5 hours by the time of described ion-exchanger.
5. the ion exchange resin dearsenicating method for acidic etching liquid according to claim 1 is characterized in that:
Step C
4In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.
6. the method for the used ion exchange resin regeneration of acidic etching liquid arsenic removal, it is characterized in that: used resin is extration resin 941 types, when the volume of the acidic etching waste liquid of handling when described extration resin 941 types is 390～410 times of volume of these extration resin 941 types, the adsorptive power of these extration resin 941 types reaches capacity, then described extration resin 941 types need carry out manipulation of regeneration, comprise the steps: according to this
C
1The entrance of hydrochloric acid from described ion-exchanger pumped in this ion-exchanger, make this hydrochloric acid by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
2After described hydrochloric acid has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
3After described tap water has cleaned described extration resin 941 types, the entrance of sodium hydroxide solution from described ion-exchanger pumped in this ion-exchanger, make this sodium hydroxide solution by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
C
4After described sodium hydroxide has washed described extration resin 941 types, then allow tap water flow in this ion-exchanger from the entrance of described ion-exchanger again, make this tap water by described extration resin 941 types, it is washed, and flow out from the outlet of described ion-exchanger;
Through above C
1～C
4Each step, described extration resin 941 type manipulation of regeneration finish, and can be reused for the processing printed circuit board acidic etching waste liquor.
7. the method for the used ion exchange resin regeneration of acidic etching liquid arsenic removal according to claim 6 is characterized in that:
Described step C
1In, the concentration of described hydrochloric acid is 7～10%, and the consumption of this hydrochloric acid is 1.5～2.5 times of described extration resin 941 type volumes, and this hydrochloric acid is 1.5～2.5 hours by the time of described ion-exchanger.
8. the method for the used ion exchange resin regeneration of acidic etching liquid arsenic removal according to claim 6 is characterized in that:
Described step C
2And C
4In, the consumption of described tap water is 1.5～2.5 times of described extration resin 941 type volumes, this tap water is 20～40 minutes by the time of described ion-exchanger.
9. the method for the used ion exchange resin regeneration of acidic etching liquid arsenic removal according to claim 6 is characterized in that:
Described step C
3In, the concentration of described sodium hydroxide solution is 7～10%, and the consumption of this sodium hydroxide is 1.5～2.5 times of described extration resin 941 type volumes, and this sodium hydroxide is 1.5～2.5 hours by the time of described ion-exchanger.
10. ion exchange resin arsenic removal treatment system that is used for acidic etching liquid, be for the treatment system in early stage of producing basic copper chloride from printed circuit board acidic etching waste liquor, comprise ion-exchanger (10) and liquid absorbing pump (20) that resin is housed, and be arranged on the feed valve (30) between the outlet of the entrance (11) of described ion-exchanger (10) and liquid absorbing pump (20); Described liquid absorbing pump (20) pumps into pending acidic etching liquid and carries out arsenic removal in this ion-exchanger (10) and handle from the entrance (11) of described ion-exchanger (10), the acidic etching liquid after arsenic removal is handled flows out through bleeder valve (31) from the outlet (12) of described ion-exchanger (10); It is characterized in that:
Described resin is extration resin 941 types; Described ion exchange resin arsenic removal treatment system also comprises the extration resin regenerating unit, and this extration resin regenerating unit comprises hydrochloric acid pond (41), takes out hydrochloric acid pump (42), hydrochloric acid feed valve (43), hydrochloric acid pond for recovering (44), hydrochloric acid bleeder valve (45), sodium hydroxide pond (46), take out hydroxide sodium pump (47), sodium hydroxide feed valve (48), sodium hydroxide pond for recovering (49), sodium hydroxide bleeder valve (50), tap water feed valve (51), tap water pond for recovering (52) and tap water bleeder valve (53);
The outlet in described hydrochloric acid pond (41) is connected with the entrance (11) of described ion-exchanger (10) after taking out hydrochloric acid pump (42) and hydrochloric acid feed valve (43) through described, the outlet (12) of described ion-exchanger (10) is connected with the entrance of described hydrochloric acid pond for recovering (44) behind described hydrochloric acid bleeder valve (45), the described hydrochloric acid pump (42) of taking out pumps into described ion-exchanger (10) with the hydrochloric acid in the described hydrochloric acid pond (41) and flows through behind described extration resin 941 types, from the outlet (12) of described ion-exchanger (10) in described hydrochloric acid bleeder valve (45) flow into described hydrochloric acid pond for recovering (44);
The outlet in described sodium hydroxide pond (46) is connected with the entrance (11) of described ion-exchanger (10) after taking out hydroxide sodium pump (47) and sodium hydroxide feed valve (48) through described, the outlet (12) of described ion-exchanger (10) is connected with the entrance of described sodium hydroxide pond for recovering (49) behind described sodium hydroxide bleeder valve (50), the described hydroxide sodium pump (47) of taking out pumps into described ion-exchanger (10) with the sodium hydroxide solution in the described sodium hydroxide pond (46) and flows through behind described extration resin 941 types, from the outlet (12) of described ion-exchanger (10) in described sodium hydroxide bleeder valve (50) flow into described sodium hydroxide pond for recovering (49);
Described tap water feed valve (51) is arranged on the entrance (11) of described ion-exchanger (10) and from the beginning between the water source, the outlet (12) of described ion-exchanger (10) is connected with the entrance of described tap water pond for recovering (52) behind described tap water bleeder valve (53), after described tap water flows into extration resin 941 types of described ion-exchanger (10) through described tap water feed valve (51), from the outlet (12) of described ion-exchanger (10) in described tap water bleeder valve (53) flow into described tap water pond for recovering (52).
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| CN106115982A (en) * | 2016-08-29 | 2016-11-16 | 湖南艾布鲁环保科技有限公司 | A kind of antimony and the processing means of association slag landfill percolate and method |
| CN106587263A (en) * | 2016-12-19 | 2017-04-26 | 广州达意隆包装机械股份有限公司 | Water treatment device, ion exchanger decontamination method and water treatment method |
| CN110095331A (en) * | 2018-01-29 | 2019-08-06 | 中国辐射防护研究院 | A kind of the experiment pretreatment unit and preprocess method of unused resin |
| CN109133497A (en) * | 2018-08-02 | 2019-01-04 | 深圳市华星光电技术有限公司 | Liquid waste treating apparatus and method for treating waste liquid |
| CN114180672B (en) * | 2021-04-22 | 2024-03-19 | 江苏和达电子科技有限公司 | Etching solution recovery system and application thereof |
| CN114308142A (en) * | 2022-01-05 | 2022-04-12 | 韶关绿鑫环保技术有限公司 | Copper ion exchange column analysis process |
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