CN204057991U - A kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate - Google Patents
A kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate Download PDFInfo
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- CN204057991U CN204057991U CN201420427308.XU CN201420427308U CN204057991U CN 204057991 U CN204057991 U CN 204057991U CN 201420427308 U CN201420427308 U CN 201420427308U CN 204057991 U CN204057991 U CN 204057991U
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- reactive tank
- rinse bath
- oxidation trough
- cover
- production line
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Abstract
The utility model relates to a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate, comprises reactive tank, oxidation trough, rinse bath, the travelling belt of connection for transmission mechanism, air blowing pipeline and cover; According to mass transport direction travelling belt successively road through reactive tank, oxidation trough and rinse bath; The side of reactive tank and oxidation trough is equipped with the fluid inlet with reaction mother liquor reservoir, and reactive tank and the bottom of oxidation trough are equipped with the liquid outlet be communicated with filtering for crystallizing device; The side of rinse bath is provided with the fluid inlet be communicated with clear water supply-pipe, and the bottom of rinse bath is provided with the liquid outlet with reaction mother liquor reservoir; Cover lid is located at the top of reactive tank, oxidation trough and rinse bath, and the side that cover is positioned at the feed end of reactive tank is provided with opening for feed, and the side that cover is positioned at the discharge end of rinse bath is provided with discharge port; Air blowing pipeline is laid on the bottom of reactive tank and oxidation trough.The utility model improves working (machining) efficiency, and fundamentally improves Working environment.
Description
Technical field
The utility model relates to a kind of production line preparing copper sulfate, particularly a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate.
Background technology
Copper-clad plate and electronic circuit board, formed by copper base and insulcrete compoiste adhering.Along with the develop rapidly of electron trade, waste and old copper-clad plate has become various lots of industrial refuse, and processes these waste and old copper-clad plates, usually adopts the method pulverized or burn, removes its insulcrete and reclaim copper material.Burn processing method will cause serious pollution for environment.And pulverization process method not only can not by waste and old copper-clad plate effective recycling, and need to spend more cost.Therefore the production method utilizing waste and old copper-clad plate black sulfuric acid copper has been had.This production method solves the process problem of various lots of waste and old copper-clad plate.But along with the utilization of this production method, there is again new problem to produce.Present production method waste and old copper-clad plate is tied up rear vertically hanging in be equipped with in the reactive tank of reaction mother liquor, then hung in oxidation trough through reaction after a while again and react further, finally hung in rinse bath and clean.Just because of its Production Flow Chart, what is bad to make production environment, and there is a large amount of ponding on ground, has a large amount of sour gas in air, and also affects its production efficiency when lifting, and needs to drop into certain staff.
Utility model content
The purpose of this utility model is to provide a kind of effectively to enhance productivity and the production line of copper sulfate is prepared in the waste and old copper-clad plate that utilizes of Working environment, and this production line also can utilize old circuit board or cupric scrap stock to be prepared copper sulfate.
The technical scheme realizing the utility model object is: the utility model comprises reactive tank, oxidation trough, rinse bath, the travelling belt of connection for transmission mechanism, air blowing pipeline and cover; According to mass transport direction travelling belt successively road through reactive tank, oxidation trough and rinse bath, and below liquid level material can being sent into liquid in reactive tank, oxidation trough and rinse bath; The side of described reactive tank and oxidation trough is equipped with the fluid inlet with reaction mother liquor reservoir, and reactive tank and the bottom of oxidation trough are equipped with the liquid outlet be communicated with filtering for crystallizing device; The side of described rinse bath is provided with the fluid inlet be communicated with clear water supply-pipe, and the bottom of rinse bath is provided with the liquid outlet with reaction mother liquor reservoir; Described cover lid is located at the top of reactive tank, oxidation trough and rinse bath, and the side that cover is positioned at the feed end of reactive tank is provided with opening for feed, and the side that cover is positioned at the discharge end of rinse bath is provided with discharge port; Described air blowing pipeline is laid on the bottom of reactive tank and oxidation trough, and its surface is evenly equipped with gas hole.Wherein reaction mother liquor container is the container holding playback mother liquor, and filtering for crystallizing device is the device that existing conventional filtering for crystallizing prepares cupric sulphate crystal.Wherein travelling belt is made up of the material can standing reaction mother liquor corrosion, such as stainless steel, acid-proof resin etc.
Above above-mentioned reactive tank, oxidation trough and rinse bath, equal correspondence is provided with a briquetting, and briquetting is fixedly installed on cover; The bottom surface of described every block briquetting is all pressed into below the liquid level of liquid in the reactive tank of its correspondence, oxidation trough and rinse bath; The bottom surface of described each briquetting forms material conveying passage with the loading surface of corresponding travelling belt; The bottom surface of described each briquetting is provided with the diversion trench guiding flow direction.
Fluid inlet on above-mentioned reactive tank is arranged on the side of reactive tank discharge end, and just to material conveying passage; Fluid inlet on described oxidation trough is arranged on the side of oxidation trough discharge end, and just to material conveying passage; Fluid inlet on described rinse bath is arranged on the side of rinse bath discharge end, and just to material conveying passage.
The bottom of above-mentioned reactive tank, oxidation trough and rinse bath be equipped with a blowdown notch and a connection for transmission mechanism for the blowdown scraper plate bottom wiper; Described blowdown notch is arranged on the side, bottom of its place reactive tank or oxidation trough or rinse bath, and blowdown scraper plate is slidably arranged in the bottom of its place reactive tank or oxidation trough or rinse bath and slides to blowdown notch.
Above-mentioned production line also comprises condensation of gas retrieving arrangement, and condensation of gas retrieving arrangement comprises inlet pipe, condensing works and drain pipe; Described cover is provided with production well, and production well is connected with the inlet pipe of condensation of gas retrieving arrangement and communicates, and the drain pipe of condensation of gas retrieving arrangement is connected with reaction mother liquor container and communicates.
Above-mentioned cover inner is fixed with dividing plate, and dividing plate is located between reactive tank and oxidation trough, and cover inner is divided into the firstth district and the secondth district by dividing plate; The loading surface of described dividing plate and travelling belt leaves material conveying passage; Production well on described cover is arranged on the secondth district.
Above-mentioned air blowing pipeline comprises the gas blow pipe of an inlet pipe and more than two, and every root gas blow pipe is all connected with inlet pipe and communicates; Described gas blow pipe extends to the bottom of oxidation trough from the bottom of reactive tank; The part that described gas blow pipe is positioned at reactive tank and oxidation trough inside is evenly equipped with gas hole.
Above-mentioned production line also comprises water leg; Described water leg is placed on the bottom of reactive tank, oxidation trough and rinse bath; The bottom of described water leg is provided with water port.
As distortion, in reactive tank, oxidation trough and rinse bath can also wholely be packaged in by above-mentioned water leg; Described reactive tank, oxidation trough and rinse bath are fixedly installed on water leg inside vacantly; The bottom of described water leg is provided with water port; The described pipeline be communicated with fluid inlet and the liquid outlet of rinse bath with reactive tank, oxidation trough all accesses through water leg.
In order to solve the problem of solid accumulation, the opening for feed on above-mentioned cover and discharge port are equipped with charging guide plate; The side that described dividing plate is positioned at reactive tank is also provided with charging guide plate.
The outside of above-mentioned reactive tank, oxidation trough, rinse bath and cover is equipped with thermal insulation layer.
Above-mentioned travelling belt according to mass transport direction successively road through reactive tank, oxidation trough and rinse bath, and return from the inside of rinse bath, oxidation trough and reactive tank successively formed loop.
Above-mentioned travelling belt according to mass transport direction successively road through reactive tank, oxidation trough and rinse bath, and return from the outside of rinse bath, oxidation trough and reactive tank successively formed loop.
The utility model has positive effect: waste and old copper-clad plate is prepared the production process of copper sulfate continuously and steadily by travelling belt by (1) the utility model, decreases the transfer time of material, improves production efficiency; (2) the utility model covers and establishes cover above reactive tank, oxidation trough and rinse bath, greatly reduces the sour gas in air, substantially improves Working environment; (3) the utility model adds condensation of gas retrieving arrangement on cover, fundamentally solves the problem of sour gas, and rationally recycles sour gas, decreases cost and drops into; (4) setting of briquetting in the utility model, the duration of contact effectively improving material and reaction mother liquor with contact effect, enhance productivity; (5) water leg arranged in the utility model, fundamentally solves ground area water problem, further improves Working environment; (6) flow-guiding channel in the utility model on briquetting lower surface can effectively improve when reaction mother liquor injects and the contact effect of material, improves reaction efficiency, thus enhances productivity; (7) the utility model is equipped with thermal insulation layer in the outside of reactive tank, oxidation trough, rinse bath and cover, can ensure the temperature of reaction formula to greatest extent, ensures reaction effect; (8) the utility model arranges blowdown notch and blowdown scraper plate in the bottom of reactive tank, oxidation trough and rinse bath, can solve the problem of reactive tank periodic cleaning difficulty, improves convenient degree, increases productivity; (9) travelling belt is arranged to outer loop by the utility model, can reduce the duration of contact of travelling belt and reaction mother liquor, improves the work-ing life of travelling belt; (10) the utility model has liberated labor force, only need add material at regular time and quantity, while enhancing productivity, decrease the input of cost.
Accompanying drawing explanation
In order to make content of the present utility model more easily be clearly understood, below according to specific embodiment also by reference to the accompanying drawings, the utility model is described in further detail, wherein
Fig. 1 is the schematic perspective view of the utility model embodiment one;
Fig. 2 is the schematic perspective view of the utility model embodiment two;
Fig. 3 is the structural representation of the utility model embodiment one;
Fig. 4 is the structural representation of the utility model embodiment two;
Fig. 5 is the structural representation of the lower surface of briquetting in the utility model;
Fig. 6 is the structural representation of pipeline of blowing in the utility model;
Fig. 7 is the structural representation of reaction tank bottom blowdown notch and blowdown scraper plate in the utility model.
Embodiment
(embodiment 1)
See Fig. 1, Fig. 3, Fig. 5, Fig. 6 and Fig. 7, the utility model comprises reactive tank 1, oxidation trough 2, rinse bath 3, the travelling belt 4 of connection for transmission mechanism, air blowing pipeline 5 and cover 6; According to mass transport direction travelling belt 4 successively road through reactive tank 1, oxidation trough 2 and rinse bath 3, and below liquid level material can being sent into liquid in reactive tank 1, oxidation trough 2 and rinse bath 3; Described reactive tank 1 and the side of oxidation trough 2 are equipped with the fluid inlet 11 be communicated with reaction mother liquor container 9, and reactive tank 1 and the bottom of oxidation trough 2 are equipped with the liquid outlet 12 be communicated with filtering for crystallizing device 10; The side of described rinse bath 3 is provided with the fluid inlet 11 be communicated with clear water supply-pipe, and the bottom of rinse bath 3 is provided with the liquid outlet 12 be communicated with reaction mother liquor container 9; Described cover 6 lid is located at the top of reactive tank 1, oxidation trough 2 and rinse bath 3, and the side that cover 6 is positioned at the feed end of reactive tank 1 is provided with opening for feed 6-1, and the side that cover 6 is positioned at the discharge end of rinse bath 3 is provided with discharge port 6-2; Described air blowing pipeline 5 comprises an an inlet pipe 5-1 and three gas blow pipe 5-2, and every root gas blow pipe 5-2 is all connected with inlet pipe 5-1 and communicates; Described gas blow pipe 5-2 extends to the bottom of oxidation trough 2 from the bottom of reactive tank 1; The part that described gas blow pipe 5-2 is positioned at reactive tank 1 and oxidation trough 2 inside is evenly equipped with gas hole; Above described reactive tank 1, oxidation trough 2 and rinse bath 3, equal correspondence is provided with a briquetting 13, and briquetting 13 is fixedly installed on cover 6; The bottom surface of described every block briquetting 13 is all pressed into below the liquid level of liquid in the reactive tank 1 of its correspondence, oxidation trough 2 and rinse bath 3; The bottom surface of described each briquetting 13 forms material conveying passage with the loading surface of corresponding travelling belt 4; Fluid inlet 11 on described reactive tank 1 is arranged on the side of reactive tank 1 discharge end, and just to material conveying passage; Fluid inlet 11 on described oxidation trough 2 is arranged on the side of oxidation trough 2 discharge end, and just to material conveying passage; Fluid inlet 11 on described rinse bath 3 is arranged on the side of rinse bath 3 discharge end, and just to material conveying passage; The bottom surface of described each briquetting 13 is provided with the diversion trench 13-1 guiding flow direction, with fully the contacting of material when ensureing that reaction mother liquor enters, improves reaction effect, enhances productivity; The bottom of described reactive tank 1, oxidation trough 2 and rinse bath 3 be equipped with a blowdown notch 15 and a connection for transmission mechanism for the blowdown scraper plate 16 bottom wiper; Described blowdown notch 15 is arranged on the side, bottom of its place reactive tank 1 or oxidation trough 2 or rinse bath 3, and blowdown scraper plate 16 is slidably arranged in the bottom of its place reactive tank 1 or oxidation trough 2 or rinse bath 3 and slides to blowdown notch 15, so that periodic cleaning blowdown; The outside of described reactive tank 1, oxidation trough 2, rinse bath 3 and cover 6 is equipped with thermal insulation layer, and during to ensure to react, temperature is constant, ensures reaction effect.
This production line also comprises condensation of gas retrieving arrangement 7, and condensation of gas retrieving arrangement 7 comprises inlet pipe 7-1, condensing works 7-2 and drain pipe 7-3; Described cover 6 is provided with production well, and production well is connected with the inlet pipe 7-1 of condensation of gas retrieving arrangement 7 and communicates, and the drain pipe 7-3 of condensation of gas retrieving arrangement 7 is connected with reaction mother liquor container 9 and communicates.
This production line also comprises water leg 8; It is inner that described reactive tank 1, oxidation trough 2 and rinse bath 3 are fixedly installed on water leg 8 vacantly; The bottom of described water leg 8 is provided with water port; The described pipeline be communicated with fluid inlet 11 and the liquid outlet 12 of rinse bath 3 with reactive tank 1, oxidation trough 2 all accesses through water leg 8; Described travelling belt 4 according to mass transport direction successively road through reactive tank 1, oxidation trough 2 and rinse bath 3, and return from the outside of rinse bath 3, oxidation trough 2 and reactive tank 1 successively formed loop.
(embodiment 2)
See Fig. 2, Fig. 4, Fig. 5, Fig. 6 and Fig. 7, the utility model comprises reactive tank 1, oxidation trough 2, rinse bath 3, the travelling belt 4 of connection for transmission mechanism, air blowing pipeline 5 and cover 6; According to mass transport direction travelling belt 4 successively road through reactive tank 1, oxidation trough 2 and rinse bath 3, and below liquid level material can being sent into liquid in reactive tank 1, oxidation trough 2 and rinse bath 3; Described reactive tank 1 and the side of oxidation trough 2 are equipped with the fluid inlet 11 be communicated with reaction mother liquor container 9, and reactive tank 1 and the bottom of oxidation trough 2 are equipped with the liquid outlet 12 be communicated with filtering for crystallizing device 10; The side of described rinse bath 3 is provided with the fluid inlet 11 be communicated with clear water supply-pipe, and the bottom of rinse bath 3 is provided with the liquid outlet 12 be communicated with reaction mother liquor container 9; Described cover 6 lid is located at the top of reactive tank 1, oxidation trough 2 and rinse bath 3, and the side that cover 6 is positioned at the feed end of reactive tank 1 is provided with opening for feed 6-1, and the side that cover 6 is positioned at the discharge end of rinse bath 3 is provided with discharge port 6-2; Described air blowing pipeline 5 comprises an an inlet pipe 5-1 and three gas blow pipe 5-2, and every root gas blow pipe 5-2 is all connected with inlet pipe 5-1 and communicates; Described gas blow pipe 5-2 extends to the bottom of oxidation trough 2 from the bottom of reactive tank 1; The part that described gas blow pipe 5-2 is positioned at reactive tank 1 and oxidation trough 2 inside is evenly equipped with gas hole; Above described reactive tank 1, oxidation trough 2 and rinse bath 3, equal correspondence is provided with a briquetting 13, and briquetting 13 is fixedly installed on cover 6; The bottom surface of described every block briquetting 13 is all pressed into below the liquid level of liquid in the reactive tank 1 of its correspondence, oxidation trough 2 and rinse bath 3; The bottom surface of described each briquetting 13 forms material conveying passage with the loading surface of corresponding travelling belt 4; Fluid inlet 11 on described reactive tank 1 is arranged on the side of reactive tank 1 discharge end, and just to material conveying passage; Fluid inlet 11 on described oxidation trough 2 is arranged on the side of oxidation trough 2 discharge end, and just to material conveying passage; Fluid inlet 11 on described rinse bath 3 is arranged on the side of rinse bath 3 discharge end, and just to material conveying passage; The bottom surface of described each briquetting 13 is provided with the diversion trench 13-1 guiding flow direction, with fully the contacting of material when ensureing that reaction mother liquor enters, improves reaction effect, enhances productivity; The bottom of described reactive tank 1, oxidation trough 2 and rinse bath 3 be equipped with a blowdown notch 15 and a connection for transmission mechanism for the blowdown scraper plate 16 bottom wiper; Described blowdown notch 15 is arranged on the side, bottom of its place reactive tank 1 or oxidation trough 2 or rinse bath 3, and blowdown scraper plate 16 is slidably arranged in the bottom of its place reactive tank 1 or oxidation trough 2 or rinse bath 3 and slides to blowdown notch 15, so that periodic cleaning blowdown; The outside of described reactive tank 1, oxidation trough 2, rinse bath 3 and cover 6 is equipped with thermal insulation layer, and during to ensure to react, temperature is constant, ensures reaction effect.
This production line also comprises condensation of gas retrieving arrangement 7, and condensation of gas retrieving arrangement 7 comprises inlet pipe 7-1, condensing works 7-2 and drain pipe 7-3; Described cover 6 is provided with production well, and production well is connected with the inlet pipe 7-1 of condensation of gas retrieving arrangement 7 and communicates, and the drain pipe 7-3 of condensation of gas retrieving arrangement 7 is connected with reaction mother liquor container 9 and communicates; Described cover 6 inside is fixed with dividing plate 6-3, and dividing plate 6-3 is located between reactive tank 1 and oxidation trough 2, and cover 6 inside is divided into the first district 6-4 and the second district 6-5 by dividing plate 6-3; The loading surface of described dividing plate 6-3 and travelling belt 4 leaves material conveying passage; Production well on described cover 6 is arranged on the second district 6-5.
This production line also comprises water leg 8; It is inner that described reactive tank 1, oxidation trough 2 and rinse bath 3 are fixedly installed on water leg 8 vacantly; The bottom of described water leg 8 is provided with water port; The described pipeline be communicated with fluid inlet 11 and the liquid outlet 12 of rinse bath 3 with reactive tank 1, oxidation trough 2 all accesses through water leg 8; Described travelling belt 4 according to mass transport direction successively road through reactive tank 1, oxidation trough 2 and rinse bath 3, and return from the outside of rinse bath 3, oxidation trough 2 and reactive tank 1 successively formed loop.
Above-described specific embodiment; the purpose of this utility model, technical scheme and beneficial effect are further described; be understood that; the foregoing is only specific embodiment of the utility model; be not limited to the utility model; all within spirit of the present utility model and principle, any amendment made, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. the production line utilizing waste and old copper-clad plate to prepare copper sulfate; It is characterized in that: comprise reactive tank (1), oxidation trough (2), rinse bath (3), the travelling belt (4) of connection for transmission mechanism, air blowing pipeline (5) and cover (6); According to mass transport direction travelling belt (4) successively road through reactive tank (1), oxidation trough (2) and rinse bath (3), and below liquid level material can being sent into liquid in reactive tank (1), oxidation trough (2) and rinse bath (3); Described reactive tank (1) and the side of oxidation trough (2) are equipped with the fluid inlet (11a) be communicated with reaction mother liquor container (9), and reactive tank (1) and the bottom of oxidation trough (2) are equipped with the liquid outlet (12a) be communicated with filtering for crystallizing device (10); The side of described rinse bath (3) is provided with the fluid inlet (11b) be communicated with clear water supply-pipe, and the bottom of rinse bath (3) is provided with the liquid outlet (12b) be communicated with reaction mother liquor container (9); Described cover (6) lid is located at the top of reactive tank (1), oxidation trough (2) and rinse bath (3), the side that cover (6) is positioned at the feed end of reactive tank (1) is provided with opening for feed (6-1), and the side that cover (6) is positioned at the discharge end of rinse bath (3) is provided with discharge port (6-2); Described air blowing pipeline (5) is laid on the bottom of reactive tank (1) and oxidation trough (2), and its surface is evenly equipped with gas hole.
2. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 1, it is characterized in that: described reactive tank (1), oxidation trough (2) and rinse bath (3) top all correspondence is provided with a briquetting (13), and briquetting (13) is fixedly installed on cover (6); The bottom surface of described every block briquetting (13) is all pressed into below the liquid level of liquid in the reactive tank (1) of its correspondence, oxidation trough (2) and rinse bath (3); The bottom surface of described each briquetting (13) forms material conveying passage with the loading surface of corresponding travelling belt (4); The bottom surface of described each briquetting (13) is provided with the diversion trench (13-1) guiding flow direction.
3. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 2, it is characterized in that: the fluid inlet (11a) on described reactive tank (1) is arranged on the side of reactive tank (1) discharge end, and just to material conveying passage; Fluid inlet (11a) on described oxidation trough (2) is arranged on the side of oxidation trough (2) discharge end, and just to material conveying passage; Fluid inlet (11b) on described rinse bath (3) is arranged on the side of rinse bath (3) discharge end, and just to material conveying passage.
4. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 3, is characterized in that: the bottom of described reactive tank (1), oxidation trough (2) and rinse bath (3) be equipped with a blowdown notch (15) and a connection for transmission mechanism for the blowdown scraper plate (16) bottom wiper; Described blowdown notch (15) is arranged on the side, bottom of its place reactive tank (1) or oxidation trough (2) or rinse bath (3), and blowdown scraper plate (16) is slidably arranged in the bottom of its place reactive tank (1) or oxidation trough (2) or rinse bath (3) and slides to blowdown notch (15).
5. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 4, it is characterized in that: also comprise condensation of gas retrieving arrangement (7), condensation of gas retrieving arrangement (7) comprises inlet pipe (7-1), condensing works (7-2) and drain pipe (7-3); Described cover (6) is provided with production well, production well is connected with the inlet pipe (7-1) of condensation of gas retrieving arrangement (7) and communicates, and the drain pipe (7-3) of condensation of gas retrieving arrangement (7) is connected with reaction mother liquor container (9) and communicates.
6. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 5, it is characterized in that: described cover (6) inside is fixed with dividing plate (6-3), dividing plate (6-3) is located between reactive tank (1) and oxidation trough (2), and cover (6) inside is divided into the firstth district (6-4) and the secondth district (6-5) by dividing plate (6-3); Described dividing plate (6-3) leaves material conveying passage with the loading surface of travelling belt (4); Production well on described cover (6) is arranged on the secondth district (6-5).
7. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 6, it is characterized in that: described air blowing pipeline (5) comprises the gas blow pipe (5-2) of an inlet pipe (5-1) and more than two, every root gas blow pipe (5-2) is all connected with inlet pipe (5-1) and communicates; Described gas blow pipe (5-2) extends to the bottom of oxidation trough (2) from the bottom of reactive tank (1); Described gas blow pipe (5-2) is positioned in the inner part of reactive tank (1) and oxidation trough (2) and is evenly equipped with gas hole.
8. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 7, is characterized in that: also comprise water leg (8); It is inner that described reactive tank (1), oxidation trough (2) and rinse bath (3) are fixedly installed on water leg (8) vacantly; The bottom of described water leg (8) is provided with water port; The described pipeline be communicated with fluid inlet (11a, 11b) and the liquid outlet (12a, 12b) of reactive tank (1), oxidation trough (2) and rinse bath (3) all accesses through water leg (8).
9. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 8, is characterized in that: the outside of described reactive tank (1), oxidation trough (2), rinse bath (3) and cover (6) is equipped with thermal insulation layer.
10. a kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate according to claim 9, it is characterized in that: described travelling belt (4) according to mass transport direction successively road through reactive tank (1), oxidation trough (2) and rinse bath (3), and return from the outside of rinse bath (3), oxidation trough (2) and reactive tank (1) successively formed loop.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420427308.XU CN204057991U (en) | 2014-07-30 | 2014-07-30 | A kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420427308.XU CN204057991U (en) | 2014-07-30 | 2014-07-30 | A kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204057991U true CN204057991U (en) | 2014-12-31 |
Family
ID=52199546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420427308.XU Withdrawn - After Issue CN204057991U (en) | 2014-07-30 | 2014-07-30 | A kind of production line utilizing waste and old copper-clad plate to prepare copper sulfate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204057991U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150523A (en) * | 2014-07-30 | 2014-11-19 | 江苏夏博士节能工程股份有限公司 | Production line for preparing copper sulfate from waste copper clad plates |
| CN109534384A (en) * | 2019-01-24 | 2019-03-29 | 苏州华锋环保技术有限公司 | High purity copper sulfate production line |
-
2014
- 2014-07-30 CN CN201420427308.XU patent/CN204057991U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150523A (en) * | 2014-07-30 | 2014-11-19 | 江苏夏博士节能工程股份有限公司 | Production line for preparing copper sulfate from waste copper clad plates |
| CN109534384A (en) * | 2019-01-24 | 2019-03-29 | 苏州华锋环保技术有限公司 | High purity copper sulfate production line |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141231 Effective date of abandoning: 20160330 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |