CN102849701A - Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate - Google Patents
Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate Download PDFInfo
- Publication number
- CN102849701A CN102849701A CN2012103172706A CN201210317270A CN102849701A CN 102849701 A CN102849701 A CN 102849701A CN 2012103172706 A CN2012103172706 A CN 2012103172706A CN 201210317270 A CN201210317270 A CN 201210317270A CN 102849701 A CN102849701 A CN 102849701A
- Authority
- CN
- China
- Prior art keywords
- chemical nickel
- waste liquid
- phosphorus
- plating waste
- calcium phosphate
- 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.)
- Pending
Links
Abstract
The invention relates to a method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate. The method comprises the following process steps: weighing and putting a certain amount of chemical nickel plating waste liquid in a beaker; adding an excess amount of an oxidizing agent into the chemical nickel plating waste liquid containing Ni<2+>, sodium hypophosphite, sodium phosphate, carboxylate, sodium sulfate or ammonium sulfate, wherein the oxidizing agent may be hydrogen peroxide, hypochlorite, sodium permanganate or potassium permanganate; oxidizing hypophosphite radicals in the chemical nickel plating waste liquid and a by-product of chemical plating phosphite radicals into phosphate radicals; and then adding a sufficient amount of calcium chloride into the chemical nickel plating waste liquid under stirring so as to allow orthophosphate radicals to form precipitate with calcium ions and carrying out filtering after standing for a period of time so as to obtain the precipitate which is a phosphorus-containing substance, i.e., calcium phosphate. With the method provided by the invention, the phosphorus element in the chemical plating waste liquid can be extracted in the form of phosphate; calcium phosphate is prepared by using the nickel plating waste liquid as a raw material, and the advantages of a simple process and low production cost are obtained.
Description
Technical field
The invention belongs to the process field of chemical nickel phosphor plating, particularly a kind ofly from chemical nickel phosphor plating, extract the method that phosphorus prepares calcium phosphate.
Background technology
Chemical plating nickel-phosphorus alloy has excellent solidity to corrosion, wear resistance, high homogeneity and the special characteristics such as magnetic property, and it is used widely in fields such as aerospace, petrochemical complex, machinery and electronics.But the chemical plating nickel-phosphorus alloy plating bath will be scrapped after using some cycles, scrap and generally contain nickel ion 4 ~ 7g/L, sodium hypophosphite 20 ~ 35g/L, sodium phosphite 150 ~ 350g/L in the plating bath, sodium sulfate or ammonium sulfate 24 ~ 140g/L, carboxylate salt (complexing agent, buffer reagent) 40 ~ 60g/L.
Scrap and contain a large amount of utilizable resources in the plating bath, such as elements such as nickel, phosphorus.At present domestic patent " a kind of method of in alkaline chemical nickel-plating waste liquid, directly extracting nickel " (license notification number CN 101805831 B), " a kind of method of directly extracting nickel in acidic chemical nickel plating waste solution " (license notification number CN 101817607 B) and United States Patent (USP) " Method of recycling electroless nickel waste " are (US2008241410A1), this patent domestic application name " recovery method of electroless nickel waste " (application number: 200880008635.9) all mentioned the detailed recoverying and utilizing method of nickel element, do not had detailed mentioning about the recoverying and utilizing method of phosphoric.And phosphoric is the principal element of eutrophication, and the recovery extraction and application of therefore studying phosphoric in the waste liquid is necessary.
Summary of the invention
Purpose of the present invention, provide a kind of method that phosphorus prepares calcium phosphate of from chemical nickel phosphor plating, extracting, this method is for present prior art simultaneously nickel deposited, phosphorus or extract separately nickel, makes that phosphoric can be recovered utilization in the waste liquid, reduces the difficulty of follow-up water treatment with this.
The technical scheme that adopts is:
A kind ofly from chemical nickel phosphor plating, extract the method that phosphorus prepares calcium phosphate, comprise following processing step:
Get a certain amount of chemical nickel waste liquid in beaker, at first to containing Ni
2+, sodium hypophosphite, sodium phosphite, carboxylate salt, sodium sulfate or ammonium sulfate chemical nickel plating waste solution in add oxygenant, the amount of oxygenant is controlled at least 150g of every liter of waste liquid, described oxygenant is hydrogen peroxide, hypochlorite, sodium permanganate or potassium permanganate, Hypophosporous Acid, 50 root in the chemical nickel plating waste solution and electroless plating by product orthophosphite are oxidized to phosphate radical, then adding while stirring capacity calcium chloride in the above-mentioned chemical nickel plating waste solution makes ortho-phosphoric acid root and calcium ion form calcium phosphate precipitation, filter after leaving standstill for some time, precipitation is the material calcium phosphate of phosphorus element-containing.
The excessive method of above-mentioned judgement oxygenant is: the chemical nickel plating waste solution that takes a morsel after fully stirring can make the iodine liquid that adds starch be become colorless by blueness, and the excessive method of above-mentioned judgement calcium chloride is: get chemical nickel plating waste solution supernatant liquor adding calcium chloride and do not precipitate generation.
The invention has the advantages that:
Adopt that method can extract the form of phosphoric in the plating wastewater with calcium phosphate among the present invention, to adopt chemical nickel plating waste solution be the raw material preparation in the present invention in addition, and technique is simple, production cost is low.
Embodiment
Embodiment 1
A kind ofly from chemical nickel phosphor plating, extract the method that phosphorus prepares calcium phosphate, comprise following processing step:
Get chemical nickel waste liquid 500 ml in beaker, at first in chemical nickel plating waste solution, add the 75g clorox, the Hypophosporous Acid, 50 root in the chemical nickel plating waste solution and electroless plating by product orthophosphite are oxidized to phosphate radical; Then add at least while stirring 120g calcium chloride in the above-mentioned chemical nickel plating waste solution and make ortho-phosphoric acid root and calcium ion form calcium phosphate precipitation, leave standstill after 24 hours and filter, precipitation is the material calcium phosphate of phosphorus element-containing.
Claims (3)
1. one kind is extracted the method that phosphorus prepares calcium phosphate from chemical nickel phosphor plating, it is characterized in that, comprises following processing step:
Get a certain amount of chemical nickel waste liquid in beaker, at first to containing Ni
2+, sodium hypophosphite, sodium phosphite, carboxylate salt, sodium sulfate or ammonium sulfate chemical nickel plating waste solution in add oxygenant, the amount of oxygenant is controlled at least 150g of every liter of waste liquid, Hypophosporous Acid, 50 root in the chemical nickel plating waste solution and electroless plating by product orthophosphite are oxidized to phosphate radical, then adding while stirring capacity calcium chloride in the above-mentioned chemical nickel plating waste solution makes ortho-phosphoric acid root and calcium ion form calcium phosphate precipitation, filter after leaving standstill for some time, precipitation is the material calcium phosphate of phosphorus element-containing.
2. according to right 1 described a kind of method that phosphorus prepares calcium phosphate of from chemical nickel phosphor plating, extracting, it is characterized in that described oxygenant is hydrogen peroxide, hypochlorite, sodium permanganate or potassium permanganate.
3. according to right 1 described a kind of method that phosphorus prepares calcium phosphate of from chemical nickel phosphor plating, extracting, it is characterized in that, judge that the excessive method of oxygenant is: the chemical nickel plating waste solution supernatant liquor that takes a morsel after fully stirring can make the iodine liquid that adds starch be become colorless by blueness;
Judge that the excessive method of calcium chloride is: get chemical nickel plating waste solution supernatant liquor adding calcium chloride and do not precipitate generation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103172706A CN102849701A (en) | 2012-08-31 | 2012-08-31 | Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103172706A CN102849701A (en) | 2012-08-31 | 2012-08-31 | Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102849701A true CN102849701A (en) | 2013-01-02 |
Family
ID=47396752
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012103172706A Pending CN102849701A (en) | 2012-08-31 | 2012-08-31 | Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102849701A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104386662A (en) * | 2014-11-03 | 2015-03-04 | 贵州省化工研究院 | Method for coproducing tricalcium phosphate and ferric oxide by virtue of phosphated waste residues |
CN110078250A (en) * | 2018-01-26 | 2019-08-02 | 鹏鼎控股(深圳)股份有限公司 | The processing method of chemical nickle-plating wastewater |
CN111747592A (en) * | 2020-06-30 | 2020-10-09 | 深圳市深投环保科技有限公司 | Chemical nickel plating waste liquid recycling system and chemical nickel plating waste liquid treatment method |
CN112158978A (en) * | 2020-09-14 | 2021-01-01 | 浙江海拓环境技术有限公司 | Method for treating hypophosphite in chemical nickel plating waste liquid |
CN112551732A (en) * | 2020-11-03 | 2021-03-26 | 浙江海拓环境技术有限公司 | Hypophosphite treatment device and method for preventing iodine loss |
CN112759115A (en) * | 2020-12-17 | 2021-05-07 | 南京师范大学 | Method and device for treating chemical nickel plating waste bath solution |
CN113816517A (en) * | 2021-08-05 | 2021-12-21 | 青田永拓金属表面技术处理有限公司 | Resource recovery method for self-catalytic reduction chemical nickel plating waste liquid |
CN114408890A (en) * | 2022-03-14 | 2022-04-29 | 上海太洋科技有限公司 | Method for preparing optical calcium metaphosphate from phosphorus-containing waste liquid |
-
2012
- 2012-08-31 CN CN2012103172706A patent/CN102849701A/en active Pending
Non-Patent Citations (1)
Title |
---|
戎馨亚: "化学镀镍废液的处理及资源回收利用", 《中国优秀硕士学位论文全文数据库(工程科技Ⅰ辑)》 * |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104386662A (en) * | 2014-11-03 | 2015-03-04 | 贵州省化工研究院 | Method for coproducing tricalcium phosphate and ferric oxide by virtue of phosphated waste residues |
CN104386662B (en) * | 2014-11-03 | 2016-04-20 | 贵州省化工研究院 | A kind of method utilizing phosphatization waste residue to produce tricalcium phosphate co-production ferric oxide |
CN110078250A (en) * | 2018-01-26 | 2019-08-02 | 鹏鼎控股(深圳)股份有限公司 | The processing method of chemical nickle-plating wastewater |
CN111747592A (en) * | 2020-06-30 | 2020-10-09 | 深圳市深投环保科技有限公司 | Chemical nickel plating waste liquid recycling system and chemical nickel plating waste liquid treatment method |
CN112158978A (en) * | 2020-09-14 | 2021-01-01 | 浙江海拓环境技术有限公司 | Method for treating hypophosphite in chemical nickel plating waste liquid |
CN112158978B (en) * | 2020-09-14 | 2021-08-10 | 浙江海拓环境技术有限公司 | Method for treating hypophosphite in chemical nickel plating waste liquid |
CN112551732A (en) * | 2020-11-03 | 2021-03-26 | 浙江海拓环境技术有限公司 | Hypophosphite treatment device and method for preventing iodine loss |
CN112551732B (en) * | 2020-11-03 | 2022-07-12 | 浙江海拓环境技术有限公司 | Hypophosphite treatment device and method for preventing iodine loss |
CN112759115A (en) * | 2020-12-17 | 2021-05-07 | 南京师范大学 | Method and device for treating chemical nickel plating waste bath solution |
CN113816517A (en) * | 2021-08-05 | 2021-12-21 | 青田永拓金属表面技术处理有限公司 | Resource recovery method for self-catalytic reduction chemical nickel plating waste liquid |
CN114408890A (en) * | 2022-03-14 | 2022-04-29 | 上海太洋科技有限公司 | Method for preparing optical calcium metaphosphate from phosphorus-containing waste liquid |
CN114408890B (en) * | 2022-03-14 | 2023-08-04 | 上海太洋科技有限公司 | Method for preparing optical grade calcium metaphosphate from phosphorus-containing waste liquid |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102849701A (en) | Method of extracting phosphorus from chemical nickel-phosphorus plating waste liquid for preparation of calcium phosphate | |
CN101434441B (en) | Processing method of chemical nickel phosphor plating | |
CN102452743A (en) | Method for treating complex-containing nickel plating wastewater | |
CN105800822A (en) | Method and equipment for standards-reaching treatment of chemical nickel plating waste liquid | |
CN101423309A (en) | Electroplating waste and heavy metal double recovery method | |
CN110395817A (en) | The recycling processing method of chemical nickel plating waste solution | |
CN101805831B (en) | Method for directly extracting nickel in alkaline chemical nickel-plating waste liquid | |
CN113526752B (en) | Method for recycling copper and phosphorus resources in pyrophosphoric acid copper plating wastewater | |
CN102676814A (en) | Method for removing impurity ferrum in nickel sulfate solution | |
CN102765834A (en) | Method for treating industrial nitrogenous waste water through chemical precipitation method | |
CN104876200A (en) | Method for recycling phosphorus resource from electroless nickel plating wastewater | |
Lee | Separation and recovery of nickel from spent electroless nickel-plating solutions with hydrometallurgical processes | |
CN106348415A (en) | QCL-T complexing breaking agent and preparation method thereof | |
CN106430775A (en) | Comprehensive treatment and resource treatment method of nickel-containing waste liquid | |
CN103466770B (en) | Copper ammonia complexation wastewater treatment method | |
CN103482811A (en) | Method for sulfuric acid waste water containing low-concentration metal ions | |
CN106241897A (en) | A kind of method that nickel plating Ageing solution prepares metal sulfate nickel, sodium dihydrogen phosphate and sodium sulfate | |
CN203529996U (en) | Cuprammouium complexing wastewater treatment device | |
CN103241720A (en) | Method for preparing amorphous iron phosphate by using phosphate sludge | |
CN106145458A (en) | A kind of processing method of electroplating wastewater | |
CN102107960A (en) | Method for processing high-arsenic and high-alkali wastewater | |
CN102051489A (en) | Method for recycling indium from acid pressure oxidative leaching liquid of zinc smelting product | |
CN104058523B (en) | A kind for the treatment of process of vanadium oxide manufacture waste water | |
CN101713025B (en) | Method for wet separation of mixed solution containing nickel and zinc | |
CN104108812A (en) | Treating method for copper pyrophosphate electroplating wastewater |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20130102 |