GB2073725A - A Method of Recovering Lead Values from Scrap Batteries - Google Patents
A Method of Recovering Lead Values from Scrap Batteries Download PDFInfo
- Publication number
- GB2073725A GB2073725A GB8110998A GB8110998A GB2073725A GB 2073725 A GB2073725 A GB 2073725A GB 8110998 A GB8110998 A GB 8110998A GB 8110998 A GB8110998 A GB 8110998A GB 2073725 A GB2073725 A GB 2073725A
- Authority
- GB
- United Kingdom
- Prior art keywords
- lead
- solution
- nitrate
- nitric acid
- added
- 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.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims abstract description 17
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 34
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 34
- RLJMLMKIBZAXJO-UHFFFAOYSA-N lead nitrate Chemical compound [O-][N+](=O)O[Pb]O[N+]([O-])=O RLJMLMKIBZAXJO-UHFFFAOYSA-N 0.000 claims abstract description 32
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 claims abstract description 26
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000007790 solid phase Substances 0.000 claims abstract description 8
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims abstract description 5
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 4
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims abstract description 3
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 44
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 20
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 229910052742 iron Inorganic materials 0.000 claims description 10
- 238000001914 filtration Methods 0.000 claims description 9
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 9
- 239000010949 copper Substances 0.000 claims description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 7
- 229910052802 copper Inorganic materials 0.000 claims description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910052797 bismuth Inorganic materials 0.000 claims description 4
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 4
- 239000001569 carbon dioxide Substances 0.000 claims description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 3
- 239000007791 liquid phase Substances 0.000 claims description 3
- YADSGOSSYOOKMP-UHFFFAOYSA-N dioxolead Chemical compound O=[Pb]=O YADSGOSSYOOKMP-UHFFFAOYSA-N 0.000 abstract description 54
- 229910052751 metal Inorganic materials 0.000 abstract description 16
- 239000002184 metal Substances 0.000 abstract description 16
- HTUMBQDCCIXGCV-UHFFFAOYSA-N lead oxide Chemical compound [O-2].[Pb+2] HTUMBQDCCIXGCV-UHFFFAOYSA-N 0.000 description 23
- 239000007787 solid Substances 0.000 description 19
- KEQXNNJHMWSZHK-UHFFFAOYSA-L 1,3,2,4$l^{2}-dioxathiaplumbetane 2,2-dioxide Chemical compound [Pb+2].[O-]S([O-])(=O)=O KEQXNNJHMWSZHK-UHFFFAOYSA-L 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 14
- 239000000463 material Substances 0.000 description 10
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 9
- 229910052708 sodium Inorganic materials 0.000 description 9
- 239000011734 sodium Substances 0.000 description 9
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 7
- 229910002651 NO3 Inorganic materials 0.000 description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 4
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 229910052787 antimony Inorganic materials 0.000 description 3
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- MFEVGQHCNVXMER-UHFFFAOYSA-L 1,3,2$l^{2}-dioxaplumbetan-4-one Chemical compound [Pb+2].[O-]C([O-])=O MFEVGQHCNVXMER-UHFFFAOYSA-L 0.000 description 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 229910000003 Lead carbonate Inorganic materials 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 2
- 239000001099 ammonium carbonate Substances 0.000 description 2
- 235000012501 ammonium carbonate Nutrition 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- ZWWCURLKEXEFQT-UHFFFAOYSA-N dinitrogen pentoxide Inorganic materials [O-][N+](=O)O[N+]([O-])=O ZWWCURLKEXEFQT-UHFFFAOYSA-N 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000001999 grid alloy Substances 0.000 description 2
- 229910000464 lead oxide Inorganic materials 0.000 description 2
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 2
- 239000001272 nitrous oxide Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- 229910004809 Na2 SO4 Inorganic materials 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 229910052924 anglesite Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- MOUPNEIJQCETIW-UHFFFAOYSA-N lead chromate Chemical compound [Pb+2].[O-][Cr]([O-])(=O)=O MOUPNEIJQCETIW-UHFFFAOYSA-N 0.000 description 1
- 150000002611 lead compounds Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 150000003385 sodium Chemical class 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B13/00—Obtaining lead
- C22B13/04—Obtaining lead by wet processes
- C22B13/045—Recovery from waste materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G21/00—Compounds of lead
- C01G21/18—Nitrates
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/54—Reclaiming serviceable parts of waste accumulators
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Secondary Cells (AREA)
Abstract
Lead is recovered from the paste fraction of scrap lead batteries as a solution of lead nitrate by a wet process which involves a preliminary desulphation of the paste fraction by treatment with a carbonate or hydroxide of an alkali metal or of ammonium. The solid phase of the reaction product is then treated with nitric acid, to convert into lead nitrate the lead present as metal, as lead monoxide and as lead dioxide, in the presence of hydrogen peroxide or of added lead.
Description
SPECIFICATION
A Method of Recovering Lead Values from Scrap Batteries
Scrap lead batteries are treated in a battery breaker, which separates the crushed material into three main fractions, one containing the paste, a second containing metal derived from the battery grids and a third consisting of the plastics material constituting the casings and separators. The third fraction is generally waste, the second fraction is subjected to smelting and refining to recover lead and antimony and the first or paste fraction is normally also subjected to smelting and refining.
The paste fraction consists predominatingly of lead sulphate, the next main constituent is PbO2 and PbO and some metallic lead are also present
We have found that the total lead contents of a series of samples taken from different battery breaking machines varied between 70% and 80% of the solids present in the paste. The amount of lead present as sulphate varied between 24% and 41%, the amount as metal between 1% and 25%, and the amount as lead dioxide between 1 1% and 26%. All these figures are given as percentages by weight on the solids in the paste. The variations in the amounts of lead as lead sulphate and as lead dioxide arise from variations in the state of charge of individual batteries as they are scrapped.The metallic lead in the paste fraction has its origin partly in the "sponge lead" which constitutes the active material of negative plates in the charged condition, and partly in the ingress of fragments of broken grid alloy into the paste fraction when the battery is broken and its components separated. Sponge lead, when wet, is readily oxidized in the atmosphere, and as a result the paste fraction contains between 2% and 15% of lead monoxide.
The object of the present invention is to avoid the necessity for smelting and to provide a wet process for converting the lead present in the paste fraction at high yield into an aqueous solution of lead nitrate, which is a useful intermediate in the manufacture of lead chromate pigments.
It is not feasible to treat the paste fraction directly with nitric acid because, while metallic lead and lead monoxide both dissolve readily in nitric acid, lead sulphate and lead dioxide do not and must therefore be converted into acid-soluble forms. Lead monoxide dissolves according to the equation: Pb0+2HNQ#Pb(N03)2+2 H20 (1)
Metallic lead dissolves in nitric acid producing lead nitrate and a variety of gaseous products including nitrous oxide (N2O), nitrogen (N2) and nitric oxide (NO). The proportions of these gases vary according to the temperature and the concentration of the nitric acid, and therefore vary during the course of a dissolution. The dissolution of metal is a slower process than that of lead monoxide at low temperature and at low concentrations of acid.
It is therefore necessary to subject the paste fraction to a preliminary desulphation treatment to convert the lead sulphate into a water soluble sulphate and a compound of lead which is soluble in nitric acid. This may be achieved in accordance with the invention by treating the paste fraction either with a carbonate of an alkali metal, e.g. sodium carbonate or potassium carbonate, or with ammonium carbonate to convert the lead sulphate into lead carbonate, which is soluble in nitric acid, or with an alkali metal hydroxide, e.g. sodium or potassium hydroxide, or with ammonium hydroxide, which converts the lead sulphate into a hydrated lead oxide which is also soluble in nitric acid.
This desulphation treatment may be carried out at room temperature, but it may be advantageous in order to speed up the reaction to use a hot solution. Thus the reaction may be carried out at a temperature in the range of 10--100"C.
These are known reactions. Thus U.S. Patent No. 3689253 describes desulphation of battery sludge with an alkali metal hydroxide or carbonate as a preliminary to smelting.
There remains the problem of converting the desulphated battery paste, after removal of the liquid phase, e.g. by filtration, to lead nitrate solution. The desulphated material is soluble in nitric acid apart from the lead dioxide and such minor amount of unconverted lead sulphate as may be present following the desulphation step.
One way of rendering the lead dioxide amenable to treatment with nitric acid in a wet process is to reduce it to lead monoxide. Most reducing agents produce by-products which will contaminate the resulting solution of lead nitrate but we have found hydrogen peroxide to be effective. It reacts as follows with lead dioxide in the presence of nitric acid:~ PbO2+H202+2HNO3oPb(NO3)2+2H2O+O2 (2) the oxygen escaping and leaving no contaminant in the lead nitrate.
We have also found that lead dioxide is capable of reacting as follows with nitric acid if lead dioxide and metallic lead are present in the material to be treated in the correct relative proportions, without the necessity of using a reducing agent: Pb+Pbo2+4HNo3e2Pb(No3)2+2H2o (3)
As a practical matter, the paste fraction is highly unlikely to contain sufficient lead for this reaction to take place and it will normally be necessary to add up to 1 2 parts of lead, e.g. in the form of granulated lead or of broken battery grid, by weight per cent weight of lead dioxide. The amount of nitric acid should of course be sufficient for reaction with the lead dioxide, the lead monoxide and all the lead present.
The reaction with nitric acid, in the presence of added lead, requires to be carried out at an elevated temperature in the range of 40-900C.
The invention accordingly provides a method of recovering lead as an aqueous solution of lead nitrate from the paste fraction derived from scrap lead batteries, which comprises subjecting the paste fraction to desulphation by treatment with a carbonate or hydroxide of an alkali metal or of ammonium, separating the solid and liquid phases of the reaction product, and then treating the solid phase with nitric acid in the presence of hydrogen peroxide, or in the presence of added lead and at a temperature in the range of 40-900 C, to convert to lead nitrate substantially all of the lead present in the solid phase.
While the relative proportions of the different lead values in the paste fraction will inevitably vary from time to time, analysis of the paste fraction from time to time will enable the amount of added lead to be so organised that procedure in accordance with equation (3) will result in recovery of the great bulk of the lead values. All that will be lost is any excess of either lead or Pub02, generally the latter, over that which reacts in accordance with equation (3).
The product is an impure aqueous solution of lead nitrate having a pH value of 1-2. Two of the impurities are bismuth and iron, the bismuth being derived from the lead in the batteries and the iron from corrosion of parts of the battery breaking plant. These impurities can be removed by raising the pH of the solution to a value in the range of 3 to 4 by addition of PbO and filtering to remove the compounds of bismuth and iron. The added PbO reacts with excess nitric acid to form lead nitrate and adjustment of the pH value removes dissolved antimony a small amount of which is often present in a lead nitrate solution prepared wholly or in part from grid metal.When reaction of the lead dioxide with nitric acid is effected in the presence of added lead, it may be desirable to oxidize the iron to the ferric state by addition of hydrogen peroxide before adjusting the pH value. Another impurity is copper derived from cable ends, which can be removed by taking advantage of a form of cementation reaction in which a relatively more noble metal is precipitated by a more base metal, in this case metallic lead.
Copper nitrate in solution reacts with lead according to the equation:
Cu (NO3)2+PbeCu+Pb (NO3)2 (4)
Copper can therefore be precipitated as metal by addition of lead, as rolled strip, granules or powder.
Preferably the removal of copper is effected after iron and other elements have been removed by adjustment of the pH of the solution to 3 4; in this pH range the concentration of free acid is too low for any risk of redissolution of copper to exist.
If sodium carbonate is used for desulphation, the lead sulphate is converted into a double salt, lead sodium carbonate, in which some sodium is chemically combined. The final lead nitrate solution accordingly contains some sodium. For many purposes this sodium can be tolerated; if it has to be
removed it is necessary to introduce an extra step in which the desulphated solids are slurried in water and carbon dioxide is passed through before treatment with nitric acid. In Example 8 below, in which the removal of sodium was so carried out, the final solution contained 0.21% of sodium. In example 9, in which sodium was not removed, there was ten times as much.
The purified lead nitrate solution can be concentrated to a desired strength for sale or,
alternatively, the lead nitrate can be recovered as crystals from the solution.
In the following Examples, all parts are by weight unless otherwise stated:~
Example 1
10 g of lead dioxide were stirred with 15 g of granulated lead in 100 cm3 of a 20% (w/v) solution
of nitric acid for 30 minutes at 600. The lead dioxide all dissolved in 30 minutes.
Example 2
A similar reaction mixture to that of Example 1 was stirred at room temperature. A clear solution was produced after 2 hours.
These two examples illustrate only the reaction of lead dioxide with nitric acid in the presence of
lead. Together they show that the reaction is more rapid at elevated temperatures, and in practice it
has been found that in the treatment of actual desulphated battery paste using broken grid metal to
dissolve the lead dioxide the rate of reaction at room temperature is unacceptably low.
Example 3
This example concerns a battery paste fraction containing:~
Total lead 78.5%
Lead as lead sulphate 28.4%
Lead as metal 18.1% Lead as lead dioxide 20.4%
Lead as lead monoxide 11.6%
100 9 of the material was stirred for one hour with a solution of 1 8 g of sodium carbonate in 1 50 cm3 of water, at room temperature. After filtration the solids were slurried in 300 cm3 of water. Nitric acid was added, in the form of the 70% w/w solution (specific gravity 1.42) until the pH was 1.5.The amount required was 22.5 cm3, which corresponds to 22.5 g of anhydrous HN03. It will be noted that this is the approximate equivalent (24.3 g is the calculated equivalent) of those lead compounds, the lead monoxide and the lead carbonate formed from the lead sulphate by the action of the sodium carbonate, that are readily soluble in dilute nitric acid. Next 8.6 g of granulated lead was added to bring the ratio of lead to lead dioxide to 3 parts to 2 by weight, the suspension was warmed to 700, and a further 37.5 g of nitric acid in the form of 37.5 cm3 of the 70% w/w solution were added. After stirring for two hours, no lead dioxide remained. After filtration there were obtained a residue weighing 10 g (dry bases) and a solution containing 81.8 g of lead as nitrate.Allowing for the 8.6 g of added lead, the amount extracted from the battery material was 73.2 g, representing a yield of 93.2%.
Example 4
This example concerns a battery paste fraction containing~ Total lead 72.3%
Lead as lead sulphate 41.6%
Lead as metal 3.2%
Lead as lead dioxide 25.7%
Lead as lead monoxide 1.8% 100 g of material were treated as in Example 3, with the following changes in the amounts of reagents, made to take account of the different composition. The material was desulphated at 250C by stirring for one hour with a solution of 26.5 g of sodium carbonate in 150 cm3 of water. The resulting solids were slurried in water, and the pH brought to 1.5 by adding 32 g of nitric acid in the form of 32 cm3 of the 70% w/w solution (26.4 g constitute the equivalent of the lead sulphate and the lead monoxide contents).The temperature was raised to 700 and stirred for two hours with a further 43 g of nitric acid, added in the form of 43 cm3 of the 70% w/w solution, and 30.8 g of granulated lead. There were produced a residue weighing 6 g and a solution containing 102.7 g of lead as lead nitrate. After allowing for the added lead, the amount of lead extracted from the battery paste fraction was 71.9 g representing an extraction of 99.4%.
Example 5
This example concerns a battery paste fraction containing:~
Total lead 72.7%
Lead as lead sulphate 39.5%
Lead as metal 10.7%
Lead as lead dioxide 11.4% Lead as lead monoxide 11.1% 200 g of this material were stirred for two hours with a solution of 33.6 g of sodium hydroxide in 400 cm2 of water, at room temperature. After filtration the solids were slurried at 600 cm3 of water at 600, and 100 g of nitric acid as HNO, were added, in the form of 100 cm3 of the 70% w/w solution (specific gravity 1.42), followed by 30 cm3 of "100-volume" (30% w/v) hydrogen peroxide. After stirring for 30 minutes, the reaction mixture was filtered and a solution of lead nitrate was produced containing 139.5 g of lead, corresponding to a percentage extraction of 95.9%.
The amount of sodium hydroxide used in this example is 11 0% of the stoichiometric amount required to effect the conversion of lead sulphate to hydrated lead monoxide according to the equation:
PbSO4+2 NaCHoPbO+HzO+Na2 SO4 (5)
Example 6
This example concerns the same battery paste fraction as that used in Example 5 and the experimental conditions were the same except that the amount of sodium hydroxide was reduced to 30.5 g. The final percentage extraction of lead as dissolved lead nitrate was 89.9%.
In this example the amount of sodium hydroxide used was exactly the stoichiometric equivalent of the lead sulphate.
Example 7
This example concerns the same battery paste fraction as that used in Example 5; it illustrates the use of broken grid metal to take up lead dioxide.
200 g of the battery paste fraction was desulphated as described in Example 5 and the solids, after filtration, were slurried in 600 cm2 of water at 700. A total of 25.3 g of broken grid metal fraction containing 90% of lead, was added, together with 125 g of nitric acid in the form of 1 25 cm3 of the 70% wYw solution. The completion of the dissolution of the lead dioxide was indicated by the disappearance of the characteristic dark brown colour of this substance after 12 hours. After a further 30 minutes, the reaction mixture was filtered and a solution of lead nitrate was produced containing 156.7 g of lead. After allowing for 22.8 g introduced by the grid metal fraction the amount of lead extracted from the paste fraction in the form of lead nitrate was 133.9 g, representing a percentage yield of 92.1%.
Example 8
This example describes the whole process, including the purification of the solution, and gives the amounts of typical impurity elements in the product.
1 850 g of battery paste were stirred at room temperature for two hours with 2 litres of water in which were dissolved 390 g of sodium carbonate. The analysis of the battery paste was:~ Total lead 65.7%
Lead as lead sulphate 37.5%
Lead as metal 2.9% Lead as lead dioxide 20.2%
Lead as lead monoxide 5.1%
The desulphated solids were filtered off and reslurried in 2 litres of water. Carbon dioxide was passed through the solution for 41 hours at a rate of 100 cm3 per minute, to free the solids of combined sodium. The solids were filtered off once more.
Two such portions, representing 3700 g of the original paste, were slurried in 5.5 litres of water and reacted first with 800 cm3 of 70% w/w nitric acid corresponding to 800 g of anhydrous nitric acid.
Then 850 kg of broken battery grid alloy containing 94% of lead were introduced, together with a further 1000 cm3 of 70% w/w nitric acid corresponding to 1 kg of anhydrous nitric acid, the temperature was raised to 650C, and the mixture stirred for four hours. A further 2 litres of water were added before filtration. To the filtrate were added 15 cm2 of hydrogen peroxide, to oxidize iron to the tervalent state. The solution was brought to pH 3.5 by the addition of 47 g of lead oxide (litharge), and filtered.
There were finally obtained 7.400 litres of a solution containing 326 g of lead per litre as nitrate.
This was stirred overnight with a small quantity of rolled metallic lead strip to precipitate copper. The solution was then diluted with 0.913 1 of water to provide 8.313 litres of a solution of lead nitrate containing 290 g of lead per litre, equivalent to 463 g of lead nitrate per litre.
Exhaustive washing of the residue produced a further 221 g of lead nitrate in the form of a dilute solution. The filtration residue weighed 1088 g and contained 45.7% of lead.
A mass balance for lead was drawn up as follows:
Input:
3700 g of battery paste at 65.7% 2431 g
850 g of grid metal at 94.0% 799 g
47 g of litharge at 44g 3273 g
Output:
8.313 litres of solution at 290 g 1-' 2411 g
2.980 litres of solution at 74.2 91-1 221 g
1088 g of residue at 45.1% 497 g
unaccounted for 144g 3273 g
The analysis of the solution for impurities was as follows, the figures represent the percentage of impurity element calculated on the contained lead nitrate.
Sodium 0.21 Copper 0.003
Antimony 0.0008 Iron indetectable
Example 9
500 kg of wet battery paste containing 306 kg of dry solids were sieved with water through a 1/8" stainless steel mesh screen and the volume made up to 3000 litres. 28 kg of plastics waste were retained on the screen.
The slurried solids were stirred with 1 50 kg of sodium carbonate. The suspension was centrifuged and yielded 412 kg of solids and 3000 litres of a solution containing 86 kg of sodium sulphate.
The original battery paste contained 215 kg of lead, representing a lead content of 70.3% on the dry solids. Included in this were 26.5% of lead as lead dioxide. The iron content was 0. 1 5%.
The centrifuged desulphated solids were stirred into 2000 litres of water and 240 kg of 60% nitric acid were added. There were next added 25 kg of 27% hydrogen peroxide, 83 kg of 60% nitric acid, and a further 28 kg of 27% hydrogen peroxide. After 13 hours stirring the pH of the solution was raised by 3.0 by the addition of 75 kg of litharge. The reaction mixture was then centrifuged.
This yielded 83 kg of wet centrifuge cake containing 54 kg of dry solids; the lead content was 40.7% based on the dry solids. The liquor contained 419 kg of lead nitrate containing 262 kg of lead in 2990 litres; the sodium and iron contents each expressed as a percentage of the contained lead nitrate were 2.1% and less than 0.002%.
The mass balance for lead was as follows~ Input:
306 kg of dry battery paste solids at 70.3% 215.0 kg
75 kg of litharge 69.6 kg
284.6 kg
Output:
2990 litres of solution at 87.8 g 1-1 262.4 kg
54 kg of dry residue at 40.7% 22.0 kg
unaccounted for 0.2 kg
284.6 kg
The yield of lead nitrate from the battery paste was 89.7%
Example 10
The battery paste fraction used had the composition stated in Examples 5, 6 and 7, namely:
Total lead 72.7%
Lead as lead sulphate 39.5%
Lead as metal 10.7%
Lead as lead dioxide 11.4%
Lead as lead monoxide 11.1%
200 g of the material was stirred for two hours at room temperature with a solution containing 37.5 g of commercial ammonium carbonate and 13 cm3 of ammonia solution (35% w/w NH3) in a total volume of 400 cm3. The solids were filtered off and reacted with nitric acid and hydrogen peroxide as described in Example 5. The final solution contained 137.8 g of lead, corresponding to a percentage extraction of 94.8%.
Example 11
The composition of the battery paste fraction and the conditions of the experiment were as above except that the desulphating solution consisted of 46 cm3 of ammonia solution (35% w/w NH3) diluted with water to 400 cm3. The yield of lead as nitrate was 112.2 g, corresponding to a percentage extraction of 77.2%.
Claims (8)
1. A method of recovering lead as an aqueous solution of lead nitrate from the paste fraction derived from scrap lead batteries, which comprises subjecting the paste fraction to desulphation by treatment with a carbonate or hydroxide of an alkali metal or of ammonium, separating the solid and liquid phases of the reaction product, and then treating the solid phase with nitric acid in the presence of hydrogen peroxide, or in the presence of added lead and at a temperature in the range of 40#900 C, to convert to lead nitrate substantially all of the lead present in the solid phase.
2. A method according to claim 1, wherein the added lead is granulated lead.
3. A method according to claim 1, wherein the added lead is lead derived from broken battery grid.
4. A method according-to any one of the preceding claims, wherein the desulphation treatment is carried out at a temperature in the range of 10-1 000C.
5. A method according to any one of the preceding claims, in which sodium carbonate is used for desulphation and the solid phase is slurried in water and treated with carbon dioxide prior to reaction with nitric acid.
6. A method according to any one of the preceding claims, in which the solution of lead nitrate is purified of bismuth and iron by raising its pH to a value in the range of 3 to 4 by addition of lead monoxide followed by filtration.
7. A method according to any one of the preceding claims, in which the solution of lead nitrate is purified of copper by addition of lead.
8. A method according to claim 1, substantially as described herein with reference to any one of the foregoing Examples 3 to 11.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8110998A GB2073725A (en) | 1980-04-11 | 1981-04-08 | A Method of Recovering Lead Values from Scrap Batteries |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8012128 | 1980-04-11 | ||
| GB8110998A GB2073725A (en) | 1980-04-11 | 1981-04-08 | A Method of Recovering Lead Values from Scrap Batteries |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB2073725A true GB2073725A (en) | 1981-10-21 |
Family
ID=26275154
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB8110998A Withdrawn GB2073725A (en) | 1980-04-11 | 1981-04-08 | A Method of Recovering Lead Values from Scrap Batteries |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB2073725A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0158626A3 (en) * | 1984-04-10 | 1986-08-27 | VOEST-ALPINE Aktiengesellschaft | Process for recovering metals from galvanic waste elements |
| FR2590277A1 (en) * | 1985-11-19 | 1987-05-22 | Tecneco Spa | PROCESS FOR DESULFURIZING THE PASTE FROM SINKED BATTERIES |
| FR2592662A1 (en) * | 1986-01-09 | 1987-07-10 | Tecneco Spa | PROCESS FOR RECOVERING THE CONSTITUENTS OF LEAD BATTERIES |
| EP0313153A1 (en) * | 1987-10-20 | 1989-04-26 | B.U.S. ENGITEC SERVIZI AMBIENTALI S.r.l. | Hydrometallurgical process for recovering in pure metal form all the lead contained in the active mass of exhausted batteries |
| EP0572552A4 (en) * | 1991-02-22 | 1994-01-05 | Nl Industries, Inc. | |
| WO2005007904A1 (en) * | 2003-07-18 | 2005-01-27 | Kandy S. A. | Process for the high yield recovery of lead from spent lead-acid batteries with reduced associated production of slag and gaseous emissions |
| EP1619261A1 (en) * | 2004-07-20 | 2006-01-25 | ENGITEC S.r.l. | Desulfurization process of pastel and grids of lead accumulators |
| CN102352216A (en) * | 2011-08-24 | 2012-02-15 | 浙江天能电池(江苏)有限公司 | Heavy metal lead powder chemical dedusting agent |
| CN110468279A (en) * | 2019-09-09 | 2019-11-19 | 赵坤 | A method of recycling lead from the lead plaster material of waste lead storage battery |
-
1981
- 1981-04-08 GB GB8110998A patent/GB2073725A/en not_active Withdrawn
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0158626A3 (en) * | 1984-04-10 | 1986-08-27 | VOEST-ALPINE Aktiengesellschaft | Process for recovering metals from galvanic waste elements |
| GB2183623B (en) * | 1985-11-19 | 1990-04-11 | Tecneco Spa | Hydrometallurgic process for recovering in the metal form the lead contained in the paste of the exhausted batteries |
| FR2590277A1 (en) * | 1985-11-19 | 1987-05-22 | Tecneco Spa | PROCESS FOR DESULFURIZING THE PASTE FROM SINKED BATTERIES |
| GB2183623A (en) * | 1985-11-19 | 1987-06-10 | Tecneco Spa | Hydrometallurgic process for recovering in the metal form the lead contained in the paste of exhausted batteries |
| FR2592662A1 (en) * | 1986-01-09 | 1987-07-10 | Tecneco Spa | PROCESS FOR RECOVERING THE CONSTITUENTS OF LEAD BATTERIES |
| US4927510A (en) * | 1987-10-20 | 1990-05-22 | Engitec Impianti S.P.A. | Hydrometallurgical process for recovering in pure metal form all the lead contained in the active mass of exhausted batteries |
| EP0313153A1 (en) * | 1987-10-20 | 1989-04-26 | B.U.S. ENGITEC SERVIZI AMBIENTALI S.r.l. | Hydrometallurgical process for recovering in pure metal form all the lead contained in the active mass of exhausted batteries |
| EP0572552A4 (en) * | 1991-02-22 | 1994-01-05 | Nl Industries, Inc. | |
| WO2005007904A1 (en) * | 2003-07-18 | 2005-01-27 | Kandy S. A. | Process for the high yield recovery of lead from spent lead-acid batteries with reduced associated production of slag and gaseous emissions |
| EP1619261A1 (en) * | 2004-07-20 | 2006-01-25 | ENGITEC S.r.l. | Desulfurization process of pastel and grids of lead accumulators |
| US7498012B2 (en) | 2004-07-20 | 2009-03-03 | Engitec S.R.L. | Desulfurization process of pastel and grids of lead accumulators |
| RU2379364C2 (en) * | 2004-07-20 | 2010-01-20 | ЭНДЖИТЕК С.р.л. | Method of sulphur removing of active mass and lead accumulators lattices |
| CN100590930C (en) * | 2004-07-20 | 2010-02-17 | 恩吉泰克有限公司 | Desulfurization process of pastel and grids of lead accumulators |
| CN102352216A (en) * | 2011-08-24 | 2012-02-15 | 浙江天能电池(江苏)有限公司 | Heavy metal lead powder chemical dedusting agent |
| CN110468279A (en) * | 2019-09-09 | 2019-11-19 | 赵坤 | A method of recycling lead from the lead plaster material of waste lead storage battery |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113039295A (en) | Method for extracting metals from lithium ion batteries | |
| US2576314A (en) | Extracting of nickel values from nickeliferous sulfide material | |
| US4412861A (en) | Method for the recovery of uranium values from uranium tetrafluoride | |
| WO1979000142A1 (en) | Uranium recovery from wet process phosphoric acid | |
| CN111926187A (en) | Method for comprehensively recovering selenium, mercury, lead and silver from acid sludge | |
| GB2073725A (en) | A Method of Recovering Lead Values from Scrap Batteries | |
| US4247522A (en) | Method of purifying uranium tetrafluoride hydrate and preparing uranium (VI) peroxide hydrate using a fluoride precipitating agent | |
| US2733126A (en) | Ukanium liberation | |
| US4071422A (en) | Process for concentrating and recovering gallium | |
| US5840262A (en) | Process for the manufacture of pure lead oxide from exhausted batteries | |
| US3658464A (en) | Molybdenum oxide refining process | |
| CN111235396B (en) | Wet processing method for copper smelting acid making sludge | |
| US4689178A (en) | Method for magnesium sulfate recovery | |
| US3677700A (en) | Process for producing battery-grade manganese dioxide | |
| JP2004182533A (en) | Cobalt recovery method | |
| US4043804A (en) | Recovery of metal values from copper reverberatory slag | |
| US3087786A (en) | Preparation of high purity vanadium pentoxide from oxidic vanadium materials | |
| EP0846656A1 (en) | Process for regenerating sodium sulphide from the sodium sulphate which forms in treating lead paste from exhausted batteries | |
| US4258012A (en) | Method of purifying uranium tetrafluoride hydrate and preparing uranium (VI) peroxide hydrate using a fluoride complexing agent | |
| US3007770A (en) | Extraction of lithium | |
| CA2222639C (en) | Metal and fluorine values recovery from fluoride salt matrices | |
| US5516496A (en) | Metal and fluorine values recovery from fluoride salt matrices | |
| US3740199A (en) | Ore separation process | |
| US2780519A (en) | Recovery of uranium from ores | |
| JPS5924731B2 (en) | Method for removing and recovering uranium or/and thorium from a liquid containing uranium or/and thorium |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| WAP | Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1) |