Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
200 words
THE PROCESS FOR EXTRACTING ZINC FROM IRON CONTAINING ZINCIFEROUS MINERAL SULPHIDES WHICH COMPRISES THE STEPS OF DISPERSING FINELY DIVIDED IRON CONTAINING ZINCIFEROUS SULPHIDES IN AN AQUEOUS SULPHUR ACID SOLUTION TO FORM A SLURRY; ADJUSTING THE RELATIVE AMOUNTS OF ACID AND SAID SULPHIDES IN THE SLURRY SUCH THAT THERE IS AT LEAST SUFFICIENT ACID PRECENT TO COMBINE WITH THE ZINC CONTENT OF SAID SULPHIDES AS ZINC SULPHATE, PROVIDING IN SAID SLURY AN EFFECTIVE AMOUNT OF A SURFACE ACTIVE COMPOUND COMPATIBLE WITH THE ACID SULPHATE LEACH SOLUTION WHICH IS OPERATIVE, UNDER THE REACTION CONDITIONS OF THE FOLLOWING OXHGEN REACTION STEP, TO RENDER SAID SULPHIDES WETTABLE BY AQUEOUS ACID SOLUTION IN PREFERENCE TO MOLTEN SULPHUR, REACTING THE SLURRY WITH FREE OXYGEN BEARING GAS IN A CLOSED REACTION VESSEL AT A TEMPERATURE ABOVE THE MELTING POINT OF SULPHUR BUT BELOW THAT TEMPERATURE AT WHICH ANY SUBSTANTIAL PORTION OF THE SULPHIDE SULPHUR IS OXIDIZED TO SULPHATE FORM, CONTINUING SAID REACTION WITH ACTIVE AGITATION TO EFFECT SUBSTANTIALLY COMPLETE EXTRACTION OF ZINC VALUES FROM SAID SULPHIDES AS SOLUBLE ZINC SULPHATE WITH CONCURRENT CONVERSION OF SULPHIDE SULPHUR ASSOCIATED WITH SAID ZINC VALUES TO ELEMENTAL FROM, AND SEPARATING PRODUCT LEACH SOLUTION CONTAINING DISSOLVED ZINC VALUES FROM THE UNDISSOLVED RESIDUE.
Claim 2
Dependent Claim
200 words
THE PROCESS FOR EXTRACTING ZINC FROM IRON CONTAINING ZINCIFEROUS MINERAL SULPHIDES WHICH COMPRISES THE STEPS OF DISPERSING FINELY DIVIDED IRON CONTAINING ZINCIFEROUS SULPHIDES IN AN AQUEOUS SULPHUR ACID SOLUTION TO FORM A SLURRY; ADJUSTING THE RELATIVE AMOUNTS OF ACID AND SAID SULPHIDES IN THE SLURRY SUCH THAT THERE IS AT LEAST SUFFICIENT ACID PRECENT TO COMBINE WITH THE ZINC CONTENT OF SAID SULPHIDES AS ZINC SULPHATE, PROVIDING IN SAID SLURY AN EFFECTIVE AMOUNT OF A SURFACE ACTIVE COMPOUND COMPATIBLE WITH THE ACID SULPHATE LEACH SOLUTION WHICH IS OPERATIVE, UNDER THE REACTION CONDITIONS OF THE FOLLOWING OXHGEN REACTION STEP, TO RENDER SAID SULPHIDES WETTABLE BY AQUEOUS ACID SOLUTION IN PREFERENCE TO MOLTEN SULPHUR, REACTING THE SLURRY WITH FREE OXYGEN BEARING GAS IN A CLOSED REACTION VESSEL AT A TEMPERATURE ABOVE THE MELTING POINT OF SULPHUR BUT BELOW THAT TEMPERATURE AT WHICH ANY SUBSTANTIAL PORTION OF THE SULPHIDE SULPHUR IS OXIDIZED TO SULPHATE FORM, CONTINUING SAID REACTION WITH ACTIVE AGITATION TO EFFECT SUBSTANTIALLY COMPLETE EXTRACTION OF ZINC VALUES FROM SAID SULPHIDES AS SOLUBLE ZINC SULPHATE WITH CONCURRENT CONVERSION OF SULPHIDE SULPHUR ASSOCIATED WITH SAID ZINC VALUES TO ELEMENTAL FROM, AND SEPARATING PRODUCT LEACH SOLUTION CONTAINING DISSOLVED ZINC VALUES FROM THE UNDISSOLVED RESIDUE.
Claim 3
Dependent Claim
36 words
The process according to claim 1 wherein the leached slurry is treated with oxygen and an acid neutralizing reagent to lower the free acid content thereof to about 1.5 g.p.l. and to precipitate dissolved iron therefrom.
Claim 4
Dependent Claim
16 words
The process according to claim 2 wherein the acid neutralizing reagent is calcined zinc sulphide concentrate.
Claim 5
Dependent Claim
27 words
The process according to claim 3 wherein the calcined zinc sulphide concentrate is added to the leach end slurry prior to its discharge from the reaction vessel.
Claim 6
Dependent Claim
27 words
The process according to claim 1 wherein said surface active compound is at least one member of the group consisting of lignins, lignosulphonates, tannins and alkylaryl sulphonates.
Claim 7
Dependent Claim
22 words
The process according to claim 5 wherein from about 0.1 to about 1.0 g.p.l. of said compound is added to said slurry.
Claim 8
Dependent Claim
61 words
The process according to claim 1 wherein the acid to zinc Molar ratio in said slurry is adjusted to between about 1.0:1 and about 1.2:1 and said reaction with free oxygen bearing gas is carried out at a temperature within the range of about 125*C. to about 175*C. under an oxygen partial pressure between about 5 p.s.i. and about 100 p.s.i.
Claim 9
Dependent Claim
35 words
The process according to claim 7 wherein the acid to zinc molar ratio is maintained at about 1.1:1, the temperature at about 150*C. and the oxygen partial pressure between about 25 and about 50 p.s.i.
Claim 10
Dependent Claim
13 words
The process according to claim 5 wherein said surface active compound is quebracho.
Claim 11
Dependent Claim
14 words
The process according to claim 5 wherein said surface active compound is calcium lignosulphonate.
Claim 12
Dependent Claim
14 words
The process according to claim 5 wherein said surface active compound is sodium lignosulphonate.
Claim 13
Dependent Claim
14 words
The process according to claim 5 wherein said surface active compound is ammonium lignosulphonate.
Claim 14
Dependent Claim
16 words
The process according to claim 5 wherein said surface active compound is an arylalkyl sodium sulphonate.
Claim 15
Dependent Claim
29 words
The process according to claim 1 wherein the dissolved zinc is recovered from the leach solution by electrolysis and the electrolysed solution is recycled to the slurry forming step.