US958986A - Process of regenerating stannic-chlorid solutions. - Google Patents
Process of regenerating stannic-chlorid solutions. Download PDFInfo
- Publication number
- US958986A US958986A US49910709A US1909499107A US958986A US 958986 A US958986 A US 958986A US 49910709 A US49910709 A US 49910709A US 1909499107 A US1909499107 A US 1909499107A US 958986 A US958986 A US 958986A
- Authority
- US
- United States
- Prior art keywords
- stannic
- solution
- weakened
- chlorid
- tin
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 10
- 230000001172 regenerating effect Effects 0.000 title 1
- 239000000243 solution Substances 0.000 description 21
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 20
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 14
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 12
- 235000011941 Tilia x europaea Nutrition 0.000 description 12
- 239000004571 lime Substances 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- 239000007864 aqueous solution Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000004043 dyeing Methods 0.000 description 5
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- -1 that is Inorganic materials 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
Definitions
- the lime present in the weakened bath comes chiefly from the water that is drawn into the bath by the silk, while the lead is dissolved from the walls of the apparatus containing the stannic chlorid bath used in the process.
- the lead is present in considerable quantities after the bath has been used for a long period of time, as it has been found that lead is quite soluble in dilute solutions of stannic chlorid, although it is absolutely in- Specification of Letters Patent.
- the amount of lime in the weakened stannic chlorid solution is, according to my method, first determined quantitatively by analysis of the solution.
- an amount of sulfuric acid calculated according to the amount of lime present in the bath, all the limo will be precipitated in the form of calcium sulfate, together with the lead.
- the chief impurities in the weakened stannic chlorid solution are eliminated, and the weakened solution after settling and filtration is then in condition for concentration.
- the concentration of the weakened solution is then effected in the manner before stated by the addition of anhydrous tetrachlorid of tin, up to about 60 B.
- anhydrous tetrachlorid of tin up to about 60 B.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Removal Of Specific Substances (AREA)
Description
UNITED STATES PATENT OFFICE.
JOSEF WEBER, OF ESSEN-ON-THE-RUHR, GERMANY.
PROCESS OF REGENERATING STANNIC-GHLORID SOLUTIONS.
No Drawing.
solution of stannic chlorid that has been used as a bath for a considerable period of time in silk dyeing and has become so loaded with impurities, especially lime and lead, as to be unfit for further use while in that condition.
In the art of silk dyeing as practiced for many years, it has been customary to employ baths containing solutions of stannic chlorid of from 20 to 30 Be. for the purpose of weighting the silk. After the baths had been used for a considerable period of time and had become weakened by the passage through them of a predetermined quantity of silk it was formerly the practice to restore them to working condition by adding a concentrated solution of stannic chlorid of 50 to Be. This method of concentrating a weakened solution of stannic chlorid has, however, been superseded by the use of anhydrous tetrachlorid of tin. It is now the practice to transfer a part of the weakened solution from the bath to another vessel, for example, an enameled receptacle, and concentrate it, while in such vessel, up to 50 to 60 Be. by adding a suitable quantity of anhydrous tetraehlorid of tin. I have frequently observed that during the concentration of such a weakened solution by the addition of the anhydrous tetrachlorid a precipitate is formed. Numerous analyses have shown that this precipitate consists of chlorid of load, sulfate of lead and calcium sulfate, that is, gypsum.
The lime present in the weakened bath comes chiefly from the water that is drawn into the bath by the silk, while the lead is dissolved from the walls of the apparatus containing the stannic chlorid bath used in the process. The lead is present in considerable quantities after the bath has been used for a long period of time, as it has been found that lead is quite soluble in dilute solutions of stannic chlorid, although it is absolutely in- Specification of Letters Patent.
Application filed May 29, 1909.
Patented May 24:, 1910.
Serial No. 499,107,
soluble in a concentrated solution of stannic chlorid. The silk treated by such a weakened solution of stannic chlorid contaminated with considerable quantities of lime is very injuriously affected by both of these impurities, and especially by the lead, which destroys or seriously impairs the luster and touch of the silk. Because of this it has been customary to renew the baths that become weakened by long use and to recover the tin content from the solution that is removed from the apparatus.- This recovery of the tin has been effected by transforming the stannic chlorid of the weakened bath into oxid of tin; but the process involves a large financial loss, the main elements of which are the cost of converting the tin from one form into another and the reduced value of the oxid of tin in this form as compared with that of stannic chlorid and of tin itself. I have found that all of this loss that has resulted from the removal of weakened solutions of stannic chlorid from the baths and their transformation into oXid of tin can be entirely avoided, and that the weakened stannic chlorid solution can be concentrated and used in a continuous silk treating process without converting it into any other form of tin. In order to accomplish this result it is necessary first to determine quantitatively the principal impurities in the weakened stannic chlorid solution, and then to precipitate them out by means of a suitable reagent, after which the weakened solution from which such impurities have been eliminated may be concentrated and used again.
The amount of lime in the weakened stannic chlorid solution is, according to my method, first determined quantitatively by analysis of the solution. As a result of numerous experiments I have found that by adding to the weakened stannic chlorid solution of the bath an amount of sulfuric acid calculated according to the amount of lime present in the bath, all the limo will be precipitated in the form of calcium sulfate, together with the lead. By the addition of the exact amount of sulfuric acid necessary to precipitate all the lime in the bath the chief impurities in the weakened stannic chlorid solution are eliminated, and the weakened solution after settling and filtration is then in condition for concentration. The concentration of the weakened solution is then effected in the manner before stated by the addition of anhydrous tetrachlorid of tin, up to about 60 B. By this process the tin content of the bath is maintained at all times in the form of stannic chlorid, the impurities removed by precipitation after determination of the quantities present, and the bath restored to Working condition by the mere addition of the proper amount of the anhydrous tetrachlorid, thus making it possible in a continuous process to utilize all the tin in the baths for Weighting the silk.
lVhat I claim is:
1. The process of purifying an aqueous solution of stannic ohlorid that has been contaminated With lime by use in silk dyeing, which consists in adding to said aqueous solution a suflioient amount of sulfuric acid to precipitate all the lime content.
2. The process of purifying an aqueous solution of stannic chlorid that has been contaminated with lime and lead by use in silk dyeing, Which consists in adding to said aqueous solution a sufficient amount of sulfuric acid to precipitate all the lime and lead contents.
3. The process of purifying and concentrating an aqueous solution of stannic chlorid that has been contaminated With lime and lead by use in silk dyeing, Which consists in first adding to said aqueous solution a suflicient amount of sulfuric acid to precipitate all the lime and lead content, and afterward suitably concentrating said purified solution by adding anhydrous tetrachlorid of tin.
JOSEF VEBER. [L. s] lVitnesses: v
OTTO KoNIG,
C. J. WRIGHT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US49910709A US958986A (en) | 1909-05-29 | 1909-05-29 | Process of regenerating stannic-chlorid solutions. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US49910709A US958986A (en) | 1909-05-29 | 1909-05-29 | Process of regenerating stannic-chlorid solutions. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US958986A true US958986A (en) | 1910-05-24 |
Family
ID=3027388
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US49910709A Expired - Lifetime US958986A (en) | 1909-05-29 | 1909-05-29 | Process of regenerating stannic-chlorid solutions. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US958986A (en) |
-
1909
- 1909-05-29 US US49910709A patent/US958986A/en not_active Expired - Lifetime
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2721562A (en) | Pickling and pickling agent regeneration apparatus | |
| US4349514A (en) | Process for recovery of reusable chromic acid from the waste chromic acid solution containing impurities | |
| US3860419A (en) | Process for the recovery of molybdenum from roasted molybdenum concentrates | |
| US6592830B1 (en) | Treating niobium and or tantalum containing raw materials | |
| CA2139642A1 (en) | Recovery of metal values from process residues | |
| JPS60103028A (en) | Treatment of iron or zinc-containing waste hydrochloric acid | |
| WO2019077302A1 (en) | Polyferric sulphate solution | |
| KR930009915A (en) | Recovery of sulfuric acid from spent sulfuric acid containing metal sulfate | |
| US2423385A (en) | Process of pickling and of recovering pickling agent | |
| US2662812A (en) | Regeneration of spent pickle liquor and recovery of ferrous sulfate monohydrate | |
| US3687828A (en) | Recovery of metal values | |
| US4524001A (en) | Method of purifying uraniferous aqueous solutions | |
| US2812232A (en) | Prevention of scale formation in uranium solvent extractor | |
| US2462499A (en) | Process for recovering manganese values from manganese ores | |
| US3816593A (en) | Method of regenerating waste pickle liquor | |
| US2797143A (en) | Uranium-vanadium recovery and separation by phosphate precipitation | |
| US1471514A (en) | Process for the extraction of metals from ores | |
| US2258310A (en) | Treatment of spent pickle liquor or the like | |
| NO131895B (en) | ||
| US4036941A (en) | Preparation of ferric sulfate solutions | |
| US3397130A (en) | Process for manganese recovery from leach solutions | |
| DE3012246A1 (en) | Recovering iron from organic extractant soln. - by redn., then washing with water or aq. acid | |
| US3434797A (en) | Process for treatment of hydrochloric acid waste pickle liquor | |
| DE1091590B (en) | Process for refining ferro-silicon and silicon | |
| US2963343A (en) | Method of separating molybdenum and tungsten values from leach liquors |