US558240A - Method of utilizing saline solutions - Google Patents
Method of utilizing saline solutions Download PDFInfo
- Publication number
- US558240A US558240A US558240DA US558240A US 558240 A US558240 A US 558240A US 558240D A US558240D A US 558240DA US 558240 A US558240 A US 558240A
- Authority
- US
- United States
- Prior art keywords
- solution
- caustic
- saline solutions
- cell
- chlorid
- 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
- 239000011780 sodium chloride Substances 0.000 title description 24
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 title description 10
- 239000003518 caustics Substances 0.000 description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 18
- 239000000835 fiber Substances 0.000 description 14
- 150000003839 salts Chemical class 0.000 description 14
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 12
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 12
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 12
- 241000565357 Fraxinus nigra Species 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 8
- 229920002522 Wood fibre Polymers 0.000 description 6
- 235000012255 calcium oxide Nutrition 0.000 description 6
- 239000000292 calcium oxide Substances 0.000 description 6
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000002025 wood fiber Substances 0.000 description 6
- 238000009835 boiling Methods 0.000 description 4
- 239000000344 soap Substances 0.000 description 4
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- WGSLWEXCQQBACX-UHFFFAOYSA-N Chlorin Chemical compound C=1C(C=C2)=NC2=CC(C=C2)=NC2=CC(C=C2)=NC2=CC2=NC=1CC2 WGSLWEXCQQBACX-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000003247 decreasing Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920000591 gum Polymers 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/12—Combustion of pulp liquors
Definitions
- the black ash which results from the roasting contains salt and the carbonate of soda and some impurities-such as coal, tarry matters, and the like. ably treat this ash by lixiviating with a limited amount of water, which results in the removal of the larger proportion of the carbonate of soda. The latter being more soluble than the salt will go into solution first. The salt and the remainder of the carbonate of soda containing the tarry matters, &c., are then dissolved and enough quicklime is added to causticize the carbonate of soda.
- the resulting dirty solution is then run into the cathode side of the electrolytic cell and reelectrolyzed until there is again produced in it such a percentage of the hydrate or caustic as will interfere with the efficient and economic working of the cell by decreasing the efficiency of the current beyond the economic limit.
- the dirty solution referred to should be used only on the cathode side of the cell, since the presence in the anode-compartment of the cell of a small percentage of caustic and of the tarry matters would destroy the efficient Working of the cell.
- the chlorid if the chlorid of sodium be employed, can be used up entirely, only enough salt being added to make up for soda lost in the fiber from imperfect Washing, With out any loss of efiiciency in the electrolysis and With no Waste of salt.
Landscapes
- Paper (AREA)
Description
UNITED STATES PATENT OFFICE.
CHARLES N. IVAITE, OF RUMFORD, MAINE, ASSIGNOR TO THE ELECTRO- CHEMICAL OOMPANY, OF RUMFORD FALLS, MAINE.
METHOD OF UTILIZING SALINE SOLUTIONS.
SPECIFICATION forming part of Letters Patent No. 558,240, dated April 14, 1896.
Application filed March 19, 1894. Serial No. 504,242. (No specimens.)
To all whom it may concern.-
Be it known that I, CHARLES N. WAITE, a citizen of the United States, residing at Rumford, in the county of Oxford and State of Maine, have invented certain new and useful Improvements in Methods of Utilizing Saline Solutions, of which the following is a specification.
My invention has for its object an improved method for the utilization of saline solutions. It is fully set forth in the following description, and its novel features are pointed out in the claim which is appended hereto.
In the production of chlorin and of caustic by the electrolysis of a chlorid of an alkaline base the solution of chlorid is subjected in an electrolytic cell to the action of an electric current until the efficient working of the electrolytic cell is interfered with by the presence of such a percentage of the hydrate or caustic as will decrease the efficiency of the current beyond the limit at which the cell may be economically operated. \Vhen this occurs, the solution in the compartment of the cell is removed and new solution supplied. The solution removed has lost only about onethird of the chlorid, and thus there occurs aloss of a considerable portion of chlorid which cannot be economically employed in the cell owing to the presence of the hydrate or caustic.
In the production of chemical fiber which is employed in the manufacture of paperthe wood fibers or chips are boiled in a digester with the liquor containing caustic in solution. As a result of this treatment the gum and resin in the wood are converted into a soap and the fiber is left free. The fiber is then removed and the soap liquor containing the excess of caustic is evaporated and roast-ed in a rotary furnace, yielding black ash, which is recausticized with quicklime and used over and over again, enough efficient caustic being added to make up for the loss in recovery.
By means of my process I utilize the solution which is drawn from the cathode-coinpartment of an electrolytic cell, and which contains, as above stated, the chlorid of the alkaline base and a considerable percentage (usually six to eight per cent.) of the hydrate of the base, by employing the said solution for the treatment of the wood fiber in the digesters in the production of chemical fiber. The presence in this solution of the chlorid, ordinarily chlorid of sodium, does not interfere with the use of the solution for this purpose. After the wood fiber has been boiled in this solution from the cathode-compartment of the electrolytic cell the fiber is Washed and the soapy liquor containing salt and the excess of caustic is evaporated and the residuum roasted. The black ash which results from the roasting contains salt and the carbonate of soda and some impurities-such as coal, tarry matters, and the like. ably treat this ash by lixiviating with a limited amount of water, which results in the removal of the larger proportion of the carbonate of soda. The latter being more soluble than the salt will go into solution first. The salt and the remainder of the carbonate of soda containing the tarry matters, &c., are then dissolved and enough quicklime is added to causticize the carbonate of soda. The resulting dirty solution is then run into the cathode side of the electrolytic cell and reelectrolyzed until there is again produced in it such a percentage of the hydrate or caustic as will interfere with the efficient and economic working of the cell by decreasing the efficiency of the current beyond the economic limit. The dirty solution referred to should be used only on the cathode side of the cell, since the presence in the anode-compartment of the cell of a small percentage of caustic and of the tarry matters would destroy the efficient Working of the cell.
Instead of lixiviating the black ash to remove the greater portion of the carbonate of soda I may omit this step and instead dissolve the whole of the black ash, adding to the solution quicklime to causticize the carbonate and then proceeding as above described. By proceeding, however, without lixiviating the black ash a larger amount of caustic will be present in the dirty solution which is used in the cathode-compartment of the cell and less work can be done before it becomes necessary to draw off the caustic, for reasons stated above. Whenin the operation of the electrolytic cell the solution in the cathode-compartment again contains a sufficient percentage of the hydrate to interfere I now preferwith the working of the cell, the liquor is again used in the digesters for the treatment of fiber and the process is repeated. By this method the chlorid, if the chlorid of sodium be employed, can be used up entirely, only enough salt being added to make up for soda lost in the fiber from imperfect Washing, With out any loss of efiiciency in the electrolysis and With no Waste of salt.
In some localities Where paper-making is carried on salt is expensive, and in such 10- calities my process is particularly desirable and effects a considerable saving.
What I claim is- That improvement in the utilization of saline solutions which consists in subjecting the solution to electrolysis in an electrolyticcell,
Publications (1)
Publication Number | Publication Date |
---|---|
US558240A true US558240A (en) | 1896-04-14 |
Family
ID=2626969
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US558240D Expired - Lifetime US558240A (en) | Method of utilizing saline solutions |
Country Status (1)
Country | Link |
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US (1) | US558240A (en) |
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0
- US US558240D patent/US558240A/en not_active Expired - Lifetime
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