US558240A - Method of utilizing saline solutions - Google Patents

Method of utilizing saline solutions Download PDF

Info

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
Application number
Publication date
Application granted granted Critical
Publication of US558240A publication Critical patent/US558240A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00Regeneration of pulp liquors or effluent waste waters
    • D21C11/12Combustion 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.

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,
US558240D Method of utilizing saline solutions Expired - Lifetime US558240A (en)

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
US (1) US558240A (en)

Similar Documents

Publication Publication Date Title
US3698995A (en) Digestion and bleaching of wood pulp followed by recovery of chemicals and countercurrent flow of wash water
US2308564A (en) Recovery of cellulose and lignin from wood
US3833462A (en) Process of removing sodium chloride from kraft pulping process chemical recovery systems
US558240A (en) Method of utilizing saline solutions
US558241A (en) Charles n
US3453174A (en) Pulping and bleaching process wherein effluent liquor from alkaline extraction of bleached pulp is used to dissolve smelt
US2828253A (en) Process of digesting fibrous plant material
US2743220A (en) Method of recovering cellulose
US4131508A (en) Recovery system for oxygen bleaching of pulp
US1879503A (en) Method of relieving alkaline solutions, particularly waste liquors from the soda or sulphate pulp manufacture, of silica
US1557338A (en) Method of producing half stuffs and cellulose
CN104854263B (en) With the method and its electrolysis unit of polysulfide production-scale cell continuous electrolysis
US2381369A (en) Processes for separation of asbestos fiber from associated solids
US3578553A (en) Nitrogen dioxide pulping process
CN101608411B (en) Process for manufacturing paper pulp by using oxidation-reduction potential water and biological enzyme
CN104088184A (en) Pulp washing auxiliary agent and pulping process
US775829A (en) Production of paper-pulp.
US1062016A (en) Process of precipitating ulmic compounds from the black liquors of soda pulp-mills.
CN116065414B (en) Circulation digestion method for recovering lignin and alkali from black liquor of paper mill without lime treatment
US1620938A (en) Altering viscosity of cellulose-containing materials
US1742218A (en) Process for the production of high alpha cellulose fiber
CN102212974A (en) Method for producing dissolving pulp
Pomilio Gas Chlorination on Cellulose Manufacture
US331323A (en) Baoul piebee pictet
US1780347A (en) Process of manufacturing alpha cellulose