US558241A - Charles n - Google Patents

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US558241A
US558241A US558241DA US558241A US 558241 A US558241 A US 558241A US 558241D A US558241D A US 558241DA US 558241 A US558241 A US 558241A
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solution
cell
caustic
chlorid
fiber
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    • 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 wood fibers or chips are boiled in a digester with liquor containing caustic in solution.
  • 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.
  • salt and the carbonate of soda and some impurities such as coal, tarry matters, and the like.
  • I now 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 causticise the carbonate of soda.
  • the resulting dirty solution is then run into the cathode side of the electrolytic cell and subjected to electrolytic action 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 in the cathode side of the cell,
  • the chlorid if 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 without any loss of efliciency in the electrolysis and with no Waste of salt.
  • My process is particularly desirable in localities 'where paash, then lixiviating to remove a portion of the carbonate from the ash, then dissolving the residuum eausticizing it with quicklime and subjecting it to electrolytic action in the cathode-compartment of an electrolytic cell, substantially as described.

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Description

UNITED STATES PATENT OFFICE CHARLES N. IVAITE, OF RUMFORD FALLS, MAINE, ASSIGNOR TO THE ELECTROCHEMICAL COMPANY, OF SAME PL ACE.
METHOD OF UTILIZING SALINE SOLUTIONS.
SPECIFICATION forming part of Letters Patent No. 558,241, dated April 14, 1896.
Application filed October 5, 1895. $erial No. 564,800. N p im n To all whom it may concern.-
Be it known that 1, CHARLES N. WAITE, a citizen of the United States, residing at Rumford Falls, 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. I
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. WVhen this occurs, the solution in the cathode-compartment of the cell is removed and new solution supplied. The solution removed has lost only about one-third of the chlorid, and thus there occurs a loss 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 paper, the wood fibers or chips are boiled in a digester with 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 soapy liquor containing the excess of caustic is evaporated and roasted in a rotary furnace, yielding black ash, which is recausticised 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-compartment of an electrolytic cell and which contains, as above stated, the chlorid of the alkaline base and a considerable percentageusually from six toIeight 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 chloridordinarily 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. I now 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 causticise the carbonate of soda. The resulting dirty solution is then run into the cathode side of the electrolytic cell and subjected to electrolytic action 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 in the cathode side of the cell,
since the presence in the anode-compartment of the cell of a small percentage of caustic and 0f the tarry matters would destroy the efficient working of the cell. When in the operation of the electrolytic cell the solution in the cathode-compartment again contains a sufficient percentage-of the hydrate to interfere with 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 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 without any loss of efliciency in the electrolysis and with no Waste of salt. My process is particularly desirable in localities 'where paash, then lixiviating to remove a portion of the carbonate from the ash, then dissolving the residuum eausticizing it with quicklime and subjecting it to electrolytic action in the cathode-compartment of an electrolytic cell, substantially as described.
In testimony whereof I affix my signature in presence of two Witnesses.
CHARLES N. \VAITE.
\Vitnesses:
GEORGE D. BIsBEE, RUSSELL II. DEARBORN.
US558241D Charles n Expired - Lifetime US558241A (en)

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