US1633733A - Process and apparatus for manufacturing ground-wood pulp - Google Patents

Process and apparatus for manufacturing ground-wood pulp Download PDF

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US1633733A
US1633733A US43596A US4359625A US1633733A US 1633733 A US1633733 A US 1633733A US 43596 A US43596 A US 43596A US 4359625 A US4359625 A US 4359625A US 1633733 A US1633733 A US 1633733A
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liquor
pulp
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extractives
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Jr Frederick K Fish
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/06Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods
    • D21B1/063Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by dry methods using grinding devices
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T24/00Buckles, buttons, clasps, etc.
    • Y10T24/21Strap tighteners
    • Y10T24/2143Strap-attached folding lever
    • Y10T24/2155Jewelry-watch straps

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  • FREDERICK K FISH, m, 01' m M61800, CAIJJ'OBYIA.
  • This invention relates toa-process and apparatus for manufacturing ground wood 11] p Iii the manufacture of paper pulp, I have found that unusual results can be obtained by the employmentof liquor previously used in digesting and cooking the'pul'p, the resinous and solvent const tuents with which this li uor. is charged, apparently-serving to attaiik and-otherwiseact on like constituents and on the fiber material'to greatly disintegrate the fibers and im rovetheir condition for pulp purpose. lthout attempting a full explanation as to how or why reuse of the digesting liquor brings about such favorable results, I may say without contradiction that the fact remainsthat there is an action.
  • Another o bject 'of'this invention is to rovide a process-for:'treatingjthe logs Iw ile and previous" to grinding-with a liquor charged with dissolved solvent extractives from wood to soften, saturate,-and penetrate, the fibers to "insure of longer and stronger fibers in'the final product, hence a better and-stronger product.
  • Another objectof the invention is the provision of means for introducing liquor charged with dissolved solvent extractives from wood into the individual fibers at the point of se aration from the log, so that they
  • the invention also comprehends improvements in the construction "and arrangement of parts, and steps in the process, which will be hereinafter described and particularly pointed out in the claims.
  • a pipe 9 cominunicates with the bottom of tank 3,, and it is provided with a valve 10 and communicates with the exhaust side of a pump 11, the opposite side of which is connected with a pipe 12 which leads to the bottom of the magazine in close proximity to the periphery of the grinding stone 2, as shown at 12.
  • This polnt of communication 12 of pipe 12 with the magazine is so located that excess liquor from the sprays-and what may be squeezed from the pulp in the rotation of the stone and the logs is withdrawn from the magazine before it passes out of the magazine and becomes mixed with the pump and dischar ed therewith into the grinder pit. While have shown but one such connection, it is obvious that I may withdraw this excess liquor at several points to accomplish this end.
  • a valved steam inlet pipe 13 is provided at one or more points at the lower portion of the magazine above the pulp forming zone, to admitsufiicient steam to maintain and increase the temperature'of the liquid.
  • wood in the form of logs, is fe into the magazine and supported on the stone which forms a bottom.
  • One or more of the valves 8 are opened, depending on the height of logs in the magazine, and water previously heated b steam passed throu h pipe 4, and preferably primarily charged with solvent extractives and stored in tank 3, under pressure, is s rayed through pipes 7 to-the wood.
  • the temperature of the spray of liquor on the logs while-in the magazine may be regulated by passing steam through pipe 13, which with the heat in the liquor and the continued movement of the logs causes vapor and gases formed by the dissolved constituents in the logs to rise in the magazine and around the logs.
  • vapors condense and the liquor. of condensation accumulates in the bottom of the magazine, but as stated, care must be taken to avoid too much of the liquor in the grinding zone.
  • the vapors, consequently the liquor become surcha-rged with the extractives and constituents liberated from the logs.
  • the constituents in the logs are attacked and acted upon by like constituents which better prepares the wood for the grinding action, and leads to a definite and defined separation of the fibers,
  • the liquor accumulates at the bottom of the magazine and is drawn through ipe 12', by 11 to the tank 3 and is t ere reheate is liquor may be continuously or periodically umped, but in any event, it is continuous y surcharged with the extractives and constituents liberated in the magazine, so that in'the continued operation of the pump, the spray, heat, and the contained wood constituents in the liquor softens, dissolves, and removes, portions of the encrusting material'of the wood fiber and thus prepares the wood for efiicient economical grindin 7 Steam may be admitted to the ma azine from time to time, through the valve pipe 13, which will discharge into the magazine at a point or points best ada ted to secure the required temperature in t e charge, but
  • valve 10 In order to prevent the accumulation of too great a quantity of liquor in the product produced, the valve 10 is opened and the operation of the pump 11 is regulated through the medium of the valve 10 to withdraw liquor from the magazine and return it to the tank 3 where it may be reheated to the required point by the admission of steam to the tankthrough the valved pipe 4. By withdrawing the excess liquor in this manner and returnin it directly for reuse, its heat and containe extractive properties are conserved.
  • the remaining liquor containing solvent extractives in the magazine at the grinding zone acts on the fibers as they are separated at the stone and so affects the encrusting materials of the wood, as to produce from the treated product a whiter and more desirable pulp.
  • An important characteristic of the improved process is that the wood is subjected to the action of the charged liquor in advance of the grinding zone, so that the function of the solvents in the liquor is of gradually increasing effect toward the grind ng zone, with its maximum effect at "the point where the fibers are separated--that is at the grinding'zone.
  • the li uor, 1nc1 dent to its being charged with tie extractives of the wood being treated is of gradually-increasing strength toward the inding zone, and hence its maximum e ect is had at that point where the wood is most susceptible to the treatment, that is where i the fibers are separated one from the other.
  • the product is given the maximum treatment in gradually-increasing steps from the initial spraying to the grinding point, thus insuring the most effective separation and treatment of the fibers.
  • Apparatus as defined in claim 2 having means for returning the mid withdrawn liquor to the grinder for reuse.
  • Apparatus as defined in claim 2 having means for returning said withdrawn liquor to the grinder for reuse, and means for heating said liquor during circulation.
  • a process of making ground wood pulp in a magazine grinder the step which consists in subjecting the wood in said grinder to the action of water and steam to heat and soften the Wood and withdrawing excess water before it becomes mixed with the pulp in the grinder it.
  • a process of making ground wood pulp consisting in spraying the wood before and during the grinding period with preheated water charged with extractives from wood to soften and impregnate the wood with moisture and extractives to thereby prepare the wood for grinding and at the same time release contained extractives, the released extractives being intermixed with the water to enrich the same, withdrawing a substantial proportion of the excess water charged with extractives above the actual grinding point, and recharging the grinder with the withdrawn water charged with extractives.
  • the herein-described method of making ground wood pulp consisting in initially subjecting the wood in the grinder to sprays of liquor char ed with the extractives of the wood, t e spraying action being remote from the grinding zone to thereby soften the wood and increasingly enrich the treating liquor with the removed oxtractives, and finally subjecting the wood at the grinding zone to the liquor at its maximum charge of extractives to thereby directly affect the fibers of the wood as they are liberated by grinding.
  • a process of making wood pulp in a grinder which consists 'in spraying super heated water charged with solvent wood extractives onto the wood in the grinder prior to the grinding action, subjecting this charged water to the further heat of the friction incident to the grinding action on the wood, withdrawing a substantial portion of such charged and heated water from the lower portion of the grinder, and circulating such withdrawn charged water to the initial spray.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Description

I 1,633 733 June 28, 1927. F. K. FISH'JR PROCESS AND APPARATUS FOR MANUFACTURING GROUND WOOD PULP Filed Ju1yl4. 1925 ATTORNEYS.
liatented 28,1927.
UNITED STATES PATENT OFFICE.
FREDERICK K. FISH, m, 01' m M61800, CAIJJ'OBYIA.
P300388 AND RPmTU 'B I03 IAC'IUBING GBOUND-WOOD PULP.
Application fled m 14, ms, mm In. ,5, a in Canada 1mm 21, ms.
This invention-relates toa-process and apparatus for manufacturing ground wood 11] p Iii the manufacture of paper pulp, I have found that unusual results can be obtained by the employmentof liquor previously used in digesting and cooking the'pul'p, the resinous and solvent const tuents with which this li uor. is charged, apparently-serving to attaiik and-otherwiseact on like constituents and on the fiber material'to greatly disintegrate the fibers and im rovetheir condition for pulp purpose. lthout attempting a full explanation as to how or why reuse of the digesting liquor brings about such favorable results, I may say without contradiction that the fact remainsthat there is an action. brought about, whether chemical or physical, lfcannot' say,which has ens abled me to'lgreatl greduce the cost of the] manufacture of, vp'u p: from mater als which it has been .Ithough be wholly unfitted for pulp pu' josesf These resu tshaveflledime .toutilize this broad principle. 7 in, the manufacture of, groundwood-pul'p', and it is therefore the object of thepresent invention to rovide: an a paratus and a process for treating the woo -beforeau'd. at thev time of grinding to faoilitategseparation of the individual fibers and saturate the fibers with solvents or extractives, which materially enhances the value of the product and greatly expedites its manufacture. v I
In grinding 'pulpwood', it is the usual practice to moisten'the stone and the log at-or about the grinding surfaces, and great in; preventing too care must be exerc much of the water xing 1 with the pulp stock. According-tomyfkinvention, I. introduce liquor tot 'e-"logs vinthe form of a spray, care bein takento regulate the spray to a suificientdeg'ree fso that the logs wi l absorb only the necessary and desired suppallz of moisture, and: then provide 'means to t e up any excess; liquor,and subsequently circulate itiniisp'ray form tothe logs.
' Another o bject 'of'this inventionis to rovide a process-for:'treatingjthe logs Iw ile and previous" to grinding-with a liquor charged with dissolved solvent extractives from wood to soften, saturate,-and penetrate, the fibers to "insure of longer and stronger fibers in'the final product, hence a better and-stronger product.
Another objectof the invention is the provision of means for introducing liquor charged with dissolved solvent extractives from wood into the individual fibers at the point of se aration from the log, so that they The invention also comprehends improvements in the construction "and arrangement of parts, and steps in the process, which will be hereinafter described and particularly pointed out in the claims.
In the accompanying drawing, I: have shown diagrammatically an apparatus for carryin out the invention.
1 .--'n icates a magazine, suitably located andl-su 'fported above a rotating stone 2, the lattero '3 represents I a" tank located conveniently above the'stone and magazine, and it is providedwitha'"valved steam inlet .4, and a valved liquor inlet 4. 7 is a pipe communicating with the bottomofthe tank 3, and extending therefrom are branch pipes 7", having valves 8, and discharging into the magazine at varlous levels. A pipe 9 cominunicates with the bottom of tank 3,, and it is provided with a valve 10 and communicates with the exhaust side of a pump 11, the opposite side of which is connected with a pipe 12 which leads to the bottom of the magazine in close proximity to the periphery of the grinding stone 2, as shown at 12. This polnt of communication 12 of pipe 12 with the magazine is so located that excess liquor from the sprays-and what may be squeezed from the pulp in the rotation of the stone and the logs is withdrawn from the magazine before it passes out of the magazine and becomes mixed with the pump and dischar ed therewith into the grinder pit. While have shown but one such connection, it is obvious that I may withdraw this excess liquor at several points to accomplish this end.
A valved steam inlet pipe 13 is provided at one or more points at the lower portion of the magazine above the pulp forming zone, to admitsufiicient steam to maintain and increase the temperature'of the liquid.
course beingthe grinding medium.
In the pulp industry, it is well recognized of pulp as wood well saturated.
that dry or partially dried wood does not grind as readily or produce as good grinding the wood, it is necessary to limit the amount of water orliquor supplied to the grinder, and ultimately mixed with the ground wood from which the pulp stock is ultimatel formed, otherwise the pulp is of low gra e and frequently, when too wet,
is useless.
In the process of grinding heretofore known to me, it has not been possible to obtain the required saturation of the wood in the grinder, and at the same time maintain the required suppl of water in the subsequently-formed pu p. According to my invention, I am not only able to regulate the liquor .supply to saturate the logs for convenient grinding, but in addition, I am able to regulate the moisture content of the pulp stock, and thus meet the objection heretofore pointed out.
In the operation of m invention, wood, in the form of logs, is fe into the magazine and supported on the stone which forms a bottom. One or more of the valves 8 are opened, depending on the height of logs in the magazine, and water previously heated b steam passed throu h pipe 4, and preferably primarily charged with solvent extractives and stored in tank 3, under pressure, is s rayed through pipes 7 to-the wood.
he spray or sprays injected into the magazine has considerable force, with the result that the liquor thoroughly penetrates and saturates the wood, and the solvent extractives contained in the liquor attack the constituents of the wood and partially dissolve and extract same. These partially melted and dissolved constituents, in the transit of the logs through the magazine, are largely released by the ever increasingly-enriched liquor which is continuously circulated over and between the logs in the magazine.
The temperature of the spray of liquor on the logs while-in the magazine may be regulated by passing steam through pipe 13, which with the heat in the liquor and the continued movement of the logs causes vapor and gases formed by the dissolved constituents in the logs to rise in the magazine and around the logs. These vapors condense and the liquor. of condensation accumulates in the bottom of the magazine, but as stated, care must be taken to avoid too much of the liquor in the grinding zone. The vapors, consequently the liquor, become surcha-rged with the extractives and constituents liberated from the logs. Hence, the constituents in the logs are attacked and acted upon by like constituents which better prepares the wood for the grinding action, and leads to a definite and defined separation of the fibers,
' features most important and essential in the making of ground pulp. The heat from ad ii? iii the liquor is largely conserved in the magazine, which assists largely in assisting the sprayed liquor penetrating the logs.
The liquor accumulates at the bottom of the magazine and is drawn through ipe 12', by 11 to the tank 3 and is t ere reheate is liquor may be continuously or periodically umped, but in any event, it is continuous y surcharged with the extractives and constituents liberated in the magazine, so that in'the continued operation of the pump, the spray, heat, and the contained wood constituents in the liquor softens, dissolves, and removes, portions of the encrusting material'of the wood fiber and thus prepares the wood for efiicient economical grindin 7 Steam may be admitted to the ma azine from time to time, through the valve pipe 13, which will discharge into the magazine at a point or points best ada ted to secure the required temperature in t e charge, but
care must be taken not to raise the temperature excessively by admitting too much steam.
In the usual processes of grinding wood, the vapors which ordinarily pass upwardly in the magazine, owing to the heat generated at the stone, have a tendency to cause discoloration of the resulting pulp, but this is overcome in my rocess owing to the uantity of liquor use which liquor absorbs t e steam and vapors and adapts them for advantageous use in the process.
In order to prevent the accumulation of too great a quantity of liquor in the product produced, the valve 10 is opened and the operation of the pump 11 is regulated through the medium of the valve 10 to withdraw liquor from the magazine and return it to the tank 3 where it may be reheated to the required point by the admission of steam to the tankthrough the valved pipe 4. By withdrawing the excess liquor in this manner and returnin it directly for reuse, its heat and containe extractive properties are conserved.
Moreover, it will be noted that the remaining liquor containing solvent extractives in the magazine at the grinding zone acts on the fibers as they are separated at the stone and so affects the encrusting materials of the wood, as to produce from the treated product a whiter and more desirable pulp.
In practical grinding, it has been found that bundles of fiber frequently appear in the product and these have a bad effect when the pulp is run into paper. I have been able to overcome this objectionable feature because of the prior softening eflect of the liquor when charged with the extractives, with the result that the fibers readily se arate one from the other under the grinding action.
An important characteristic of the improved process is that the wood is subjected to the action of the charged liquor in advance of the grinding zone, so that the function of the solvents in the liquor is of gradually increasing effect toward the grind ng zone, with its maximum effect at "the point where the fibers are separated--that is at the grinding'zone. Thus the li uor, 1nc1 dent to its being charged with tie extractives of the wood being treated is of gradually-increasing strength toward the inding zone, and hence its maximum e ect is had at that point where the wood is most susceptible to the treatment, that is where i the fibers are separated one from the other. Thus the product is given the maximum treatment in gradually-increasing steps from the initial spraying to the grinding point, thus insuring the most effective separation and treatment of the fibers.
It will be apparent that I may use in my process any desired character of liquor which will have the required effect on the wood in the magazine.
What I claim is:
1. In combination with a grinder, a liquor supply tank, means for distributing liquor in the upper portion of the magazine, and means for withdrawing liquor from the lower portion of the grinder and discharging it into said tank.
2. In combination with a pulp grinder, means for removing excess liquor from the grinder before said liquor reaches the point at which the pulp is discharged from said grinder.
3. Apparatus as defined in claim 2 having means for returning the mid withdrawn liquor to the grinder for reuse.
4. Apparatus as defined in claim 2 having means for returning said withdrawn liquor to the grinder for reuse, and means for heating said liquor during circulation.
5. A process of making ground wood pulp in a magazine grinder, the step which consists in subjecting the wood in said grinder to the action of water and steam to heat and soften the Wood and withdrawing excess water before it becomes mixed with the pulp in the grinder it.
6. In a process 0 making ground wood pulp in a grinder, the step which consists in withdrawing from the lower portion of the grinder excess water, applied to the wood for the purpose of softening it before said water becomes mixed with the pulp in the grinder pit.
7. A process of making ground wood pulp, consisting in spraying the wood before and during the grinding period with preheated water charged with extractives from wood to soften and impregnate the wood with moisture and extractives to thereby prepare the wood for grinding and at the same time release contained extractives, the released extractives being intermixed with the water to enrich the same, withdrawing a substantial proportion of the excess water charged with extractives above the actual grinding point, and recharging the grinder with the withdrawn water charged with extractives.
8. The herein-described process of making ground wood pulp, consisting in subjecting the wood in the grinder to a spray of heated .water more or less charged with the wood extractives, to thereby soften the wood and directly affect and release the contained extractives, and finally withdraw undesirable excess of water charged with the wood extractives substantially at the grinding zone to prevent excess water in the ground pul the withdrawn charged water being redeiivered to the wood above the grinding zone.
9. The herein-described process of making ground wood pulp, consisting in spraying water charged with extractives of the wood onto the wood above the grinding zone to thereby prepare the wood for grinding through softening the same and liberating undesirable constituents, collecting the excess water with liberated constituents at the grinding zone, withdrawin such excess charged water from the grinding zone to prevent super-saturation of the ground pulp, and utilizing such withdrawn water for recharging the wood above the grinding zone.
10. The herein-described process of making ground wood pulp, consisting in subjecting the wood in the grinderto the action of heated water charged with extractives of wood to thereby soften and liberate extractives from the wood before the wme reaches the grinding zone, maintaining a desired saturation of the wood at the grinding zone by withdrawing excess water with its charged extractives at the grinding zone,
and utilizing such excess charged water for initial wood treatment in the grinder.
11. The herein-described method of making ground wood pulp, consisting in initially subjecting the wood remote from the grinding zone to sprays of heated liquor charged with wood extractives with the effeet to soften the wood and increasingly charge the liquor with the wood extractives, subjecting the wood as in fiber form at the grinding zone to the liquor with a maximum charge of extractives, and finally withdrawinlg all charged liquor at the grinding zone ot er than that necessary to the proper pulp consistency. I
12. The herein-described method of making ground wood pulp consisting in initially subjecting the wood in the grinder to sprays of liquor char ed with the extractives of the wood, t e spraying action being remote from the grinding zone to thereby soften the wood and increasingly enrich the treating liquor with the removed oxtractives, and finally subjecting the wood at the grinding zone to the liquor at its maximum charge of extractives to thereby directly affect the fibers of the wood as they are liberated by grinding.
13. In a process of mechanically making wood pulp, that step which consists in dissolving t ose encrustin materials of the wood which are not soluble in water by subjecting the wood prior to and while being mechanically acted on to water intermingled with extractives of wood to thereby dissolve the said encrusting materials.
14.In a process of mechanically making wood pulp, that step which consists in dissolving those encrusting materials of the wood which arenot soluble in water by subjecting the wood "means mechanically acted on to heated water intermingled with extractives of wood to thereby dissolve the said encrusting materials.
15. A process of making wood pulp in a grinder which consists 'in spraying super heated water charged with solvent wood extractives onto the wood in the grinder prior to the grinding action, subjecting this charged water to the further heat of the friction incident to the grinding action on the wood, withdrawing a substantial portion of such charged and heated water from the lower portion of the grinder, and circulating such withdrawn charged water to the initial spray.
In testimon whereof I afiix my si nature.
F EDERICK K. FIS JR.
iii to and while being a
US43596A 1925-03-21 1925-07-14 Process and apparatus for manufacturing ground-wood pulp Expired - Lifetime US1633733A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2620988A (en) * 1950-01-10 1952-12-09 Edgar H Tellier Fluorescent lamp bulb breaking device
US2668110A (en) * 1948-06-18 1954-02-02 Spencer Method for fiber liberation in cotton stalks and the pulp
US3255070A (en) * 1957-11-13 1966-06-07 Norton Co Machine and process for making wood pulp
FR2486556A1 (en) * 1980-07-09 1982-01-15 Mo Och Domsjoe Ab PROCESS FOR THE MANUFACTURE OF SPRAYED WOOD PULP FROM LIGNOCELLULOSIC MATERIALS
US4456182A (en) * 1980-12-13 1984-06-26 J. M. Voith Gmbh Pulp grinder with liquid retention
US4578148A (en) * 1980-07-09 1986-03-25 Mo Och Domsjo Aktiebolag Process for manufacturing bright and strong bleached groundwood pulp of uniform quality

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2668110A (en) * 1948-06-18 1954-02-02 Spencer Method for fiber liberation in cotton stalks and the pulp
US2620988A (en) * 1950-01-10 1952-12-09 Edgar H Tellier Fluorescent lamp bulb breaking device
US3255070A (en) * 1957-11-13 1966-06-07 Norton Co Machine and process for making wood pulp
FR2486556A1 (en) * 1980-07-09 1982-01-15 Mo Och Domsjoe Ab PROCESS FOR THE MANUFACTURE OF SPRAYED WOOD PULP FROM LIGNOCELLULOSIC MATERIALS
US4578147A (en) * 1980-07-09 1986-03-25 Mo Och Domsjo Aktiebolag Process for manufacturing groundwood pulp while maintaining a high and uniform moisture content in the wood in the grinding zone
US4578148A (en) * 1980-07-09 1986-03-25 Mo Och Domsjo Aktiebolag Process for manufacturing bright and strong bleached groundwood pulp of uniform quality
US4456182A (en) * 1980-12-13 1984-06-26 J. M. Voith Gmbh Pulp grinder with liquid retention

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