US1553976A - Method of manufacturing paper pulp - Google Patents
Method of manufacturing paper pulp Download PDFInfo
- Publication number
- US1553976A US1553976A US440470A US44047021A US1553976A US 1553976 A US1553976 A US 1553976A US 440470 A US440470 A US 440470A US 44047021 A US44047021 A US 44047021A US 1553976 A US1553976 A US 1553976A
- Authority
- US
- United States
- Prior art keywords
- lye
- fibres
- paper pulp
- cylinder
- treatment
- 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
- 238000004519 manufacturing process Methods 0.000 title description 11
- 229920001131 Pulp (paper) Polymers 0.000 title description 7
- 238000011282 treatment Methods 0.000 description 13
- 239000000463 material Substances 0.000 description 11
- 239000000126 substance Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 238000005406 washing Methods 0.000 description 8
- 239000007788 liquid Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000010924 continuous production Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
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
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/24—Continuous processes
Definitions
- This invention relates -to a method and apparatus for the manufacture of paper pulp.
- the current method of manufacture of paper pulp comprises a series of successive operations such as sorting the raw material in the shape of natural or artificial vegetable fabrics, Washing or dust removal, cutting up, lye treatment, washing after the same, separation of fibres, bleaching; and subsequent Washing.
- the most important of these operations are the lye treatment and the separation of fibre.
- the first of these operations serves to dissolve as much as possible the foreign bodies which surround and connect the fibres of pure cellulose, and is usually carried out in a digester at a pressure of about 3 kilogrammes per square centimeter, the Operation lasting from' 2 to 8 hours, or often more.
- the lye-treated rlaterial is submitted to a fibre separating process, for the purpose of separating the fibres Which are still collected in larger or smaller masses.
- This mechanical operation is generally carried out in a drum containing fixed and moving blades.
- the paper pulp which is thus Obtained is only in the partially finished condition, inasmuch as it is not homogeneous and requires to be refined in order toi be used for'the manufacture of high grade paers.
- the process of manufacture as thus carried' out requires successive treatments of the material, and cannot be considered as a continuous process.
- Figure 1 is a diagrammatic view of the Whole series of apparatus.
- Figure 2 is a longitudinal section of a lye-treating apparatus and alfibre-s'eparating apparatus suitably combined.
- Figure 3 is an elevational View of one of the perforated plates.
- the lye-treating apparatus comprises a horizontal cylinder 1 Whereon is disposed a feed hopper 2 employed for the continuous feeding of the ve etable matter to be treated 4by the lye-bat
- the said cylinder contains ashaft 3 having formed or secured thereon a screw conveyor 4 for propolling the material under treatment from the ⁇ end adjacent the feeding hopper to theopposite end of the device.
- a portion of the said screw-member is preferably adapted to cooperate with the internal edge.
- a member 6 in the form of a wheel which is loosely rotatable upon the shaft thereof 7 and engages the threads o-f the screw member 4.
- the said wheel serves to prevent the free movement of the material about the said screw, member which might take place in spite of the fluid nature thereof, and the material is now obliged to move forward as the screw rotates.
- the said cylinder which is chiefiy -used for the lye treatment, is heated, if
- the duration of the lye treatment does not usually exceed 30 minutes.
- the matter which arrives at the end 9 of the cylinder still retains substantially the same shape as it had at the feeding end, and the separation of the material is carried out chiefiy in the fibre-separatingapparatus. It may however be advantageous to dispose adjacent the perforated end- 9 of the cylinder 1 a rotary knife 10 for a rough cutting up of the fibrous matter, the said knife cooperating with the bottom part 9 somewhat after the manner of the knife member and perforated type of meat cutter.
- the fibre-separating apparatus comprises a cylinder 11 preferably disposed in alignment with the lye-treating cylinder and having therein a series of stationary partitions 12a, 12b, 12 etc. forming various chambers, 10 for instance, such as 13, 13b', .13 etc. the said partitions being provided with the apertures 14a, 14b etc.l of decreasing width, the apertures 14a having for instance several centimeters width whereas lthe apertures 14k are reduced to very narrowslits for the purpose of allowing only the individual fibres to pass through, Within the said chambers are disposed the rotary stirring members 15, 15" 15k which are secured to the shaft 16 disposed according to the axis of the cylinder 11.
- the said shaft is situated preferably within the shaft 3, this latter being made hollow to this effect, and it also carries the rotary knife 10.
- the shafts 3 and 16 are actuated for instance by belting disposed u on the pulleys 17 and 18 or by gearing or t e like, 1n such manner as to effect the rotation of the stirring members 15 at a much higher speed than that of the screw 4, whereby the forward movement of the lye bath and the material shall be much slower than that of out through the slits of the partition 12k.
- the paste drops into one or more filter presses 19 of any suitable construction whereby the cellulose fibres are retained and separated from the lyebath.
- the lye bath which is discharged from the filter press'or presses kis conducted through the piping 20 to a pump 21 or other elevating device which returns the same to the hopper 21
- the fibres remaining in the filtering devices are discharged therefrom at more or less frequent intervals or by a continuous process, according to the character of the apparatus employed, and the libres are then ready for the washing process. After a sufficient washing, they constitute a pulp which is suitable for paper manufacture.
- the apparatus takesup but a small space and requires a minimum of hand labor.
- the lye bath is used in a systematic and complete manner, resulting in a minimum w cost of lye substances.
- the quantity of material under treatment at any given moment is relatively small, whencev it follows that a large or small amount of substance may be treated with equal facility and with the same relative economy, and a great variety of substances can be treated successively without requiring any stoppage or cleaning of the apparatus, whereby paper paste of various qualities may be produced in a continuous manner.
- a process for the manufacture of paper paste in an endless current of suitable liquid wherein the raw brous substances are introduced in a continuo/us manner at a given point of the said current and are caused to pass through the libre-removing elements ater having vbeen saturated With the said liquid, the bres being removed from the current a second point in the stream of liquid in the form of a pulp Which is ready for use, ⁇ whereby the liquid does not pass again through the same points before all the fibres are removed.
Landscapes
- Paper (AREA)
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL11900D NL11900C (enrdf_load_stackoverflow) | 1921-01-27 | ||
US440470A US1553976A (en) | 1921-01-27 | 1921-01-27 | Method of manufacturing paper pulp |
GB382821A GB178962A (en) | 1921-01-27 | 1921-02-01 | Improved method for the manufacture of paper pulp and apparatus therefor |
DEB98060D DE407832C (de) | 1921-01-27 | 1921-02-03 | Verfahren und Vorrichtung zur Herstellung von Papierstoff in einem ununterbrochenen Strom von Aufschlussfluessigkeit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US440470A US1553976A (en) | 1921-01-27 | 1921-01-27 | Method of manufacturing paper pulp |
Publications (1)
Publication Number | Publication Date |
---|---|
US1553976A true US1553976A (en) | 1925-09-15 |
Family
ID=23748879
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US440470A Expired - Lifetime US1553976A (en) | 1921-01-27 | 1921-01-27 | Method of manufacturing paper pulp |
Country Status (3)
Country | Link |
---|---|
US (1) | US1553976A (enrdf_load_stackoverflow) |
DE (1) | DE407832C (enrdf_load_stackoverflow) |
NL (1) | NL11900C (enrdf_load_stackoverflow) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2645982A (en) * | 1949-11-14 | 1953-07-21 | Cowles Co | Apparatus for treating paper stock |
US2657131A (en) * | 1949-05-26 | 1953-10-27 | American Defibrator | Discharge device for finely divided fibrous material from a pressure system |
US2718178A (en) * | 1948-02-04 | 1955-09-20 | Wandel Kurt | Machine for effecting a refining treatment of fibrous material |
US2730931A (en) * | 1948-12-31 | 1956-01-17 | Reisten Werner | Mill for fibrous substances |
US4121967A (en) * | 1976-09-07 | 1978-10-24 | Reinhall P G | Screw conveyor in pulp-making equipment |
US20050172837A1 (en) * | 2004-02-09 | 2005-08-11 | Derek Flor | Screw press with radial gate valve and supported screw shaft |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE745116C (de) * | 1941-07-02 | 1944-02-26 | Johannes Jung | Vorrichtung zum Zerfasern von Rinden, Borken, Bast, Holzsplittern u. dgl. |
DE1047000B (de) * | 1953-09-30 | 1958-12-18 | Aschaffenburger Zellstoffwerke | Verfahren zur Herstellung von Halbzellstoff |
DE1051109B (de) * | 1953-09-30 | 1959-02-19 | Aschaffenburger Zellstoffwerke | Verfahren zur Herstellung von Halbzellstoff |
-
0
- NL NL11900D patent/NL11900C/xx active
-
1921
- 1921-01-27 US US440470A patent/US1553976A/en not_active Expired - Lifetime
- 1921-02-03 DE DEB98060D patent/DE407832C/de not_active Expired
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2718178A (en) * | 1948-02-04 | 1955-09-20 | Wandel Kurt | Machine for effecting a refining treatment of fibrous material |
US2730931A (en) * | 1948-12-31 | 1956-01-17 | Reisten Werner | Mill for fibrous substances |
US2657131A (en) * | 1949-05-26 | 1953-10-27 | American Defibrator | Discharge device for finely divided fibrous material from a pressure system |
US2645982A (en) * | 1949-11-14 | 1953-07-21 | Cowles Co | Apparatus for treating paper stock |
US4121967A (en) * | 1976-09-07 | 1978-10-24 | Reinhall P G | Screw conveyor in pulp-making equipment |
US20050172837A1 (en) * | 2004-02-09 | 2005-08-11 | Derek Flor | Screw press with radial gate valve and supported screw shaft |
US7152522B2 (en) * | 2004-02-09 | 2006-12-26 | Derek Flor | Screw press with radial gate valve and supported screw shaft |
WO2006086290A3 (en) * | 2005-02-08 | 2007-06-21 | Derek Flor | Screw press with radial gate valve and supported screw shaft |
Also Published As
Publication number | Publication date |
---|---|
NL11900C (enrdf_load_stackoverflow) | |
DE407832C (de) | 1925-01-02 |
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