US3118622A - Recirculating disk refiner - Google Patents

Recirculating disk refiner Download PDF

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Publication number
US3118622A
US3118622A US172194A US17219462A US3118622A US 3118622 A US3118622 A US 3118622A US 172194 A US172194 A US 172194A US 17219462 A US17219462 A US 17219462A US 3118622 A US3118622 A US 3118622A
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disk
blades
passageways
passageway
inlet
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Expired - Lifetime
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US172194A
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Dwight E Jones
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E D JONES CORP
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Ed Jones Corp
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C7/00—Crushing or disintegrating by disc mills
    • B02C7/02—Crushing or disintegrating by disc mills with coaxial discs
    • B02C7/06—Crushing or disintegrating by disc mills with coaxial discs with horizontal axis
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00—Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20—Methods of refining
    • D21D1/30—Disc mills
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00—Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20—Methods of refining
    • D21D1/30—Disc mills
    • D21D1/303—Double disc mills

Definitions

  • This invention relates to machines for refining paper pulp and other materials of the type comprising a rotary disk having a set of blades on one or both sides and a set of stationary blades facing each of the rotary sets with a passageway extending radially between the tips of the blades of each pair of opposed rotary and stationary blades and a circumferential space at the outer end of said passageway or passageways.
  • a machine is disclosed in my Patent 2,991,020, granted July 4, 1961.
  • This machine has various drawbacks.
  • One drawback is that the output of the machine cannot be varied to suit different mill requirements from time to time without affecting the degree of refining.
  • a bypass is provided from the outlet to the inlet so that some of the material may be recir slated through the aforesaid radial passageway or passageways and the width of the passageways is adjusted to produce the desired degree of refining at maximum output. Then, as the discharge valve is moved toward closed position, an increasing amount of the material is recirculated through the bypass so that the rate of flow through the machine is maintained, the radial passageways are kept flooded and all of the material is properly refined at all outputs from maximum down to a small percent of maximum. For example, in a machine having a maximum capacity of 1,000 g.p.m. (gallons per minute), the output may be reduced as low as 200 g.p.m., permitting 800 g.p.m. to recirculate, while maintaining the quality of the pulp.
  • Curtis 2,982,482 discloses a disk refining machine with a by-pass but it is diflerently located for a different purpose and does not serve the purpose of the present invention.
  • the outlet of the machine is not located at the periphery of the disk; on the contrary,-both inlet and outlet are located at the axis, the material flowing from the axis to the periphery through one passageway and from the periphery to the axis through the other passageway. And instead of the by-pass leading from the outiet to the inlet it leads from a location halfway between.
  • PEG. 1 is a side view of one embodiment with a portion in central axial section;
  • FIGS. 2, 3 and 4 are similar views of other embodiments.
  • FIG. 1 The particular embodiment shown in FIG. 1 comprises a housing 1 in which is journalcd a shaft 2.
  • a disk 3 carrying the aforesaid blades 4 on opposite sides thereof.
  • Facing each set of rotary blades is a set of stationary blades 5 mounted on the housing 1 opposite the rotary blades 4 with narrow passageways 6 and 7 therebetween.
  • the end of the shaft 2 is hollow to provide an inlet 3 communicating with the passageways 6 and 7 through ducts 9. Extending around the outer ends of the two passageways is an annular space ll.
  • An inlet pipe 12 containing a valve 13 leads to the inlet 3 and an outlet pipe 14 containing a discharged valve 15 leads from annular space 11.
  • a bypass 16 is connected between the inlet and outlet pipes 12 and 14, the by-pass contain ng a valve 17.
  • the valves 13, 15 and 17 the output of the machine can be adjusted to suit the requirements of a mill from time to time, the amount of recirculation through the pipe 16 increasing as the output decreases.
  • FIG. 2 The embodiment shown in FIG. 2 is like that shown in FIG. 1 and corresponding parts are correspondingly designated.
  • the second embodiment has a second inlet 13 to the left passageway 6, the inlet 8 supplying material only to the right passageway 7.
  • the inlet pipe 12 has two branches l2 and 12" leading to the two inlets respectively, the branches containing valves 13 and 13'', and by-passes l6 and 15 lead from the outlet to the two inlets respectively.
  • the operation of the second embodiment is like that of the first embodiment. However by closing one of the valves 13' and 13" only one of the two passageways 6 and 7 may be utilized, thereby further reducing the output.
  • FIGS. 3 and 4 are like those shown in P6. 2 and FIG. 1 respectively and corresponding parts are correspondingly designated, the modifications having only one pair of disks and one by-pass instead of two.
  • apparatus for refining material such as pulp, apparatus comprising a rotary disk having a set of blades on one side, a housing surrounding the disk, a set of stationary blades in the housing facing said set with a radial passageway between the sets throughout the circumference of the disk, the housing having an inlet to the inner end of said passageway and an outlet from the outer end of the passageway so that the material flows outwardly from the center of the disk to its periphery, and a by-pass from said outlet to said inlet to keep the inner end of said passageway properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
  • apparatus for refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, the housing having an inlet to the inner end of said passageways and an outlet from the outer end of the passageways so that the material flows outwardly from the center of the disk to its periphery through said passageways in parallel, and a by-pass from said outlet to said inlet to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
  • apparatus for refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, the housing having separate inlets to the inner end of said passageways and an outlet from the outer end of the passageways so that the material flows only outwardly from the center of the disk to its periphery, and a bypass from said outlet to each or" said inlets to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
  • apparatus for refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, a shaft supporting said disk, the shaft having an opening extending lengthwise thereof with ducts communicating with said passageways respectively, said opening having an inlet through which material may be fed and the housing having an outlet at the periphery of the passageways so that material flows outwardly through said passageways in parallel from the center of the disk to said periphery, and a by-pass from said outlet to said inlet to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.

Description

D. E. JONES RECIRCULATING DISK REFINER Jan. 21, 1964 2 Sheets-Sheet 1 Filed Feb. 9, 1962 D. E. JONES RECIRCULATING DISK REFINER Jan. 21, 1964 2 Sheets-Sheet 2 Filed Feb. 9, 1962 United States Patent 3,118,622 REtIECULATlNG DISK REFINER Dwight E. lanes, Pitts'field, Mass, assignor to E. D. enes Qorporation, hittsfield, lVlass, a corporation of Delaware Filed Feb. 9, 1962, Ser. No. 172,194 4 Claims. (Cl. 24197) This invention relates to machines for refining paper pulp and other materials of the type comprising a rotary disk having a set of blades on one or both sides and a set of stationary blades facing each of the rotary sets with a passageway extending radially between the tips of the blades of each pair of opposed rotary and stationary blades and a circumferential space at the outer end of said passageway or passageways. Such a machine is disclosed in my Patent 2,991,020, granted July 4, 1961. However this machine has various drawbacks. One drawback is that the output of the machine cannot be varied to suit different mill requirements from time to time without affecting the degree of refining. As the output is increased, as by opening the outlet valve Wider, the rate of flow through the passageways increases and the degree of refining decreases. Conversely as the discharge valve is closed down the rotary disk pumps the material to the outer periphery of the passageways and the inner ends of the passageways are not properly flooded. When the passageways are not fully flooded the opposed refining blades are not properly lubricated, therefore wearing rapidly, and the quality of refined stock is inferior.
According to this invention a bypass is provided from the outlet to the inlet so that some of the material may be recir slated through the aforesaid radial passageway or passageways and the width of the passageways is adjusted to produce the desired degree of refining at maximum output. Then, as the discharge valve is moved toward closed position, an increasing amount of the material is recirculated through the bypass so that the rate of flow through the machine is maintained, the radial passageways are kept flooded and all of the material is properly refined at all outputs from maximum down to a small percent of maximum. For example, in a machine having a maximum capacity of 1,000 g.p.m. (gallons per minute), the output may be reduced as low as 200 g.p.m., permitting 800 g.p.m. to recirculate, while maintaining the quality of the pulp.
The patent to Curtis 2,982,482 discloses a disk refining machine with a by-pass but it is diflerently located for a different purpose and does not serve the purpose of the present invention. The outlet of the machine is not located at the periphery of the disk; on the contrary,-both inlet and outlet are located at the axis, the material flowing from the axis to the periphery through one passageway and from the periphery to the axis through the other passageway. And instead of the by-pass leading from the outiet to the inlet it leads from a location halfway between. This arrangement is suitable for making slight variations in the by-pass to maintain equal pressure on opposite sides of the disk, the purpose of the patent, but it is entir ly unsuitable to make substantial variations in the by-pass to control fne output of the machine. Indeed substantial variations in the by-pass would defeat the purpose of the patent because they would upset the balance of pressure on the two sides of the disk, thereby adversely affecting the flow of material, causing excessive wear on one pair of opposed disks and producing an inferior product.
For the purpose of illustration typical embodiments of the invention are shown in the accompanying drawing in which PEG. 1 is a side view of one embodiment with a portion in central axial section; and
3,ll8,fi22 Patented Jan. 21, 1964 FIGS. 2, 3 and 4 are similar views of other embodiments.
The particular embodiment shown in FIG. 1 comprises a housing 1 in which is journalcd a shaft 2. Fast to the shaft is a disk 3 carrying the aforesaid blades 4 on opposite sides thereof. Facing each set of rotary blades is a set of stationary blades 5 mounted on the housing 1 opposite the rotary blades 4 with narrow passageways 6 and 7 therebetween. The end of the shaft 2 is hollow to provide an inlet 3 communicating with the passageways 6 and 7 through ducts 9. Extending around the outer ends of the two passageways is an annular space ll. An inlet pipe 12 containing a valve 13 leads to the inlet 3 and an outlet pipe 14 containing a discharged valve 15 leads from annular space 11.
From the foregoing it will be understood that the stock flowing through the inlet 3 is divided equally between the two passageways 6 and 7 so that the pressure on opposite sides of the disk is equalized, all. as described in my Patent 2,991,020 granted July 4, 1961.
According to this invention a bypass 16 is connected between the inlet and outlet pipes 12 and 14, the by-pass contain ng a valve 17. By adjusting the valves 13, 15 and 17 the output of the machine can be adjusted to suit the requirements of a mill from time to time, the amount of recirculation through the pipe 16 increasing as the output decreases.
The embodiment shown in FIG. 2 is like that shown in FIG. 1 and corresponding parts are correspondingly designated. However the second embodiment has a second inlet 13 to the left passageway 6, the inlet 8 supplying material only to the right passageway 7. The inlet pipe 12 has two branches l2 and 12" leading to the two inlets respectively, the branches containing valves 13 and 13'', and by-passes l6 and 15 lead from the outlet to the two inlets respectively. The operation of the second embodiment is like that of the first embodiment. However by closing one of the valves 13' and 13" only one of the two passageways 6 and 7 may be utilized, thereby further reducing the output.
The modifications shown in FIGS. 3 and 4 are like those shown in P6. 2 and FIG. 1 respectively and corresponding parts are correspondingly designated, the modifications having only one pair of disks and one by-pass instead of two.
It should be understood that the present disclosure is for the purpose of illustration only and that this invention includes all modifications and equivalents which fall within the scope of the appended claims.
I claim:
1. For refining material such as pulp, apparatus comprising a rotary disk having a set of blades on one side, a housing surrounding the disk, a set of stationary blades in the housing facing said set with a radial passageway between the sets throughout the circumference of the disk, the housing having an inlet to the inner end of said passageway and an outlet from the outer end of the passageway so that the material flows outwardly from the center of the disk to its periphery, and a by-pass from said outlet to said inlet to keep the inner end of said passageway properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
2. For refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, the housing having an inlet to the inner end of said passageways and an outlet from the outer end of the passageways so that the material flows outwardly from the center of the disk to its periphery through said passageways in parallel, and a by-pass from said outlet to said inlet to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
3. For refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, the housing having separate inlets to the inner end of said passageways and an outlet from the outer end of the passageways so that the material flows only outwardly from the center of the disk to its periphery, and a bypass from said outlet to each or" said inlets to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
4. For refining material such as pulp, apparatus comprising a rotary disk having a set of blades on each side, a housing surrounding the disk, a set of stationary blades in the housing facing each of said sets with a radial passageway between each pair of opposed rotary and stationary blades throughout the circumference of the disk, a shaft supporting said disk, the shaft having an opening extending lengthwise thereof with ducts communicating with said passageways respectively, said opening having an inlet through which material may be fed and the housing having an outlet at the periphery of the passageways so that material flows outwardly through said passageways in parallel from the center of the disk to said periphery, and a by-pass from said outlet to said inlet to keep the inner end of said passageways properly flooded when the output is decreased, thereby keeping said blades properly lubricated at low output.
References Cited in the file of this patent UNITED STATES PATENTS 1,875,743 Letz Sept. 6, 1932 2,718,178 Wandel Sept. 20, 1955 2,727,440 Jones et a1. Dec. 20, 1955 2,991,020 Jones July 4, 1961

Claims (1)

1. FOR REFINING MATERIAL SUCH AS PULP, APPARATUS COMPRISING A ROTARY DISK HAVING A SET OF BLADES ON ONE SIDE, A HOUSING SURROUNDING THE DISK, A SET OF STATIONARY BLADES IN THE HOUSING FACING SAID SET WITH A RADIAL PASSAGEWAY BETWEEN THE SETS THROUGHOUT THE CIRCUMFERENCE OF THE DISK, THE HOUSING HAVING AN INLET TO THE INNER END OF SAID PASSAGEWAY AND AN OUTLET FROM THE OUTER END OF THE PASSAGEWAY SO THAT THE MATERIAL FLOWS OUTWARDLLY FROM THE CENTER OF THE DISK TO ITS PHERIPHERY, AND A BY-PASS FROM SAID OUTLET TO SAID INLET TO KEEP THE INNER END OF SAID PASSAGEWAY PROPERLY FLOODED WHEN THE OUTPUT IS DECREASED, THEREBY KEEPING SAID BLADES PROPERLY LUBRICATED AT LOW OUTPUT.
US172194A 1962-02-09 1962-02-09 Recirculating disk refiner Expired - Lifetime US3118622A (en)

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Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3204880A (en) * 1962-03-05 1965-09-07 Stecco Sa De Tech Chimique Method and apparatus for grinding solid particles
US3311309A (en) * 1964-07-21 1967-03-28 Ed Jones Corp Method and apparatus for locking a paper pulp refiner disc
US3331560A (en) * 1963-07-29 1967-07-18 British Titan Products Process for milling of particulate solids in liquids
DE2716728A1 (en) * 1976-04-15 1977-11-03 Enso Gutzeit Oy DISC REFINER
US4093130A (en) * 1977-03-24 1978-06-06 Koppers Company, Inc. Twin refiner apparatus
US5425508A (en) * 1994-02-17 1995-06-20 Beloit Technologies, Inc. High flow, low intensity plate for disc refiner
DE19808355A1 (en) * 1998-02-27 1999-09-02 Voith Sulzer Papiertech Patent Paper fiber suspension grinding operation for papermaking fibers
US11118313B2 (en) 2019-03-21 2021-09-14 Eastman Chemical Company Ultrasonic welding of wet laid nonwoven compositions
US11230811B2 (en) 2018-08-23 2022-01-25 Eastman Chemical Company Recycle bale comprising cellulose ester
US11286619B2 (en) 2018-08-23 2022-03-29 Eastman Chemical Company Bale of virgin cellulose and cellulose ester
US11299854B2 (en) 2018-08-23 2022-04-12 Eastman Chemical Company Paper product articles
US11306433B2 (en) 2018-08-23 2022-04-19 Eastman Chemical Company Composition of matter effluent from refiner of a wet laid process
US11313081B2 (en) 2018-08-23 2022-04-26 Eastman Chemical Company Beverage filtration article
US11332885B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Water removal between wire and wet press of a paper mill process
US11332888B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Paper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en) 2018-08-23 2022-05-24 Eastman Chemical Company Paper bag
US11390996B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Elongated tubular articles from wet-laid webs
US11390991B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Addition of cellulose esters to a paper mill without substantial modifications
US11396726B2 (en) 2018-08-23 2022-07-26 Eastman Chemical Company Air filtration articles
US11401659B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Process to produce a paper article comprising cellulose fibers and a staple fiber
US11401660B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Broke composition of matter
US11408128B2 (en) 2018-08-23 2022-08-09 Eastman Chemical Company Sheet with high sizing acceptance
US11414791B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Recycled deinked sheet articles
US11414818B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Dewatering in paper making process
US11420784B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Food packaging articles
US11421387B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Tissue product comprising cellulose acetate
US11421385B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Soft wipe comprising cellulose acetate
US11441267B2 (en) 2018-08-23 2022-09-13 Eastman Chemical Company Refining to a desirable freeness
US11466408B2 (en) 2018-08-23 2022-10-11 Eastman Chemical Company Highly absorbent articles
US11479919B2 (en) 2018-08-23 2022-10-25 Eastman Chemical Company Molded articles from a fiber slurry
US11492755B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Waste recycle composition
US11492757B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Composition of matter in a post-refiner blend zone
US11492756B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Paper press process with high hydrolic pressure
US11512433B2 (en) 2018-08-23 2022-11-29 Eastman Chemical Company Composition of matter feed to a head box
US11519132B2 (en) 2018-08-23 2022-12-06 Eastman Chemical Company Composition of matter in stock preparation zone of wet laid process
US11525215B2 (en) 2018-08-23 2022-12-13 Eastman Chemical Company Cellulose and cellulose ester film
US11530516B2 (en) 2018-08-23 2022-12-20 Eastman Chemical Company Composition of matter in a pre-refiner blend zone
US11639579B2 (en) 2018-08-23 2023-05-02 Eastman Chemical Company Recycle pulp comprising cellulose acetate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1875743A (en) * 1930-02-03 1932-09-06 Letz Mfg Co Grinding mill
US2718178A (en) * 1948-02-04 1955-09-20 Wandel Kurt Machine for effecting a refining treatment of fibrous material
US2727440A (en) * 1954-06-15 1955-12-20 E D Jones & Sons Company Refining apparatus
US2991020A (en) * 1960-04-29 1961-07-04 Ed Jones Corp Double-disk refiner

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1875743A (en) * 1930-02-03 1932-09-06 Letz Mfg Co Grinding mill
US2718178A (en) * 1948-02-04 1955-09-20 Wandel Kurt Machine for effecting a refining treatment of fibrous material
US2727440A (en) * 1954-06-15 1955-12-20 E D Jones & Sons Company Refining apparatus
US2991020A (en) * 1960-04-29 1961-07-04 Ed Jones Corp Double-disk refiner

Cited By (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3204880A (en) * 1962-03-05 1965-09-07 Stecco Sa De Tech Chimique Method and apparatus for grinding solid particles
US3331560A (en) * 1963-07-29 1967-07-18 British Titan Products Process for milling of particulate solids in liquids
US3311309A (en) * 1964-07-21 1967-03-28 Ed Jones Corp Method and apparatus for locking a paper pulp refiner disc
DE2716728A1 (en) * 1976-04-15 1977-11-03 Enso Gutzeit Oy DISC REFINER
FR2348314A1 (en) * 1976-04-15 1977-11-10 Enso Gutzeit Oy DISC CLEANER
US4114818A (en) * 1976-04-15 1978-09-19 Enso-Gutzeit Osakeyhtio Disk refiner
US4093130A (en) * 1977-03-24 1978-06-06 Koppers Company, Inc. Twin refiner apparatus
US5425508A (en) * 1994-02-17 1995-06-20 Beloit Technologies, Inc. High flow, low intensity plate for disc refiner
DE19808355A1 (en) * 1998-02-27 1999-09-02 Voith Sulzer Papiertech Patent Paper fiber suspension grinding operation for papermaking fibers
US11396726B2 (en) 2018-08-23 2022-07-26 Eastman Chemical Company Air filtration articles
US11414791B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Recycled deinked sheet articles
US11286619B2 (en) 2018-08-23 2022-03-29 Eastman Chemical Company Bale of virgin cellulose and cellulose ester
US11299854B2 (en) 2018-08-23 2022-04-12 Eastman Chemical Company Paper product articles
US11306433B2 (en) 2018-08-23 2022-04-19 Eastman Chemical Company Composition of matter effluent from refiner of a wet laid process
US11313081B2 (en) 2018-08-23 2022-04-26 Eastman Chemical Company Beverage filtration article
US11332885B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Water removal between wire and wet press of a paper mill process
US11332888B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Paper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en) 2018-08-23 2022-05-24 Eastman Chemical Company Paper bag
US11390996B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Elongated tubular articles from wet-laid webs
US11390991B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Addition of cellulose esters to a paper mill without substantial modifications
US11639579B2 (en) 2018-08-23 2023-05-02 Eastman Chemical Company Recycle pulp comprising cellulose acetate
US11401659B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Process to produce a paper article comprising cellulose fibers and a staple fiber
US11401660B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Broke composition of matter
US11408128B2 (en) 2018-08-23 2022-08-09 Eastman Chemical Company Sheet with high sizing acceptance
US11230811B2 (en) 2018-08-23 2022-01-25 Eastman Chemical Company Recycle bale comprising cellulose ester
US11414818B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Dewatering in paper making process
US11420784B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Food packaging articles
US11421387B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Tissue product comprising cellulose acetate
US11421385B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Soft wipe comprising cellulose acetate
US11441267B2 (en) 2018-08-23 2022-09-13 Eastman Chemical Company Refining to a desirable freeness
US11466408B2 (en) 2018-08-23 2022-10-11 Eastman Chemical Company Highly absorbent articles
US11479919B2 (en) 2018-08-23 2022-10-25 Eastman Chemical Company Molded articles from a fiber slurry
US11492755B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Waste recycle composition
US11492757B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Composition of matter in a post-refiner blend zone
US11492756B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Paper press process with high hydrolic pressure
US11512433B2 (en) 2018-08-23 2022-11-29 Eastman Chemical Company Composition of matter feed to a head box
US11519132B2 (en) 2018-08-23 2022-12-06 Eastman Chemical Company Composition of matter in stock preparation zone of wet laid process
US11525215B2 (en) 2018-08-23 2022-12-13 Eastman Chemical Company Cellulose and cellulose ester film
US11530516B2 (en) 2018-08-23 2022-12-20 Eastman Chemical Company Composition of matter in a pre-refiner blend zone
US11118313B2 (en) 2019-03-21 2021-09-14 Eastman Chemical Company Ultrasonic welding of wet laid nonwoven compositions
US11668050B2 (en) 2019-03-21 2023-06-06 Eastman Chemical Company Ultrasonic welding of wet laid nonwoven compositions

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