USRE19288E - Method of treating fibrous - Google Patents
Method of treating fibrous Download PDFInfo
- Publication number
- USRE19288E USRE19288E US19288DE USRE19288E US RE19288 E USRE19288 E US RE19288E US 19288D E US19288D E US 19288DE US RE19288 E USRE19288 E US RE19288E
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- passage
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- mixture
- discharge
- coil
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- 238000000034 method Methods 0.000 title description 20
- 239000000243 solution Substances 0.000 description 47
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 45
- 239000000203 mixture Substances 0.000 description 35
- 229920000742 Cotton Polymers 0.000 description 28
- 239000000463 material Substances 0.000 description 20
- 235000011121 sodium hydroxide Nutrition 0.000 description 15
- 238000009835 boiling Methods 0.000 description 12
- 238000001816 cooling Methods 0.000 description 10
- 239000002657 fibrous material Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 5
- 239000003518 caustics Substances 0.000 description 5
- 239000010902 straw Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 230000006978 adaptation Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- 101710110315 Bacchus Proteins 0.000 description 1
- -1 as for example Substances 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 238000004380 ashing Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 238000000926 separation method Methods 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
- My invention relates to a method for treating fibrous materials, as for example, cotton linters,
- dry cotton linters are placed in a kier or digester with, for example, a 1%-4% sodium hydroxide .solution in, for example, the ratio of 6 parts of sodium hydroxide solution to 1 part cotton linters.
- Steam is applied to the kier or digester at a pressure of, for example, 60 pounds and maintained for a period of, for example, 5 hours, after which the pressure is released, the liquor drained oil and the treated linters washed with water,
- the method heretofore used in the treatment of fibrous materials is disadvantageous for many reasons, chief among which are that it involves batch operation, requires large and expensive apparatus, which in operation, presents various problems of control, is expensive to maintain, and, at the same time, is capable of only a limited output.
- the desired treatment for the purification of fibrous materials and desired reduction in viscosity may be eifected in a continuous manner by continuously passing the material to be treated in admixture with a desired 5 solution for effecting the treatment, through a zone wherein the fibrous material is subjected to the action of heat and pressure, the discharge from such a zone being controlled,
- the fibrous material as cotton linters, straw, comminuted wood, or the like, to bepurified, in admixture with a purifying solution
- a purifying solution may be pumped through a passage, the discharge from which is controlled and in which the mixture of fibrous I material and purifying solution is subjected to heat at the desired temperature and maintained under the desired pressure.
- the temperature will desirably be substantially above the boiling point of the treating solution, 1. e. substantially above, and preferably will be above about 140 C.
- cotton linters, straw, comminuted wood or the like may be mixed in a suitable container with a purifying solution, such as a solution of sodium hydroxide, sulphate liquor solution, etc.
- a purifying solution such as a solution of sodium hydroxide, sulphate liquor solution, etc.
- the mixture may be pumped from the container through a coil of tubing, the outlet from which is suitably controlled as, for example,
- A indicates a container desirably fitted with some form of agitating device in which the material to be treated may be mixed with a treating solution.
- B indicates a pump, the suction side of which is connected, with the container A and the discharge side of which is connected to the inlet end of a coil ofpipe C.
- a portion of the coil of pipe C adjacent to the discharge of the pump B is jack- 1 eted as shown at d, the jackets being connected and provided with an inlet and dischargefor steam.
- the coil adjacent its discharge end is jacketed as shown at e, the jackets being connectedand provided with an inlet and discharge for cooling water.
- the portion of the coil intermediate the jackets d, e is covered with insulating material, as for example, asbestos, or the like, as indicated at G.
- the discharge or outlet end of the coil C is connected to a valve casing H, within which is provided a valve seat on which is adapted to seat a conoidal shaped valve 1' provided with a stem 1: extending through a stufiingbox l .in the casing, and provided at its outer end with a head m against which abuts one end of a spring n, the
- the valve casing H is desirably connected to a standpipe Q, which extends upward for a substantial distance and returns to connection with a surge tank or receiving tank R from which a discharge S is provided. Adjacent the upper portion of the stand pipe Q a vent t, provided with a suitable valve u, is provided. If desired the standpip'e Q may be omitted and the valve casing connected directly to the surge tank R, or the valve ii may be omitted and the coil C connected directly'to standpipe Q.
- Pipe V is connected to the discharge side of a pump X, the inlet side, through a pipe Y, being connected with a suitable source of purifying solution or of water.
- cotton linters are placed in the container A together with an aqueous caustic soda I solution of .5 %-,-2% strength, in the-proportion of say 1 part of cotton linters to parts of caustic soda solution by weight.
- the mixture of cotton linters and caustic liquor is then pumped bythe pump B through the coil C at. a velocity of say 'about 2 feet per second.
- the mixture of cotton linters and caustic solution are brought to a suitits up 'standpipe Q and down into tank 1%.
- The] standplpe Q may be made of any desired height
- the section of the coilprovided with steam jackets d may be of any suitable length to obtain the desiredtemperature and the portion of coil provided with cooling jackets 2 may be of any lieve any jani.
- the valve will tend to unitormly control discharge from, and hence equalize the pressure on the coil C.
- the mixture of cotton linters and caustic solution discharged from the' coil 0 will, after passing-through the valve, pass its purpose being primarily tocooperate with the valve i in controlling the discharge from and through the valve i.
- the standpipe Q is provided with a vent controlled by a suitable valve in order to prevent or control the creation of a vacuum by the downwardly passing cotton linters and solution upon the column communicating with the coil. .7
- spent caustic soda solution or water is desirably pumped by pump K through the pipe V and passes with the cotton linters and solution discharged from the coil through the valve 1'.
- the spent caustic soda solution or water supplied by pump X acts to increase the ratio of caustic soda solution to cotton over that of the mixture discharged from the coil with the result that the mixture will more readily pass
- the cotton linters. discharged into tank B. may be drawn therefrom as desired for separation from the purifying solution, ashing and subjecting to such other treatme t as may be desired.
- the productwithdrawn from tank R as for example, cotton linters, straw, comminuted wood, or the like, which may have been treated, will be found to have great purity, to be free from waxes, 1
- oils and from hulls and encrusting materials and to be of a desired reduced viscosity.
- the product will be obtained with great reduction of time
- the precise temperature and pressure used and the time or treatment will depend upon the material treated and the desired characteristics of purity, reduced viscosity, soft ness, etc. desired. It will be appreciated that the time oi? treatment may be readily varied for the treatment of any particular material and for the production of any particular grade of product by a regulation of the velocity at which the material and the extent of the zone or coil.
- the method of treating fibrous material which includes forcing a mixture of fibrous ma- 14o terial and a treating solution under pressure through a passage, heating the mixture adjacent the'inletend of said passage, cooling the mixture adjacent the discharge end of said passage'and controlling thedischargejrom said passage.
- the method of treating cotton linters which includes forcing a mixture of cotton linters and a caustic soda solution under, pressurethrough apassage, heating the mixture at a point within said passage, cooling the adjacent the 56 discharge end of said passage and controlling the discharge from said passage.
- the method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and an alkaline treating solution through a passage, heating the mixture within the passage to a temperature substantially above the boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to a temperature below the boilingpoint of the treating solution and controlling the discharge from said passage.
- the method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and an alkaline treating solution comprising an aqueous solution of caustic soda, through a passage, heating the mixture within the passage to a temperature higher than about 140 C., cooling the mixture adjacent the discharge end of said passage to a temperature below the boiling point at atmospheric pressure of the treating solution and controlling the, discharge from said passage.
- the method of treating cotton linters which includes forcing a mixture of cotton lintersand a treating solution comprising an aqueous solution of caustic soda, through a passage, heating the mixture within the passage to a temperature substantially abovethe boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to' a temperature below the boiling point of the treating solution and controlling the discharge from said passage.
- the method of treating cotton linters which includes forcing a mixture of cotton linters and a treating solution comprising an aqueous solution containing about 0.5-2% sodium hydroxide by weight, through a passage, heating the mixture within the passage to a temperature substantially above the boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to a temperature below the boiling point of the treating solution and controlling the discharge from said passage.
- the method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and a treating solution comprising an aqueous solution containing about 0.5-2% sodium hydroxide by weight through a passage, heating the mixture within the passage to a temperature of about 165 C., cooling the mixture adjacentthe discharge end of said passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage.
- the method of treating fibrous cellulosic .material which includes forcing a mixture of fibrous cellulosic material and a treating solution through a passage, introducing steam into the passage to heat the mixture to a temperature substantially above the boiling point of the treating solution, cooling the mixture adjacent to the discharge end of the passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage.
- the method of treating cotton linters which includes forcing a mixture of cotton linters and a treating solution comprising an aqueous solution containing about 0.5-2 by weight of sodium hydroxide through a passage, introducing steam into the passage to eifect heating of the mixture to a temperature higher than about 140 C., cooling the mixture adjacent the discharge end of the passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage.
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- Paper (AREA)
Description
Aug. 28, 1934. T. w. BAccHUs R- 19,288
' METHOD OF TREATING FIBROUS MATERIALS Original Filed Sept. 23, 1930 Reissuecl Aug 28, 1934 UNITED STATES PATENT OFFICE METHOD OF TREATING FmRoUs V MA'rERIaLs Thomas W. Bacchus, Wilmington, Del., assignor to Hercules Powder Company, -Wilmington, Del., a corporation of Delaware 9 Claims. (01. 92-7) My invention relates to a method for treating fibrous materials, as for example, cotton linters,
straw, wood, or the like. In the preparation of fibrous materials for various purposes, it is desired to efiect removal from the materials of hull particles or lignous impurities, to efiect saponification of the oils and emulsification of.the waxes, etc., and for certain purposes, as in the preparation of cellulose 10 materialsfifor nitration, it is desirable to effect reduction in the viscosity of such materials.
Heretofore in the treatment of fibrous materials, it has been generally customary to place the materials in large kiers or digesters together with an aqueous caustic soda solution of suitable concentration, or with sulphate liquor, or other purifying solution, and the contents heated, either directly or indirectly, under a pressure between about atmospheric and 150 pounds, depending upon the result desired to be obtained. The treatment in the kiers or digesters has heretofore been continued for from 1 to 18 hours or more. At the end of the period of treatement the pressure is released from the kiers or digesters, the liquor drained from the material and the material washed, bleached, dried, etc. as desired.
As an example of the treatment of fibrous materials by methods heretofore known, dry cotton linters are placed in a kier or digester with, for example, a 1%-4% sodium hydroxide .solution in, for example, the ratio of 6 parts of sodium hydroxide solution to 1 part cotton linters. Steam is applied to the kier or digester at a pressure of, for example, 60 pounds and maintained for a period of, for example, 5 hours, after which the pressure is released, the liquor drained oil and the treated linters washed with water,
subjected to treatment with a suitable bleaching agent and finally dried.
The method heretofore used in the treatment of fibrous materials, as above briefiy outlined, is disadvantageous for many reasons, chief among which are that it involves batch operation, requires large and expensive apparatus, which in operation, presents various problems of control, is expensive to maintain, and, at the same time, is capable of only a limited output.
Now, in accordance with my invention, I have 0 discovered that the desired treatment for the purification of fibrous materials and desired reduction in viscosity may be eifected in a continuous manner by continuously passing the material to be treated in admixture with a desired 5 solution for effecting the treatment, through a zone wherein the fibrous material is subjected to the action of heat and pressure, the discharge from such a zone being controlled,
In the practical adaptation of the method in accordance with my invention, for example, the fibrous material, as cotton linters, straw, comminuted wood, or the like, to bepurified, in admixture with a purifying solution may be pumped through a passage, the discharge from which is controlled and in which the mixture of fibrous I material and purifying solution is subjected to heat at the desired temperature and maintained under the desired pressure. The temperature will desirably be substantially above the boiling point of the treating solution, 1. e. substantially above, and preferably will be above about 140 C.
As a more specific illustration of the practical adaptation of my invention, cotton linters, straw, comminuted wood or the like, may be mixed in a suitable container with a purifying solution, such as a solution of sodium hydroxide, sulphate liquor solution, etc. The mixture may be pumped from the container through a coil of tubing, the outlet from which is suitably controlled as, for example,
by providing a suitable' valve, connecting with a 30 standpipe, or otherwise providing for control 01' the outlet.
Having now indicated in a general way the nature and purpose of my invention, I will more specifically describe a preferred practical adapta- 35 tion thereof by way of illustration in connection with, for example, the purification of cotton linters and with reference to the accompanying drawing by which is illustrated diagrammatically a form of apparatus adaptable for the carrymg out of the method embodying myinvention.
Referring to the drawing, A indicates a container desirably fitted with some form of agitating device in which the material to be treated may be mixed with a treating solution. B indicates a pump, the suction side of which is connected, with the container A and the discharge side of which is connected to the inlet end of a coil ofpipe C. A portion of the coil of pipe C adjacent to the discharge of the pump B is jack- 1 eted as shown at d, the jackets being connected and provided with an inlet and dischargefor steam. The coil adjacent its discharge end is jacketed as shown at e, the jackets being connectedand provided with an inlet and discharge for cooling water. The portion of the coil intermediate the jackets d, e, is covered with insulating material, as for example, asbestos, or the like, as indicated at G.
The discharge or outlet end of the coil C is connected to a valve casing H, within which is provided a valve seat on which is adapted to seat a conoidal shaped valve 1' provided with a stem 1: extending through a stufiingbox l .in the casing, and provided at its outer end with a head m against which abuts one end of a spring n, the
- other end of which abuts against an adjustable stop 0 "carried by a bracket p attached to the casing. The valve casing H is desirably connected to a standpipe Q, which extends upward for a substantial distance and returns to connection with a surge tank or receiving tank R from which a discharge S is provided. Adjacent the upper portion of the stand pipe Q a vent t, provided with a suitable valve u, is provided. If desired the standpip'e Q may be omitted and the valve casing connected directly to the surge tank R, or the valve ii may be omitted and the coil C connected directly'to standpipe Q.
Connected to the discharge or outlet end of the coil C, or connected to the coil adjacent. the dischargeor outlet end, is a pipe V provided with a suitable valve w. Pipe V is connected to the discharge side of a pump X, the inlet side, through a pipe Y, being connected with a suitable source of purifying solution or of water.
In carrying out the method in accordance with my invention, in the apparatus'above described, for example, cotton linters are placed in the container A together with an aqueous caustic soda I solution of .5 %-,-2% strength, in the-proportion of say 1 part of cotton linters to parts of caustic soda solution by weight. The mixture of cotton linters and caustic liquor is then pumped bythe pump B through the coil C at. a velocity of say 'about 2 feet per second. The mixture of cotton linters and caustic solution are brought to a suitits up 'standpipe Q and down into tank 1%. The] standplpe Q may be made of any desired height,
able temperature, say about 165 C. by the introduction of steam into the jackets d or, if desired, live steam may be injected into the coil at a suitable point or points to obtain the desired temperature.- The temperature ofthe'mixture of cotton linters and caustic solution is maintained at approximatlylfifi" C. in its travel through that part of the coil whlch is insulated,
and is suitably reduced toa point below the boiling point of the caustic solution before discharge from the coil through the introduction of cooling water into the jackets e. -The mixture is desirably maintained under a pressure of about 200 lbs. per square inch in its passage through the coil, by adjustment of valve 1. P
In the treatment of cotton linters as indicated above, the section of the coilprovided with steam jackets d may be of any suitable length to obtain the desiredtemperature and the portion of coil provided with cooling jackets 2 may be of any lieve any jani. Thus, the valve will tend to unitormly control discharge from, and hence equalize the pressure on the coil C. The mixture of cotton linters and caustic solution discharged from the' coil 0 will, after passing-through the valve, pass its purpose being primarily tocooperate with the valve i in controlling the discharge from and through the valve i.
is passed through the zoneoi' treatment or coil equalize the pressure on the coil C. Under certain circumstances the control of the discharge from the coil 0 may be eflected by connecting the discharge directly with the standpipe Q, the valvei being omitted. In such case the standpipe Q would be made of sufllcient height' so that desired control of the discharge from the coil would be eiiected through the pressure of the column of cotton linters and solution in the standpipe. It will be noted thatthe standpipe is provided with a vent controlled by a suitable valve in order to prevent or control the creation of a vacuum by the downwardly passing cotton linters and solution upon the column communicating with the coil. .7
, During the passage of cotton linters and solution through the coil C spent caustic soda solution or water is desirably pumped by pump K through the pipe V and passes with the cotton linters and solution discharged from the coil through the valve 1'. The spent caustic soda solution or water supplied by pump X acts to increase the ratio of caustic soda solution to cotton over that of the mixture discharged from the coil with the result that the mixture will more readily pass The cotton linters. discharged into tank B. may be drawn therefrom as desired for separation from the purifying solution, ashing and subjecting to such other treatme t as may be desired.
The productwithdrawn from tank R, as for example, cotton linters, straw, comminuted wood, or the like, which may have been treated, will be found to have great purity, to be free from waxes, 1
oils and from hulls and encrusting materials and to be of a desired reduced viscosity. The product will be obtained with great reduction of time,
labor, and with very simple apparatus.
It will be appreciated that in the carrying out 113 of my invention the precise temperature and pressure used and the time or treatment will depend upon the material treated and the desired characteristics of purity, reduced viscosity, soft ness, etc. desired. It will be appreciated that the time oi? treatment may be readily varied for the treatment of any particular material and for the production of any particular grade of product by a regulation of the velocity at which the material and the extent of the zone or coil.
It will be appreciated that the method in accordance with my invention is not dependent upon, the use of any particular form of apparatus and that-that described herein is disclosed merely forpurposes of illustration. It will be further appreciated that in carrying out the method in accordance with my invention various modifications may be made without departingfrom my inven 135 tion. I
"What I claim and desire protect by Patent is:.-
1. The method of treating fibrous material which includes forcing a mixture of fibrous ma- 14o terial and a treating solution under pressure through a passage, heating the mixture adjacent the'inletend of said passage, cooling the mixture adjacent the discharge end of said passage'and controlling thedischargejrom said passage.
2; The method of treating cotton linters which includes forcing a mixture of cotton linters and a caustic soda solution under, pressurethrough apassage, heating the mixture at a point within said passage, cooling the adjacent the 56 discharge end of said passage and controlling the discharge from said passage.
3. The method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and an alkaline treating solution through a passage, heating the mixture within the passage to a temperature substantially above the boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to a temperature below the boilingpoint of the treating solution and controlling the discharge from said passage.
4. The method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and an alkaline treating solution comprising an aqueous solution of caustic soda, through a passage, heating the mixture within the passage to a temperature higher than about 140 C., cooling the mixture adjacent the discharge end of said passage to a temperature below the boiling point at atmospheric pressure of the treating solution and controlling the, discharge from said passage.
5. The method of treating cotton linters which includes forcing a mixture of cotton lintersand a treating solution comprising an aqueous solution of caustic soda, through a passage, heating the mixture within the passage to a temperature substantially abovethe boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to' a temperature below the boiling point of the treating solution and controlling the discharge from said passage.
6. The method of treating cotton linters which includes forcing a mixture of cotton linters and a treating solution comprising an aqueous solution containing about 0.5-2% sodium hydroxide by weight, through a passage, heating the mixture within the passage to a temperature substantially above the boiling point of the treating solution at atmospheric pressure, cooling the mixture adjacent the discharge end of said passage to a temperature below the boiling point of the treating solution and controlling the discharge from said passage.
' 7. The method of treating fibrous cellulosic material which includes forcing a mixture of fibrous cellulosic material and a treating solution comprising an aqueous solution containing about 0.5-2% sodium hydroxide by weight through a passage, heating the mixture within the passage to a temperature of about 165 C., cooling the mixture adjacentthe discharge end of said passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage. 8. The method of treating fibrous cellulosic .material which includes forcing a mixture of fibrous cellulosic material and a treating solution through a passage, introducing steam into the passage to heat the mixture to a temperature substantially above the boiling point of the treating solution, cooling the mixture adjacent to the discharge end of the passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage.
9. The method of treating cotton linters which includes forcing a mixture of cotton linters and a treating solution comprising an aqueous solution containing about 0.5-2 by weight of sodium hydroxide through a passage, introducing steam into the passage to eifect heating of the mixture to a temperature higher than about 140 C., cooling the mixture adjacent the discharge end of the passage to a temperature below the boiling point of the treating solution at atmospheric pressure and controlling the discharge from the passage.
THOMAS W. BACCHUS.
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USRE19288E true USRE19288E (en) | 1934-08-28 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2573321A (en) * | 1946-01-19 | 1951-10-30 | Certain Teed Prod Corp | Defibering apparatus |
US2573322A (en) * | 1946-01-19 | 1951-10-30 | Certain Teed Prod Corp | Defibering apparatus |
US2771361A (en) * | 1951-12-07 | 1956-11-20 | Process Evaluation Devel | Defibration processes |
-
0
- US US19288D patent/USRE19288E/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2573321A (en) * | 1946-01-19 | 1951-10-30 | Certain Teed Prod Corp | Defibering apparatus |
US2573322A (en) * | 1946-01-19 | 1951-10-30 | Certain Teed Prod Corp | Defibering apparatus |
US2771361A (en) * | 1951-12-07 | 1956-11-20 | Process Evaluation Devel | Defibration processes |
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