US751139A - Alfeed beddies - Google Patents
Alfeed beddies Download PDFInfo
- Publication number
- US751139A US751139A US751139DA US751139A US 751139 A US751139 A US 751139A US 751139D A US751139D A US 751139DA US 751139 A US751139 A US 751139A
- Authority
- US
- United States
- Prior art keywords
- pulp
- peat
- water
- fibers
- disintegrating
- 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
- 239000003415 peat Substances 0.000 description 90
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 78
- 239000000835 fiber Substances 0.000 description 76
- 229920001131 Pulp (paper) Polymers 0.000 description 46
- 238000000034 method Methods 0.000 description 42
- 238000003490 calendering Methods 0.000 description 14
- 239000002245 particle Substances 0.000 description 12
- 238000003825 pressing Methods 0.000 description 12
- 239000002253 acid Substances 0.000 description 10
- 239000003795 chemical substances by application Substances 0.000 description 8
- 239000002023 wood Substances 0.000 description 8
- 241000681094 Zingel asper Species 0.000 description 6
- 239000000159 acid neutralizing agent Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 229940035295 Ting Drugs 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000003472 neutralizing Effects 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
- D21H27/38—Multi-ply at least one of the sheets having a fibrous composition differing from that of other sheets
Definitions
- the object of my invention is to convert in a continuous process raw peat as obtained directly from the bog into a smooth, consistent, and homogeneous pulp suitable for papermaking. I accomplish this by subjecting the raw peat to a continuous series of successive mechanical treatments, whereby the raw peat is converted into paper and paper products.
- Figure 1 is a sectional view showing a means for conveying the peat from the bog to the disintegrator, also showing a portion of a separating-trough.
- Fig. 2 is a similar view showing a settling-tank and a portion of a separating-trough.
- Fig. 8 is a like view of a stirring tank or reservoir.
- Fig. 4: is an elevation of a rotary crusher.
- Fig. 5 is a sectional view of the disintegrating-tank used subsequently to the crushing operation.
- Fig. 6 is a sectional view of the separating and mixing tanks used subsequently to the crushing and disintegrating operations, and
- Fig. 7 is a sectional view of a sheet-making device which may be used in connection with my process.
- the peat, whlch in some cases may have to be transported by means of suitable vehicles to a certain distance, is extracted from the bog by an apparatus such as is shown in Fig. l in the accompanying drawings.
- Any suitable excavating and conveying device 1 may be used to transfer the peat from the bog to the disintegrator 2.
- This disintegrator may be of any desired form.
- the form which I prefer and which is illustrated in the drawings shows a vertical chamber provided with a vertical shaft 3, carrying blunt knives 4, by means of which the peat is roughly disintegrated.
- the shaft and the arms carried thereby may be rotated by any suitable means connected with a source of power such as is shown at 5.
- the conduit may be one hundred or' more meters in length, according to the distance which it is required to transport the material.
- the settling-tank and the succeeding devices may thus be housed in a suitable factory at a distance from the bog. 4
- the baflie-plates b are incline'd relative to the flow of the current, as indicated by the arrow on the drawings, toward the direction from which the current comes.
- a screen 0 of a rotary type Near the surface of the water in this tank is arranged a screen 0 of a rotary type.
- This screen has for its object the interception of the lighter fibers which rise to the top of the tank. These fibers are deposited by the action of the screen upon its surface and from thence are transferred to a belt or apron 8, traveling in contact therewith and by means of which they are returned to the tank at a point 9.
- Suitable showers are arranged over the surfaces of the screen and apron, as at c and 10, respectively, to keep the surfaces thereof in efficient working condition.
- the fibers suspended in water are transferred through the pipe 11 by means of any suitable pumping apparatus, to be further disintegrated in the devices d and 62'.
- the pulp is preferably conducted to a reservoir or tank 0 provided with stirring devices, as shown, to keep the fibrous matter uniformly suspended in the water. While in this tank there may be added to the pulp a binding material, such as a solution of resin, and eventually a certain quantity of wood-pulp or the like, or in case the acidity has not been completely removed from the pulp by the washing to which it has been subjected a neutralizing agent, such as asolution of soda or of lime-water, may be added to the pulp while in this tank.
- a binding material such as a solution of resin, and eventually a certain quantity of wood-pulp or the like, or in case the acidity has not been completely removed from the pulp by the washing to which it has been subjected
- a neutralizing agent such as asolution of soda or of lime-water
- the pulp is fed from this tank a to the disintegrating and beating devices (Z d, in which the knots and particles of wood, long fibers, &c.,' contained in the pulp are disintegrated, the pulp is converted into a more uniform consistency, and the fibers separated and distributed evenly in suspension in the water.
- Z d disintegrating and beating devices
- the device (Z, Fig. 4, is a crushing device of the type known as edge-runners, in which the knots and wood particles, stems, &c., are ground and crushed between the disks and pan 2' and it; but any other type of crusher may of course be used. From this crushing device the pulp is conducted to the device d, Fig. 5, of the well-known form of Hollander rag-engine or beating-engine. In this the fibers are torn apart and the pulp reduced to the proper condition for use in papermaking machinery.
- the pulp still contains, as compared with ground wood-pulp, particles of varying character and density. These may be partly removed by conducting the pulp over a sand-trap or series of baifie-plates Z1 as in Fig. 6, by means of which the denser particles are removed before the pulp is admitted to a reservoir 6, provided with a stirrer to prevent settling of the fibrous matter.
- the elimination of irregularities in the pulp product may, however, be more effectively done and an absolutely smooth finished product obtained by separately adding to the peat-pulp as an outer layer a surface of absolutely uniform wood-pulp. This'is accomplished in the paper-making machine f f f of any suitable construction by means of several cylinders, such as f and f, Fig.
- the adjustable cylinder f is employed. This cylinder is adjusted by any suitable means to feed a peat-pulp layer to the apron or felt 12, from which it is transferred to the roll f where it is allowed to form a layer of the desired thickness.
- cylinder f is then lowered out of contact with the felt, and cylinder f is raised, so as to feed a thin layer of wood-pulp to the felt 12, which deposits it on the peat-pulp layer on roll
- the alternate action of cylinders f f may be automatic.
- a composite pulp product may be built up of successive layers of difi erent varieties or grades of pulp. For instance, one cylinder may deposit peat-pulp, another wood-pulp, and another a mixture in any desired proportions of peat and wood pulps.
- the pulp board or paper having been formed is dried in the usual manner by means of drying-cylinders, either in the usual continuous paper-making machines or with the help of the known intermittingly-working presses. In every case the sheet must be passed between calender .rolls f which impart a smooth surface to the board or paper. When completed, the product possesses as even a texture and smooth a finish as paper and board made from wood-pulp.
- the process of converting raw peat into a homogeneous pulp product comprising the following steps: disintegrating the raw peat, separating heavier and inorganic matter; adding wood-pulp; crushing the fibers; tearing apart and separating said fibers, and converting the resultant pulp into a sheet.
- the process of converting raw peat into a homogeneous pulp product comprising the following steps: disintegrating the raw peat; separating heavier and inorganic matter; adding wood-pulp; crushing the fibers; tearing apart and separating saidlfibers; converting the resultant pulp into a sheet; overlaying said sheet with wood-pulp, and pressing and calendering said sheet.
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- Paper (AREA)
Description
PATENTED PEB. 2, 1904.
A. BBDDIES.
PROCESS OF CONVERTING RAW PEAT INTO PAPER PULP.
APPLICATION FILED AUG. 5, 1902.
N0 MODEL.
UNITED STATES Patented February 2, 1904.
ALFRED BEDDIES, OF BERLIN, GERMANY.
PROCESS OF CONVERTING RAW PEAT INTO PAPER-PULP.
SPECIFICATION forming part of Letters Patent No. 751,139, dated February 2, 1904;.
Application filed August '5, 1902. Serial No. 118,442. (No specimens.)
To all whom it may concern:
Be it known that I, ALFRED BEDDIES, a subject of the German Emperor, residing at Hannoverschestrasse 1, Berlin, Germany, have invented a certain new and useful Process of Converting Raw Peat into Paper-Pulp, of which the following is a specification.
The object of my invention is to convert in a continuous process raw peat as obtained directly from the bog into a smooth, consistent, and homogeneous pulp suitable for papermaking. I accomplish this by subjecting the raw peat to a continuous series of successive mechanical treatments, whereby the raw peat is converted into paper and paper products.
It is well known that by a simple process of grinding pulp of comparatively uniform consistency may be obtained from wood and pulp and paper made in a continuous operation at the same place of manufacture. This process is not available for peat by reason of its complex and heterogeneous character, whereas wood possesses a comparatively uniform and homogeneous texture. By the process about to be described I produce directly from raw peat by mechanical or physical means a uniform pulp or pulp product in a continuous operation.
In the accompanying drawings there is illustrated schematically and in the way of an example the apparatus employed in carrying out my process. The different views are numbered in the order of sequence in which the various mechanical devices are employed.
Figure 1 is a sectional view showing a means for conveying the peat from the bog to the disintegrator, also showing a portion of a separating-trough. Fig. 2 is a similar view showing a settling-tank and a portion of a separating-trough. Fig. 8 is a like view of a stirring tank or reservoir. Fig. 4: is an elevation of a rotary crusher. Fig. 5 is a sectional view of the disintegrating-tank used subsequently to the crushing operation. Fig. 6 is a sectional view of the separating and mixing tanks used subsequently to the crushing and disintegrating operations, and Fig. 7 is a sectional view of a sheet-making device which may be used in connection with my process.
The peat, whlch in some cases may have to be transported by means of suitable vehicles to a certain distance, is extracted from the bog by an apparatus such as is shown in Fig. l in the accompanying drawings. Any suitable excavating and conveying device 1 may be used to transfer the peat from the bog to the disintegrator 2. This disintegrator may be of any desired form. The form which I prefer and which is illustrated in the drawings shows a vertical chamber provided with a vertical shaft 3, carrying blunt knives 4, by means of which the peat is roughly disintegrated. The shaft and the arms carried thereby may be rotated by any suitable means connected with a source of power such as is shown at 5. broken and tempered, water being introduced at 6, the earthy matter, stones, and heavier matter being separated from the peat in the conduit or trough b. A current of water is supplied to this trough near the inlet to the sameby a pipe 6. The bottom of this trough is provided with inclined baifie-plates 6 the purpose of which is to intercept the heavier particles and sediment carried by the current. The fibers and lighter particles are floated along the trough by the water-current to a settling-tank c, of larger area than the conduit and in which by reason of the checking of the flow the fibers and other matter carried by'the current are deposited. The length of this conduit may be regulated according to conditions under which the processis carried out. It may be from twenty to fifty meters in length where the apparatus for further disintegrating and purifying the peat is situated in proximity to the source of raw material; but where this apparatus is situated at a remote distance from the source of raw material the conduit may be one hundred or' more meters in length, according to the distance which it is required to transport the material. The settling-tank and the succeeding devices may thus be housed in a suitable factory at a distance from the bog. 4
In the conduit 6 the baflie-plates b are incline'd relative to the flow of the current, as indicated by the arrow on the drawings, toward the direction from which the current comes. By means of treatment of water as In this disintegrator the peat is above described not only are the larger and heavier constituents of the peat separated out, but the acids contained in the peat are washed out by the water.
From the settling-tank c the overflow of the water is conducted away at the point marked 7 in the drawings. Near the surface of the water in this tank is arranged a screen 0 of a rotary type. This screen has for its object the interception of the lighter fibers which rise to the top of the tank. These fibers are deposited by the action of the screen upon its surface and from thence are transferred to a belt or apron 8, traveling in contact therewith and by means of which they are returned to the tank at a point 9. Suitable showers are arranged over the surfaces of the screen and apron, as at c and 10, respectively, to keep the surfaces thereof in efficient working condition.
From the settling-tank c the fibers suspended in water are transferred through the pipe 11 by means of any suitable pumping apparatus, to be further disintegrated in the devices d and 62'. Before proceeding to these disintegrating devices the pulp is preferably conducted to a reservoir or tank 0 provided with stirring devices, as shown, to keep the fibrous matter uniformly suspended in the water. While in this tank there may be added to the pulp a binding material, such as a solution of resin, and eventually a certain quantity of wood-pulp or the like, or in case the acidity has not been completely removed from the pulp by the washing to which it has been subjected a neutralizing agent, such as asolution of soda or of lime-water, may be added to the pulp while in this tank. The pulp is fed from this tank a to the disintegrating and beating devices (Z d, in which the knots and particles of wood, long fibers, &c.,' contained in the pulp are disintegrated, the pulp is converted into a more uniform consistency, and the fibers separated and distributed evenly in suspension in the water.
The device (Z, Fig. 4, is a crushing device of the type known as edge-runners, in which the knots and wood particles, stems, &c., are ground and crushed between the disks and pan 2' and it; but any other type of crusher may of course be used. From this crushing device the pulp is conducted to the device d, Fig. 5, of the well-known form of Hollander rag-engine or beating-engine. In this the fibers are torn apart and the pulp reduced to the proper condition for use in papermaking machinery.
Notwithstanding the above series of mechanical treatments, the pulp still contains, as compared with ground wood-pulp, particles of varying character and density. These may be partly removed by conducting the pulp over a sand-trap or series of baifie-plates Z1 as in Fig. 6, by means of which the denser particles are removed before the pulp is admitted to a reservoir 6, provided with a stirrer to prevent settling of the fibrous matter. The elimination of irregularities in the pulp product may, however, be more effectively done and an absolutely smooth finished product obtained by separately adding to the peat-pulp as an outer layer a surface of absolutely uniform wood-pulp. This'is accomplished in the paper-making machine f f f of any suitable construction by means of several cylinders, such as f and f, Fig. 7 the position of which is preferably adjustable, and subsequent calendering of the product between calender-rolls f When an entire peat-pulp product is desired, the peat fibers are led from the reservoir 6 to the paper-machine by the pipe 0'. \Vhen a wood-pulp as above mentioned is desired, the adjustable cylinder f is employed. This cylinder is adjusted by any suitable means to feed a peat-pulp layer to the apron or felt 12, from which it is transferred to the roll f where it is allowed to form a layer of the desired thickness. The cylinder f" is then lowered out of contact with the felt, and cylinder f is raised, so as to feed a thin layer of wood-pulp to the felt 12, which deposits it on the peat-pulp layer on roll The alternate action of cylinders f f may be automatic.
There may be three or four or more, adjustable or not adjustablacylinders arranged similarly to those shown in Fig. 7 with means to cause any one of them to be placed in or withdrawn from working relation to the felt 12 and roll f By this means a composite pulp product may be built up of successive layers of difi erent varieties or grades of pulp. For instance, one cylinder may deposit peat-pulp, another wood-pulp, and another a mixture in any desired proportions of peat and wood pulps.
The pulp board or paper having been formed is dried in the usual manner by means of drying-cylinders, either in the usual continuous paper-making machines or with the help of the known intermittingly-working presses. In every case the sheet must be passed between calender .rolls f which impart a smooth surface to the board or paper. When completed, the product possesses as even a texture and smooth a finish as paper and board made from wood-pulp.
It is necessary that the peat be subjected to all of the treatments described in order to obtain therefrom a smooth and uniform product, as each operation contributes its share to producing the result.
By the process described I have succeeded in converting an irregular and heterogeneous raw material into a product of regular and consistent texture solely by physical treatment.
Having thus described my invention, the following is what I claim as new therein and desire to secure by Letters Patent:
1. The process of converting raw peat into a homogeneous pulp product, comprising the following steps: disintegrating the raw peat, separating heavier and inorganic matter; adding wood-pulp; crushing the fibers; tearing apart and separating said fibers, and converting the resultant pulp into a sheet.
2. The process of converting raw peat into a homogeneous pulp product, comprising the following steps: disintegrating the raw peat; separating heavier and inorganic matter; adding wood-pulp; crushing the fibers; tearing apart and separating saidlfibers; converting the resultant pulp into a sheet; overlaying said sheet with wood-pulp, and pressing and calendering said sheet.
3. The process of converting raw peat into a homogeneous pulp .product, comprising the following steps: disintegrating the raw peat; separating heavier and inorganic matter; crushing the fibers; tearing apart and separating said fibers; forming with the resultant pulp a sheet built of successive layers of peat-pulp and wood-pulp, and pressing and calendering said sheet.
4. The process of converting raw peat into a homogeneous pulp product, which consists in disintegrating the raw peat while subjecting it to treatment with water; separating heavier and inorganic matter by means of a flow of water; checking the flow and allowing fibrous matter to settle; crushing the harder and knotty portions of fibrous matter evenly throughout a body of water, and converting the same into a sheet.
5. The process of converting raw peat into a homogeneous pulp product, which consists in excavating the peat from the bog, disintegrating the same while subjecting to treatment with water, further separating the peat by means of water, separating heavier and inorganic matter by means of a flow of water, checking the flow and allowing fibrous matter to settle, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of water, and converting the same into a sheet.
6. The process of converting raw peat into a homogeneous pulp product, which consists in excavating the peat from the bog, disintegrating the same while subjecting to treatment with water, separating heavier and inorganic matter by means of a flow of water, checking the flow and allowing fibrous matter to settle, distributing the fibers throughout a body of water, adding a cementing agent, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of Water, and converting the same into a sheet.
7 The process of converting raw peat into a homogeneous pulp product, which consists in excavating the peat from the bog, disintegrating the same while subjecting to treatment with water, separating heavier and inorganic matter by means of a flow of water, checking the flow and allowing fibrous matter to settle, distributing the fibers throughout a body of water, adding a cementing agent and wood-pulp, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of water, and converting the same into a sheet.
8. The process of converting raw peat into a homogeneous pulp product, which consists in disintegrating the raw peat, removing heavy and inorganic matter and acid therefrom, settling the fibrous matter, suspending the fibers throughout a body of water While adding anacid-neutralizing agent, conveying the fibrous matter to crushing devices and crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of water, and converting the same into a sheet.
9. The process of converting raw peat into a homogeneous pulp product, which consists in excava'ting'peat from the bog, disintegrating the same, removing heavy and inorganic matter and acid therefrom, settling the fibrous matter, suspending the fibers throughout a body of water while adding an acid-neutralizing agent, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of'water, and converting the same intoa sheet.
10. The process of converting raw peat into a homogeneous pulp product, which consists in excavating peat from the bog, disintegrating the same, removing heavy and inorganic matter and acid therefrom, settling the fibrous matter, suspending the fibers throughout a body of water while adding an acid-neutralizing agent, adding wood-pulp, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of water, converting the same into a sheet, overlaying said sheet with wood-pulp, and pressing and calendering said sheet.
11. The process of converting raw peat into a homogeneous pulp product, which consists in excavating peat from the bog, disintegrating the same, removing heavy and inorganic matter and acid therefrom, settling the fibrous matter, suspending the fibers throughout a body of water while adding an acid-neutralizing agent, adding wood-pulp, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of water, forming in continuous operations a sheet built of successive layers of peat-pulp and wood-pulp, and pressing and calendering said sheet.
12. The process of converting raw peat into a pulp product, which consists in excavating the peat from the bog, disintegrating the same While subjecting it to treatment with water, separating heavier and inorganic matter by means of a flow of Water, checking the flow and allowing fibrous matter to settle, adding Wood-pulp, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of Water, converting the same into a sheet, overlaying said sheet With Wood-pulp, and pressing and calendering said sheet.
13. The process of converting raw peat into a pulp product, which consists in excavating the peat from the bog, disintegrating the same While subjecting to treatment with water, separating heavier and inorganic matter by means of a flow of water, checking the flow and allowing fibrous matter to settle, adding Woodpulp, crushing the harder and knotty portions of fibrous matter, separating and disintegrating the fibers, distributing the fibers evenly throughout a body of Water, forming in continuous operations a sheet built of alternative layers of peat-pulp and Wood-pulp, and pressing and calendering said sheet.
ALFRED BEDDIES.
Witnesses:
WVILLIAM MAYNER, HENRY HASPER.
Publications (1)
Publication Number | Publication Date |
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US751139A true US751139A (en) | 1904-02-02 |
Family
ID=2819632
Family Applications (1)
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US751139D Expired - Lifetime US751139A (en) | Alfeed beddies |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2529335A (en) * | 1947-01-21 | 1950-11-07 | Helland John Gundersen | Preparation of a heat insulating material from peat |
EP0104905A2 (en) * | 1982-09-24 | 1984-04-04 | JOHNSON & JOHNSON INC. | Process for manufacturing a calendered peat moss board |
US20040162654A1 (en) * | 2002-08-01 | 2004-08-19 | Jianbo Lu | System and method for determining a wheel departure angle for a rollover control system with respect to road roll rate and loading misalignment |
-
0
- US US751139D patent/US751139A/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2529335A (en) * | 1947-01-21 | 1950-11-07 | Helland John Gundersen | Preparation of a heat insulating material from peat |
EP0104905A2 (en) * | 1982-09-24 | 1984-04-04 | JOHNSON & JOHNSON INC. | Process for manufacturing a calendered peat moss board |
US4473440A (en) * | 1982-09-24 | 1984-09-25 | Johnson & Johnson Inc. | Calendered peat moss board |
EP0104905A3 (en) * | 1982-09-24 | 1986-03-19 | Johnson & Johnson, Inc. | Calendered peat moss board |
US20040162654A1 (en) * | 2002-08-01 | 2004-08-19 | Jianbo Lu | System and method for determining a wheel departure angle for a rollover control system with respect to road roll rate and loading misalignment |
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