US331713A - John w - Google Patents
John w Download PDFInfo
- Publication number
- US331713A US331713A US331713DA US331713A US 331713 A US331713 A US 331713A US 331713D A US331713D A US 331713DA US 331713 A US331713 A US 331713A
- Authority
- US
- United States
- Prior art keywords
- pyroxyline
- solvent
- paper
- pulp
- sheets
- 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
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- FJWGYAHXMCUOOM-QHOUIDNNSA-N [(2S,3R,4S,5R,6R)-2-[(2R,3R,4S,5R,6S)-4,5-dinitrooxy-2-(nitrooxymethyl)-6-[(2R,3R,4S,5R,6S)-4,5,6-trinitrooxy-2-(nitrooxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-3,5-dinitrooxy-6-(nitrooxymethyl)oxan-4-yl] nitrate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O)O[C@H]1[C@@H]([C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@@H](CO[N+]([O-])=O)O1)O[N+]([O-])=O)CO[N+](=O)[O-])[C@@H]1[C@@H](CO[N+]([O-])=O)O[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O FJWGYAHXMCUOOM-QHOUIDNNSA-N 0.000 description 62
- 239000002904 solvent Substances 0.000 description 56
- 229920001220 nitrocellulos Polymers 0.000 description 54
- 238000000034 method Methods 0.000 description 16
- 244000144992 flock Species 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 8
- 150000001875 compounds Chemical class 0.000 description 6
- 230000001105 regulatory Effects 0.000 description 6
- 238000009738 saturating Methods 0.000 description 6
- DSSYKIVIOFKYAU-UHFFFAOYSA-N Camphor Chemical compound C1CC2(C)C(=O)CC1C2(C)C DSSYKIVIOFKYAU-UHFFFAOYSA-N 0.000 description 4
- 229960000846 Camphor Drugs 0.000 description 4
- 241000723346 Cinnamomum camphora Species 0.000 description 4
- 229930007890 camphor Natural products 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 235000015096 spirit Nutrition 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000000149 penetrating Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D101/00—Coating compositions based on cellulose, modified cellulose, or cellulose derivatives
- C09D101/08—Cellulose derivatives
- C09D101/16—Esters of inorganic acids
- C09D101/18—Cellulose nitrate
Definitions
- the drawing represents a cylinder papermaking machine for making paper from pyroxyline pulp and sprinkling the same with spirits of camphor or other solvent after it has passed over the drying cylinders.
- a a are the two making-cylinders;
- b b the couching-rolls. From these the paper is taken by the endless felt a to the first press-rolls, (l d, where it is slightly pressed between the felt o and another felt, e, which revolves around the upper pressroll.
- the paper is then detached from the first felt and led upon another endless felt, f, which conducts it to the second press-rolls, g 1, where it is further slightly compressed, and, after passing over the guiderolls h h, is carried to the third set of rolls, it, where a greater pressure is imparted, and thence to the steam -hcated cylinders J J, whereitisdried.
- Two finely-perforatedtubes. B B are arranged so as to sprinkle spirits of eamphor upon both sides of the paper as it passes from the drying-cylinders and into a suitable box, 0.
- the pump A supplies the solvent in measured quantities from the tank F, and is driven by means of the crank-shaft D, operated bya belt from the pulley E,which is revolved by power.
- the crank disk is provided with a slot, S, for moving the crankpin from or toward the center of the shaft to increase or decrease the stroke of the pump, and thereby regulate the quantity of solvent to be supplied to the sprinkler.
- This process requires that the sheets made from the pyroxyline pulp be of a thickness proportioned to the amount of liquid solvent to be applied to the same. I recommend a uniform thickness to gage of about one thirty-second of an inch. hen the sheets are much thicker than this, they refuse to absorb the solvent,a-nd when they are made too thin they absorb it too readily, some parts taking more than the necessary supply.
- the box 0 has received enough of the saturated paper for a batch, it is removed and another box substituted for it. After removing the box, it is closed to prevent evaporation of the solvent, and permitted to rest from one to two days, or until the mass of pyroxyline has been thoroughly penetrated by the solvent, after which it is converted into a homogeneous compound in masticating-rolls, or by heat and pressure otherwise applied, as is well understood. It is obvious that this is not the only means of carrying out the present invention. It is not necessary that the pyroxyline paper he made into a continuous sheet, or that the operation be confined to an ordinary papermaking machine.
- a sheet formed from the pyroxyline pulp by any means will answer the purpose, it merely being necessary that it be of the proper thickness. Even when made in small sheets, it would still be possible to sprinkle the proper amount of solvent upon them, and afterward carry out the remainder of the process as already described; but the method I have described and which involves the use of a paper-making machine is more accurate, and for large quantities more economical, and will be found to perform the required operation in a satisfactory manner.
- WVhat Iclaim is 1. The process of making pyroxyline compounds in the following steps: first, grinding pyroxyline in pulp or flock; second, forming the pulp or flock into a thin sheet or sheets; third, applying a suitable solvent to the sheet by sprinkling or equivalent means; fourth, completing the material in masticating-rolls or by the use of heat and pressure, substantially as described.
- pyroxyline compounds consisting of the following steps: first, forming films or sheets from pyroxyline flock or pulp; second, saturating the sheets with the requisite quantity of solvent; third, massing the sheets together in a closed receptacle; fourth, completing the material by means of masticating rolls or heat and pressure, sub stantially as described.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Paper (AREA)
Description
KW 00 8 1 1 A nu D d e Lld n St [PM Uv 0 mm raw w WL O ms F 0 (No Model.)
GOMPOUNDING PYRDXYLINE WITH IT S SOLVENTS IN THEMANUFAGTURE u. PETERS. mw-mm w. Wnhinglm 0.x;
llsrrnn S ra'rns Parent @rrrcno JOHN \V. HYATT,'OF NEVVARK, NEvV JERSEY.
COMPOUNDlNG PYROXYLINE WITH ITS SOLVENTS IN THE MANUFACTURE OF SOUD COMPOUNDS.
SPECIFICATION forming part of Letters Patent No. 331,713, dated December 1, 1.885.
Application filed May 14, 1885.
To all whom it may concern.-
Be it known that I, J oHNXV. Hrnrr, of the city of Xewark, county of Essex, State of New Jersey, have invented certain Improvements in the Process of Combining Pyroxyline with its Solvents in the Manufacture of Solid Oompounds, of which the following is a specification.
In making pyroxyliue compounds it is very difficult to combine the pyroxyline with activesolvents, unless the proportions of such solvents are largely in excess of the amount of pyroxyline used. The reason for this is that the pyroxyline absorbs the solvent so readily that whenever the two come together the greater portion of the solvent is taken up at the first point touched. In a mass of pyroxyline any part which comes into contact with the solvent will first absorb several times its own weight before it permits any of the liquid to seek other parts of the mass. As it is not only unnecessary, but positivcl y objectionable, to use so large a proportion of solvent as the pyroxyline naturally absorbs, the importance of methods by means of which the proportions can be regulated at will has long been recognized by those skilled in this art.
Although it is impossible, under ordinary conditions, to penetrate a large mass of dry pyroxyline with a small quantity of active solvent, still it has been found that the pyroxyline possesses the power, to a very limited extent, of absorbing the solvent from those portions of the mass already saturated. I propose to make use of this limited penetrative power of active solvents in the following process: I first cut the pyroxyline, while in a dampened condition, into a flock, preferring to use for this purpose the machine described in my patent of September 6, 1881, and numbered 246,678. I have found that pulp made in this manner is more suitable for making pyroxyline paper than that ground in an ordinary paper-engine. In order to grind the pyroxyline in this machine, it must contain no more moisture than is necessary to render it non-inflammablesay from six to eight parts of water to each ten parts of pyroxyline. After the pulp is formed, I mix it with water and make it into paper.
SerinlXo. 165,479. (No model.)
The drawing represents a cylinder papermaking machine for making paper from pyroxyline pulp and sprinkling the same with spirits of camphor or other solvent after it has passed over the drying cylinders. a a are the two making-cylinders; b b, the couching-rolls. From these the paper is taken by the endless felt a to the first press-rolls, (l d, where it is slightly pressed between the felt o and another felt, e, which revolves around the upper pressroll. The paper is then detached from the first felt and led upon another endless felt, f, which conducts it to the second press-rolls, g 1, where it is further slightly compressed, and, after passing over the guiderolls h h, is carried to the third set of rolls, it, where a greater pressure is imparted, and thence to the steam -hcated cylinders J J, whereitisdried. Two finely-perforatedtubes. B B, are arranged so as to sprinkle spirits of eamphor upon both sides of the paper as it passes from the drying-cylinders and into a suitable box, 0. The pump A supplies the solvent in measured quantities from the tank F, and is driven by means of the crank-shaft D, operated bya belt from the pulley E,which is revolved by power. The crank disk is provided with a slot, S, for moving the crankpin from or toward the center of the shaft to increase or decrease the stroke of the pump, and thereby regulate the quantity of solvent to be supplied to the sprinkler. This process requires that the sheets made from the pyroxyline pulp be of a thickness proportioned to the amount of liquid solvent to be applied to the same. I recommend a uniform thickness to gage of about one thirty-second of an inch. hen the sheets are much thicker than this, they refuse to absorb the solvent,a-nd when they are made too thin they absorb it too readily, some parts taking more than the necessary supply. The supply of solvent is so regulated that only the proportion necessary to convert the pyroxyline is added. Experience has shown thata mixture, by weight, of one hundred parts pyroXyline, forty parts of alcohol, and forty parts of cam phor is sufficient to accomplish this result. These proportions can be varied at will, according to the necessities of the case, as is well understood by those familiar with this art.
WVhen the box 0 has received enough of the saturated paper for a batch, it is removed and another box substituted for it. After removing the box, it is closed to prevent evaporation of the solvent, and permitted to rest from one to two days, or until the mass of pyroxyline has been thoroughly penetrated by the solvent, after which it is converted into a homogeneous compound in masticating-rolls, or by heat and pressure otherwise applied, as is well understood. It is obvious that this is not the only means of carrying out the present invention. It is not necessary that the pyroxyline paper he made into a continuous sheet, or that the operation be confined to an ordinary papermaking machine. A sheet formed from the pyroxyline pulp by any means will answer the purpose, it merely being necessary that it be of the proper thickness. Even when made in small sheets, it would still be possible to sprinkle the proper amount of solvent upon them, and afterward carry out the remainder of the process as already described; but the method I have described and which involves the use of a paper-making machine is more accurate, and for large quantities more economical, and will be found to perform the required operation in a satisfactory manner.
I do not limit myself to sprinkling the solvent upon the pyroxyline, because by properly regulating the conditions-such as the thickness of the paper and the duration of the contact-itis possible to apply the requisite quantity by dipping the pyroxyline intothe solvent. Thus-it will be seen that the essence of the inventionis the forming of the pyroxyline into the necessary shape for the reception and absorption of the solvent.
WVhat Iclaim is 1. The process of making pyroxyline compounds in the following steps: first, grinding pyroxyline in pulp or flock; second, forming the pulp or flock into a thin sheet or sheets; third, applying a suitable solvent to the sheet by sprinkling or equivalent means; fourth, completing the material in masticating-rolls or by the use of heat and pressure, substantially as described.
2. The process of manufacturing pyroxyline compounds, consisting of the following steps: first, forming films or sheets from pyroxyline flock or pulp; second, saturating the sheets with the requisite quantity of solvent; third, massing the sheets together in a closed receptacle; fourth, completing the material by means of masticating rolls or heat and pressure, sub stantially as described.
3. The process of manufacturing pyroxyline compounds by first forming thin sheets from pyroXyline flock or pulp and then saturating such sheets with the requisite quantity of liquid solvent, substantially as described.
4:. The process of manufacturing pyroXyline compounds, consisting of the following steps: first, forming a pulp or flock of pyroxyline by means of revolving knives in a-drum; second, forming a paper from the pulp by means of a paper-making machine; third, saturating the pyroxyline-paper with liquid solvents; fourth, massing the saturated paper together and permitting it to rest for a definite time until the solvents are absorbed; fifth, completing the conversion by means of masticating-rolls or heat and pressure, substantially as described.
JOHN WV. HYATT.
\Vitnesses:
vABRAHAM MANNERs, NEIL CAMPBELL.
Publications (1)
Publication Number | Publication Date |
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US331713A true US331713A (en) | 1885-12-01 |
Family
ID=2400813
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US331713D Expired - Lifetime US331713A (en) | John w |
Country Status (1)
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US (1) | US331713A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2701210A (en) * | 1950-02-01 | 1955-02-01 | Eastman Kodak Co | Continuous process for preparing a solution of constant composition |
-
0
- US US331713D patent/US331713A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2701210A (en) * | 1950-02-01 | 1955-02-01 | Eastman Kodak Co | Continuous process for preparing a solution of constant composition |
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