US54510A - Improved apparatus for the manufacture of paper-pulp - Google Patents
Improved apparatus for the manufacture of paper-pulp Download PDFInfo
- Publication number
- US54510A US54510A US54510DA US54510A US 54510 A US54510 A US 54510A US 54510D A US54510D A US 54510DA US 54510 A US54510 A US 54510A
- Authority
- US
- United States
- Prior art keywords
- digester
- pulp
- pump
- valve
- paper
- 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
- 229920001131 Pulp (paper) Polymers 0.000 title description 2
- 238000004519 manufacturing process Methods 0.000 title description 2
- 239000000463 material Substances 0.000 description 10
- 239000007788 liquid Substances 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000013505 freshwater Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001868 water Inorganic materials 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 102000004726 Connectin Human genes 0.000 description 1
- 108010002947 Connectin Proteins 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C7/00—Digesters
Definitions
- B is alower perforated diaphragm, having a passage, O, for the escape of the pulp.
- a space, E n' for they accumulation of the liquid.
- the passage O is closed by a valve at D or at F, except when the pulp is to escape.
- a circulating tube passes from below the diaphragm B to the upper part of the digester. In the course of this tube a rotary or reciproeatin g pump, I-I, is placed.
- This pump is to be driven by machinery, andproduces a constant circulation of the digestingliquid from the lower chamber, E, below the diaphragm, through G, into the upper part of the digester, or, vice versa, from the upper part of the chamber down through tube G and the pump into the bottom of the digester, and thence upl land opening cock 3 the pump can be made to wardly, by virtue of the force of the pump, through the mass to be pulped.
- the valves Dand F may be both opened and the material permitted to escape directly on the valve.
- D may be first opened, and the material permitted to pass into the tubular space or passage between D and F, and then, when the valve D is closed and the valve F opened, the material between D and F will escape.
- Theoperation of the apparatus is as follows: The wood, straw, or other material, in a nely divided state, is to be introduced through the man-hole at the .top of the digester A. A solution of caustic soda, or lime, or water alone, or other digestingliquid, is to be introduced, and when the digester is closed up heat is to be applied below to the bottom of the digester, and the pump started, the cocks 2 being open ⁇ and cocks l Iand 3 closed.
- the pump may be operated so as to force the liquid from below B through G into the top of the digester, whence it would descend through the material being pulped, or the pumps may be used to force the heated liquor vice versathat is, up through the diaphragm B and through the mass being pulped to the top of the digester, whence it would descend outside through G again into the pump and the bottom of the di gester.
- Fresh material may be introduced while the operation is going on by opening the valve K and introducing the charge of wood, &c., between the valve K and valve L. ⁇ The valve K is then to be closed and the valve L opened, when the charge falls by its own gravity into the boiler.
- any other mode of heating thecirculating liquid might be adopted, such as an exterior boiler or coil or a coil within the main digester.
- the pulp-digester iu combination with a lower perforated diaphragm, a central pulppassage, a circulating tube and pump, to produce a circulation through the mass from bottom to top, or vice versa.
- valves for introducing fresh material without disturbing the operation.
Landscapes
- Paper (AREA)
Description
JOHN W. DIXON AND GEORGE HABDING, OF PHILADELPHIA, PA.
IMPROVED APPARATUS FORATHE MANUFACTURE OF PAPER-PULP.
Specification forming part of Letters Patent N0. al, dated May 8, 1866.
reference being had to the annexed drawing,
making a part of this specification, in whichrepresents a strong digester, capableof resistmg heavy pressure. B is alower perforated diaphragm, having a passage, O, for the escape of the pulp. Below B is a space, E n', for they accumulation of the liquid. The passage O is closed by a valve at D or at F, except when the pulp is to escape.
In this particular apparatus the digester is shown as heated by fire placed below the digester, although all of the improvements herein described, except one combination, could be used with any otherform of heating apparatus. A circulating tube passes from below the diaphragm B to the upper part of the digester. In the course of this tube a rotary or reciproeatin g pump, I-I, is placed. This pump is to be driven by machinery, andproduces a constant circulation of the digestingliquid from the lower chamber, E, below the diaphragm, through G, into the upper part of the digester, or, vice versa, from the upper part of the chamber down through tube G and the pump into the bottom of the digester, and thence upl land opening cock 3 the pump can be made to wardly, by virtue of the force of the pump, through the mass to be pulped. When it is desired to withdraw the pulp the valves Dand F may be both opened and the material permitted to escape directly on the valve. D may be first opened, and the material permitted to pass into the tubular space or passage between D and F, and then, when the valve D is closed and the valve F opened, the material between D and F will escape.
In order to facilitate the withdrawal of the valve D and prevent the pulp from escaping with too great a shock a small steam-pipe extends from the upper part of the digester into the space between D and F, and by opening the cock 1 the pressure on both sides of D is put in equilibrium. This cock is to be closed before F is opened. In this way a portion of the contents can be quietly withdrawn at any time while thepulpingoperationis still goin gon,
Theoperation of the apparatus is as follows: The wood, straw, or other material, in a nely divided state, is to be introduced through the man-hole at the .top of the digester A. A solution of caustic soda, or lime, or water alone, or other digestingliquid, is to be introduced, and when the digester is closed up heat is to be applied below to the bottom of the digester, and the pump started, the cocks 2 being open `and cocks l Iand 3 closed. The pump may be operated so as to force the liquid from below B through G into the top of the digester, whence it would descend through the material being pulped, or the pumps may be used to force the heated liquor vice versathat is, up through the diaphragm B and through the mass being pulped to the top of the digester, whence it would descend outside through G again into the pump and the bottom of the di gester. p
Fresh material may be introduced while the operation is going on by opening the valve K and introducing the charge of wood, &c., between the valve K and valve L. `The valve K is then to be closed and the valve L opened, when the charge falls by its own gravity into the boiler.
In order to relieve the valves of pressure from the inside we employ the tube p, when the cock 4 places the space between K and L in equilibrium with the digester by causing steam to pass between K and L.
By opening the cock l and closing cock 2 force fresh water or liquid into the bottom ofthe digester from a heating apparatus, T, or tank T, (such as described in a former patent of J. W. Dixon,) where it becomes heated, and then up through the material, and the refuse liquid could pass through cock 3 into the coil U U U U, and thus heats the incoming liquid entering through cock 1 in the manner fully described in other patents heretofore granted to us. The introduction of fresh water belowV into the digester, in combination with the introduction of fresh charges of material above, would cause the fresher water always to bein 4contact with the most nished pulp.
So far as relates to the subject-matter of the five first claims, herein after set forth, any other mode of heating thecirculating liquid might be adopted, such as an exterior boiler or coil or a coil within the main digester.
Having thus described our improvement, what we claim as our invention, and desire to secure by Letters Patent, isi 1. rlhe pulp-digester,in combination with a lower perforated diaphragm having a central pulp-passage, a circulating tube or tubes connectin g the upperandlower part ofthe digester.
2. The pulp-digester, iu combination with a lower perforated diaphragm, a central pulppassage, a circulating tube and pump, to produce a circulation through the mass from bottom to top, or vice versa.
3. The two valves D and F in the pulp-escape tube, for withdrawing a portion of the contents without interfering with the operation within the digester.
4. The charging-pipe S, with its double;
valves, for introducing fresh material without disturbing the operation.
5. The combination of pulp-digester, circulating tube, and pump, when the fire is applied directly beneath the digester.
6. The continual forcing in of fresh liquid below and upward through the mass to be pulped, in combination with the introduction of the fresh charges of the material into the digester above, whereby the cleaner liquid would always be in contact with the pulp most cooked.
JOHN W. DIXON. GEORGE HARDING.
Witnesses:
GEORGE BUGKLEY, BENJN. MOMAKIN, Jr.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US54510A true US54510A (en) | 1866-05-08 |
Family
ID=2124053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US54510D Expired - Lifetime US54510A (en) | Improved apparatus for the manufacture of paper-pulp |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US54510A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4133714A (en) * | 1975-10-03 | 1979-01-09 | Vorobiev Jury P | Reaction vessel with pulsating means for producing lignocellulose product from crushed vegetable raw materials |
-
0
- US US54510D patent/US54510A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4133714A (en) * | 1975-10-03 | 1979-01-09 | Vorobiev Jury P | Reaction vessel with pulsating means for producing lignocellulose product from crushed vegetable raw materials |
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