US1089691A - Manufacture of sulfite pulp from resinous woods. - Google Patents
Manufacture of sulfite pulp from resinous woods. Download PDFInfo
- Publication number
- US1089691A US1089691A US78390013A US1913783900A US1089691A US 1089691 A US1089691 A US 1089691A US 78390013 A US78390013 A US 78390013A US 1913783900 A US1913783900 A US 1913783900A US 1089691 A US1089691 A US 1089691A
- Authority
- US
- United States
- Prior art keywords
- turpentine
- solvent
- chips
- manufacture
- sulfite pulp
- 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
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 title description 9
- 238000004519 manufacturing process Methods 0.000 title description 2
- 239000002904 solvent Substances 0.000 description 24
- 241000779819 Syncarpia glomulifera Species 0.000 description 18
- 239000001739 pinus spp. Substances 0.000 description 18
- 229940036248 turpentine Drugs 0.000 description 18
- 239000011347 resin Substances 0.000 description 12
- 229920005989 resin Polymers 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 239000002023 wood Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000004087 circulation Effects 0.000 description 3
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 2
- 235000011613 Pinus brutia Nutrition 0.000 description 2
- 241000018646 Pinus brutia Species 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000344 soap Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- D21C3/222—Use of compounds accelerating the pulping processes
Definitions
- turpentine is COIltillIlQd in the wood prima- Patented Mar. 10, 1914;. Serial No. 733,900.
- the turpentine emulsifying with the alkali solvent A specific procedure may be as follows: A battery, or' series, of autoclaves is employed, preferably eight in number and interconnected by appropriate pi ing and provided with heaters and valves. Klumbers one to six will contain chips submerged in alkaline solvent, numbers seven and eight chips submerged in turpentine solvent. By means of compressed air the solvent in number one is forced forward, a draw of alkaline solvent being taken from number six; simultaneously fresh turpentine solvent is forced into number seven and a draw of such solvent taken from number eight. Then number one is dumped of its charge of spent chips, and filled with fresh, or unextracted. chips.
- Number eight is now connected with number one, and by running fresh alkaline solvent into number two circu lation is forced through the battery and tur. pcntine solvent from number eight is forced over into number one, saturating the fresh chips there.
- the battery is now ready for compressed air in number two, a draw of alkaline solvent'from number seven; fresh turpentine solvent into number eight, and a draw of turpentine solvent from number one.
- the draw of alkaline solvent contains resins as soaps, and residual turpentine; the turpentine isrecovered by appropriate distillation, and by evaporation the resin soaps are obtained.
- the draw of turpentine solvent contains resins, and by distillation of the turpentine the resins are Whatever rily, is collected and appears in the turpentine reclaimed.
- the spent chips are practically free of resin and yellow stain, and after draining or drying may be cooked by the conventional sulfite process.
Landscapes
- Paper (AREA)
- Medicines Containing Plant Substances (AREA)
Description
circulation promoting the result.
UNITE STATES PATENT oEEIoE.
- OMA CARE, OF ASHEVILLE, NQRTH CAROLINA.
MANUFACTURE OF SULFITE PULP FROM RESINOUS WOODS.
No Drawing. I
To all whom it may concern Be it known that I, OMA CARR, a citizen of the United States of America, residing at Asheville, county of B'uncombe, State of North Carolina, have invented certain new and useful Improvementsin the Mannfacture of Sulfite Pulp from Resinous lVoods, of which the following specification is a clear description.
Practically all resin-bearing woods store the greater part of their resin in the summer ringof the wood, the rest being stored in the medullary rays. Vhere'ver the resins are stored the cellulose is stained yellow or yellow-brown. In many varieties of pine this stain is of such character that'it does not dissolve out under the action of the sulfite cook liquor, the stained fibers being only partially cooked and eventuall showing in the pulp as shieves or ye low shiners. These pines are not, therefore, available for pulp by the sulfite process in their naturaljstate; and as they are very abundant, of rapid growth, and of insignificant value for lumber or fuel use, it is economically desirable to render them suitable.
It is the object of my invention to attack the yellow ring, or stained fibers, before subjecting the wood to the sulfite cook, the desirable characteristics of which, as compared with the soda process, are well known. This I accomplish by the use of turpentine and alkali in combination. The resins causing the stain are complex in chemical composition, some being acid in nature and soluble in alkaline solvent, while others act as neutral resins and aresoluble in turpentine. r
An outline of one general method of procedure is as follows: The wood is chipped in the usual way and the chips placed in an autoclave (one of a series); they are then extracted by turpentine, a large part of the resins responding to this solvent, heat and Following the turpentine extraction I place on the chips a solution of alkali (common soda ash is convenient, but caustic soda is more effective), and by heat and circulation'remove the remaining resins. The extraction may be conducted with the autoclaves as a series, inter-connected, or intermittently, the alkali solvent may precede the turpentine, or, the
Specification of Letters Patent.
Application filed August 9, 1913.
obtained in the f free state. turpentine is COIltillIlQd in the wood prima- Patented Mar. 10, 1914;. Serial No. 733,900.
two solvents may be used together. the turpentine emulsifying with the alkali solvent. A specific procedure may be as follows: A battery, or' series, of autoclaves is employed, preferably eight in number and interconnected by appropriate pi ing and provided with heaters and valves. Klumbers one to six will contain chips submerged in alkaline solvent, numbers seven and eight chips submerged in turpentine solvent. By means of compressed air the solvent in number one is forced forward, a draw of alkaline solvent being taken from number six; simultaneously fresh turpentine solvent is forced into number seven and a draw of such solvent taken from number eight. Then number one is dumped of its charge of spent chips, and filled with fresh, or unextracted. chips. Number eight is now connected with number one, and by running fresh alkaline solvent into number two circu lation is forced through the battery and tur. pcntine solvent from number eight is forced over into number one, saturating the fresh chips there. The battery is now ready for compressed air in number two, a draw of alkaline solvent'from number seven; fresh turpentine solvent into number eight, and a draw of turpentine solvent from number one. Thus the extraction proceeds, the fresh chips being bathed in turpentine solvent and. the nearly spent chips bathed in alkaline solvent. The draw of alkaline solvent contains resins as soaps, and residual turpentine; the turpentine isrecovered by appropriate distillation, and by evaporation the resin soaps are obtained. The draw of turpentine solvent contains resins, and by distillation of the turpentine the resins are Whatever rily, is collected and appears in the turpentine reclaimed.
The spent chips are practically free of resin and yellow stain, and after draining or drying may be cooked by the conventional sulfite process.
Obviously the process may be reversed, the alkaline solvent preceding the turpentine solvent, while it is also apparent that the two solvents may be merged together; and it is further apparent that the extraction may be conducted in an intermittent manner instead of serially. The specific pro subjecting the wood chips to turpentineand 1O cedu re described above, however gives best also an alkaline solvent, and then cooking results. i Y the chips by the 'sulfite process. Having described my invention, what I In testimony whereof I hereunto a ffix my claim as new and desire to secure by Letsignature in the presence of two witnesses. ters Patent is: y OM-A CARR. I
lhe method herein described of making, Vitnesses:
' sulfite pulp from. resinous woods, consisting JOHN T. SMITH, J r.
in dissolying out the resinous matters by R. M. Ronnn'rs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US78390013A US1089691A (en) | 1913-08-09 | 1913-08-09 | Manufacture of sulfite pulp from resinous woods. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US78390013A US1089691A (en) | 1913-08-09 | 1913-08-09 | Manufacture of sulfite pulp from resinous woods. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1089691A true US1089691A (en) | 1914-03-10 |
Family
ID=3157910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US78390013A Expired - Lifetime US1089691A (en) | 1913-08-09 | 1913-08-09 | Manufacture of sulfite pulp from resinous woods. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1089691A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE749200C (en) * | 1940-04-18 | 1944-11-20 | Benjamin Boehme | Process for making pulp from wood rich in resin |
-
1913
- 1913-08-09 US US78390013A patent/US1089691A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE749200C (en) * | 1940-04-18 | 1944-11-20 | Benjamin Boehme | Process for making pulp from wood rich in resin |
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