US260749A - Making and for textile and other purposes - Google Patents
Making and for textile and other purposes Download PDFInfo
- Publication number
- US260749A US260749A US260749DA US260749A US 260749 A US260749 A US 260749A US 260749D A US260749D A US 260749DA US 260749 A US260749 A US 260749A
- Authority
- US
- United States
- Prior art keywords
- magnesia
- pressure
- fibers
- solution
- per cent
- 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
- 239000004753 textile Substances 0.000 title description 12
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 80
- 239000000835 fiber Substances 0.000 description 50
- 239000000395 magnesium oxide Substances 0.000 description 40
- 239000000243 solution Substances 0.000 description 30
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 30
- 238000009835 boiling Methods 0.000 description 26
- 241000196324 Embryophyta Species 0.000 description 24
- 238000000034 method Methods 0.000 description 18
- 239000000126 substance Substances 0.000 description 14
- 241000208202 Linaceae Species 0.000 description 10
- 235000004431 Linum usitatissimum Nutrition 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 8
- 239000011780 sodium chloride Substances 0.000 description 8
- 235000013311 vegetables Nutrition 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000002023 wood Substances 0.000 description 8
- LSNNMFCWUKXFEE-UHFFFAOYSA-L Sulphite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000001264 neutralization Effects 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 240000000218 Cannabis sativa Species 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000007514 bases Chemical class 0.000 description 2
- 239000003637 basic solution Substances 0.000 description 2
- 235000009120 camo Nutrition 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 235000005607 chanvre indien Nutrition 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 231100000078 corrosive Toxicity 0.000 description 2
- 231100001010 corrosive Toxicity 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000011487 hemp Substances 0.000 description 2
- 235000012765 hemp Nutrition 0.000 description 2
- 230000000266 injurious Effects 0.000 description 2
- 230000004301 light adaptation Effects 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000006193 liquid solution Substances 0.000 description 2
- 235000012766 marijuana Nutrition 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
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
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
- D21C3/022—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes in presence of S-containing compounds
Definitions
- present invention is predicated upon the process described in said Letters Patent, and is subordinate thereto; anditconsistsin the adaptation of the same to the treatment of vegetable substances other than wood, so as to reduce them to a state useful in the manufacture of paper, or to obtain fiber or filaments suitable to be spun -into yarn for the manufacture of textile fabrics or felted goods.
- the process hereinafter described may be conducted bythe aid of a boiler capable of being tightly closed and surrounded by a jacket, within which, and around the outside of the boilerproper, steam can be admitted by means of pipes connectinga steamgenerator with the space formed by such surrounding jacket.
- the boiler or digester should be lined with lead or a suitable material capable of resisting the corrosive action of'chemical agents,
- the solution used may contain only about 0.45 per cent. magnesia or equivalent alkali and about 0.85 per cent. of sulphurous acid,.although a stronger solution will generally be preferable.
- the boiler having been closed tight, steam is let into the jacket until the pressure within the digester or boiler proper has reached, say, fifty pounds to the square inch, when it should be continued at this pressure for about three hours.
- the strength of the solution of sulphurous acid and magnesia or equivalent alkaline agent, the degree of pressure in the boiler, and the duration of the boiling operation are to be varied according to the necessities of the particular case, for the reason that plants which are compact in structure or resinous in character require more vigorous treatment than those which are soft or free from resinous matter.
- the solution of sulphurous acid and magnesia, or alkaline substitute having like properties as magnesia should be of greater strength, and the boiling operation be conducted for a greater length of time and under a greater pressure than will be proper in case filaments are to be obtained composed of a number of fibers. If only long filaments are desired, it will be well to use a more basic solution by adding magnesia in a finely-divided state, or a' more basic compound of sulphurous acid and magnesia.
- the general process is in all cases the same and the plants are to be boiled under pressure in a close boiler while submerged in a solution of the character described, the action of which is to dissolve the incrusting matter which binds together the component fibers, and also to render soft and pliable the body of the fibers themselves
- the treatment should have regard to the structure of the plant, to the nature of the gummy inerustation, and to the product that is desired to be obtained, and the strength of the solution, the duration of the boiling operation, and the degree of pressure to which by heat the solution is raised should be adapted to the requirements of the case.
- either fine, white, soft, silky, but short fibers can be obtained, or coarser, darker, stiffer, but longer fibers or filaments, with the different gradations lying between the extremes, all depending on the treatment being varied and adapted in the manner referred to.
- the solution used contains 1.4. per cent. of magnesia and 4.2 per cent. of sulphurous acid, and the boiling is carried on with about fifteen pounds pressure for about two hours and a halt, coarser filaments of a darker color are obtained; but if the boiling is carried on with thirty pounds pressure for about three hours the filaments obtained are finer, more flexible,
- the boiling is or may be carried on with seventy pounds pressure for about three hours with a solution containing 1.6 per cent. of magnesia and 3.8 per cent. of sulphurous acid, and (mixed with the flax) about one per cent. of weight of the water of caustic magnesia. finely divided.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Description
UNITED STATES PATENT OFFICE.
CARL DANIEL EKMAN, OF LONDON, ENGLAND.
METHOD OF TREATING FIBROUS VEGETABLE SUBSTANCES TO OBTAlN FIBER SUITABLE FOR PAPER- MAKING AND FOR TEXTILE AND OTHER PURPOSES.
SPECIFICATION formingpart of Letters Patent No. 260,749, dated July 11, 1882.
Application filed June 5, 1882. (No specimens.) Patented in England July 13, 1881, No. 8,062; in France November 10, 1881, No. 145,744, and in Belgium November 12, 1881, No 56,244.
to obtain fiber suitable for paper-ma-kin g. My
present invention is predicated upon the process described in said Letters Patent, and is subordinate thereto; anditconsistsin the adaptation of the same to the treatment of vegetable substances other than wood, so as to reduce them to a state useful in the manufacture of paper, or to obtain fiber or filaments suitable to be spun -into yarn for the manufacture of textile fabrics or felted goods.
Inasmuch as the treatment required to be given to different plants varies considerably according to their respective peculiarities and the amount of resistance which is encountered in dissolving the incrusting matter which binds the fibers together, and varies also with the uses to which the fiber when obtained is to be applied, it will be convenient to describe the process which I employ, first, in its application to the production of material suitable for paper-makin g, and, secondly, to the obtaining for the manufacture of textiles the ultimate fibers from plants, or the compound fibers making filaments from the same plants, composed of a number of the ultimate fibers cemented together by the incrusting matter which the plants contain. 7
Asdescribed in the said Letters Patent dated February 7, 1882, the process hereinafter described may be conducted bythe aid of a boiler capable of being tightly closed and surrounded by a jacket, within which, and around the outside of the boilerproper, steam can be admitted by means of pipes connectinga steamgenerator with the space formed by such surrounding jacket.
The boiler or digester should be lined with lead or a suitable material capable of resisting the corrosive action of'chemical agents,
and it should also be provided with an escapevalve, to enable from time to time injurious gases or resultants formed from the chemicals to be discharged.
It will generally be found convenient to use a vertical cylindrical boiler of, say, four feet inside diameter and twelve feet between the two ends, and to facilitate the filling and emptying of the same it should be mounted on trunnions, so as to be readily turned on its bearlngs.
For paper-making, if the incrusting matter in the vegetable plants selected to be reduced to pulp is to be completely dissolved, the treatment is similar to that which is described in my said patent for the treatment of wood; but it is not necessary in general to crush or mechanically disintegrate the plan ts, though it would be advisable to cutthem into short pieces. The pressure, too, at which the boiling is to be conducted and the length of time for which it is to be continued differ from that required when wood is to be dealt with. Neither are so strong chemicals essential, and in proportion as the pressure required is below that necessary for reducing wood to pulp the total durationdof the whole boiling process will be shortene I will now, by way of illustration, describe the process for treating straw and esparto in order to obtain fiber for paper-making.
After the raw material has been suitably cleansed it is put into the boileror digester, and
completely covered with or submerged in a liquid solution containing sulphurous acid and magnesia or other alkaline substitute for the magnesia-as soda-possessing substantially the equivalent chemical properties both with respect to its reaction upon the sulphurous acid and its effect upon the fiber of the plant. The solution used may contain only about 0.45 per cent. magnesia or equivalent alkali and about 0.85 per cent. of sulphurous acid,.although a stronger solution will generally be preferable. The boiler having been closed tight, steam is let into the jacket until the pressure within the digester or boiler proper has reached, say, fifty pounds to the square inch, when it should be continued at this pressure for about three hours. In case any sulphurous acid has been set free from the magnesia it will become converted under the continued influence of heat and pressure into sulphuric acid, and therefore it should be blown off through the escapevalve of the boiler; otherwise it will blacken or discolor the material under treatment. Below a pressure of fifty pounds, however, there is little liability of the existence of free sulphurous acid. After the boiling has been completed the steam is blown off and the contents of the boiler are turned out. The fiber resulting from the process is then to be washed and treated in the usual or in any other suitable way.
The strength of the solution of sulphurous acid and magnesia or equivalent alkaline agent, the degree of pressure in the boiler, and the duration of the boiling operation are to be varied according to the necessities of the particular case, for the reason that plants which are compact in structure or resinous in character require more vigorous treatment than those which are soft or free from resinous matter.
I have discovered that there is a special value in the employment of a solution composed of sulphurous acid and magnesia in obtaining from plants fibers or filaments to be used in the manufacture of textiles, from the fact that the action of the magnesia is specifically to render the fiber soft and pliable, and quite the opposite of the effect of the lime hitherto used, which leaves the fiber harsh and difficult to be spun or worked by machinery. In applying my process for this purpose the raw material employed must be such as yields fibers ofsufficient length-as, for example, flax or hemp-and the process can be so adapted to the end sought that there can be obtained either the ultimate fibers or filaments composed of many ultimate fibers cemented together. If fibers are to be obtained which are wholly freed from incrustin g matter, the solution of sulphurous acid and magnesia, or alkaline substitute having like properties as magnesia, should be of greater strength, and the boiling operation be conducted for a greater length of time and under a greater pressure than will be proper in case filaments are to be obtained composed of a number of fibers. If only long filaments are desired, it will be well to use a more basic solution by adding magnesia in a finely-divided state, or a' more basic compound of sulphurous acid and magnesia. Otherwise stated, although the general process is in all cases the same and the plants are to be boiled under pressure in a close boiler while submerged in a solution of the character described, the action of which is to dissolve the incrusting matter which binds together the component fibers, and also to render soft and pliable the body of the fibers themselves, the treatment should have regard to the structure of the plant, to the nature of the gummy inerustation, and to the product that is desired to be obtained, and the strength of the solution, the duration of the boiling operation, and the degree of pressure to which by heat the solution is raised should be adapted to the requirements of the case. In treating flax, for example, either fine, white, soft, silky, but short fibers can be obtained, or coarser, darker, stiffer, but longer fibers or filaments, with the different gradations lying between the extremes, all depending on the treatment being varied and adapted in the manner referred to. If the solution used contains 1.4. per cent. of magnesia and 4.2 per cent. of sulphurous acid, and the boiling is carried on with about fifteen pounds pressure for about two hours and a halt, coarser filaments of a darker color are obtained; but if the boiling is carried on with thirty pounds pressure for about three hours the filaments obtained are finer, more flexible,
of improved appearance, and rather lighter I in color. A good result can even be obtained by using a solution containing only 0.25 per cent. of magnesia and 0.8 per cent. of sulphurous acid and boiling about three hours with forty pounds pressure. Even sulphite of magnesia (the single salt) may be used; but since that salt is little soluble in water asalt is preferred containing so much sulphurous acid that it dissolves easily in the requisite or a less quantity of water. When this neutral salt is used it is strewn on the flax as it is placed in the boiler, so that it may be pretty evenly spread, and then the boiler is afterward filled up with water to the sameheight as when a solution is used. Two per cent. of single sulphite of magnesia and boiling for three hours with fifty pounds pressure will yield fiber of a fair quality.
For obtaining filaments that are soft, silky, lustrous, and of pale color, the boiling is or may be carried on with seventy pounds pressure for about three hours with a solution containing 1.6 per cent. of magnesia and 3.8 per cent. of sulphurous acid, and (mixed with the flax) about one per cent. of weight of the water of caustic magnesia. finely divided.
When only a small proportion of the inerusting matter is required to be dissolved very small quantities of the chemicals may be used. Even 0.3 per cent. of the waters weight of neutral sulphite of magnesia has a perceptible effect but as a rule it is preferred to have no less than one per cent. of this salt. A solution of 0.035 per cent. of magnesia and 0.1 per cent. of sulphurous acid can be used; but a stronger solution is preferred. Even as small a pressure as three pounds will have some eifect; but it is advisable to work with no less pressure than ten pounds.
The foregoingexample for the treatment of flax will serve as a guide for the treatment of other plants containing fibers suitable for textile purposes, especially hemp.
I do not claim in this patent the invention ICO - set forth and claimed in the said Letters Patsubstances under pressure in a solution conent heretofore granted to me, dated February taining sulphurous acid and magnesia or other 10 7,1S82,No. 253,357; but alkaline equivalent having the properties of What I do claim herein is I magnesia, as set forth. 5 The method, substantially as hereinbefore CARL DANIEL EKMAN. 1 described, of treating fibrous vegetable plants Witnesses:
for Wholly or partially resolving their fibrous W. H. THURSTON, constituents, Which consists in boiling such I. KNIGHT.
Publications (1)
Publication Number | Publication Date |
---|---|
US260749A true US260749A (en) | 1882-07-11 |
Family
ID=2330027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US260749D Expired - Lifetime US260749A (en) | Making and for textile and other purposes |
Country Status (1)
Country | Link |
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US (1) | US260749A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2643957A (en) * | 1951-08-07 | 1953-06-30 | Ralph M Lindgren | Process of preserving wood |
US2924547A (en) * | 1954-11-08 | 1960-02-09 | Hawaiian Dev Company Ltd | Rapid neutral sulfite process for pulping bagasse and other non-woody plant lignocellulose |
US3046182A (en) * | 1956-01-13 | 1962-07-24 | Smith Paper Mills Ltd Howard | Sulphite pulping process |
-
0
- US US260749D patent/US260749A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2643957A (en) * | 1951-08-07 | 1953-06-30 | Ralph M Lindgren | Process of preserving wood |
US2924547A (en) * | 1954-11-08 | 1960-02-09 | Hawaiian Dev Company Ltd | Rapid neutral sulfite process for pulping bagasse and other non-woody plant lignocellulose |
US3046182A (en) * | 1956-01-13 | 1962-07-24 | Smith Paper Mills Ltd Howard | Sulphite pulping process |
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