US1165689A - Method of treating vegetable substances for the recovery oftheir values. - Google Patents
Method of treating vegetable substances for the recovery oftheir values. Download PDFInfo
- Publication number
- US1165689A US1165689A US617715A US1165689A US 1165689 A US1165689 A US 1165689A US 617715 A US617715 A US 617715A US 1165689 A US1165689 A US 1165689A
- Authority
- US
- United States
- Prior art keywords
- recovery
- values
- oftheir
- steam
- carbohydrates
- 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
- 238000011084 recovery Methods 0.000 title description 13
- 238000000034 method Methods 0.000 title description 10
- 235000013311 vegetables Nutrition 0.000 title description 9
- 239000000126 substance Substances 0.000 title description 6
- 229920002472 Starch Polymers 0.000 description 11
- 235000014633 carbohydrates Nutrition 0.000 description 11
- 150000001720 carbohydrates Chemical class 0.000 description 11
- 235000019698 starch Nutrition 0.000 description 11
- 239000008107 starch Substances 0.000 description 11
- 238000011282 treatment Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000000835 fiber Substances 0.000 description 8
- 239000006227 byproduct Substances 0.000 description 7
- 239000002657 fibrous material Substances 0.000 description 7
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 7
- 229940081974 saccharin Drugs 0.000 description 7
- 235000019204 saccharin Nutrition 0.000 description 7
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000003513 alkali Substances 0.000 description 4
- 229920000742 Cotton Polymers 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 235000000346 sugar Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 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 2
- 230000000694 effects Effects 0.000 description 2
- 238000011221 initial treatment Methods 0.000 description 2
- 229920001220 nitrocellulos Polymers 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000009991 scouring Methods 0.000 description 2
- 244000291564 Allium cepa Species 0.000 description 1
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 1
- 229920002160 Celluloid Polymers 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 240000006240 Linum usitatissimum Species 0.000 description 1
- 235000004431 Linum usitatissimum Nutrition 0.000 description 1
- 239000000020 Nitrocellulose Substances 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 238000009993 causticizing Methods 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 230000000266 injurious effect Effects 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 229940079938 nitrocellulose Drugs 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 150000008163 sugars Chemical class 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
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/0007—Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T292/00—Closure fasteners
- Y10T292/85—Knob-attaching devices
Definitions
- My present invention relates to the treatment of vegetable matter, and more particularly annual plants, such as cotton stalks, sugar cane, straw, and analogous growths, containing saccharin, starch, and invertible carbohydrates, as distinguished from those containing resinous or oily matter, for the removal of the extractive in such form as to permit of the easy rendering or recovery of the chemical values or by-products thereof, and for the ultimate recovery of the fibrous portion, consisting of welldefined' cylindrical bast fibers and short cellulose or woody fibers, which is available for the manufacture of a high grade of paper, or which, and this applies especially to the purified cotton cellulose, may be nitrated and after colloiding employed in the manufacture of smokeless powder either as a pulp dried in layers and afterward comminuted or disintegrated or as an unsized paper or in any other suitable form.
- extractive is in the form of a saccharin.
Landscapes
- Paper (AREA)
Description
n earns rarnnr onion,
MARK W. MARSDEN, PHILADELPHIA, PENNSYLVANIA.
METHOD 0F TREATING VEGETABLE SUBSTANCES FOR THE RECOVERY OF THEIR VALUES.
intense,
1% Drawing.
To all whom it may concern:
Be it known that 1, MARK W. Mansnnn,'
for the Recovery of Their Values, of which i the following is a specification.
My present invention relates to the treatment of vegetable matter, and more particularly annual plants, such as cotton stalks, sugar cane, straw, and analogous growths, containing saccharin, starch, and invertible carbohydrates, as distinguished from those containing resinous or oily matter, for the removal of the extractive in such form as to permit of the easy rendering or recovery of the chemical values or by-products thereof, and for the ultimate recovery of the fibrous portion, consisting of welldefined' cylindrical bast fibers and short cellulose or woody fibers, which is available for the manufacture of a high grade of paper, or which, and this applies especially to the purified cotton cellulose, may be nitrated and after colloiding employed in the manufacture of smokeless powder either as a pulp dried in layers and afterward comminuted or disintegrated or as an unsized paper or in any other suitable form.
The commercial value of the cellular and fibrous portions as well as thelvarious by products of the stock mentioned is well lmown, but the methods of treatment heretofore in vogue are expensive and injurious because large quantities of chemicals were used to decompose the rather considerable amount of pectin and cementing matter present in the cellulose. Indeed, attempts were made to reduce the cost and to some extent have the treatment pay for itself by recovering and using the chemicals over and over again. The use of alkali, its recovery by causticizing, etc., are too well known to require comment. The losses of the alkali Specification of Letters Patent.
Patented Dec, 28, 19115,
Application filed February 4, 1915. Serial No. 8,177.
.it impossible to recover the alkali except at the cost of all the sugar, and under perfe'ct conditions about ten per cent. of the stalks is convertible into sugar.
It is the object of the present invention to obviate and overcome the above mentioned disadvantages and-to provide for the economical separation and recovery ofthe extractive, and for the economical recovery of the fibrous portion of vegetable stock of the nature indicated, each of which operations is efiected by my method of treatment without the aid of. alkali or equivalent chemical substance and in such a way as to insure a maximum yieldof bast and cellulosio fibers retaining all of their original strength and pliancy. With this and other objects in view my invention resides the matters hereinafter described and claimed.
The stock remainder, after harvesting, is
out, into uniform lengths of from one to two" inches and steeped or soaked in a bath of hot'or cold water until complete saturationoccurs whereby it undergoes a conditionin not unlike retting as applied to the flax p ant, the effect of which is to loosen the outer coating of the bark and soften thewoody fibrous tissue. "When this is accomplished, the stock is removed from the bath andfrun through a grinderor shredder, which breaks up thecut stalks into a uniform and fibrous mass. This is put in-a closed digester containing water and steamunder a pressure of from ten to forty pounds, more or less. The effect of this treatment with heat, moisture, and pressure, is to separate and dissolve the soluble bodies and to convert the starch and invertible carbohydrates into saccharin. it is evident that the initial treatment of softening and shredding the the sugars, residual gums, coloring matter,
and other valuable components, and this re-'- covery may beaccomplished by inversion, fermentation, distillation, or in any appropriate way. The comparatively pure fibrous portion, that is to say the stock relieved of its extractive and with the liquor drawn oil, is now subjected to the direct action of steam at a pressure in excess of that previously employed. This operation may be facilitated and shortened if the fibrous material is subjected to a shaking or tumbling action so as to present all parts thereof to the pressure scouring and separating action of the steam. The efiect of this treatment is to separate the fibers and to condition them for their after treatment in the ordinary beating engine for the manufacture of pulp. When so reduced and if desired the pulp may be bleached or colored in any ap ropriate manner.-
s regards the purecellulose obtained from cotton stalks by the above method of treatment, the presence of a large percentage of short woody fibers in admixture with the long bast fibers will be of benefit to it for paper making since-one class of fibers will complement the other,uthe long fibers interlacing'and strengthening the sheet and the shorter ones filling in and giving it -body. Both are equally capable of conversion into pyroxylin and gun cotton and "available for celluloid or smokeless powder manufacture. Test treatments demonstrated that nitration took place readily and that an excellent product with a high-percentage of nitrogen was obtainable. This applies to the pulp as well as to paper both of which are contemplated by this invention.
Having described the nature and objects of the invention, I claim 1. The herein described method of treating vegetable matter containing starch and invertible carbohydrates for the recovery of its values, which consists in subjecting it in a uniformly divided state to an initial treatment analogous to retting, digesting it in carbohydrates into saccharin, drawing oil? and recovering the liquor in the form of useful by-products, and subjecting the fibrous material to the direct action of steam at a treatment analogous to retting, then shredding it, then digesting it in the presence of 4 7 water and steam pressure in order to convert the starch andinvertible carbohydrates into saccharin, drawing off and recovering the liquor in the form of useful by-products, and subjecting the fibrous material to the direct action of steam at a pressure in excess of that previously employed.
' 3. The herein described method of treat-. ing vegetable matter containing starch and invertible carbohydrates for the recovery of its values, which consists in immersing it in lengths of from one to two. inches in water.
until complete saturation takes place, then shredding it, then digesting it in the presence of water and steam pressure of from ten to forty pounds, more or less, until. the
extractive is in the form of a saccharin.
liquor, drawing off and recovering. the liquor in the form of useful lay-products, subjecting the fibrous material to the direct action of steam at a pressure in excess of that previously employed, and thereafter proceeding in any suitable manner for the manufacture of pulp or paper.
4. The
herein described method of treating vegetable matter containing starch and invertible carbohydrates for the recovery of its values, which consists in subjecting it in comparatively short lengths to saturation with water, then shredding it, then digesting it in the presence of water and steam pressure in order to convert the starch and invertible carbohydrates into saccharin,
the fibrous material to agitation in the presence of steam at a pressure in excess of that previously employed.
5. The herein described method of treating vegetable matter containing starch and invertible carbohydrates for the. recovery of its values, which consists in subjecting it in comparatively short lengths to saturation withwater, then shredding it, then digesting it in the presence of water and steam pressure in order to convert the starch and drawing off and recovering the liquor in the a formof useful by-products, and subjecting invertible carbohydrates into saccharin,
drawing ofi' and recovering the liquor in the form ofuseful, by-products, steam scouring the presence of water and steam pressure in order to convert the starch and invertible the fibrous material and agitating the latter so as to present all parts thereof to the ac- -tion of the steam, and thereafter proceeding in any suitablemanner for the manufacture .of paper.
herein described method of treatmatter containing starch and 6. The ing vegetable invertible carbohydrates for the recovery of itsvalues, which consists in subjecting it in [comparatively short lengths to saturation meeeee {e3 in the form of useful by-products, and tumbling or shaking the fibrous material in the presence of steam at a pressure in excess of that previously employed.
In testimony whereof. I afix my simeture in presence of two Witnesses MARK W. MARSDEN.
Witnesses:
E. W. STRAIN, ALLAN I. HUCKINS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US617715 US1165689A (en) | 1915-02-04 | 1915-02-04 | Method of treating vegetable substances for the recovery oftheir values. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US617715 US1165689A (en) | 1915-02-04 | 1915-02-04 | Method of treating vegetable substances for the recovery oftheir values. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1165689A true US1165689A (en) | 1915-12-28 |
Family
ID=3233714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US617715 Expired - Lifetime US1165689A (en) | 1915-02-04 | 1915-02-04 | Method of treating vegetable substances for the recovery oftheir values. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1165689A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2776228A (en) * | 1952-07-23 | 1957-01-01 | Corn Prod Refining Co | Process for destarching wet milling fractions |
| US2794738A (en) * | 1951-05-10 | 1957-06-04 | Fibre Corp Of America Inc | Fibrous board and sheet for insulation and other purposes of matted long cotton stalk fiber |
-
1915
- 1915-02-04 US US617715 patent/US1165689A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2794738A (en) * | 1951-05-10 | 1957-06-04 | Fibre Corp Of America Inc | Fibrous board and sheet for insulation and other purposes of matted long cotton stalk fiber |
| US2776228A (en) * | 1952-07-23 | 1957-01-01 | Corn Prod Refining Co | Process for destarching wet milling fractions |
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