US17387A - charles mellibe - Google Patents
charles mellibe Download PDFInfo
- Publication number
- US17387A US17387A US17387DA US17387A US 17387 A US17387 A US 17387A US 17387D A US17387D A US 17387DA US 17387 A US17387 A US 17387A
- Authority
- US
- United States
- Prior art keywords
- boiler
- straw
- steam
- charles
- solution
- 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
- 239000010902 straw Substances 0.000 description 34
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 18
- 238000000034 method Methods 0.000 description 14
- 239000003513 alkali Substances 0.000 description 12
- 238000009835 boiling Methods 0.000 description 12
- 239000003518 caustics Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000000835 fiber Substances 0.000 description 10
- 239000002657 fibrous material Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 6
- 235000015450 Tilia cordata Nutrition 0.000 description 6
- 235000011941 Tilia x europaea Nutrition 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 6
- 239000004571 lime Substances 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 235000011121 sodium hydroxide Nutrition 0.000 description 6
- 235000013311 vegetables Nutrition 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000011118 potassium hydroxide Nutrition 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
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
- 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
- the process for the treating of straw, and other vegetable fibrous materials requiring like treatment, preparatory to the use of such fibers in the manufacture of paper; and the improvement consists in subjecting straw or such other librous materials to a pressure of at least seventy pounds on the square inch when boiling such fibrous matters in a solution of caustic alkali.
- the straw or fibrous matters are cut into short lengths, soaked in warm water and washed. They are then placed in a suitable boiler, and I use for such purpose a rotatory boiler provided with a coil or coils of steam pipe for the purpose of heating the contents; and I prefer that the boiling should be carried on at a temperature to produce at or above 80 lbs.
- the quantity of alkali used is at the rate of about 16 per cent. of caustic soda or potash of the straw or fibrous substances under process.
- the fibers may then be bleached by the use of a comparatively small quantity of bleaching powder, or chlorid of lime.
- the straw or other fibrous material requiring alike process to prepare the same for the paper manufacture is first, as here tofore, to be cut in a chaff-cutting or other machine into short lengths, and to be freed from knots, dirt and dust, and then steeped for a few hours in hot water.
- the straw or fibrous materials and a weak solution of caustic alkali are then to be placed in a suitable closed boiler heated by steam as hereafter explained, and the heatis to be raised to such a degree as to attain and maintain for a time a pressure internally of the boiler equal to or exceeding seventy pounds on the square inch, that is about 310 of Fahrenheit; by which means a considerable saving of alkali, as well as time and fuel, results, as compared with the means of using a hot solution of caustic alkali, as now practiced in preparing straw and other bers for paper-makers.
- the boiler employed for the purpose and the manner of heating it by steam may be varied; but 1st it must have a rotatary motion either on its long or on its small axis by means which are very well known; and
- the plan of construction of the boiler I would recommend would be, if the boiler is to rotate vertically on its small axis, as very well known, to cover it with a jacket so that the steam could circulate from one end to the other between the two plates; or rather if it is to revolve horizontally or upon its long axis, as is equally very well known, to x near each end of the boiler, and inside of it, a diaphragm or partition, which partitions are connected together by numerous tubes, which are arranged in a circle near the outer circumference of each partition.
- the steam is introduced through the hollow axis at one end of the boiler, and it passes through the steam pipes, and thence into the compartment at the other end of the boiler, where it and the condensed steam are conveyed away as is well understood through the other hollow axis.
- the solution which I prefer to use is to be from two to Vthree degrees of Baum or of a specific gravity of from 1.013 to 1.020, and at the rate of above 7 0 gallons of such solution to each cwt. of straw or other fibrous vegetable matters requiring like treatment.
- the boiler is to be filled with straw and alkaline solution and then closed Huid and steam tight.
- the boiler is made to revolve slowly, say, about one or two revolutions per minute, and the steam is to be admitted. I find it desirable to keep up the heat and pressure during about three hours after the pressure above mentioned has been obtained,
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Description
Ny PETERS, PHTDLITHOGRAPHER. WASHINGTON, D C.
UNITED STATES PATENT OFFICE.
M. A. CHARLES MELLIER, OF PARIS, FRANCE.
MAKING PAPER-PULP.
Specicaton of Letters Patent No. 17,387, dated May 26, 1857.
process for the treating of straw, and other vegetable fibrous materials requiring like treatment, preparatory to the use of such fibers in the manufacture of paper; and the improvement consists in subjecting straw or such other librous materials to a pressure of at least seventy pounds on the square inch when boiling such fibrous matters in a solution of caustic alkali. For this purpose the straw or fibrous matters are cut into short lengths, soaked in warm water and washed. They are then placed in a suitable boiler, and I use for such purpose a rotatory boiler provided with a coil or coils of steam pipe for the purpose of heating the contents; and I prefer that the boiling should be carried on at a temperature to produce at or above 80 lbs. on the square inch in the boiler where are the brous materials to be acted upon, but so high a temperature is not absolutely necessary but I have found by experi ment that it is essential that a temperature equivalent to seventy pounds on the square inch must be employed. The quantity of alkali used is at the rate of about 16 per cent. of caustic soda or potash of the straw or fibrous substances under process. The fibers may then be bleached by the use of a comparatively small quantity of bleaching powder, or chlorid of lime.
To enable others skilled in the art to make and use my invention, I will proceed to describe more fully the manner of using the same.
The straw or other fibrous material requiring alike process to prepare the same for the paper manufacture, is first, as here tofore, to be cut in a chaff-cutting or other machine into short lengths, and to be freed from knots, dirt and dust, and then steeped for a few hours in hot water. The straw or fibrous materials and a weak solution of caustic alkali are then to be placed in a suitable closed boiler heated by steam as hereafter explained, and the heatis to be raised to such a degree as to attain and maintain for a time a pressure internally of the boiler equal to or exceeding seventy pounds on the square inch, that is about 310 of Fahrenheit; by which means a considerable saving of alkali, as well as time and fuel, results, as compared with the means of using a hot solution of caustic alkali, as now practiced in preparing straw and other bers for paper-makers.
The boiler employed for the purpose and the manner of heating it by steam may be varied; but 1st it must have a rotatary motion either on its long or on its small axis by means which are very well known; and
Qdly I prefer not to send the steam directly.
into the liquid in which the materials are immersed, but to pass it either in a jacket around the boiler, or through a coil or a system of steam pipes inside of it, so that the steam does not mix with the caustic alkaline solution in the middle portion of the boiler, but is kept separate and does not therefore in condensing dilute the caustic alkaline solution used.
The plan of construction of the boiler I would recommend would be, if the boiler is to rotate vertically on its small axis, as very well known, to cover it with a jacket so that the steam could circulate from one end to the other between the two plates; or rather if it is to revolve horizontally or upon its long axis, as is equally very well known, to x near each end of the boiler, and inside of it, a diaphragm or partition, which partitions are connected together by numerous tubes, which are arranged in a circle near the outer circumference of each partition. By this arrangement the steam is introduced through the hollow axis at one end of the boiler, and it passes through the steam pipes, and thence into the compartment at the other end of the boiler, where it and the condensed steam are conveyed away as is well understood through the other hollow axis.
In adopting the plan of not sending directly the steam into the boiler I found the three following advantages: 1st not to dilute, as I have already said, the alkaline solution; Qdly to avoid the trouble of having sometimes the end of the steam-pipe in the boiler choked with straw, and to prevent, in case that by one cause or another the pressure in the steam boiler would fall under the degree of the pressure in the straw boiler, the priming of the rst by the second, viz, the absorption of straw and alkaline solution from the straw boiler into the steam boiler; Bdly the greater facility of cooling the straw-boiler, when thepressure has been maintained for a sufficient length of time, by means of turning off the l or other fibrous materials after boiling.
By means of submitting the straw or similar fibrous material to a pressure of between 70 to 84 pounds on the square inch inside of the boiler, I can reduce considerably the proportion of alkali and the solution which I prefer to use is to be from two to Vthree degrees of Baum or of a specific gravity of from 1.013 to 1.020, and at the rate of above 7 0 gallons of such solution to each cwt. of straw or other fibrous vegetable matters requiring like treatment.
The boiler is to be filled with straw and alkaline solution and then closed Huid and steam tight. The boiler is made to revolve slowly, say, about one or two revolutions per minute, and the steam is to be admitted. I find it desirable to keep up the heat and pressure during about three hours after the pressure above mentioned has been obtained,
Y when the process of boiling is complete. A
steam gage properly iiXed upon the boiler will enable one to ascertain when the pressure has attained the required degree.
When the apparatus and the fibers under process have been cooled by the means hereinbefore mentioned or rather when the pressure has been reduced to nothing, I open the man holes of the boiler, empty the materials in suitable vessels, and wash them, rst with hot water, then with cold water, until the liquor runs perfectly clear. I then steep the, fiber for about an hour in hot water acidulated with a quantity of sulfuric acid equal to about 2 per cent. of the weight of the iibers under process and nally the washing is completed with cold water. The straw or fiber may then be bleached in the ordinary manner and itv will be found to be accomplished by a comparatively small quantity of chlorid of lime. y
Having thus described the nature of my said invention and the manner of performing the same I would have it understood that I do not claim the general use of caustic alkaline solutions nor the employment generally of a close boiler for boiling straw or other vegetable fibrous substances; Vbut What I claim as my invention and desire to secure by Letters Patent is 1. The use of a solution of caustic soda (NaO) in a compartment of a rotary vessel separate from that which contains the steam heat substantially as described.
2. I also claim the within described process for bleaching straw, consisting in boiling it in a solution of pure caustic soda (NaO) from 2 to 3 Baum, at a temperature not less than 310o Fahrenheit, after it has been soaked and cleaned and before submitting it to the action of a solution of chlorid ofl lime from 1 to 1% degrees substantially as described.
M. A. CHARLES MELLIER.
Vitnesses ALLERME, AMAszm.
Publications (1)
Publication Number | Publication Date |
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US17387A true US17387A (en) | 1857-05-26 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US17387D Expired - Lifetime US17387A (en) | charles mellibe |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070187387A1 (en) * | 2005-12-12 | 2007-08-16 | Lg Electronics Inc. | Oven |
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0
- US US17387D patent/US17387A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070187387A1 (en) * | 2005-12-12 | 2007-08-16 | Lg Electronics Inc. | Oven |
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