US50835A - Improvement in treating straw for paper-pulp - Google Patents
Improvement in treating straw for paper-pulp Download PDFInfo
- Publication number
- US50835A US50835A US50835DA US50835A US 50835 A US50835 A US 50835A US 50835D A US50835D A US 50835DA US 50835 A US50835 A US 50835A
- Authority
- US
- United States
- Prior art keywords
- straw
- liquor
- boiler
- pulp
- 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
- 239000010902 straw Substances 0.000 title description 28
- 229920001131 Pulp (paper) Polymers 0.000 title description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 10
- 238000009835 boiling Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 235000017550 sodium carbonate Nutrition 0.000 description 5
- 229910000029 sodium carbonate Inorganic materials 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 238000013019 agitation Methods 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 238000003339 best practice Methods 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 239000002699 waste material 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
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
Definitions
- the character and quality of the pulp made from straw depends entirely upon the mode of treatment by which it is produced. 1f the alkaline liquor used in the reduction of the straw be of too high a degree of strength, there will benotonlyawaste ofthea1kali,but thefiber will be in a measure reduced to a pasty condition and will waste largely during the after process of washing the stock; besides, the quality of the stock will be injured by being made short, and thereby injuring the strength of the paper to be manufactured therefrom.
- a liquor marking from 3 to 5 of strength Bapm hasformerlybeen used. The result was that the fiber was much shortened and injured thereby. Much of the stock was thereby converted to a paste and washed away in the after treatment. I have found it better to use a much weaker solution of caustic alkali, marking in strength from 1 to 2 Bauni, and never exceeding 2 strength. I have also found that it is much better to increase the quantity of liquor, even when byso doing the strength of the boiling liquor is'reduced.
- My method of preparing my boilingliquor is as follows: It is composed of water, soda ash, and lime, and also grease or other like alkaline and oleaginous substance.
- I use three iron pans, hold ing one thousand gallons each, with agitators to mix the soda-ash and lime with the water.
- I also use a reservoir holding about two thousand gallons.
- I then take five hundred and fifty pounds of soda-ash, dissolve it in a pan of water holding one thousand gallons, to which I add about three hundred and eighty-five pounds of unslaked lime, or sufficient lime to combine with and properly caustify the sodaash, which will be according to the strength of the lime.
- siphon I draw about one-third of this liquor into the reservoir.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Description
UNITED STATES PATENT OFFICE.
HARRISON B. MEEOH, OF FORT EDWARD, NEW YORK.
IMPROVEMENT lN TREATING STRAW FOR PAPER-PULP.
Specification forming part of Letters Patent No. 50,835, dated November 7, 1865.
To all whom "it may concern:
Be it known that I, HARRISON B. MEEoH, of Fort Edward, in the county of Washington and State of New York, have invented a new and improved process for treating straw for the purpose of preparing the same to be converted into pulp for the manufacture of white paper for writing, printing, and other purposes for which white paper is used; and I hereby declare that the following is an exact description of said process.
The character and quality of the pulp made from straw depends entirely upon the mode of treatment by which it is produced. 1f the alkaline liquor used in the reduction of the straw be of too high a degree of strength, there will benotonlyawaste ofthea1kali,but thefiber will be in a measure reduced to a pasty condition and will waste largely during the after process of washing the stock; besides, the quality of the stock will be injured by being made short, and thereby injuring the strength of the paper to be manufactured therefrom.
Another difficulty has attended the treatment of straw preparatory to the manufacture of pulp therefrom, and that is there has been too much agitation during the period of boiling or cooking the straw.
The usual course of treatment by those using rotary boilers has been to commence the rotation of them as soon as the heat began to be applied, and to continue their rotation until the boiling or cooking was finished and the mass treated was ready to be discharged. The effect of this continued agitation was to separate the portions of straw first acted upon from the stock or stem of the straw and expose such finer portion thus separated to the further action of the alkali, thereby reducing it to a semi-fluid or pasty condition. My experience has been that the less agitation there is vof the straw during the period of its treatment in alkali without permitting it to burn the better. There is another evil consequence attending the too early rotation of the boiler While introducing the liquor and raising the temperature. Ifthe boiler is rotated while the contents are unequally saturated with the alkaline liquor, the consequence will be that the contents of the boiler willbe agglomerated together in uneven and unequal mass, making it impossible afterward to treat the mass evenly. For that reason I have found that the better way was to allow the rotary to remain at rest while charging the same with the straw and the necessary amount of liquor. By this means the mass in the boiler was undisturbed until the liquor was fully in, and when the rotation afterward commenced the action within the rotary would be more even and uniform. I have thus found it to be the best practice not to commence rotating the boiler until I had fully charged it with the straw and liquor, and had let the steam into and put the fire under the same.
My only object in rotating the boiler during the treatment of the straw is to prevent burning the material within the rotary. For that reason as soon as a temperature indicated by an internal pressure of one hundred pounds to the square inch within the boiler is attained I stop the fire and cease rotating the boiler. The principle is this: There should be as little agitation of the straw as possible after the boiling has progressed far enough to begin to separate the fine particles of straw from the stock. This point is reached as soon as the one hundred pounds pressure is obtained. Then the boiler should rest. the fire he stopped, and it should be permitted to stand and cook for aboutthree hours longer, when it will be found that the stock is well prepared for washing. I also find it advisable to use a much weaker liquor for boiling than has been heretofore used. A liquor marking from 3 to 5 of strength Bapm hasformerlybeen used. The result was that the fiber was much shortened and injured thereby. Much of the stock was thereby converted to a paste and washed away in the after treatment. I have found it better to use a much weaker solution of caustic alkali, marking in strength from 1 to 2 Bauni, and never exceeding 2 strength. I have also found that it is much better to increase the quantity of liquor, even when byso doing the strength of the boiling liquor is'reduced. Thus I use about eighteen hundred gallons of the weaker liquor where others use about fourteen hundred gallons-that is, were I to take their liquor at fourteen hundred gallons to twentytwo hundred pounds of straw, I should find it a better practice to add from four hundred to six hundred gallons of clear soft water, thereby redueing the strength of their boiling-liquor in that proportion. The reason for this is, first, by increasing the quantity of the boilingliquor the straw being treated is more completely immersed continually in the boiling liquor; second, the strength of the liquor thus diluted does not injure the fibers of the stock being treated, and the result is 1 get a more uniform, longer, and better fiber.
My method of preparing my boilingliquor is as follows: It is composed of water, soda ash, and lime, and also grease or other like alkaline and oleaginous substance. In preparing such liquor I use three iron pans, hold ing one thousand gallons each, with agitators to mix the soda-ash and lime with the water. I also use a reservoir holding about two thousand gallons. I then take five hundred and fifty pounds of soda-ash, dissolve it in a pan of water holding one thousand gallons, to which I add about three hundred and eighty-five pounds of unslaked lime, or sufficient lime to combine with and properly caustify the sodaash, which will be according to the strength of the lime. By means of siphon I draw about one-third of this liquor into the reservoir. I then add water to that in the pan, agitate it, let it settle, and draw off, as before, into the reservoir. I proceed in this way four times, or until I have in my reservoir about eighteen hundred gallons of liquor testing at from 1 to 2 Baum. lVhat remains in the pan I use in the preparation of the liquor for the next boiling. ()f the liquor thus prepared I use about seventy gallons to the one hundred pounds of straw prepared and packed in the boiler, as follows: In addition to this liquor, I take about sixteen pounds of grease or other oily substance, and twelve pounds of soda-ash or potash, and boil them in sixty gallons of water by steam until a soapy solution is produced.
I prepare my straw thus I cut it intolengths of about two inches, pass it through a fanningmill to separate any grain there may be in it. I remove all weeds and sticks, then pass it through heavy iron rollers for the purpose of crushing the knots and straw and increasing the surface exposed to the action of the alkali. I then charge my rotary with it, packing itin as closely as two men can do by stamping it in, for I find the more compactI can make the straw within the boiler the more perfect is the action of the alkaline solution upon it. My boiler is six feet in diameter and twenty-two feet in length, and I thus put into it about twenty-eight hundred pounds of straw to a boiling. Having thus charged my boiler with straw, I then pour upon the straw Within the boiler the soapy solution prepared as about hot, together with a weak alkaline solution, prepared as above described, taking care that the boiler shall remain stationary while filling in the entire quantity of liquor, for reasons already stated. After my boiler is thus full, charged with straw and the proper amount of boiling-liquor and soapy solution, I commence rotating it and letting in steam from the adjoining boiler in the method well known to the art, and, also, I put a fire under the rotating boiler and raise the temperature thereby to such a degree as is indicated by an internal pressure of one hundred pounds to the square inch within the boiler. As soon as this degree of temperature is indicated I stop the rotation of the boiler and remove the fire from beneath the same and permit itthus to remain for from two to three hours, when the straw is properly cooked and prepared for washing and treating in the manner Well known to the art and trade of paper-making.
By this particular method of treatment I obtain a superior quality of stockfor the manufacture of paper-pulp.- The fiber is freed from foreign substances, is long, strong, and little or none of it is reduced to a paste or a state by which it is wasted in the after-washing process.
Having thus fully described my improvement, what I claim as my invention, and for which I desire to secure Letters Patent, is-- 1. My above-described method of treating straw or other material preparatory for making paper-pulp by so charging it into the boiler, letting into and onto it the liquor and solutions, applying the steam and fire heat, rotating the boiler, and letting the same remain at rest,in the manner substantially and for the purpose ZLbOW-L, described.
2. The use of a weak alkaline liquor, not to exceed 2 of strength, (Baum,) in the treatment of straw under pressure, in the manner substantially and for the purpose above described.
3. The combination of the use of such weak alkaline liquor with my method of treating straw, as set out in my first claim herein, in the manner substantially and for the purpose above described.
HARRISON B. MEEGEI. Witnesses:
ASAHEL WING,
A. O. HOSSMAN.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US50835A true US50835A (en) | 1865-11-07 |
Family
ID=2120386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US50835D Expired - Lifetime US50835A (en) | Improvement in treating straw for paper-pulp |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US50835A (en) |
-
0
- US US50835D patent/US50835A/en not_active Expired - Lifetime
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