USRE19470E - Paper pulp bleaching process - Google Patents
Paper pulp bleaching process Download PDFInfo
- Publication number
- USRE19470E USRE19470E US19470DE USRE19470E US RE19470 E USRE19470 E US RE19470E US 19470D E US19470D E US 19470DE US RE19470 E USRE19470 E US RE19470E
- Authority
- US
- United States
- Prior art keywords
- pulp
- paper
- hydrosulphite
- color
- paper 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
Links
- 229920001131 Pulp (paper) Polymers 0.000 title description 17
- 238000000034 method Methods 0.000 title description 9
- 238000004076 pulp bleaching Methods 0.000 title description 2
- GRWZHXKQBITJKP-UHFFFAOYSA-L dithionite(2-) Chemical compound [O-]S(=O)S([O-])=O GRWZHXKQBITJKP-UHFFFAOYSA-L 0.000 description 10
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- JVBXVOWTABLYPX-UHFFFAOYSA-L Sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 description 5
- LSNNMFCWUKXFEE-UHFFFAOYSA-L Sulphite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000007844 bleaching agent Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 235000010269 sulphur dioxide Nutrition 0.000 description 3
- 239000004291 sulphur dioxide Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000001143 conditioned Effects 0.000 description 2
- 230000003750 conditioning Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- PENRVBJTRIYHOA-UHFFFAOYSA-L Zinc dithionite Chemical compound [Zn+2].[O-]S(=O)S([O-])=O PENRVBJTRIYHOA-UHFFFAOYSA-L 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000003638 reducing agent Substances 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1084—Bleaching ; Apparatus therefor with reducing compounds
- D21C9/1089—Bleaching ; Apparatus therefor with reducing compounds with dithionites
Definitions
- hydrosulphite has been mentioned above because it is the cheapest and best known representative of these compounds. But other hydrosulphites, such as potassium or ammonium'hydrosulphite, calcium, or those of the alkaline earth group have been used by me with satisfactory results, and zinc hydrosulphite (2218204) which is particularly easy to manufacture has also been found suitable for this purpose.
- a further advantage of the use of a hydrosulphite for the bleaching of mechanical pulp is the ease of its application. It can be dissolved in water and run as an aqueous solution into a mixer or beater where the pulp is being mixed, or it can be added as a solid direct to the wet pulp and thoroughly incorporated therewith. Since the reaction is completed within very few minutes it is only necessary to add the hydrosulphite to the beater or mixer in which the pulp is agitated before going to the paper machines.
- News print paper resulting from a mixture of about 83% ground wood to about 17% bleached sulphite pulp may be closely approximated in grade by using unbleached sulphite pulp with the ground wood if a small quantity of a hydrosulphite is incorporated in the proportions indicated.
- the advantages are in substituting the cheaper unbleached sulphite pulp for the bleached pulp ordinarily required.
- I claim 1 The process of lightening the color of mechanical wood pulp which comprises agitating the same substantially at room temperature for about ten minutes with an aqueous solution of a hydrosulphite as substantially the only active agent therein and in amount ranging from .25% to 10% of theweight of the pulp and thereby obtaining a bleached mechanical wood pulp suit-- able for direct conversion into paper without subsequent washing.
- the process or making paper from mechanical wood pulp which comprises agitating the pulp at substantially room temperature for a short time with an aqueous solution or a hydrosulphite as substantially the only active bleaching agent therein and in amount ranging from 25% to 10% of the weight of the pulp, and without subsequent washing converting the pulp into paper before reversion of color can take place in the pulp.
- hydrosulphite present as substantially the only active bleaching agent in an amount ranging from 0.25% to 10% of the weight of pulp in said suspension and then conditioning the bleached pulp for formation into paper and directly converting said reduced pulp containing reduced col- I oring matter into paper before reversion of color can take place in said reduced pulp due to oxidation of said reduced coloring matter.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
Description
. some extent.
which is considerably off color.
Reissued Feb. 19, 1935 UNITED STATES PATENT OFFICE PAPER PULP BLEACHING PROCESS Wilhelm Hirschkind, Berkeley,alif., assignor'to Great Western Electra-Chemical 00., San Francisco, Calif.', a corporation of California No Drawing. Original No. 1,873,924, dated August 23, 1932, Serial No. 323,575, December 3, 1928 Application for reissue October 22, 1934, Serial No. 749,362 Claims.
highly bleached or white pulp but rather to cause a lightening of the original dark color of a mechanical pulp. Ground wood pulp can not be converted into a white pulp because all of the lignin and incrusting matters are still present. This precludes the use of oxidizing agents asfor instance chlorine so necessary for producing whitepulp. The dark color of such pulp can be lightened somewhat by treatment with reducing agents, and some of these have been so used for some time.
Sulphur dioxide gas or bisulphite liquor will brighten or lighten dark mechanical pulps to The action however is slow and the quantity of sulphite necessary is considerable. I have discovered that the compound, sodium hydrosulphite of the chemical composition Na2SzO4 has a lightening action on the color of ground wood pulp infinitely greater and far more rapid than sulphur dioxide or bisulphites. I found that sodium hydrosulphite when added to very darkly colored mechanical wood pulp in a quantity of one quarter of one percent by weight and thoroughly mixed therewith in the presence of water, produced a lightening of the color far beyond any effect obtainablewith sulphur dioxide or the bisulphites, and that the whole process was completed in very few minutes. Ground wood which has been in storage for some time gradually darkens and produces a.
paper, after treatment in the ordinary way, A hydrosulphite added to the pulp in quantities of as little as one quarter of one per cent of the weight of the dry ground wood pulp will bring back the color of fresh ground wood, and a very small additional quantity will lighten the color beyond the original color. p
I have already mentioned the rapidity of the action of the hydrosulphite in treatment of paper pulp and it is quite remarkable that this action is hardly influenced by'temperature ranges between 50" F. and 120 F. so that at the rather low temperatures of approximately 50F. the effect is just the same. 'The temperature of the pulp suspension during the treatment may vary widely without affecting the treatment and the process therefore canbe carried out at the normal temperatures maintaining'in the room in which the process is carried out without substantially adding or subtracting heat to or from the pulp suspension.
Sodium hydrosulphite has been mentioned above because it is the cheapest and best known representative of these compounds. But other hydrosulphites, such as potassium or ammonium'hydrosulphite, calcium, or those of the alkaline earth group have been used by me with satisfactory results, and zinc hydrosulphite (2218204) which is particularly easy to manufacture has also been found suitable for this purpose.
A further advantage of the use of a hydrosulphite for the bleaching of mechanical pulp is the ease of its application. It can be dissolved in water and run as an aqueous solution into a mixer or beater where the pulp is being mixed, or it can be added as a solid direct to the wet pulp and thoroughly incorporated therewith. Since the reaction is completed within very few minutes it is only necessary to add the hydrosulphite to the beater or mixer in which the pulp is agitated before going to the paper machines.
As an example of its application to news print paper 2,300 poundsof ground wood pulp were mixed with 400 pounds of sulphite pulp to a stock density of approximately five per cent. Five and three-quarter pounds of anhydrous sodium hydrosulfite were added to this mixture. Ten minutes later the pulp was conditioned by adding the necessary sizing and bluing ingredients to the bath and the material was run directly onto the paper machine.
News print paper resulting from a mixture of about 83% ground wood to about 17% bleached sulphite pulp may be closely approximated in grade by using unbleached sulphite pulp with the ground wood if a small quantity of a hydrosulphite is incorporated in the proportions indicated. The advantages are in substituting the cheaper unbleached sulphite pulp for the bleached pulp ordinarily required.
Since various quantities of the chemical from .25% to of the weight of the pulp produce corresponding degrees of action on the color of the pulp, the amount to be, used will be governed entirely by the effects desired and I do not confine myself to any particular quantity or percentage of the chemical to the pulp treated.
I claim 1. The process of lightening the color of mechanical wood pulp which comprises agitating the same substantially at room temperature for about ten minutes with an aqueous solution of a hydrosulphite as substantially the only active agent therein and in amount ranging from .25% to 10% of theweight of the pulp and thereby obtaining a bleached mechanical wood pulp suit-- able for direct conversion into paper without subsequent washing.
2. The process of lightening the color-oi mechanical wood pulp which comprises agitating the samesubstantially at room temperature for about ten minutes with an aqueous solution of sodiumhydrosulphite substantially as the only active agent therein and in amount ranging from 25% to 10% of the weight of the pulp and thereby obtaining a bleached mechanical wood pulp suitable for direct conversion into paper without subsequent washing.
3, The process or making paper from mechanical wood pulp, which comprises agitating the pulp at substantially room temperature for a short time with an aqueous solution or a hydrosulphite as substantially the only active bleaching agent therein and in amount ranging from 25% to 10% of the weight of the pulp, and without subsequent washing converting the pulp into paper before reversion of color can take place in the pulp.
hydrosulphite present as substantially the only active bleaching agent in an amount ranging from 0.25% to 10% of the weight of pulp in said suspension and then conditioning the bleached pulp for formation into paper and directly converting said reduced pulp containing reduced col- I oring matter into paper before reversion of color can take place in said reduced pulp due to oxidation of said reduced coloring matter.
5. The process of making a paper from a mechanical wood pulp which consists in forming a suspension of said pulp in water, agitating said suspended pulp for a short time at about room temperature with a hydrosulphite present as the only active bleaching agent in an amount ranging from 0.25% to 10% of said pulp to bleach said pulp, then conditioning the bleached pulp for formation into paper, and directly converting said conditioned and bleached pulp into paper.
Publications (1)
Publication Number | Publication Date |
---|---|
USRE19470E true USRE19470E (en) | 1935-02-19 |
Family
ID=2083613
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US19470D Expired USRE19470E (en) | Paper pulp bleaching process |
Country Status (1)
Country | Link |
---|---|
US (1) | USRE19470E (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2598580A (en) * | 1947-10-08 | 1952-05-27 | Buffalo Electro Chem Co | Bleaching or brightening a web of mixed fibers |
US2862784A (en) * | 1955-03-04 | 1958-12-02 | Virginia Smelting Company | Oxidative-reductive multi-stage bleaching of ground wood pulp |
-
0
- US US19470D patent/USRE19470E/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2598580A (en) * | 1947-10-08 | 1952-05-27 | Buffalo Electro Chem Co | Bleaching or brightening a web of mixed fibers |
US2862784A (en) * | 1955-03-04 | 1958-12-02 | Virginia Smelting Company | Oxidative-reductive multi-stage bleaching of ground wood pulp |
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