SE506228C2 - Delignification process with the addition of additives in the form of an aqueous solution comprising phenols and pyrazolidones - Google Patents
Delignification process with the addition of additives in the form of an aqueous solution comprising phenols and pyrazolidonesInfo
- Publication number
- SE506228C2 SE506228C2 SE9600182A SE9600182A SE506228C2 SE 506228 C2 SE506228 C2 SE 506228C2 SE 9600182 A SE9600182 A SE 9600182A SE 9600182 A SE9600182 A SE 9600182A SE 506228 C2 SE506228 C2 SE 506228C2
- Authority
- SE
- Sweden
- Prior art keywords
- aqueous solution
- phenols
- pyrazolidones
- grams per
- per liter
- Prior art date
Links
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
- D21C3/003—Pulping cellulose-containing materials with organic compounds
-
- 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
- D21C3/22—Other features of pulping processes
- D21C3/222—Use of compounds accelerating the pulping processes
Abstract
Description
15 20 25 30 35 506 22s_ 2 vara. Trots att det endast små mängder av antrakinon, be- -räknat på vedmängden, satsas i koket, så är kostnaderna mycket höga. Varför andra alternativ är önskvärda. 15 20 25 30 35 506 22s_ 2 vara. Despite the fact that only small amounts of anthraquinone, calculated on the amount of wood, are invested in the cooking, the costs are very high. Why other options are desirable.
Tidigare känd teknik.Prior art.
I det amerikanska patentet US, A, 4,213,821 beskrivs en process, som utnyttjar denna redox-jämvikt.U.S. Patent No. 4,213,821 discloses a process utilizing this redox equilibrium.
Till kokvätskan tillsätts antrakinonföreningar tillsammans med reduktionsmedel, såsom natrium-eller zinkditionit, natriumborhydrid eller zinkpulver och natrium hydroxid. I ett annat amerikanskt patent US, A, 4,786,365 framställs massa genom att antrakinon och små mängder av natrium sulfid tillsätts kokvätskan.Anthraquinone compounds are added to the cooking liquid together with reducing agents, such as sodium or zinc additionite, sodium borohydride or zinc powder and sodium hydroxide. In another U.S. patent, A, 4,786,365 pulp is prepared by adding anthraquinone and small amounts of sodium sulfide to the cooking liquid.
Kinoner och antrakinoner är effektiva additiv och de är stabila under massaprocessen. I föreliggande uppfinning använder man sig av motsvarande redox-jämvikt, som nämnts ovan. De föreningar som är av speciellt intres- se är olika fenoler, såsom kinon, antrakinon, aminofenoler m.fl., vilka är i redox-jämvikt med motsvarande ketofor- mer. Föredragna fenoler är sådana, som har oxiderbara grupper i paraställning. Sådana fenoler kan ha struktur- formel I eller II: on oH 111 H1 OH NHRQ I II där H, OH, , NH,, NHR, SO§, Cl, eller Br, H, metyl, etyl, fenyl, bensyl, eller cnzcoon .Quinones and anthraquinones are effective additives and are stable during the pulping process. The present invention uses the corresponding redox equilibrium, as mentioned above. The compounds of particular interest are various phenols, such as quinone, anthraquinone, aminophenols and others, which are in redox equilibrium with the corresponding keto forms. Preferred phenols are those which have oxidizable groups in the para position. Such phenols may have structural formula I or II: on o H 111 H1 OH NHRQ I II where H, OH,, NH, NHR, SO§, Cl, or Br, H, methyl, ethyl, phenyl, benzyl, or benzone .
Föreliggande uppfinning innefattar en vattenlös- ning bl.a. innehållande fenoler och pyrazolidoner, som tillsätts kokvätskan och får delta i koket. vattenlös- ningen är företrädesvis alkalisk och är en restprodukt R1 kan vara R2 kan vara från fotobranchen och används för framkallningen av filmer och fotografier. Genom att använda sig av dessa restpro- 10 15 20 25 30 35 506 228 3 dukter kan man pà ett effektivt sätt bringa ned kostnader- ^na för additivet samtidigt som restprodukten kommer in i ett nytt industriellt kretslopp och därmed inte ytterli- gare belastar miljön.The present invention comprises an aqueous solution i.a. containing phenols and pyrazolidones, which are added to the cooking liquid and allowed to participate in the cooking. the aqueous solution is preferably alkaline and is a residual product R1 may be R2 may be from the photo industry and is used for the development of films and photographs. By using these residual products, the costs of the additive can be effectively reduced at the same time as the residual product enters a new industrial cycle and thus does not further burden the environment. .
Pyrazolidoner är ämnen, som samverkar med fenoler och förstärker deras verkan genom en förbättrad redox- jämvikt.Pyrazolidones are substances that interact with phenols and enhance their action through improved redox equilibrium.
Genom att för bättra redox-jämvikten samt att finna råvaror med lågt pris förbättrar förutsättningarna avsevärt för massaindustrin, dá det fordras enorma kvanti- teter av kemikalier för att täcka produktionsbehovet.By improving the redox equilibrium and finding raw materials with a low price, the conditions for the pulp industry improve significantly, as enormous quantities of chemicals are required to cover the production needs.
Enligt en föredragen utföringsform av uppfinning- en tillsätts en vattenlösning av fenoler i en halt mellan 1 till 50 gram per liter, företrädesvis mellan 10 till 30 gram per liter, mest föredraget mellan 15 till 25 gram per liter, samt att mängden fenoler tillsätts i en mängd mel- lan 0,001% till 10%, företrädesvis mellan 0,01% till 3%, baserat pà vedvikten. Halten pyrazolidon i vatten lös- ningen är mellan 0,1 till 30 gram per liter, företrädesvis mellan 0,1 till 20 gram per liter, mest föredraget mellan 0,1 till 10 gram per liter.According to a preferred embodiment of the invention, an aqueous solution of phenols is added in a content between 1 to 50 grams per liter, preferably between 10 to 30 grams per liter, most preferably between 15 to 25 grams per liter, and that the amount of phenols is added in a amount between 0.001% to 10%, preferably between 0.01% to 3%, based on the wood weight. The content of pyrazolidone in the aqueous solution is between 0.1 to 30 grams per liter, preferably between 0.1 to 20 grams per liter, most preferably between 0.1 to 10 grams per liter.
I en annan föredragen utföringsform av uppfin- ningen innefattar fenolerna 1,4-bensendiol, hydrokinon- monosulfonat, hydrokinondisulfat, 2-kloro-hydrokinon, 2- bromo-hydrokinon, 4-aminofenol, N-(4-hydroxifenyl)-glycin monometyl-p-amino-fenolsulfat eller oxiderade former därav och att pyrazolidonerna innefattar 1-fenyl-3-pyrazolidon, 4-metyl-1-fenyl-pyrazolidon, 4-metyl-4-hydroximetyl-1-fe- nyl-3-pyrazolidon, 4,4-dimetyl-1-fenyl-3-pyrazolidon eller redox-produkter därav.In another preferred embodiment of the invention, the phenols include 1,4-benzenediol, hydroquinone monosulfonate, hydroquinone disulfate, 2-chloro-hydroquinone, 2-bromo-hydroquinone, 4-aminophenol, N- (4-hydroxyphenyl) -glycine monomethyl- p-amino-phenol sulfate or oxidized forms thereof and that the pyrazolidones include 1-phenyl-3-pyrazolidone, 4-methyl-1-phenyl-pyrazolidone, 4-methyl-4-hydroxymethyl-1-phenyl-3-pyrazolidone, 4 , 4-dimethyl-1-phenyl-3-pyrazolidone or redox products thereof.
I en ytterligare föredragen utföringsform av uppfinningen är vattenlösningen alkalisk eller sur.In a further preferred embodiment of the invention, the aqueous solution is alkaline or acidic.
I en ytterligare föredragen utföringsform av uppfinningen innefattar vattenlösningen även glutaralde- hyd, di-eller tri-etylenglykol och/eller ättiksyra.In a further preferred embodiment of the invention, the aqueous solution also comprises glutaraldehyde, di- or tri-ethylene glycol and / or acetic acid.
I den mest föredragna utföringsformen av uppfin- ningen är vattenlösningen en restprodukt från framkallning av fotografisk film eller fotografiskt papper. 10 15 20 25 30 506 228 4 I restprodukten kan även ingá oorganiska ämnen 'såsom natriumsulfit, natriumhydroxid och natriumkarbonat, vilka redan ingár i kokvätskan och därför är till nytta för kokprocessen.In the most preferred embodiment of the invention, the aqueous solution is a residual product from the development of photographic film or photographic paper. The residual product may also contain inorganic substances such as sodium sulphite, sodium hydroxide and sodium carbonate, which are already present in the cooking liquid and are therefore useful for the cooking process.
För att undersöka effekten av additivet gjordes en jämförande studie, där olika mängder tillsatt additiv jämfördes med ett konventionellt sulfatkok. Det gjordes två jämförande kok-serier och resultaten visas i tabell 1 och 2. Försöksserierna är inte begränsande för uppfinning- en utan illustrerar den.To investigate the effect of the additive, a comparative study was done, where different amounts of added additive were compared with a conventional sulfate cooker. Two comparative cooking series were made and the results are shown in Tables 1 and 2. The experimental series are not limiting of the invention but illustrate it.
Serie 1 300 g Torkad industriell barrvedflis, med en torrhalt pà 92,5%, impregnerades vid 5 bars tryck, följt av kokning i 115 minuter. Kokningen utfördes i en rote- vedförhál- landet pà 4:1, en effektiv alkalinitet på 20% beräknat pà ved och sulfiditet pà 35%. Till kokvätskan tillsattes rande autoklav och genomfördes med ett vätske varierande mängder av "additivet". En koktemperatur pà 170°C uppnàddes efter en temperaturökning pà 1'C/min. Vid avslutat kok tvättades massorna och avvattnades, varefter de analyserades. Analysdata samanfattades i tabell 1.Series 1,300 g Dried industrial softwood chips, with a dry content of 92.5%, were impregnated at 5 bar pressure, followed by boiling for 115 minutes. The boiling was carried out in a rotary wood ratio of 4: 1, an effective alkalinity of 20% calculated on wood and sulphidity of 35%. A boiling autoclave was added to the cooking liquid and various amounts of the "additive" were carried out with a liquid. A boiling temperature of 170 ° C was reached after a temperature increase of 1 ° C / min. At the end of boiling, the masses were washed and dewatered, after which they were analyzed. Analysis data were summarized in Table 1.
Tabell 1 Kok addi- Kappa- Sila- Spet % Totalt Visko- nr. tiv ml tal tut- utbyte sitet byte % % ml/g 1 O 24,6 44,2 0,8 45,0 - 2 1,5 24,1 43,7 1,0 44,7 - 3 15 24,2 44,8 0,6 45,4 - 4 30 23,9 44,2 0,7 45,0 - 5 75 24,2 44,5 0,6 45,1 - 6 150 24,3 44,5 0,9 45,3 - 10 15 20 Serie 2 Försöksserie 2 genomfördes under_samma betingel- 506 228 ser och med sama förlopp som försöksserie 1. Resultatet av analyserna visas i tabell 2.Table 1 Boil addi- Kappa- Sila- Spet% Total Visco- no. tiv ml number spout yield site byte%% ml / g 1 O 24.6 44.2 0.8 45.0 - 2 1.5 24.1 43.7 1.0 44.7 - 3 15 24.2 44.8 0.6 45.4 - 4 30 23.9 44.2 0.7 45.0 - 5 75 24.2 44.5 0.6 45.1 - 6 150 24.3 44.5 0, 9 45.3 - 10 15 20 Series 2 Experimental series 2 was carried out under the same conditions and with the same procedure as experimental series 1. The results of the analyzes are shown in Table 2.
Tabell 2 Kok addi- Kappa- Sila- Spet % Totalt Visko- nr. tiv ml tal tut- utbyte sitet byte % % ml/g 1 O 21,9 43,1 0,5 43,6 1030 2 1,5 23,7 43,5 0,9 44,4 - 3 15 22,3 43,5 o,9 44,4 1050 " ll 4 30 22,8 43,6 0,9 44,4 - 5 75 25,2 43,6 1,1 44,7 - 6 150 27,0 42,6 1,6 44,2 - “ De báda försöksserierna visar att "additivet" in- nehállande fenoler och pyrazolidonerökar utbytet med 0,4%.Table 2 Boil addi- Kappa- Sila- Spet% Total Visco- no. tiv ml number spout yield site byte%% ml / g 1 O 21.9 43.1 0.5 43.6 1030 2 1.5 23.7 43.5 0.9 44.4 - 3 15 22.3 43.5 o, 9 44.4 1050 "ll 4 30 22.8 43.6 0.9 44.4 - 5 75 25.2 43.6 1.1 44.7 - 6 150 27.0 42.6 1.6 44.2 - The two series of experiments show that the "additive" containing phenols and pyrazolidone increases the yield by 0.4%.
Additiv innehållande fenoler och pyrazolidoner är därför intressanta vid pappersmassa framställning och är använd- bara alternativ jämfört med de dyra konventionella additi- Ven , såsom antrakinon.Additives containing phenols and pyrazolidones are therefore of interest in pulp production and are useful alternatives to the expensive conventional additives, such as anthraquinone.
Claims (8)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9600182A SE506228C2 (en) | 1996-01-18 | 1996-01-18 | Delignification process with the addition of additives in the form of an aqueous solution comprising phenols and pyrazolidones |
AU13275/97A AU1327597A (en) | 1996-01-18 | 1997-01-20 | Delignification of lignocellulosic material with a cooking liquor containing phenols and pyrazolidones |
PCT/SE1997/000082 WO1997026402A1 (en) | 1996-01-18 | 1997-01-20 | Delignification of lignocellulosic material with a cooking liquor containing phenols and pyrazolidones |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE9600182A SE506228C2 (en) | 1996-01-18 | 1996-01-18 | Delignification process with the addition of additives in the form of an aqueous solution comprising phenols and pyrazolidones |
Publications (3)
Publication Number | Publication Date |
---|---|
SE9600182D0 SE9600182D0 (en) | 1996-01-18 |
SE9600182L SE9600182L (en) | 1997-07-19 |
SE506228C2 true SE506228C2 (en) | 1997-11-24 |
Family
ID=20401068
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE9600182A SE506228C2 (en) | 1996-01-18 | 1996-01-18 | Delignification process with the addition of additives in the form of an aqueous solution comprising phenols and pyrazolidones |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU1327597A (en) |
SE (1) | SE506228C2 (en) |
WO (1) | WO1997026402A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP7242483B2 (en) * | 2019-09-12 | 2023-03-20 | 日華化学株式会社 | Cooking accelerator for lignocellulosic material and method for producing pulp using the same |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA773044B (en) * | 1976-06-02 | 1978-04-26 | Australian Paper Manufacturers | Improvements in pulping processes |
CA1110413A (en) * | 1977-12-14 | 1981-10-13 | Oji Paper Co., Ltd. | Process for pulping lignocellulosic material |
US4248663A (en) * | 1978-07-05 | 1981-02-03 | Pulp And Paper Research Institute Of Canada | Pulping with an alkaline liquor containing a cyclic keto compound and an amino compound |
-
1996
- 1996-01-18 SE SE9600182A patent/SE506228C2/en not_active IP Right Cessation
-
1997
- 1997-01-20 WO PCT/SE1997/000082 patent/WO1997026402A1/en active Application Filing
- 1997-01-20 AU AU13275/97A patent/AU1327597A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
AU1327597A (en) | 1997-08-11 |
SE9600182L (en) | 1997-07-19 |
SE9600182D0 (en) | 1996-01-18 |
WO1997026402A1 (en) | 1997-07-24 |
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