CS200799B1 - Method of preparing oxidized pectins available as sequestring additive into detergent mixtures - Google Patents

Method of preparing oxidized pectins available as sequestring additive into detergent mixtures Download PDF

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CS200799B1
CS200799B1 CS480878A CS480878A CS200799B1 CS 200799 B1 CS200799 B1 CS 200799B1 CS 480878 A CS480878 A CS 480878A CS 480878 A CS480878 A CS 480878A CS 200799 B1 CS200799 B1 CS 200799B1
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Czechoslovakia
Prior art keywords
pectin
pectins
additive
sequestring
available
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CS480878A
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Czech (cs)
Slovak (sk)
Inventor
Kamil Antos
Pavol Hodul
Elena Markusovska
Anton Blazej
Jan Cesnek
Frantisek Rendos
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Kamil Antos
Pavol Hodul
Elena Markusovska
Anton Blazej
Jan Cesnek
Frantisek Rendos
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Application filed by Kamil Antos, Pavol Hodul, Elena Markusovska, Anton Blazej, Jan Cesnek, Frantisek Rendos filed Critical Kamil Antos
Priority to CS480878A priority Critical patent/CS200799B1/en
Publication of CS200799B1 publication Critical patent/CS200799B1/en

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  • Biological Depolymerization Polymers (AREA)

Description

Predmetom vynálezu Je příprava oxidovaných pektínov ako eekvestračných přísad do detergentných zmesí, ktorými možno nahradil až 50 » doteraz používaných polyfosfátov, najma tripolyfosfátu sodného.SUMMARY OF THE INVENTION It is an object of the present invention to prepare oxidized pectins as e-extraction ingredients in detergent compositions which can replace up to 50 polyphosphates used hitherto, in particular sodium tripolyphosphate.

Doposiaí sa ako sekvenčně činidlá do pracích prostriedkov používajú najma polyfosfáty, menovite tripolyfoefát sodný, ktorý Je nutnou přísadou pre pranie v tvrdéJ vodě. Ide tu o komplexně viazanie kovov alkalických zemin vápnika a horčíka, ktoré sú příčinou tvrdosti vody a o viazanie Saláích kovov ako Je železo, med apod. Velkou nevýhodou polyfosfátov Je ich pósobenie na odpadové vody, kde fosforečnany vyvolávajú eutrofizačné procesy, tj. mimoriadny rast fytoplanktonu, najma rias. Uvedené procesy obzvláSt v stojacich vodách (Jazerá, vodné nádrže, ústia riek v moru), vyvolávajú udusenie vod, přechod na anaerobně procesy spojené s uvolňováním sirovodika a zániku biologických procesov živých organizmov. Z uvedeného dovodu sa hladajú náhrady polyfosfátov, ktoré by zmaedzili uplatneniu eutrofizačných procesov v odpadných vodách. Doteraz boli navrhnuté organické zlúčeniny, ktoré sú schopné komplexně viazat kovy alkalických zemin. Ide menovite o následovně zlúčeniny vo formě alkalických, sodných solí (komplexóny): kyselina nitrilotrioctová, kyselina etyléndiamíntetraoctová; polymérne kyseliny: ako kyselina polyakrylová, kyselina polyetylénmaleionová; oxidované škroby; nižSie di a trikarboxylové kyseliny: kyselina citrónová, kyselina vinna atp.Up to now, polyphosphates, namely sodium tripolyphosphate, which is a necessary additive for washing in hard water, are used as sequencing agents in detergents. It is a complex binding of alkaline earth metals calcium and magnesium, which are the cause of water hardness and binding of Salami metals such as iron, honey, etc. A major disadvantage of polyphosphates is their interaction with wastewater, where phosphates induce eutrophication processes, ie. extraordinary growth of phytoplankton, especially algae. These processes, especially in standing waters (lakes, reservoirs, estuaries), cause water suffocation, transition to anaerobic processes associated with the release of hydrogen sulfide and the disappearance of biological processes in living organisms. For this reason, polyphosphate substitutes are being sought which would limit the application of eutrophication processes in waste water. So far, organic compounds have been proposed which are capable of complex binding of alkaline earth metals. These are, in particular, the following compounds in the form of alkaline, sodium salts (complexones): nitrilotriacetic acid, ethylenediaminetetraacetic acid; polymeric acids: such as polyacrylic acid, polyethylene maleic acid; oxidized starches; lower di and tricarboxylic acids: citric acid, tartaric acid and the like.

200 799200 799

Uvedené zlúčeniny pokial obsahujú v menšeJ molekule niekolko karboxylových kyselin, vyznačujú sa vo formě alkalických solí len slabšou aekveetračnou účinnoatou pri súčasnej dobrej biologickéj odbúratelnosti, napr. kyselina citrónová. Naopak, u polymérnych kyselin, ako napr. kyselina polyakrylová, ide o dobrú sekvestračnú účinnost, ale o súčasne slabú biologickú odbúrateínoet.Said compounds, if contained in a smaller molecule of several carboxylic acids, are characterized in the form of alkali salts only by a weaker aeketetration efficiency while at the same time good biodegradability, e.g. citric acid. Conversely, for polymeric acids such as e.g. polyacrylic acid, it is a good sequestering efficiency, but at the same time a poor biodegradability.

Uvedené nedostatky odstraňuje vynález, ktorého podstata je v tom, že aa nfa pektín poaobí plynným chlórom v prostředí vodného roztoku hydroxidu sodného pri teplote 0 až 30 °C, s výhodou 10 až 20 °C a produkt sa izoluje vllatím do organického rozpúšíadle miešatelného 8 vodou, s výhodou alkoholu, napr. metanolu.The aforementioned drawbacks are overcome by the invention, wherein the aa nfa pectin is treated with chlorine gas in an aqueous sodium hydroxide solution at a temperature of 0 to 30 ° C, preferably 10 to 20 ° C, and the product is isolated by blowing into a water-miscible organic solvent. , preferably an alcohol, e.g. methanol.

Přednost navrhovaného použitia oxidovaných pektínov spočívá v tom, že ea už samotné pektíuy vyznačujú vysokou komplexotvornou účinnostou viazania kovov alkalických zemin vápnika a horčíka a táto ich účinnost aa oxidáciou póaobením chlóru v prostředí hydroxidu eodného umocní vytvořením Salších dvoch karboxylových skupin na jednotku galakturonovej kyseliny podlá rovnice:The advantage of the proposed use of oxidized pectins is that the pectins themselves are characterized by a high complexing efficiency of the binding of alkaline earth metals calcium and magnesium, and this efficiency and by oxidation by chlorination in the sodium hydroxide environment will be enhanced.

ClCl

COOH oxidacia Na 01?COOH oxidation Na 01?

COONaCOONa

V dósledku toho ea uplatňuje vysoká schopnost viazania kovov alkalických zemin a sekvestračná účinnost.As a result, ea exerts high alkaline earth metal binding and sequestering efficiency.

V Salšom je příprava oxidovaných pektínov za účelom ich využitia ako sekveatračných činidiel popísaná v príkladoch prevedenia bez toho, že by sa na tieto výlučné vztahovala.In Saler, the preparation of oxidized pectins for use as sequencing agents is described in the Examples without being limited to these.

Příklad 1Example 1

100 g slnečnicového pektínu aa suspenduje v 900 ml vody a nechá napuchat. pH hodnota suspenzie sa nastaví roztokom hydroxidu eodného na hodnotu 9. Potom aa bahom 4 hodin privedie 290 g chlóru a 325 g NaOH vo formě 25 X^ného vodného roztoku synchronně tak, aby pH roztoku sa udržiavalo v medziach 8 až 9. Teplota reakčnej nádoby sa chladením ladom udržuje medzi 10 až 20 °C. Potom sa ešte mieša pri pH 8 až 9 za normálněj teploty, čím aa oxidačná reakcia ukončí. Potom sa reakčná zmes zbaví nepatrného rozpustného podielu filtráciou a vleje sa za intenzívneho miešania do 7 litrov metanolu. Produkt vypadne vo formě dobré flltrovatelnej zrazeniny ako sodná sol. Odsaje sa a premyje 1 litrom metanolu a vysuší vo vákuovom exikátore. Získá sa 87 g bieleho produktu.100 g of sunflower pectin aa is suspended in 900 ml of water and allowed to swell. The pH of the suspension is adjusted to 9 with sodium hydroxide solution. Thereafter, 290 g of chlorine and 325 g of NaOH in the form of a 25% aqueous solution are introduced in a synchronous manner over a period of 4 hours so that the pH of the solution is kept between 8 and 9. is maintained at between 10 and 20 ° C with ice cooling. It is then stirred at pH 8 to 9 at normal temperature to complete the oxidation reaction. Thereafter, the reaction mixture was freed from the insoluble matter by filtration and poured into 7 L of methanol with vigorous stirring. The product precipitates as a good filterable precipitate as the sodium salt. It is filtered off with suction and washed with 1 l of methanol and dried in a vacuum desiccator. 87 g of a white product are obtained.

Takto získaný produkt sa použije ako přísada pri praní, pričom aa nahradí určité množstvo tripolyfoefátu eodného.The product thus obtained is used as a laundry additive, replacing aa some of the sodium tripolyphosphate.

Pranie sa uakutočnilo na bavlnenej sprievodnej tkanině podlá ČSN 80 01 01 počee 10 mlnút pri teplote 80 °C špinenej modelovou špinou nasledovneho zloženie:Washing was carried out on a cotton companion fabric according to CSN 80 01 01 in 10 mills at a temperature of 80 ° C, soiled with a model dirt of the following composition:

Sunar - 40 g, želatina - 3 g, čierna tuš - 22 g, slnečnicový olej rafinovaný - 60 g, chlorid uhličitý - 25 g, destilovaná voda - 200 g. Pralo aa na laboratórnej pračka Kolteet. BělostSunar - 40 g, gelatin - 3 g, black ink - 22 g, refined sunflower oil - 60 g, carbon tetrachloride - 25 g, distilled water - 200 g. Laundry on laboratory washing machine Kolteet. whiteness

200 798 zašpiněnoj vzorky, ako aj vypratej vzorky a nešpinenej vzorky sa stanovila na leukometri fy Zeies Jena pri bielom filtri. Obsah zložiek pracieho kúpeía /celkove 5 g pracích přísad na liter kúpeía/, ako aj percento vyprania vypláva z tab. 1.200,798 soiled samples as well as washed and unclean samples were determined on a Zeies Jena leukometer with a white filter. The content of the components of the washing bath (total of 5 g of detergents per liter of bath), as well as the percentage of washing results, are shown in Tab. First

Tab. 1. Percento vyprania modelovej Spiny zo sprievodnej bavlnenej tkaniny za použitia g pracej přísady na liter pracieho kúpeía, pričom pracia přísada obsahuje oxidovaný slnečnicový pektínTab. 1. Percent wash of model cotton spin spin using g washing additive per liter of washing bath, the washing additive containing oxidized sunflower pectin

Zložkacomponent

Percentuálně zloženie pracej přísadyDetergent composition percentage

ABSABS

TPF oxid. pektín Na2OO3 Na2S04 CMC/LovozaTPF oxide. pectin Na 2 OO 3 Na 2 SO 4 CMC / Lovoza

25 25 25 25 40 40 30 30 - - 10 10 19 19 19 19 15 15 15 15 1 1 1 1

25 25 25 25 20 20 10 10 20 20 30 30 19 19 19 19 15 15 15 15 1 1 1 1

25 25 25 25 - - - - 40 40 - - 19 19 19 19 15 15 15 15 1 1 1 1

Tvrdoaí vody °N 20 °NHard water ° N 20 ° N

66,18 64,9466.18 64.94

55,55 54,4055.55 54.40

Percento vypraniaPercentage of wash

63„23 58,1363 '23 58,13

53,41 52,8053.41 52.80

43,83 41,5243.83 41.52

38,03 38,8938.03 38.89

Příklad 2Example 2

Ako příklad 1, avšak miesto slnečnicovšho pektínu ea použije citrusový pektín Výíažk 91 g produktuAs Example 1, however, instead of sunflower pectin ea, citrus pectin will yield 91 g of product.

Příklad 3Example 3

Ako příklad 1, avšak miesto slnečnicovšho pektínu sa použije repný pektín Výlažok 82 g produktuAs Example 1, however, instead of sunflower pectin, beet pectin was used. Yield 82 g.

Claims (4)

1. Sposob přípravy oxidovaných pektínov vhodných ako sekvestračných přísad do detergentnýeh zmesí, vyznačujúci sa tým, že ša na pektín posobí plynným chlórom v prostředí vodného roztoku hydroxidu sodného pri teplote 0 až 30 °C, s výhodou 10 až 20 °C a produkt sa izoluje vliatím do organického roupúšíadla miešateíného s vodou, s výhodou alkoholu například metanolu.Process for the preparation of oxidized pectins suitable as sequestering additives for detergent compositions, characterized in that the pectin is treated with chlorine gas in an aqueous solution of sodium hydroxide at 0 to 30 ° C, preferably 10 to 20 ° C and the product is isolated by pouring into a water miscible organic solvent, preferably an alcohol such as methanol. 2. Sposob pódia bodu 1, vyznačujúci ea tým, že aa ako pektín použije slnečnicový pektín.2. A method according to claim 1, wherein aa is sunflower pectin. 3. Sposob pódia bodu 1, vyznačujúci sa tým, že sa ako pektín použije citrusový pektín.3. The method of claim 1, wherein the pectin is citrus pectin. 4. Sposob pódia bodu 1, vyznačujúci sa tým, že sa ako pektín použije repný pektín.4. A method according to claim 1, wherein the pectin is a beet pectin.
CS480878A 1978-07-19 1978-07-19 Method of preparing oxidized pectins available as sequestring additive into detergent mixtures CS200799B1 (en)

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