METHOD FOR WASHING A GLASS CONTAINER
The present invention relates to a method for washing a glass container comprising the steps of washing the glass container with a liquid containing a chelating agent, and controlling the concentration of the free-available chelating agent within the liquid by a colorimetric detection. The invention further relates to an apparatus for carrying out such a method and the use of such an apparatus.
1 . A method for washing a glass container comprising the steps of:
(A) washing the glass container with a liquid containing a chelating agent, and
(B) Controlling the concentration of the free-available chelating agent within the liquid by a calorimetric detection.
2 . The method of claim 1 , wherein
i) the method is an automatic and/or continuous method;
ii) the method is carried out for refilling the glass container;
iii) the glass container is a bottle, preferably a bottle for beer or beverages,
iv) step (A) is carried out as a pre-final rinse step; and/or
v) step (B) is controlled by at least two independent calorimetric detections.
3 . The method of claim 1 , wherein the chelating agent is selected from the group consisting of EDTA (ethylenediaminetetracetic acid), EGTA (ethyleneglycol-bis-(b-aminoethyl ether)-N,N-tetraacetic acid), NTA (nitrilotriacetic acid), DTPA (diethylenetriaminepentaacetic acid), HEIDA (N-(2-hydroxyethyl)iminodiacetic acid disodium salt), IDS (iminodisuccinate sodium salt), MGDA(methylglycine diacetate0, glucomic acid, 2,2′-bipyridyl and mixtures thereof, in particular ethylenediaminetetracetic acid (EDTA) and/or the liquid is an aqueous solution.
4 . The method of claim 1 , wherein the concentration of the free-available chelating agent within the liquid in step (A) is between 2.5 and 25 ppm and/or the pH-value of the liquid is between 6.5 and 8.5.
5 . The method of claim 1 , wherein the colorimetric detection comprises taking a sample from the liquid employed in step (A) and said sample is transferred to a calorimetric detection unit for carrying out step (B).
6 . The method of claim 5 , wherein the change in colour of the colorimetric detection is between 525 and 880 nm and/or the colorimetric detection is carried out by reacting the free-available chelating agent with a precise amount of a compound to form a complex.
7 . The method of claim 6 , wherein the compound, which reacts with the free-available chelating agent during the calorimetric detection to form a complex is selected from the group consisting of MgSO 4 , Mg(NO 3 ) 2 , MgCl 2 , CaSO 4 , Ca(NO 3 ) 2 , CaCl 2 , ZnSO 4 , Zn(NO 3 ) 2 , and ZnCl 2 and/or the indicator employed in the calorimetric detection is 3-hydroxy-4-[(1-hydroxy-2-naphthalenyl)azo]-7-nitro-1-naphalenesulfonic acid monosodium salt, 2-hydroxy-1-(2-hydroxy-4-sulfonaphtyl-1-azo)-naphthalene-3-carboxylic acid, 2,7-bis [bis(carboxymethyl)-aminomethyl]-fluorescin, 6-(5-chloro-2-hydroxy-4-sulfophenylazo)-5-hydroxy-1-naphtalenesulfonic acid disodium salt, ammonium purpurate hydrate or 3-hydroxy-4-(6-hydroxy-m-tolylazo)naphthalene-1-sulfonic acid.
8 . The method of claim 1 , wherein an acoustic and/or visible signal is effected by the calorimetric detection in case the concentration of the free-available chelating agent within the liquid in step (A) is below 2.5 or above 25 ppm.
9 . The method of claim 8 , wherein in case o a continuous method and the detection of a concentration of the free-available chelating agent of below 2.5 ppm, the washing of the glass container is stopped until the concentration of the free-available chelating agent is raised above 2.5 ppm by adding additional chelating agent into step (A).
10 . The method of claim 8 , wherein in case of a continuous method and the detection of a concentration of the free-available chelating agent of above 25 ppm, the addition of additional chelating agent into step (A) is stopped until said concentration is below 25 ppm.
11 . The method of claim 1 , further comprising the steps of:
(C) optionally washing the glass container by a pre-wash step;
(D) washing the glass container with a caustic liquid;
(E) washing the glass container with heated water; and/or
(F) washing the glass container by a final rinse step.
12 . The method of claim 11 , wherein the order of the washing steps is (D), (E), (A), and (F) and step (C) is optionally carried out prior to the step (D).
13 . An apparatus comprising at least one section (I) for washing glass containers and said section (I) is connected with at least two independent colorimetric detection units.
14 . The apparatus of claim 13 , wherein the section (I) is the second last section of all washing sections employed within the apparatus.
15 . The apparatus of claim 13 , wherein the calorimetric detection unit comprises:
i) a linear peristaltic pump or a membrane pump;
ii) an electronic control panel;
iii) a calorimeter, optionally with a solid-state mixing system;
iv) a supply for the chemicals employed during calorimetric detection; and
v) a corrosion-resistant case.
16 . The apparatus of claim 13 , wherein the apparatus further comprises
optionally a section (II) for carrying out a pre-washing step;
a section (III) for carrying out a caustic washing;
a section (IV) for carrying out thermal treatment with heated water;
a section (V) for carrying out a final rinse step; and/or
optionally a filter.
17 . The apparatus of claim 16 , wherein each section is an individual tank.
18 . The use of an apparatus as claimed in claim 13 , to control the concentration of a free-available chelating agent in a liquid.
19 . The use of claim 18 , wherein the concentration is controlled in a process for washing containers, preferably PET bottles or glass bottles, in a laundry process, preferably washing of textiles, in a process for cleaning in place applications in the food and beverage industry, in a process for crate washing, in a process for water treatment, in a process of mechanical ware washing, in a process for lubricating and cleaning of feed and conveyance installations and in a process for cleaning hospital equipment.
20 . The use of claim 18 , wherein the concentration is controlled in a process after a caustic washing step.