DIN 19643-2-2012 Treatment of water of swimming pools and baths - Part 2 Combinations of process with fixed bed filters and precoat filters《游泳池和洗澡池水的处理 第2部分 吸附法和预涂过滤机处理方法组合》.pdf

1、 November 2012 DIN 19643-2 ICS 13.060.30 Supersedes DIN 196432:199704 and DIN 196435:200009 Treatment of water of swimming pools and baths Part 2: Combinations of process with fixed bed filters and precoat filters, English translation of DIN 19643-2:2012-11 Aufbereitung von Schwimm und Badebeckenwas

2、ser Teil 2: Verfahrenskombinationen mit Festbett und Anschwemmfiltern, Englische bersetzung von DIN 196432:201211 Traitement de leau des bassins des piscines et des bains Partie 2: Combinaisons du procs avec filtres matriaux granulaire et filtres couches, Traduction anglaise de DIN 196432:201211 Doc

3、ument comprises 20 pages Translation by DINSprachendienst. In case of doubt, the Germanlanguage original shall be considered authoritative. No part of this standard may be reproduced without prior permission of DIN Deutsches Institut fr Normung e. V., Berlin. Beuth Verlag GmbH, 10772 Berlin, Germany

4、, has the exclusive right of sale for German Standards (DINNormen). English price group 11 www.din.de www.beuth.de!$?u“ 1972882 11.15DIN 19643-2:2012-11 2 A comma is used as the decimal marker. Contents Page Foreword . 3 1 Scope 5 2 Normative references 5 3 Principle of the respective process combin

5、ations. 6 3.1 Flocculation filtration - chlorination . 6 3.2 Adsorption by powdered activated carbon flocculation filtration chlorination 6 3.3 Flocculation multi-layer filtration using adsorptive carbon chlorination . 6 3.4 Flocculation filtration adsorption by granular activated carbon chlorinatio

6、n . 7 3.5 Flocculation filtration ultraviolet radiation chlorination . 7 3.6 Adsorption by powdered activated carbon filtration using precoat filter chlorination 7 4 Process stages . 7 4.1 Acid neutralizing capacity adjustment 7 4.1.1 General 7 4.1.2 Compounds used to adjust acid neutralizing capaci

7、ty . 7 4.1.3 Acid neutralizing capacity values 8 4.1.4 Checking the acid neutralizing capacity 8 4.2 pH value adjustment . 8 4.3 Flocculation . 8 4.3.1 General 8 4.3.2 Flocculants . 8 4.3.3 Minimum quantity of flocculant to be added 9 4.3.4 Checking the flocculation 9 4.4 Filtration . 9 4.4.1 Genera

8、l 9 4.4.2 Filtration by rapid filters as specified in DIN 19605 . 10 4.4.3 Filtration using precoat filters as specified in DIN 19624 13 4.5 Eliminating disinfection by-products 14 4.5.1 General . 14 4.5.2 Adsorption by multi-layer filtration 14 4.5.3 Adsorption by powdered activated carbon. 14 4.5.

9、4 Adsorption by granular activated carbon . 15 4.5.5 Ultraviolet radiation 17 4.6 Testing the flocculation filtration and sorption filtration systems 18 4.7 Chlorination 20 5 Load capacity factor, k . 20 DIN 19643-2:2012-11 3 Foreword This standard has been prepared by Working Committee NA 119-04-13

10、 AA Schwimmbeckenwasser of the Normenausschuss Wasserwesen (Water Practice Standards Committee). This revision was prompted by the need to merge Parts 2 and 5 of the DIN 19643 series of standards from 1997 and 2000, respectively, into a new single part, and by the need to take changes in the general

11、 requirements for the treatment of water of swimming pool and baths as specified in DIN 19643, Part 1 into account. This new standard focuses largely on describing those basic process combinations that include a fixed bed filter (referred to in the following as granular media filter) or precoat filt

12、er as one of the treatment stages. The process combinations specified in this standard illustrate various ways to implement methods of preventing and removing disinfection by-products. In addition to the application of powdered activated carbon and granular activated carbon in the downstream sorptio

13、n filters and adsorptive carbon in the top layer of a multi-layer filter, as was common up to now, the application of ultraviolet radiation as a method of eliminating chloramine compounds has now been included as well. The following individual process combinations have been defined: Flocculation fil

14、tration chlorination Flocculation multi-layer filter using adsorptive carbon chlorination Adsorption by powdered activated carbon flocculation filtration chlorination Flocculation filtration adsorption by granular activated carbon chlorination Flocculation filtration ultraviolet radiation chlorinati

15、on Flocculation multi-layer filtration using adsorptive carbon ultraviolet radiation chlorination Adsorption by powdered activated carbon filtration using precoat filters chlorination. Other process combinations can be used as a function of the application. DIN 19643 consists of the following parts,

16、 under the general title Treatment of water of swimming pools and baths: Part 1: General requirements Part 2: Combinations of process with fixed bed filters and precoat filters Part 3: Combinations of process with ozonization Part 4: Combinations of process with ultrafiltration Further parts may be

17、added to this standard in future. In order to ensure that the requirements set down in this standard are met, and bearing in mind economic aspects, it is recommended that only experienced specialist companies with appropriate references be DIN 19643-2:2012-11 4 commissioned to plan, build and instal

18、l the treatment facilities. Furthermore, effectiveness of the treatment should be checked at regular intervals by experienced staff. Attention is drawn to the possibility that some of the elements of this document may be the subject of patent rights. DIN (and/or DKE) shall not be held responsible fo

19、r identifying any or all such patent rights. Amendments This standard differs from DIN 19643-2:1997-04 and DIN 19643-5:2000-09 as follows: a) the contents of the two standards have been merged; b) a detailed description of the methods used to eliminate disinfection by-products has been added; c) the

20、 process combination using UV radiation has been included; d) the contents of the standard have been brought in line with state-of-the art technology; e) normative references have been updated. Previous editions DIN 19643: 1984-04 DIN 19643-2: 1997-04 DIN 19643-5: 2000-09 DIN 19643-2:2012-11 5 1 Sco

21、pe This standard, in conjunction with DIN 19643-1, applies to the treatment of water of swimming pools and baths by process combinations using granular media filters and precoat filters. It does not apply to therapeutic baths. 2 Normative references The following documents, in whole or in part, are

22、normatively referenced in this document and are indispensable for its application. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) applies. DIN 19605, Fixed bed filters for water treatment Structur

23、e and components DIN 19624, Precoat filters for water treatment DIN 19643-1:2012-11, Treatment of water of swimming pools and baths Part 1: General requirements DIN 19645, Treatment of spent filter backwash water from systems for treatment of water of swimming-pools and baths DIN 38409-7, German sta

24、ndard methods for the examination of water, waste water and sludge Parameters characterizing effects and substances (group H) Part 7: Determination of acid and base-neutralizing capacities (H 7) DIN EN 12904, Products used for treatment of water intended for human consumption Silica sand and silica

25、gravel DIN EN 12913, Products used for treatment of water intended for human consumption Powdered diatomaceous earth DIN EN 12914, Products used for treatment of water intended for human consumption Powdered perlite DIN EN 15031, Chemicals used for treatment of swimming pool water Aluminium-based co

26、agulants DIN EN 15075, Chemicals used for treatment of swimming pool water Sodium hydrogen carbonate DIN EN 15362, Chemicals used for treatment of swimming pool water Sodium carbonate DIN EN 15797, Chemicals used for treatment of swimming pool water Iron-based coagulants DIN EN 15798, Chemicals used

27、 for treatment of swimming pool water Filter media DIN EN 15799, Chemicals used for treatment of swimming pool water Powdered activated carbon DIN EN ISO 6878, Water quality Determination of phosphorus Ammonium molybdate spectrometric method DIN EN ISO 7027, Water quality Determination of turbidity

28、DIN EN ISO 10304-1, Water quality Determination of dissolved anions by liquid chromatography of ions Part 1: Determination of bromide, chloride, fluoride, nitrate, nitrite, phosphate and sulphate DIN EN ISO 15681-1, Water quality Determination of orthophosphate and total phosphorus contents by flow

29、analysis (FIA and CFA) Part 1: Method by flow injection analysis (FIA) DIN 19643-2:2012-11 6 DIN EN ISO 15681-2, Water quality Determination of orthophosphate and total phosphorus contents by flow analysis (FIA and CFA) Part 2: Method by continuous flow analysis (CFA) Deutsche Gesellschaft fr das Ba

30、dewesen e. V.: Zustzliche Desinfektionsmanahmen durch Hochchlorung im Bereich der Badewasseraufbereitung Muster einer Dienstanweisung1)(Additional disinfection measures by means of high chlorination levels in pool water treatment Example of work instructions) DVGW W 240, Beurteilung von Aktivkohlen

31、fr die Wasseraufbereitung2)(Assessment of activated carbon for water treatment) TRGS 500, Schutzmanahmen3)(Protective measures) 3 Principle of the respective process combinations 3.1 Flocculation filtration chlorination Dissolved colloidal impurities are destabilized by flocculation using iron(III)

32、and/or aluminium salts, and orthophosphates are partially precipitated. For this process, the pH value of the raw water is kept within a range consistent with the type of flocculant used. The mixture of iron(III) hydroxide and/or aluminium hydroxide and colloids is then removed by filtration. The fi

33、ltrate is chlorinated and fed to the pool or bath. The load capacity factor, k, is 0,5 m-3, equivalent to a supply water volume of 2 m3per person. 3.2 Adsorption by powdered activated carbon flocculation filtration chlorination The disinfection by-products are adsorbed by the powdered activated carb

34、on and possibly chemically converted. Dissolved colloidal impurities and finest particles of the powdered activated carbon are destabilized by flocculation using iron(III) salts and/or aluminium salts, and orthophosphates are partially precipitated. For this process, the pH value of the raw water is

35、 kept within a range consistent with the type of flocculant used. The mixture of contaminated powdered activated carbon, iron(III) hydroxide and/or aluminium hydroxide and colloids is then removed by filtration. The filtrate is chlorinated and fed to the pool or bath. The load capacity factor, k, is

36、 0,5 m-3, equivalent to a supply water volume of 2 m3per person. 3.3 Flocculation multi-layer filtration using adsorptive carbon chlorination Dissolved colloidal impurities are destabilized by flocculation using iron(III) salts and/or aluminium salts, and orthophosphates are partially precipitated.

37、For this process, the pH value of the raw water is kept within a range consistent with the type of flocculant used. The mixture of iron(III) hydroxide and/or aluminium hydroxide and colloids is then removed by multi-layer filtration. In this process, the adsorptively acting carbon layer in the filte

38、r removes the disinfection by-products. The filtrate is chlorinated and fed to the pool or bath. The load capacity factor, k, is 0,5 m-3equivalent to a supply water volume of 2 m3per person. 1) Obtainable from: Deutsche Gesellschaft fr das Badewesen e.V., Postfach 340201, 45074 Essen. 2)Obtainable f

39、rom: Wirtschafts- und Verlagsgesellschaft Gas und Wasser mbH, Postfach 140151, 53056 Bonn. 3) Source of supply: Bundesanstalt fr Arbeitsschutz und Arbeitsmedizin (German Federal Agency for Occupational Safety and Occupational Medicine; Internet: http:/www.baua.de). DIN 19643-2:2012-11 7 3.4 Floccula

40、tion filtration adsorption by granular activated carbon chlorination Dissolved colloidal impurities are destabilized by flocculation using iron(III) salts and/or aluminium salts, and orthophosphates are partially precipitated. For this process, the pH value of the raw water is kept within a range co

41、nsistent with the type of flocculant used. The mixture of iron(III) hydroxide and/or aluminium hydroxide and colloids is then removed by filtration. In the following stage, the disinfection by-products are adsorbed by granular activated carbon and possibly chemically converted. The filtrate is chlor

42、inated and fed to the pool or bath. The load capacity factor, k, is 0,5 m-3, equivalent to a supply water volume of 2 m3per person. 3.5 Flocculation filtration ultraviolet radiation chlorination Dissolved colloidal impurities are destabilized by flocculation using iron(III) salts and/or aluminium sa

43、lts, and orthophosphates are partially precipitated. For this process, the pH value of the raw water is kept within a range consistent with the type of flocculant used. The mixture of iron(III) hydroxide and/or aluminium hydroxide and colloids is then removed by filtration. In the following stage, c

44、hloramine compounds are eliminated by ultraviolet radiation. The filtrate is chlorinated and fed to the pool or bath. The load capacity factor, k, is 0,5 m-3, equivalent to a supply water volume of 2 m3per person. 3.6 Adsorption by powdered activated carbon filtration using precoat filters chlorinat

45、ion Disinfection by-products are adsorbed by the powdered activated carbon and possibly chemically converted. The mixture of contaminated powdered activated-carbon and other particles is then removed by filtration. The filtrate is chlorinated and fed to the pool or bath. The load capacity factor, k,

46、 is 0,5 m-3, equivalent to a supply water volume of 2 m3per person. It may be necessary to remove phosphates by suitable methods. Where the filling water has an increased phosphate concentration, it may be necessary to precipitate phosphates by flocculation filtration before feeding the water into t

47、he water tank. 4 Process stages 4.1 Acid neutralizing capacity adjustment 4.1.1 General To achieve satisfactory flocculation, the acid neutralizing capacity (KS4,3as defined in DIN 38409-7) of the raw water shall be maintained at a given minimum value, depending on the type of flocculant used. This

48、can be achieved by adding suitable filling water and/or chemicals to increase the acid neutralizing capacity. 4.1.2 Compounds used to adjust acid neutralizing capacity a) Sodium carbonate (soda) as in DIN EN 15362; b) sodium hydrogen carbonate as in DIN EN 15075; c) calcium carbonate, in solid form,

49、 as in DIN EN 15798 (to be used as filtration medium). DIN 19643-2:2012-11 8 4.1.3 Acid neutralizing capacity values a) When applying the respective process combination for bathing facilities other than spa pools (bubbling pools) (with their own treatment facility): KS4,3 0,7 mol/m3; b) when applying the respective process combination for spa pools (bubbling pools) with their own treatment facility: KS4,3