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    Flo ccula nt s fo r a ll Applicat io ns

    invo lving So lid /Liq uid Sepa ra t io n

    PRAESTOL

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    1. Introduction

    2. Mode of Action

    3. Properties

    4. Production of PRAESTOL Solutions

    5. Dosage Quantities

    6. Method of Dosage

    7. Operating Reliability and Accident Prevention

    8. Storage

    9. Packing

    10. Examples of Use and Applications of PRAESTOL Flocculants

    11. PRAESTOL

    Product Range

    11.1 Non-ionic and Anionic PRAESTOLProducts

    11.2 Cationic PRAESTOL Products

    11.3 Special Products

    12. PRAESTOLTR Grades for Processing Potable Water

    12.1 Product Range

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    Contents Page

    Ashland Deutschland GmbHEnvironmental and Process SolutionsFtingsweg 20, D-47805 KrefeldP.O. Box 10 04 52, D-47704 KrefeldPhone: +49 2151 38 3555Fax: +49 2151 38 [email protected]

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    Anionic

    Cationic

    Charge characterNon-ionic

    Supply forms

    Granulates

    Oil-free dispersions

    1. Introduction

    PRAESTOL products are organic, synthetic, high molecular flocculants based on polyacryl-

    amide.

    Non-ionic PRAESTOL flocculant types (formula 1) are technically pure polyacrylamides. Theyexhibit neutral (i. e. non-ionic) properties in aqueous solution.

    Anionic PRAESTOL flocculants (formula 2) are co-polymers of acrylamide with increasing

    proportions of acrylate groups, which give the polymers negative charges, and thus anionicac-

    tive character, in aqueous solution.

    Cationic PRAESTOL products (formula 3) are co-polymers of acrylamide with increasing

    proportions of a cationic co-monomer. The cationic groups, which are thus introduced into the

    polymer, have positive charges in aqueous solution.

    Emulsions

    PRAESTOL flocculants are available both as granular (solid) products and in liquid form as

    water-in-oil emulsions, as oil-free dispersions and as aqueous solutions.

    The granular products are white, granular, free-flowing, low-dust products with a grain size

    up to 1.2 mm.

    The water-in-oil emulsions are viscous free-flowing gel dispersions.

    The oil-free dispersions are somewhat more viscous than the water-in-oil emulsions. This higher

    viscosity does not imply any disadvantages for handling the products, i. e. the advantages of

    the liquid products (handling, ease of dosage) are preserved. The oil-free flocculants show very

    good solubility properties in water. While special attention must be given in water-in-oil emul-

    sions to the solubility properties, the so-termed reversal behavior, the oil-free dispersions

    mix with water immediately, i. e. without maturing time, and produce a ready-to-use solution

    for dosage. The ready-to-use solutions are gel-free.

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    Viscosities

    pH values

    * 1 dH = 1 (German) degree of hardness = hardness due to 10 mg of lime (CaO) in 1 l of water or 17.8 mg CaCO3in 1 l of water.

    Charge exchangeDestabilisation

    Surface potencial

    Original suspension

    Effectiveness

    Product properties =mean values

    Bulk density

    2. Mode of Action

    PRAESTOLflocculants incorporate reactive groups in aqueous solution, which have a strong

    affinity to the surfaces of suspended colloids or very fine particles in aqueous suspensions or

    slurries. According to the ionicity of the PRAESTOL types, interactions between them and the

    solid particles are based on the formation of hydrogen bonds, as is the case with the non-ionic

    polymers, or on electrostatic interactions and charge exchange, resulting in the destabilization

    of the particle surface; the anionic (= negatively charged) and cationic (= positively charged)

    PRAESTOL products act in this way. Destabilization and coagulation of a large number of

    single particles leads to the formation of voluminous macro-flocs, which are easy to separate

    from the suspension.

    Thus the optimum effect of a PRAESTOL polymer is mainly determined by the surface po-

    tential acting on the particle. These potentials are dependent both on the particle itself and on

    the conditions in the environment, i. e. on the ionic strength of the water and the properties

    resulting from this, such as pH value, electrical conductivity, hardness, surfactant content.

    The most suitable PRAESTOL type for a particular application can be easily determined by

    carrying out relatively simple preliminary tests. It is important that these tests are carried out

    on the original suspension (solids and water), under the specified operating conditions (such

    as temperature, turbulence, addition of other processing aids).

    PRAESTOL products, as polymeric flocculants, are able to flocculate solid particles, colloids,

    hydroxides and for example, bacterial substances. In the flocculated state, the solids can be

    quickly and completely separated from the surrounding water. PRAESTOL flocculants are not

    used to separate dissolved ingredients from water.

    PRAESTOL polymers are effective in the pH range 1 to 14, depending on the particular typeinvolved. They are also effective in systems with low electrolyte concentrations, right up to

    saturated salt solutions. Furthermore they cover the complete temperature range in which the

    aqueous suspension is liquid, i. e. from approx. 0 C to 100 C.

    3. Properties

    The numerical values for the product properties, which are given in the product overview tables

    are mean values, which may vary in individual cases.

    The bulk density is measured using a running out breaker. This property must be taken into

    consideration when designing storage tanks and feeding equipment for dissolving plants basedon volumetric dosage.

    Viscosities are determined with the Brookfield viscometer at 20 C. Solutions for viscosity

    measurements are prepared in distilled or de-ionized water. The viscosities quoted thus represent

    the typical value, for a particular concentration of product, which has to be considered when

    designing stirrers, pumps, measuring sections etc.

    The solutions for determining the pH value were prepared with Krefeld tap water (approx.

    25 dH*, pH value approx. 7, electrical conductivity approx. 600 S/cm). The pH values must be

    taken into account when selecting the material for dissolving and dosing equipment.

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    Molecular weights

    Ready-to-use solution /Stock solution

    Granulates

    Dispersers

    The molecular weights of the anionic products are between 6 to 30 million, whereby as a general

    rule the molecular weights of the granulates in the 23 series are in the lower range and those of

    the granulates in the 26 series are in the upper range. The molecular weights of the non-ionic

    and anionic emulsion grade polymers are in the same order of magnitude.

    The molecular weights of the cationic products are about 6 to 20 million; usually granulates of

    the 6 series are in the lower range and granulates of the 8 series as well as emulsion polymers

    in the upper range. Cationic solution polymers have a molecular weight of approx. 1 million.

    4. Production of PRAESTOLSolutions

    PRAESTOL flocculants are used in highly diluted aqueous solutions (e. g. 0.1 % by weight).

    To keep the dissolving time low, it is recommendable when producing the ready-to-use solution

    to use a concentrated stock solution (e. g. 0.5 % by weight) first, which can be diluted later to

    the required application concentration. Alternatively, the ready-to-use solution can be prepared

    immediately at the desired low concentration but a longer dissolving time must be taken into

    account here. Tested and proven dissolving equipment is available for preparing solutions. Both

    the stock and ready-to-use solutions require a maturing time, during which time the solution

    should be kept gently agitated.

    In producing aqueous solutions of PRAESTOL granulates, the following points must be

    observed:

    When adding the PRAESTOL granulates, it is important that each single particle is

    individually wetted by the water. It is therefore recommended to add the granulates

    slowly into the turbulent water.

    It is particularly recommended to use an auxiliary unit, e. g. a disperser.

    See our special information for details.

    Emulsions

    The subsequent dissolving procedure is aided by a turbulent agitation of the water

    (stirrer, compressed-air swirling).

    The dissolving time depends on the product type and on the quality and temperature

    of the solution water. It usually takes about 60 minutes for the product to develop its

    effectiveness completely. This should be taken into account when designing the dissolving units.

    The production of aqueous solutions from PRAESTOL emulsions can be done by carefully

    pouring the product into the vigorously stirred solution water or by use of special mixing units

    (in-line mixers).

    To guarantee developing of the full effectiveness of the product, sufficient time

    should be allowed for dissolving. A dissolving time of 5 to 20 minutes is sufficient,

    depending on the concentration of the solution. With increasing concentration of

    the solution the required dissolving time will decrease.

    Automatic dissolving units are used specially for the continuous, operational use

    of PRAESTOL emulsions.

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    Fig. 4:Dependence of the rate of sedimentationon the dosage quantity for suspensionswith varying solids content

    Suspension A: solids content 36 g/lSuspension B: solids content 64 g/l

    5. Dosage Quantities

    Owing to the very different flocculating properties of the sludges to be dewatered, the required

    dosing quantities can only be determined by laboratory tests or directly by carrying out plant

    trials in each individual case.

    In the case of mechanical sludge dewatering of mostly inorganic solids on rotary vacuum

    filters, centrifuges, belt presses, chamber filter presses, PRAESTOL flocculants can increase

    the output with almost completely dry cakes. The required dosing quantities lie between 80

    and 300 g/t dry substance dependent on the dewatering unit.

    In mechanical dewatering of mostly organic sludge on (heavy-duty) centrifuges, belt presses,

    chamber and membrane filter presses, cationic-active PRAESTOL flocculants are used negating

    the need for inorganic agents such as metallic salts or lime. The addition rates of polyelectrolyteare normally between 2 and 8 kg/t dry substance.

    When used to accelerate the rate of sedimentation or as a clarifying agent in settling tanks, a

    dose rate of 1 to 20 g/m3of the suspension to be clarified is normally sufficient.

    Higher dose rates may be necessary:

    Where there is a high solids content in the suspension

    With increasing fineness of the suspended solids

    Where the suspension has a low temperature

    Figure 4 shows the relative dependence of the sedimentation speed obtained with flocculationon the different solids contents of the respective suspension.

    Aqueous solutions

    Feeding and dosing

    PRAESTOLproducts in the form of aqueous solutions are diluted by stirring and mixing to

    the required concentration for use. A dissolving time is not necessary.

    Excessively fast stirrers should not be used to produce PRAESTOL stock solutions and dur-

    ing their further dilution. The stirrers maximum circumferential speed should be 10 m/s as

    otherwise the effectiveness of the highly-molecular polymer will be reduced by excessive

    shearing of the chain lengths.

    Progressive cavity pumps and not centrifugal or gear pumps should be used to feed and dose

    the PRAESTOL solutions.

    Stock solutions

    Sludge dewatering ofinorganic solids

    Organic sludge

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    Even distribution

    Type and point of dosage

    Non-corrosive

    Danger of slipping

    6. Method of Dosage

    As the dosage quantities of synthetic flocculants are low, an even distribution of the PRAESTOL

    solution in the suspension to be treated is a prerequisite for its optimum effect.

    This even distribution can be achieved by:

    Diluting the flocculant solution as much as possible

    The corresponding duration and intensity of the mixture of the flocculant solution

    with the suspension or thickened sludge

    Multiple dosage: The total quantity of flocculant solution required is added to the

    suspension to be treated at different points. In many cases, multiple dosage helps toimprove the purification of the suspension being treated.

    The advantageous type and the right point for adding the PRAESTOL solution to the suspension

    or sludge depends on the properties of the suspension, the type of clarification or dewatering

    process and the operating result required, e. g., fast rate of sedimentation, very good clarifica-

    tion, high flocculation stability.

    The following points apply:

    A type of dosage of the flocculant solution to the suspension or sludge must be

    selected which will ensure that the solution is distributed evenly.

    A dosage point must be selected which will ensure sufficient reaction time betweenthe flocculant and the solid particles to be flocculated.

    Flocs already formed should have the opportunity of uniting to form larger entities.

    On the other hand, the destruction of the flocs by means of gravitational forces,

    e. g. because of unfavorable flow conditions, should be avoided.

    7. Operating Reliability and Accident Prevention

    Our experience has shown that PRAESTOL solutions are non-corrosive in contact with materi-

    als used for tanks and pipes, such as fiberglass, plastics, plastic-lined materials and stainless

    steel.

    Owing to the properties of organic solvent in the liquid products, plastic containers (pipes,

    pump components) coming into contact with the undiluted product must be made of solvent-

    proof material.

    Scattered granular product on a wet floor, liquid product or solution which has been spilt onto

    the floor, will cause slipping.

    In this case the solid product or solution can be soaked up with absorbent material, e. g. saw-

    dust, sand etc. and disposed of.

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    Water sensitivity

    Homogenization

    Storage temperature

    8. Storage

    Highly-molecular flocculants like PRAESTOLare basically sensitive to moisture, such as

    condensation, splashes and humidity. Contact with water (droplets) can lead to local formation

    of knots and lumps. The product should therefore be stored in dry, closed containers, protected

    against moisture (bags, big bags, containers).

    After prolonged storage emulsion grade polymers might tend to separate into layers. After

    homogenization by intensive stirring, pumping or re-circulation by gas injection (nitrogen,

    air) the products may be re-used without any loss in quality.

    The storage temperature should not exceed 40 C for long periods.

    The product viscosity of emulsion grade polymers increases at low temperatures. The product

    can no longer be pumped below -10 C. After warming up to approx. 8 to 10 C and homo-

    genization, however, the product can be reused without any loss in efficiency.

    Storage stability under correct storage conditions:

    Granulates in original packing : at least 12 months

    Emulsions in original packing: at least 6 months

    Oil-free dispersions: at least 3 months

    The storability of the stock solution and ready-to-use solution depends on the individual product.

    We refer you to the corresponding PRAESTOL technical leaflet.

    9. Packing

    Granular products: Paper valve bags shrink-wrapped on pallets

    Big bag

    Liquid products: Drum

    Container

    Road tanker

    Storage stability

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    Fields of Application

    Drinking Water

    Industrial Water

    Mining (coal / ore / salts) Wash water

    Filtration of concentrates Flotation tailings Flotation pulps Acidic brines Alkaline brines

    Chemical Industry Pigments (inorganic) Pigments (organic) Leaching liquors Biotechnological suspensions

    Metal Producing and Metal Processing Industry

    Paper Industry Retention/White water and Waste water

    Waste Water (industrial, municipal) Waste water, also after neutralization

    Sludge Dewatering Raw sludge Digested sludge Surplus sludge (also thickening,

    centrifuging or flotation)

    Non-ionic

    slightly medium strongly slightly medium strongly

    Anionic Cationic

    10. Examples of Use and Applications of PRAESTOLFlocculants

    To select the optimum product for your process from our product range, please see the

    supplementary information Laboratory Tests with PRAESTOL Flocculants.

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    Polyacrylamides

    Very low residualcontent of monomeracrylamide

    1 Letter by WHO dated January 21, 19942 DWI, London: Water Industry Act 1991: Section 69

    Water Supply (Water Quality) Regulations 1989

    Water Supply (Water Quality) (Amendment) Regulations 19913 DIN EN 1407 and EN 14104 DWI, London: Regulation 25 Letter 2/2002 of November 7, 2002

    12. PRAESTOLTR Grades for Processing Potable Water

    The synthetic polyelectrolytes which are now increasingly used in the preparation of potable

    water are mainly water-soluble polyacrylamides.

    A prerequisite for the use of polyacrylamides for this purpose is that they should have a very

    low residual content of monomer acrylamide.

    The World Health Organization (WHO) recommends limiting the amount of monomer acryl-

    amide in drinking water to less than 0.5 g/l. Thus, in consideration of all safety measures

    in a daily consumption of 2 liters of drinking water the total amount of monomer acrylamide

    should not exceed 0.017 mg per kilogram of body weight per day.1

    A residual monomer content of 0.05 % by weight (500 ppm) and a dosage of 1 mg/l (1 ppm), as

    prescribed by the Food and Drug Administration (FDA) for the USA (CFR 40, 141.111), are

    already within this limit.

    Regulations in other countries reflect these requirements:

    Germany

    In Germany the use of PRAESTOL TR grades for the preparation of potable water is controlled

    under the Foodstuffs, Consumer Goods and Animal Feed Code (Lebensmittel-, Bedarfsgegen-

    stnde- und Futtermittelgesetzbuch, LFGB). The LFGB requires that with appropriate use of

    auxiliary agents in the processing of potable water these agents must, except for technically

    unavoidable and technologically inactive residues, be removed from the potable water. Whenproperly used, the PRAESTOL TR grades meet these requirements, which are set out in the

    LFGB.

    In keeping with 11 of the 2001 Drinking Water Act, approved conditioning agents appear

    on a list published by the Federal Ministry of Health and Social Security (Bundesministerium

    fr Gesundheit und Soziale Sicherung, BMGS). Only anionic and non-ionic grades with a

    residual monomer content of below 0.025 % at a polymer dosage of 0.4 mg/l (DIN EN 1407)

    are approved for use.

    Great Britain

    As of December 2003, the amount of monomer acrylamide may not exceed 0.02 %. The

    quantity of the polymer dosed may not exceed 0.5 mg/l.2,3,4

    European Union

    The standards EN 1407 and EN 1410 were adopted by CEN (European Standards Committee)

    on March 23, 1998. They prescribe polyacrylamide for conditioning potable water with a re-

    sidual monomer content of less than 0.025 % acrylamide with a polymer dosage not to exceed

    0.4 mg/l. Both standards are also valid for Germany.

    These standards, as well as those for Germany and Great Britain, are in compliance with EU

    guidelines 98/83/EG concerning the quality of water for human consumption (EU Drinking

    Water Guideline, limit: 0.1g/l in the drinking water).

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    International certifyingorganizations

    USA

    Certification is awarded by the National Sanitation Foundation International (NSF) and con-

    forms to the requirements of Standard 60 Drinking Water Treatment Chemicals - Health

    Effects. A residual monomer content of < 0.05 % by weight at a dosage of not more than

    1 mg/l is prescribed.

    USA: National Sanitation Foundation International (NSF),Ann Arbor, Michigan

    GB: Department for Environment, Food and Rural Affairs,Drinking Water Inspectorate (DWI)London

    Approved for use are polymers which comply with the standards

    DIN EN 1407 and EN 1410. Packaging is appropriately labeled.5

    PRAESTOLTR Grades

    PRAESTOL TR grades are produced using a special method and every production batch is very

    carefully monitored with regard to the residual content of monomer acrylamide.

    For every consignment of our PRAESTOL TR product types we guarantee a residual monomer

    content of < 0.02 % (by weight) of monomer acrylamide (with reference to the polymer).

    On special request we can supply the relevant certificate of analysis with every consignment

    of PRAESTOL TR flocculants.

    The following institutes have issued certificates declaring the PRAESTOL TR grades (shown

    in the table)to be safe for use in potable water preparation:

    National Sanitation Foundation International, USA

    ANSI/NSF Standard 60 Drinking Water Treatment Chemicals - Health Effects

    All anionic and cationic PRAESTOL TR flocculant types are certified.

    Department for Environment, Food and Rural Affairs,

    Drinking Water Inspectorate, Great Britain All anionic and cationic PRAESTOL TR flocculants types have been approved

    for use in conditioning drinking water.

    Federal Ministry of Health and Social Security, Germany

    Approval for anionic and non-ionic PRAESTOL TR flocculant types.

    Further fields of application for PRAESTOL TR flocculants for water treatment are lime water

    production, water works sludge treatment and phosphate removal.

    5 DWI, London: Regulation 25 Letter 11/2000 of September 29, 2000

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    2500 TR non- 650 200 50 7 1 - 7 USAionic Great Britain

    Germany

    2515 TR weakly 650 3000 400 7 7 - 10 USA anionic Great Britain Germany

    2530 TR medium 700 4000 500 7 6 - 10 USA 2540 TR anionic 700 5500 600 7 6 - 13 Great Britain

    Germany

    650 TR medium 650 700 65 7 1 - 14 USAcationic Great Britain

    851 TR weakly 650 600 50 7 1 - 14 USA

    cationic Great Britain

    DW = De-ionized water

    TW = Krefeld tap water: approx. 25 dH (German) degree of hardness, electrical conductivity approx. 600 S/cm, pH value approx. 7

    12.1 Product Range

    PRAESTOLTR Grades for Processing Potable Water

    PRAESTOL Ionic Bulk Viscosity pH Effective in Approved inCharge Density the pH Range

    0.5 % by wt. 0.1 % by wt. 0.1 % by wt.DW DW TW

    approx. approx. approx. approx. kg/m3 mPa.s mPa.s

    All statements, information and data presented herein are believed to be accurate and reliable but are not to betaken as a guarantee, express warranty or implied warranty of merchantability or fitness for a particular purpose,

    or representation, express or implied, for which seller assumes legal responsibility, and they are offered solely

    for your consideration, investigation and verification. Statements or suggestions concerning possible use of this

    product are made without representation or warranty that any such use is free of patent infringement and are not

    recommendations to infringe on any patent.

    Ashland Deutschland GmbHEnvironmental and Process SolutionsFtingsweg 20, D-47805 KrefeldP.O. Box 10 04 52, D-47704 KrefeldPhone: +49 2151 38 3555Fax: +49 2151 38 [email protected]

    egisteredtrademark,

    Ashland|

    2006,Ashland|December2006,V01


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