Title of Invention

A PROCESS FOR THE PREPARATION OF THE PARTIALLY HYDROPHOBIC PRECIPITATED SILICA

Abstract

The present invention relates to a process for the preparation of the partially hydrophobic precipitated silica, characterised in that, to obtain the desired degree of water-repellence, the requisite amount of water-repellent agent such as si1icone oil is mixed using high shearing forces with precipitated silica suspension prepared using a known process according to a given ratio with very short residence time and low pH value, filtering off the water-repellent agent-containing precipitated silica suspension and washing this free of salt, drying the precipitated silica filter cake homogeneously mixed with water-repellent agent using a known process, providing thermic post-treatment or tempering and then carrying out mechanical or radiation milling.

Full Text

-1A- The invention relates to partially hydrophobic silicas, a process for their preparation, their use as carrier for hydrolysis-sensitive active substances and their use in defoaming agents. The use of hydrophobic silicas in a hydrophobic-liquid for the preparation of a defoaming agent is known (DE-C 2829906); US-A 4377 493; DE-C 3411 759; US-A 4344 858; Kalman Koczo et al., Journal of Colloid and Interface Science 166, 225-238 (1994), WO 95/05880). Known defoaming agents consist of a mixture of non-polar oils and hydrophobic particles. The solids content is typically 1-20%. These mixtures are more effective defoaming agents than the oil or the hydrophobic particles alone. Defoaming agents are used in the textile, paper, paint, coating and detergent industries. Known crop protection agents are substantially used in the form of wettable powders, as dust concentrates, dispersible granulates or as emulsifiable concentrates. Known wettable powders (WP) consist of the following components: Pesticide active substance, carrier, dispersing and wetting agents as well as optionally additional additives. Thorough premixing of these constituents is followed by coarse milling succeeded by fine milling. Use is in the form of an aqueous spray. Known dust concentrates consist solely of activesubstance and filler. Formulation is by analogy with the formulation of wettable powders. Fine milling is, however, often omitted. The dust are applied as dust (DP) after blending with mineral fillers such as kaolin, talcum or dolomite. 950112 2 Known dispersible granulates (WG) are solid formulations consisting of pesticide active substance, carrier, dispersing and wetting agent as well as optionally other additives. This mixture is finely milled and then granulated using known methods. Use takes the form of aqueous sprays. Known emulsifiable concentrates (EC) are liquid and contain- solvent-containing constituents. Attempts are made to replace the emulsifiable concentrates by solid formulations to avoid solvents that can pose a burden to the environment. The use of hydrophilic precipitated silica as carrier in the preparation of crop protection agents, pest control agents or concentrated cattle feedstuffs is known (DE-B 16 19 865). The silicas conventionally used have a high oil uptake and a high absorption capacity. The reduced storage stability of the active substances is, however, a disadvantage in the use of the known precipitated hydrophilic silicas in the preparation of agents containing active substances that are sensitive to hydrolysis. This applies in particular to active substances used in crop protection which could hitherto only be further processed as emulsifiable concentrates because of their sensitivity to hydrolysis. Known hydrophobic precipitated silicas, such as for example the precipitated silicas according to DE 26 28975 C2, DE-C 27 29 244, DE-A 24 35 860, EP-A 492 124, DE-A 25 13 608, are fully hydrophobised and therefore have the disadvantage of needing a large amount of wetting agent in the formulation. It is therefore an object to provide a carrier for, in particular, hydrolysis-sensitive active substances, such as crop protection agents or feedstuffs as well as active 950112 Degussa 3 substances from the chemical industry which ensures a longer storage stability of the active substance. When defoaming agents are used, the known silica has the disadvantage that this silica sediments out when the defoaming agent is stored for longer periods, in particular with the use of low-viscous oils and a low solids content. The defoaming activity deteriorates because of sedimentation of the known silica. Moreover, the sedimented silica also has to be stirred up again in a laborious process before the defoaming agent is used. To prevent a tendency to sedimentation, it may be necessary to add a dispersing agent to the defoaming mixture, such as for example a pyrogenic silica, as well as the known silica (Degussa Technical Bulletin Pigments No. 42, page 11). This necessitates a change in the defoaming formulation which, in turn, necessitates further testing, makes the product more expensive and means an additional process step to work in the dispersing agent. It is, for example, known from DE 28 29 906 C3 that the defoaming active substances may be prepared in such a manner as to achieve a high dispersion stability by adding to a mixture of a defoaming oil and an emulsifier first the hydrophobic and then the requisite amount of hydrophilic silica, with further stirring. The instant invention has the advantage over this in that the silica can be stirred into a defoaming oil in one process step and then dispersed, thereby obtaining a stable defoaming dispersion without an additional process step. The object of the invention is a partially hydrophobic precipitated silica which is characterised by a methanol wettability of 10 to 49 %. The precipitated silica of the invention may have a DBP-uptake (dried substance) of greater than 250g/100g (DBP number) and optionally a mean particle size of 1-12 µm. 4 The partially hydrophobic precipitated silica of the invention can have a carbon content of 0.3 to 1.85 %, preferably of 0.5 to 1.5 % and/or a pH value of 5.5 to 10 and/or a loss on drying of 2.6 to 10 %, preferably of 3 to 6 %. In particular, the partially hydrophobic precipitated silica of the invention can have one or several of the following physical chemical characteristic values: Surface (BET), m2/g 75 - 250 Tamped density, g/l 70 - 150' (DIN ISO 787/11) Loss on drying 2h/105°C,% 2.6 - 10.0 (DIN ISO 787/2) Loss at red heat related to 2h/105°C 2.5 - 7.5 dried substance, % (DIN ISO 3262/11) pH value, 5 % (methanol-aqueous soln.) 5.5 - 10 (DIN ISO 787/9) Conductivity (methanol-aqueous soln.) (µS/cm) DBP uptake, dried substance, g/l00g > 250 Methanol wettability, titrated, % 10-49 Mean particle size, Coulter counter, µm 1-12 Carbon content, % 0.3-1.85 SiO2, % (DIN ISO 3262/19) > 98 The silica may be a precipitated silica which has been treated with a water-repellent agent after its production and/or also during its production in order to obtain the above-described characteristics. Precipitated silicas are known from Ullmanns Enzyklopadie der technischen Chemie, 4th edition, volume 21, pages 458 to 473 (1988) . 950112 Degussa 5 The production of fully hydrophobic silicas is, for example, known from DE 44 19 234 Al, DE-C 27 29 244, DE 26 28 975 C2 and DE-OS 21 07 082. DE 26 28 975 C2 and DE-C 27 29 244 relate to fully hydrophobic precipitated silicas. The two other patent specifications or Unexamined German publications relate to fully hydrophobic and partially hydrophobic, pyrogenic silicas with different physical chemical characteristics that are not identical with the characteristics of the precipitated silica of the invention. The use of fully hydrophobic pyrogenic silicas for dusting onto pesticide granulates is described in DE 29 28 585 Al, the use of pyrogenic silicas as additive in active substance formulations is explained in EP 0 111 112 Al. The partially hydrophobic precipitated silica of the invention can consist of 85 to 98 % by weight of precipitated silica and 15 to 2 % by weight of water-repellent agent (silicon oil that can have a carbon content of 32.4 %). To obtain the desired degree of water-repellence, it can be prepared by mixing the requisite amount of water-repellent agent using high shearing forces with precipitated silica suspension prepared using a known process according to a given ratio with very short residence time and low pH value, filtering off the water-repellent agent-containing precipitated silica suspension and washing this free of salt, drying the precipitated silica filter cake homogeneously mixed with water-repellent agent using a known process, providing thermic post-treatment or tempering and then carrying out mechanical or radiation milling. It is, in particular, possible to mix silicon oil homogeneously using high shearing energy with precipitated silica suspension produced using known processes, with or without addition of phase transmitters (e.g. wetting agents, emulsifiers). 950112 6 The continuous shearing device that may be used may be an Ultra-Turrax, a Kothoff-Mischsirene or a Rheinhütte mixer. The precipitated silica suspension homogeneously mixed with water-repellent agent is then separated using known filtration apparatuses (e.g. chamber filtration press, rotary filter) and the solid matter containing water-repellent agent is washed free of salt. In so doing, the water-repellent agent is entirely taken up by the precipitated silica filter cake. The_filtrates_yielded are no longer contaminated with organosilicon compounds, with the result that the measured TOC contents are The precipitated silica suspensions used in the mixing process and the water-repellent agent are characterised by the following physical chemical material data: 950112 Degussa Precipitated silica A (the substance data relate to a filtered, washed and dried precipitated silica sample, without added water-repellent agent): BET surface according to DIN 66131 150±50 [m2/g] Mean size of primary particles from 15-25 [nm] EM photos Loss on drying according to DIN 55921 2.5-4.5 [%] after 2 h at 105°C Loss at red heat (related to the substance 3+0.5 [%] dried for 2 h at 105°C according to DIN 55921) pH value (in 5% aqueous dispersion 3.5-6.5 according to DIN 53200) Conductivity (in 4% aqueous dispersion) SO3 content (related to the substance 0.3 [%] dried for 2h at 105°C according to DIN 55921) Na2O content (related to the substance dried 0.3 [%] for 2h at 105°C according to DIN 55921) 950112 8 Precipitated silica B (the substance data relate to a filtered, washed and dried precipitated silica, without added water-repellent agent): BET surface according to DIN 66131 300±50 [m2/g] Mean size of primary particles from 10-15 [nm] EM photos Loss on drying according to DIN 55921 2.5-4.5[%J after 2 h at 105°C Loss at red heat (related to the substance 3±0.5 [%] dried for 2h at 105°C according to DIN 55921) pH value (in 5% aqueous dispersion 3.5-6.5 according to DIN 53200) Conductivity (in 4% aqueous dispersion) SO3 content (related to the substance dried Na2O content (related to the substance dried For hydrophobizing it is, in particular, possible to use silicon oil, consisting of dimethylpoly siloxanes with a viscosity of 20 to 1000 mPas, preferably with 50 mPas as water-repellent agents. It is also possible to use: R2R'Si, where R=CH3O-, C2H5o-, Cl-, R'=CH3-, C2H5-, HMDS (hexamethyl disilazane), D4 (octamethyl tetrasiloxane), D6, D8, R3Si-CnH2n+1', where n=l-18, R=CH3O-, C2H5O-, C3H7_O-, Cl-, in particular Si 108 (trimethoxyocty1 silane), Si 116, polymethyl siloxanes, polymethyl siloxane emulsions, (trimethyloxyhexadecyl silane), aminopropyl silanes, vinyl silanes, methacrylic silanes. 950112 Degussa 9 The resultant precipitated silica filter cake homogeneously mixed with water-repellent agent is dried in the subsequent process step in known drying aggregates, The drying aggregate for drying the water-repellent agent-containing filter cake can be a band dryer or spin-flash dryer. To achieve the desired degree of water-repellence, the dry product containing water-repellent agent is subjected to thermic post-treatment at 300°C to 400°C, preferably 350°C for 30 to 60 minutes in a discontinuous, electrically heated stirrer container or in a continuous electrically heated double screw reactor thermicly treated or tempered and then milled mechanically or using jet mills. Compared with the above-described preparation comparable in principle with known processes, the partially hydrophobic precipitated silica of the invention can in particular be prepared according to the following process of wet water-repellence which cannot be deduced from the state of the art: A mass stream of 0.424 kg/h polymethyl siloxane is added using a continuous mixer with high shearing energy input to a mass stream of 160 kg/h of an aqueous precipitated silica suspension with a solids content of 85 g/l, that was prepared using known manufacturing processes, while maintaining a pH value of 3, the temperature of the two components to be mixed being 25 ± 5°C. In so doing, the residence time in the mixer may not exceed 5 seconds. The command reference input for the coating process is taken to be the dimensionless coating index Bi which describes the ratio to one another of the active substance portions of the two mass streams to be mixed. A coating index of 32 is needed to achieve the hydrophobic property of the precipitated silica of the invention. The precipitated silica coated with silicone oil is then separated using known processes without using a subsequent 950112 - Degussa 10 post-reaction time, washed almost free of electrolyte, dried at 105°C, tempered for 1.0 hour at 370°C and then milled. It has been found that the silica of the invention can be prepared in the mixer due in particular to the low pH value and the short residence time in the mixer. Methanol wettability, which is a measure of the water-repellence, is determined as follows: 1. Basic principles Silicas, the surfaces of which are modified with non-hydrolysable organic groups, are generally not wettened with water. These hydrophobic silicas can, however, be wetted using a methanol/water mixture. The proportion of methanol in this mixture - expressed in percent by weight - is a measure of the water-repellence of the modified silica. The higher the proportion of methanol, the better the substance is hydrophobised. 2. Apparatus and reagents A 20 ml measuring pipette with graduation of scale A 250 ml separating funnel Methanol p.a. 3. Method 200 mg of the hydrophobic silica and 50 ml water are added to a 250 ml separating funnel. The silica remains on the surface of the water. The tip of the measuring pipette filled with methanol is then immersed in the liquid phase (to prevent direct contact between the silica and the pure methanol) and the methanol is allowed to run in slowly. In so doing, the separating funnel is shaken with a circular movement of the hand so that a vortex arises in the 11 liquid. Methanol is added until the solid substance is wetted. This is the case when a) the silica is no longer distributed over the entire surface of the liquid phase (already containing methanol) and the relatively clear, film-free liquid becomes visible. b) the silica film forming over the phase limiting surface at the wall of the separating funnel disappears. c) moist silica agglomerates remain adhering to the wall of the separating filter on shaking. 4. Calculation Methanol wettability is given in % by weight methanol of the methanol/water mixture according to the formula: Methanol wettability = 0.79 x .100 0.79 + 50 x = methanol consumption in ml In this method, methanol consumption can differ by 2 ml with the same person and the same sample. DBP uptake (DBP-number which is a measure of the absorbency of the precipitated silica, is determined as follows: 1. Basic principles The dibutylphthalate number is determined using a Brabender plastograph. The DBP number is a measure of the liquid absorbency or absorption capacity of a product in powder form. Absorption capacity depends on moisture content, on granulation and initial weight of the material investigated. 950112 Degussa 12 2. Apparatus and reagents Brabender plastograph with plotter Multi-Dosimat E 415 (50 1) manufactured by Metrohm Dibutylphthalate 3. Method 12.5 g silica are added to the kneader of the Brabender plastograph. Dibutylphthalate flows into the mixture at a speed of 4 ml/minute with constant mixing (revolution speed- of the kneader paddles 125 rpm). Power consumption is low during mixing. Towards the end of the determination the mixture becomes poorly flowing. This fact is documented by a rise in power consumption which is shown on a scale. Addition of DBP is automatically discontinued at a scale reading of 300. 4. Calculation The density of DBP is 1.047 g/ml. ml DBP.1.047 100 % by weight DBP uptake = 12.5 The DBP uptake is related to the anhydrous, dried substance. When using precxpitated silicas with higher moisture contents, the value must be corrected using the correction table if these precipitated silicas are not dried before determining the DBP number. Use of the correction table can lead to clear deviations compared to a determination of dried precipitated silicas. Correction table for dibutylphthalate uptake - anhydrous - 950112 Degussa 13 (Add correction values corresponding to the water content to the value obtained) % Water ? ? ,0 ,2 ,4 ,6 ,8 % Dibutylphthalate 0 0 2 4 5 7 1 9 10 12 13 15 2 16 18 19 20 22 3 23 24 26 27 28 4 28 29 29 30 31 5 31 32 32 33 33 6 34 34 35 35 36 7 36 37 38 38 39 8 39 40 40 41 41 9 42 43 43 44 44 10 45 45 46 46 47 950112 Degussa 14 DBP uptake Initial weight 12.5 g F = 8.376 ml DBP consumption ? ? ,0 ,1 ,2 ,3 ,4 ,6 ,1 ,9 % DBP uptake 15 126 126 127 128 129 130 131 132 132 133 16 134 135 136 137 137 138 139 140 141 142 17 142 143 144 145 146 147 147 148 149 150 18 151 152 152 153 154 155 156 157 157 158 19 159 160 161 162 162 163 164 165 166 167 20 168 168 169 170 171 172 173 173 174 175 21 176 177 178 178 179 180 181 182 183 183 22 184 185 186 187 188 188 189 190 191 192 23 193 193 194 195 196 197 198 199 199 200 24 201 202 203 204 204 205 206 207 208 209 25 209 210 211 212 213 214 214 215 216 217 26 218 219 219 220 221 222 223 224 224 225 27 226 227 228 229 230 230 231 232 233 234 28 235 235 236 237 238 239 240 240 241 242 29 243 244 245 245 246 247 248 249 250 250 30 251 252 253 254 255 255 256 257 258 259 31 260 260 261 262 263 264 265 266 266 267 32 268 269 270 271 271 272 273 274 275 276 33 276 277 278 279 280 281 281 282 283 284 34 285 286 286 287 288 289 290 291 291 292 35 293 294 295 296 297 297 298 299 300 301 36 302 302 303 304 305 306 307 307 308 309 37 310 311 312 312 313 314 315 316 317 317 38 318 319 320 321 322 322 323 324 325 326 39 327 327 328 329 330 331 332 333 333 334 40 335 336 337 338 338 339 340 341 342 343 41 343 344 345 346 347 348 348 349 350 351 42 352 353 353 354 355 356 357 358 358 359 43 360 361 362 363 364 364 365 366 367 368 44 369 369 370 371 372 373 374 374 375 376 45 377 378 379 379 380 381 382 383 384 384 Determining the particle size (Coulter counter) Application; The determination of particle size (charac-teristic particle size curve) of silicas using the Coulter counter occurs in an aqueous electrolyte solution (isotone II). Determination method: 950112 Degussa . 15 The beakers (2 per count), the magnet and the pipette tips are blown dust-free in a stream of nitrogen at 5-6 bar. The beakers are then inverted on dust-free lens paper, the magnet and the pipette tips being placed into a petri dish that has also been blown out. 0.100 g of the substance to be examined are weighed on an analytical balance and transferred to the beaker. The magnet is added, first moistened with a little isotonic solution and then filled up to the 60 ml mark with isotone. The suspension is then stirred with the magnetic stirrer for 1/2 minute at setting 3 (scale 1-10). The beaker is then suspended in the ultrasonic bath and sonicated for exactly 1 minute. In so doing, care must be taken to ensure that the depth of immersion in the distilled water of the ultrasonic bath reaches exactly to the 60 ml marking of the beaker. After sonication, the beaker is replaced on the magnetic stirrer and a sample of the suspension is removed using the automatic pipette during stirring (setting 3 again). The total amount removed should be used for the count. If a little less suspension is needed, less suspension should be drawn into the tip of the pipette. The second 100 ml beaker is filled with isotone II solution, placed on the beaker platform and the capillary (100 µm) and the stirrer immersed. The stirrer is set to a moderate speed. Solutions and apparatus; 100 ml beakers Automatic pipette - Pipetman manufactured by Gilson Plastic pipette tips Magnetic stirrer and magnet (length 3 mm) Ultrasonic bath: Bandelin, Sonorex RK 102 Analytical balance Dust-free lens paper Nitrogen bottle with drying device and nozzle 950112 Degussa 16 Petri dish Stopwatch Grain analysis paper Isotone II solution Coulter counter model TA II The silica of the invention can be used to manufacture crop protection agents with active substances sensitive to hydrolysis. In so doing it is possible to manufacture wettable powders or water-dispersible granulates which can be used in water soluble foil bags in outer cardboard packagings. This achieves advantages during transport, with hazardous substance classification, with savings in wasted packaging and the cost reductions associated therewith. The silica of the invention can, in particular, be used when making use of active substances of the group of phosphoric acid esters (malathion, diazinone, etc.). The form of application of every other active substance may be formulated by analogy. The active substance formulations prepared using the silica of the invention, such as for example crop protection agents have the additional advantage of long active substance storage stability. Storage of 50WP malathion and active substance stability Preparation as 50WP malathion: A premix is first prepared in the ratio 1 : 1 using Wessalon S and the wetting agent Ampholak XIO. 28 g of the partially hydrophobic precipitated silicas as well as Wessalon S as comparison substance are briefly fluidised in a 500 ml Quickfit stirring apparatus. 52.1 g malathion (96 %) are then gradually added dropwise before adding 6 g of the premix as well as 3.0 g Empikol LZ/P dispersing 950112 Degussa 17 agent. 10.9 g filler (Rollokalk) are subsequently mixed therewith and the mixture is homogenised using a Turbula mixer. The samples are stabilised by storing them for 4 days at room temperature. The initial values of CIPAC suspension and the malathion contents are then determined according to CIPAC. The initial values of malathion according to WHO and isomalathion according to WHO are also determined after 4 days and the samples then stored at 54°C and measured after 7 days, 14 days, 28 days and 56 days. Testing suspension according to CIPAC-12/3/(M) 1 before and after storage at 54°C: This method is a spectroanalytical process with UV as light source. Malathion reacts/hydrolyses with alkali in Na-00-dimethyldithiophosphate and is converted with Cu/Fe solution into a yellow copper complex and measured at 420 µm. The influence of wetting agent on malathion release is presumably great in the case of this method. Testing malathion content according to WHO/SIF/10.R5 using gas chromatography before and after storage at 54°C: The method is based on separation of a substance mixture through substance-specific distribution between stationary phase (column) and a stream of carrier gas which lead to different speeds/retention times. In this method, there is an extraction equilibrium between solvent and silica during detachment of the malathion from the silica that may possibly favour the hydrophobic silica types. The wetting agent presumably exerts hardly any influence. Testing isomalathion content after WHO/SIF/10.R5 using HPLC before and after storage at 54°C: To determine the isomalathion content, 0.6 g 50WP malathion are weighed in and mixed with 65 % aqueous 950112 18 acetonitrile solution for 30 minutes. The sample is measured against a reference solution after centrifugation and filtration. With this method there is also an extraction equilibrium between solvent and silica that may possibly favour the hydrophobic silica. The wetting agent presumably exerts hardly any influence. Storage of 1:1 malathion concentrates and active substance stability The active substance solution (96%) is applied to the partially hydrophobic carrier in a ratio of 1:1. This mixture is then tested for storage stability. The values obtained in this manner are exclusively attributable to the effect of the carrier. The tests employed in the examples section are described as: Malathion 1:1 formulation 28 g malathion (96%) are added dropwise within 30 minutes to 28 g carrier and then post-stirred for 3 minutes and mixed at a medium setting in a Turbula mixer for 5 minutes. It is striking that the mixtures are markedly drier compared to the previously formulated 50WP malathion (28 g hydrophobic carrier + 52.1 g malathion + residual formulation constituents). Testing malathion content according to CIPAC 12/3 (MI)l by means of UV/VIS before and after storage at 54°C: Storage by analogy with 50WP malathion. Testing malathion content according to WHO/SIF/10.R5 by means of GC before and after storage at 54°C: Storage by analogy with 50WP malathion. 19 Table 1 Precipitated silica Methanol wettability titrated % pH Surface m2/g DBP uptake, original material g/l00g DBP uptake, anhydrous g/l00g Carbon % Mean particle size Coulter Counter µm Standard (Wessalon S) - 6.3 182 240 272 0.05 8.2 Silica No. 1 (comparison) 43 7.5 121 291 297 2.4 7.7 Silica No. 2 (comparison) 48 7.8 189 260 282 2.3 5.3 Silica No. 3 20 7.8 209 259 283 1.6 5.3 Silica No. 4 28 7.3 94 233 250 1.0 11.8 Standard (Sipernat D10) 62 9.4 113 n. c. n. c. 2.9 4.3 Silica No. 5 49 6.9 150 226 257 0.5 7.4 Silica No. 6 49 7.7 160 235 265 0.9 3.5 Precipitated silica Tamped density g/1 Loss on drying % Loss at red heat % Conduc-tivity µS/cm Sieve residue Mocker >45 µm % S1O2 % Na2O % Fe2O3 ppm Sulfate as SO3 % Standard (Wessalon S) 107 5.3 4.4 710 0.06 n.c. n. c. n.c. n.c. Silica No. 1 (comparison) 152 0.7 n.c. n. c. n. c. n.c. n.c. n.c. n.c. Silica No. 2 (comparison) 139 2.8 n.c. n.c. n. c. n.c. n.c. n.c. n.c. Silica No. 3 122 3.2 3.8 62 0.02 99.5 0.15 315 0.03 Silica No. 4 125 4.9 2.8 124 0.02 99.1 0.20 347 0.08 Standard (Sipernat D10) 106 2.8 6.2 330 n.c. n. c. n.c. n.c. n.c. Silica No. 5 133 5.0 3.9 390 0.04 98.8 0.68 346 0.8 Silica No. 6 96 4.7 4.3 380 n.c. = not calculated 20 Table 2 Trial results (use as carrier) Results of the technical application and active substance examination results of 50 WP malathion Standard (Wessalon S) Precipitated silica No. 1* Precipitated silica No. 2* Precipitated silica No. 3 After 4 days AT (C) in % 94.2 ± 0.45 87.9 ± 0.46 91.0 ± 1.30 94.0 ± 0.80 at RT ZFE (M2) in % 54.3 50.5 52.7 49.8 (Initial w.) (M) in % 49.3 ± 0.65 50.0 48.8 49.0 (I) in % After 7 days' AT (C) in % 85.9 ± 0.90 89.6 ± 1.51 88.3 ± 0.78 92.3 ± 0.56 storage ZFE (M2) in % 45.1 41.2 45.4 45.3 at 54°C (M) in % 49.6 47.6 47.0 48.5 (I) in % 0.65 0.79 0.47 0.56 After 14 days' AT (C) in % 86.4 ± 0.34 89.2 ± 3.11 87.4 ± 1.70 93.3 ± 0.46 storage ZFE (M2) in % 37.6 45.2 46.3 43.8 at 54°C (M) in % 47.0 ± 0.53 48.8 45.1 46.5 (I) in % 0.97 ± 0.03 1.39 0.93 0.99 After 28 days' AT (C) in % 87.4 ± 1.22 81.4 ± 0.78 81.9 ± 2.99 84.2 ± 2.35 storage ZFE (M2) in % 40.9 42.6 44.7 44.3 at 54°C (M) in % 45.9 47.9 45.7 45.1 (I) in % 1.06 1.23 0.98 0.98 After 56 days' AT (C) in % 90.2 ± 4.53 74.2 ± 3.20 75.5 ± 4.17 77.0 ± 2.25 storage ZFE (M2) in % 30.5 34.7 40.0 36.1 at 54°C (M) in % 44.0 46.0 40.7 42.9 (I) in % 1.94 2.70 1.66 2.16 *Comparative example Table 3 Deviations. absolute in % 21 (initial value - measured value) after storage at 54°C of the 50WP malathion ?Comparative example 22 Table 4 Active substance analytical examination results of the 1 1 malathion concentrates Standard (Wessalon S) Precipitated silica No. 3 Precipitated silica No. 1* Precipitated silica No. 5 Precipitated silica No.4 Initial RT ZFE (M, ZFE (M2, value GC) UV) 1 day in % in % 48.4 ± 1.33 44.8 49.2 ± 0.27 55.4 52.3 ± 2.39 47.1 46.8 ± 1.28 46.1 48.9 ± 0.09 50.7 After 7 ZFE (M, ZFE (M2, days GC) UV) 54°C in % in % 46.1 ± 0.98 40.7 48.5 ± 0.27 45.6 46.8 ± 1.12 41.7 46.2 ± 1.11 41.7 57.1 ± 0.76 51.2 After 14 ZFE (M, ZFE (M2, days GC) UV) 54°C in % in % 43.8 ± 0.81 40,5 48.3 ± 0.86 42.8 48.1 ± 0.40 47.6 46.1 ± 5.68 38.7 55.1 47.7 After 29 ZFE (M, ZFE (M2, days GC) UV) 54°C in % in % 40.6 ± 2.44 36.1 46.7 ± 0.26 45.4 46.9 ± 1.25 41.1 43.5 ± 0.34 35.2 51.3 ± 0.5 38.9 After 56 ZFE (M, ZFE (M2, days GC) UV) 54°C in % in % 34.3 ± 1.60 34.5 44.9 ± 0.45 41.9 44.3 ± 0.32 43.9 39.7 ± 1.17 33.3 - ZFE (M, GC) = Malathion content according to WHO using GC ZFE (M2, UV) = Malathion content according to CIPAC using UV/VIS AT (C) = CIPAC suspension power ZFE (M) = Malathion content according to WHO using GC ZFE (M2) = Malathion content according to CIPAC using UV/VIS (M) = Malathion content according to WHO using GC (I) = Isomalathion content according to WHO using HPLC ?Comparative example 950112 Degussa 23 The possible influences of, for example, wetting agents on the accuracy of measurements should be considered when evaluating the results of the Fischer suspension power and of the malathion contents and the isomalathion contents of the 50WP malathion. The process error when determining the malathion content according to CIPAC using UV/VIS is given as ± 5 % malathion. A double determination that shows a standard deviation of 0.7 % is carried out on one sample after 14 days. The malathion contents according to WHO show a standard deviation between 0.1 and 0.7 %. The standard deviation of the isomalathion contents, with two double determinations in the total series of measurements, is 0 to 0.03 %. The results of the active substance stability are shown graphically in Figures 1 to 5. The trials show that the active substance stability can be increased by using the partially hydrophobic precipitated silicas of the invention and that wetting and dispersing agents can be economised on, for example, in crop protection formulations in comparison to known fully hydrophobic precipitated silicas. Preparation of the defoaming dispersions To prepare the 5 % defoaming dispersions 57 g of the corresponding oil, for example Shell Risella G 118 (now Shell Risella G 18), viscosity 40cSt., are prepared in 250 ml beakers, 3 g of the silica of the invention or of Sipernat D10 are then added and carefully stirred together. Dispersing then occurs using an Ultra Turrax T50 at 10000 rpm for 5 minutes. Degussa 24 Stability testing of the defoaming dispersions For this purpose the still hot dispersions are filled into 100 ml glass cylinders, stored in a vibration-free location at room temperature and any possible phase separation recorded at regular time intervals (value in ml clear oil phase). Trial result fuse in defoaming agents Defoamer dispersion 1 month 3 months clear oil phase[ml]% KS6 M 0 0 KS6 S 0 0 D10 M 60 60 D10 S 27 50 KS6 M = silica No. 6 in mineral oil KS6 S = silica No. 6 in silicone oil D10 M = Sipernat D10 in mineral oil D10 S = Sipernat D10 in silicone oil Figures 6 and 7 Figures 6 and 7 show that the precipitated silica of the invention, worked into mineral oil and silicone oil, shows no phase separation at all after 3 months. A considerable phase separation is already encountered with the known Sipernat D10 both used oils after just one month. Defoaming testing using latex 950112 Degussa 25 160 g latex are weighed into a stainless steel beaker and foamed up for 3 minutes using a Hamilton-Beach-Scovill mixer in switch setting L (lowest stirrer speed: approx. 4000 rpm) after adding 0.3 g defoaming agent. The weight of 100 ml of this foam is determined by differential weighing in a stainless steel measuring cylinder. A high latex weight (almost 100 g) indicates a good defoaming capacity of the corresponding sample. The mean values are determined from at least two single determinations. A Hamilton-Beach-Scovill mixer is a milkshake mixer normally put to household use which can be set at three stirrer speeds (L, M and H). The switch setting "L" means approx. 4000 rpm. The substance to be stirred up is stirred up using a paddle stirrer with moveable "paddles". Experimental result fuse in defoaming agents) Batches: Latex weight g/100 ml Mean value/standard deviation 1 KS6 M 71 / 0.5 2 KS6 S 89 / 0.3 3 D10 M 78 / 0.2 4 D10 S 90/0.3 Blank value 53 / 0.9 KS6 M = silica No. 6 in mineral oil KS6 S = silica No. 6 in silicone oil D10 M = Sipernat D10 in mineral oil D10 S = Sipernat D10 in silicone oil 950112 Degussa 26 Formula for calculating foam content in % after performing the latex test: 100 g-weighed latex weight [g] after adding defoaming agent* X100 100 g weighed blank value*2[g] *1; differential weighing after adding the corresponding defoaming agent for latex dispersion and subsequent stirring for three minutes *2; differential weighing after stirring the latex dispersion for three minutes without adding defoaming agent Figure 8 Figure 8 shows that while the precipitated silica of the invention displays a marginally lower defoaming effect than Sipernat D10 in mineral oil, this result must not necessarily continue in subsequent technical application tests, but that the stability is far better than with Sipernat D10. In silicone oil, the precipitated silica of the invention displays an identical defoaming effect to Sipernat D10. The investigations conducted show that the stability of a defoaming dispersion can be substantially improved using the partially hydrophobic precipitated silica of the invention, whereas the defoaming effect is comparable with a known fully hydrophobic precipitated silica. German priority application 196 12 501.4 is relied on and incorporated herein by reference. 28 28 WE CLAIM: 1. A process for the preparation of the partially hydrophobic precipitated silica characterised in that, to obtain the desired degree of water-repellence, the requisite amount of water-repellent agent such as silicone oil is mixed using high shearing forces with precipitated silica suspension prepared using a known process according to a given ratio with very short residence time and low pH value, filtering off the water-repellent agent-containing precipitated silica suspension and washing this free of salt, drying the precipitated silica filter cake homogeneously mixed with water-repellent agent using a known process, providing thermic post-treatment or tempering and then carrying out mechanical or radiation mi11ing. 2. A process as claimed in claim 1 wherein said partially hydrophobic precipitated silica has a methanol wettability of 10- 49%. 3. A process as claimed in claim 2 wherein said partially hydrophobic precipitated silica has a DBP uptake (dried substance) of greater than 230 g/100 g 4. A process as claimed in claim 1 wherein said partially hydrophobic precipitated silica has a mean particle size of 1 to 12 µm. 5. A process as claimed in claim 1 wherein said partially hydrophobic precipitated silica has a carbon content of 0.3 to 1.85%. 191463 29 6. A process as claimed in claim 5 wherein said partially hydrophobic precipitated silica has a loss on drying of 2.6 to 10%. 7. A process as claimed in claim 6 wherein said partially hydrophobic precipitated silica has a pH of 5.5 to 10, 8. A process as claimed in claim 3 wherein said partially hydrophobic precipitated silica has a carbon content of 0-3 to 1.85%. 9. A process as claimed in claim 8 wherein said partially hydrophobic precipitated silica has a with a loss on drying of 2.6 to 10%- 10. A process as claimed in claim 9 wherein said partially hydrophobic precipitated silica has a pH value of 5-5 to 10- 11. A process as claimed in claim 4 wherein said partially hydrophobic precipitated silica has a carbon content of 0-3 to 1.85%. 12. A process as claimed in claim 11 wherein said partially hydrophobic precipitated silica has a loss on drying of 2.6 to 10%. 13. A process as claimed in claim 12 wherein said partially hydrophobic precipitated silica has a pH value of 5-5 to 10.

Documents:

00475-cal-1997-abstract.pdf

00475-cal-1997-claims.pdf

00475-cal-1997-correspondence.pdf

00475-cal-1997-description(complete).pdf

00475-cal-1997-drawings.pdf

00475-cal-1997-form-1.pdf

00475-cal-1997-form-2.pdf

00475-cal-1997-form-3.pdf

00475-cal-1997-form-5.pdf

00475-cal-1997-letters patent.pdf

00475-cal-1997-pa.pdf

00475-cal-1997-priority document.pdf