会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明申请
    • GRANULAR FERTILIZER WITH CONTROLLED RELEASE OF NUTRIENTS
    • 控制释放营养物质的粒状肥料
    • WO2011146027A4
    • 2012-03-15
    • PCT/SK2011050007
    • 2011-05-16
    • DUSLO ASKOVACIK JANHERENCSAROVA GABRIELATOKAR ZDENKOKRALIK MILANFERENCI MICHALKERDO PAVOL
    • KOVACIK JANHERENCSAROVA GABRIELATOKAR ZDENKOKRALIK MILANFERENCI MICHALKERDO PAVOL
    • C05G3/00C05G1/00
    • C05G3/0029
    • Granular fertilizer with controlled release of nutrients can be prepared by coating the fertilizer granules with a mixture of epoxide resin with low molecular weight between 100 and 400 in the amount of 50 to 85 % w/w, imidazole derivative in the amount of 1 to 20 % w/w and modified vegetable oil in the amount of 10 to 30 % w/w. The epoxide resin with low molecular weight between 100 and 400 is preferably bisphenol A diglycidyl ether with epoxide equivalent of 182-192 g/mol, imidazole derivative is preferably 2-ethyl-4-methylimidazole and modified vegetable oil is preferably methylester of rape oil. The coating mixture contains preferably 77.3 % w/w of epoxide resin, 3.4 % w/w of imidazole derivative and 19.3 % w/w of methylester of rape oil, and the fertilizer is coated by gradual spraying of 3 to 20 doses of the coating mixture, wherein the coating is performed in the rotary cylindrical container or fluid apparatus at the temperature of 60 to 120 °C, preferably 105 to 115 °C. The layer of coating mixture makes 6 to 25 % w/w of the overall weight of the coated granule.
    • 具有控制释放营养素的颗粒肥料可以通过用含量为50至85%w / w的低分子量100至400的环氧树脂和1至20的咪唑衍生物 %w / w和10-30%w / w量的改性植物油。 低分子量为100-400的环氧树脂优选环氧当量为182-192g / mol的双酚A二缩水甘油醚,咪唑衍生物优选为2-乙基-4-甲基咪唑,改性植物油优选为菜油的甲酯。 涂料混合物优选包含77.3%w / w的环氧树脂,3.4%w / w的咪唑衍生物和19.3%w / w的菜油甲酯,并且通过逐渐喷涂3至20个剂量的涂料 其中涂层在旋转圆柱形容器或流体装置中在60至120℃,优选105至115℃的温度下进行。 涂层混合物层占涂层颗粒总重量的6-25%w / w。
    • 6. 发明申请
    • GRANULATED FERTILIZER CONTAINING WATER SOLUBLE FORMS OF NITROGEN, MAGNESIUM AND SULPHUR, AND METHOD OF ITS PREPARATION
    • 含有氮,镁和硫的水溶性形式的颗粒肥料及其制备方法
    • WO2008013510A8
    • 2008-07-03
    • PCT/SK2007050017
    • 2007-07-25
    • DUSLO ASLENCSES LADISLAVKRALIK MILANLEHOCKY PETERSTEFANCOVA RADKAKERDO PAVOLFERENCI MICHALPOLAK ANTON
    • LENCSES LADISLAVKRALIK MILANLEHOCKY PETERSTEFANCOVA RADKAKERDO PAVOLFERENCI MICHALPOLAK ANTON
    • C05C1/00C05C3/00C05D5/00C05D9/00
    • C01C1/18C01C1/24C01F5/40C05C1/00C05C3/00C05D5/00C05G3/0058
    • Granulated fertilizer, containing water soluble forms of nitrogen, magnesium and sulphur, contains 15 to 30 % by weight of nitrogen, 1 to 18 % by weight of sulphur, 2 to 10 % by weight of magnesium, expressed as magnesium oxide MgO, in the form of boussingaultite - (NH 4 ) 2 SO 4 .MgSO 4 .6H 2 O and binary salts ammonium nitrate - 2NH 4 NO 3 .(NH 4 ) 2 SO 4 and 3NH 4 NO 3 .(NH 4 ) 2 SO 4 , wherein the content of boussingaultite in the fertilizer is 40 to 45 % by weight. Magnesite is treated with concentrated nitric acid containing 30 to 80 % of HNO 3 at a temperature of 60 °C to 130 °C, under formation of reaction mixture containing magnesium nitrate, calcium nitrate, or possibly, according to the content of metallic compounds in magnesite, nitrates of iron, manganese and further metallic elements, and the remainder of undecomposed magnesite, the reaction mixture is subseguently neutralized with an alkaline agent to pH of 3 to 7.5, the neutralized reaction mixture is subseguently left to react with ammonium sulphate at a temperature of 80 to 130 °C for 20 to 80 minutes under formation of a slurry of boussingaultite (NH 4 ) 2 SO 4 -MgSO 4 .6H 2 O, containing 10 to 30 % by weight of water, which slurry is mixed with dried recycle from the preceding production in the ratio of 1 :2 to 1 :10 and it is granulated under formation of wet granulate, from which, after removing free water, the final product is obtained.
    • 含有水溶性形式的氮,镁和硫的颗粒肥料含有​​15至30重量%的氮,1至18重量%的硫,2至10重量%的镁,以氧化镁MgO表示,在 硫酸钠的形式 - (NH 4)2 SO 4 SO 4,4 H 2, (NH 4)2 SO 2和二元盐硝酸铵 - 2NH 4 NO 3(NH 4)2 SO 3 (NH 4)2 SO 3(SO 4)2 SO 3(SO 4)3 SO 3 其中肥料中膨润土的含量为40〜45重量%。 在60℃至130℃的温度下,在含有30至80%HNO 3的浓硝酸中处理菱镁矿,形成含有硝酸镁,硝酸钙的反应混合物,或者根据 对于菱镁矿中的金属化合物,铁,锰和其他金属元素的硝酸盐和未分解的菱镁矿的剩余部分,将反应混合物用碱性试剂中性以至pH3至7.5,中和的反应混合物随后残留 在80至130℃的温度下与硫酸铵反应20至80分钟,形成膨润土(NH 3)2 SO 4的浆液 含有10-30%(重量)水的浆液与上述生产中的干燥再循环混合,比例为1:0.5%-MgSO4 为1:2至1:10,并在湿颗粒形成时造粒,从中除去游离水后,最终产品 ct。
    • 7. 发明申请
    • METHOD OF DIPHENYLAMINE PRODUCTION FROM ANILINE CATALYZED BY FLUOROBORATES
    • 由氟虫腈催化的苯胺生产二苯胺的方法
    • WO2009011665A1
    • 2009-01-22
    • PCT/SK2008/050012
    • 2008-07-11
    • DUSLO, A.S.UHLAR, JanKRALIK, MilanANDRUSKOVA, VieraHORAK, JaroslavSEITZ, OtoMRLLAK, Jozef
    • UHLAR, JanKRALIK, MilanANDRUSKOVA, VieraHORAK, JaroslavSEITZ, OtoMRLLAK, Jozef
    • C07C209/64C07C211/55
    • C07C209/64C07C211/55
    • The invention concerns a method of diphenylamine production from aniline by a continuous procedure in liquid phase catalysed by thermolabile compounds of fluorine with boron which convert under conditions of diphenylamine formation from aniline to NH 4 BF 4 . NH 4 BF 4 crystals arising in the reaction medium of the reactor are maintained in uplift during a time,which is at least so long as the dwell time of aniline in the reactor. The maintaining in uplift is ensured by circulation stirring of the reaction mixture with a stirrer of minimum volume-rate of 0.1-multiple ofthe reaction mixture volume per hourand it is realized by mechanical stirring providing turbulent axial-radial flow of the reaction mixture in the reactor. An input overheated water steam is supplied countercurrentlyto the catalyst into the reactor withpressure higher than the sum of saturated vapour tension of the reaction mixture at the working temperature and hydrostatic pressure of the reaction mixture. Aninput reactant aniline is supplied into the reactor countercurrently to the catalyst input with such speed which ensures at least the same residence time of the catalyst in uplift as is the residence time of aniline in the reactor.
    • 本发明涉及一种由苯胺生产二苯胺的方法,该方法是通过氟与硼的热不稳定化合物在由二苯胺形成的苯胺转化为NH4BF4的条件下催化的液相中连续进行的。 在反应器的反应介质中产生的NH4BF4晶体在一段时间内保持升高,其至少等于苯胺在反应器中的停留时间。 通过循环搅拌反应混合物,用搅拌器循环搅拌,保证反应混合物的最小体积速率为每小时反应混合物体积的0.1倍,并通过机械搅拌实现反应混合物在反应器中的湍流轴向 - 径向流动 。 输入过热水蒸汽逆流向催化剂供给反应器,其压力高于反应混合物在工作温度和反应混合物的静水压力下的饱和蒸汽张力的总和。 将输入反应物苯胺以这样的速度与催化剂输入端逆流供应到反应器中,这确保了催化剂在提升中的停留时间至少相同于苯胺在反应器中的停留时间。
    • 8. 发明申请
    • GRANULAR FERTILIZER WITH CONTROLLED RELEASE OF NUTRIENTS
    • 颗粒肥料与营养素的控制释放
    • WO2011146027A3
    • 2012-01-19
    • PCT/SK2011050007
    • 2011-05-16
    • DUSLO ASKOVACIK JANHERENCSAROVA GABRIELATOKAR ZDENKOKRALIK MILANFERENCI MICHALKERDO PAVOL
    • KOVACIK JANHERENCSAROVA GABRIELATOKAR ZDENKOKRALIK MILANFERENCI MICHALKERDO PAVOL
    • C05G3/00C05G1/00
    • C05G3/0029
    • Granular fertilizer with controlled release of nutrients can be prepared by coating the fertilizer granules with a mixture of epoxide resin with low molecular weight between 100 and 400 in the amount of 50 to 85 % w/w, imidazole derivative in the amount of 1 to 20 % w/w and modified vegetable oil in the amount of 10 to 30 % w/w. The epoxide resin with low molecular weight between 100 and 400 is preferably bisphenol A diglycidyl ether with epoxide equivalent of 182-192 g/mol, imidazole derivative is preferably 2-ethyl-4-methylimidazole and modified vegetable oil is preferably methylester of rape oil. The coating mixture contains preferably 77.3 % w/w of epoxide resin, 3.4 % w/w of imidazole derivative and 19.3 % w/w of methylester of rape oil, and the fertilizer is coated by gradual spraying of 3 to 20 doses of the coating mixture, wherein the coating is performed in the rotary cylindrical container or fluid apparatus at the temperature of 60 to 120 °C, preferably 105 to 115 °C. The layer of coating mixture makes 6 to 25 % w/w of the overall weight of the coated granule.
    • 可以通过用50至85%w / w的量的100至400的低分子量环氧树脂的混合物涂覆肥料颗粒来制备具有受控释放营养物质的颗粒肥料,量为1至20的咪唑衍生物 %w / w和10-30%w / w的改性植物油。 低分子量为100〜400的环氧化物树脂优选为环氧当量为182〜92g / mol的双酚A二缩水甘油醚,咪唑衍生物优选为2-乙基-4-甲基咪唑,改性植物油优选为油菜油的甲酯。 涂料混合物优选含有77.3%w / w的环氧树脂,3.4%w / w的咪唑衍生物和19.3%w / w的油菜油的甲酯,并且通过逐渐喷洒3至20剂的涂层来涂覆肥料 混合物,其中涂层在旋转圆柱形容器或流体装置中在60至120℃,优选105至115℃的温度下进行。 涂层混合物层的涂层颗粒总重量为6〜25%w / w。
    • 9. 发明申请
    • GRANULAR FERTILIZER WITH CONTROLLED RELEASE OF NUTRIENTS
    • 颗粒肥料与营养素的控制释放
    • WO2011146027A2
    • 2011-11-24
    • PCT/SK2011/050007
    • 2011-05-16
    • DUSLO, A.S.KOVACIK, JanHERENCSAROVA, GabrielaTOKAR, ZdenkoKRALIK, MilanFERENCI, MichalKERDO, Pavol
    • KOVACIK, JanHERENCSAROVA, GabrielaTOKAR, ZdenkoKRALIK, MilanFERENCI, MichalKERDO, Pavol
    • C05G3/0029
    • Granular fertilizer with controlled release of nutrients can be prepared by coating the fertilizer granules with a mixture of epoxide resin with low molecular weight between 100 and 400 in the amount of 50 to 85 % w/w, imidazole derivative in the amount of 1 to 20 % w/w and modified vegetable oil in the amount of 10 to 30 % w/w. The epoxide resin with low molecular weight between 100 and 400 is preferably bisphenol A diglycidyl ether with epoxide equivalent of 182-192 g/mol, imidazole derivative is preferably 2-ethyl-4-methylimidazole and modified vegetable oil is preferably methylester of rape oil. The coating mixture contains preferably 77.3 % w/w of epoxide resin, 3.4 % w/w of imidazole derivative and 19.3 % w/w of methylester of rape oil, and the fertilizer is coated by gradual spraying of 3 to 20 doses of the coating mixture, wherein the coating is performed in the rotary cylindrical container or fluid apparatus at the temperature of 60 to 120 °C, preferably 105 to 115 °C. The layer of coating mixture makes 6 to 25 % w/w of the overall weight of the coated granule.
    • 可以通过用50至85%w / w的量的100至400的低分子量环氧树脂的混合物涂覆肥料颗粒来制备具有受控释放营养物质的颗粒肥料,量为1至20的咪唑衍生物 %w / w和10-30%w / w的改性植物油。 低分子量为100〜400的环氧化物树脂优选为环氧当量为182〜92g / mol的双酚A二缩水甘油醚,咪唑衍生物优选为2-乙基-4-甲基咪唑,改性植物油优选为油菜油的甲酯。 涂料混合物优选含有77.3%w / w的环氧树脂,3.4%w / w的咪唑衍生物和19.3%w / w的油菜油的甲酯,并且通过逐渐喷洒3至20剂的涂层来涂覆肥料 混合物,其中涂层在旋转圆柱形容器或流体装置中在60至120℃,优选105至115℃的温度下进行。 涂层混合物层的涂层颗粒总重量为6〜25%w / w。