摘要:
A cylindrical support and centering device for a sensitive viscometer comprises a hollow cylindrical support member open at opposite ends. The viscometer is supported on the upper end with its cylindrical pivot housing slip-fitted into the upper end in snug contact with an inner cylindrical surface of the support. The pivot housing either rests against an annular stop surface formed below the cylindrical surface or is supported by contact of the viscometer with the upper end. The lower end of the support is dimensioned to snugly engage the outer cylindrical surface of the stator so that the longitudinal axis of the stator is coaxial with the longitudinal axis of the rotor for precise centering.
摘要:
There is disclosed a method for upgrading of hydrocarbon mixtures, so as to reduce their content of gum precursors such as diolefins and pseudo-diolefins, and provide a resulting product mixture suitable for mild hydrogenation, for use as a motor fuel or as a feed stock to an extraction unit. The process comprises obtaining a hydrocarbon mixture containing about 60-90 wt. % of aromatic components, about 3-40 wt. % of dienes and pseudodienes, and monoolefins, and up to about 6 wt. % of relatively unreactive organic compounds, reacting this mixture with elemental sulfur in the approximate weight ratio of about 5-95 wt. % of the hydrocarbon mixture with about 95-5 wt. % of elemental sulfur, the reaction being carried out at a temperature in the range of 100.degree.-150.degree. C. for about 10 minutes to 24 hours with good mixing, removing the unreacted materials by distillation and separating a sulfur-hydrocarbon reaction product to provide the upgraded hydrocarbon mixture.
摘要:
Phosphate is upgraded to remove slimes therefrom by a process which comprises the steps of:(a) contacting the phosphate ore with a phosphoric acid solution having a concentration of about 1 to 20 weight percent in a desliming unit for a sufficient time to form a suspension containing the slimes and the calcium and phosphate components;(b) passing said suspension through a solids separator to separate deslimed phosphate ore from the slime suspension and recovering the deslimed phosphate ore;(c) removing the slime suspension to a separator to separate the slime solids from the filtrate liquids; and(d) recycling the filtrate liquids to the desliming unit to provide at least a portion of the phosphoric acid solution.
摘要:
A novel sulfur-based adduct formed by reacting sulfur with a diene-containing by-product hydrocarbon mixture available from petrochemical operations and/or from coal processing. The adduct is a reaction product of sulfur and each of the dienes contained in the by-product mixture. Also disclosed is a road surface composition containing this adduct as an asphalt extender or as a replacement for asphalt, and there are also disclosed other compositions containing this adduct such as sulfur cements, sulfur concretes, coatings, foams, structural materials and insulators.
摘要:
Alkali metal sulfates are produced from an aqueous solution containing alkali metal hydrogen sulfate which comprises contacting the aqueous solution of alkali metal hydrogen sulfate with a hydrophilic solvent, the hydrophilic solvent being effective to extract at least a portion of the sulfuric acid formed as the alkali metal hydrogen sulfate is converted to alkali metal sulfate in the solution, together with at least a portion of the water present; permitting the alkali metal sulfate solid to crystallize; and recovering the solid alkali metal sulfate product. The hydrophilic solvent may then be extracted and separated from the sulfuric acid with a hydrophobic solvent and both solvents can be recovered and recycled.
摘要:
Substantially fluoride-free phosphoric acid is produced by the acidulation of phosphate rock with sulfuric acid wherein the acidulation reaction is conducted in the presence of added potassium as K.sub.2 O bearing compounds, e.g. KHSO.sub.4, K.sub.2 SO.sub.4, KH.sub.2 PO.sub.4 or KOH, and additional silica, to precipitate fluorides and silica as potassium silicofluoride and then removed on separation of the gypsum formed. Optionally, additional silica may be added to the phosphoric acid solution recovered after precipitation and removal of the gypsum, to precipitate additional fluoride as potassium silicofluoride to further purify the phosphoric acid. In a further embodiment sufficient potassium may be added along with additional silica in the acidulation step to produce potassium dihydrogen phosphate and phosphoric acid as additional products. The phosphoric acid and potassium dihydrogen phosphate are recovered substantially free from fluoride contamination and the reaction is carried out in the substantial absence of fluorine evolution into the atmosphere. Also disclosed is a process for conducting a conventional phosphoric acid facility to produce phosphoric acid and gypsum wherein defluorination of the phosphoric acid recovered is achieved by silicon dioxide and K.sub.2 O addition and the fluorides are removed from the system, the process including steps for production of pure phosphoric acid and potassium dihydrogen phosphate.
摘要翻译:通过用硫酸酸化磷酸盐岩产生基本上不含氟化物的磷酸,其中酸化反应在加入的K 2存在下作为带有K2O的化合物,例如, KHSO 4,K 2 SO 4,KH 2 PO 4或KOH和另外的二氧化硅,以氟硅酸钠和二氧化硅的形式沉淀,然后在形成的石膏分离后除去。 任选地,可以在沉淀和除去石膏之后回收的磷酸溶液中加入另外的二氧化硅,以沉淀另外的氟化硅作为氟硅酸钾以进一步纯化磷酸。 在进一步的实施方案中,在酸化步骤中可以连同另外的二氧化硅一起加入足量的钾,以产生磷酸二氢钾和磷酸作为附加产物。 基本上没有氟化物污染物回收磷酸和磷酸二氢钾,并且基本上没有氟进入大气中进行反应。 还公开了一种用于进行常规磷酸设备来生产磷酸和石膏的方法,其中通过二氧化硅和K 2 O添加实现回收的磷酸的脱氟,并且从体系中除去氟化物,该方法包括生产纯的 磷酸和磷酸二氢钾。
摘要:
Monocalcium phosphate, phosphoric acid and/or potassium phosphate containing fertilizers are produced in a process involving acidulation of phosphate rock with phophoric acid in the presence of added silicon dioxide and potassium ion whereby fluorides contained in the rock are converted to K.sub.2 SiF.sub.6, wherein monocalcium phosphate dissolved in phosphoric acid is formed during acidulation. In an important feature, the K.sub.2 SiF.sub.6 is separated and hydrolyzed to regenerate the K.sub.2 O from K.sub.2 SiF.sub.6 as recycled KH.sub.2 PO.sub.4 /H.sub.3 PO.sub.4 solution for further reaction with fluoride from fresh phosphate rock feed. A portion of the MCP/H.sub.3 PO.sub.4 solution and/or crystallized monocalcium phosphate can then be reacted with potassium sulfate, potassium bisulfate, or mixtures thereof, to form KH.sub.2 PO.sub.4, or KH.sub.2 PO.sub.4 /H.sub.3 PO.sub.4 solutions, and gypsum. In a closely related embodiment, the remaining MCP/H.sub.3 PO.sub.4 solution is reacted with sulfuric acid to produce phosphoric acid product and/or the recycle phosphoric acid required in the phosphate rock acidulation step.
摘要翻译:磷酸二钙,磷酸和/或磷酸钾的肥料是在添加二氧化硅和钾离子的存在下,用磷酸酸化磷酸盐岩的方法生产的,由此将岩石中所含的氟化物转化为K 2 SiF 6,其中磷酸一钙溶解 在酸化期间形成磷酸。 在一个重要的特征中,K2SiF6被分离并水解,从K2SiF6中再生K2O,作为循环的KH 2 PO 4 / H 3 PO 4溶液,与来自新鲜磷酸盐岩石料的氟化物进一步反应。 然后可以将一部分MCP / H 3 PO 4溶液和/或结晶的一磷酸钙与硫酸钾,硫酸氢钾或其混合物反应,以形成KH 2 PO 4或KH 2 PO 4 / H 3 PO 4溶液和石膏。 在紧密相关的实施方案中,剩余的MCP / H 3 PO 4溶液与硫酸反应以产生磷酸盐酸化步骤中所需的磷酸产物和/或再循环磷酸。
摘要:
Substantially fluoride-free phosphoric acid is produced by the acidulation of phosphate rock with sulfuric acid wherein the acidulation reaction is conducted in the presence of added potassium as K.sub.2 O bearing compounds, e.g. KHSO.sub.4, K.sub.2 SO.sub.4, KH.sub.2 PO.sub.4 or KOH, and additional silica, to precipitate fluorides and silica as potassium silicofluoride and then removed on separation of the gypsum formed. Optionally, additional silica may be added to the phosphoric acid solution recovered after precipitation and removal of the gypsum, to precipitate additional fluoride as potassium silicofluoride to further purify the phosphoric acid. In a further embodiment sufficient potassium may be added along with additional silica in the acidulation step to produce potassium dihydrogen phosphate and phosphoric acid as additional products. The phosphoric acid and potassium dihydrogen phosphate are recovered substantially free from fluoride contamination and the reaction is carried out in the substantial absence of fluorine evolution into the atmosphere. Also disclosed is a process for conducting aconventional phosphoric acid facility to produce phosphoric acid and gypsum wherein defluorination of the phosphoric acid recovered is achieved by silicon dioxide and K.sub.2 O addition and the fluorides are removed from the system, the process including steps for production of pure phosphoric acid and potassium dihydrogen phosphate.
摘要翻译:通过用硫酸酸化磷酸盐岩产生基本上不含氟化物的磷酸,其中酸化反应在加入的K 2存在下作为带有K2O的化合物,例如, KHSO 4,K 2 SO 4,KH 2 PO 4或KOH和另外的二氧化硅,以氟硅酸钠和二氧化硅的形式沉淀,然后在形成的石膏分离后除去。 任选地,可以在沉淀和除去石膏之后回收的磷酸溶液中加入另外的二氧化硅,以沉淀另外的氟化硅作为氟硅酸钾以进一步纯化磷酸。 在进一步的实施方案中,在酸化步骤中可以连同另外的二氧化硅一起加入足量的钾,以产生磷酸二氢钾和磷酸作为附加产物。 基本上没有氟化物污染物回收磷酸和磷酸二氢钾,并且基本上没有氟进入大气中进行反应。 还公开了一种用于进行常规磷酸设备以生产磷酸和石膏的方法,其中通过二氧化硅和K 2 O添加实现回收的磷酸的脱氟,并且从体系中除去氟化物,该方法包括生产纯磷酸的步骤 酸和磷酸二氢钾。
摘要:
In a process for the reaction of phosphate rock and sulfuric acid in the presence of potassium ion to form a mixture of phosphoric acid and a precipitated gypsum wherein the presence of the potassium ion causes precipitation of fluorides from the phosphate rock as potassium silicofluoride as a coprecipitate with the gypsum, and the phosphoric acid is separated from the gypsum slurry, the potassium silicofluoride is separated from the gypsum by extraction with phosphoric acid which may contain from 0-25 weight percent of sulfuric acid based on the amount of gypsum to be extracted or such phosphoric acid which may contain some fluorine. This extraction procedure provides a substantially fluoride-free gypsum product and an extraction solution containing recoverable potassium silicofluoride.
摘要:
Potassium sulfate (K.sub.2 SO.sub.4) is prepared by reaction of potassium chloride and sulfuric acid in an aqueous medium by initially removing evolved HCl in the gaseous form at temperatures of about 65.degree.-120.degree. C., then removing the remaining HCl as an HCl/water azeotrope at temperatures of about 90.degree. to 110.degree. C., restoring to the reaction mixture the amount of water removed with the azeotrope, and permitting the potassium sulfate to crystallize from the solution.
摘要翻译:通过氯化钾和硫酸在水性介质中的反应制备硫酸钾(K 2 SO 4),首先在约65-120℃的温度下,以气态形式去除放出的HCl,然后以HCl /水的形式除去剩余的HCl 共沸物,在约90℃至110℃的温度下,向反应混合物中恢复用共沸物除去的水量,并允许硫酸钾从溶液中结晶。