Abstract:
It is intended to provide a chromium (III)-containing aqueous solution which has widely adjustable molar ratios of various acid radicals to Cr and is useful as a source of trivalent chromium or a supplementary source of trivalent chromium for the bath in the surface treatment of various metals. Specifically, the chromium (III)-containing aqueous solution is characterized by containing a complex chromium (III) salt which is produced by performing chromic acid reduction reaction in the simultaneous or sequential presence of two or more acids selected from an inorganic acid other than chromic acid and an organic acid. Furthermore, it is intended to provide a process for producing a chromium (III)-containing aqueous solution by performing chromic acid reduction reaction by the contact of chromic acid with an acid other than chromic acid and/or an organic reducing agent in a water solvent, characterized in that the chromic acid reduction reaction is performed in the simultaneous or sequential presence of at least two or more acids selected as the acid other than chromic acid from an inorganic acid and an organic acid.
Abstract:
The chromium (III) carbonate of the present invention exhibits a light blue color in a solid state. This chromium (III) carbonate has an L* value of 50 to 70, an a* value of −4 to −2, and a b* value of −10 to −7, which are represented by the L*a*b* color system (JIS Z8729). This chromium (III) carbonate is preferably completely dissolved within 30 minutes when the chromium (III) carbonate is added, in an amount corresponding to a Cr content of 1 g, to 1 liter of an aqueous solution of hydrochloric acid having a pH of 0.2 at a temperature of 25° C. This chromium (III) carbonate is preferably obtained by contacting an aqueous solution of carbonate and an aqueous solution containing trivalent chromium at a pH of 6 to 12 under the condition of a reaction liquid temperature of 0° C. or more and less than 50° C. Also, preferably, after production of the chromium (III) carbonate, filtration is performed, and the chromium (III) carbonate is washed with water until the conductivity of the filtrate is 5 mS/cm or less.
Abstract translation:本发明的碳酸铬(III)表现出固态的浅蓝色。 该碳酸铬(III)的L *值为50〜70,a *值为-4〜-2,ab *为-10〜-7,由L * a * b *颜色 系统(JIS Z8729)。 当碳酸铬(III)以相当于Cr含量的1g的量添加碳酸铬(III)至1升pH为0.2的盐酸水溶液时,优选在30分钟内完全溶解该碳酸铬(III) 该温度为25℃。这种碳酸铬(III)优选通过在反应液温度为0℃的条件下使碳酸盐水溶液和含有三价铬的水溶液在6至12的pH下接触 以上且小于50℃。此外,优选在碳酸铬(III)的制造之后,进行过滤,并用水洗涤碳酸铬(III),直至滤液的电导率为5mS / cm 或更少。
Abstract:
In a method for manufacturing chromium hydroxide according to the present invention, chromium hydroxide having higher solubility in an acidic aqueous solution than chromium hydroxide obtained by conventional manufacturing methods can be obtained. The method is characterized by simultaneously adding an aqueous solution of an inorganic alkali and an aqueous solution containing trivalent chromium to an aqueous medium under the condition of a reaction liquid temperature of 0° C. or more and less than 50° C. to produce chromium hydroxide. The pH of the reaction liquid while the aqueous solution containing trivalent chromium and the aqueous solution of the inorganic alkali are added is preferably maintained in the range of 7.0 to 12.
Abstract:
The chromium (III) carbonate of the present invention exhibits a light blue color in a solid state. This chromium (III) carbonate has an L* value of 50 to 70, an a* value of −4 to −2, and a b* value of −10 to −7, which are represented by the L*a*b* color system (JIS Z8729). This chromium (III) carbonate is preferably completely dissolved within 30 minutes when the chromium (III) carbonate is added, in an amount corresponding to a Cr content of 1 g, to 1 liter of an aqueous solution of hydrochloric acid having a pH of 0.2 at a temperature of 25° C. This chromium (III) carbonate is preferably obtained by contacting an aqueous solution of carbonate and an aqueous solution containing trivalent chromium at a pH of 6 to 12 under the condition of a reaction liquid temperature of 0° C. or more and less than 50° C. Also, preferably, after production of the chromium (III) carbonate, filtration is performed, and the chromium (III) carbonate is washed with water until the conductivity of the filtrate is 5 mS/cm or less.
Abstract translation:本发明的碳酸铬(III)表现出固态的浅蓝色。 该碳酸铬(III)的L *值为50〜70,a *值为-4〜-2,ab *为-10〜-7,由L * a * b *颜色 系统(JIS Z8729)。 当碳酸铬(III)以相当于Cr含量的1g的量添加碳酸铬(III)至1升pH为0.2的盐酸水溶液时,优选在30分钟内完全溶解该碳酸铬(III) 该温度为25℃。这种碳酸铬(III)优选通过在反应液温度为0℃的条件下使碳酸盐水溶液和含有三价铬的水溶液在6至12的pH下接触 以上且小于50℃。此外,优选在碳酸铬(III)的制造之后,进行过滤,并用水洗涤碳酸铬(III),直至滤液的电导率为5mS / cm 或更少。
Abstract:
A press working control method for controlling the press working operation of a press having a pressure cylinder for applying a working pressure to a workpiece, a press slide operatively connected to the pressure cylinder and carrying a movable die, a bed fixedly mounted with a fixed die, a plurality of control cylinders supporting the press slide in a level position during the press working operation, and a press control system for carrying out the press working control method. The press control system comprises a first pressure detector for detecting the operative pressure of the pressure cylinder, quick-response control valves each for regulating the height of the control cylinder, height detectors each for detecting the height of the control cylinder, second pressure detectors each for detecting the operative pressure of the control cylinder, servovalves each for detecting the operative pressure of the control cylinder, and a control unit including a computer for deciding manipulated variables for the height and operative pressure control of the control cylinders on the basis of data obtained by the detectors. The respective heights of the control cylinders are regulated individually so that the press slide is maintained in a level position during the press working operation, while the respective operative pressure of the control cylinders are regulated so that a desired working pressure is applied to the workpiece.