80results about How to "Meet high-end needs" patented technology

The invention discloses a production method of a corrosion-resistant aluminum alloy profile. The corrosion-resistant aluminum alloy profile comprises, by mass percent, 3%-8% of Cu, 2%-5% of Fe, 5%-9% of Mn, 1%-2% of Mg, 1%-2% of Zn, 0.3%-0.8% of Si, 0.1% of Ni, 0.05% of Ti and the balance Al. The materials are smelted for 6-8 hours at high temperature to obtain molten aluminum alloy; horizontal continuous casting is carried out on the obtained molten aluminum alloy and cleaning is conducted; the aluminum alloy profile is obtained through continuous extruding and forming; second-stage aging heat treatment is carried out on the obtained aluminum alloy profile, and a finished corrosion-resistant aluminum alloy profile product is obtained. The alloy production process is simplified and the alloy production period is shortened without homogenization and pre-heating treatment, and the energy-saving and environment-friendly production requirements of a short-process technology are completely met. Besides, the manufactured aluminum alloy profile has excellent corrosion resistance and tensile strength and can meet high-end requirements increasing day by day.

The invention relates to a synthesis method of isopropanolamine. The synthesis method comprises the following steps: (1) liquid ammonia and water are mixed to form ammonia water which is mixed with propylene oxide; mixed solution is preheated until the temperature reaches 120 to 125 DEG C, and the inputting molar ratio of the ammonia and the propylene oxide is controlled within 10 to 15; (2) the materiel after preheating is delivered into a reactor, the reaction temperature ranges from 128 to 138 DEG C, the pressure ranges from 12.6 to 13.8MPa, and the reaction time ranges from 1.5 to 3 hours; (3) the surplus unreacted ammonia is separated from the obtained mixture after the reaction by using a flash distillation column, the pressure in the flash distillation column ranges from 0.6 to 1.6MPa, and the temperature of a column kettle ranges from 140 to 160 DEG C; (4) the mixture which is separated through the flash distillation column is delivered into a leading tower for rectification dehydration, the pressure in the leading tower ranges from minus 0.080 to minus 0.085MPa, the temperature at the top of the leading tower is 45 to 55 DEG C, and the temperature at the bottom in a towerkettle ranges from 110 to 130 DEG C; (5) the mixture after dehydration is delivered into a rectification column for rectification, the pressure in the rectification column ranges from minus 0.095 to minus 0.099MPa, the temperature in the column kettle ranges from 135 to 160 DEG C, the temperature at the top of the rectification column ranges from 60 to 70 DEG C, isopropanolamine products are obtained at the top of the rectification column, and the mixture composed of diisopropanolamine and triisopropanolamine is obtained in the column kettle. The synthesis method has simple production procedure, little equipment investment, and high product quality.

The invention discloses an environment-friendly high-toughness hard aluminum alloy profile production process. The production process comprises burdening and smelting; the burdening is performed for the following component in percentage by mass: 5-5.5% of Cu, 2-4.5% of Fe, 0.1-0.3% of Mn, 0.5-3% of Mg, 1.1-1.5% of Zn, 0.1-1% of Si, 0.1% of Ni, 0.2% of Ti, and the balance of Al; the smelting is performed for 6-8 h under high temperature to obtain aluminum alloy molten liquid; and then, the horizontal continuous casting, the continuous extrusion and the three-stage ageing heat treatment are performed. The process shortens the alloy production process and period without needing the homogenization and the preheating treatment, and totally accords with the production requirements of energy conservation and greenness of a short-flow process; and a prepared aluminum alloy profile has excellent toughness and tensile strength, and can satisfy the gradually increasing high-end demands.

The invention relates to a method of manufacturing diisopropanolamine. Liquid ammonia and water are mixed to form ammonia water which is fully mixed with propylene oxide; the mixed solution is preheated until the temperature reach 140 to 145 DEG C and then is delivered into a reactor for reacting, the temperature is controlled within 148 to 155 DEG C when in reacting, the pressure is controlled within 16.0 to 18.0MPa, the inputting molar ratio of the ammonia and the propylene oxide is controlled within 5 to 8, and the reaction is fully performed for 1.5 to 3 hours; the mixture products obtained in the reaction are separated to obtain isopropanolamine products, diisopropanolamine products and triisopropanolamine products through flash evaporation and rectification in a stepwise way. In thediisopropanolamine products which are manufactured by adopting the method, the component of 1, 1<1>-nitrousalkyl-dipropyl-2-alcohol accounts for more than 99 percent (hereinafter referred to as mass percent), and the isomeride thereof is less than 1 percent. In addition, the cost of the production operation in the method is less, the production cost is low, the product quality is high, and the high-end requirement of products such as synthetic medicine, farm insecticide, etc. is satisfied.