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132 results about "Monoisopropanolamine" patented technology

Monoisopropanolamine MIPA; Threamine. Identifiers CAS Number. ... 1-Amino-2-propanol is an intermediate in the synthesis of a variety of pharmaceutical drugs and is the very basic building block of the opioid methadone.

Method of synthesizing monoisopropanolamine

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 tower kettle 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.
Owner:NANJING BAOCHUN CHEMICAL INDUSTRY CO LTD

Preparation method of diethylene monoisopropanolamine

The invention relates to a preparation method of diethylene monoisopropanolamine. The preparation method comprises the following steps of (1) introducing an inert gas to replace air inside a reaction kettle into the reaction kettle; (2) premixing epoxy propane and diethanolamine, then adding to the reaction kettle, introducing the inert gas to keep the pressure inside the reaction kettle to 0.1-0.5 Mpa, stirring and mixing materials, then raising temperature, keeping the temperature, and reacting to obtain a diethylene monoisopropanolamine product. According to the preparation method disclosed by the invention, diethanolamine and epoxy propane are utilized as raw materials and the conventional way of taking water as a solvent is abandoned, and the materials are premixed, so that the viscosity and solidification point of the reacted materials are reduced; the fast progress of reaction is facilitated due to the uniform dispersion of the two materials in a reactor; in addition, under the condition of low alkane-amine ratio, the improvement of the utilization ratio of epoxy propane and the reduction of generation probability of side reaction are facilitated. The whole process has the advantages of low energy consumption, high material transformation rate, high product purity, stable quality and no wastes.
Owner:NANJING BAOCHUN CHEMICAL INDUSTRY CO LTD

Preparation method of modified molasses waste liquid and cement grinding aid

ActiveCN104609765AGive full play to auxiliary grindingGive full play to the effect of hydrationLiquid wasteMonoisopropanolamine
The invention provides a preparation method of a modified molasses waste liquid. The preparation method comprises the following steps: A, regulating the PH of the molasses waste liquid to the range of 9-11 by use of a sodium hydroxide solution, and filtering under a normal pressure to obtain a molasses filtrate A; B, adding an acetic acid solution to the molasses filtrate A until the PH is within the range of 2-3, thereby obtaining a molasses waste liquid B; C, thoroughly oxidizing the molasses waste liquid B by using 35% hydrogen peroxide, potassium permanganate or ozone, thereby obtaining a molasses waste liquid C; D, regulating the PH of the molasses waste liquid C to the range of 9-11 by use of the sodium hydroxide solution, thereby obtaining the modified molasses waste liquid. The invention also provides a cement grinding aid which is prepared by mixing the following raw materials in parts by weight with water: 2-5 parts of triethanolamine, 18-25 parts of diethanol monoisopropanolamine, 3-5 parts of industrial salt and 20-30 parts of modified molasses waste liquid. The modified molasses waste liquid has the characteristics of low production cost, and good grinding assisting and hydration assisting effects on the cement.
Owner:华润水泥技术研发(广西)有限公司

Method for joint production of isopropanolamine

The invention belongs to the field of chemical building materials and relates to a method for joint production of DEIPA (diethanolisopropanolamine) and TIPA (triisopropanolamine). The method has the characteristics that the industrialized production is environmentally friendly, the production efficiency is high, the economic benefit is relatively good and a grinding aid formula is convenient to adjust. The method comprises the following steps: A, continuously adding PO (propylene oxide) into an ammonia water solution in a reactor 1, controlling the reaction temperature and the pressure, and reacting until an intermediate product is obtained; B, transferring the intermediate product obtained in the step A to a reduced pressure distillation tower, distilling off an ammonia water recovery solution from the top of the tower and MIPA (monoisopropanolamine) from a side line, and collecting high-boiling-point substances from the bottom of the tower; C, adding MIPA obtained in the step B into a reactor 2, continuously adding EO (ethylene oxide), controlling the reaction temperature and the pressure, and reacting until DEIPA is obtained; adding the high-boiling-point substances at the bottom of the tower obtained in the step B into a reactor 3, continuously adding PO, controlling the reaction temperature and the pressure, and reacting until TIPA is obtained.
Owner:安徽海螺材料科技股份有限公司

Method for preparing diisopropanolamine

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 the diisopropanolamine 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.
Owner:NANJING BAOCHUN CHEMICAL INDUSTRY CO LTD

Method for preparing tri-isopropanolamine

The invention relates to a method of manufacturing triisopropanolamine. Firstly, air in a reaction kettle is replaced by nitrogen, and the reaction kettle is vacuumized; then after being injected with the nitrogen, the reaction kettle is vacuumized; the step is repeated for three to five times; secondly, isopropanolamine or diisopropanolamine or isopropanolamine mixture are put in the reaction kettle, the nitrogen is injected until the pressure reach more than minus 0.05MPa, then propylene oxide is added in continuously, wherein, the molar ratio between the propylene oxide and the number of hydrogen atoms contained on nitrogen atoms in the isopropanolamine is controlled within 1.0 to 1.1, the reaction temperature ranges from 50 to 90 DEG C, the reaction pressure ranges from minus 0.1 to 1.0MPa, and the reaction time is 8 to 15 hours; after the reaction is finished, products are discharged and packed under the protection of the nitrogen. The method greatly lowers the energy consumption, reduces the caused environmental pollution, increases the product quality, has low demand to equipment, saves the cost, has wide demanding range to raw material, and can make the best of waste materials which are generated when manufacturing the isopropanolamine and the diisopropanolamine. The purity of the products which is manufactured by adopting the method can reach more than 99 percent, the moisture content is less than 0.3 percent, and the colority of Pt-Co is less than 50.
Owner:NANJING BAOCHUN CHEMICAL INDUSTRY CO LTD

Method of synthesizing monoisopropanolamine

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.
Owner:NANJING BAOCHUN CHEMICAL INDUSTRY CO LTD
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