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31results about How to "Purity unchanged" patented technology

Solvate crystal of 9,9-bis(6-hydroxy naphthalene-2-group) fluorene and preparation thereof

The invention discloses a solvate crystal of 9,9-bis(6-hydroxy naphthalene-2-group) fluorene and preparation thereof. A solvate crystal prepared from the 9,9-bis(6-hydroxy naphthalene-2-group) fluorene and acetonitrile is a solvate crystal I of the 9,9-bis(6-hydroxy naphthalene-2-group) fluorene, and a solvate crystal prepared from the 9,9-bis(6-hydroxy naphthalene-2-group) fluorene and ethyl acetate is a solvate crystal II of the 9,9-bis(6-hydroxy naphthalene-2-group) fluorene. The solvate crystal I and solvate crystal II of the 9,9-bis(6-hydroxy naphthalene-2-group) fluorene, which is prepared through the invention achieve the maximum melting endothermic peaks of 261-266 DEG C and the stacking density of 0.4 g / mL after being desolvated, is basically unchanged in color and purity after being preserved at 40 DEG C for three months due to high heat stability and has the advantages of high stacking density, good flowability and easiness for loaded material transfer.
Owner:JIANGSU EVER GALAXY CHEM CO LTD

Energy-saving rectification system and method for purifying fusel oil

The invention discloses an energy-saving rectification system for purifying fusel oil. The system comprises a fusel oil feeding heat exchanger (22), a methanol rectification column (2), an ethanol rectification column (6), a fusel rectification column (14), and an extractant recovery column (18), wherein a methanol rectification column bottom heat exchanger (23) is further arranged at the bottom of the methanol rectification column (2), a fusel oil feeding line (S1) passes through the fusel oil feeding heat exchanger (22) and then is introduced into the methanol rectification column (2), a bottom discharging line of the methanol rectification column (2) is taken as a feeding line of the ethanol rectification column (6), a bottom discharging line of the ethanol rectification column (6) is taken as a feeding line of the fusel oil rectification column (14), a bottom discharging line of the fusel oil rectification column (14) is taken as a feeding line of the extractant recovery column (18), a bottom discharging line (S2) of the extractant recovery column passes through the methanol rectification column bottom heat exchanger (23) at the bottom of the methanol rectification column (2) and the fusel oil feeding heat exchanger (22) in sequence for heat exchange and then is divided into two branches, one of which is introduced to the ethanol rectification column (6) and the other is introduced to the fusel rectification column (14).
Owner:高能时代环境(滕州)环保技术有限公司 +1

Automatic weaving-chain welding machine

The invention provides an automatic weaving-chain welding machine. A main shaft (3) is installed on the upper portion of the machine, a toothed belt wheel (2) is installed at one side of the main shaft (3), the toothed belt wheel (2) is connected with an engine through a toothed belt (1), a transmission gear (6) is installed at the other end of the main shaft (3), the transmission gear (6) is connected with a disc cam gear (7) through a gear, the disc cam gear (7) is connected with a sector gear (8) through a gear, cams (4) and cam swinging rods (5) are further installed on the main shaft (3), a laser focusing lens (10) is further installed at the outer side of the upper portion of the machine, a swing rod (9) is installed at the bottom of the machine, and the machine further comprises a line feeding mechanism (11), a cutting mechanism (12) and a formation rotary mechanism (13). The automatic weaving-chain welding machine has the advantages that weaving-chain production efficiency is remarkably improved, productivity is greatly raised, and sealing quality is greatly improved.
Owner:浙江立新珠宝科技股份有限公司

Multi-shaft common-rail pulse liquid micro-refinement apparatus

The invention discloses a multi-shaft common-rail pulse liquid micro-refinement apparatus. The apparatus comprises a refinement chamber, above two pipelines and a high pressure pump; the refinement chamber is provided with the above two pipelines, one ends of the pipelines are positioned outside the refinement chamber, have three-way structures, and are connected with the high pressure pump and a slurry raw material tube respectively, the slurry raw material tube is provided with a valve, the other ends of the pipelines are positioned in the refinement chamber and are provided with nozzles, the central shafts of the nozzles intersect in the refinement chamber, and the refinement chamber is provided with a material outlet. The apparatus which rapidly breaks and refines the material through utilizing the superposed energy has the characteristics of unique technology, compact structure, stable performances, strong effect, multifunction and the like. The apparatus is mainly used for the controllable refinement treatment of the material in a liquid state, and has the compounding, surface treatment and emulsification functions, and the obtained treated product has a smallest particle size reaching above 1nm nanometer level dimension, has particle size specification uniformity reaching above 80% and an improved functionality.
Owner:XIAMEN TENGYUAN RESOURCE APPL TECH DEV

Energy-saving rectification system and energy-saving rectification method for purifying fusel oil

The invention discloses an energy-saving rectification system for purifying fusel oil. The system comprises a fusel oil feeding heat exchanger (22), a methanol rectification column (2), an ethanol rectification column (6), a fusel rectification column (14), and an extractant recovery column (18), wherein a methanol rectification column bottom heat exchanger (23) is further arranged at the bottom of the methanol rectification column (2), a fusel oil feeding line (S1) passes through the fusel oil feeding heat exchanger (22) and then is introduced into the methanol rectification column (2), a bottom discharging line of the methanol rectification column (2) is taken as a feeding line of the ethanol rectification column (6), a bottom discharging line of the ethanol rectification column (6) is taken as a feeding line of the fusel oil rectification column (14), a bottom discharging line of the fusel oil rectification column (14) is taken as a feeding line of the extractant recovery column (18), a bottom discharging line (S2) of the extractant recovery column passes through the methanol rectification column bottom heat exchanger (23) at the bottom of the methanol rectification column (2) and the fusel oil feeding heat exchanger (22) in sequence for heat exchange and then is divided into two branches, one of which is introduced to the ethanol rectification column (6) and the other is introduced to the fusel rectification column (14).
Owner:高能时代环境(滕州)环保技术有限公司 +1
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