Technological process and device for separating isopropanol water solution

A process method, isopropanol technology, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of high investment and energy consumption, complex process operation, unsatisfactory isopropanol purity, etc. The effect of equipment investment saving

Inactive Publication Date: 2008-12-31
CHINA UNIV OF PETROLEUM (EAST CHINA)
View PDF4 Cites 30 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After separation, isopropanol can be recycled, and ethylene glycol monomethyl ether can be returned to the raw material without causing environmental pollution. However, this operation equipment investment and energy consumption are high, and the purity of isopropanol cannot meet the requirements of some industries.
[0006] Patent CN1249294A invents a method for refining isopropanol in a combined process of adding salt, extraction, azeotropic rectification, first the dilute aqueous solution of isopropanol in industrial production is roughly extracted to the top of the tower through rectification to obtain initially concentrated isopropanol, and then C6 aliphatic hydrocarbon is used as the extraction agent, and the aqueous solution of inorganic sodium salt or potassium salt is used as the salting-out separation agent for salt extraction, and the extracted organic p

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Technological process and device for separating isopropanol water solution
  • Technological process and device for separating isopropanol water solution
  • Technological process and device for separating isopropanol water solution

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0018] Example 1: if figure 1 process shown. The next-wall azeotropic distillation column adopts a tray column with a column diameter of 1600mm and a column height of 12000mm. The cross-sectional area ratio of the dehydration section (2) and the side line rectification section (3) is 0.51:1. The mass flow rate of the liquid phase flowing into the dehydration section (2) from the top of the partition wall (6) is 38.5% of the mass flow rate of the liquid phase at the top of the partition wall (6). The number of theoretical plates, feed flow rate and composition of each area are shown in Table 1. Cyclohexane is used as the entraining agent, the feeding position of the raw material isopropanol aqueous solution (counted from top to bottom, the same below) is the sixth theoretical plate of the public rectification section (1), and the heavy phase reflux position in the phase separator is the side line In the 10th theoretical plate of the rectification section (3), supplementary en...

example 2

[0021] Example 2: if figure 1 process shown. The azeotropic rectification column with the next wall adopts a tray and packing mixed tower with a diameter of 2200mm, and the height of the tower is 14000mm. The side line rectification section (1) uses trays, and the dehydration section (2) and side line rectification section (3) use packing. , the cross-sectional area ratio of the dehydration section (2) to the side rectification section (3) is 0.47:1. The mass flow rate of the liquid phase flowing into the dehydration section (2) from the top of the partition wall (6) is 43.4% of the mass flow rate of the liquid phase at the top of the partition wall (6). The feed position and the number of theoretical plates in each region are the same as in Example 1, and the entrainer is still cyclohexane, but the feed composition and flow rate are changed to some extent. The flow rate and composition of each stream are shown in Table 2. The temperature at the top of the tower is 63.8°C; ...

example 3

[0024] Example 3: if figure 1 process shown. The next-wall azeotropic distillation column adopts a tray column with a column diameter of 1600 mm and a column height of 16000 mm. The cross-sectional area ratio of the dehydration section (2) and the side line rectification section (3) is 0.51:1. The mass flow rate of the liquid phase flowing into the dehydration section (2) from the top of the partition wall (6) is 38.5% of the mass flow rate of the liquid phase at the top of the partition wall (6). Feed composition, feed flow rate and the number of theoretical plates in each area are the same as example 1, and the entrainer is still cyclohexane, but the feed position is changed, and the isopropanol aqueous solution feed position becomes the public rectification section (1) No. 3 theory boards. The temperature at the top of the tower is 61.0°C; the temperature of the bottom of the dehydration section (2) is 80°C; the temperature of the bottom of the side rectification section ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a novel azeotropic distillation technical method and a device, particularly to a technical method and a device using a bulkhead azeotropic distillation column to produce anhydrous isopropanol. The invention enables the separation between isopropanol and water, as well as the recovery of entrainer to be integrated into the same distillation column. The bulkhead azeotropic distillation column refers to a piece of bulkhead (6) which is arranged in the vertical direction inside the conventional distillation column and extended from the upper part of the distillation column to the bottom part of the distillation column; the total height of the bulkhead (6) is less than that of the distillation column; the bottom of the bulkhead is closed; the bulkhead (6) divides the distillation column into three parts: a public distillation segment (1), a dehydration segment (2) and a lateral line distillation segment (3). The isopropanol aqueous solution which needs to be separated enters into the distillation column from the lower part of the public distillation segment (1) and get the high-purity isopropanol from the bottom of the dehydration segment (2); the , ternary azeotrope is steamed out from the top of the distillation column; the steam at the top of the distillation column is condensed through a condenser (5) and then enters into a phase splitter (4) to be divided into light and heavy two-phase liquid; the light phase (entrainer) flows back, while the heavy phase enters into the lower part of the lateral line distillation segment (3) to get the water containing a small amount of isopropanol at the bottom of the lateral line distillation segment (3).

Description

technical field [0001] The invention relates to an azeotropic rectification process and device, in particular to a novel process and device for producing anhydrous isopropanol by using a next-wall azeotropic rectification tower, which can separate isopropanol and water, entrainer Recycling is combined in one column. Background technique [0002] Isopropanol (IPA) is one of the earliest petrochemical products produced in the world. It is mainly used in the production of acetone and as a solvent. It can also be used to synthesize glycerin, ethyl propyl acetate, ethyl propylamine salt, diethyl nitrite The raw material of propylamine, isopropyl nitrate, hydrogen peroxide, ethyl propyl halide and other products, IPA is also widely used as antifreeze additive of petroleum fuel, used in the manufacture of fungicides, insecticides, disinfectants and preservatives, etc. In recent years, with the strengthening of environmental protection, IPA has been used to replace chlorine solvent...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C07C31/10C07C29/82
Inventor 孙兰义昌兴武李军李青松
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products