Bubbling tower and method for producing benzoic acid by liquid phase oxidation of toluene with the same

A liquid phase oxidation, benzoic acid technology, applied in chemical methods, chemical instruments and methods for reacting liquids and gaseous media, and liquid and gas reactions under foam/aerosol/bubble, etc., can solve the problem of crystalline benzoic acid. The content is difficult to reach 99.99%, the yield of industrial grade benzoic acid and its content are reduced, and the benzoic acid is not easy to be purified, etc., to achieve the effects of high gas-liquid mass transfer capacity and material mixing capacity, efficient use of reaction heat, and easy cleaning of scale.

Active Publication Date: 2019-07-23
WUHAN YOUJI IND
View PDF11 Cites 5 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Trichlorotoluene hydrolysis method is owing to contain chlorine, serious corrosion equipment, pollutes environment; The harmful impurity of phthalic anhydride decarboxylation method is less, but the benzoic acid of generation is difficult for refining, and production cost is higher; And toluene liquid-phase air oxidation method reaction condition Mild, less waste, is the most important production method of benzoic acid
Therefore, if crude product benzoic acid content is too high, will cause the yield of industrial grade benzoic acid and the reduction of content thereof in the follow-up rectification process
[0008] In addition, when the content of industrial-grade benzoic acid is lower than a certain value, such as 99.0%, it will be difficult for the content of crystalline benzoic acid in the melt crystallization section to reach 99.99%, which is the required content of pharmaceutical-grade benzoic acid
[0009] In addition, the problem encountered in the use of existing bubble column reactors: the gas is dispersed into smaller bubbles after passing through the gas distributor, but the bubbles will regroup into large bubbles in the process of rising, which is very difficult for gas-liquid phase transmission. quality is unfavorable
This kind of bubble accumulation that is not conducive to mass transfer will cause the decline of the overall reaction rate, and more seriously, it will cause the oxygen content in the tail gas at the outlet of the oxidation reaction device to be too high. If it is higher than 1.5%, it will form an explosive mixture with toluene, and there will be Security risks

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
  • Bubbling tower and method for producing benzoic acid by liquid phase oxidation of toluene with the same
  • Bubbling tower and method for producing benzoic acid by liquid phase oxidation of toluene with the same
  • Bubbling tower and method for producing benzoic acid by liquid phase oxidation of toluene with the same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] In order to facilitate the description of the size of the bubble tower device, the following symbols are used to represent the size of each component: diameter of the cylindrical tower body D; height of the cylindrical tower body H; height of the spiral plate member H1; width of the spiral plate W; distance between the spiral plates G1; Tube diameter D1; spoiler height H2; corrugated plate spacing G2.

[0048] In this embodiment, the heat exchanger of the bubble column device used for the liquid-phase oxidation of toluene to produce benzoic acid is a tube-and-tube heat exchanger, with a single heat exchange area of ​​5m 2 , the specific dimensions of other components are as follows (in m):

[0049] D H H1 W G1 D1 H2 G2 0.4 1 0.6 0.02 0.12 0.07 0.1 0.002

[0050] Use the bubble column device of the present invention to carry out toluene oxidation reaction under the following conditions, during stable production, toluene flow rate 1.6t / h, a...

Embodiment 2

[0054] In this example, the heat exchanger of the bubble column device used for the liquid-phase oxidation of toluene to produce benzoic acid is a plate heat exchanger, with a single heat exchange area of ​​7m 2 , the specific dimensions are as follows (in m):

[0055] D H H1 W G1 D1 H2 G2 0.4 1 0.45 0.04 0.05 0.07 0.05 0.003

[0056] Use the bubble column device of the present invention to carry out toluene oxidation reaction under the following conditions, during stable production, toluene flow rate 1.6t / h, air 700Nm 3 / h, catalyst concentration 160ppm, reaction temperature 165°C, reaction pressure 0.65MPa. The oxygen content in the tail gas is 0.08%, and the main components and contents of the oxidation liquid in the liquid phase outlet 8 are:

[0057] Oxidizing solution components Content / wt% benzene 0.63 toluene 55.8 benzoic acid 38.2 Benzyl Benzoate 1.7 biphenyl 0.007 other balance

[...

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 discloses a bubbling tower device for producing benzoic acid by liquid phase oxidation of toluene. The bubbling tower device includes a cylinder tower body, a tower top head, a tower bottom head, a gas phase outlet, a safety pressure relief port and a liquid phase outlet. A gas distributor, a spiral plate member and a flow disturbing member are arranged in the cylinder tower from bottom to top. Outer circulation pipes are arranged on the two sides of the cylinder tower body. Heat exchangers are arranged on the outer circulation pipes. Lower end outlets of the outer circulation pipes are located between the gas distributor and the spiral plate member. Upper end inlets of the outer circulation pipes are located at the upper part of the flow disturbing member. A toluene inlet, acatalyst inlet and a gas inlet are arranged on the cylinder tower body and located at the lower end of the corresponding outer circulation pipe. The gas inlet is connected to the gas distributor. Thebubbling tower device of the invention can effectively realize material circulation of the whole tower without moving members, is sufficient in gas-liquid mass transfer, can improve the yield of thebenzoic acid, can reduce the content of impurities such as biphenyl, and can ensure production safety. The external heat exchangers of the device can be repaired without stopping, which saves energy and reduces consumption.

Description

technical field [0001] The invention relates to a reaction device for liquid-phase oxidation, in particular to a bubble column device and a method for producing benzoic acid by liquid-phase oxidation of toluene. Background technique [0002] Benzoic acid, also known as benzoic acid, is the simplest aromatic carboxylic acid, which exists in benzoin gum and the stem bark and leaves of some plants, often in the form of free acid, ester or its derivatives. The pure product is needle-like or scale-like crystals, slightly soluble in water, easily soluble in organic solvents such as ether and ethanol. Benzoic acid can be used as an antirust agent for iron and steel equipment, a mordant for dyeing and printing, and a modifier for carboxylic acid resins. It can also be used as an intermediate for pharmaceuticals and dyes. It is an important raw material for the preparation of caprolactam and phenol. Benzoic acid and its sodium salt are important food preservatives with high safety a...

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): B01J10/00C07C51/265C07C63/06
CPCB01J10/002C07C51/265C07C63/06
Inventor 袁鹏孙波李毅周峰陈波聂少春方磊黄正望
Owner WUHAN YOUJI IND
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