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Reaction device and system and method for synthesizing acetic acid from carbonyl

A reaction device, acetic acid technology, applied in the chemical industry, can solve problems such as difficult stable and safe operation, easy damage to shaft seals and bearings, uneven liquid distribution, etc., to eliminate hidden dangers of parking, reduce temperature difference, and uniform temperature field Effect

Pending Publication Date: 2021-05-28
SHANGHAI HUAYI ENERGY CHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Traditional gas-liquid mixing mostly adopts the conventional mechanical stirring mode. The reaction equipment using mechanical stirring can effectively mix liquid-liquid and gas-liquid. However, the shaft seals and bearings required for mechanical transmission are easily damaged during long-term operation. Cause shutdown maintenance, it is difficult to achieve continuous, stable and safe operation
In recent years, the use of hydraulic agitation has become an important direction for the technical improvement of methanol carbonylation acetic acid plant. At present, the main problems in the use of hydraulic agitation technology are as follows: the single-layer ring distributor has uneven gas distribution, which causes catalyst precipitation; liquid Uneven distribution, resulting in uneven reaction, uneven distribution of temperature field; production capacity decline, etc.

Method used

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  • Reaction device and system and method for synthesizing acetic acid from carbonyl
  • Reaction device and system and method for synthesizing acetic acid from carbonyl
  • Reaction device and system and method for synthesizing acetic acid from carbonyl

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0097] Methanol low-pressure synthetic acetic acid reaction device, the height of the cylinder of the reactor (i.e. the length of the straight side of the cylinder of the reactor) is 5m, and the diameter is 3m. After the transformation of the reactor, the figure 1 , image 3 and Figure 4 As shown in the circulating fluid stirring part and the three-dimensional multi-ring raw material gas distribution stirring part, the included angle of the vertical projection of the central axis of the two circulating fluid feeds on the radial plane of the reactor is 150°, and the two circulating fluid feeding The nozzle at the end of the material pipe is located at 5 / 6m below the liquid surface (1 / 6 of the length of the straight side of the reactor), the fluid flow rate of the nozzle of the circulating fluid feeding pipe is 5m / s, and the circulating fluid feed The total flow of fluid at the outlet of the pipe is 200m 3 / h, 5 times the volume of the reaction solution. The raw material gas...

Embodiment 2

[0099] Methanol low-pressure synthetic acetic acid reaction device, the height of the reactor cylinder is 5m, the diameter is 3m, after the transformation of the reactor, adopt figure 2 , image 3 and Figure 4 The circulating fluid stirring part shown and the three-dimensional multi-ring raw material gas distribution stirring part, three circulating fluid feeding pipes, and the folder of the vertical projection of the central axis of the adjacent circulating fluid feeding pipe 121 on the radial plane of the reactor The angle is 120°, the nozzle at the end of the circulating fluid feeding pipe is located at 10 / 6m below the liquid surface (2 / 6 of the length of the straight side of the reactor), and the flow rate of the fluid ejected from the nozzle of the circulating fluid feeding pipe is 11m / s, the total fluid flow at the outlet of the circulating fluid feed pipe is 260m 3 / h is 6.2 times the volume of the reaction solution. The raw material gas distribution stirring unit ...

Embodiment 3

[0101] Methanol low-pressure synthesis of acetic acid reaction device, the height of the reactor cylinder is 5m, the diameter is 3m, after the transformation of the reactor, adopt figure 2 , image 3 and Figure 4 The shown circulating fluid stirring part and the three-dimensional multi-ring material gas distribution stirring part, four circulating fluid feed pipes, and the folder of the vertical projection of the central axis of the adjacent circulating fluid feed pipe 121 on the radial plane of the reactor The angle is 60°, the nozzle at the end of the circulating fluid feeding pipe is located at 15 / 6m below the liquid surface (1 / 2 of the length of the straight side of the reactor), and the flow rate of the fluid ejected from the nozzle of the circulating fluid feeding pipe is 15m / s, the total fluid flow at the outlet of the circulating fluid feed pipe is 320m 3 / h is 7.5 times the volume of the reaction solution. The raw material gas distribution and stirring components ...

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Abstract

The invention provides a reaction device and a system and a method for synthesizing acetic acid from carbonyl. The reaction device comprises a reaction kettle, a circulating fluid stirring part and a raw material gas distribution stirring part. The gas distribution stirring part comprises more than two gas distribution stirring units, and the more than two gas distribution stirring units are distributed in multiple layers along the central shaft of the reaction kettle and are communicated. A circulating fluid feeding pipe penetrates through a circulating fluid inlet and is communicated with a circulating fluid outlet. A raw material gas feeding pipe penetrates through a raw material gas inlet and is communicated with the gas distribution stirring part. When the reaction device is used for synthesis of acetic acid from carbonyl, a shaft seal and a bottom fixed bearing are prevented from being easily damaged in the operation process during mechanical stirring, there is no movable sealing point, and safe and stable operation of a reaction system is guaranteed. Meanwhile, the more than two gas distribution stirring units which are distributed in multiple layers and are sequentially communicated enable gas in the reaction kettle to be distributed more uniformly, the gas-liquid two-phase mixing effect is improved, the reaction state in the system is optimized, the temperature difference in the reaction kettle is reduced, and side reactions are reduced.

Description

technical field [0001] The invention belongs to the field of chemical industry, and relates to a reaction device, a system and a method for oxo-synthesizing acetic acid. Background technique [0002] Acetic acid is an important chemical intermediate and solvent for chemical reactions. Among the acetic acid synthesis processes currently in use, the most commonly used one is the methanol low-pressure oxo synthesis process, which was pioneered by the American Monsanto Company in the 1970s. After decades of innovation and development, the device capacity, product quality, and production cost major breakthroughs have been achieved. Traditional gas-liquid mixing mostly adopts the conventional mechanical stirring mode. The reaction equipment using mechanical stirring can effectively mix liquid-liquid and gas-liquid. However, the shaft seals and bearings required for mechanical transmission are easily damaged during long-term operation. Cause parking maintenance, it is difficult t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/18B01J8/08B01D3/06C07C51/12C07C53/08
CPCB01J8/18B01J8/1818B01J8/085B01J8/08B01D3/06C07C51/12C07C53/08Y02P20/584
Inventor 陈大胜顾明兰刘文艳李永朋吴良泉孟庆军顾卫忠王培新钱永明
Owner SHANGHAI HUAYI ENERGY CHEM
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