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Separation device for maleic anhydride hydrogenation product and process thereof

A technology for a hydrogenation product and a separation device, which is applied in the field of chemical rectification, can solve the problems of large floor space, low energy utilization rate, and large number of rectification towers.

Pending Publication Date: 2021-09-07
CHANGMAO BIOCHEMICAL ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] Existing literature 1 (Sun Jiashi et al., Research on the separation process of succinic anhydride products from hydrogenation of maleic anhydride. Shanghai Chemical Industry, 2017, 42(12):12-15.) The 2-column rectification method provided for separation does not consider adding The influence of the hydrogen by-product 1,4-butanediol, while using the direct feed rectification method, the hydrogenation by-products succinic acid and maleic acid are high-melting boiling point substances, which may be precipitated during the rectification process The solid phase will block the packing, pipes, valves, etc. in the tower, which will affect the operation safety of the distillation tower
[0004] Chinese patent CN207031313U uses 3 towers in series to separate maleic anhydride hydrogenation products, but still does not consider the impact of hydrogenation by-products such as succinic acid, maleic acid and other high melting boiling point substances on the rectification system, and there are rectification towers Disadvantages such as large number, large floor area and low energy utilization
[0005] Chinese patent application CN 108822063A uses a sublimation method to purify succinic anhydride to remove acrylic acid and other low-melting small molecule organics in the crude succinic anhydride product, but the maleic anhydride hydrogenation product contains a large amount of solvents γ-butyrolactone, butanediol Acid anhydride cannot be directly separated by sublimation, and this method cannot mass-produce high-purity succinic anhydride
[0006] The separation of high-purity (mass fraction ≮99.0%) succinic anhydride and the recovery of solvent γ-butyrolactone are the core of the separation process of maleic anhydride hydrogenation products. Through the above introduction, there are still some problems in the separation of maleic anhydride hydrogenation products. defect

Method used

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  • Separation device for maleic anhydride hydrogenation product and process thereof
  • Separation device for maleic anhydride hydrogenation product and process thereof
  • Separation device for maleic anhydride hydrogenation product and process thereof

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Experimental program
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Effect test

Embodiment 1

[0035] Such as figure 1 As shown, the separation device of the present invention includes a preheater 1, a vapor-liquid separation tank 2, a bulkhead tower 3 and a vacuum device 4 connected in sequence, and the vapor-liquid separation tank 2 is provided with a defoaming section 2-1, A partition 3-5 is vertically arranged in the next-door tower 3, and the inner cavity of the next-door tower 3 is divided into two regions by the partition 3-5. The left side of the partition 3-5 is the main tower, and the main tower includes the main tower fine Distillation section 3-1, main tower stripping section 3-2 and the feed section arranged between main tower rectifying section 3-1 and main tower stripping section 3-2, main tower includes at least one feed inlet; The right side of the dividing plate 3-5 is the auxiliary tower, which includes the rectifying section 3-6 of the auxiliary tower; the feed material entering the feed section of the main tower is the gas phase material distilled f...

Embodiment 2

[0056] The difference between embodiment 2 and embodiment 1 lies in that the number of trays in each part of the dividing wall column 3 is different and the selection of process parameters is different.

[0057] The maleic anhydride hydrogenation reactant A of 200kmol / h enters the preheater 1 and is heated to 180° C., and after the pressure is 15kPa, it is sent into the vapor-liquid separation tank 2, and the mass fraction of succinic acid produced at the bottom of the tank is 12%. The mass fraction of butenedioic acid is 8% and the heavy fraction is 1.1 kmol / hr. The tank top gas phase enters the main tower of the next-door tower 3, the pressure at the top of the main tower is 13kPa, the number of plates in the rectifying section 3-1 of the main tower is 25 plates, the stripping section 3-2 of the main tower is 30 plates, The reflux ratio of the main tower of the main tower is 0.5, the temperature of the first stage condenser 3-3 of the main tower of the next wall tower 3 is c...

Embodiment 3

[0062] The difference between embodiment 3 and embodiment 1 lies in that the number of trays in each part of the dividing wall column 3 is different and the selection of process parameters is different.

[0063] The maleic anhydride hydrogenation reactant A of 300kmol / h enters the preheater 1 and is heated to 155° C., and after the pressure is 9kPa, it is sent into the vapor-liquid separation tank 2, and the mass fraction of succinic acid produced at the bottom of the tank is 18%. The mass fraction of butenedioic acid is 1.5kmol / hr of the heavy fraction of 12%. The gas phase at the top of the tank enters the main tower of the next-door tower 3, and the pressure at the top of the main tower is 7kPa. The reflux ratio of the main tower of the main tower is 1.0, the temperature of the first stage condenser 3-3 of the main tower of the next wall tower 3 is controlled at 110°C, the temperature of the second stage condenser 3-4 of the main tower 3 of the next wall tower is controlled...

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Abstract

The invention relates to the technical field of chemical rectification, and discloses a separation device for maleic anhydride hydrogenation products, the separation device comprises a preheater, a vapor-liquid separation tank, a dividing wall column and a vacuumizing device which are connected in sequence, a partition plate is vertically arranged in the dividing wall column, the partition plate divides an inner cavity of the dividing wall column into a left area and a right area, a main tower is arranged on the left side of the partition plate, and the main tower comprises a main tower rectifying section, a main tower stripping section and a feeding section arranged between the main tower rectifying section and the main tower stripping section; an auxiliary tower is arranged on the right side of the partition plate and comprises an auxiliary tower rectifying section; a reboiler is arranged at the bottom of the dividing wall column; a primary condenser of the main tower is arranged at the top of the main tower of the dividing wall tower, and a secondary condenser of the main tower is arranged on the primary condenser of the main tower; and an auxiliary tower condenser is arranged at the top of the auxiliary tower of the dividing wall column. The process provided by the invention has the beneficial effects that succinic anhydride is obtained through separation by using the dividing wall column, the solvent gamma-butyrolactone is recovered, and the energy utilization rate and the device operation safety in the rectification process are improved.

Description

technical field [0001] The invention relates to a separation device and process for hydrogenation products of maleic anhydride, in particular to a device and a process for separating hydrogenation products of maleic anhydride by using a dividing wall tower, and belongs to the technical field of chemical distillation. Background technique [0002] Succinic anhydride is an important chemical intermediate, which can be used to produce thermoplastic fully biodegradable plastic polybutylene succinate (PBS), which is widely used in catering packaging, building materials, plastic films and other fields, and has been approved by the state Included in the encouraged development category of industries. Catalytic hydrogenation of maleic anhydride (maleic anhydride, referred to as: maleic anhydride) is one of the important process technologies for producing succinic anhydride, and the separation of its products is the key to obtain high-purity (mass fraction ≮99.0%) succinic anhydride p...

Claims

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Application Information

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IPC IPC(8): C07D307/60C07D307/33
CPCC07D307/60C07D307/33Y02P20/50
Inventor 冷一欣王俊芮新生黄春香
Owner CHANGMAO BIOCHEMICAL ENG CO LTD