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Method for preparing isophorone by plug flow rectification tray and liquid phase condensation of acetone

A technology of plug flow and rectification tower, which is applied in the preparation of carbon-based compounds, preparation of organic compounds, chemical instruments and methods, etc. It can solve the problems of large tray pressure drop, catalyst waste, and large liquid holdup

Active Publication Date: 2020-04-10
WANHUA CHEM GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Although the current reactive distillation process overcomes some shortcomings of the traditional process, there are still many problems in the traditional reactive distillation reactor: such as large liquid holding capacity, uneven liquid phase flow, many side reactions, and low distillation efficiency , the pressure drop of the tray is large (the pressure drop of a single plate in conventional technology can exceed 2kPa), and the energy consumption is high.
Although it can suppress the problems caused by foaming to a certain extent, it also brings a series of problems such as the introduction of other components to pollute the reaction system, difficulty in wastewater treatment, waste of catalysts, and decomposition and loss of defoamers under harsh conditions.

Method used

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  • Method for preparing isophorone by plug flow rectification tray and liquid phase condensation of acetone
  • Method for preparing isophorone by plug flow rectification tray and liquid phase condensation of acetone
  • Method for preparing isophorone by plug flow rectification tray and liquid phase condensation of acetone

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Experimental program
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Effect test

Embodiment 1

[0133] In this embodiment, the structure diagram of the flat plug flow distillation tray is shown in Figure 8 , 6a , 6b.

[0134] The flat plug flow distillation tray 1 includes a tray 3 and a flat plug flow assembly 48 arranged on the tray 3. The flat plug flow assembly 48 includes a staged overflow weir 9, a downcomer plate 16, a light and heavy phase splitting element 13, and The liquid pan I6 and the guide element 20. The plug flow rectification tray of this embodiment is a single overflow, that is, in the rectification tower, a downcomer 5 and a liquid receiver are respectively installed on the trays of each layer of the flat plug flow rectification tray installed up and down. Disk I6, that is, a set of flat plug flow components 48 is installed. The downcomers 5 of the plug flow assembly 48 of the upper and lower plug flow rectification trays are arranged in a staggered manner. Therefore, the liquid receiving trays I6 and 7 in the upper and lower layers are also arranged i...

Embodiment 2

[0138] This embodiment is basically the same as embodiment 1, except that the spray hood used in the flat plug flow distillation tray is a strip spray hood with a rectangular cross section (or called a rectangular spray hood):

[0139] As attached image 3 with 4 As shown, the strip spray hood 27 is provided on the tray 3, and the same structural parts of the strip spray hood 27 and the cylindrical spray hood 17 of Embodiment 1 will not be repeated here. Please refer to Embodiment 1, below The main differences are explained as follows: the cross section of the riser tube 19 is rectangular, the length and width are 240mm and 20mm respectively. The longer side of the rectangle is installed on the tray 3 along the direction of liquid flow, and the riser tube 19 is higher than the tray 3. 160mm. The total height of the spray hood 27 is 200 mm, the spray hood 27 is arranged on the riser pipe 19, and the overall cross-sectional shape of the spray hood 27 is also rectangular. The spray...

Embodiment 3

[0142] The process diagram of preparing isophorone (or IP for short) by liquid-phase condensation of acetone is as attached Figure 5 As shown, the acetone and NaOH aqueous solution are preheated by the preheater 28 and fully mixed by the mixer 29 (this embodiment specifically uses the SMV static mixer of Sulzer, Switzerland) and then enters the first condensation reactor 30 (this embodiment The reactor 30 used is a tubular fixed-bed reactor), the reaction temperature is 210°C, the pressure is 3.5MPa (G), the acetone processing capacity is 600kg / h, the mass ratio of acetone and water is 5:1, and the catalyst is NaOH to react The total flow of the liquid is the benchmark, and the mass concentration of NaOH is 0.1%.

[0143] The acetone conversion rate corresponding to the outlet of the first condensation reactor 30 is 10%, and the reaction liquid (that is, the liquid phase stream) then enters the pressure reaction rectification tower 31, and the pressure reaction rectification towe...

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Abstract

The invention provides a plug-flow rectification tray and a method for preparing isophorone by liquid-phase condensation of acetone. The plug-flow rectification tray provided by the invention includes a tray and a plug-flow rectification tray arranged on the tray. Assemblies, the flat push flow assembly includes downcomer, graded overflow weir, light and heavy phase diversion element, liquid receiving plate I and flow guide element; the downcomer is connected with the tray, and the graded overflow weir is arranged on the inlet of the downcomer The light-heavy phase splitting element is located in the downcomer and below the grading overflow weir; the liquid receiving tray I is connected to the tray, and is located on the opposite side of the side where the downcomer and the tray are connected; the flow guide element is located at Above the connection between the liquid receiving tray I and the tray, the guide element is provided with a plurality of guide passages; the pressurized reaction rectification tower containing the plug flow rectification tray of the present invention is used to carry out the IP (isotropic) easily foaming The post-treatment of phorone) / alkali system can make the liquid phase distribute and flow more evenly, which in turn helps to improve the reaction effect.

Description

Technical field [0001] The invention relates to a reactive distillation tray and a process for preparing isophorone by using the reactive distillation tray. Background technique [0002] Isophorone is one of the important products of acetone deep processing, chemical name: 3,5,5-trimethyl-2-cyclohexen-1-one, English name: Isophorone (abbreviated as IP), molecular formula is C 9 H 14 O. Isophorone has a wide range of uses, with strong dissolving ability, good dispersibility, and good leveling. It is an excellent high boiling point green solvent. Because of its conjugated unsaturated ketone structure, it can be further reacted to obtain important products such as alcohols, acids, amines, esters and isocyanates, especially its downstream derivatives isophorone nitrile (IPN) and isophorone diamine (IPDA), isophorone diisocyanate (IPDI) and oxoisophorone (KIP) are of great significance in the fields of specialty amines, polyurethanes and nutritional chemicals. [0003] Industrially, i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D3/14C07C49/603C07C45/74C07C45/82
CPCB01D3/14C07C45/74C07C45/82C07C2601/16C07C49/603Y02P20/10
Inventor 何岩黎源田博边路路周锐员玫李金明孙媛媛
Owner WANHUA CHEM GRP CO LTD