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A kind of molecular sieve membrane, membrane reactor and its application in the preparation of p-tert-butylphenol

A technology of p-tert-butylphenol and membrane reactor, which is applied in the direction of molecular sieve catalysts, preparation of organic compounds, membranes, etc., and can solve problems such as difficult product separation

Active Publication Date: 2022-02-18
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the problem that the existing preparation method of p-tert-butylphenol (PTBP) produces a large number of by-products o-tert-butylphenol (OTBP) and 2,4-di-tert-butylphenol (2,4-DTBP), and the separation of the products is difficult, this paper The invention provides a molecular sieve membrane, a membrane reactor and its application in the preparation of p-tert-butylphenol, which is conducive to improving the product conversion rate and raw material selectivity, and greatly reducing device investment and operating costs

Method used

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  • A kind of molecular sieve membrane, membrane reactor and its application in the preparation of p-tert-butylphenol

Examples

Experimental program
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Effect test

Embodiment 1

[0060] (1) Prepare the low-temperature synthesis mother liquor of MCM-22 molecular sieve:

[0061] Add 5400g water and 72g NaOH to the container successively, and stir for 30min; then add 33.7g alumina, stir 1830g silica sol (30wt% silica concentration) for 2h, and finally add 350g CTAB and stir for 3h to obtain a gel. The gel was transferred to a reaction kettle, and crystallized at a low temperature of 100° C. for 8 hours to prepare a low-temperature synthesis mother liquor of MCM-22 molecular sieve. In the synthesis mother liquor, the molar ratio of each component is: SiO 2 :Al 2 o 3 :Na + :CTAB=9.14:0.33:1.8:0.96.

[0062] (2) Preparation of molecular sieve membrane:

[0063] Prepare a cylindrical steel mesh with a diameter of 20 cm and a height of 30 cm (aperture 1 μm), and coat a layer of Al on the inside of the steel mesh 2 o 3 Adhesive, coated with a thickness of about 1mm, placed in a high-temperature baking furnace at 600°C for 4 hours to make α-Al 2 o 3 Ine...

Embodiment 2

[0067] (1) Prepare the low-temperature synthesis mother liquor of ZSM-5 molecular sieve:

[0068] Weigh 400g NaOH, add it to 1600g deionized water, stir until completely dissolved, then add 15290g 25% TPAOH solution and stir for 20min; then, slowly drop 14120g 34% silica sol solution into the above solution, stir for 4h; add 695g TPAOH solution Aluminum, stirred for 4 hours to obtain a gel; transfer the above gel to a stainless steel hydrothermal kettle, carry out the first stage of crystallization reaction in an oven at 100°C, and quench the crystallized mother liquor under cold water at 20°C after 8 hours Cool to obtain the first section of crystallization solution; under the condition of 20°C water bath, add 3530g 34% silica sol and 1300g water to the first section of crystallization solution, stir for 20min, and put it into the stainless steel crystallization kettle again, at 180 The second-stage crystallization reaction is carried out at ℃, and the second-stage crystalliz...

Embodiment 3

[0076] [Example 3] Preparation of p-tert-butylphenol by membrane reactor MR-1

[0077] Using phenol and isobutylene as raw materials, under the action of HMCM-22 molecular sieve catalyst, the membrane reactor MR-1 reacts continuously. Wherein, the catalyst loading accounts for 50% of the reactor volume in the membrane, the molar feed ratio of phenol and isobutylene is 10:1, the reaction temperature is 120°C, the reaction pressure inside the membrane is set at 50KPaG, and the external pressure of the membrane is 5KPaG. The reaction liquid is sent to a rectification tower, the unreacted phenol is recovered at the top of the tower, and p-tert-butylphenol is obtained at the bottom of the tower (product purity 99.77%). In this example, the conversion rate of isobutene is 99.92%, and the selectivity to p-tert-butylphenol is 99.92%.

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Abstract

The invention provides a molecular sieve membrane, a membrane reactor and an application in preparing p-tert-butylphenol. In the molecular sieve membrane, a layer of transalkylation catalyst is attached to the inside of the membrane; preferably, the transalkylation catalyst is at least one of Beta molecular sieve, TS-1, and SAPO-5. In the present invention, the molecular sieve membrane is mainly used in the preparation process of PTBP. On the one hand, the product selectivity is improved through membrane separation; The base transfer reaction further generates the product PTBP before membrane separation, which has the advantage of high product selectivity.

Description

technical field [0001] The invention relates to a molecular sieve membrane, in particular to a molecular sieve membrane, a membrane reactor and its application in preparing p-tert-butylphenol. Background technique [0002] 4-tert-butylphenol (PTBP) has antioxidant properties, can be used as a polymerization inhibitor and stabilizer, and is an important intermediate in the production of fine chemicals, especially in the synthesis of pesticides, medicines, liquid crystals and fragrances. The preparation of p-tert-butylphenol mainly uses phenol and isobutylene as raw materials, but the traditional preparation process not only has low product selectivity and raw material conversion rate, but also has a large number of by-products o-tert-butylphenol (OTBP), 2,4-di-tert-butyl 2,4-DTBP and excess phenol are not easy to remove, and need to be continuously separated through multiple rectification devices, resulting in complicated separation processes and high device investment costs....

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/40C01B39/04B01D71/02B01D69/10B01D67/00C07C37/14B01J29/70B01J29/40
CPCC01B39/40C01B39/04B01D71/028B01D69/10B01D67/0079C07C37/14B01J29/7038B01J29/40B01D2311/263
Inventor 姜志成刘运海赵欣方子来张鹏何光文杨国忠代红涛林少宁
Owner WANHUA CHEM GRP CO LTD