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Composite molecular sieve catalyst for MTP (methanol to propylene) as well as application thereof

A technology for preparing composite molecular sieve and methanol is applied in the field of composite structure bi-molecular sieve catalyst, which can solve the problems of low propylene yield and high gasoline yield

Active Publication Date: 2014-06-25
洛阳市科创石化科技开发有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

To solve the problems of low propylene yield and high gasoline yield in the existing ZSM-5 molecular sieve synthesis phase separation and MTP technology

Method used

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  • Composite molecular sieve catalyst for MTP (methanol to propylene) as well as application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment l

[0035] Take 24.4g of silica sol, 7.8g of sodium aluminum metaphosphate, 7.6g of ammonium hydrogen phosphate, and 150.2g of distilled water, mix them evenly, age at room temperature for 24 hours; evaporate at 70°C for 24 hours to make a concentrated gel mixture. According to the molar ratio of SiO 2 :A1 2 0 3 :P 2 0 5 :Morpholine:H 2 0=0.6:1:1:1:60 Add morphineline and water, put it into a pressure-resistant reaction kettle lined with polytetrafluoroethylene, slowly raise the temperature to 130°C for static crystallization for 12 hours; cool down to prepare a product containing SAPO-34 microcrystalline molecular sieve semi-finished slurry.

[0036] SiO 2 :A1 2 0 3 :NaO 2 :TPAOH:H 2 0=30:1:3.25:5:20, formulated to contain 0.2 moles of SiO 2 The gel mixture is then added to the semi-finished slurry containing SAPO-34 microcrystalline molecular sieve prepared above. Their mixture was stirred for 30 minutes and then transferred to a crystallization kettle. Raise the te...

Embodiment 2

[0039] Take 9.0g ethyl orthosilicate, 5.8g aluminum nitrate, 6.6g phosphoric acid, 170.2g distilled water, mix well, age at room temperature for 1 hour; evaporate at 100°C for 4 hours to make a concentrated gel mixture. According to the molar ratio of SiO 2 :A1 2 0 3 :P 2 0 5 :C6H15N:H 2 0=0.6:1:1:1:60 Add triethylamine and water, put it into a pressure-resistant reactor lined with polytetrafluoroethylene, slowly raise the temperature to 160°C for static crystallization for 4 hours; cool down to prepare Semi-finished slurry containing SAPO-34 microcrystalline molecular sieve.

[0040] Silicic acid, aluminum sulfate, sodium hydroxide, tetrapropylammonium hydroxide, and deionized water are prepared according to the molar ratio: SiO 2 :A1 2 0 3 :NaO 2 :TPAOH:H 2 0=30:1:3.25:5:20, formulated to contain 0.2 moles of SiO 2 The gel mixture is then added to the semi-finished slurry containing SAPO-34 microcrystalline molecular sieve prepared above. Their mixture was stirr...

Embodiment 3

[0043] Take 6.0g of silicon dioxide, 5.8g of aluminum nitrate, 7.6g of ammonium hydrogen phosphate, and 192.6g of distilled water, mix them evenly, age at room temperature for 6 hours; evaporate at a temperature of 85°C for 6 hours to make a concentrated gel mixture. According to the molar ratio of SiO 2 :A1 2 0 3 :P 2 0 5 : Organic template agent: H 2 0=0.6:1:1:1:60 Add tetraethylammonium hydroxide and water, put it into a pressure-resistant reactor lined with polytetrafluoroethylene, slowly raise the temperature to 145°C for static crystallization for 8 hours; cool down , prepared into semi-finished slurry containing SAPO-34 microcrystalline molecular sieve.

[0044] Tetraethyl orthosilicate, aluminum sulfate, sodium hydroxide, tetrapropylammonium hydroxide, and deionized water are prepared according to the molar ratio: SiO 2 :A1 2 0 3 :NaO 2 :TPAOH:H 2 0=30:1:3.25:5:20, formulated to contain 0.2 moles of SiO 2 The gel mixture is then all added to the semi-finishe...

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Abstract

The invention relates to a composite molecular sieve catalyst for MTP (methanol to propylene) as well as application thereof. The composite molecular sieve catalyst for MTP is prepared by the following steps: (1) preparing a silicon source, an aluminum source, a phosphorus source and deionized water according to mole ratio into a mixture, and stirring fully; (2) sealing a crystallization mixture into a kettle or a tank, aging and evaporating so as to prepare a concentrated gel mixture; (3) adding an organic template agent according to the mole ratio, crystallizing and quenching for later use; (4) preparing the silicon source, the phosphorus source, alkaline, the organic template agent and water into a mixture according to mole ratio; (5) adding the gel mixture obtained in the step (3) into a sealed kettle filled with the mixture in the step (4) and crystallizing; (6) washing the product obtained in the step (5) with deionized water, drying and roasting so as to obtain a compound molecular sieve; (7) carrying out ion exchanging on the compound molecular sieve, filtering, roasting, and adding a binding agent for forming so as to obtain a hydrogen-type compound molecular sieve catalyst. The technical scheme provided by the invention can effectively improve the selectivity and yield of propylene in the MTP reaction.

Description

technical field [0001] The invention relates to a composite molecular sieve catalyst used for methanol to prepare propylene, in particular to a composite structure bimolecular sieve catalyst synthesized directional in a very concentrated system and its application in methanol conversion to prepare propylene. Background technique [0002] Propylene is one of the most important basic organic raw materials next to ethylene. With the year-by-year expansion of the application field of its derivatives, the demand is increasing day by day, but the lack of petroleum resources makes it urgent to develop a non-petroleum-based propylene preparation process. Propane dehydrogenation to propylene technology and ethylene and butene disproportionation to propylene technology can produce propylene with high selectivity, but the former uses propane-rich natural gas as a raw material, which is limited geographically, and the latter needs to consume ethylene resources, which are not in line wit...

Claims

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Application Information

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IPC IPC(8): B01J29/85B01J35/02C07C11/06C07C1/20
CPCY02P20/52
Inventor 龚旭辉
Owner 洛阳市科创石化科技开发有限公司