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Fluid bed catalyst for producing ethylene and propylene by catalytic cracking method

A fluidized bed catalyst, catalytic cracking technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, molecular sieve catalysts, etc., can solve the problem of high reaction temperature, low yield, and poor catalyst activity Advanced problems, to achieve the effect of strong low temperature activity and good technical effect

Active Publication Date: 2008-06-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] The technical problem to be solved by the present invention is to overcome the problems of high reaction temperature, low activity and low yield of the catalyst used in the existing catalytic cracking technology

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Get 3 grams of ammonium metavanadate, add 100 milliliters of water, drop into 2 milliliters of 80% phosphoric acid, add 3 grams of oxalic acid, heat until the ammonium metavanadate dissolves, and obtain solution (I).

[0033] Another 5.89 g of bismuth nitrate was dissolved in 10 ml of 1:1 concentrated nitric acid to obtain a yellow solution. Another 30 grams of ammonium molybdate was dissolved in 200 milliliters of water, poured into the bismuth nitrate solution, and stirred to obtain solution (II).

[0034] Take 7.86 grams of cobalt nitrate, 5.58 grams of cerium nitrate, and 6.72 grams of calcium nitrate, and dissolve the three together in 250 milliliters of water to obtain solution (III).

[0035] Mix the solutions (I), (II) and (III), heat and stir in a water bath at 70-80°C, add 26 grams of silicon dioxide weighed, reflux for 5 hours, and then dry it with a spray dryer to form. After sieving the obtained powder, place it in a muffle furnace and raise the temperatur...

Embodiment 2

[0041]Take 284 grams of sodium metasilicate, dissolve it into solution A with 300 grams of distilled water, take 33.3 grams of aluminum sulfate, and make solution B with 100 grams of distilled water, slowly pour B solution into A solution, stir vigorously, and then add 24.4 grams of B Diamine, after stirring for 30 minutes, adjust the pH value at 11.5 with dilute sulfuric acid, and control the molar ratio of the sol: Si: Al: ethylenediamine: H 2 O=1:0.1:0.4:40, put the mixed solution in an autoclave, keep it at 180°C for 40 hours, then take it out and wash it twice, dry at 120°C for 4 hours, and roast at 550°C for 3 hours to prepare ZSM -5 and mordenite composite molecular sieve. Use ammonium nitrate solution with a concentration of 5%, exchange twice at 70°C, and then roast at 550°C for 3 hours, repeat twice to prepare hydrogen ZSM-5 / mordenite composite molecular sieve.

[0042] Prepare solution (I) with embodiment 1.

[0043] Another 30 g of ammonium molybdate, 7.61 g of i...

Embodiment 3

[0049] Take 284 grams of sodium metasilicate, dissolve it into solution A with 300 grams of distilled water, take 33.3 grams of aluminum sulfate, and make solution B with 100 grams of distilled water, slowly pour B solution into A solution, stir vigorously, and then add 24.4 grams of B Diamine, after stirring for 30 minutes, adjust the pH value at about 11 with dilute sulfuric acid, add 5 grams of Y zeolite seed crystals, and control the molar ratio of the sol: Si: Al: ethylenediamine: H 2 O=1:0.1:0.4:40, put the mixed solution into an autoclave, keep it at 120°C for 36 hours, then take it out and wash it twice, dry it at 120°C for 4 hours, and bake it at 550°C for 3 hours to obtain ZSM-5 Composite molecular sieve with Y zeolite. Using 5% ammonium nitrate solution, exchanging twice at 70°C, roasting at 550°C for 3 hours, and repeating twice to prepare hydrogen ZSM-5 / Y zeolite composite molecular sieve.

[0050] Prepare solution (I) with embodiment 1.

[0051] Another 30 g of...

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Abstract

The invention relates to a fluidized bed activator used for preparing ethene and propylene by catalyzing and cracking, mainly solving the problems of high temperature, low low-temperature activity of activator and low yield of ethene and propylene in the reaction in which ethene and ropylene are prepared by catalyzing and cracking with naphtha. The invention adopts at least one from SiO2 or composite molecular sieve as the carrier and contains the following compounds with chemical formula measured by atom ratio: Mo1.0VaAbBcCdOx; wherein, B is chosen from at least one of lanthanon; A is chosen from at least one out of VIII, IB, IIB, VIIB, VIB, IA or IIA in element periodic table; C is chosen from at least one activator technical proposal of Bi or P; the invention well solves the problems and can be applied in the industrial production, in which ethene and propylene are prepared by catalyzing and cracking with naphtha.

Description

technical field [0001] The invention relates to a fluidized bed catalyst for producing ethylene and propylene by catalytic cracking. Background technique [0002] With the development of society, the market demand for ethylene propylene in my country has increased sharply, the import volume of ethylene propylene and its downstream products has increased year by year, and the market share of domestic products is less than half. At present, ethylene in the world mainly uses naphtha (or ethane) as raw material and adopts steam pyrolysis technology (at a temperature of about 800°C) to produce ethylene, and its output exceeds 90% of the total output. Compared with steam thermal cracking, the reaction temperature of catalytic cracking is about 50-200℃ lower than that of standard cracking reaction, so the energy consumption is less than that of ordinary steam cracking, and the coking rate of the inner wall of cracking furnace tube will be reduced, which can prolong the operation pe...

Claims

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Application Information

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IPC IPC(8): B01J23/882B01J29/80C07C11/04C07C11/06
CPCY02P20/52
Inventor 陈亮谢在库马广伟姚晖胡永君
Owner CHINA PETROLEUM & CHEM CORP