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Naphtha catalytic pyrolysis catalyst for preparing ethylene propylene

A catalytic cracking and ethylene propylene technology, which is applied in physical/chemical process catalysts, molecular sieve catalysts, hydrocarbon cracking and hydrocarbon production, etc. It can solve problems such as high operating temperature, low ethylene propylene yield, and low catalyst activity.

Active Publication Date: 2009-08-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is that the catalyst activity used in the existing naphtha catalytic cracking reaction is low, the yield of ethylene propylene is low, and the use temperature is high. A new method for producing ethylene by naphtha catalytic cracking Propylene Catalyst

Method used

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  • Naphtha catalytic pyrolysis catalyst for preparing ethylene propylene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] 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 a period of time, adjust the pH value at 11.5 with dilute sulfuric acid, and control the molar ratio of the sol: Si: Al: ethylamine: H 2 O=1:0.1:0.4:40, add 2.8 grams of Y zeolite seed crystals, put the mixed solution in an autoclave, keep it at 130°C for 40 hours, then take it out and wash it twice, dry at 120°C for 4 hours, and bake at 550°C 3 hours, made ZSM-5 / Y zeolite intergrowth molecular sieve, XRD diffraction pattern is as follows figure 1 As shown in curve 1, XRD diffraction quantification shows that the intergrown molecular sieve contains 94.5% ZSM-5 and 5.5% Y zeolite in weight percentage. Use ammonium nitrate solution with a concentration of 5%, exchange ...

Embodiment 2~4

[0020] According to the method of Example 1, the pH of the solution was controlled to be 10.5, 11 and 12 respectively, and ZSM-5 / Y zeolite intergrowth molecular sieves were synthesized respectively, which were respectively marked as FH-2, FH-3 and FH-4. The ratio of ZSM-5 and Y zeolite is shown in Table 4. Evaluation according to the method of Example 1, the results are shown in Table 5.

Embodiment 5~12

[0022] According to the method of Example 1, the different molar ratios of the solutions are controlled, and the ZSM-5 / Y zeolite intergrowth molecular sieves synthesized respectively are shown in Table 2, and the ratios of ZSM-5 and Y zeolite are shown in Table 4. Evaluation according to the method of Example 1, the results are shown in Table 5.

[0023] Table 2

[0024] Example Solution molar ratio Sample serial number Example 5 Si:Al:M:H 2 O=1:0.005:0.4:40 FH-5 Example 6 Si:Al:M:H2O=1:0.01:0.4:40 FH-6 Example 7 Si:Al:M:H 2 O=1:0.05:0.4:40 FH-7 Example 8 Si:Al:M:H 2 O=1:0.125:0.4:40 FH-8 Example 9 Si:Al:M:H 2 O=1:0.143:0.4:40 FH-9 Example 10 Si:Al:M:H 2 O=1:0.1:0.2:30 FH-10 Example 11 Si:Al:M:H 2 O=1:0.1:0.5:100 FH-11 Example 12 Si:Al:M:H 2 O=1:0.1:0.4:80 FH-12

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Abstract

The present invention relates to a catalyst used for manufacturing ethylene and propylene by naphtha catalytic pyrolysis which mainly solves the problems of high reaction temperature and low yield of catalyst to ethylene and propylene in the existing catalytic pyrolysis reaction. The present invention better solves the problems by adopting the technical proposal of taking a ZSM-5 / Y zeolite symbiosis molecular sieve as the catalyst. The present invention can be used for the industrial production of ethylene and propylene by naphtha catalytic pyrolysis.

Description

technical field [0001] The invention relates to a catalyst for producing ethylene propylene by catalytic cracking of naphtha. 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 period an...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/80C07C4/06C07C11/02
CPCY02P20/52
Inventor 马广伟谢在库胡永君肖景娴杨霞琴
Owner CHINA PETROLEUM & CHEM CORP