Unlock instant, AI-driven research and patent intelligence for your innovation.

Method for producing propylene through catalytic cracking C4 olefin

A catalytic cracking and olefin technology, applied in the direction of hydrocarbon cracking, organic chemistry, etc., can solve problems affecting conversion rate, selectivity and high space velocity performance, etc.

Active Publication Date: 2007-02-21
CHINA PETROLEUM & CHEM CORP +1
View PDF10 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] The technical problem to be solved by the present invention is that the existence of the molecular sieve catalyst binder in the prior art affects its conversion rate, selectivity and high space velocity performance, and a new C 4 Method for producing propylene by catalytic cracking of olefins

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1 and comparative example 1

[0021] After crystallization, 150 grams of ZSM-5 molecular sieve a, washed and dried, was mixed with 18 grams of 40% (weight) silica sol, extruded and dried at 120° C. to obtain sample A-1.

[0022] Put 80 grams of sample A-1 into a closed reaction kettle, and treat it at a temperature of 110°C for 120 hours in an aqueous solution containing n-butylamine template agent. ml, 5 wt% NH 4 NO3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After the exchange, it was dried at 120°C and calcined at 600°C to obtain catalyst A with a crystallinity of 98.8%.

[0023] After 80 grams of sample A-1 was roasted, it was placed in 1000 milliliters of 5% by weight NH 4 NO 3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After the exchange, it was dried at 120°C and calcined at 600°C to obtain comparative catalyst A.

[0024] Catalyst A and A comparative catalyst were used respectively, and the mixed carbon fou...

Embodiment 2~5 and comparative example 2~3

[0027] After crystallization, 150 grams of ZSM-5 molecular sieve b, washed and dried, was mixed with 71 grams of 40% (weight) silica sol, extruded and dried at 120°C to obtain sample B-1.

[0028] Put 70 grams of sample B-1 into a closed reaction kettle, and treat it at a temperature of 150°C for 96 hours in the steam containing n-butylamine template agent. ml, 5 wt% NH 4 NO 3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After the exchange, catalyst B was obtained by drying at 120°C and calcining at 600°C with a crystallinity of 91.2%.

[0029] After 70 grams of sample B-1 was roasted, it was placed in 800 ml of 5% by weight NH 4 NO 3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After exchange, dry at 120°C and calcinate at 600°C to obtain comparative catalyst B.

[0030] Catalyst B and B comparative catalyst are used respectively, and the mixed carbon four after extraction from the ethyl...

Embodiment 6 and comparative example 4

[0033] After crystallization, 150 grams of ZSM-5 molecular sieve c, washed and dried, was mixed with 139 grams of 40% (weight) silica sol, extruded and dried at 120°C to obtain sample C-1.

[0034] Put 80 grams of sample C-1 into a closed reaction kettle, and treat it at 200°C for 24 hours in the steam containing the templating agent. % wt NH 4 NO 3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After the exchange, it was dried at 120°C and calcined at 600°C to obtain catalyst C with a crystallinity of 96.1%.

[0035] After 80 grams of sample C-1 was roasted, it was placed in 1000 ml of 5% by weight NH 4 NO 3 In the solution, exchange at a temperature of 85-90°C for 2 hours, and repeat 3 times. After the exchange, it was dried at 120°C and calcined at 600°C to obtain comparative catalyst C.

[0036] Catalysts C and C were used as comparative catalysts respectively, and the etherified C4 from the ethylene plant was used as the raw m...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
crystallinityaaaaaaaaaa
Login to View More

Abstract

This invention relates to a method for manufacturing propylene by C4 alkenes catalytic cracking. The method comprises contacting C4 alkenes with ZSM molecular sieve catalyst at 400-600 deg.C, 0-0.15 MPa, and weight space velocity of 2-50 h-1. The method solves the problems of low conversion rate, low selectivity and low space velocity of propylene caused by molecular sieve catalyst adhering, and can be used in propylene industrial manufacture of C4 alkenes catalytic cracking.

Description

technical field [0001] The present invention relates to a C 4 Process for the production of propylene by catalytic cracking of olefins, especially with regard to the use of novel binderless molecular sieve catalysts, C 4 A method for producing propylene by catalytic cracking of olefins. Background technique [0002] With the increase in global ethylene production and crude oil processing capacity, the C of ethylene plants and refineries 4 The number of olefinic hydrocarbons will increase substantially. How to make good use of this considerable amount of precious hydrocarbon resources, increase their added value, and improve the efficiency of petrochemical enterprises has become an increasingly urgent task. At the same time, experts predict strong demand for propylene, driven by growth in demand for polypropylene and alkylaromatic compounds. Therefore put C 4 The conversion of olefins to propylene is a promising process. On the one hand, this...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/06C07C4/06
Inventor 谢在库滕加伟金文清赵国良
Owner CHINA PETROLEUM & CHEM CORP