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Method for co-producing isobutene from n-butene to gasoline components

A technology of n-butene and isobutene, applied in chemical instruments and methods, petroleum industry, isomerization hydrocarbon production, etc., can solve the problem of low yield of isobutene

Active Publication Date: 2019-06-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems to be solved by the present invention is the low yield of isobutene from gasoline components co-produced on molecular sieve catalysts in the prior art, and provides a method for co-producing isobutene from n-butene to gasoline components

Method used

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  • Method for co-producing isobutene from n-butene to gasoline components
  • Method for co-producing isobutene from n-butene to gasoline components
  • Method for co-producing isobutene from n-butene to gasoline components

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Catalyst preparation: NaZSM-35 molecular sieve raw powder (SiO 2 / Al 2 o 3 The ratio is 22) to remove the templating agent by calcining at 550° C. for 4 hours. The obtained material was treated with 0.3M NaOH at 75° C. for 2 h with alkali, then filtered and dried with suction to obtain an alkali-modified molecular sieve. The material obtained by alkali treatment modification is mixed with alumina at a weight ratio of 1:0.5. Add nitric acid solution to the mixture, knead and extrude, and cut into pellets after drying and roasting. After ammonium exchange, the obtained material was heated at 550°C and space velocity for 2 hours -1 Under the condition of water vapor treatment for 2 hours, the catalyst was prepared.

[0034] Catalyst evaluation: using ether post-mixed C4 (n-butene content 93.1%) as raw material, the raw material composition is shown in Table 1; at a temperature of 420 ° C, a reaction pressure of 0.1 MPa, and a C4 liquid volume space velocity of 2 hours...

Embodiment 2

[0057] Catalyst preparation: NaZSM-35 molecular sieve raw powder (SiO 2 / Al 2 o 3 The ratio is 20) to remove the templating agent by calcining at 550° C. for 4 hours. The obtained material was treated with 0.3M NaOH at 75° C. for 2 h with alkali, then filtered and dried with suction to obtain an alkali-modified molecular sieve. The material obtained by alkali treatment modification is mixed with alumina at a weight ratio of 1:0.5. Add nitric acid solution to the mixture, knead and extrude, and cut into pellets after drying and roasting. After ammonium exchange, the obtained material was heated at 550°C and space velocity for 2 hours -1 Under the condition of water vapor treatment for 2 hours, the catalyst was prepared.

[0058] Catalyst evaluation: using ether post-mixed C4 (n-butene content 93.1%) as raw material, the raw material composition is shown in Table 1; at a temperature of 420 ° C, a reaction pressure of 0.1 MPa, and a C4 liquid volume space velocity of 2 hours...

Embodiment 3

[0060] Catalyst preparation: NaZSM-35 molecular sieve raw powder (SiO 2 / Al 2 o 3 The ratio is 20) to remove the templating agent by calcining at 550° C. for 4 hours. The obtained material was treated with 0.3M NaOH at 75° C. for 2 h with alkali, then filtered and dried with suction to obtain an alkali-modified molecular sieve. The material obtained by alkali treatment modification is mixed with alumina at a weight ratio of 1:0.5. Add nitric acid solution to the mixture, knead and extrude, and cut into pellets after drying and roasting. After ammonium exchange, the obtained material was heated at 550°C and space velocity for 2 hours -1 Under the condition of water vapor treatment for 2 hours, the catalyst was prepared.

[0061] Catalyst evaluation: using ether post-mixed C4 (n-butene content 93.1%) as raw material, the raw material composition is shown in Table 1; at a temperature of 420 ° C, a reaction pressure of 0.1 MPa, and a C4 liquid volume space velocity of 2 hours...

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Abstract

The invention relates to a method for preparing gasoline component together with isobutylene from n-butylene and mainly solves the problems of low yield and low isobutylene content of gasoline liquid oligomerized from n-butylene in the prior art. By adopting the technical scheme that the method for preparing the gasoline components together with the isobutylene from the n-butylene comprises the following step of carrying out reaction on the n-butylene under the existence of a ZSM-35 catalyst, thus preparing the gasoline components together with the isobutylene, wherein a molar ratio of SiO2 to Al2O3 of the ZSM-35 catalyst is 15 to 40, the reaction temperature is 400 to 500 DEG C, and the reaction pressure is 0 to 0.1MPa, the problem is well solved, and the method can be used for industrial production of preparing the gasoline component together with the isobutylene from the n-butylene.

Description

technical field [0001] The invention relates to a method for co-producing isobutene from n-butene to gasoline components. Background technique [0002] C4 low-carbon olefins and mixed hydrocarbons containing C4 low-carbon olefins are by-products of the petrochemical and refining industries, produced in ethylene engineering, refineries and natural gas purification processes. Except for a small number of components in the mixed carbon tetraolefins that are extracted and used as chemical raw materials, most of them are used as cheap fuels, mainly due to the high fuel prices. With the successful implementation of my country's western development strategy and the West-East Gas Transmission Project, as well as the large-scale use of the technology of synthesizing dimethyl ether from coal, mixed carbon tetraolefins will eventually be squeezed out by pipeline natural gas and other cheaper fuels for civilian use market. Converting these mixed carbon tetraolefins into gasoline compon...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G50/00B01J29/65C07C5/27C07C11/09
CPCB01J29/65B01J2229/37B01J2229/38C07C5/2775C07C2529/65C10G50/00C07C11/09
Inventor 李云龙吕建刚金照生
Owner CHINA PETROLEUM & CHEM CORP