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Combination catalyst for the production of light olefins

A technology combining catalysts and carbon olefins, applied in the direction of carbon compound catalysts, catalysts, molecular sieve catalysts, etc., can solve the problems of high energy consumption and material consumption, low catalyst activity, long conversion path, etc.

Active Publication Date: 2020-11-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] CN1683079A relates to a catalyst for the reaction of methanol to olefins, which mainly solves the problem of low catalyst activity, low selectivity of ethylene, propylene and butene, low selectivity of ethylene, propylene and butene, and low ethylene and the problem of low yield of propylene
[0010] In summary, although some of the existing technologies have a high CO conversion rate, the selectivity of olefins, especially the selectivity of low-carbon olefins, is low, which is far from the ideal goal of industrial application; some adopt two-step In this method, syngas needs to be converted into methanol first, and then converted into light olefins. This technology has high selectivity, but the conversion path required for the two-step reaction is long, the reaction device is complicated, and the intermediate product / product needs to be separated many times. , large fixed investment, high consumption of energy and materials

Method used

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  • Combination catalyst for the production of light olefins
  • Combination catalyst for the production of light olefins

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] ZnCr 0.25 -Na0.06 Catalyst is prepared as follows:

[0036] Weigh 1 mol of zinc nitrate and 0.25 mol of chromium nitrate, dissolve them in 1000 mL of distilled water, then dissolve 4 mol of NaOH in 1000 mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3 hours, and filter at 100°C Dry overnight at 400°C for 12 hours. After the calcination is completed, the catalyst intermediate supports 0.03mol of Na 2 CO 3 , dried overnight at 80°C, and fired at 400°C for 1 hour to obtain ZnCr 0.25 -Na 0.06 catalyst.

[0037] The SAPO-34 catalyst is prepared according to the following steps: phosphoric acid, pseudoboehmite, ethyl orthosilicate, and morpholine are respectively used as phosphorus source, aluminum source, silicon source, template agent, and the molar ratio Al 2 o 3 :P 2 o 5 : SiO 2 :MOR:H 2 O=1:1:0.6:3:100, add to the reactor and age for 2 hours, stir and crystallize at 200°C for 24 hours, wash the obtained solid with deionized water until ...

Embodiment 2

[0040] ZnCr 3 -Cu 0.08 Li 0.8 Catalyst is prepared as follows:

[0041] Weigh 0.1mol of zinc nitrate, 0.3mol of chromium nitrate, 0.008mol of copper nitrate, dissolve in 1000mL of distilled water, then dissolve 2mol of KOH in 1000mL of water, co-precipitate the two aqueous solutions, and age at 70°C 3h, dried at 100°C overnight after filtration, and calcined at 400°C for 12h. After the calcination is completed, the catalyst intermediate supports 0.04 mol of Li 2 CO 3 , dried overnight at 80°C, and fired at 400°C for 1 hour to obtain ZnCr 3 -Cu 0.08 Li 0.8 catalyst.

[0042] The SAPO-34 catalyst was prepared according to [Example 1].

[0043] 1 gram of prepared ZnCr 0.25 -Na 0.06 Catalyst and 0.5 gram of prepared SAPO-34 were mixed, and packed into a quartz reaction tube with an internal diameter of 6 mm, the (n 氢气 :n 一氧化碳 =50:50) into the reaction tube, into the catalytic bed reaction, the reaction temperature is 400 ℃, the reaction system pressure is 4MPa, the ga...

Embodiment 3-1

[0045] ZnCr 1.5 -Ga 0.4 Catalyst is prepared as follows:

[0046] Weigh 0.1mol of zinc nitrate, 0.15mol of chromium nitrate, 0.04mol of gallium nitrate, dissolve in 1000mL of distilled water, then dissolve 2mol of KOH in 1000mL of water, co-precipitate the two aqueous solutions, and age at 70°C 3h, filtered and dried overnight at 100°C, and roasted at 400°C for 12h to obtain ZnCr 1.5 -Ga 0.4 catalyst.

[0047] The SAPO-34 catalyst was prepared according to [Example 1].

[0048] 0.75 g of prepared ZnCr 1.5 -Ga 0.4 Catalyst and 0.75 gram of prepared SAPO-34 were mixed, and packed into a quartz reaction tube with an internal diameter of 6 mm, the (n 氢气 :n 一氧化碳 =50:50) into the reaction tube, into the catalytic bed reaction, the reaction temperature is 400 ℃, the reaction system pressure is 4MPa, the gas volume space velocity is 4,000h -1 The reaction of syngas to light olefins is carried out under the conditions. The activity evaluation results are shown in Table 1.

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Abstract

The invention belongs to the technical field of chemical engineering, and is specifically a combined catalyst for producing low-carbon olefins from synthesis gas and its use. It mainly solves the problem of low low-carbon olefin selectivity of existing catalysts for producing olefins from synthesis gas. The catalyst couples the synthesis gas to methanol catalyst and the methanol to olefins catalyst to realize the one-step direct production of olefins from synthesis gas. The catalyst for methanol production from synthesis gas is an improved high-temperature and high-pressure ZnCr catalyst, with the general molecular formula of ZnCr a Cu b X c Y d O e , where At least one of ‑34, SAPO‑11 and SAPO‑18. This catalyst can better solve the above problems and produce C2-C4 olefin products efficiently, continuously and stably, and can be used in the industrial production of low-carbon olefins from synthesis gas.

Description

technical field [0001] The invention belongs to the technical field of chemistry and chemical engineering, and specifically relates to a combined catalyst for producing low-carbon olefins, in particular to a combined catalyst for directly producing low-carbon olefins with high selectivity from synthesis gas and a preparation method thereof. Background technique [0002] Low-carbon olefins represented by ethylene and propylene are important standards for measuring the level of a country's chemical industry, and are also important organic chemical raw materials, which can produce bulk synthetic materials such as plastics, synthetic resins, fibers, and rubber. In recent years, the production capacity of low-carbon olefins in my country has continued to increase, and the production has reached a considerable scale, but the import volume has continued to grow for a long time. In 2011, my country's ethylene and propylene production reached 15.275 million tons and 14.530 million to...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/85C07C1/04C07C11/04C07C11/06C07C11/08
CPCC07C1/043B01J29/85C07C2529/85C07C2523/83C07C2523/86C07C2523/26C07C2523/34B01J23/26B01J23/34B01J23/83B01J23/86B01J23/002B01J2523/00B01J35/19C07C11/04C07C11/06C07C11/08B01J2523/12B01J2523/27B01J2523/67B01J2523/11B01J2523/17B01J2523/32B01J2523/33B01J2523/72B01J2523/48B01J2523/13B01J2523/3706B01J2523/3712B01J2523/15Y02P20/52
Inventor 周海波刘苏刘畅王仰东
Owner CHINA PETROLEUM & CHEM CORP