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One-step method for producing olefins from syngas

A technology for synthesis gas and olefin production, which can be used in chemical instruments and methods, hydrocarbon production from carbon oxides, physical/chemical process catalysts, etc., and can solve the problems of low selectivity, long conversion path, and high energy and material consumption.

Active Publication Date: 2021-11-30
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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  • One-step method for producing olefins from syngas
  • One-step method for producing olefins from syngas
  • One-step method for producing olefins from syngas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] In 2 o 3 +Cr 2 o 3 Catalyst is prepared as follows:

[0046] Weigh 1 mol of indium nitrate, dissolve it in 1000 mL of distilled water, then dissolve 3.2 mol of NaOH in 1000 mL of water, co-precipitate the two aqueous solutions, age at 70 °C for 3 h, filter and dry overnight at 100 °C, Calcined at 400°C for 12h to obtain In 2 o 3 catalyst.

[0047] Weigh 1mol of chromium nitrate, dissolve it in 1000mL of distilled water, then dissolve 3.2mol of NaOH in 1000mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3h, filter and dry overnight at 100°C, Calcined at 400°C for 12 hours to obtain Cr 2 o 3 catalyst.

[0048] AlPO 4 -5 catalyst is prepared as follows:

[0049] Pseudoboehmite, phosphoric acid, and tri-n-propylamine (TPA) were used as aluminum source, phosphorus source, and template agent respectively, and the molar ratio of Al 2 o 3 :P 2 o 5 :TPA:Ethanol:H 2 O=1:1.2:2.66:80:1000, add to the reactor and age for 2 hours, stir and cryst...

Embodiment 2

[0052] Cr 2 o 3 The catalyst was prepared according to [Example 1].

[0053] AlPO 4 -17 catalyst is prepared as follows:

[0054] Pseudoboehmite, phosphoric acid, and cyclohexylamine were used as aluminum source, phosphorus source, and template respectively, and the molar ratio of Al 2 o 3 :P 2 o 5 :CHA:HF:H 2 O=1:1:1:1:40, add to the reactor and age for 2 hours, stir and crystallize at 200°C for 72 hours, wash the obtained solid with deionized water until neutral, separate the solid, dry it, and put it in a muffle furnace Calcined at 550°C for 6 hours to obtain AlPO 4 -17 molecular sieves.

[0055] 0.77 g of prepared Cr 2 o 3 Catalyst and 0.7 g of prepared AlPO 4 -17 mixed, packed into a quartz reaction tube with an inner 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 ...

Embodiment 3

[0057] ZnGa 0.3 Catalyst is prepared as follows:

[0058] Weigh 1 mol of zinc nitrate and 0.3 mol of gallium nitrate, dissolve them in 1000 mL of distilled water, then dissolve 3 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 and bake at 400°C for 12 hours to obtain ZnGa 0.3 catalyst.

[0059] AlPO 4 -18 catalyst is prepared as follows:

[0060] Pseudoboehmite, phosphoric acid, and N,N-diisopropylethylamine are used as aluminum source, phosphorus source, and template agent respectively, and the molar ratio of Al 2 o 3 :P 2 o 5 :TPA:H 2 O=1:1:1:50, add to the reactor and age for 2 hours, stir and crystallize at 200°C for 48 hours, wash the obtained solid with deionized water until neutral, separate the solid, dry it, and put it in a muffle furnace for 550 ℃ roasting for 6 hours to get AlPO 4 -18 molecular sieve, its XRD spectrum is shown in figure 1 .

[0061] 0.77 g of p...

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Abstract

The invention belongs to the technical field of chemistry and chemical engineering, and specifically relates to a method for preparing olefins from syngas in one step, which mainly solves the problem that the selectivity of low-carbon olefins in the existing catalysts used for syngas to olefins is not high. Synthesis gas is reacted through a composite catalyst bed layer to obtain olefins, which is characterized in that the composite catalyst used includes phosphorus-aluminum molecular sieves, realizing the high-selectivity one-step preparation of olefins from synthesis gas. The catalyst solves the above problems well, and can efficiently, continuously and stably produce C 2 -C 4 Olefin products can be used in the industrial production of syngas to light olefins.

Description

technical field [0001] The invention belongs to the technical field of chemistry and chemical engineering, and specifically relates to a method for producing olefins by one-step synthesis gas, in particular to a composite catalyst of phosphorus-aluminum molecular sieves used for high-selectivity direct production of low-carbon olefins 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 re...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/04B01J29/83C07C11/04C07C11/06C07C11/08
CPCY02P20/52
Inventor 周海波刘苏王仰东刘畅
Owner CHINA PETROLEUM & CHEM CORP