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Preparation method of dehydrogenation catalyst with low carbon deposition rate

A dehydrogenation catalyst and catalyst technology are applied in the field of preparation of propane dehydrogenation catalysts, which can solve the problems of difficulty in high dispersion, reduction of propane conversion rate and propylene selectivity, and deactivation of Pt active phase, and achieve stable active phase structure and process. The effect of mature technology and simple preparation method

Active Publication Date: 2020-12-01
LIAONING UNIVERSITY OF PETROLEUM AND CHEMICAL TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Supported Pt-based catalysts are widely used in propane dehydrogenation technology. The main problem currently facing is: the active component Pt is highly sensitive to heat at high temperatures, and it is easy to migrate, agglomerate or even sinter, making it difficult to maintain a high degree of dispersion, resulting in the Pt active phase catalysis. The efficiency drops rapidly, the amount of carbon deposits increases sharply, and even the Pt active phase is permanently deactivated due to sintering
Chinese patent CN200710020064.8 adopts the method of platinum-tin co-impregnation with molecular sieve as the carrier. After 720 hours of continuous operation, the conversion rate of propane is above 30%, and the selectivity of propylene is above 96%, but the activity drops rapidly after regeneration.
Although the catalysts in the prior art can exhibit certain performances under certain reaction conditions, they often cannot be balanced in terms of catalyst activity, stability, product selectivity and preparation economy.
In the traditional technology, the method of immersing Pt is often used, but the high temperature will greatly weaken the interaction between PtSn, which will eventually lead to the aggregation and growth of Pt particles, reducing the conversion rate of propane and the selectivity of propylene.

Method used

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  • Preparation method of dehydrogenation catalyst with low carbon deposition rate
  • Preparation method of dehydrogenation catalyst with low carbon deposition rate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 20ml, volume. A certain amount of sodium edetate was weighed and dissolved in deionized water, and the volume was adjusted to 30mL, and added to 20ml of Sn-containing alumina samples, aged for 4h, and dried at 80°C for 8h to obtain Sn and Na-containing alumina carrier samples. The dried sample is placed in a rotary evaporator, vacuumized, the absolute pressure of the system is controlled below 10kPa, the chloroplatinic acid solution is added to the above sample under normal pressure, and the vacuum treatment is continued, the absolute pressure of the system is controlled below 10kPa , heated to reflux, the heating temperature was 80°C, and the treatment time was 4h. Then the reflux was stopped and the solvent was evaporated to dryness. The sample obtained in the above steps ...

Embodiment 2

[0029] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 20ml. A certain amount of sodium edetate was weighed and dissolved in deionized water, and the volume was adjusted to 25mL, and added to 20ml of Sn-containing alumina sample, aged for 4h, and dried at 80°C for 8h to obtain a Sn, Na-containing alumina carrier sample. The dried sample is placed in a rotary evaporator, vacuumized, and the absolute pressure of the system is controlled below 10kPa. Under normal pressure, the chloroplatinic acid solution is added to the above sample, and the vacuum is continued. The absolute pressure of the system is controlled at Below 10kPa, heat to reflux, the heating temperature is 80°C, and the processing time is 4h. Then the reflux was stopped and the solvent was evaporated to dryness. The sample obtained in the above steps is placed in a tu...

Embodiment 3

[0031] Weigh an alumina carrier (spherical, 1 mm in diameter, 0.73 cm in pore volume) containing a certain amount of Sn 3 / g, specific surface area 232m 2 / g, the carrier used in the following examples) 20ml. Weigh a certain amount of sodium edetate and dissolve it in deionized water, dilute it to 35mL, and add it to the 20ml Sn-containing alumina sample. Aged for 4 hours, dried at 80°C for 8 hours to obtain an alumina carrier sample containing Sn and Na. The dried sample is placed in a rotary evaporator, vacuumized, and the absolute pressure of the system is controlled below 10kPa. Under normal pressure, the chloroplatinic acid solution is added to the above sample, and the vacuum is continued. The absolute pressure of the system is controlled at Below 10kPa, heat to reflux, the heating temperature is 70°C, and the processing time is 4h. Then the reflux was stopped and the solvent was evaporated to dryness. The sample obtained in the above steps is placed in a tubular hea...

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Abstract

The invention discloses a preparation method of a dehydrogenation catalyst with a low carbon deposition rate. The preparation method comprises the following steps: with Sn-containing aluminum oxide asa carrier, modifying the carrier with sodium ethylene diamine tetracetate; then loading an active component Pt, carrying out drying, and performing roasting by introducing a gas mixture of air and water vapor at 300-550 DEG C for 0.5-8 hours at an air speed of 200-2,000 h<-1>; and finally, loading an assistant Na, and carrying out drying and roasting to obtain the dehydrogenation catalyst for propane. According to the method, accurate anchoring of Sn and Pt can be promoted, high dispersion of Pt is achieved, and interaction between Pt and Sn is enhanced. Besides, the catalyst provided by theinvention can realize step-by-step impregnation of alkali metal and avoids the problem of an excessive coking amount of the catalyst and competitive adsorption of the alkali metal and Pt caused by excessive loss of alkali metal in the use process of the catalyst, promotes high dispersion of active components, and finally improves the selectivity of the target product propylene and the activity andstability of the catalyst.

Description

technical field [0001] The invention relates to a preparation method of a low carbon deposition rate dehydrogenation catalyst, in particular to a preparation method of a low carbon deposition rate propane dehydrogenation catalyst. Background technique [0002] Propylene is one of the most important basic raw materials for the chemical industry. In the past 5 years, the average annual growth rate was 1.8 times of GDP. The production capacity of propylene in the traditional process is seriously insufficient, and an alternative process for propylene production must be sought. Propane dehydrogenation to propylene technology (PDH) is the most competitive approach and will become one of the key technologies for countries to ensure their core competitiveness in the global competition of the petrochemical industry. [0003] Supported Pt-based catalysts are widely used in propane dehydrogenation technology. The main problem currently facing is: the active component Pt is highly sen...

Claims

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Application Information

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IPC IPC(8): B01J23/62B01J37/10B01J37/02B01J37/08C07C5/333C07C11/06
CPCB01J23/626B01J37/10B01J37/0207B01J37/082C07C5/3337C07C2523/62C07C11/06Y02P20/52
Inventor 张海娟高塬刘洁王卫强伍盛一
Owner LIAONING UNIVERSITY OF PETROLEUM AND CHEMICAL TECHNOLOGY