Olefin preparation method comprising reduction pretreatment

A pretreatment, olefin technology, applied in chemical instruments and methods, catalyst activation/preparation, dehydrogenation to hydrocarbons, etc., can solve the problems of unfavorable overall process performance, low selectivity, low catalyst life process stability, etc. The number of compressor stages, the effect of saving energy costs and reducing equipment costs

Inactive Publication Date: 2020-01-10
GAS CO +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] However, even in the process of limiting the contact time between the hydrocarbon and the catalyst, at the initial stage of the reaction, the hydrocarbon reacts with the catalyst to rapidly generate by-products such as carbon dioxide and carbon monoxide that are not olefins. Although the conversion rate of the reaction raw material is high, there is a high selectivity. low disadvantage
In addition, the process stability that directly affects the life of the catalyst is low, and there are still problems that have an adverse effect on the overall process performance

Method used

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  • Olefin preparation method comprising reduction pretreatment
  • Olefin preparation method comprising reduction pretreatment
  • Olefin preparation method comprising reduction pretreatment

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preparation example Construction

[0058] The production process of the invention relates in particular to a dehydrogenation process for the production of olefins from hydrocarbons. In particular, the production method of the present invention can be used in the process of producing propylene by dehydrogenating propane. At this time, when preparing the olefins, a catalyst, especially a metal oxide catalyst, is usually used. In the prior art, when the olefins were prepared from hydrocarbons through the catalyst, the temperature of the catalyst showed a sharp change in the initial stage of the reaction with the reaction time. increasing trend, followed by a gradual decrease in temperature.

[0059] At this time, when considering the change in catalyst temperature over time, the conversion rate, and the selectivity of olefins, the conversion rate reaches 100% in the early stage of the reaction when the catalyst temperature is increased, but most of the carbon dioxide is produced by the oxidation reaction of the hy...

Embodiment 1

[0111] Olefin Preparation 1

[0112] Step 1: Before the catalyst prepared above is supplied to the reaction section through the catalyst supply section, hydrogen (H 2 ) is supplied to the catalyst pretreatment section through the reducing gas supply section, and the temperature of the catalyst passing through the catalyst supply section is increased by 10 to 40°C to about 640 to 660°C due to the pretreatment.

[0113] Step 2: The catalyst heated up in the step 1 was supplied to the riser so as to have a space velocity (WHSV: ml / gcat.hr) 4240, and propane was supplied to the riser through the hydrocarbon supply to produce propylene.

[0114] Step 3: The catalyst reacted with the propylene prepared in the step 2 is separated in the separation part to obtain propylene, and the reacted catalyst is resupplied to the regenerator for regeneration.

[0115] Step 4: The catalyst regenerated in the regenerator is supplied to the riser after the process of step 1 is repeated.

Embodiment 2

[0116] Olefin Preparation 2

[0117] In step 1 of Example 1 of the present invention, the reduction time was changed to 300 seconds, and the space velocity (WHSV: ml / gcat.hr) was changed to 8400, except that it was performed in the same manner as in Example 1 to prepare Propylene.

[0118] When hydrogen is supplied as a reducing gas, the temperature of the catalyst in the propane dehydrogenation reaction is measured, the more the amount of hydrogen required for the pretreatment of the active oxygen carrier increases, the temperature of the catalytic bed due to the rapid combustion reaction at the initial stage of the reaction in the dehydrogenation reaction The more the increase decreases.

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Abstract

The present invention enables more effective increase in an olefin yield by means of applying a novel catalyst and reduction pretreatment to a circulating fluidized bed process, which uses a high-speed fluidized bed, and thus enhancing the selectivity and yield. By means of the reduction pretreatment, hydrocarbon is prevented from coming into contact with a catalyst during the early part of a reaction and thus is prevented from converting into an unnecessary by-product. Therefore, the conversion from the hydrocarbon to olefin is simple, the catalyst can be efficiently utilized, and unnecessaryapparatuses are reduced and the facility cost can be lowered. Since the catalyst is directly heated by means of a catalytic reaction of the pretreatment process, the energy cost for increasing catalyst reaction temperature can be saved compared to the existing indirect heating. Since the number of compressor gears is reduced by means of positive pressure operation, investment cost for an apparatus is reduced.

Description

technical field [0001] The present invention relates to a process for the production of olefins utilizing a circulating fluidized bed process including reducing pretreatment. Background technique [0002] Olefins such as ethylene, propylene are widely used in the petrochemical industry. Generally, such olefins are obtained in the pyrolysis process of naphtha. However, due to the shale gas revolution, etc., the competitiveness of processes using lower hydrocarbons as raw materials has gradually increased, and an on-purpose olefin production process through a catalytic dehydrogenation process is required. [0003] The catalytic contact dehydrogenation process required for olefin production uses various types of lower hydrocarbon compounds as raw materials, showing excellent olefin production yields. However, in the fixed-bed commercial dehydrogenation process, although the yield of olefins is high at the initial stage of the reaction when the hydrocarbons are in contact with...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/32C07C11/06C07C9/08B01J37/16
CPCC07C2523/26C07C2521/06C07C2521/04C07C5/324B01J23/26B01J37/0242B01J37/0207B01J23/92B01J37/18B01J35/023Y02P20/584Y02P20/52C07C11/06C07C5/322C07C9/08B01J37/16C07C2523/02B01J2208/00557B01J2208/00539B01J35/026C07C5/32
Inventor 朴德守洪雄基安亨赞崔源春朴容起
Owner GAS CO
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