Work starting method for hydrogenation process

A process and technology for starting oil, applied in refining to remove heteroatoms, etc., can solve the problems of affecting the timely start of hydrogenation units, increase processing costs, and take a long time to achieve shortened production cycle, efficient utilization, and reduced usage. Effect

Active Publication Date: 2013-01-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its main disadvantage is that the amount of catalyst that needs to be presulfurized outside the device is large, the pretreatment process outside the device takes a long time, and the processing cost increases. In the case of short delivery time of presulfurized catalyst or large production tasks , which may affect the on-time start-up of the hydrogenation unit

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] 50 g of the catalyst 100 g is impregnated in 10 g of organic solvent (organic solvent is coking kerosene fraction), the ratio of carbon number 9 to 12 in the organic solvent is not less than 50%, and the immersion time is 1 hour. Elemental sulfur 10g and 5g (NH 4 ) 2 S mixed. The impregnated catalyst was mixed with a vulcanizing agent, treated at 180° C. for 3 hours, and cooled naturally to obtain a pre-sulfided catalyst A. Mix the obtained presulfurized catalyst A with the remaining 50g of the unpresulfurized catalyst evenly, put it into a small reactor, and make it airtight, adjust the hydrogen partial pressure to 6.0MPa and start to raise the temperature at 20°C / h, and start to rise to 80°C Add vulcanized oil from the bottom of the reactor to carry out closed-circuit circulation of the device. The vulcanized oil is straight-run kerosene, and the conditions are hydrogen-oil volume ratio 350:1, volume space velocity 2.0h -1 . When the temperature rises to 270°C, ke...

Embodiment 2

[0051] 70 g of the catalyst 100 g was immersed in 10 g of organic solvent (the organic solvent was a mixture of coker kerosene fraction and cottonseed oil at a volume ratio of 2:1), and the soaking time was 1 hour. Elemental sulfur 10g and 5g (NH 4 ) 2 S mixed. The impregnated catalyst was mixed with a vulcanizing agent, treated at 150° C. for 5 hours, and cooled naturally to obtain a pre-sulfided catalyst A. The obtained vulcanizing agent A and the remaining non-presulfurized catalyst are respectively loaded into a small reactor, and the presulfurized catalyst is loaded in the lower part of the remaining oxidation state catalyst. The airtightness is qualified, the hydrogen partial pressure is adjusted to 6.0MPa, and the temperature is raised at 20°C / h. When it rises to 80°C, sulfurized oil is added from the bottom of the reactor to perform closed-circuit circulation of the device. The sulfurized oil is straight-run kerosene, and the condition is the volume ratio of hydrogen...

Embodiment 3

[0053] 30 g of the catalyst 100 g was immersed in 10 g of organic solvent (the organic solvent was a fraction of coked diesel oil), and the immersion time was 1 hour. Elemental sulfur 12g and 5g (NH 4 ) 2 S mixed. The impregnated catalyst was mixed with a vulcanizing agent, treated at 200° C. for 2 hours, and cooled naturally to obtain a pre-sulfided catalyst A. The obtained presulfided catalyst A and the oxidation state catalyst without presulfurization treatment are loaded into small reactors respectively, and the loading is to load the presulfided catalyst at the lower part of the oxidation state catalyst. The airtightness is qualified, the hydrogen partial pressure is adjusted to 6.0MPa, and the temperature is raised at 20°C / h. When it rises to 80°C, sulfurized oil is added from the bottom of the reactor to perform closed-circuit circulation of the device. The sulfurized oil is straight-run kerosene, and the condition is the volume ratio of hydrogen to oil. 350:1, volum...

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PUM

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Abstract

The invention discloses a work starting method for a hydrogenation process, which comprises the following steps of: taking the required oxidation state hydrogenation catalyst, and performing presulfurizing treatment on 20 to 80 weight percent of oxidation state hydrogenation catalyst, wherein a sulfurizing agent contained in partial oxidation state hydrogenation catalyst subjected to the presulfurizing treatment is 85 to 115 percent of theoretically required sulfur of all oxidation state hydrogenation catalyst; filling the presulfurized hydrogenation catalyst and the non-presulfurized hydrogenation catalyst in reactor, raising the temperature, introducing work starting oil and hydrogen into the reactor from the bottom of the reactor, keeping the constant temperature of between 200 and 280DEG C for 1 to 6 hours, and continuously raising the temperature to 300-340 DEG C to finish the work starting; and regulating to meet required conditions of hydrogenation reaction and performing normal hydrogenation operation. By the method, a part of the required catalyst can be subjected to the presulfurizing treatment only, the production period of presulfurizing the catalyst is reduced, the production cost is reduced, the economic performance is improved, and a proper work starting method can further improve the use performance of the catalyst.

Description

technical field [0001] The invention relates to a hydrogenation process start-up method, in particular to a hydrogenation process start-up method using both an oxidized hydrogenation refining catalyst and a sulfide-containing hydrogenation refining catalyst. technical background [0002] Due to the slow growth of crude oil production and increasingly heavy quality, the demand for clean oil products in today's world is increasing, and the product quality requirements are becoming more and more stringent. The hydrogenation process of petroleum distillate is the main technology for producing clean oil products at present, and the preparation technology of hydrogenation catalyst is the key of hydrogenation technology. The active metal component of the hydrogenation catalyst prepared by the common method is in an oxidized state. Before the oxidized state catalyst is used in industry, the active metal must be converted into a sulfurized state to have a high catalytic activity. Th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G45/04
Inventor 陈光高玉兰徐黎明李崇慧
Owner CHINA PETROLEUM & CHEM CORP
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