Production process of vulcanization-free gas hydrogenation catalyst

A hydrogenation catalyst and production process technology, applied in the field of coal chemical industry, can solve the problems of shortened service life, long start-up time, environmental pollution, etc., and achieve the effect of easy purification and low exhaust gas emission

Active Publication Date: 2021-11-26
WUHAN KELIN FINE CHEM
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Problems solved by technology

The active components in the oxidized state of the catalyst in the lower layer that are not penetrated by sulfur may be 2 , CO reduction, the higher the temperature, the easier the reduction, vulcanization is a strong exothermic reaction, the temperature rise caused by the vulcanization of the upper layer catalyst will often make the lower layer catalyst reduce, the reduced catalyst is difficult to fully vulcanize, affecting the hydrogenation activity
[0012] 2. It brings about the problem of sulfide exhaust gas treatment and emission
Vulcanization waste gas is directly vented and discharged, which not only seriously pollutes the environment, but also causes high temperature, high flow, and high H 2 The sulfide gas with S content will also cause the venting to catch fire, causing safety hazards, and often interrupt the vulcanization process, making the vulcanization insufficient, reducing the activity of the catalyst, and shortening the service life.
[0013] 3. Contamination of reactors, pipelines, valves and other equipment
In the usual dry vulcanization in the device, it is inevitable that the vulcanization is shared with some pipe fittings in normal production. The H in the vulcanization gas 2 The S content is very high, and the high temperature strengthening period can reach 10~40g / m 3 , high-concentration and high-temperature sulfur gas can easily contaminate reactors, pipelines, valves and other equipment
Especially for the secondary hydrogenation, it is too close to the pipeline equipment required by the ppb level of sulfur content. Once pollution is caused, it will be very troublesome
[0014] 4. Long working hours affect production
The presulfurized hydrogenation catalysts disclosed in patents CN201110350766, CN201110350791, CN201310358571, and CN201110350794 generally need to be activated before use, and there is widespread heat release and sulfur release during activation. The emission problem is actually not much different from that of on-site vulcanization, and it is impossible to achieve ready-to-use

Method used

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  • Production process of vulcanization-free gas hydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] Production 15 m 3 Sulfur-free FeMo prehydrogenation catalyst.

[0048] ⑴Preparation of FeMo / Al 2 o 3 Gas hydrogenation catalyst. Weigh 0.93 tons of Fe(NO 3 ) 3 9H 2 O, 0.97 tons (NH 4 ) 6 Mo 7 o 24 4H 2 O, with 4.92m 3 Dissolve in water, adjust the pH value of the impregnating solution 7 to 5.5 with phosphoric acid, select 9.34 tons of spherical Al with a strength of 120N / piece and a water capacity of 65%. 2 o 3Carrier 8, equal-volume impregnation for 1 hour and 40 minutes, drying at 100°C for 3 hours-9 (the reference number is drying instead of baking, if there is no reference number, baking and drying do not matter), 350°C roasting for 4 hours-10.

[0049] ⑵ vulcanization. The catalyst prepared by step (1) is filled in the vulcanization tower 11, and the upper layer of the hydrolysis reaction tower 6 is filled with 3m 3 Ti / Al protective agent, 12m in the lower layer 3 The hydrolysis catalyst supported by magnesia-aluminum spinel, the gas enters from th...

Embodiment 2

[0054] Production 30 m 3 Sulfur-free CoMo gas hydrogenation catalyst.

[0055] ⑴Preparation of CoMo / Al 2 o 3 Gas hydrogenation catalyst. Weigh 1.84 tons of Co(NO 3 ) 2 ·6H 2 O, 2.19 tons (NH 4 ) 6 Mo 7 o 24 4H 2 O, use 11.05m 3 Dissolve in water, adjust the pH value of the impregnating solution 7 to 6.2 with phosphoric acid, select 18.69 tons of spherical Al with a strength of 142N / piece and a water capacity of 71%. 2 o 3 Carrier 8, impregnated with equal volume for 1 hour and 40 minutes, dried at 110°C for 2.5 hours-9, and calcined at 450°C for 3.2 hours-10.

[0056] ⑵ vulcanization. The catalyst prepared by step (1) is filled in the vulcanization tower 11, and the upper layer of the hydrolysis reaction tower 6 is filled with 12m 3 Ti / Al protective agent, 18m in the lower layer 3 The hydrolysis catalyst supported by magnesia-aluminum spinel, the gas enters from the top and exits from the bottom. Prepare 1000LCS 2 , 290kg water vapor. First, the temperature ...

Embodiment 3

[0061] Production 20 m 3 Sulfur-free NiMo coke oven gas secondary hydrogenation catalyst.

[0062] ⑴ Preparation of NiMo / Al 2 o 3 Gas hydrogenation catalyst. Weigh 1.63 tons of Ni (NO 3 ) 2 ·6H 2 O, 1.68 tons (NH 4 ) 6 Mo 7 o 24 4H 2 O, with 7.74m 3 Dissolved in water, phosphoric acid adjusts the pH of the impregnation solution to 6.8, and selects 12.21 tons of spherical Al with a strength of 165N / piece and a water capacity of 78%. 2 o 3 Carrier 8 was impregnated with equal volume for 1 hour and 40 minutes, dried at 120°C for 2 hours-9, and calcined at 550°C for 2.5 hours-10.

[0063] ⑵ vulcanization. The catalyst prepared by step (1) is filled in the vulcanization tower 11, and the upper layer of the hydrolysis reaction tower 6 is filled with 6 m 3 Ti / Al protective agent, 14m in the lower layer 3 The hydrolysis catalyst supported by magnesia-aluminum spinel, the gas enters from the top and exits from the bottom. Prepare 800LCS 2 , 230kg water vapor. First, ...

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Abstract

The invention discloses a production process of a vulcanization-free gas hydrogenation catalyst. The preparation method comprises the following steps: preparing FeMo / Al2O3, CoMo / Al2O3 and NiMo / Al2O3 gas hydrogenation catalysts by an equivalent-volume impregnation method, carrying out ex-situ prevulcanization on the catalysts by adopting a limited hydrogen control circulating vulcanization process, removing H2S from sulfur discharge tail gas through Cu / C or Cu / Al2O3, emptying, and passivating after sulfur discharge is finished. The process is flexible to operate, low in hydrogen consumption, high in utilization rate of the vulcanizing agent, short in vulcanizing time and good in vulcanizing effect. In the whole ex-situ prevulcanization process, the waste gas emission amount is small, and the waste gas component is simpler than that of coke-oven gas and is easy to purify; Cu / C or Cu / Al2O3 is used as a gas mercury removal agent after being desulfurized, so that the method is green and economical.

Description

technical field [0001] The invention relates to a production process of a sulfide-free gas hydrogenation catalyst, which belongs to the field of coal chemical industry. Background technique [0002] my country is a big country of coke production, and a large amount of coke oven gas is produced as a by-product. The production of methanol / LNG from coke oven gas has a good application prospect. Methanol synthesis catalysts and methanation catalysts are used in the production of methanol and LNG. The active components are Cu and Ni respectively, which are easily deactivated by reaction with sulfide. Therefore, it is of great significance to remove various sulfides in coke oven gas. [0003] The sulfur content in coke oven gas is related to the total sulfur content of the coal charge. Generally, dry coal contains 0.5-1.2% (weight) of total sulfur, of which 20-45% is transferred to coke oven gas, and hydrogen sulfide accounts for the total sulfur content. More than 95% of the s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/051B01J37/02B01J37/08B01J37/20B01D53/86B01D53/52
CPCB01J27/0515B01J37/0201B01J37/088B01J37/20B01D53/8612B01D2257/304B01D2258/02Y02P20/52
Inventor 张先茂王天元王泽王海洋王国兴金建涛赵志杰王骥飞郑敏陈凯彭渺郑峰伟
Owner WUHAN KELIN FINE CHEM
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