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Sulfur tail gas hydrogenation catalyst and preparation method thereof

A hydrogenation catalyst and tail gas technology, applied in the direction of sulfur preparation/purification, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of poor anti-coking performance and poor oxygen resistance of catalysts , pollute the environment and other issues, and achieve the effects of strong antioxidant capacity, significant economic and social benefits, and high water vapor content

Active Publication Date: 2021-08-10
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst has poor oxygen resistance. At the same time, ammonia water is used in the preparation process, which has the problem of ammonia escape and pollutes the environment.
[0005] "CN101108348A" discloses a nickel-based Claus tail gas hydrogenation catalyst and its preparation method. The catalyst consists of three components: main active component, auxiliary active component and alumina. The main active component is nickel oxide. The auxiliary active component is any one of chromium oxide, copper oxide, and iron oxide or a mixture of more than one of them. Although it has the characteristics of good low-temperature catalytic activity, it has poor anti-coking performance.

Method used

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  • Sulfur tail gas hydrogenation catalyst and preparation method thereof
  • Sulfur tail gas hydrogenation catalyst and preparation method thereof
  • Sulfur tail gas hydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Put the diatomite in 95°C water and stir to remove the sediment, lower the temperature to 5°C, treat it with 20% phosphoric acid at an acid / soil ratio of 1 for 5 hours, filter, dry, and roast at 400°C to obtain modified diatomite.

[0038] Get 25 grams of above-mentioned modified diatomite, pseudo-boehmite (specific surface area is 300m 2 / g) 200 grams, 3 grams of calcium oxide, 4 grams of asparagus powder, 28 grams of nitric acid, 11.22 grams of ferric nitrate nonahydrate dissolved in 270 grams of deionized water and mixed evenly, extruded on the extruder, and dried at 120 ° C 4 hours, and calcined at 500° C. for 4 hours to obtain a catalyst carrier.

[0039] Take 5ml of phosphoric acid and add it to 80ml of deionized water, mix 1.34g of basic nickel carbonate and 10g of molybdenum trioxide evenly, add it into the aqueous solution containing phosphoric acid, stir until it is completely dissolved, impregnate the carrier with equal volume of the above immersion solution ...

Embodiment 2

[0045] Put the diatomite in 95°C water and stir to remove the sediment, lower the temperature to 15°C, treat it with 25% phosphoric acid at an acid / soil ratio of 1 for 8 hours, filter, dry, and roast at 450°C to obtain modified diatomite.

[0046] Get above-mentioned modified diatomite 20 grams, pseudo-boehmite (specific surface area is 300m 2 / g) 180 grams, 3 grams of barium oxide, 4 grams of asparagus powder, 28 grams of nitric acid, 33.66 grams of ferric nitrate nonahydrate dissolved in 263 grams of deionized water, mixed evenly, extruded on the extruder, and dried at 120 ° C 4 hours, calcined at 550° C. for 4 hours to obtain a catalyst carrier.

[0047] Take 5ml of phosphoric acid and add it to 80ml of deionized water, mix 10.05g of basic nickel carbonate and 40g of molybdenum trioxide evenly, add it into the aqueous solution containing phosphoric acid, stir until it is completely dissolved, impregnate the carrier with an equal volume of the above immersion solution for 2 ...

Embodiment 3

[0053] Put the diatomite in 95°C water and stir to remove the sediment, lower the temperature to 40°C, treat it with 40% phosphoric acid at an acid / soil ratio of 1 for 12 hours, filter, dry, and roast at 600°C to obtain modified diatomite.

[0054] Get above-mentioned modified diatomite 20 grams, pseudo-boehmite (specific surface area is 300m 2 / g) 190 grams, 3 grams of calcium oxide, 8ml polyethylene glycol, 28 grams of nitric acid, 22.44 grams of ferric nitrate nonahydrate dissolved in 267 grams of deionized water and mixed evenly, extruded on the extruder, dried at 120 ° C 4 hours, and calcined at 500° C. for 6 hours to obtain a catalyst carrier.

[0055] Take 5ml of citric acid and add it to 80ml of deionized water, mix 3.35g of basic nickel carbonate and 24.52g of ammonium heptamolybdate tetrahydrate evenly, add it to the aqueous solution containing citric acid, stir until it is completely dissolved, and impregnate the carrier with an equal volume of the above immersion s...

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Abstract

The invention belongs to the technical field of sulfur recovery, and in particular relates to a sulfur tail gas hydrogenation catalyst and a preparation method thereof. The raw materials of the carrier include pseudo-boehmite, modified diatomite and antioxidant additives, and the active components are molybdenum, nickel and iron; the modified diatomite is as follows: diatomite is treated with phosphoric acid, filtered, Roasting after drying to obtain modified diatomite; the specific surface area of ​​diatomite is greater than 50m 2 / g. The invention further increases the oxygen resistance by adding low-temperature catalytic active components and anti-oxidation additives, and has the characteristics of strong anti-oxidation ability, high low-temperature activity, anti-coke and adaptability to high water vapor content, and can be used to induce liquid sulfur removal The gas enters the hydrogenation reactor for treatment, which meets the new national environmental protection standards to be implemented, and has significant economic and social benefits; it can be widely used in various sulfur recovery tail gas treatment devices.

Description

technical field [0001] The invention belongs to the technical field of sulfur recovery, and in particular relates to a sulfur tail gas hydrogenation catalyst and a preparation method thereof. Background technique [0002] In recent years, some large-scale high-sulfur gas fields in my country have been developed one after another, which puts forward new requirements for natural gas purification process. So far, the Puguang Gas Field Natural Gas Purification Plant of Sinopec Zhongyuan Oilfield is the largest gas purification plant in my country. The plant has an annual processing capacity of 12 billion cubic meters of mixed natural gas and an annual sulfur production capacity of 2.4 million tons. It has six sets (12 trains) with a single train scale of 20 The 10,000-ton / year sulfur recovery device adopts the technology package of Black&Veatch Company in the United States, and the supporting catalysts are all imported. Imported catalysts are expensive, and it costs a lot to repl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755C01B17/04
CPCB01J23/002B01J23/755B01J2523/00C01B17/04B01J2523/842B01J2523/847B01J2523/68
Inventor 刘爱华商剑峰刘增让陈平文刘剑利陶卫东徐翠翠
Owner CHINA PETROLEUM & CHEM CORP
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