Unlock instant, AI-driven research and patent intelligence for your innovation.

Catalyst for removing carbon oxides in gas

A technology for carbon oxides and gas removal, which is used in the production of hydrocarbons from carbon oxides, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., and can solve the problems of poor stability and high operating temperature.

Active Publication Date: 2007-10-31
CHINA PETROLEUM & CHEM CORP +1
View PDF3 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In order to solve the problems of high service temperature and poor stability of existing catalysts for removing carbon oxides in gases, the present invention proposes a methanation catalyst with high activity and good stability at relatively low temperature and high space velocity

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Catalyst for removing carbon oxides in gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Weigh 120 grams of the commercially available BYAC-206 alumina carrier after roasting at 600°C for 4 hours, mix 8 grams of stannous chloride (SnCl 2 2H 2 O) Dissolved in 120 ml of ethanol to prepare an ethanol solution, impregnated the solution on the above carrier, and dried at 110°C for 4 hours to obtain A.

[0027] 450 grams of nickel nitrate [Ni(NO 3 ) 2 ·6H 2 O] and 52 grams of manganese nitrate were dissolved in 60 milliliters of water to make a solution, and this solution was impregnated on A. Dry at 110°C for 5 hours to obtain B.

[0028] Place B in a stainless steel tube with air and decompose it at 300° C. for 5 hours to obtain C, thus preparing Catalyst 1 of this example. The catalyst 1 contains 40% nickel, 5% manganese, 2% tin, and the balance is alumina carrier.

Embodiment 2

[0030] Take by weighing 240 grams of alumina carrier after roasting at 500 DEG C for 4 hours, the carrier is the same as the carrier in Example 1, except that 6.5 grams of tin protochloride (SnCl 2 2H 2 0) be dissolved in the ethanol of 260 milliliters, 345 grams of nickel nitrate and 160 grams of manganese nitrate are dissolved in the water of 310 milliliters and make solution respectively, the method of impregnating stannous chloride, nickel nitrate and manganese nitrate is identical with embodiment 1, Catalyst 2 of this example was obtained. After the same decomposition and reduction as in Example 1, the catalyst 2 contains 20% nickel, 1% tin, 10% manganese, and the balance is alumina carrier.

Embodiment 3

[0032] Take by weighing 160 grams of alumina carrier after roasting at 580 DEG C for 4 hours, the carrier is the same as the carrier in Example 1, and 32 grams of lanthanum nitrate [La(NO 3 ) 3 ·6H 2 O] was dissolved in 160 ml of water to make a solution, then impregnated onto the carrier, and dried at 110°C for 4 hours to obtain D.

[0033] 12 grams of stannous chloride (SnCl 2 2H 2 O) was dissolved in 160 ml of ethanol to make a solution, then dipped on D, and dried at 110°C for 4 hours to obtain E.

[0034] 450 grams of nickel nitrate [Ni(NO 3 ) 2 ·6H 2 O] and 140 g of manganese nitrate were dissolved in 100 ml of water to make a solution, which was then impregnated onto E. Dry at 110°C for 5 hours to obtain F.

[0035] Put F in a stainless steel tube with air and decompose it at 350°C for 5 hours. After reduction, the catalyst 3 contains 30% nickel, 10% manganese, 3% tin, 5% lanthanum, and the balance is alumina carrier.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
diameteraaaaaaaaaa
Login to View More

Abstract

The invention relates to the catalyst for removing impurities from gases to solve existing issue like high temperature and poor stability, improving adding catalyst element Tin and Mn, or La, Ce, or Yt or sodium with high reactive feature and fine stability.

Description

technical field [0001] The invention relates to a catalyst for removing carbon oxides in gas, in particular, the invention relates to a catalyst for removing a small amount of carbon oxides in the process gas of an ammonia plant or the hydrogen-rich gas of an ethylene plant. Background technique [0002] In existing catalysts for removing carbon oxides (methanation), generally, alumina-supported nickel is used or other catalytic promoter components are added on this basis. For example, RU 2185240 and RU 2186623 disclose catalytic promoter components chromium, potassium, Sodium, silicon, iron, calcium, magnesium; CN 1043639A discloses procatalyst components barium, sodium; CN 1016146B discloses procatalyst components rare earth elements and magnesium; US 4,132,672 discloses that the nickel content of catalyst is 25%, and It is iridium, its content is 0.1% to 1%, and the use temperature is 350-500°C. In addition, currently disclosed catalytic promoter components include chrom...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889C07C1/04C07C9/04
Inventor 戴伟王秀玲王红亚
Owner CHINA PETROLEUM & CHEM CORP