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

Residual oil hydrotreatment method for prolonging device operating cycle

A technology for residual oil hydrogenation and treatment method, which is applied in the fields of hydroprocessing process, hydrocarbon oil treatment, hydrocarbon oil cracking, etc. Problems such as pressure drop and reduction of the loading amount of the main catalyst can be achieved to increase the effect of backwashing, increase the porosity of the bed, and save the amount of consumption

Active Publication Date: 2012-01-11
CHINA PETROLEUM & CHEM CORP +1
View PDF4 Cites 43 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, even if the upflow reactor processes residual oil with high content of Fe, Ca, and particles for a long time, the pressure drop will increase due to the clogging of the upflow reactor. This phenomenon has occurred in industrial equipment
[0009] The industrialized method also has in addition: (1) increase the loading of protective agent, but this method has reduced the loading of main catalyst; The new catalyst continuously replaces the deactivated catalyst in the reactor to reduce the pressure drop and increase the metal content and carbon residue content of the raw oil, but the process is complex, the equipment investment is huge, and the operation is difficult; (3) HYVAHL of IFP in France The process adopts a switchable protective reactor in the hydrotreating of residual oil, and its advantage is that the heavy metal deposited on the catalyst in the protective reactor reaches 100% of the allowable amount of the catalyst, thereby reducing the generation of coke and metal deposition in the main reactor However, the investment in the process equipment is huge and the demand for the catalyst is large, which has not fundamentally solved the problem of metal deposition in the raw oil and the pressure drop of the reactor; (4) United Oil Company proposed the use of protective reactor Technology, add a protective reactor before the main reactor, fill the residual oil hydrodemetallization and hydrodesulfurization catalysts in the protective reactor, until the upper limit of the pressure drop of the protective reactor is allowed, and then throw away the protective reactor and take the bypass Until the whole unit replaces the catalyst to prolong the catalyst operation period
The above processes either require huge investment and are difficult to operate, or cannot fundamentally solve the pressure drop of the catalyst bed, and can only be operated at relatively low space velocities

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
  • Residual oil hydrotreatment method for prolonging device operating cycle
  • Residual oil hydrotreatment method for prolonging device operating cycle
  • Residual oil hydrotreatment method for prolonging device operating cycle

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-3

[0047] The test was carried out on the continuous high-pressure fixed-bed hydrogenation pilot plant imported from XYTEL Company of the United States. The device adopts three reactors connected in series, the raw material oil is from top to bottom, and a filtering device is added behind each reactor.

[0048] The catalyst used in the test is a full range of residual oil hydrotreating catalysts developed by Fushun Petrochemical Research Institute, including four types of catalysts with four different functions: desulfurization (HDS), demetallization (HDM), denitrogenation (HDN) and protective agent. The main physicochemical properties of the catalysts are listed in Table 1. The loading conditions of the catalysts in each reactor are as follows: one side fills CEN-2, CEN4, FZC-16, CEN-5, CEN6 from top to bottom, and the filling ratio (volume ratio) is: 1:1.5:2.2:2.4:13, The second reactor is filled with ZTS01 and ZTS02 from top to bottom, the filling ratio (volume ratio) is 7.5:...

Embodiment 4

[0069] Embodiment 4 adopts the same test device, catalyst loading scheme, standard operating conditions, and test feedstock oil as in Example 1 to carry out the test, and the device obtains the hydrogenation-generated oil value of 3000 hours of stable operation of the feedstock oil in Table 2 under standard operating conditions. For the impurity removal data and the pressure drop values ​​of each reverse, under the same conditions as the standard operating conditions, the reaction pressure and the hydrogen-to-oil ratio, the temperature of each reverse was reduced to 320°C at 10°C / h (space velocity 0.2), and after stabilization, the temperature was reduced to 0.24h -1 The volume space velocity is reversely introduced into the device containing vulcanizing agent (CS 2 ) heavy diesel oil (Saudi Arabia's third line), and the diesel fraction generated by itself is recycled back to the reactor inlet as supplementary distillate oil, and the amount of circulating oil is 20% of the feed...

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

No PUM Login to View More

Abstract

The invention discloses a residual oil hydrotreatment method for prolonging a device operating cycle. The methods comprises the steps that under the hydro-conversion condition, the mixture of raw material residual oil and hydrogen passes through at least one reactor containing residual oil hydrotreatment catalysts; and at the steady-state inactivation stage of the residual oil catalysts, residual oil feed is switched into distillate containing a vulcanizer without shutdown and reversely passes through a catalyst bed layer in the hydrogenation reactor, and the distillate is switched to normal residual oil raw material after being reversely vulcanized and into an operation process. The method disclosed by the invention can play roles of delaying pressure drop rise and the appearance of hot spots, improving fluid distribution and prolonging a device operating cycle. The method disclosed by the invention can also be used in a restart process of an industrial device which is shut down emergently due to device failure, and can bring considerable economic benefits for a refinery.

Description

technical field [0001] The invention relates to a method for prolonging the operation cycle of a hydrogenation unit. The method is suitable for treating hydrogenation units with high content of impurities (solid particles, mechanical impurities, metals, colloids, asphaltenes), especially for fixed-bed residue hydrogenation reactors for processing inferior and heavy residues. Background technique [0002] As we all know, in recent years, as the world's crude oil has gradually become heavier and worse (increased sulfur, nitrogen, residual carbon, and metal content), and environmental protection regulations have become increasingly stringent, residual oil hydrotreating has become more and more important. At present, the hydrogenation processes for processing inferior and heavy residues mainly include fixed bed, ebullating bed, suspension bed, moving bed, etc. The fixed bed residue hydrotreating process is widely used because of its mature technology and simple operation. No ma...

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
IPC IPC(8): C10G65/02C10G65/12C10G49/00C10G47/00C10G45/00
Inventor 张庆军蒋立敬胡长禄韩照明耿新国彭派吴锐李洪广刘铁斌翁延博
Owner CHINA PETROLEUM & CHEM CORP