Hydrocarbon residue upgradation process

Patent metadata

Field	Value
Publication number	US-2016137931-A1
Application number	US-201314898378-A
Country	US
Kind code	A1
Filing date	Aug 27, 2013
Priority date	Jun 14, 2013
Publication date	May 19, 2016
Grant date	—

Abstract

The present subject matter provides a process for hydrocarbon residue upgradation. The combination of the hydrocarbon residue along with aromatic rich hydrocarbons, catalysts and surfactants allow the operation of visbreaking unit at higher temperature while producing a stable bottom product.

First claim

I/We claim:

1 . A process for hydrocarbon residue upgradation, the process comprising:
(a) mixing hydrocarbon residue with aromatic rich hydrocarbon to obtain a first mixture; (b) contacting the first mixture with a combination of a oil soluble catalyst and a surfactant to obtain a second mixture; (c) heating the second mixture in a furnace at a temperature range of 400-500° C. for a residence time of 1-5 min; (d) treating effluent from the furnace with aromatic rich hydrocarbon and the surfactant to form a third mixture; (e) adding an aqueous solution of a water soluble catalyst to the third mixture to obtain a fourth mixture; (f) subjecting the fourth mixture in a soaking vessel to a pressure in the range of 4-30 kg/cm 2 at a temperature in the range of 400-480° C. and a residence time in the range of 10-50 min; and (g) passing effluent from the soaking vessel to fractionating column followed by visbreaking vapour recovery section to obtain gas, naphtha, gas oil, visbroken tar, and sour water

2 . The process as claimed in claim 1 , wherein the hydrocarbon residue contains Conradson Carbon Residue in excess of 10 wt %.

3 . The process as claimed in claim 1 , wherein the hydrocarbon residue has viscosity in the range of 300-2000 cSt.

4 . The process as claimed in claim 1 , wherein the hydrocarbon residue is selected from group comprising of atmospheric tower bottom, vacuum tower bottom, extra heavy crude and combinations thereof.

5 . The process as claimed in claim 1 , wherein the aromatic rich hydrocarbon is hydro-aromatic solvent having more than 70% w/w aromatic content.

6 . The process as claimed in claim 1 , wherein the aromatic rich hydrocarbon have at least 20% of aromatic hydrogens and 15% of alpha hydrogens of the total hydrogen content.

7 . The process as claimed in claim 1 , wherein the aromatic rich hydrocarbon is selected from the group comprising of bottom products from FCC unit, delayed coker unit, naphtha cracker unit, gas cracker unit and combinations thereof.

8 . A process as claimed in claim 1 , wherein the aromatic rich hydrocarbon is in the range of 1 to 25 w/w with respect to the hydrocarbon residue.

9 . A process as claimed in claim 1 , wherein the oil soluble catalyst is selected from the group comprising of molybdenum disulfide, molybdenum carbonyl, molyebdenum acetyl acetonate, molybdenum 2-ethyl hexanoate, and mixtures thereof.

10 . A process as claimed in claim 1 , wherein the oil soluble catalyst is in the range of 0.001 to 0.5 w/w with respect to the hydrocarbon residue.

11 . A process as claimed in claim 1 , wherein the water soluble catalyst is selected from the group comprising of magnesium sulphate, magnesium chloride, and mixtures thereof.

12 . A process as claimed in claim 1 , wherein the aqueous solution of the water soluble catalyst contains 30-50% w/w water soluble catalyst.

13 . A process as claimed in claim 1 , wherein the aqueous solution of the water soluble catalyst contains 40% w/w water soluble catalyst.

14 . A process as claimed in claim 1 , wherein the water soluble catalyst is in the range of 0.01 to 1% w/w with respect to the hydrocarbon residue.

15 . A process as claimed in claim 1 , wherein the surfactant is selected from the group comprising of synthetic surfactant, bio-surfactant, and mixtures thereof, preferably from the group comprising of dodecyl benzene sulphonic acid, sodium lauryl sulfate, nonyl phenol, dodecyl resorcinol, rhamnolipids, glycolipids, trehalolipids, sophrolipids, and mixtures thereof.

16 . A process as claimed in claim 1 , wherein the surfactant is in the range of 0-1000 ppmw with respect to the hydrocarbon residue.

17 . A process as claimed in claim 15 , wherein the synthetic surfactant is dodecyl benzene sulphonic acid.

18 . A process as claimed in claim 15 , wherein the bio-surfactant is rhamnolipid biosurfactant.

19 . A process as claimed in claim 1 , wherein the oil soluble catalyst, water soluble catalyst, surfactants and aromatic rich hydrocarbon injection can be injected at multiple points so that simultaneous cracking and saturation of free radicals occurs to improve the product stability.

20 . A process as claimed in claim 1 , wherein sour water has a pH of not less than 5.5.

21 . A process as claimed in claim 1 , wherein visbroken tar is obtained in reduced yield and improved stability.

22 . A process as claimed in claim 1 , wherein the effluent from the soaking vessel is treated with visbroken tar and aromatic rich hydrocarbon for quenching cracking reaction before passing to the fractionating column.

23 . A process for hydrocarbon residue upgradation, the process comprising:
(a) mixing vacuum tower bottom with bottom product from FCC unit to obtain a first mixture; (b) contacting the first mixture with a combination of molybdenum disulfide and rhamnolipid to obtain a second mixture; (c) heating the second mixture in a furnace at a temperature range of 440-460° C. for a residence time of 2-4 min; (d) treating effluent from the furnace with bottom product from FCC unit and dodecyl benzene sulphonic acid to form a third mixture; (e) adding an aqueous solution of magnesium sulphate to the third mixture to obtain a fourth mixture; (f) subjecting the fourth mixture in a soaking vessel to a pressure in the range of 10-15 kg/cm 2 at a temperature in the range of 430-440° C. and a residence time in the range of 20-25 min; and (g) passing effluent from the soaking vessel to fractionating column followed by visbreaking recovery section to obtain gas, naphtha, gas oil, Visbroken tar, and sour water.

Assignees

• Hindustan Petroleum Corp Ltd

Inventors

• Kumar Pramod
• Kumar Madan K
• Peddy Venkata Chalapathi Rao
• Nettem Venkateswarlu Choudary
• Gandham Sri Ganesh

Classifications

• C10G9/007

  Visbreaking · CPC title

• C10G2400/26

  Fuel gas · CPC title

• C10G47/34

  Organic compounds, e.g. hydrogenated hydrocarbons · CPC title

• C10G2300/302

  Viscosity · CPC title

• C10G51/026

  only catalytic cracking steps · CPC title