Process for the production of surfactants from renewable materials, comprising a step for hydrotreatment and a step for transforming paraffins into surfactants

Patent metadata

Field	Value
Publication number	US-9260385-B2
Application number	US-201314409654-A
Country	US
Kind code	B2
Filing date	Apr 18, 2013
Priority date	Jun 21, 2012
Publication date	Feb 16, 2016
Grant date	Feb 16, 2016

Abstract

A process for the production of surfactant compounds from a feed obtained from renewable sources, comprising hydrotreatment of feed in a fixed bed reactor having a plurality of catalytic zones disposed in series containing a hydrotreatment catalyst. The feed is injected in a staggered manner and injected in increasing proportions in order to produce an effluent containing at least hydrocarbon compounds containing linear paraffins.

First claim

The invention claimed is:

1. A process for the production of surfactant compounds from a feed obtained from renewable sources, comprising an oil or fat of vegetable or animal origin, or mixtures thereof, said oil or fat containing triglycerides and/or free fatty acids and/or esters, said process comprising:
a) hydrotreatment of said feed in the presence of hydrogen in excess of theoretical hydrogen consumption and under hydrotreatment conditions, in a fixed bed reactor having a plurality of catalytic zones disposed in series and comprising a hydrotreatment catalyst, in order to produce an effluent containing at least linear paraffin hydrocarbon compounds,
i) dividing the total flow of feed F into a certain number of different part flows, F1 to Fn, equal to the number of catalytic zones Zn in the reactor, injecting the first part flow F1 into a first catalytic zone Z1, injecting a second part flow F2 into a second catalytic zone, if n is greater than 2, up to n, various part flows being injected into successive catalytic zones in increasing proportions such that F1/F is less than or equal to F2/F, which itself is less than or equal to F3/F if present until F(n−1)/F is less than or equal to Fn/F,
the temperature of a flow injected into the inlet to the first catalytic zone Z1 comprising part flow of the feed F1 mixed with a hydrogen-rich flow H1 entering the zone Z1 and with a liquid recycle R, (F1+R+H1), being greater than 250° C. and the temperature of flows at the inlet to the subsequent zones Z2 to Zn being greater than 300° C.;
ii) separating from said effluent containing linear paraffin hydrocarbon compounds, a gaseous fraction containing hydrogen, CO, CO 2 , H 2 S, water and light gases and a liquid hydrocarbon fraction containing linear paraffins;
iii) recycling at least a portion R of said liquid hydrocarbon fraction containing linear paraffins is recycled to the first catalytic zone Z1 such that the weight ratio between flows of said recycle R and the part flow F1 introduced into the first catalytic zone Z1, R/F1, is 8 or more;
b) transforming at least a portion of said liquid hydrocarbon fraction containing linear paraffins obtained from a) into surfactant compounds, by
alkylating of at least a portion of said liquid hydrocarbon fraction containing linear paraffins obtained from a), with aromatic hydrocarbons that are benzene, toluene, xylenes or mixtures of these hydrocarbons, in order to produce aromatic compounds alkylated by long chain paraffins;
or sulfonating of at least a portion of said liquid hydrocarbon fraction containing linear paraffins obtained from a) in order to produce paraffinic sulfonate compounds.

2. The process according to claim 1 , in which the excess hydrogen used in the hydrotreatment step is at least 50% beyond theoretical consumption.

3. The process according to claim 1 , in which the weight ratio between the recycle flow sent to the first catalytic zone and the total flow of feed is less than 1, preferably less than 0.5.

4. The process according to claim 1 , in which the feed obtained from renewable sources is oil or fat of vegetable or animal origin, or mixtures thereof, containing triglycerides and/or free fatty acids and/or esters.

5. The process according to claim 1 , in which the temperature of the flow F1 injected into the inlet to the first catalytic zone Z1 is greater than 260° C.

6. The process according to claim 5 , in which the temperature of the flow F1 injected into the inlet to the first catalytic zone Z1 is greater than 270° C.

7. The process according to claim 1 , in which the temperature of the flows at the inlet to the catalytic zones Z2 to Zn is greater than 310° C.

8. The process according to claim 1 , in which the hydrotreatment is operated at a temperature in the range 200° C. to 400° C., a total pressure in the range 2 MPa to 15 MPa, at an hourly space velocity in the range 0.1 h −1 to 5 h −1 and in the presence of a total quantity of hydrogen mixed with the feed such that the hydrogen/feed ratio is in the range 300 to 1500 Nm 3 of hydrogen/m 3 of feed.

9. The process according to claim 1 , in which the hydrotreatment catalyst is a sulfur containing catalyst comprising one or more elements from groups 6, 8, 9 and 10 of the periodic classification of the elements, used alone or as a mixture, and a support of alumina, silica, silica-aluminas, magnesia, clays or mixtures of at least two of these minerals.

10. The process according to claim 1 , in which the hydrotreatment catalyst is a metallic catalyst which comprises nickel, platinum, palladium, ruthenium and rhodium, supported on a support that is alumina, silica, silica-alumina, carbon, activated carbon, cerine, zirconia or a mixture of these compounds.

11. The process according to claim 1 , in which at least a portion of the liquid hydrocarbon fraction containing linear paraffins obtained from the separation (ii) is recycled to the first catalytic zone Z1 such that the weight ratio between the flow for said recycle and the part flow F1 introduced into the first catalytic zone Z1 is greater than or equal to 10.

12. The process according to claim 1 , in which the portion of the liquid hydrocarbon fraction containing linear paraffins obtained from the separation (ii) which is not recycled to supplement the flow of feed injected into the zone Z1 as a liquid recycle (R) is sent to a fractionation section in order to separate a liquid hydrocarbon fraction constituted by linear paraffins containing at most 17 carbon atoms (C17− fraction) and a liquid hydrocarbon fraction constituted by linear paraffins containing 18 carbon atoms or more (C18+).

13. The process according to claim 12 , in which only the linear paraffins containing at most 17 carbon atoms are sent to the step b) for transformation in accordance with the process of the invention.

14. The process according to claim 1 , wherein the linear paraffins in (b) have at most 17 carbon atoms.

15. The process according to claim 9 , wherein the catalyst contains nickel, molybdenum, tungsten, cobalt or a mixture thereof.

Assignees

• IFP Energies Nouvelles

Inventors

• Chapus Thierry

Classifications

• C07C1/24

  by elimination of water · CPC title

• C10G3/60

  Controlling or regulating the processes · CPC title

• C07C2523/28

  Molybdenum · CPC title

• C07C2523/755

  Nickel · CPC title

• B01J8/0492

  Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title