The present invention relates to a Fischer-Tropsch gasoil fraction, cleaning compositions comprising the Fischer-Tropsch gasoil fraction, and use of the Fischer- Tropsch gasoil fraction.

Hydrocarbon gasoils may be crude oil derived in nature or be synthetically-derived. US2010/0113847 discloses a synthetic gasoil derived from an olefin oligomerisation process. Currently, Fischer-Tropsch derived gasoils receive significant commercial attention. Fischer-Tropsch derived gasoils may be obtained by various processes. A Fischer-Tropsch derived gasoil is obtained using the so-called Fischer-Tropsch process. A Fischer-Tropsch process produces a range of hydrocarbon products, including naphtha, gasoil, base oil and other products. The gasoil product is also referred to as the full-range Fischer-Tropsch derived gasoil. An example of such process producing a Fischer-Tropsch derived gasoil is disclosed in WO 02/070628.

In US5906727, a Fischer-Tropsch derived solvent based on a full-range Fischer-Tropsch derived gasoil is disclosed with a boiling range from approximately 160 to 370°C. US 2009/0111723 discloses the use of Fischer- Tropsch derived gasoil in metal working applications.

There is a need in the art for Fischer-Tropsch gasoils fractions that have a more narrow boiling point range compared to the solvent disclosed in US5906727.

It has now surprisingly been found that specific Fischer-Tropsch gasoil fractions of the full-range

Fischer-Tropsch derived gasoil can be advantageously used in dry cleaning and metal cleaning applications. To this end, the present invention provides a

Fischer-Tropsch gasoil fraction having an initial boiling point of at least 165°C and a final boiling point of at most 220°C.

Typically, the Fischer-Tropsch gasoil fraction according to the present invention has very low levels of aromatics, naphthenic paraffins (also referred to a naphthenics) and impurities. The low level of impurities, aromatics and naphthenics gives the Fischer-Tropsch gasoil fraction according to the present invention an improved odor compared to crude oil derived gasoil, even after dearomatization . While the presence of normal paraffins and mono-methyl branched isoparaffins may provide improved bio-degradability compared to other isoparaffins.

The Fischer-Tropsch gasoil fraction according to the present invention is a fraction of the full-range

Fischer-Tropsch gasoil that is derived from a Fischer- Tropsch process. Full-range Fischer-Tropsch derived gasoil, herein also referred to as Fischer-Tropsch gasoil, is known in the art. By the term "Fischer-Tropsch derived" is meant that the gasoil, is, or is derived from, a synthesis product of a Fischer-Tropsch process. In a Fischer-Tropsch process, synthesis gas is converted to a synthesis product. Synthesis gas or syngas is a mixture of predominantly hydrogen and carbon monoxide that is obtained by conversion of a hydrocarbonaceous feedstock. Suitable feedstocks include natural gas, crude oil, heavy oil fractions, coal, biomass or

lignocellulosic biomass and lignite. A Fischer-Tropsch derived gasoil may also be referred to as a GTL (Gas-to- Liquids) gasoil. The Fischer-Tropsch gasoil is

characterized as the product of a Fischer-Tropsch process wherein a synthesis gas, or mixture of predominantly hydrogen and carbon monoxide, is processed at elevated temperature over a supported catalyst comprised of a Group VIII metal, or metals, e.g., cobalt, ruthenium, iron, etc. At least part of the Fischer-Tropsch product is contacted with hydrogen, at hydrocracking/

hydroisomerization conditions over a, preferably, bifunctional, catalyst, or catalyst containing a metal, or metals, hydrogenation component and an acidic oxide support component active in producing both hydrocracking and hydroisomerization reactions. A least part of the resulting hydrocracked/hydroisomerized Fischer-Tropsch product may be provided as the Fischer-Tropsch derived gasoil feedstock.

Fischer-Tropsch gasoils are different from crude oil-derived gasoils. Despite having a similar boiling point range, the specific molecular composition of the Fischer-Tropsch gasoils may allow for, amongst others, improved viscosity characteristics, improved pour point characteristics, improved density characteristics and in particular a combination of any of the aforementioned characteristics with specific desired flash point characteristics. For example, Fischer-Tropsch gasoils may combine a low volatility with a high flash point, whereas the viscosity of such Fischer-Tropsch gasoils may be lower than the viscosity of crude oil-derived gasoil feedstock having a similar volatility and flash point.

The different characteristics of the Fischer-Tropsch gasoils, compared to the crude oil-derived gasoils, are generally attributed to their particular isoparaffin to normal paraffin weight ratio (i/n ratio), relative amount of mono-methyl branched isoparaffins and the molecular weight distribution of the paraffins . A particular advantage of the Fischer-Tropsch derived gasoils is that these gasoils are almost

colorless. Color as used herein is the Saybolt color as measured by its Saybolt number (ASTM D156 : Standard Test Method for Saybolt Color of Petroleum Products) . A high

Saybolt number, +30, indicates colorless fluids, whereas lower Saybolt numbers, in particular below zero, indicate a discoloration. A Saybolt number lower than 25 already indicates the presence of a visually observable

discoloration. Fischer-Tropsch gasoils typically have the highest Saybolt number, i.e. +30. The good color

characteristics, together with the above mentioned improved viscosity, pour point, density and flash point characteristics make the Fischer-Tropsch derived gasoils highly suitable for dry cleaning and metal cleaning applications .

It has now been found that it may be possible to meet specific requirements of particular applications of the Fischer-Tropsch derived gasoil by using a specific fraction of a Fischer-Tropsch gasoil, wherein the fraction has a more narrow boiling point range compared to the full-range Fischer-Tropsch gasoil. By

fractionating the Fischer-Tropsch gasoil, isoparaffins and normal paraffins are distributed unevenly over the fractions and Fischer-Tropsch gasoil fractions may be obtained that have an i/n ratio different from the original Fischer-Tropsch gasoil. Also the relative amount of mono-methyl branched isoparaffins and the molecular weight distribution of the paraffins may be different. As a consequence the viscosity, pour point, density and flash point characteristics of the Fischer-Tropsch gasoil fractions may be changed, beyond the change that would be expected on the basis of a fractionation on the basis of boiling ranges alone . Fischer-Tropsch gasoil contain primarily isoparaffins, however they also contain normal paraffins. Preferably, the Fischer-Tropsch gasoil fraction comprises more than 60 wt% of iso-paraffins , preferably more than 65 wt%, still more preferably more than 68wt% iso-paraffins .

A fraction of the Fischer Tropsch gasoil is a narrower boiling range distillation cut of the Fischer Tropsch gasoil.

According to the present invention, the Fischer-

Tropsch gasoil fraction has an initial boiling point of at least 165°C and a final boiling point of at most 220°C, at atmospheric conditions. Suitably, the Fischer- Tropsch gasoil has an initial boiling point of at least 170°C, more preferably at least 175°C, at atmospheric conditions .

The Fischer-Tropsch gasoil fraction preferably has a final boiling point of at most 215°C, at atmospheric conditions. Further, the Fischer-Tropsch gasoil fraction preferably has a final boiling point of most 208°C, at atmospheric conditions. By excluding lower boiling hydrocarbons that normally considered to be part of a full-range Fischer-Tropsch gasoil a lower volatility and higher flash point may be obtained. By excluding higher boiling hydrocarbons that normally considered to be part of a full-range Fischer-Tropsch gasoil better evaporation characteristics can be obtained. It also provided for a more convenient recycling of the fraction, while for instance in metal cleaning less staining may be observed.

A preferred Fischer-Tropsch gasoil fraction has an initial boiling point of at least 175°C and a final boiling point of at most 208°C, at atmospheric

conditions . By boiling points at atmospheric conditions is meant atmospheric boiling points, which boiling points are determined by ASTM D86.

Preferably, the Fischer-Tropsch gasoil fraction has a T10 vol% boiling point in the range of from 177 to

195°C, more preferably of from 180 to 192°C, most preferably of from 183 to 189°C and a T90 vol% boiling point in the range of from 191 to 209°C, preferably of from 194 to 206°C and more preferably of from 197 to 203°C.

T10 vol% boiling point is the temperature

corresponding to the atmospheric boiling point at which a cumulative amount of 10 vol% of the product is recovered. Similarly, T90 vol% boiling point is the temperature corresponding to the atmospheric boiling point at which a cumulative amount of 90vol% of the product is recovered. The atmospheric distillation method ASTM D86 is used to determine the level of recovery.

The Fischer-Tropsch gasoil fraction comprises preferably paraffins having from 7 to 14 carbon atoms; the Fischer-Tropsch derived paraffin gasoil fraction comprises preferably at least 70 wt%, more preferably at least 85 wt%, more preferably at least 90 wt%, more preferably at least 95 wt%, and most preferably at least 98 wt% of Fischer-Tropsch derived paraffins having in the range of from 7 to 14 carbon atoms based on the total amount of Fischer-Tropsch derived paraffins.

Further, the Fischer-Tropsch gasoil fraction preferably has a density at 15°C according to ASTM D4052 in the range of from 720 kg/m ³ to 726 kg/m ³ , more

preferably of from 721 kg/m ³ to 725 kg/m ³ , and most preferably of from 722 kg/m ³ to 724 kg/m ³ . Suitably, the kinematic viscosity at 25°C according in the range of from 0.8 to 1.4 cSt, preferably of from 0.9 cSt to 1.3 cSt, and more preferably of from 1.0 cSt to 1.2 cSt.

Preferably, the flash point the Fischer-Tropsch gasoil fraction has a flash point according to ASTM D93 of at least 53 °C, preferably in the range of from 53 to 67 °C, more preferably of from 56 to 64 °C, and most preferably of from 57 to 63 °C.

The Fischer-Tropsch gasoil fraction has a smoke point according to ASTM D1322 of more than 50 mm.

Typically, the Fischer-Tropsch gasoil fraction according to the present invention comprises less than 500 ppm aromatics, preferably less than 360 ppm

aromatics, more preferably less than 300 ppm aromatics, less than 3 ppm sulphur, preferably less than 1 ppm sulphur, more preferably less than 0.2 ppm sulphur, less than 1 ppm nitrogen and less than 4wt% naphthenics, preferably less than 3 wt% and more preferably less than 2.5 wt% naphthenics.

Further, the Fischer-Tropsch gasoil fraction preferably comprises less than 0.1 wt% polycyclic aromatic hydrocarbons, more preferably less than 25 ppm polycyclic aromatic hydrocarbons and most preferably less than 1 ppm polycyclic aromatic hydrocarbons.

The amount of isoparaffins is suitably more than 60 wt% based on the total amount of paraffins having in the range of from 7 to 14 carbon atoms, preferably more than 65 wt%.

Further, the Fischer-Tropsch gasoil fraction may comprise normal paraffins, also referred to as n- paraffins, and cyclo-alkanes . The Fischer-Tropsch gasoil fraction preferably has an isoparaffin to normal paraffin weight ratio (also referred to as i/n ratio) of in the range of from 2 to 3. This i/n ratio may advantageously affect amongst others the viscosity of the Fischer-Tropsch gasoil fraction. The concentration of isoparaffin may be high enough to benefit a lower overall viscosity. At the same time the significant amount of normal paraffins may benefit the bio-degradability .

Preferably, the Fischer-Tropsch gasoil fraction comprises in the range of from 45 to 65 wt%, more preferably of from 50 to 60wt%, of mono-methyl branched isoparaffins , based on the total weight of isoparaffins in the Fischer-Tropsch gasoil fraction. Mono-methyl branched isoparaffins exhibit desirable bio degradation characteristic compared to other isoparaffins. A relative high concentration of mono-methyl isoparaffins to other isoparaffins may advantageously affect amongst others the bio degradation characteristics of the Fischer-Tropsch gasoil fractions. A higher relative concentration of mono-methyl isoparaffin to other isoparaffins may provide the Fischer-Tropsch gasoil fraction with bio degradation characteristics beyond the bio degradation

characteristics of the Fischer-Tropsch gasoil.

The Fischer-Tropsch gasoil fraction has a much narrower boiling range compared to the Fischer-Tropsch gasoil, allowing for its use in many applications. Due to its relative highly paraffinic nature and relative low levels of naphthenic and aromatic components and in addition the relative low levels of impurities, the

Fischer-Tropsch gasoil fraction of the invention

incorporates several technical benefits over conventional, crude oil derived fluids. Compared to existing isoparafflnic fluids currently on the market, the Fischer- Tropsch gasoil fraction has a more desirable mix of isoparaffins and n-paraffins . While competitive

isoparaffinic fluids predominantly contain isoparaffins , and especially the higher boiling isoparaffins, including naphthenic paraffins, this Fischer-Tropsch gasoil fraction of the invention contains isoparaffins and n-paraffins, while containing very minor amounts of naphthenic

paraffins .

When used in for instance dry cleaning and metal cleaning applications the low odor and relatively low toxicity, due to the low aromatic content, are a distinct benefit as well as the improved bio degradation due to the high concentration of normal paraffins and mono-methyl isoparaffins. The Fischer-Tropsch gasoil fractions according to the invention combine good oxidation

stabilities and long shelf time. The low level of

impurities allow for a beneficial non-staining performance in for dry cleaning and metal cleaning applications . A high flash point is desirable for safety reasons. Where prior art gasoils used for these application suffered from an undesired high viscosity when using a high flash point gasoil, the Fischer-Tropsch gasoil fraction of the present invention having its specific composition and branching provides a high flash point while maintaining a viscosity that is relatively low compared to prior art isoparaffinic fluids, at same flash point levels. The combination of having a low viscosity and at the same time a relatively high flash point may find its benefits numerous

applications by increasing safety.

The preparation of the Fischer-Tropsch gasoil feedstock used as a basis for the Fischer-Tropsch gasoil fraction of the present invention described in e.g. WO02/070628 and WO-A-9934917 (in particular the process as described in Example VII of WO-A-9934917, using the catalyst of Example III of WO-A-9934917), both of which are hereby incorporated by reference . As mentioned above these Fischer-Tropsch derived gasoil feedstocks have a different molecular composition and have significantly different properties compared to crude oil-derived gasoil feedstock. Therefore, Fischer-Tropsch derived gasoil feedstocks can be clearly distinguished from crude oil- derived gasoil feedstocks.

In a further aspect, the present invention provides a cleaning composition comprising a Fischer-Tropsch gasoil fraction according the invention. One particularly preferred cleaning composition is a dry cleaning

composition. A dry cleaning composition is a composition used in dry cleaning applications for cleaning clothing or other fabrics . Another particularly preferred cleaning composition is a metal cleaning composition, typically used for cleaning metal surfaces. The Fischer-Tropsch gasoil fraction may be used alone or in combination with other compounds in the composition. Other compounds that are used in combination with the Fischer-Tropsch gasoil fraction include additives for functional fluid

formulations such as, but are not limited to, corrosion and rheology control products, emulsifiers and wetting agents, borehole stabilizers, high pressure and anti-wear additives, de- and anti-foaming agents, pour point depressants, and antioxidants. Preferably, the other compounds comprise one or more compounds of corrosion and rheology control products, emulsifiers and wetting agents, borehole stabilizers, high pressure and anti-wear additives, de- and anti-foaming agents, pour point depressants, and antioxidants. In another aspect, the invention provides for the use of the Fischer-Tropsch gasoil fraction in various applications. The Fischer-Tropsch gasoil fraction may be used in combination with other compounds.

Typically, Fischer-Tropsch gasoil fraction may be used in many areas, for instance oil and gas exploration and production, process oils, agro chemicals, process chemicals, construction industry, food and related industries, paper, textile and leather, and various household and consumer products. Other compounds that are used in combination with the Fischer-Tropsch gasoil fraction include additives for functional fluid

formulations such as, but are not limited to, corrosion and rheology control products, emulsifiers and wetting agents, borehole stabilizers, high pressure and anti-wear additives, de- and anti-foaming agents, pour point depressants, and antioxidants.

Preferred applications using the Fischer-Tropsch gasoil fraction according to the present invention include, but is not limited to, drilling fluids, heating fuels or oil, lamp oil, barbeque lighters, concrete demoulding, pesticide spray oils, paints and coatings, personal care and cosmetics, consumer goods, pharmaceuticals, industrial and institutional cleaning, adhesives, inks, air fresheners, sealants, water treatment, cleaners, polishes, car dewaxers, electric discharge machining, transformer oils, process oil, process chemicals, silicone mastic, two stroke motor cycle oil, metal cleaning, dry cleaning, lubricants, metal work fluid, aluminum roll oil, explosives, chlorinated paraffins, heat setting printing inks, Timber treatment, polymer processing oils, rust prevention oils, shock absorbers, greenhouse fuels, fracturing fluids and fuel additives formulations.

In particular the invention provides the use of a Fischer-Tropsch gasoil fraction according to the invention or a cleaning composition comprising such Fischer-Tropsch gasoil fraction in metal cleaning applications .

Equally particular the invention provides the use of a Fischer-Tropsch gasoil fraction according to the invention or a cleaning composition comprising such Fischer-Tropsch gasoil fraction in dry cleaning applications .

The present invention is described below with reference to the following Examples, which are not intended to limit the scope of the present invention in any way .

Examples

Example 1

Preparation of a Fischer-Tropsch gasoil fraction having an initial boiling point of 175°C and a final boiling point of 208°C

A Fischer-Tropsch product was prepared in a process similar to the process as described in Example VII of WO-A-9934917, using the catalyst of Example III of

WO-A-9934917. The C5+ fraction (liquid at ambient conditions) of the product thus obtained was continuously fed to a hydrocracking step (step (a)) . The C5+ fraction contained about 60 wt% C30+ product. The ratio C50+/C30+ was about 0.55. In the hydrocracking step the fraction was contacted with a hydrocracking catalyst of Example 1 of EP-A-532118. The effluent of step (a) was continuously distilled under vacuum to give light products, fuels and a residue "R" boiling from 370 °C and above. The

conversion of the product boiling above 370 °C into product boiling below 370 °C was between 45 and 55 wt%. The residue "R" was recycled to step (a) . The conditions in the hydrocracking step (a) were: a fresh feed Weight Hourly Space Velocity (WHSV) of 0.8 kg/l.h, recycle feed WHSV of 0.4 kg/l.h, hydrogen gas rate = 1000 Nl/kg, total pressure = 40 bar, and a reactor temperature in the range of from 330 °C to 340 °C.

The obtained fuels fraction (C5 ⁺ - 370°C) was

continuously distilled to give Fischer-Tropsch gasoil fraction having an initial boiling point of 175°C and a final boiling point of 208°C and an approximate gasoil fraction yield as shown in Table 1.

The physical properties are given in Table 2.

Table 1

Fischer-Tropsch gasoil fraction

Yield 12

ASTM D2892 (wt%)

Table 2

Fischer-Tropsch gasoil fraction

Kinematic viscosity at 25°C 1.08

According to ASTM D445 [mm ² /s]

content of aromatics <200

According to SMS 2728

[mg/kg]

content of n-paraffins 27

According to GCxGC - internal

testing methodology

[wt%]

content of isoparaffins 70

According to GCxGC - internal

testing methodology

[wt%]

Density at 15°C 723

According ASTM D4052 [kg/m ³ ]

T10 vol.% boiling point 186

According to ASTM D86

[°C]

T90 vol.% boiling point 200

According to ASTM D86

[°C]

Smoke point >50

[mm]

Carbon number range paraffins 7-14

Flash point 60

According to ASTM D93

[°C]

content of monomethyl isoparaffins 54

According to GCxGC - internal

testing methodology

[wt%, based on total isoparaffins]

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