Patent application title:

USE OF RE-REFINED BASE OIL

Publication number:

US20260176543A1

Publication date:
Application number:

19/132,520

Filed date:

2023-12-13

Smart Summary: Re-refined base oil can be used in industrial lubricating fluids. These fluids contain a base oil and some additives. Using re-refined base oil helps improve how well the fluid resists oxidation, which means it lasts longer without breaking down. It also enhances the fluid's performance in low temperatures, making it work better in cold conditions. Overall, this approach makes industrial lubricants more effective and reliable. 🚀 TL;DR

Abstract:

The present invention provides the use of a re-refined base oil in an industrial lubricating fluid, said industrial lubricating fluid comprising at least one base oil and at least one additive, in order to improve one or more of oxidation stability and low temperature performance of said industrial lubricating fluid.

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Classification:

C10M101/02 »  CPC main

Lubricating compositions characterised by the base-material being a mineral or fatty oil Petroleum fractions

C10M2203/1006 »  CPC further

Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions; Petroleum or coal fractions, e.g. tars, solvents, bitumen used as base material

C10N2030/43 »  CPC further

Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives; Low content or no content compositions Sulfur free or low sulfur content compositions

Description

FIELD OF THE INVENTION

The present invention relates to the use of re-refined base oils in industrial lubricant oil formulations.

BACKGROUND OF THE INVENTION

Lubricating fluids are required in all industrial equipment with moving parts. Industrial lubricating fluids, therefore, include hydraulic oils, gear oils, compressor oils, circulating oils and turbine oils, etc. Such industrial lubricating fluids generally comprise one or more base oils and one or more additives. Typically, the additive treat rate for industrial lubricating fluids is considerably lower than for engine oils, with additive treat rates of less than 5 wt % being usual.

With such a low additive treat rate, the base oil being used is of key importance. Typically, so called ‘virgin’ base oils are used in the manufacture of industrial lubricating fluids. These are typically produced from crude oil or natural gas, directly via refining or via synthetic processes.

The disposal of used lubricating fluids requires careful processing and waste streams are often used as burner fuel. In all technology areas, it is necessary to consider the carbon footprint of a product and to try and ensure that raw materials are re-used and recycled where possible. This has led to the development of so called “re-refined base oils”. Re-refined base oils (RRBOs) are base oils derived from reprocessing of used lubricating oils to remove contaminants, oxidized products, and additives.

Technologies such as distillation, thermal de-asphalting, or solvent (often propane) de-asphalting are used as recycling technologies for used lubricating fluids. The intermediate products created by recycling technologies are unfinished and typically unsuited for use as lubricants without further improvement. Finishing technologies such as clay treatment, hydrotreatment (see, for example, EP3921390A1, U.S. Ser. No. 11/034,895B1), or solvent extraction (as described in CN107574012A may then be used to “finish” the quality of the intermediates into marketable base oils. When a recycling technology and a finishing technology are coupled together, they are generally referred to as a re-refining technology. A further, pre-treatment, step may also be used to remove sludge, water and additive metals before recycling occurs.

Previously, re-refined base oils have been viewed as inferior in quality to virgin base oils. With the development of improved re-refining technologies this is no longer the case. However, the focus on re-refining technologies and the re-refined base oil thus produced has focused on producing and using base oils of sufficient quality that they can pass the standards set for lubricating oils across industrial technologies (see, for example, CN104673460A and CN104673461A). It is the intention of the present inventors to develop improved lubricating oils using RRBOs.

SUMMARY OF THE INVENTION

The present invention therefore provides the use of a re-refined base oil in an industrial lubricating fluid, said industrial lubricating fluid comprising at least one base oil and at least one additive, in order to improve one or more of oxidation stability and low temperature performance of said industrial lubricating fluid.

DETAILED DESCRIPTION OF THE INVENTION

One or more specific embodiments of the present disclosure will be described below. These described embodiments are examples of the presently disclosed techniques. Additionally, in an effort to provide a concise description of these embodiments, not all features of an actual implementation may be described in the specification.

When introducing elements of various embodiments of the present disclosure, the articles “a,” “an,” and “the” are intended to mean that there are one or more of the elements. The terms “comprising,” “including,” and “having” are intended to be inclusive and mean that there may be additional elements other than the listed elements. Additionally, it should be understood that references to “one embodiment” or “an embodiment” of the present disclosure are not intended to be interpreted as excluding the existence of additional embodiments that also incorporate the recited features.

The present inventors have surprisingly found that re-refined base oils may be used in order to provide improved fluids for use as industrial lubricating fluids.

Industrial lubricating fluids include, but are not limited to, those used as hydraulic oils, gear oils, compressor oils, circulating oils and turbine oils. An industrial lubricating fluid according to the present invention comprises at least one base oil and at least one additive.

The industrial lubricating fluid preferably comprises at least 95 wt % of base oil. According to the invention, of this base oil, at least a portion and up to 100 wt % is re-refined base oil. Preferably at least 10 wt % of the base oil in the industrial lubricating fluid is re-refined base oil. Depending on the viscosity grades of industrial lubricating fluid, RRBO treat rates could be as high as almost 100% for the light grades of industrial lubricating fluid while heavy virgin base oils might be needed to close the viscosity gap for heavy grades of industrial lubricating fluid.

Base oil in the industrial lubricating fluid that is not re-refined base oil may be any suitable base oil typically used in a lubricating fluid. Specific examples include base oils belonging to Groups I to IV of the API (American Petroleum Institute—see Table 1) base oil categories, which can be used alone or in a mixture.

TABLE 1
API base oil categories
Sulfur Saturates Viscosity
Category (%) (%) index
Group I >0.03 and/or <90 80-<120
Group II ≤0.03 and ≥90 80-<120
Group III ≤0.03 and ≥90 ≥120
Group IV PAO Synthetic Lubricants
Group V All other base oils

The re-refined base oil used in the present invention is preferably Group I or Group II according to the API base oil categories. More preferably, the re-refined base oil used in the present invention is Group I according to the API base oil categories. Typical re-refined Group I base oils, while falling within the API categorisation for Group I base oils have features not typical for a virgin Group I base oil. Preferably, the saturates content of the Group I re-refined base oil is preferably at least 80%, more preferably at least 90%. The viscosity index of the Group I re-refined base oil is preferably at least 95 and more preferably at least 105. The sulphur content of the Group I re-refined base oil is preferably no more than 0.3% and more preferably no more than 0.1%. The sulphur content of the Group I re-refined base oil is greater than 0.03%, in line with the API classification.

The re-refined base oil use in the present invention is preferably base oil that has been recycled from used lubricant fluid using solvent extraction or hydrotreatment.

Preferably the overall amount of additives in the industrial lubricating fluid is less than 5 wt %, more preferably less than 3 wt %, even more preferably less than 2 wt % based on the overall weight of the industrial lubricating fluid. Suitably, the overall amount of additives in the industrial lubricating fluid is at least 0.1 wt % based on the overall weight of the industrial lubricating fluid. The additives may be incorporated into the industrial lubricating fluid singly or as part of one or more additive packages. Whether added singly or in additive packages, a diluent oil may be included with the additive and form part of the finished industrial lubricating fluid.

Different types of additives will be suitable depending on the end use of the industrial lubricating fluid. These include, but are not limited to anti-wear additives, extreme pressure additives, friction modifiers, viscosity index improvers, pour point depressants, anti-oxidants, rust and corrosion inhibitors, dispersants, demulsifiers and foam inhibitors.

Anti-wear additives and extreme pressure additives include phosphorus compounds, such as phosphate esters, acidic phosphate esters, amine salts of acidic phosphate esters, basic phosphate esters, phosphite esters, phosphorothionates, zinc dithiophosphates, esters of dithiophosphoric acid and alkanols or polyether-type alcohols, and derivatives thereof, phosphorus-containing carboxylic acids and phosphorus-containing carboxylic acid esters.

As examples of viscosity-index improvers mention may be made of non-dispersant type viscosity-index improvers such as polymethacrylates and olefin polymers such as ethylene-propylene copolymers, styrene-diene copolymers, polyisobutylene and polystyrene, and dispersant type viscosity-index improvers where nitrogen-containing monomers have been copolymerised with these, and they may be made with kinds different from the copolymers of olefins and alkyl methacrylates.

As examples of pour-point depressants mention may be made of polymethacrylate-based polymers.

Suitable antioxidants include amine-based antioxidants, sulphur-based antioxidants, phenol-based antioxidants and phosphorus-based antioxidants. These antioxidants may be used singly or in combination.

As examples of demulsifiers suitable for use in industrial lubricating fluids according to this invention, mention may be made of those in the known art normally used as additives for lubricating oils.

Defoaming agents may also be added in order to impart defoaming characteristics to the lubricating oil composition of this invention.

As examples of defoaming agents suitable for use in industrial lubricating fluids according to this invention, mention may be made of organosilicates such as dimethylpolysiloxane, diethylsilicate and fluorosilicone, and non-silicone type defoaming agents such as polyalkylacrylates.

The present invention will now be illustrated through the following, non-limiting examples.

Examples

A range of industrial lubricant formulation were blended and tested as set out in Tables 3 to 6. The following base oils (with properties as set out in Table 2) were used in the Examples.

The Group I 150SN & 500SN are commercially available from Hindustan Petroleum Corporation Limited (HPCL) under the brand name of Alprol N32 & Alprol N100.

The Group II 150N & 500N are commercially available from Hainan Handi Sunshine Petrochemical Co. under the brand name of HDS-150N & HDS-500N.

The Group I RRBO 150SN is commercially available from Hebei Jingu Recycling Resources Development Co. under the brand name of JINGU 150SN.

The Group II RRBO 150N is commercially available from Changzhou FINAS Energy Technology Co. under the brand name of FINAS 150N.

TABLE 2
HANDI HANDI JINGU FINAS
Test HPCL HPCL SUNSHINE SUNSHINE RRBO RRBO
Properties method 150SN 500SN 150N 500N 150SN 150N
Vk @ 100° C. ASTM 5.293 10.67 5.386 10.13 5.492 5.318
(cSt) D445
Vk @ 40° C. ASTM 31.56 93.54 31.54 82.61 31.27 28.97
(cSt) D445
Viscosity ASTM 98 97 104 103 112 118
Index D2270
Saturates IP 74.4 61.5 99.8 99.8 96.6 97
(%) 368/ASTM
D7419
Sulphur ASTM 0.97 1.38 0.0001 0.0002 0.0477 0.0077
content (%) D5453

The hydraulic oil package used in the formulations is a commercially available standard industrial hydraulic oil additive package.

The pour point depressant used in the formulations is a standard, commercially available, pour point depressant.

The anti-foam additive used in the formulations is a commercially available anti-foam additive.

It can be seen from Tables 3 to 6 that Group I or Group II RRBO based samples show performance advantages, against their virgin base oil counterparts, like higher VI, lower viscosity at 0° C., better oxidation stability as reflected by RPVOT and TOST test outcomes.

TABLE 3
Comp Comp
Ex. 1 Ex. 2 Ex 1 Ex 2
Group I 150SN 89.5
Group I 500SN 9.94
Group II 150N 95.47
Group II 500N 3.97 6.34 11.79
Group I RRBO 150SN 92.7
Group II RRBO 150N 87.7
Hydraulic oil package 1 0.45 0.45 0.45 0.45
Pour point depressant 2 0.1 0.1 0.5 0.05
Anti-foam additive 3 0.01 0.01 0.01 0.01
Test
Properties method
Appearance Visual B&C B&C B&C B&C
Vk @ 40° C. (cSt) GB/T 265 35.27 34.31 33.63 32.76
Vk @ 100° C. (cSt) GB/T 265 5.751 5.760 5.843 5.762
Viscosity Index GB/T 1995 103 108 117 118
Vk @ 0° C. (cSt) GB/T 265 383.0 346.3 317.3 304.7
Copper, 3 h, 100° C. GB/T 5096 1b 1b 1a 1a
Rust, SSW, Method B - GB/T 11143 No No No No
24 Hours Rusting Rusting Rusting Rusting
Foaming Seq I, ml · ml GB/T 12579 0/0 30/0 10/0 50/0
Seq II, ml/ml 30/0  10/0 10/0 30/0
Seq III, ml/ml 0/0  0/0 10/0 50/0
water separation @ 54° C. GB/T 7305 25 20 10 10
TOST Oxidation Stability GB/T 12581
Total acid number 0.3 0.24 0.093 0.12
after 1000 hrs
RPVOT, 150° C. (min) SH/T 0193 205 212 265 228
Filterability (Stage I)-Dry (%) ISO 13357- 84.7 88.6 96.3 94.2
2:2017
Filterability (Stage II)-Dry (%) 67.0 78.6 94.7 90.1
Filterability (Stage I)-Wet ISO 13357- 91.9 78.3 87.0 82.0
1:2017
Filterability (Stage II)-Wet 83.9 54.9 79.0 64.0

TABLE 4
Comp Comp
Ex. 3 Ex. 4 Ex 3 Ex 4
Group I 150SN 29.83
Group I 500SN 69.61
Group II 150N 14.92
Group II 500N 84.52 69.04 74.49
Group I RRBO 150SN 30
Group II RRBO 150N 25
Hydraulic oil package 1 0.45 0.45 0.45 0.45
Pour point depressant 2 0.1 0.1 0.5 0.05
Anti-foam additive 3 0.01 0.01 0.01 0.01
Test
Properties method
Appearance Visual B&C B&C B&C B&C
Vk @ 40° C. (cSt) GB/T 265 67.2 68.31 65.92 68.01
Vk @ 100° C. (cSt) GB/T 265 8.631 9.060 8.992 9.109
Viscosity Index GB/T 1995 99 107 111 109
Vk @ 0° C. (cSt) GB/T 265 957.6 938.3 826.9 916.0
Copper, 3 h, 100° C. GB/T 5096 1b 1b 1a 1a
Rust, SSW, Method B - GB/T 11143 No No No No
24 Hours Rusting Rusting Rusting Rusting
Foaming Seq I, ml · ml GB/T 12579 0/0 60/0 10/0 0/0
Seq II, ml/ml 60/0  30/0 20/0 30/0 
Seq III, ml/ml 0/0  0/0 10/0 0/0
water separation @ 54° C. GB/T 7305 30 20 15 10
TOST Oxidation Stability GB/T 12581
Total acid number 0.25 0.19 0.10 0.17
after 1000 hrs
RPVOT, 150° C. (min) SH/T 0193 173 215 202 208
Filterability (Stage I)-Dry ( %) ISO 13357- 82.7 93.1 93.3 85
2:2017
Filterability (Stage II)-Dry (%) 65.7 86.0 86.5 74.5
Filterability (Stage I)-Wet ISO 13357- 92.5 80.5 88.0 83
1:2017
Filterability (Stage II)-Wet 84.1 61.2 80.0 74

TABLE 5
Example 5 Example 6
Group I 150SN
Group I 500SN
Group II 150N
Group II 500N 39.96 43.41
Group I RRBO 150SN 59.08
Group II RRBO 150N 56.08
Hydraulic oil package 1 0.45 0.45
Pour point depressant 2 0.5 0.05
Anti-foam additive 3 0.01 0.01
Properties Test method
Appearance Visual B&C B&C
Vk @ 40° C. (cSt) GB/T 265 46.51 46.68
Vk @ 100° C. (cSt) GB/T 265 7.170 7.204
Viscosity Index GB/T 1995 114 114
Vk @ 0° C. (cSt) GB/T 265 517.9 509.2
Copper, 3 h, 100° C. GB/T 5096 1a 1a
Rust, SSW, Method B - GB/T 11143 No No
24 Hours Rusting Rusting
Foaming Seq I, ml/ml GB/T 12579 10/0 0/0
Seq II, ml/ml 10/0 30/0 
Seq III, ml/ml 10/0 0/0
water separation @ 54° C. GB/T 7305 10 10
TOST Oxidation Stability GB/T 12581
Total acid number after 0.089 0.11
1000 hrs *mg KOH/g
RPVOT, 150° C. (min) SH/T 0193 226 267
Filterability (Stage I)- ISO 13357- 96.5 87.5
Dry (%) 2:2017
Filterability (Stage II)- 93.1 76.6
Dry (%)
Filterability (Stage I)- ISO 13357- 86 78
Wet 1:2017
Filterability (Stage II)- 76 58
Wet

TABLE 6
Comp Comp Example
Ex. 5 Ex 6 7
Group I 150SN 64.41
Group I 500SN 34.63 36.67
Group II 150N 59.7
Group II 500N 39.79
Group I RRBO 150SN 62.37
Group II RRBO 150N
Hydraulic oil package 1 0.45 0.45 0.45
Pour point depressant 2 0.5 0.05 0.5
Anti-foam additive 3 0.01 0.01 0.01
Test
Properties method
Appearance Visual B&C B&C B&C
Vk @ 40° C. (cSt) GB/T 265 46.20 45.11 46.52
Vk @ 100° C. (cSt) GB/T 265 6.710 6.869 6.850
Viscosity Index GB/T 1995 97 108 102
Vk @ 0° C. (cSt) GB/T 265 558.2 510.3 520.4
Copper, 3 h, 100° C. GB/T 5096 1a 1a 1a
Rust, SSW, Method B - GB/T 11143 No No No
24 Hours Rusting Rusting Rusting
Foaming Seq I, ml/ml GB/T 12579 0/0 0/0 0/0
Seq II, ml/ml 10/0  20/0  10/0 
Seq III, ml/ml 0/0 0/0 0/0
water separation @ 54° C. GB/T 7305 30 10 25
TOST Oxidation Stability GB/T 12581
Total acid number after 0.64 0.22 0.11
1000 hrs *mg KOH/g
RPVOT, 150° C. (min) SH/T 0193 192 216 244
Filterability (Stage I)- ISO 13357- 95.8 94.6 96.3
Dry (%) 2:2017
Filterability (Stage II)- 92.3 90.4 92.6
Dry (%)
Filterability (Stage I)- ISO 13357- 64 82 88
Wet 1:2017
Filterability (Stage II)- 20 67 74
Wet

Claims

1. Use of a re-refined base oil in an industrial lubricating fluid, said industrial lubricating fluid comprising at least one base oil and at least one additive, in order to improve one or more of oxidation stability and low temperature performance of said industrial lubricating fluid.

2. Use according to claim 1, wherein the industrial lubricating fluid comprises at least 95 wt % of base oil.

3. Use according to claim 1, wherein at least a portion and up to 100 wt % of the base oil is re-refined base oil.

4. Use according to claim 1, wherein the re-refined base oil is selected from one or both of Group I and Group II according to the API base oil categories.

5. Use according to claim 4, wherein the re-refined base oil is a Group I base oil with a viscosity index of at least 95, a sulphur content of no more than 0.3% and a saturates content of at least 90%.

6. Use according to claim 1, the re-refined base oil is base oil that has been recycled from used lubricant fluid using solvent extraction or hydrotreatment.

7. Use according to claim 1, wherein the overall amount of additives in the industrial lubricating fluid is less than 5 wt %, more preferably less than 3 wt %, even more preferably less than 2 wt % based on the overall weight of the industrial lubricating fluid.