Showing posts with label API. Show all posts
Showing posts with label API. Show all posts

Tuesday, 31 January 2017

Lastest Oil Sequences ACEA 2016



1st December 2016, with mandatory for new claims 1st December 2017, ACEA has published the European oil sequences issue 2016, these new sequences include some interesting news, in this report, we also go to compare them with the latest news from API / ILSAC.  

Keeping with laster issues, ACEA keeps the Class A/B, for gasoline and light-duty diesel engines, Class C, for catalyst compatible oils for gasoline and light-duty diesel engines with after-treatment devices, and Class E, for heavy-duty diesel engines.



ACEA A/B:

First new in Class A/B is Category 1 (A1/B1) has been removed, this Category is related with high SAPS content and low HTHS viscosity, from 2.9 up to 3.5 cP except for SAE xW-20 lubricants with HTHS viscosity upper to 2.6 cP.

The remaining Categories A3/B3, A3/B4 and A5/B5 keep the same conditions that last issue (A3/B3 and A3/B4 with HTHS viscosity upper to 3.5 cP and A5/B5 extended drain intervals with HTHS viscosity from 2.9 up to 3.5 cP) but all of them add a new test on effects of biodiesel (CEC L-104-16).

In this way, ILSAC proposes new GF-6 specifications, for the first license in April 2018 and the date of mandatory claim April 2019. This new ILSAC GF-6 encompasses two potential specifications, ILSAC GF-6A, which would replace the current ILSAC GF-5, with Phosphorous content from 0.06 % up to 0.08 %, and Sulphur content up to 0.5 %, with similar values to ACEA Class C. And the proposed ILSAC GF-6B, that would provide the same performance, but with the added aim of lower HTHS viscosity, from 2.3 cP up to 2.6 cP, to deliver potential further fuel economy benefits. This offers the possibility of operating at new viscosity ranges SAE 0/5W-16.


High Viscosity

HTHS > 3.5
Low Viscosity

2.9 < HTHS < 3.5
Very Low Viscosity
SAE XW-16
2.3<HTHS<2.6

ACEA (High SAPS)

A3/B3
A3/B4

A5/B5

--

ILSAC


GF-6A

GF-6B



ACEA C:

The main new in this Class is the introduction of a new Category 5 (C5), with same performance that Category C3 (TBN up to 6.0, Sulphur content up to 0.3 %, Phosphorous content from 0.07 % up to 0.09 % and Sulphur Ash content up to 0.8 %) but very low HTHS viscosity, from 2.6 cP up to 2.9 cP. The viscosity is similar to API GF-6B, so ACEA considers Class C to develop lubricants to deliver fuel economy.

In respect of the rest of the parameters, all the Class C add a new test on oil oxidation with biodiesel (CEC L-109-6) and effects of biodiesel, with the same performance that Class A/B.


High Viscosity
HTHS > 3.5
Low Viscosity
HTHS > 2.9
Very Low Viscosity
2.6 < HTHS < 2.9
Mid SAPS
S < 0.3 %
0.07 % < P < 0.09 % SA < 0.8 %

C3

C2

C5
Low SAPS
S < 0.2 %
SA < 0.5 %

C4

C1

--


ACEA E:

   This Class keeps their Categories E4, E6, E7, and E9, almost unchanged. We should keep in mind that all these categories have an HTHS viscosity upper to 3.5 cP, Categories E4 and E7 with High SAPS content, and Categories E6 and E9 with Low SAPS content; with requirements on bore polishing, piston cleanliness and wear (tests CEC L-101-08 and CEC L-099-08) for extended drain intervals (UHPD - Ultra-High-Performance Diesel), and requirements on soot induced wear and wear in liner, rings, and bearings (test ASTM D7468 and ASTM D7422) for standard drain intervals (SHPD - Super High-Performance Diesel) grouping Categories ACEA E4 and E6 in UHPD and Categories ACEA E7 and E9 for SHPD oils.

Also, Class includes new requirements on oil oxidation with biodiesel and, just for Categories E6 and E9, requirements on biofuel impacted piston cleanliness and engine sludge.

On the other hand, new API diesel engine oil standards, from December 2016, CK-4 and FA-4. Summarized, API CK-4 describes high HTHS viscosity upper to 3.5 cP and low SAPS content, in the same way, that CJ-4, but provide higher performance than this category and the older API CI-4 Plus, CI-4, and CH-4.

New API FA-4 describes the same performance that API CK-4 but with low HTHS viscosity from 2.9 up to 3.2 cP and viscosity ranges SAE 0/5/10W-30. So, heavy-duty diesel engine oils, even off-road, deliver potential further fuel economy benefits.


Bore polishing, piston cleanliness, and wear
(CEC L-101-08, CEC L-099-08)
Extended Drain Intervals
Soot induced wear and wear in liner, rings, and bearings
(ASTM D7468, ASTM D7422)

Standard Drain Intervals

High SAPS


E4

E7

Low SAPS
and
Biofuel impact

E6
E9
API CK-4

Low Viscosity


--

API FA-4

Monday, 23 January 2017

Nuevas Especificaciones Lubricantes ACEA 2016

En diciembre de 2016, con fecha límite de aplicación obligatoria diciembre 2017, ACEA ha publicado la versión 2016 de las secuencias de lubricantes para Europa (ACEA European Oil Sequences), esta nueva secuencia presenta algunas novedades interesantes, además de comentarlas en este informe las vamos a comparar con las novedades de API / ILSAC.  

En línea con las últimas versiones, ACEA mantiene las Clases de lubricantes A/B, para motores gasolina y diésel ligero; C, para motores gasolina con catalizador y motores diésel ligero con sistemas de post-tratamiento de gases de escape; y E para motores diésel pesado.


ACEA A/B:

La primera novedad en esta Clase es la eliminación de la Categoría 1 (A1/B1) referente a lubricantes de alto contenido en cenizas SAPS, baja viscosidad HTHS, entre 2.9 y 3.5 cP excepto lubricantes xW-20 con HTHS superior a 2.6 cP.

El resto de Categorías A3/B3, A3/B4 y A5/B5 se mantienen en las mismas condiciones que la versión anterior (A3/B3 y A3/B4 con viscosidades HTHS superiores a 3.5 cP y A5/B5 con HTHS entre 2.9 y 3.5 cP) a las que se añaden un ensayo de efectos de la utilización de biodiesel (CEC L-104-16).

En este sentido ILSAC presenta la nueva Categoría GF-6, con primera licencia en abril de 2018 y fecha límite de obligatoriedad en abril 2019. En este caso ILSAC presenta dos versiones, ILSAC GF-6A, que sustituye a ILSAC GF-5, con contenido en fósforo entre 0.06 y 0.08 % y en azufre entre hasta 0.5 %, con valores similares a las ACEA Clase C. Y una nueva ILSAC GF-6B, con el mismo nivel de rendimiento, pero de muy baja viscosidad con viscosidades SAE 0/5W-16 para mejorar el ahorro de combustible.


Alta Viscosidad

HTHS > 3.5
Baja Viscosidad

2.9 < HTHS < 3.5
Muy baja Viscosidad
SAE XW-16
2.3<HTHS<2.6

ACEA (Alto SAPS)

A3/B3
A3/B4

A5/B5

--

ILSAC


GF-6A

GF-6B



ACEA C:

La principal novedad en esta Clase es la introducción de una nueva Categoría 5 (C5), para lubricantes con nivel de rendimiento de Categoría C3 (TBN superior a 6.0, contenido en azufre hasta 0.3 %, en fósforo entre 0.07 y 0.09 % y en cenizas sulfatadas hasta 0.8 %) pero con muy baja viscosidad HTHS, entre 2.6 y 2.9 cP. Un nivel de viscosidad similar a API GF-6B, con lo que ACEA apuesta por la Clase C para desarrollar lubricantes que proporcionen ahorro de combustible.

En cuanto al resto de parámetros, en toda la Clase C se añaden ensayos de oxidación de lubricante en presencia de biodiesel (CEC L-109-6) y efectos de la utilización de biodiesel con los mismos niveles de rendimiento que la Clase A/B.


Alta Viscosidad
HTHS > 3.5
Baja Viscosidad
HTHS > 2.9
Muy baja Viscosidad
2.6 < HTHS < 2.9
Medio SAPS
S < 0.3 %
0.07 % < P < 0.09 % SA < 0.8 %

C3

C2

C5
Bajo SAPS
S < 0.2 %
SA < 0.5 %

C4

C1

--


ACEA E:

   Esta Clase se mantiene, con las mismas Categorías E4, E6, E7 y E9, sin apenas cambios. Recordamos que todas estas categorías tienen viscosidad HTHS superior a 3.5 cP, Categorías E4 y E7 con alto contenido en SAPS, y Categorías E6 y E9 con limitación de contenido en SAPS; diferentes requisitos de pulido de cilindros, limpieza de pistones y desgaste (ensayos CEC L-101-08 y CEC L-099-08) para largos periodos de cambio (UHPD - Ultra High Performance Diesel), y desgaste por carbonillas y en cojinetes y segmentos (ensayos ASTM D7468 y ASTM D7422) para perdiodos de cambio normales (SHPD - Super high Performance Diesel) agrupando las Categorías en ACEA E4 y E6 para los primeros y ACEA E7 y E9 para los segundos.

Además se incluyen los nuevos de oxidación en presencia de biodiesel y, para ACEA E6 y E9, el impacto de biocombustibles en limpieza de pistones y formación de lodos.

Por su parte, API ha presentado, en diciembre de 2016, las nuevas Categorías CK-4 y FA-4. La Categoría CK-4 presenta alta viscosidad (HTHS superior a 3.5 cP) y bajos contenidos en SAPS, como CJ-4, pero superando los niveles de rendimiento tanto de esta categoría como de las anteriores CI-4 Plus, CI-4 y CH-4.

La nueva API FA-4 presenta el mismo nivel de rendimiento de CK-4 pero con bajas viscosidades (HTHS entre 2.9 y 3.2 cP) SAE 0/5/10W-30. Con lo que los vehículos pesados, incluso de uso fuera de carretera, disponen de lubricantes de ahorro de combustible.


Preferencia Pulido de cilindros, Limpieza pistones y Desgaste
(CEC L-101-08, CEC L-099-08)
Largos Periodos de Cambio
Preferencia Desgaste por carbonillas y Desgaste cojinetes y segmentos
(ASTM D7468, ASTM D7422)

Periodos de Cambio Estandard

Alto SAPS


E4

E7

Bajo SAPS
e
Impacto Biodiesel

E6
E9
API CK-4

Baja Viscosidad


--

API FA-4

Tuesday, 15 March 2016

Formulation of Lubricants: Base Oils

Base oils are the fundamental building blocks of a finished lubricating oil or grease, their properties and endurance are depending on their quality. Typically comprise 80 % - 90 % of the finished lubricant.
Every base oil meet a series of properties related to its chemical composition, the main ones are:
· Oxidation stability, degradation process by oxidative mechanisms induced by temperature.
· Thermal stability, high-temperature stability without oxygen.
· Carbon residue, solid residues formation, as soot, produced by high temperature.
· Natural solvency, capacity to solve chemical products, as additives or contaminants.
· Seal compatibility, base stocks should protect seals.
· Viscosity index, or viscosity-temperature relationship.
· Low-temperature properties, base stocks should have low wax content, because they have got a high poor point.
· Volatility, the tendency to evaporation, high volatility reduce flashpoint.
· Oxidation, corrosion, and rust, base oils should be water and acid-free.
· Colour doesn't influence the final result. Refined base oils are brown-amber colored, hydrotreated are yellow-golden colored, synthetic base oils are uncolored, and heavy-based oils are black-greenish colored.
· Toxicity, as much refined are the base oils as low toxicity they are, reaching even no toxic base oils.
· Biodegradability, high refined and synthetic base oils are practically biodegradable. The biodegradability is ensured by bio-based ester.
· Demulsification, the ability of oil and water to separate.
· Foam characteristics, the tendency to foam formation and the stability of the foam results.

1.  Mineral Base Oils.
They are manufactured from crude oil, separated by a distillation process in a vacuum column, refining in several stages and various treatments which result in a large variety of medical, cosmetic, industrial and automotive oils and lubricants.
In any case, mineral base oils are combinations of paraffin, iso-paraffin, naphthene, aromatic, and sulfur and nitrogen compounds. According to content in paraffin and iso-paraffin, base oils are called naphthenic (content in paraffinic from 42 % to 50 %), neutral (from 50 % to 56 %) and paraffinic (from 56 % to 67 %). 
Figure 1 Mineral base oils: (a) y (b) - Paraffin, (c) - Naphthene, (d) - Aromatic.
Mineral-based oils provide good lubricity and protection against corrosion, compatibility with seals and paints, natural solvency, hydrolytic stability, and low costs.
On the other hand, they have got a low flash point, high pour point, and low oxidation and temperature stability, so the range of operation temperature and duration is limited.
API (American Petroleum Institute, USA) classifies base oils by sulfur content, saturates content and viscosity index.
Usually, Group I base oils are produced by refining and dewaxing, but Group II and Group III are produced by hydrotreating, followed by dewaxing or wax isomerization. 

 Base Oils
Saturates Content
Sulfur Content
Viscosity Index
 Group I
<90 %
>0.03 %
80 – 120
 Group II
>90 %
<0.03 %
80-120
 Group III
>90 %
<0.03 %
>120

Table 1 API Clasification (1st part)

2.  Re-refined Base Oils.
Used oils content wear metals, oxidation wastes, particles from combustion, fuel, water, and anti-freeze, so the oil should be changed, but the most of molecules of base oil are in good condition and can be used again. A re-refining process eliminates contaminants and additives to blend a new lubricant.
The regeneration process starts with a chemical treatment to bind wear metals and dirt to make their elimination easier. Next, the dewatering and vacuum distillation process removes water and lighter oils. Finally, a hydrotreating process introduces hydrogen to remove sulfur, nitrogen, chlorine and oxidation products.
The process produces Group I base oils and can reach Group II base oils by high-quality hydrotreating.

3.  Gas-to-Liquids (GTL) Base Oils.
Gas-to-Liquids is a process for converting natural gas into fuels and base oils, GTL process tears natural gas molecules apart and reassembles them into longer chain molecules. The result is extremely pure base oil, formed by iso-paraffin, free of contaminants such as sulfur, aromatics, and metals; that can be considered Group III or can be transformed to Group IV.
Iso-paraffin produced by the GTL process provides good viscosity properties, oxidation resistance, and good low-temperature conditions.

4.  Synthetic Base Oils.
Synthetic base oils are produced, mainly, from low molecular weight hydrocarbons, the process produces high quality and extended service life capability base oils under extremes operating conditions.
In general terms, synthetic base oils are able to handle a wider range of application temperatures, so they provide the best protection both to high and low temperatures.

Base Oils
Type of Base
Group IV
Polyalphaolefin
Group V
Other Synthetic Bases

Table 2 API Clasification (2nd part)

The more usual synthetic base oils are:
a.  Synthetic Hydrocarbon Fluids:
The SHFs comprise the fastest-growing type of synthetic lubricant base stock, they all are compatible with mineral base stocks.
Polyalphaolefins (PAO) are unsaturated hydrocarbons with the general formula (-CH2-)n, free of sulfur, phosphorus, metals, and waxes. Provide excellent high-temperature stability and low-temperature fluidity, high viscosity indexes, low volatility and compatible with mineral base oils. Although the oxidation stability is lower than mineral oils and their solvency of polar additives is poor, so usually PAOs are combined with other synthetic oils.
This base oil is recommended for engine oils and gear oils.
Alkylated Aromatics formed by alkylation of an aromatic compound, usually benzene or naphthalene. Provide excellent low-temperature fluidity and low pour points, good solubility for additives, thermal stability, and lubricity. Although their viscosity index is about the same as mineral oils, they are less volatile, more stable to oxidation, high temperatures, and hydrolysis. They are used as the base of engine oils, gear oils, and hydraulic fluids.
Polybutenes are produced by controlled polymerization of butenes and isobutylenes. Compared with other synthetic base oils are more volatile, less stable to oxidation and their viscosity index is lower; their tendency to produce smoke and shoot deposits is very low so they are used to formulate 2-Stroke engine oils, also as gear oils combined with mineral or synthetic base oils.
b.  Polyalkylene Glycols (PAG):
PAG are polymers made from ethylene oxide (EO), propylene oxide (PO), or their derivatives. Solubility in water or other hydrocarbon is depending on the type of oxide.
Both provide good viscosity/temperature characteristics, low pour point, high-temperature stability, high flash point, good lubricity, good shear stability, PAGs are not corrosive for most of the metals and compatible with rubber.
The main disadvantages are low additive solvency and pour compatibility with lubricants, seals, paints, and finishes.
They are used as a base for hydraulic brake fluids (DOT3 and DOT 4) due to their water solubility, 2-Stroke engine oils due to the low deposits at high temperatures, compressor lubricants, and fire-resistance fluids.
c.  Synthetic Esters:
They are oxygen-containing compounds that result from the reaction of an alcohol with an organic acid. They have good lubricity, temperature, and hydrolytic stability, the solvency of additives and compatibility with additives and other bases. But some esters can damage seals so require special compositions.
They are used as base oils for engine oils, mixed with other synthetic bases, because they improve low-temperature properties, reduce fuel consumption, increase wear protection and viscosity-temperature properties.
Also, as 2-Stroke engine base oils, they reduce deposit formation, protecting rings, pistons, and sparks. They allow reducing the quantity of lubricant from 50:1 of mineral oils to 100:1 and up 150:1 due to their outstanding lubricity.
Phosphate Esters are used as anti-wear additives due to their high lubricity and as base oils for hydraulic fluids and compressor oils due to their low flammability. But their hydrolytic and temperature stability and viscosity index is low and their low-temperature properties are poor. Also, they are aggressive with paints, coats, and seals.
Polyol Esters have good high-temperature stability, hydrolytic stability and low-temperature properties, low volatility and low Viscosity Index; the polyol esters also may have more effect on paints and cause more swelling of elastomers. To take advantage of their miscibility with hydrofluorocarbon (HFC) refrigerants, polyol esters are used in refrigeration systems.
d.  Polyethers:
In this group, we can find Perfluorinated Polyethers (PFPE) with a density nearly twice that of hydrocarbons, they are immiscible with most of the other base oils and non-flammable under all practical condition. Very good viscosity-temperature and viscosity-pressure dependence, high oxidation and water stability, inert chemically and radiation stable; these properties joined their shearing stability. They are suitable as hydraulic fluids in spacecraft and as a dielectric in transformers and generators.
Polyphenyl Ethers have excellent high-temperature properties and resistance to oxidation but they have fair viscosity-temperature properties, they are used as hydraulic fluid for high temperature and radiation resistance.
Polysiloxanes or Silicones have high viscosity index, over 300, low pour point, high-temperature stability, and oxidation stability so run well in a wide range of temperatures; they are chemically inert, non-toxic, fire-resistant, and water repellent, they have low volatility and are compatible with seals and plastics. Their disadvantage is formation of abrasive silicon oxides if oxidation does occur, effective adherent lubricating films are not formed due to their low surface tension, and also show poor response to additives. They are used are brake fluids and as antifoam agents in lubricants.
The table compares different synthetic base oils properties against mineral oil.


Table 3 Comparison among base oils.

5.  Bio-bases Oils.
They are mainly produced from soybeans, rapeseed, palm tree, sunflowers, and safflowers. Their advantages are high biodegradability, superior lubricity, higher flash point, and viscosity index; but their pour point is high and the oxidative stability is poor, also the recycling is difficult.
The main applications are hydraulic fluids, transmission fluids, gear oils, compressor oils, and greases. Better when an application is total loss, indoors or where low pour point is not an issue, food industry or environmentally-sensitive areas.