hostapur sas a traditional speciality
TRANSCRIPT
®Hostapur SAS
Exactly your chemistry.
A traditional speciality for innovative
cleaners
A traditional speciality for innovative
cleaners
Functional Chemicals DivisionFunctional Chemicals Division
02
The demands imposed on surfactants have changed in the last
few decades. Not only is an optimum price-performance
ratio expected, but high safety and environmental compatibility
are also prime considerations.
The secondary alkane sulphonate Hostapur SAS meets these
requirements in every respect. This surfactant has been
highly successful on the market for many years. To date, over
one million metric tonnes of Hostapur SAS have been
produced in our european facilities.
One of the reasons for this great success is the optimum environ-
mental properties as shown by the life cycle assessment.
We are convinced that over the coming decades Hostapur SAS
will continue to maintain and expand its position as one of the
leading principal surfactants.
This brochure describes the specific properties and universal
uses of Hostapur SAS. Further information and individual
advice can be obtained.
® Registered trademark of Clariant
®Hostapur SASAn environmentally compatible surfactant with optimum application properties
03
ContentsProduct profile 04 Toxicological and
environmental properties
Processing
Technical Data
Synthesis 06
Applications 08
Physical and chemical propertiesSurface activity 22
Foaming power 24
Rheological properties 24
pH stability 25
Heat stability 25
Detergent action 25
Solubilization 25
Emulsifying action 25
Stability to hard water 26
Electrolyte stability 26
Chlorine-/oxidation stability 26
Enzyme stability 27
Synergistic interaction with 28
soil release polymers
Solubility in water 29
Low-temperature properties 29
Dishwashing liquids 09
Detergents 12
Household cleaners 15
Cosmetic hair and body 16
care products
Industrial cleaners 19
Special technical sectors 20
Toxicological profile 30
Ecology 32
Life cycle assessment 33
Transport 34
Storage 35
Conveying/mixing 36
Dilution 36
Handling 37
C-chain distribution 38
Physical/chemical data 38
Registration status 39
Ecological data 40
Analysis 41
Summary of the properties 41
of Hostapur SAS
AbbreviationsSAS = Secondary alkane sulphonate
LES = Lauryl ether sulphate
LAS = Linear alkylbenzene sulphonate
AES = Alkyl ether sulphate
LS = Lauryl sulphate
SRP = Soil release polymer
Literature 42
environmentally friendly anionic surfactants for the detergent,
chemical-technical and cosmetic industries, based on
secondary alkane sulphonate sodium salt, starting product:
n-paraffins.
Chemical structure
m + n = 10 – 14; the sulphonate group is distributed over
the carbon chain in such a way that it is mainly the secondary
carbon atoms that are substituted.
INCI name
Sodium C14-17 sec-Alkyl sulphonate
CAS numbers
85711-69-9, USA: 68608-26-4
EINECS/ELINCS numbers
288-330-3
04
Product profileHostapur SAS grades
CH3 – (CH2)m – CH – (CH2)n – CH3
SO3-Na+
Hostapur SAS 30
Hostapur SAS 60
Active content
approx. 30 %
approx. 60 %
Appearance (25°C)
clear faintly yellowish liquid
yellowish soft paste
Commercially available grades
05
The Hostapur SAS grades are noted
for the following specific application
properties:
• Very good solubility
– spontaneous dissolving
– good low-temperature properties
• High wetting action
– good drainage properties
and rapid drying of dishes
• Pronounced foaming power
– high yield of the finished products
in use
• Excellent grease- and
soil-dispersing action
– development of finished products
with defined and optimum detergent,
cleaning and degreasing action
• Viscosity-depressing action
– permits the formulation of flowable,
highly concentrated detergents
and cleaners with low water content
and without solvents and preser-
vatives; saves transport and pack-
aging costs
• Outstanding enzyme compatibility
– positive influence on enzyme stability
• Chemical stability over a wide
pH range
– formulation of alkaline cleaners with
long storage stability
– stability to oxidizing agents; intended
for chlorine-containing all-purpose
cleaners
• Increases action of modern detergent
additives, e.g. soil release polymers
• Very good electrolyte compatibility
– manufacture of heavy-duty
detergents with high builder content
• Good skin compatibility
– formulation of mild dishwashing
liquids
• Possibility of combination with
anionic, nonionic and amphoteric
surfactants
– versatility in formulation
– synergistic effects in use
– electrically neutral salts can be
formed with cationic surfactants
• Cost reduction
– possibility of manufacturing highly
concentrated liquid cleaners without
hydrotropes
• Environmentally friendly surfactant
of low aquatic toxicity
– rapid biodegradation
• Range of grades
– Hostapur SAS is available in liquid
and paste form
06
SynthesisThe secondary alkane sulphonate Hostapur SAS is synthesized by sulphoxidation of n-paraffins. 1 – 6
Sulphoxidation, a basic reaction in aliphatic organic chemistry,
was discovered as early as 1940 by C. Platz at the Höchst
site of the former IG Farben AG 7, when n-paraffins were
treated with sulphur dioxide and oxygen and simultaneously
exposed to ultraviolet light. Since then the process has been
developed into the present Hoechst light/water process 8 – 11,
which can be described summarily by the following equation:
R–H + 2SO2 + O2 + H2O →RSO3H + H2SO4
Substitution is done largely at the methylene groups; the
terminal methyl groups are considerably less reactive. 12 – 14
Besides the monosulphonates, smaller amounts of di- and poly-
sulphonates are also formed, see Technical data, page 38.
The synthesis of
Hostapur SAS by the
Hoechst light/water
process yields detergent
raw materials of con-
sistently high quality. In
this process the raw
material and energy con-
sumption as well as the
emissions are optimized
at a minimum.
07
The flow chart above, fig. 1, shows in
diagrammatic form the industrial-scale
production of Hostapur SAS.
The industrial-scale sulphoxidation of
the n-paraffins by the Hoechst light/water
process is carried out in a multi-lamp
reactor. The gas mixture of SO2 and
O2 is introduced by means of gas
injection equipment and on exposure
to UV light produced in high-pressure
mercury lamps made of quartz glass,
sulphoxidation of the n-paraffins takes
place in the presence of water. The
reaction gas is circulated. A compressor
is needed for maintaining gas circula-
tion, as is a cooling system for adjusting
the required temperature. The reaction
liquid is removed at the bottom of the
reactor and the product phase – the
lower phase – is separated in a separating
system. The upper phase – paraffin
phase – is cooled and replenished with
water and n-paraffin and then returned
to the reactor. After concentration of the
product phase in a vacuum, separation
of the sulphuric acid and neutralization
of the concentrate with sodium hydrox-
ide solution, the remaining paraffin is
driven off with superheated steam. The
distillate is again separated in a separ-
ator and the paraffin phase is returned to
the reaction. The remaining melt is finally
processed into aqueous solutions,
Hostapur SAS 60 or Hostapur SAS 30.
Very pale reaction products of high
quality are obtained.
One characteristic of the process
described is that no other chemical
auxiliaries, for example, solid catalysts
or solvents, are required. The n-par-
affins used for synthesis are obtained as
a matter of course in the production
of kerosene, and so Hostapur SAS
manufacture offers a useful outlet for this
material. The precise material flow
and the energy balances are described
in section Life cycle assessment, page 33.
reaction
separation neutralisation
rectification
SO3 O2 n-paraffin n-paraffin H2O
H2O
SO2O2n-paraffin NaOH
SAS-paste60 %
H2O
Fig. 1: Sulphoxidation process
08
ApplicationsThe Hostapur SAS grades are principal surfactants with excellent ecological, toxicological and economic properties.
Because of their pronounced surface activity and specific
properties, they have a very wide range of uses. Their major use
is in dishwashing liquids, in which Hostapur SAS has proved
highly successful for over thirty years. The Hostapur SAS
grades are used as principal surfactants in combination with
other surfactants for the manufacture of virtually all types of
detergents and cleaners for household and industrial use.
Most important uses for Hostapur SAS
Dishwashing liquids Standard dishwashing liquids
Dishwashing liquid concentrates
Laundry detergents Liquid detergents
Detergent powders
Detergent pastes
Soaking agents
Household cleaners All-purpose cleaners
Liquid metal/ceramic cleaner
Sanitary cleaners
Floor cleaners
Glass cleaners
Cosmetic hair and Shampoos
body care products Showergels
Foam baths
Liquid soaps
Toothpastes
Industrial cleaners Automotive cleaners
Metal degreasing agents
Alkaline rust removers
Hand cleaners
Special technical Fire extinguishing foams
sectors Emulsion polymerization
Textile and leather auxiliaries
Oilfield chemicals
Advantages of
Hostapur SAS in
dishwashing liquids
Very good solubility
and thus economizing
on solubilizers
Very good rinsing action,
rapid drainage, shine
and rapid drying
Optimum cleaning
and degreasing action
with a low concentration
of active detergent and
thus high dishwashing
efficiency
Creamy, fine-bubble foam,
which can act as a
soil- and fat-suspending
agent
Compatibility with
anionic, nonionic and
amphoteric surfactants.
As a result synergistic
effects are often achieved
Faint inherent colour
and therefore only small
amounts of dye are re-
quired if coloration is
needed
Good skin compatibility,
especially in combination
with other surfactants
therefore be preserved if the finished
formulations have a low application
concentration and a high water content.
Most of the commercially available pre-
servatives are suitable for this purpose.
A preservative loading test must how-
ever always be carried out. Formulations
with a fairly high active detergent con-
tent, for example, over 40 %, usually do
not need to be preserved.
Microbiological studies of Hostapur
SAS as a function of the concentration
of active detergent showed that an
inherently bacteriostatic effect is dis-
played with concentrations as low as
about 40 %. Therefore the sixty-percent
commercial grade Hostapur SAS 60
is not preserved and, is suitable for the
manufacture of preservative-free pre-
parations.
The low-temperature stability of the
dishwashing liquids, for example, at
-5°C, can be further improved by small
additions of OH-group-containing
substances such as ethanol. An addition
of 2 % ethanol and 2 % urea is recom-
mended for concentrates with about
40 % active detergent.
pH adjustment is generally done with
sodium hydroxide solution or citric
acid. When alkyl amidobetaines are used,
an increase in viscosity may possibly
occur in the acid pH range.
If necessary, moisturizing agents
can additionally be incorporated in the
formulation. Because of the good
dermatological properties of Hostapur
SAS this is, however, not necessary
in most cases.
09
Consumers expect modern dishwashing
liquids primarily to have optimum clean-
ing action and safety in use, in other
words good skin compatibility, coupled
with optimum environmental compatibility.
Another desirable feature is high yield,
which can be achieved with concen-
trates. Adequate foaming power in the
presence of grease and absence of
streaks on dishes are taken for granted.
Hostapur SAS as a principal sur-
factant in combination with amphoteric
surfactants such as the alkyl amidobe-
taines and/or alkyl ether sulphates and/
or nonionic surfactants as co-surfactants
enables dishwashing liquids to be devel-
oped that meet the above-mentioned
requirements almost ideally. 15 – 20
The high solubility of Hostapur SAS
enables highly concentrated dishwash-
ing liquids with good storage stability to
be formulated without the addition of
cost-increasing solubilizers. The market
share of this product class is rising
steadily.
These concentrates with a low
water content offer primarily economic
advantages such as lower transport
and packaging costs. It is often possible
to dispense with a preservative for
these concentrates. Guide Formulations
are available.
Preservation of formulations contain-
ing Hostapur SAS depends foremost
on the composition of the finished product
in question. Hostapur SAS is a rapidly
biodegradable surfactant and must
Dishwashing liquids
10 20 30 40
100000
10000
1000
100
10
visc
osity
η [m
Pas]
concentration c [%]
B
A
A 4 parts SAS : 1 part LES + 10 % ethanol + 10 % ureaB 4 parts LAS : 1 part LES + 10 % ethanol + 10 % urea
10
ApplicationsOf the numerous possibilities for combin-
ing Hostapur SAS with surfactants that
have a different chemical structure two-,
three- and four-component combin-
ations are described below by way of
example; these mixtures enable dishwash-
ing liquids with tailor-made properties to
be developed.
The skin compatibility and the foaming
power can be optimized by combining
Hostapur SAS and alkyl ether sulphate,
for example, ®Genapol LRO or ZRO. In
practice a mixture of about 3 to 4 parts
Hostapur SAS and about one part alkyl
ether sulphate, relative to 100 % active
substance (ratio 3:1 or 4:1), has proved
successful.
This combination also enables liquid
concentrates with about 40 % active
detergent content to be formulated with-
out the additional use of a solubilizer.
Moreover, with this concentration the
mixture of Hostapur SAS and alkyl ether
sulphate is better and more rapidly
soluble in the dishwashing water than
the individual components separately.
The stability to hard water and the
foaming power in hard water are also
optimized by the alkyl ether sulphate
content. By adding magnesium ions or
other divalent metal ions to the Hostapur
SAS: alkyl ether sulphate mixture the
foaming power can be further improved,
especially in the extremely low water
hardness range.
A crucial parameter for the pro-
cessing and use of dishwashing liquids
is rheology. The viscosity of the com-
mercially available products is about
400 to 700 mPas/20°C. This viscosity can
be achieved easily with 5 to 7 % sodium
chloride in Hostapur SAS: alkyl ether
sulphate mixtures in the ratio 70:30,
relative to 100 % active detergent, and a
content of 12 to 15 % active detergent
in the final formulation.
More highly concentrated Hostapur
SAS: alkyl ether sulphate mixtures with
a 40 % active detergent content can
be adjusted easily to viscosities suitable
for practical purposes by incorporating
viscosity-depressing additives such as
ethanol and/or urea, as shown in fig. 2.
Fig. 2 shows the viscosity at +20°C
as a function of the concentration of
Hostapur SAS/alkyl ether sulphate mix-
tures with the addition of ethanol and
urea. This means that a 40 % formulation
consisting of 32 % Hostapur SAS and
8 % lauryl ether sulphate contains 4 %
ethanol and 4 % urea. Guide Formulati-
ons are available.
Fig. 2: Viscosity of Hostapur SAS: alkyl ether sulphate mixtures
with the addition of ethanol and urea
11
The cleaning action can be tested in
the mini-plate test on glass plates soiled
with grease or in the “plate test”.
An example is given in fig. 3 above.
Three-component mixtures can be
formulated
• with Hostapur SAS, alkyl ether
sulphate and betaine (alkyl dimethyl
betaine or alkyl amidobetaine), for
example, mixed in the ratio 5:2:1 or
7:1:1, or
• with Hostapur SAS, alkyl ether
sulphate and nonionic fatty alcohol
polyglycol ethers.
A corresponding Guide Formulation is
available.
When betaines are used, not only the
dermatological properties but also the
rheological properties are improved. As
a result additional moisturizing agents
and viscosifiers are often not required. 21
A fatty alcohol polyglycol ether con-
tent, as a function of the fatty alcohol
radical and the degree of ethoxylation,
can produce an increase in solubilizing
and emulsifying action as well as better
wetting. These influence the cleaning
effect to a marked degree when the prod-
uct is used. The pronounced solubiliz-
ing action of Hostapur SAS can also
obviate the need for special solubilizers
for slightly soluble perfume oils, and
thus cut costs.
Finally, there is the possibility of
combining the four surfactant classes:
alkane sulphonate, alkyl ether sulphate,
betaine and fatty alcohol polyglycol
ether. Guide Formulations are available.
In the aforementioned numerous
possible combinations the economical
principal surfactant Hostapur SAS is
used as the main component. Depending
on the mixing ratio, the application prop-
erties of these combinations such as
degreasing, low-temperature properties,
foaming power, feel on the skin, rheol-
ogy and dermatology can be optimized. 22, 23
15
10
5
0
num
ber o
f pla
tes
0 0.3 0.6 0.9 1.2 1.5
concentration: 0.33 g a.s./Lwater hardness: 0 ppm CaCO3 (0°d)
Mg++-concentration [%]
Fig. 3: Mini-plate test of Hostapur SAS: alkyl ether sulphate
(4:1 mixtures) as a function of magnesium ion addition
12
surfactant can be combined in amounts
of up to 40 % with alkyl ether sulphates,
nonionic surfactants, amphoteric sur-
factants and/or soap.
Another possibility of formulating
with Hostapur SAS is to develop
highly viscous to gel-like detergents with
special rheological properties in use.
Hostapur SAS permits a high surfactant
concentration and rapid dissolving
in use.
Looking ahead, the liquid detergents
will undoubtedly soon achieve a
larger share of the detergent market in
Europe. This applies particularly
to products that have an active deter-
gent content of 50 percent and above.
They thus meet the requirements for
low-energy manufacture, high efficiency
coupled with easy low metering and
environmental friendliness. Detergents
with high active substance concen-
trations can be developed without diffi-
culty with Hostapur SAS.
Detergents proximately the same ratio. In addition
they contain solubilizers such as ethanol,
propylene glycol and/or xylene sulpho-
nate, possibly enzymes, optical brighten-
ers and chelating agents.15 – 24 Guide
Formulations are available.
If enzymes are used in the formula-
tions, Hostapur SAS offers better enzyme
compatibility than most of the anionic
surfactants such as linear alkyl benzene
sulphonate or alkyl sulphate.
As with the dishwashing liquids, when
Hostapur SAS is used as the principal
surfactant, for example, instead of linear
alkyl benzene sulphonate, considerable
savings of solubilizer such as ethanol
can be achieved. Optimum liquid deter-
gents without builders contain as main
components Hostapur SAS, readily water-
soluble ethoxylated fatty alcohols and
alkyl ether sulphate as well as neutralized
coconut soap.25
If builders are also incorporated in
the liquid detergents, it is advantageous
to use freely soluble surfactants such
as Hostapur SAS. A further beneficial
property of Hostapur SAS is its good
electrolyte compatibility, in other words
good compatibility with the builders.
The liquid light-duty detergents are
used at temperatures up to a maximum
of 60°C. Hostapur SAS as a principal
Liquid detergents
Liquid detergents are a major field of
application for Hostapur SAS on
account of its pronounced detergent
properties.
The liquid detergents are divided
below into light-duty liquids for
delicate wash and heavy-duty liquid
detergents.
In the USA the importance of these
heavy-duty liquid detergents is greater-
than in Europe. The US liquid detergents
contain between 10 and 30 % active
surfactant. The builder systems used in
liquid products (e.g. citrate, silicates)
are typically less effective than those
used in powder detergents (e.g. layered
silicate, zeolite, polycarboxylate, carbo-
nate). In the USA, washing machines
are designed differently from those in
Europe and the washing temperatures
are lower and typically range from 5 to
40°C. US liquid detergent formulations
typically do not contain any bleaching
agents as they are poorly stable in this
systems.
In Europe the liquid detergents used
have a different structure. They gene-
rally consist of a mixture of anionic and
nonionic surfactants with soap in ap-
Applications
13
Good calcium ion
tolerance
Saving on enzymes
Synergistic effects with
soil release polymers
Advantages of Hostapur SAS in heavy-duty and
light-duty liquid detergents
Better solubility in water
than linear alkyl benzene
sulphonate
High solubility, enabling
highly concentrated
detergents to be manu-
factured
Hydrotropes can be
reduced in quantity or
omitted
Good detergent action
Good dispersion and
solubilization of the soil,
oil and fat particles
Pronounced foaming
power in the presence of
soil and fat
Good compatibility with
electrolytes, which
enables the hydrotropes
to be reduced or even
eliminated
Detergent powders
Hostapur SAS can also be used to
manufacture the various powder deter-
gent types. The excellent solubility
and the solubilizing properties lower the
viscosity of the slurry. This brings a
number of major advantages, especially
substantial energy savings and capacity
increases in the manufacture of deter-
gent powders by the hot spraying
process.
Fig. 4 shows an example of typical
viscosity/solids content curves, deter-
mined on rehydrated tower powders.The
powders each contained 9 % Hostapur
SAS (100 %) or linear alkyl benzene
sulphonate (100 %). The substantially
lower viscosity of the Hostapur SAS-
containing slurry is clearly discernible;
measured in the Brabender Plastograph,
model PI 3S. 26
Powder-type heavy-duty detergents
can contain between 6 and 10 %
Hostapur SAS, relative to 100 % active
detergent, in combination with fatty
alcohol polyglycol ethers and soap as
surfactant components.
Powder-type light-duty detergents
contain 10 to15 % Hostapur SAS,
relative to 100 % active detergent, in
combination with small amounts
of soap and fatty alcohol polyglycol
ethers.
14
Advantages of
Hostapur SAS in
detergent powders
Lower slurry viscosity
Higher solid content
Energy and time saving
Increase of spraying
capacity
Reduction of hydrolysis
of sodium tripolyphos-
phate due to less water
content
Applications
600
500
400
300
200
100
0
rel.
visc
osity
[sca
les*
]
55 60 65solid content [%]
SASLAS
* measured with “Brabender Plastograph”
Fig. 4: Relative viscosities of detergent slurries as a function
of the solids content and the type of sulphonate
Household cleaners Liquid metal/ceramic cleaner
Liquid metal/ceramic cleaner usually
contains a high abrasive content.
The insoluble components are dispersed
in the aqueous surfactant phase. To
prevent the solid particles from settling,
firstly abrasives with as small a particle
size as possible are used and secondly
a fairly high viscosity is employed.
By combining Hostapur SAS with
other surfactants, for example, with®Genapol UD 030, it is often possible
without adding viscosifiers to increase
the viscosity to a level where settling
of the abrasive particles is prevented
or reduced.
The usually thixotropic formulations
display advantageous properties in
use: during storage the viscosity is high
and when subject to shear stress
during application the metal cleaner
becomes less viscous, in other words it
flows readily from the bottle and can
be spread easily over the surface to be
treated.
Depending on its composition, the
liquid metal cleaner can be applied
to stainless steel, chromium, copper
and brass surfaces. Besides a mild and
gentle cleaning action, consumers
expect above all a shiny finish and a
water-repellent effect. The finished pro-
ducts are, however, intended to be
suitable as widely as possible for the
cleaning of glass ceramics. Here,
too, rapid wetting of the surface to be
cleaned, as made possible by Hostapur
SAS, is important.
Guide Formulations are available.
Advantages of Hostapur
SAS in liquid all-purpose
cleaners
Excellent wetting action
Rapid distribution over
the dirty, greasy surfaces
to be cleaned
Electrolyte compatibility
Reduction in or elimin-
ation of hydrotropes
Strong degreasing and
cleaning action
Largely streak-free
surfaces
Good solubility
Manufacture of highly
concentrated all-purpose
cleaners
Good skin compatibility
Advantages of Hostapur
SAS in liquid metal/
ceramic cleaner
Advantageous rheolog-
ical properties when
applied
Stabilization of the
abrasives
Good wetting action
increases efficiency
Good grease-dissolving
power
15
Liquid all-purpose cleaners
Liquid all-purpose cleaners are the
predominant household cleaners
because of their ease of metering and
wide range of uses. In general they
are adjusted to a fairly low concentration
of active detergent. Owing to the elec-
trolyte content, for example, sodium
chloride or sodium carbonate, solubility
problems and thus cloudiness may
occur. Hostapur SAS, on the other
hand, has specific advantages for the
formulation of all-purpose cleaners
because of its excellent solubility and
electrolyte compatibility. 27, 28
This also applies to the incorporation
of fairly large amounts of water-soluble
active detergents or to the formulation
of fairly highly concentrated finished
products. The latter can be produced
with Hostapur SAS without any great
problems; an addition of solvent such
as butyl diglycol is often advantageous
here. Abrasives such as calcium carbo-
nate can also be combined in high
amounts with Hostapur SAS. For the
effective use of liquid all-purpose
cleaners, high fat-dissolving power and
soil-dispersing power are of crucial
importance. Hostapur SAS brings these
advantages in combination with other
components.
In addition the product has an excellent
wetting action even at low temperatures.
This is particularly important for rapid
cleaning; and equally for a largely streak-
free and residue-free removal of dirt.
16
Cosmetic hair and bodycare products
ApplicationsThe allround cleaners for baths are
intended to be effective at fairly low
surfactant concentrations. As a result
of the pronounced wetting and cleaning
action of Hostapur SAS, this is also
achieved according to the EC recom-
mendation at anionic surfactant concen-
trations between 5 and 15 % in the
finished product.
The chemical stability of Hostapur
SAS also enables it to be used in toilet
cleaners with a very low pH value.
In cosmetic preparations Hostapur SAS
has proved successful particularly as a
co-surfactant on account of its
product-specific properties. This applies
especially to the combination with
alkyl ether sulphates in the manufacture
of hair and body care products. 29
Compared to alkyl ether sulphates,
Hostapur SAS has a stronger cleaning
and degreasing action. The viscosity-
depressing property of the secondary
alkane sulphonate also limits the concen-
tration used in the fairly high-viscosity
cosmetic hair and body care products.
Apart from exceptions, mixtures with
a higher content of alkyl ether sulphate
are therefore used. Guide values for the
mixing ratios are as follows:
• For finished products with a content
over 12 % active detergent: 70 parts
ether sulphate to 30 parts
Hostapur SAS.
• For finished products with less than
12 % active detergent the mixing ratio
should be: 80 parts ether sulphate to
20 parts Hostapur SAS.
The mixing ratios are calculated on
100 % active substance.
The viscosity can be adjusted with
sodium chloride and/or ammonium
chloride and/or magnesium chloride very
economically. Similarly, fatty acid alkano-
lamides and fatty alcohol polyglycol
ethers with a low degree of ethoxylation
such as Genapol L-3 in combination
with the above-mentioned electrolytes
can be used. Fatty acid polyglycol esters
Advantages of Hostapur
SAS in sanitary cleaners
Chemical stability to
oxidizing agents
Stability in the acid and
alkaline pH ranges
Good wetting power and
thus increase in effec-
tiveness
Better chlorine stability
than LAS.
Sanitary cleaners
Sanitary cleaners are used chiefly
for the easy and economical cleaning
of bathrooms and toilets. They are
intended to remove all traces of lime,
dirt and soap rapidly. Furthermore,
it is often desired to remove dark mould
patches on joints, tiles and shower
curtains. The current sanitary cleaners
are adjusted either to an acid or an
alkaline pH. In general these products
are expected to have an antimicrobial
or disinfectant action as well, which
can be achieved by special additives
such as active chlorine (hypochlorite)
hydrogen peroxide or by acids.
Surfactants with good wetting action
provide the cleaning action. Owing to
its chemical structure (C-S bond to the
sulphonate group), Hostapur SAS has
good stability to oxidizing agents and
is stable in both the acid and the alkaline
pH ranges. This stability to reducing
and oxidizing agents makes Hostapur
SAS a preferred surfactant for sanitary
cleaners.
Of special importance is the stability
of the oxidizing agents used in the indi-
vidual surfactant systems.
17
or special cellulose ethers can also
be used to increase viscosity. Fig. 5
shows the viscosity curves of Hostapur
SAS (SAS): alkyl ether sulphate (AES)
mixtures with the addition of different
electrolytes; magnesium chloride per-
forms particularly well. The viscosity
rises parallel to an increasing amount of
alkyl ether sulphate.
A combination of alkyl ether sulphate,
alkyl amidobetaine and Hostapur SAS,
for example, in the mixing ratio 6:2:2,
can bring advantages in respect of rheol-
ogy, foaming properties and dermatolog-
ical properties.
By adding Hostapur SAS to liquid
hair and body care products the low-
temperature cloud point as a function of
the active detergent content and the
mixing ratio can be lowered by about
4 to 7°C. This is a particular advantage
also for preparations containing pearl-
izing agents. Fig. 6 illustrates the good
influence of Hostapur SAS on the
low-temperature properties of the sur-
factant mixtures.
Special emulsifiers or solubilizers
are needed to solubilize slightly soluble
perfume oils. Owing to the pronounced
solubilizing action of Hostapur SAS,
the use of these auxiliaries is often
unnecessary.
The flash foam required for use,
especially in the presence of dirt and
grease, can also be increased by the
Hostapur SAS content in the formu-
lations.
The numerous uses of Hostapur SAS
in cosmetic preparations are described
briefly as follows:
+15
+10
+5
±0
– 5
– 10
tem
pera
ture
[°C]
0:10 2:8 4:6 6:4 8:2 10:0SAS : AES mixture
cloud pointclear point
Fig. 6: Low temperature cloud and clear points
as a function of the mixing ratio
7000
6000
5000
4000
3000
2000
1000
0
visc
osity
η [m
Pas]
7:3 6:4 5:5 4:6 3:7SAS : AES mixture
NaCl 10% a.s.NaCl 15% a.s.NH4OH 15% a.s.KCl 15% a.s.MgCl2 10% a.s.MgCl2 15% a.s.
Fig. 5: Viscosity increase of alkyl ether sulphate/Hostapur SAS
mixtures as a result of additions of electrolytes (5 %)
18
Hair shampoos
The addition of Hostapur SAS enables
hair shampoos with special effects to
be developed. The stronger degreasing
action of Hostapur SAS makes it pos-
sible to increase the cleaning action, for
example, in mixtures with alkyl ether
sulphates. This is an advantage in formu-
lating low-cost effective shampoos
for greasy hair.
The possibility is also afforded of
manufacturing single-application
shampoos, which can obviate the need
for washing a second time.
Shampoo concentrates with a high
active detergent content can also
be formulated with Hostapur SAS in
combination with other surfactants.
Here, the viscosity-depressing property
of Hostapur SAS is an advantage in
formulation; in other words, viscosity-
depressing additives such as ethanol
and glycols can largely be omitted.
Last but not least, Hostapur is
suitable for the manufacture of special
“clean shampoos”, which enable hair
setting products or highly substantive
cationic polymers to be washed
out of hair. Guide Formulations are
available.
Shower gels
The universally usable shower gels are
generally used for cleaning the skin
Applicationsand hair at the same time. Flash foam
formation is particularly important in
this application. With the partly use of
Hostapur SAS a fine-bubble foam and
rapid spread of the shower gel over the
skin and hair can be achieved.
Foam baths
Foam baths are used in extremely diluted
concentrations in the bath water; the
active detergent content in the bath
water is 0.002 %. The finished products
are therefore often adjusted to an active
detergent content of, for example, 50 %.
When the usual surfactants such as
alkyl ether sulphates and alkyl amidobe-
taines are used, a gel that is slightly
soluble in the bath water is usually pro-
duced in this concentration range.
By adding Hostapur SAS, the solubility
in water is improved dramatically. At
the same time beneficial rheological
properties such as flowability at room
temperature are achieved. Moreover,
it is not necessary to add the commonly
used solubilizers.
Liquid soaps
Liquid soaps have become established
as an alternative to conventional
bar soaps in the body care product
sector, above all because of their
ease of use. Since the hands are,
generally speaking, fairly dirty, a strong
cleaning action is required. By using
Hostapur SAS, this effect can be
achieved easily. Guide Formulations
are available.
Soaps
By adding, for example, 1 to 3 %
Hostapur SAS to the soap formulation,
processing can be facilitated and
dispersion of the dyes used can be im-
proved. To a certain extent the amount
of the expensive C12 fatty acid can
be reduced.
Emulsions
By adding small amounts of Hostapur
SAS to emulsions, especially oil-
in-water emulsions, the spontaneity of
emulsion formation can be improved
during manufacture. Moreover, finer
distribution of the emulsified droplets is
achieved.
Toothpastes
Hostapur SAS can also be used
in toothpastes as an alternative to the
lauryl sulphate sodium salt often
employed as a foamer in dental care
products. Advantages are the good
cleaning action as well as the good
electrolyte compatibility and dispersing
action.
19
Industrial cleanersAdvantages of Hostapur
SAS in cosmetic prep-
arations
Lowering of the raw
material costs by partial
replacement of other
principal surfactants
Improvement in low-
temperature stability
Manufacture of highly
concentrated formu-
lations
Improvement in
spontaneous solubility
in water
Reduction in solubilizers,
especially
with concentrates
Foam stabilization
By varying the
Hostapur SAS: alkyl
ether sulphate mixing
ratio the cleaning
action can be increased
High-pressure cleaners
These cleaners are in many cases
adjusted to an alkaline pH with sodium
hydroxide and sodium metasilicate.
Hostapur SAS has optimum foaming
and cleaning action in this pH range
as well.
Automotive cleaners
Hostapur SAS is used as a principal
surfactant in car shampoos for private
use and for commercial car washes.
Equally, acid, alkaline or neutral clean-
ers can be formulated with Hostapur
SAS for buses, railway trucks and lorries.
The high cleaning action of the second-
ary alkane sulphonate in particular is of
great importance here. Furthermore, the
foaming properties and the associated
soil-and oil-suspending power play a
major role in effective use. The concen-
tration of Hostapur SAS used, calculated
on 100 %, is generally between 2 and 5 %.
Hostapur SAS can however also be used
with fatty alcohol polyglycol ethers in an
approximate mixing ratio of 3:1.
Alkaline rust removers
The pH stability in the presence of
potassium hydroxide solution makes
Hostapur SAS in amounts of 1 to 2 %
ideal for use in these products.
Hand cleaners
Hand cleaners are used in industrial
plants and workshops for cleaning very
dirty hands. To increase the cleaning
action, mechanically effective sub-
20
stances such as wood flour, soda, sodium
sulphate or polymer powder are used.
Hostapur SAS in amounts of 10 to
50 % can be used as the active deter-
gent. The dispersion action and de-
greasing power of this surfactant is an
advantage for this application. Guide
Formulations are available.
Cleaners for dairies and
butchers’ shops
Hostapur SAS can be used for manufac-
ture of cleaners for butchers’ shops and
milking machines because of its excel-
lent cleaning and degreasing power.
ApplicationsSpecial technical sectors
Fire extinguishing foams
The pronounced flash foaming power
of Hostapur SAS can be used in com-
bination with other surfactants very
effectively to formulate fire extinguish-
ing agents.
Emulsion polymerization
Secondary alkane sulphonates have
been used successfully for decades in
the emulsion polymerization of vinyl
chloride. Hostapur SAS has proved
successful both as an emulsifier in con-
tinuous and discontinuous processes
and for the stabilization of the latex
following polymerization by the nucle-
ation process; in the latter process
polymerization is carried out with only
a low emulsifier concentration and
the dispersion is stabilized subsequently
by adding suitable emulsifiers. Hostapur
SAS is noted for its good dispersibility,
which is evidenced by good stability
of the latex to mechanical stress and
good process control (little tendency for
deposits to form in the reaction vessel).
Owing to the absence of double bonds,
the emulsifier does not act as a radical
interceptor. This ensures a readily re-
producible reaction course and results
Advantages of
Hostapur SAS in
Industrial cleaners
High stability in a broad
pH range (acid and
alcaline) and oxidation
agents
Good compatibility with
all types of electrolytes
Excellent wetting power
Strong degreasing and
cleaning effects
Good dispersion and
solubilization of fat, soil,
and pigments
High solubility and a
good cold stability
21
in end products with good heat stability
because of the lower demand for per-
sulphate (radical forming agent) and the
lower tendency to block polymerization
(no reaction between the emulsifier
and the reaction partners). The low salt
content of Hostapur SAS also has a
positive influence on the heat stability
of the end product.
In the manufacture of butadiene
copolymers, butadiene-styrene and
butadiene-acrylonitrile latices, soaps
(fatty soaps, resin soaps) are generally
used. The soaps have the advantage
over the synthetic anionic emulsifiers
that the polymer can be precipitated
by acidification or addition of salt and
the fatty or resin acid remaining in the
product serves as a plasticizer at the
same time. One evident disadvantage of
the soaps is the instability of the latex
(coagulation on slight change in pH and
contamination, low resistance to fillers)
and poorer chemical and heat stability.
For these reasons the synthetic emul-
sifiers are increasingly gaining ground,
particularly for special products, for
example, the carboxylated butadiene
copolymers (for carpet backcoating, for
papermaking, adhesives etc). Because
of its constant quality and low salt con-
tent, Hostapur SAS is highly suitable for
this application.
Textile and leather auxiliaries
Owing to its chemical stability and
very good wetting action, Hostapur SAS
can be used in the manufacture of
synthetic fibres and in the finishing of
textile fibres, for example, as an antistatic
agent. 30 Other uses for the secondary
alkane sulphonate are cotton scouring,
mercerizing and carbonization and the
preparation of leather fatliquors.
Oilfield chemicals
Hostapur SAS is also used successfully
in the tertiary recovery of oil.
Advantages
of Hostapur SAS
for special
technical sectors
In combination with
co-surfactants in-
creasing of the foam
stability and flash
foaming power
Good emulsifier for
the emulsion polymeri-
zation in continuous and
discontinuous processes
High wetting action in
textile and leather
auxiliaries for manu-
facture and finishing
of textile fibres
Special additive with
high heat and electrolyte
stability for the tertiary
recovery of oil
22
Physical and chemical propertiesThe secondary alkane sulphonates have a number of specific physical and chemical properties because of their structure.31 – 51 These properties are depend-ent on the chain length of the paraffin used. HostapurSAS with paraffin radicals between 14 and 17 carbonatoms has optimum surface-active and chemical properties, which are described below.
Surface activity
Micelle formation
There are extensive studies of the
surface-active properties of secondary
alkane sulphonates. 52, 53 It is interesting
to note that surfactants with a central
functional group form micelles from com-
paratively few surfactant molecules.54
For Hostapur SAS the critical micelle
concentration CM is about 2x10-3 mol ·L-1
or 0.6 g ·L-1 at 20°C. The structure of the
micelles is spherical.
Interfacial tension
The interfacial tension with decane as
the other phase is about 4.6 mN·m-1,
measured on a 1% aqueous Hostapur
SAS solution.
Surface tension
The surface tension of Hostapur SAS
(100% active substance), measured
by the “du Noüy method” at 25°C, as a
function of the concentration, is shown
in fig. 7.
70
60
50
40
30
surfa
ce te
nsio
n σ
[mN
/m]
0.001 0.01 0.1 1 10concentration [g/L]
Fig. 7: Surface tension of Hostapur SAS (25ºC)
23
Wetting action
Hostapur SAS is a rapidly wetting sur-
factant. This gives rise to advantages in
practical use in all cleaners. This applies
particularly to use in dishwashing liquids
and all-purpose cleaners. The excellent
wetting action extends over a wide tem-
perature range, not only in a neutral me-
dium but also in the alkaline and acid pH
ranges. The excellent wetting power in
low concentrations at low temperatures
is a noteworthy feature.
Fig. 8 shows the wetting action of
Hostapur SAS as a function of the con-
centration and temperature.
The superior wetting power of
Hostapur SAS compared with linear
alkyl benzene sulphonate (LAS), lauryl
ether sulphate (LES) and lauryl sulphate
(LS) is shown in fig. 9.
100
80
60
40
20
0
wet
ting
time
[s]
0.25 0.50 0.75 1.0concentration c [g/L]
20°C50°C70°C
Fig. 8: Wetting power of Hostapur SAS in accordance
with DIN 53901
90
80
70
60
50
40
30
20
10
0
wet
ting
time
[s]
SAS LAS AES LS
csurfactant 0.1 % a.s.water hardness 268 ppm CaCO3 (15°d)temperature 37°CpH 7
Fig. 9: Wetting power of various surfactants in accordance
with DIN 53901
24
Physical and chemical propertiesFoaming power
Hostapur SAS has good foaming power,
which is very pronounced, especially in
soft water. Flash foam is a characteristic
property of the secondary alkane sul-
phonates. An increase in foaming prop-
erties, especially in hard water, can be
achieved, for example, by a combination
of Hostapur SAS with an alkyl ether
sulphate in the ratio 4:1. Figs. 10 and 11
below demonstrate the foaming power
of Hostapur SAS in soft and hard water.
The good foaming properties of
the Hostapur SAS/alkyl ether sulphate
mixtures are clearly discernible.
Rheological properties
The viscosity of the aqueous Hostapur
SAS solutions rises only slightly up
to about 30 % active detergent. Above
30 %, however, a rapid rise in the
inhomogeneous paste region can be
observed. The low-concentration
aqueous Hostapur SAS solutions exhibit
Newtonian flow.
The flow properties of Hostapur
SAS 30 and paste-grade Hostapur
SAS 60 are of importance particularly
for transport and conveying. The
flow diagrams are given in section
Conveying/mixing.
300
250
200
150
100
50
0
foam
hei
ght [
mm
]
0.002 0.006 0.03 0.1 0.3 1.0concentration c [%]
AESSASAES : SAS =̂ 7:3SAS : AES =̂ 4:1
water hardness 0 ppmCaCO3 (0°d)temperature 37°C
Fig. 10: Foaming power of Hostapur SAS in distilled water
by the ROSS-MILES method
300
250
200
150
100
50
0
foam
hei
ght [
mm
]
0.002 0.006 0.03 0.1 0.3 1.0concentration c [%]
AESSASAES : SAS =̂ 7:3SAS : AES =̂ 4:1
water hardness 357 ppm CaCO3 (20°d)temperature 37°C
Fig. 11: Foaming properties of Hostapur SAS in hard water by
the ROSS-MILES method
25
pH stability
The Hostapur SAS grades are stable in
the acid and in the alkaline pH range.
Heat stability
Aqueous solutions of Hostapur SAS
are stable up to temperatures of
about 100°C.
Detergent action
The good soil removal power of
Hostapur SAS is not appreciably re-
duced by water hardness salts. The
builders used in practice increase
the cleaning effect.
Solubilization
The good solubilizing power of Hostapur
SAS towards hydrophobic oils and fats
is characteristic of this type of surfactant.
In practical use in cleaners, this means
increased degreasing and often a saving
of solubilizers, for example, for perfumes.
The solubilizing effect rises with the
surfactant concentration, the temperature
and often also with the electrolyte con-
tent of the solution. Solubilization in the
Hostapur SAS solution can also be in-
creased and speeded up by mechanical
means and lengthy stirring.
Using the solubilization of isopropyl
myristate as an example, fig. 12 illus-
trates that Hostapur SAS has greater
solubilizing power than alkyl ether
sulphate.
Emulsifying action
Secondary alkane sulphonates also
display good emulsifying action.
As co-emulsifiers, they are suitable for
the manufacture of liquid and cream
oil-in-water emulsions. Concentrations
as low as under 1% bring spontaneous
emulsion formation in manufacture
and an improvement in emulsion stability.
Moreover, finer distribution of the
emulsified droplets is possible. The
emulsifying action as a dishwashing liquid
test is described by D. MILLER. 55
5
4
3
2
1
0 0:10 2:8 4:6 6:4 8:2 10:0
SAS : LES mixture
15% a.s.10% a.s.15% a.s.
solu
bilit
y [g
IPM
/ 10
0g]
Fig. 12: Solubilization of isopropyl myristate by Hostapur SAS:
alkyl ether sulphate (LES) as a function of the mixing ratio
26
Physical and chemical propertiesStability to hard water
Hostapur SAS has a stability number
of 3 in accordance with the DIN 53905
test. Accordingly, Hostapur SAS is a
surfactant with moderate stability to hard
water.
The stability to hard water of
Hostapur SAS can be improved markedly
by combining it with alkyl ether
sulphates. As fig. 13 shows, a mixture of
4 parts Hostapur SAS (SAS) and 1 part
lauryl ether sulphate (LES) reaches
an optimum value of 75.
Electrolyte stability
Hostapur SAS has only slight sensitivity
to electrolytes. The viscosity of the
aqueous solutions is increased only
slightly by additions of electrolyte such
as sodium chloride or sodium sulphate.
Chlorine-/oxidation stability
Hostapur SAS has excellent chlorine
stability compared with many other
surfactants. In combination with amine
oxides, a synergistic effect is observed;
in other words, the mixture has a higher
stability than the individual surfactants
alone. Hostapur SAS is therefore the
ideal surfactant for formulating hypo-
chlorite-containing cleaners, whether
used alone or in combination with amine
oxides.
As illustrated in fig. 14, the chlorine
content falls fairly little in the presence
of Hostapur SAS as a function of the
storage time. The stability was deter-
mined on a solution with 2.5 % active
detergent in each case.
80
60
40
20
0
hard
wat
er s
tabi
lity
SAS LES SAS : LES =̂ 4 : 1
Fig. 13: Stability to hard water of Hostapur SAS and of mixtures
with lauryl ether sulphate determined in accordance with DIN 53905
after 6 weeks, after 12 weeks, after 20 weeksstarting value: 6.5% active chlorine
100
80
60
40
20
0
resi
dual
act
ivity
[%]
2.5% SAS 2.5% amine oxide 1.5% SAS+ 1.0% amine oxide
Fig. 14: Chlorine stability in the presence of Hostapur SAS, amine
oxide and a mixture of Hostapur SAS/amine oxide
100
80
60
40
20
0
resi
dual
act
ivity
[%]
0 1 2 3 4 5 6 7time [days]
SAS 30SAS 60
csavinase 0.3%csurfactant 3.0 g/Lwater hardness 179 ppm CaCO3 (10°d)temperature 25°C
Fig. 15: Compatibility of Hostapur SAS with protease
100
80
60
40
20
0
resi
dual
act
ivity
afte
r 7 d
ays
[%]
SAS LAS
csurfactant 3.0 g/Lwater hardness 179 ppm CaCO3 (10°d)temperature 25°C
®Savinase 16L, c = 0.3%®Lipolase 100L, c = 1.0%
Fig. 16: Compatibility of Hostapur SAS with protease and lipase
27
Enzyme stability
The stability of enzymes such as
protease (e.g. ®Savinase, manufactured
by Novo Norsk) in the presence of
Hostapur SAS is shown in fig. 15 as a
function of the storage time. It is
clearly evident that after 7 days only a
slight fall in enzyme activity (80%) can
be observed in the case of Hostapur
SAS. Hostapur SAS is a more enzyme
compatible anionic surfactant than
most anionic surfactants commonly
used in liquid laundry detergent appli-
cations (e.g. linear alkyl benzene
sulphonate, sodium alkyl sulphate).
The residual activities after 7 days’
storage at 25°C are shown in fig. 16.
Here too the good effect of Hostapur SAS
on the stability of the enzymes is con-
firmed both in the case of proteases and
of lipases.
28
Physical and chemical propertiesSynergistic interactionwith soil release polymers
In modern detergent formulations the
use of soil release polymers (SRP)
is gaining increasing importance. Soil
release polymers improve the detach-
ment of oily and fatty soil from fabrics
containing synthetic fibres, especially
polyester and polyester blended fabrics.
They are now included in the top brands
of most detergent manufacturers.
However, it is known that the effec-
tiveness of these polymers is dependent
substantially on the type of surfactants
in the detergent.
The literature describes, how the soil
release effect is generally reduced in
combination with anionic surfactants. 56
However, these studies are restricted to
the major anionic surfactants in deter-
gents, e.g. linear alkyl benzene sulpho-
nate.
The soil release effect of a commer-
cial soil release polymer in combination
with Hostapur SAS was therefore inves-
tigated in comparison with combinations
with linear alkyl benzene sulphonate
(LAS) or alkyl sulphate (AS) in the well-
known dirty motor oil test.
Fig. 17 shows that in combination
with Hostapur SAS, unlike combinations
with linear alkyl benzene sulphonate or
alkyl sulphate, a significant improvement
in the soil release effect is achieved.
As is evident from fig. 18, the builder
system as well as the surfactant influen-
ces the performance of soil release
polymers.
35
30
25
20
15
10
5
0
rem
issi
on R
[%]
LAS LAS SAS SAS+ 2.0 g NTPP + 1.5 g zeolite + 2.0 g NTPP + 1.5 g zeolite
+ 0.7 g soda + 0.7 g soda
0.05 g/L surfactant + builder without SRP1.0 g/L surfactant + builder + 0.06 g/L SRP
40
30
20
10
0
rem
issi
on R
[%]
SRP LAS AS SAS
0.06 g/L SRP1.0 g/L surfactant without SRP1.0 g/L surfactant + 0.06 g/L SRP
Fig. 18: Influence of the builder system on the performance of
soil release polymers
Fig. 17: Improvement in the soil release effect by Hostapur SAS
The soil release polymer reaches its
greatest effectiveness with the combin-
ation of Hostapur SAS plus the zeolite/
soda system.
The combination of the polymer with
Hostapur SAS plus sodium tripolyphos-
phate (STPP) is more effective than the
combination with linear alkyl benzene
sulphonate plus STPP.
Solubility in water
The very good solubility of the Hostapur
SAS grades in water is illustrated in
fig. 19. As expected, the dissolving rate
increases sharply as the temperature
of the water rises.
Hostapur SAS shows less tendency
than other surfactants to form liquid
crystalline phases or gels. Hostapur SAS
is therefore very suitable for concentra-
tes and liquid formulations.
Low-temperature properties
Hostapur SAS has good low-tempera-
ture properties, especially in high appli-
cation concentrations. This applies par-
ticularly in comparison with linear alkyl
benzene sulphonate. Fig. 20 shows in
graph form the low-temperature clear
and cloud points of the individual
Hostapur SAS (SAS)/alkyl ether sulphate
(LES) mixtures.
The low-temperature cloud points of
Hostapur SAS as a function of the con-
centration are shown in fig. 21.
80
70
60
50
40
30
20
10
0
conc
entra
tion
c [g
/100
g]
-10 0 10 20 30 40temperature [°C]
SAS 30SAS 60SAS 93
Fig. 19: Solubility of the Hostapur SAS grades in distilled water
29
35
30
25
20
15
10
5
±0
-5
-10
tem
pera
ture
[°C]
10 15 20 25 30concentration c [%]
SASLAS
Fig. 20: Low-temperature cloud and clear points of 30% Hostapur
SAS/alkyl ether sulphate mixtures
10
5
±0
-5
-10
tem
pera
ture
[°C]
10 15 20 25 30concentration c [%]
SAS : AES =̂ 4:1LAS : AES =̂ 4:1
Fig. 21: Low-temperature properties of Hostapur SAS as a
function of the concentration
30
Toxicological and environmental pA modern surfactant must not present any risk to humans, animals, plantsand the environment during manufacture, storage, transport, processing,use and in the waste water.
Skin and mucous membrane irritation
Animal studies conducted in accordance
with OECD guideline 405 lead to the
assumption that Hostapur SAS as well
as other basic surfactants, e.g. LAS,
irritates both the skin and the eyes.
Below a threshold concentration (of 15 %
active detergent), however, no signifi-
cant irritant effects are observed. Fur-
thermore, well-documented human stud-
ies showed no indications of skin
irritation caused by diluted Hostapur
SAS solutions.
Sensitization
Hostapur SAS (60 %) was tested in the
Magnusson and Kligman maximization
test and proved not to be skin-sensitizing.
Mutagenicity
Hostapur SAS was tested in the Ames
Test (± S9) with Salmonella typhimurium
and for chromosome mutations in
the micronucleus test in vivo. In both
test systems Hostapur SAS was not
mutagenic.
As the following data show, Hostapur
SAS is an environmentally friendly sur-
factant with very good biodegradability,
good ecotoxicological values and good
dermatological and toxicological com-
patibility that has been successful for
decades. It is safe to use and poses no
risk to the environment.
Detailed reports on the toxicology
and environmental properties of second-
ary alkane sulphonate are available
in the literature. 57 – 74
Toxicological profile
To confirm the safety of Hostapur SAS,
extensive toxicological and dermato-
logical investigations were carried out
over many years. The most important
test results are given below:
Acute oral toxicity
LD50 (rat) = appr. 5000 mg/kg (60 %)
LD50 (mouse) = appr. 2900 mg/kg (60 %)
31
propertiesReproduction toxicity
Hostapur SAS (60 %) was tested in a two-
generation trial for possible reproduction
toxicity properties. Up to a dose of
10,000 ppm in the feed, no maternotoxic,
embryotoxic and/or teratogenic effects
of any kind were observed.
Chronic toxicity
Hostapur SAS (60 %) was tested for
chronic toxicity and/or carcinogenicity
in two long-term studies on rats and
mice. No toxicologically significant ef-
fects were observed after oral adminis-
tration to rats of up to 2% in the feed
over a period of two years. In addition,
no signs of toxicity, either macroscopic
or microscopic, were observed after
dermal application (three times per
week for 80 weeks) to mice.
Toxicokinetics
The toxicokinetic properties of radio-
actively labelled Hostapur SAS were
investigated on rats. After oral adminis-
tration, a dose-independent two-phase
elimination with half-lives of 11 and 65
hours was observed. Over 90 % of the
dose administered was excreted within
24 hours.
Comparable toxicokinetic properties
were also observed after dermal appli-
cation to rats.
Conclusion:
Hostapur SAS
• is not sensitizing to
skin.
• is not mutagenic and/
orgenotoxic.
• presents no risk in
respect of reproduc-
tion toxicity.
• exhibited no systemic
toxicity in two long-
term studies and was
not carcinogenic.
• shows no signs of bio-
accumulative potential
and is eliminated very
rapidly.
In accordance with
the CESIO classification
Hostapur SAS with an
active detergent content
of over 15 % must be
labelled as irritant (Xi)
whereas up to an active
detergent content of
15 %, Hostapur SAS does
not require a hazard
warning label.
For detailed information
see Safety data sheet.
Hostapur SAS does not
present a health risk
under conditions of use.
32
Toxicological and environmental pEcology
Biodegradability
Secondary alkane sulphonates are
readily and rapidly biodegradable. The
primary degradability is considerably in
excess of 90 %. In the OECD Confirmatory
Test (sewage sludge simulation test)
the rate of degradation is 99 % (decrease
in MBAS). In the modified OECD Screen-
ing Test (OECD 301 E), a test for total
degradability, SAS has a DOC removal
of 95%. The “Ten-days-window” criterion
is thus met, i.e. SAS is “readily biode-
gradable”.
Compared with linear alkyl benzene
sulphonates (LAS), secondary alkane
sulphonates (SAS) are more rapidly bio-
degradable. This applies especially
at low temperatures. The degradation
properties of secondary alkane sulphon-
ates are shown on page 40.
In the Coupled Units Test (OECD 303 A,
sewage treatment plant simulation
test), the biodegradation/elimination is
96 % +/-3 %.
In a modified Coupled Units Test, in
which the sewage treatment plant simu-
lation was better matched to the cond-
itions in a modern municipal sewage
treatment plant, 99 % +/- 1 % secondary
alkane sulphonates were degraded/
eliminated (DOC decrease).
Aquatic toxicity
Current data on the acute and chronic
ecotoxicity and water biocenosis
toxicity are given in tabular form in
Technical data:
Possible toxic effects of surfactant as
well as decomposition and cleavage
products of the secondary alkane sul-
phonate were investigated in five pilot
plants, in which the route taken by the
anionic surfactant from the consumer
via the sewage treatment plant to the
surface water is simulated. Flora and
fauna of the β-mesosaprobic zone were
used as indicators of the effect on living
organisms. In addition, the embryolarval
test was used to determine the toxic
substances in the water.
The results can be summarized as
follows: High COD, BOD and MBAS de-
gradation rates of 90 % were measured.
A slightly toxic effect (“toxic” is
defined as an adverse effect on health,
growth and reproduction) on the green
algae species Spirogyra as a typical
representative of the β-mesosaprobic
zone was observed at 40 ppm secondary
alkane sulphonate in the water.
Conclusion
The surfactant has no significant effect
on golden orfes and zebra fish. Surfac-
tant residues and cleavage products
have no significant toxic effect on the
development of Cichlasome nigrofascia-
tum larvae into the fully grown organism.
Secondary alkane sulphonate has
no significant toxic effect on Planorbis
corneus.
Secondary alkane sulphonate has no
significant toxic effect on Daphnia
magna.
On the basis of the EU labelling crite-
ria in accordance with the 12th harmon-
ization of Directive 91/325/EEC no
environmental labelling is required for
alkane sulphonates.
Simplified “risk assessment”
A simplified qualitative risk assessment
for Hostapur SAS shows that there
is a sufficiently large safety margin be-
tween exposure concentration and
effect concentration, the PEC/PNEC-
ratio is far below 1.
The data used for the qualitative
risk assessment are given in the table in
Technical data.
Conclusion:
Based on data risk
assessment Hostapur
SAS presents no risk
to the environment.
Similarly, the only slight
anaerobic degradability
of secondary alkane
sulphonates, like sur-
factants with a C-S bond,
has no adverse effect
on the enviromental
properties on the basis
of the available data.
33
propertiesraw material sources, which range
from petrochemical and oleochemical/
agricultural raw materials to minerals.
The raw material consumption and
the emissions into the environment in
the manufacture of secondary alkane
sulphonate (SAS) by sulphoxidation of
n-paraffin can be summarized as follows:
734 kg oil, 105 kg sulphur (for SO2)
138 kg salt (for NaOH), 36 kg oxygen (for
sulphoxidation) are required for the pro-
duction of 1000 kg SAS.
The total raw material consumption
including the required energy is
797 kg oil, 154 kg natural gas, 180 kg coal
Of the total energy consumption of
51.9 GJ, process energy acocunts for
36 %; of the process energy 48 % is ap-
portioned to the SAS stage. 68% of
the total energy requirement is covered
by oil. The production of 1,000 kg SAS
gives rise to 64.2 kg solid waste, of
which 84 % comes from the oil; the emis-
sions into the environment amount to
38 kg. They stem mainly from the
production and incineration of the oil.
Life cycle assessment
A balance sheet on the production of
the most important surfactants at
present used in detergents in Europe
was drawn up by the European “LCI-
Surfactant Study Group (CEFIC/ECOSOL)”
and Franklin Associates Ltd. (Tenside
Surfactants Detergents 32 (1995) 2, 84 ff.).
In particular the surfactants linear
alkyl benzene sulphonate (LAS), alkyl
sulphate (AS), alkyl ether sulphate (AES),
soap, secondary alkane sulphonate
(SAS), fatty alcohol ethoxylate (AE) and
alkyl polyglucoside (APG) were studied.
These are obtained from petrochemical
and oleochemical intermediates. The ba-
lance sheet is extremely comprehensive
and includes the energy and material
requirements as well as the emissions
into the environment and the production
of waste, which are associated with all
stages of surfactant manufacture. In
accordance with the principles recom-
mended by the SETAC, a “Peer Review
Panel” has assessed the study.
The study shows that each system
has effects on the environment through
the consumption of many different raw
material sources such as oil, natural
gas, oleochemical/agricultural products
and of minerals as starting materials
as well as through energy production and
transport. On the basis of the results,
there is no clear scientific justification
for singling out one of the systems as
having a fundamental environmental
advantage, either for the production of
individual surfactants or for the various
Conclusion:
Hostapur SAS has a fa-
vourable energy balance
sheet, especially when
compared with alkyl
ether sulphates based
on natural products.
Furthermore it has good
values in respect of the
solid waste occurring
in production.
34
ProcessingHostapur SAS can be supplied in the following forms
liquid = Hostapur SAS 30
paste = Hostapur SAS 60
The homogenous Hostapur SAS 30, which is a clear liquid at
room temperature, is easy to transport, convey and store.
Hostapur SAS 60, by contrast, is a paste that flows at +20°C
but that separates out into two phases of different composition
if left to stand for a lengthy period of time. For this reason
Hostapur SAS 60 must be homogenized before use by stirring
and, if necessary, by heating. This measure is not necessary
if full drums are completely processed.
Transport
The loading temperature ex works for
delivery by road tanker is for
Hostapur SAS 30 → 50–60°C and for
Hostapur SAS 60 → 70–90°C.
Although Hostapur SAS 60 is still
pumpable at room temperature with the
pumps mentioned in section Convey-
ing/mixing, the temperature during
transport should not fall below 65°C so
as to facilitate handling and conveying.
The road tankers intended for transport-
ing Hostapur SAS 60 have standard
R 3” connections or conventional hose
couplings.
35
Storage
Containers made from the following
materials have proved successful
for storing the Hostapur SAS grades:
• fibre-glass-reinforced polyester
resin, especially for storage tanks
with a capacity of 30–70 m3,
• steel containers with suitable hard
rubber lining or with tried and
tested internal coatings, for example,
epoxy resin or phenol-formaldehyde
resin,
• stainless steel, for example, material
no. 1.4541 (V2A) or 1.4571 (V4A).
The last-mentioned materials are also
recommended for pipelines.
An example of the installation of a
storage tank is shown diagrammatically
in fig. 22.
Before storage tanks are installed,
a guarantee of compatibility with
Hostapur SAS at the intended storage
temperatures should be obtained from
the manufacturer in question.
Hostapur SAS 30 should be stored
at temperatures above 20°C, because
cloudiness may occur at lower tem-
peratures. This cloudiness has no effect
on the quality of the product. Before
use, however, the product must be
homogenized.
Fig. 22: 60-t storage tank for Hostapur SAS 60
As already mentioned, Hostapur SAS 60
separates out in storage into two phases,
one containing more surfactant than the
other. In addition, sodium sulphate
can separate out at fairly low tempera-
tures. It is therefore necessary to stir or
pump round the tank contents constantly
and at the same time to maintain a
storage temperature of 65–90°C. If a cir-
culating pump is used, entrainment of air
must be prevented by suitable design of
the return pipe. Our experts will gladly
provide technical advice on planning
and installing storage tanks for Hostapur
SAS grades.
– stainless steel
– carbon steel rubber lined
– fibre-glass reinforced polyester
36
Processing
Any stirred vessel made of suitable
material, see section Storage, with low-
speed stirrers can be used. The
soft and preserved water intended for
dilution (hot water accelerates the
dilution operation) is run into the vessel
and the Hostapur SAS 60 is added
Conveying/mixing
The rheological properties of Hostapur
SAS 30 and Hostapur SAS 60 that
are important for conveying are shown
in figs. 23–25 below.
Hostapur SAS 30 and 60 can be con-
veyed by displacement pumps such as
• gear pumps, supplied by e.g. Lederle,
79194 Gundelfingen, Germany
• Mohno pumps, supplied by e.g.
Netsch, 84478 Waldkraiburg,
Germany
• helical blade pumps or twin-screw
displacement pumps made of
stainless steel, supplied by e.g.
Bornemann, 31683 Obernkirchen,
Germany.
For homogenization, current models
of low-speed stirrers can be used. It
is important to eliminate eddying so as
to prevent entrainment of air = foam for-
mation. The stirrer blade should there-
fore rotate below the surface of the
liquid. Good results have been obtained
with low-speed interference-multistage-
impulse-counterflow stirrers (INTER-
MIG), supplied by Ekato, 79650 Schopf-
heim, Germany.
Dilution
Dilution of Hostapur SAS 60 to 30 %
or less than 30 % active detergent
The storage of Hostapur SAS 60
can be simplified by adjusting the
product on delivery to 30% or
less active detergent by diluting it
with water.
300
200
100
0
visc
osity
η [n
Pas]
20 30 40 50 60 70temperature [°C]
Fig. 23: Viscosity of Hostapur SAS 30 measured with a Brookfield
viscometer RVT, spindle 1, speed 20 min-1
10000
visc
osity
η [n
Pas]
5 10 15 20 25 30 35 40 45 50shear rate D [s-1]
5000
2000
1000
500
200
100
20°C50°C
Fig. 24: Viscosity of Hostapur SAS 60 as a function of the
shear rate, measured in a HAAKE-Rotovisco RV 20
37
and dissolved with slow stirring (eddying
should be avoided because of foam
development). The product can also be
homogenized by being pumped round.
Another possibility consists of run-
ning Hostapur SAS 60 into the storage
tank and at the same time slowly adding
hot water. The amount of water is govern-
ed by the efficiency of the pumps and
should be no more than one-fifth of the
amount pumped round per hour.
An example will illustrate this: Deliv-
ery of 20 t Hostapur SAS 60; tank size 50
m3; pumping rate 5 m3/h; water added 1/5
of 5 m3 = 1 m3/ h. In this case it takes ab-
out 20 hours to produce 40 t Hostapur
SAS 30 from 20 t Hostapur SAS 60.
Handling
Because of the strong wetting and de-
greasing action, appropriate protective
measures should be taken, particularly
where lengthy exposure is involved.
Therefore protective gloves and safety
goggles should be worn when handling
these raw materials.
8000
7000
6000
5000
4000
3000
2000
1000
visc
osity
η [n
Pas]
20 30 40 50 60 70temperature [°C]
Fig. 25: Viscosity of Hostapur SAS 60 as a function of the temperature at D=10 s-1,
measured in a HAAKE-Rotovisco RV 20
38
Technical dataC-chain distribution
Physical/chemical data
<C13 n-Paraffin max. 1 %
C13 - C15-n-Paraffin about 58 %
C16 -C17-n-Paraffin about 39 %
>C17-n-Paraffin max. 2 %
Monosulphonate* about 90 %
Disulphonate* about 10 %
* calculated on 100 % active detergent
Feature
Appearance at 20°C
Average molecular weight
Active detergent content
Sodium sulphate content
Paraffin content
pH 5 % as is in water
Hostapur SAS 30
clear faintly yellowish liquid
328 g·mol-1
approx. 30 %
max. 2.1 %
max. 0.4 %
7.0 – 8.5
Hostapur SAS 60
yellowish soft paste
328 g·mol-1
approx. 60 %
max. 4.2 %
max. 0.7 %
7.0 – 8.5
Guide product data
Temperature
20°C
30°C
40°C
50°C
60°C
70°C
80°C
Hostapur SAS 30
1.048
1.042
1.036
1.031
1.025
1.017
–
Hostapur SAS 60
1.087
1.081
1.075
1.068
1.062
1.055
1.049
Density (g·cm-3)
Specific heat
kJ·kg-1·K-1
(kcal ·kg-1· °C-1)
Thermal conductivity
W m-1·K-1
(kcal ·m-1·h-1· °C-1)
Hostapur SAS 30
3.56
(0.85)
0.47
(0.40)
Hostapur SAS 60
2.76
(0.66)
0.28
(0.25)
Calorific data
39
Registration status
• Chemical name in accordance with IUPAC
• INCI name: Sodium C14-17 sec-Alkyl Sulphonate
• Registered in Japan (MITI)
• Registered in Korea, USA, Canada, Switzerland, Australia
• Labelling in accordance with 12th harmonization directive 91/325/EWG:
no “environmental hazard labelling” required
40
Technical dataEcological data
Biodegradability
OECD Confirmatory Test
Mineralization (DOC)
SAS after 6 days (OECD Screening Test 301 E)
Radiolabelled experiments
SAS (U-14C) after 6 days
Laboratory tests at low temperatures in a trickling filter plant
SAS degradation at +1°C air temperature (+8°C in trickling filter)
Biodegradation in the OECD Coupled Units Test (OECD 303 A)
% biodegradation
99
87
45
85
> 90
Biodegradability
Acute toxicity
Fish toxicity (golden orfe, 48 h, OECD 203)
Fish toxicity
Guppy
Trout
Carp
Daphnia toxicity (Daphnia magna, 24 h, OECD 202)
Bacterial toxicity (sewage sludge)
Chronic toxicity
Chronic bacterial toxicity (Bringmann-Kühn)
Chronic algal toxicity (OECD 201)
Chronic Daphnia reproduction test (OECD 202)
Coupled Daphnia multigeneration test (toxicity of the discharge from the modified
OECD Confirmatory Test on three consecutive generations of Daphnia)
Water biocenosis toxicity
LC0
LC50
LC100
LC50
LC50
LC50
EC50
EC10
EC50
LOEC
NOEC
no toxic effect
LOEC
NOEC
7.1 mg·L-1
8.4 mg·L-1
9.9 mg·L-1
3.6 mg·L-1
2.8 mg·10L-1
2.8 mg·L-1
12.5 mg·L-1
> 1000 mg·L-1
58 mg·L-1
95.5 mg·L-1
3.0 mg·L-1
0.37 mg·L-1
3.5 (MBAS)
1.4 (MBAS)
Aquatic Toxicity
41
Summary of the propertiesof Hostapur SAS:
• good solubility
– the low viscosity of more highly
concentrated solutions thus
permits:
– easy manufacture of liquid
detergents and cleaners
– saving of packaging costs
– reduction in the use of hydrotropes
• excellent electrolyte compatibility
• chemical stability over the entire
pH range
• excellent stability in the presence of
oxidizing agents, for example,
hypochlorite
• saving of enzymes
• good cleaning and degreasing
properties
• good foaming power
• pale inherent colour
• good detergent action
• good skin compatibility
• rapid biodegradability
Analysis
For literature on the analysis of
secondary alkane sulphonates see
Literature. 75 – 92
Further information
• Safety Data Sheet
• Guide Formulations
• Detergent Raw Materials –
Product Range
1. Effects (NOEC)1)
Fish
Daphnia
Algae
2. Exposure (D,NL)
STP intake2)
STP discharge
STP removal
River water
3. Safety factors
Fish/river water
Daphnia/river water
Algae/river water
4. PEC /PNEC3)4)
1.2 mg·L-1
0.6 mg·L-1
6.1 mg·L-1
0.5 mg·L-1
2 µg·L-1
99.6 %
< 1 µg·L-1
> 1200
> 600
> 6100
0.03
Risk Assessment of Hostapur SAS
1) NOEC: no observed effect concentration 2) STP: sewage treatment plant
3) PEC: predicted environment concentration 4) PNEC: predicted no effect concentration
Sources: 1. BUA-Stoffbericht 206, S. Hirzel Verlag. 2. Internal SAS exposure data
42
Literature
Synthesis
1 Asinger, F. and Saus, A.: Beitrag zur Sulfoxidation
von Paraffinkohlenwasserstoffen in Gegenwart von
Gammastrahlen bzw. von ultraviolettem Licht,
Arbeit der TH Aachen (Techn. Chemie & Petro-
chemie), (1968)
2 Berthold, H. and Lipfert, G., in: Alkansulfonate
(H. G. Hauthal, ed.), VEB Deutscher Verlag für
Grundstoffindustrie, Leipzig, (1985), 13-50
3 Commichau, A.: Zur Kenntnis der Sulfoxidation von
Paraffinkohlenwasserstoffen und zur Sulfoxidation
bzw. Sulfochlorierung von Fettsäuren. Doktorarbeit
der Universität Aachen, (1965)
4 Beermann, C.: Über die Sulfoxidation von Paraffinen
und die verbesserte biologische Abbaubarkeit
der Alkansulfonate, Symposium über n-Paraffine in
Manchester, (1966)
5 Schneider, G.: Neue Waschrohstoffe auf petro-
chemischer Basis, SÖFW, 26 (1969)
6 Hoechst AG: Hostapur SAS: The raw material
with a sure future, (1987)
7 Platz, C. and Schimmelschmidt, K.: Pionierpatent:
DRP 735 096, (1940)
8 Ramloch, H. and Täuber, G.: Moderne Verfahren
der Großchemie: Die Sulfoxidation, Chemie in
unserer Zeit. 13, (1979), 157-162
9 Boy, A. et al.: Paraffin-sulfonates process boasts
new extraction step Chemical Engineering, 13,
Oct., (1975)
10 Graf, R.: Justus Liebigs Ann. Chem. 578, (1952), 50
11 Graf, R.: DR P J 74599, (1943)
12 Saus, A. et al.: Substitutionsverhältnisse bei der
Disulfoxidation von Paraffinkohlenwasserstoffen,
Tenside Detergents 10, 3, (1973), 113-119
13 Orthner, L.: Angewandte Chemie 62, (1950), 302
14 Hauthal, H. G.: Alkansulfonate VEB Deutscher
Verlag für Grundstoffindustrie, Leipzig, (1985)
Applications
15 Antwerpen, W. and Trautmann, M.: Formulierung
hochkonzentrierter flüssiger Wasch- und
Reinigungsmittel, SÖFW, (1984), 235-40
16 Siegel, D. and Quack, J. M.: Lessives Liquides A
Usage Menager, Vortrag Spanischer Detergentien-
kongress, Barcelona, (1978)
17 Müller, M., Quack, J. M. and Vitores, L.: Entfettung
und deren Bewertung, SÖFW, 18,19, 20, (1980)
18 Krings, Andree, H.: Anwendungstechnische
Eigenschaften der wichtigsten Tensidtypen,
“Waschmittelchemie” Hüthig Verlag, 55-73
19 Trautmann, M.: Tenside Detergents 18, (1981), 73-78
20 Hauthal, H.G., in: “Anionic Surfactants”, Marcell
Dekker, Inc. New York, Basel, Hong Kong, (1995), 143-220
21 Crass, G.: Tenside Surf. Det. 30, (1993), 408
22 Turowski, A., Antwerpen, W. and Jürges, P.: Vortrag
beim Sepawa-Kongress, Bad Dürkheim, (1994)
23 Tischer, H., Wedler, C., Knofe, E. and Haage, K.:
6. Internationale Tagung über grenzflächenaktive
Stoffe. Abh. Akad. Wiss. DDR, NI (D. Vollhardt, ed.),
Akademie-Verlag, Berlin, (1987), 583-587
24 Grey, S., in: “Proceedings of the 3rd World
Conference on Detergents: Global Perspectives”
(A. Cahn, ed.), AOCS Press, Champaign, IL, (1994),
82-87.
25 Hauthal, H. G., Seichter, E., Sowada, R. and
Trautmann, P., in: “Alkansulfonate” (H.G. Hauthal,
ed.), VEB Deutscher, Verlag für Grundstoffindustrie,
Leipzig, (1985), 143-178.
26 Hoffmann, H., Hohlfeld, G., Quack, J. M.: Unter-
suchungen über das Viskositätsverhalten von
Waschmittelslurries unter besonderer Berück-
sichtigung des Einflusses der Tenside, SÖFW 8,
(1978), 209-212
27 Trautmann, M. and Jürges, P.: Tenside Detergents
21, (1984), 57-61
28 Trautmann, M.: New test method for assessing the
cleaning action of all purpose cleaners, Vortrag
anlässlich des spanischen Detergentienkongresses
in Barcelona, (1985)
29 Quack, J. M. and Reng, A. K.: Sekundäres Alkan-
sulfonat: Eigenschaften und Einsatzmöglichkeiten
in kosmetischen Präparaten, Fette-Seifen-Anstrich-
mittel 78, (1976), 200-206
30 Kleber, R. M.: Tenside Surf. Det. 31, (1994), 358
Physical and chemical properties
31 Hauthal, H. G.: In Anionic Surfactants, Marcell
Dekker, Inc. New York, Basel, Hong Kong, (1995), 143-220
32 Hauthal, H. G. and Kretzschmar, G., in: “Alkansul-
fonate” (H.G. Hauthal, ed.), VEB Deutscher Verlag
für Grundstoffindustrie, Leipzig, (1985), 83-111.
33 Hauthal, H. G., Möhle, L., Pfestorf, R. and Quitzsch,
K.: Lecture to the 2nd World Surfactant Congress,
Sect. C2, Paris, (May 1988), 24-27
34 Hauthal, H.G., Möhle, L., Pfestorf, R. and Quitzsch,
K., in: 4. Internationale Tagung über grenzflächen-
aktive Stoffe, Abh. der Akad. der Wiss. DDR, NI (D.
VoIlhardt, ed.), Akademie-Verlag, Berlin, (1987), 63-71.
35 Möhle, L., Hauthal, H. G. and. Quitzsch, K.: Z.
Physik. Chem. 264, (1983), 281
36 Möhle, L., Opitz, S. and Ohlerich, U.: Tenside
Surf. Detergents. 30, (1993), 104-109
37 Ekwall, P. Mandell, L. and Fontell, K.: Mol. Cryst.
Liquid Cryst. 8, (1969), 157
38 Frumkin, A.: Z. Phys. Chem., Leipzig 116, (1925), 466
39 Kunieda, H. and Arai, T.: Bull. Chem. Soc. Jpn. 57,
(1984), 281
40 Lin, I. J. and Somasundaran, P. J.: Colloid Interf.
Sci. 37, (1971), 731
41 Lunkenheimer K. and Miller, R.: Tenside Det. 16,
(1979), 312
42 Lunkenheimer, K. and Kretzschmar, G.: Z. Physik.
Chem. 256, (1975), 593
43 Lunkenheimer, K., Miller, R. and Becht, J.: Colloid
Polymer Sci. 260, (1982), 1145
44 Rosen, M. J. and Murphy, D. S. J.: Colloid Interf.
Sci. 110, (1986), 224
45 Saito, M., Moroi, Y., and Matura, R. J.: Colloid
Interf. Sci. 88, (1982), 578
46 Sowada, R. J.: Prakt. Chem. 323, (1981), 93
47 Sowada, R. J.: Zur Berechnung des HLB-Wertes
isomerer und substituierter Alkansulfonate, Journal
f. prakt. Chemie, 322, (1980), 723-729
48 Sowada, R. J.: Prakt. Chem. 322, (1980), 590
49 Sowada, R. J.: Prakt. Chem. 322, (1980), 723
50 Sowada, R. J.: Prakt. Chem. 323, (1981), 951
51 Vold, M. J.: Colloid Interf. Sci. 90, (1982), 543-545
52 Asinger, F., Ebeneder, F. and Richter, G.: Über den
Einfluss von Disulfonaten auf die oberflächenakti-
ven und waschtechnischen Eigenschaften von
Monosulfonaten, Journal für prakt. Chemie,
4. Reihe, Band 2, (1955)
53 Asinger, F. and Freitag, G.: Über den Einfluss von
Tetradekandisulfonaten auf die oberflächenaktiven
und waschtechnischen Eigenschaften von Tetra-
dekanmono-Sulfonaten, Journal für prakt. Chemie,
4. Reihe, Band 7, (1959)
54 Sowada, R.: Zur Berechnung der mizellaren Aggre-
gationszahl homologer und isomerer Alkansulfonate,
Journal f. prakt. Chemie, Band 323, (1981), 951-956
55 Miller, D.: Emulgierwirkung als Spülmitteltest,
SÖFW-Journal 122, (1996), 406-408
56 WFK Forschungsprojekt AiF.FV Nr. 10186, WFK-
Forschungsinstitut für Reinigungstechnologie e.V.,
D-47798 Krefeld
Toxicological and environmental properties
57 Anionic Surfactants: Biochemistry, Toxicology,
Dermatology, 2nd ed., revised and expanded (C.
Gloxhuber and K. Künstler, eds.), Surfactant Science
Series, Vol. 43, Marcel Dekker, New York, (1992)
58 Bennen, J. A., Ruckenstein, E. and Coll, J.: Interface
Sci. 96, (1983), 469-487
43
59 Bercovici, R., Krüßmann, H.: Welttensidkongress
München, (1984)
60 Berenbold, H. and Kosswig, K.: Tenside Surf. Det.
32, (1995), 152-156
61 Brändel, S. and Dietzsch, K., in: “Alkansulfonate”
(H. G. Hauthal, ed.), VEB Deutscher Verlag für
Grundstoffindustrie, Leipzig, (1985)
62 Giesser, R.: Tenside Detergents 20, (1983), 25-527
63 Gilbert, A. and Pettigrew, R.: Surfactants and the
Environment, lnter. Journal of Cos. Science 6,
(1984), 149-158
64 Gloxhuber, C.: Arch. Toxicol. 32, (1974), 245-270
65 Hrsak, D., Bosnjak, M. and Johanides, V.: Kinetics
of linear Alkylbenzene Sulfonate and sec. alkane
sulfonate biodegradation, Tenside Detergents 18,
(1981)
66 Krone, M. and Schneider, G.: Biochemische Abbau-
barkeit von sek. Alkansulfonat unter Labor- und
Praxisbedingungen, Fette-Seifen-Anstrichmittel 70,
(1968), 10
67 Lötzsch, K.,. Neufahrt, A and Täuber, G.: Tenside
Det. 16, (1979), 155-155
68 Neufahrt, A., Lötzsch, K. and Weimer, K.: Radio-
metric studies of the biodegradation of sec. alkane
sulfonate in a sewage plant model, Inter. Deter.
Congress Barcelona, (1980)
69 Satake, I. and Matuura, R.: Bull. Chem. Soc. Japan
36, (1963), 813-817
70 Schöberl, P.: Tenside Surf. Det. 28, (1991), 6
71 Scholz, N. and Müller, F. J.: Chemosphere 25,
(1992), 563
72 Scholz, N.: Tenside Surf. Det. 28, (1991), 277
73 Schwuger, M. J.: Chem.-Ing. Techn. 42, (1970),
433-438
74 Stalmans, M. and Berenbold, H. et al: European
Life-Cycle Inventory for Detergent Surfactants
Production, Tenside Surf. Det. 32, (1995), 84-109
Analysis
75 Arens, M., Waldhoff, H. and Pfeiffer, H.: Fat Sci.
Technol. 96, (1994), 107-112
76 Berthold, H. and Janot, I., in: Alkansulfonate (H. G.
Hauthal, ed.), VEB Deutscher Verlag für Grund-
stoffindustrie, Leipzig, (1985), 189-217
77 Berthold, H. and Lipfert, G., in: Alkansulfonate (H. G.
Hauthal, ed.), VEB Deutscher Verlag für Grund-
stoffindustrie, Leipzig, (1985), 28-32
78 Eppert, G. and Liebscher, G. J.: Chromatogr. 356,
(1986), 372-378
79 Eppert, G. and Liebscher, G. J.: Chromatogr. Sci. 29,
(1991), 21-25
80 Field, J. A., Miller, D. J., Field, T. M., Hawthorne, S.
B. and Giger, W.: Anal. Chem. 64, (1992), 3161-3167
81 Field, J. A., Field, T. M., Poiger, T. and Giger, W.:
Environ. Sci. Technol. 28, (1994), 497-503
82 Field, J. A., Field, T. M., Poiger, T., Siegrist, H. and
Giger. W.: Wat. Res. 29, (1995), 1301-1307
83 Hummel, D. O.: GIT Fachz. Lab. 38, (1994), 439-447
84 Kloster, G., Schoester, M. and Schwuger, M. J.:
Journ. Com. Esp. Deterg. 24, (1993), 25-33
85 Klotz, H. and Spilker, R.: Tenside Surf. Det. 29,
(1992), 13-15
86 Liebscher, G. and Eppert, G.: Chem. 19, (1979), 69
87 Liebscher, G., Eppert, G., Oberender, H., Berthold,
H. and Hauthal, H. G.: Tenside Surf. Det. 26, (1989),
195
88 Liebscher, G.: Lecture to the Merck Forum, 14.
Sept. 1994.
89 Mahr, S. A., Wangsa, J. and Danielson, N. D.: Anal.
Chem. 64, (1992), 583-589
90 Schmitt, T. M., in: Analysis of Surfactants (M. J.
Schick and F. M. Fowkes, eds.), Vol. 40 of
Surfactant Science Series, Marcel Dekker, New
York, (1992), 37-40
91 Schoester, M., Kloster, G. and Fresenius, J.: Anal.
Chem. 345, (1993), 767-772
92 Zhou, D. and Pietrzyk, D. J.: Anal. Chem. 64, (1992),
1003-1008
Photos from page 8 – 21 courtesy of Miele & Cie.
This information is based on our present state of knowledge and is intended
to provide general notes on our products and their uses. It should not therefore be
construed as guaranteeing specific properties of the products described or their
suitability for a particular application. Any existing industrial property rights must be
observed. The quality of our products is guaranteed under our General Conditions
of Sale.
Electronically revised issue 05.2004, Federal Republic of Germany
EBR
5192
D 0
5.20
00
Clariant GmbH, Functional Chemicals Division , BU Detergents
D-65840 Sulzbach/Ts., Germany, Internet: http://www.detergents.clariant.com
Marketing, Phone + 49 61 96 757 78 22, Fax + 49 61 96 757 89 70
Research & Development, Phone + 49 69 305 22 98, Fax +49 69 31 84 35
Cm
mse
rv,
Fra
nkfu
rt a
m M
ain
o
Exactly your chemistry.