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1,4-Dioxane –A Current Topic for Household Detergent
and Personal Care Formulators
L. Matheson and G. Russell -
SASOL N.A.B. MacArthur and W. B. Sheats
-
Chemithon
100th
AOCS Annual Meeting, May 6, 2009
1,4-Dioxane: What Are The Issues?
Recent reports suggest that 1,4-Dioxane has been detected at measurable levels (1 to 100ppm) in some personal care products.
1,4-Dioxane is recognized as a toxic substance that should be controlled.
The source of 1,4-Dioxane has been inaccurately reported.
The reality is:1,4-Dioxane is not a significant by-product of the base-catalyzed ethoxylation of fatty alcohols. 1,4-Dioxane is a controllable by-product of the highly acidic sulfation process to make AES.
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What is 1,4-Dioxane?
1,4-Dioxane
Not to Be Confused with Dioxin
Dioxin
1,4-Dioxane is not the same as dioxin.
The focus of this presentation is on how and where 1,4-
Dioxane is created and what can be done to control its formation.
However, it should be noted that thorough risk assessments of 1,4-Dioxane exposure from cleaning products have been conducted.
Good examples can be found at: www.heraproject.com
HERA (Human and Environmental Risk Assessment) is a voluntary industry program to carry out risk assessements
on household cleaning product ingredients.Alcohol Ethoxylates Version 1.0. (2007, May)Alcohol Ethoxysulphates – Human Health Risk Assessment – Draft. (2003, January)
Risk from 1,4-Dioxane Exposure in Household and Personal Care Products
Where Does 1,4-Dioxane Come From?
Recent publications suggest 1,4-Dioxane is formed through ethoxylation of fatty alcohols.
However, in-house evaluation of alcohol ethoxylates produced by Sasol North America shows <5ppm of 1,4-Dioxane in the ethoxylates used in household and personal care products.
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Where Does 1,4-Dioxane Come From?
RO H + M+OH- RO- + M+ + H2OFeedstock Catalyst
EORO CH2 CH2O-
EO RO CH2 CH2 O CH2 CH2 O-
EO etc.
H+RO (CH2CH2O)nH
Ethoxylate
1,4-Dioxane is not easily formed
under conditions of alkaline catalyzed ethoxylation of fatty alcohols.
Most 1,4-Dioxane is produced during the sulfation of ethoxylated alcohols to make AES.
The thin film sulfation reaction with SO3
occurs under highly acidic conditions.
This has been recognized for some time, and control methods are practiced in the Industry.
Assuming that active levels of any one ingredient in personal care products are about 10%, then the 1,4-
Dioxane in the final product would be diluted by a factor of 10 from that of the starting ingredient.
Where Does 1,4-Dioxane Come From?
SO3 Sulfation of Alcohol Ethoxylates (AE)
R-(EO)n
-OH + SO3
R-(EO)n
-OSO3
H
Reaction occurs under strongly acidic conditions.
Neutralization of the AES acid should occur promptly after sulfation to minimize decomposition and to reduce
by-product formation.
OO
OSO3-
ROSO3
H + NaOH ROSO3
Na
Formation of 1,4-Dioxane by Excess SO3
1,4-Dioxane can be formed from ethoxymers
with >1 mole of EO when excess SO3
is used.
Factors Influencing the Level of 1,4-Dioxane During the Sulfation of AE to Make AESProcess and Equipment Factors
SO3 : AE feed mole ratioReactor loading%SO3 concentration in airResidence time of AES acid prior to neutralizationDe-aeration and stripping of AES paste
Feedstock Compositional Factors Average degree of ethoxylationPEG and moisture contentEO adduct distribution
1,4-Dioxane Study by Chemithon and Sasol
Objective: Sulfate an alcohol ethoxylate and generate response surfaces showing dependence of 1,4-Dioxane on process conditions for making AES.
Experimental Design:
Three Factorial Design -
Central CompositeSO3 : AE feed mole ratio%SO3 concentration in airReactor loading (kg/hr-cm of wetted reactor surface)
Response Measurements 1,4-Dioxane (ppm in 100% active product)Klett Color (5% active basis, 40mm path)Free Oil (wt% in 100% active product)Sodium Sulfate (wt% in 100% active product)
AE Feedstock for Experimental Design StudyFeedstock Analysis:
C1412-3 Ethoxylate –
KOH catalyzed linear, primary C12 and C14 alcohol ethoxylated to approximately 3 moles
Ave Moles EO: 2.8
Ave MW: 329
Wt.% Free Alcohol: 12.1
Wt.% PEG: 0.8
ppm 1,4-Dioxane: 0.1
ppm Moisture: 260
1,4-Dioxane vs. Loading & Mole Ratio at 3% SO3
------Then------
Constant Factor: 3% SO3 in air
Loading
Loading
Mole Ratio
Mole Ratio
1,4-Dioxane
1,4-
Dio
xane
Mole Ratio&
ReactorLoading
1,4-Dioxane
1,4-Dioxane vs. Loading & Mole Ratio at 4% SO3
Mole Ratio
Mole Rati
o
Loading
Loading
1,4-Dioxane
1,4-
Dio
xane
Constant Factor: 4% SO3 in air
Reactor Loading
Mole Ratio
1,4-Dioxane
------Then------
1,4-Dioxane vs. SO3 Concentration & Mole Ratio
SO3 Conc
SO 3Conc
Mole Ratio
Mole Ratio
1,4-Dioxane
1,4-
Dio
xane
Constant Factor: 0.92 Reactor Loading
------Then------
Mole Ratio&
SO3Concentration
1,4-Dioxane
1,4-Dioxane vs. SO3 Concentration & Reactor Loading
Loading
Loading
SO3 Conc
SO3 Conc
1,4-Dioxane
1,4-
Dio
xane
Constant Factor: 0.99 Mole Ratio(Slight excess of AE)
SO3Concentration
ReactorLoading
------Then------
1,4-Dioxane
------Then------
Color vs. SO3 Concentration and Mole Ratio
Low color is a very important quality parameter for AES for personal care formulations.
Mole Ratio
Mole Ratio
SO3 Conc
SO3 Conc
Klett C
olor
Kle
ttC
olor
Constant Factor: 0.92 Reactor Loading
SO3Concentration
KlettColor
Color vs. SO3 Concentration and Reactor Loading
0.99 Mole RatioLoading
Loading
SO3 Conc
SO3 Conc
1,4-Dioxane
1,4-
Dio
xane
Loading
Loading
SO3 Conc
SO3 Conc
Klett C
olor
Kle
ttC
olor
Conditions which yield low color (i.e. low SO3 concentration), will generally yield low levels of 1,4-
Dioxane.
SO3Concentration
1,4-Dioxane &
Klett
ColorThen
Free Oil vs. SO3 Concentration and Mole Ratio
Conditions which give lower 1,4-Dioxane generally yield
high free oil levels.
Mole Ratio
Mole Ratio
SO3 Conc
SO3 Conc
Free Oil Fr
ee O
il
Constant Factor: 0.92 Reactor Loading
Mole Ratio
------Then------
Free Oil
How to Minimize 1,4-Dioxane in AES
1.
Proper Conditions for Thin Film SO3
SulfationSO3
to AE mole ratio of 1.0 or lowerSO3
concentration in air at 3%Reactor loading at ~1 kg/hr -
cm
2.
Properly Designed Thin Film Sulfation Equipment
1,4-Dioxane Reduction by Stripping AES Paste
Reduction of 1,4-Dioxane content in neutral 70% AES paste can be accomplished by stripping.
The reduction factor (Inlet 1,4-Dioxane/Outlet 1,4-Dioxane) in a single stripping stage depends on the weight ratio of stripping steam to AES paste employed.
Reduction ratios from 2 to 10 can be achieved economically.
De-aeration of 70 wt% active AES paste occurs simultaneously upon stripping.
AES Stripping System for 1,4-Dioxane Removal
Steam
Cond
Steam
1,4-DioxaneDestruction
Product AES
AES Paste
Stripper
1,4-Dioxane Removal in Stripper
72% Active AES with 100ppm Inlet
Stri
pper
Out
let 1
,4-D
ioxa
ne
(ppm
wt 1
00%
Act
. Bas
is)
How to Minimize 1,4-Dioxane in AES
1.
Proper Conditions for Thin Film SO3
SulfationSO3
to AE mole ratio of 1.0 or lowerSO3
concentration in air at 3%Reactor loading at ~1 kg/hr -
cm
2.
Properly Designed Thin Film Sulfation EquipmentSulfation reactor and subsequent neutralizationDe-aeration and stripping of neutralized 70% active AES paste
3.
Appropriate Choice of AE Feedstock
Laboratory Studies on 1,4-Dioxane Formation
Sulfation with excess SO3
Ethoxylate Feedstock CharacteristicsDegree of Ethoxylation
Content of High Mole PEG By-Product
Content of High Mole EO Adducts
The Effect of SO3 / AE Mole Ratio
0
100
200
300
400
0 0.2 0.4 0.6 0.8 1 1.2
Mole Ratio of SO3/ETO
1,4-
Dio
xane
(ppm
)
1,4-Dioxane vs. EO Adduct Length in AESppm 1,4-Dioxane (100% active basis)
0 0
408212
812
1858 17822093
1285
0
500
1,000
1,500
2,000
2,500
0 1 2 3 4 5 6 7 8
C12 EO Adduct Chain Length
`
Ethoxylate comparisons are on equimolar
basis, sulfated at 1.03 mole ratio.
Formation of 1,4-Dioxane by Excess SO3
Excess SO3
finds few unreacted
hydroxyl groups and attacks ether oxygens
instead.Higher EO adducts have more sites to attack.
0
5
10
15
20
25
30
35
40
45
0 2 4 6 8 10 12 14
1 EO2 EO3 EO
1214GC (70:30) Alcohol EO Adduct Distributions
EO Mole Adducts
Wei
ght %
1214GC-1 10 Wt% ≥
5 EO1214GC-2 25 Wt% ≥
5 EO1214GC-3 39 Wt% ≥
5EO
0
5
10
15
20
25
30
0 2 4 6 8 10 12 14 16
BRE
NRE
EO Adduct Distributions for 1214GC-2 Mole Ethoxylates, NRE vs. BRE
EO Mole Adducts
Wei
ght %
BRE 25 Wt% ≥
5 EONRE 11 Wt% ≥
5 EO
Effect of By-Product PEG in AE
HOO
OO
OO
OO
OO
OO
OO
OH
PEG comes from residual water present during ethoxylation.
Typical PEG by-product in 1412-3 ethoxylate
•Less than 0.8 weight % PEG in AE
•Ave. MW of 750 for PEG (17 EO units) compared to 435 for alcohol ethoxylate (3 EO units)
H2 O + EO HO CH2 CH2 O H+ more
EOEthylene Glycol
Effect of Moisture in Sulfation Feed
H2
O + SO3 (gas) H2
SO4 (liquid)
H2
O combines with SO3
and forms H2
SO4
H2
SO4 condenses as liquid droplets and forms localized excess of sulfating agent.
Over-sulfation and heat of reaction can lead to increased formation of 1,4-Dioxane.
How to Minimize 1,4-Dioxane in AES
1.
Proper Conditions for Thin Film SO3
SulfationMole ratio of 1.0 or lowerSO3
concentration in air at 3%Reactor Loading at ~1 kg/hr -
cm
2.
Properly Designed Thin Film Sulfation EquipmentSulfation reactor and subsequent neutralizationStripping of neutralized 70% active AES paste
3.
Appropriate choice of AE feedstockMinimize high mole EO adductsLow PEG and low moisture levels in AE
Conclusions
The main source of the 1,4-Dioxane reported in household and personal care products is from the sulfation of AE to produce alcohol ether sulfates (AES).
Our data shows only 5ppm or less 1,4-Dioxane can be attributed to the original alcohol ethoxylate feedstock.
The use of proper sulfation equipment, optimum process conditions, and good quality AE feed should produce AES containing less than 100ppm of 1,4-Dioxane on 100% active basis.
Stripping of the 70% AES paste can reduce the 1,4-Dioxane levels even further.