Dishwashing detergent composition containing mixtures of crystallinity-disrupted surfactants
A technology of surfactant and composition, applied in the field of dishwashing compositions, can solve the problems of lack of degreasing and hard food cleaning, difficulty in preparing dishwashing detergent, poor low temperature stability, etc., and achieves improved production ease and excellent hardness. The effect of improving the resistance and the removal of grease stains
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Embodiment 1
[0056] prepared by skeletal isomerization of linear olefins
[0057] Crystallinity disrupted surfactant system step (a): at least partially reducing the linearity of olefins (by skeletal isomerization of preformed olefins to chain lengths suitable for cleaning product stain removal)
[0058] A mixture of 1-decene, 1-undecene, 1-dodecene and 1-tridecene (available for example from Chevron) in a weight ratio of 1:2:2:1 at 220°C and at any Suitable LHSV such as 1.0 is passed over a Pt-SAPO catalyst. The catalyst was prepared in the manner of the example of US 5,082,956. See WO95 / 21225, for example, Example 1 and description thereof. The product is a skeletally isomerized lightly branched olefin having a chain length suitable for the preparation of alkylbenzene sulfonate surfactants for consumer mix cleaning compositions. More typical temperatures for this step may range from about 200°C to about 400°C, preferably from about 230°C to about 320°C. Th...
Embodiment 2
[0063] prepared from linear olefins by skeletal isomerization
[0064] Surfactant systems with crystallization disruption
[0065] The procedure of Example 1 was repeated except that sulfur trioxide (without dichloromethane solvent) was used as the sulfonating agent in the sulfonation step (c). Details of sulfonation using a suitable air / sulfur trioxide mixture are given in US 3,427,342 to Chemithon. Also, step (d) uses sodium hydroxide instead of sodium methoxide for neutralization.
Embodiment 3
[0067] prepared by skeletal isomerization of linear olefins
[0068] Crystallinity disrupted surfactant system step (a): at least partially reducing the linearity of the olefin
[0069] A mixture of C11, C12 and C13 monoolefins was passed over the H-ferrierite catalyst in a weight ratio of 1:3:1 at 430°C. The method and catalyst in US5,510,306 can be used for this step. Boiling volatiles were distilled off at up to 40°C / 10mmHg. Step (b): Alkylation of the product of step (a) with an aromatic hydrocarbon
[0070] In a glass autoclave sleeve, add the slightly branched olefin mixture of 1 molar equivalent step (a), the benzene of 20 molar equivalents and the shape-selective zeolite catalyst (acidic mordenite catalyst Zeocat TM FM-8 / 25H). The glass thimble was enclosed in a stainless steel shaker autoclave. With 250 psig N 2 The autoclave was purged twice, then 1000 psig N 2 . The mixture was heated to 170-190° C. with stirring overnight...
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