IP Library Granted Patent US 8,137,456
Granted Patent B2
US 8,137,456 · App. 11/608,062 · Granted Mar 20, 2012

Process for the preparation of sulphur cement or a sulphur cement-aggregate composite

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Quick Facts
Patent No.
US 8,137,456
App. No.
11/608,062
Granted
Mar 20, 2012
Kind
B2
Abstract

The present invention provides a process for the preparation of sulphur cement or a sulphur cement-aggregate composite comprising the following steps: (a) admixing at least an inorganic filler and/or aggregate and a polysulphide-containing organosilane having at least two organosilyl groups and allowing the organosilane to react with the inorganic filler and/or aggregate; (b) admixing during or after step (a) elemental sulphur with the inorganic filler and/or aggregate at a temperature at which sulphur is liquid to obtain an admixture comprising molten sulphur and inorganic filler and/or aggregate; and (c) solidifying the admixture to obtain sulphur cement or a sulphur cement-aggregate composite. The invention further provides sulphur cement or a sulphur cement-aggregate composite obtainable by such process and the use of a polysulphide-containing organosilane having at least two organosilyl groups as coupling agent in sulphur cement or a sulphur cement-aggregate composite.

Claims (36)

1. A process for the preparation of sulphur concrete, wherein the process comprises the following steps: (a) admixing at least an inorganic filler and/or aggregate and a polysulphide-containing organosilane, bis(3-triethoxysilylpropyl)tetrasulphide, and allowing the polysulphide-containing organosilane to react with the inorganic filler and/or aggregate; (b) admixing during or after step (a) elemental sulphur with the inorganic filler and/or aggregate at a temperature at which sulphur is liquid to obtain an admixture comprising molten sulphur and inorganic filler and/or aggregate; and (c) solidifying the admixture to obtain the sulphur concrete.

2. A process according to claim 1 , wherein step (a) is performed prior to step (b).

3. A process according to claim 2 , wherein the amount of organosilane admixed with the inorganic filler and/or aggregate is in the range of from 0.01 to 0.2 wt % based on the weight of inorganic filler and aggregate.

4. A process according to claim 3 , wherein the filler or aggregate has oxide or hydroxyl groups on its surface.

5. A process according to claim 4 , wherein the filler and/or aggregate is a silicate.

6. A process according to claim 5 , wherein the polysulphide-containing organosilane is dissolved in a solvent when admixed in step (a) with the inorganic filler and/or aggregate.

7. A process according to claim 6 , wherein the organosilane is dissolved in ethanol when admixed in step (a) with the inorganic filler and/or aggregate.

8. A process according to claim 2 , wherein the amount of organosilane admixed with the inorganic filler and/or aggregate is in the range of from 0.02 to 0.1 wt % based on the weight of inorganic filler and aggregate, and wherein the filler or aggregate has oxide or hydroxyl groups on its surface.

9. A process according to claim 1 , wherein the amount of organosilane admixed with the inorganic filler and/or aggregate is in the range of from 0.01 to 0.2 wt % based on the weight of inorganic filler and aggregate.

10. A process according to claim 9 , wherein the filler or aggregate has oxide or hydroxyl groups on its surface.

11. A process according to claim 10 , wherein the filler and/or aggregate is a silicate.

12. A process according to claim 11 , wherein the polysulphide-containing organosilane is dissolved in a solvent when admixed in step (a) with the inorganic filler and/or aggregate.

13. A process according to claim 12 , wherein the organosilane is dissolved in ethanol when admixed in step (a) with the inorganic filler and/or aggregate.

14. A process according to claim 1 , wherein the amount of organosilane admixed with the inorganic filler and/or aggregate is in the range of from 0.02 to 0.1 wt % based on the weight of inorganic filler and aggregate, and wherein the filler or aggregate has oxide or hydroxyl groups on its surface.

15. A process for the preparation of sulphur concrete, wherein the process comprises the following steps:

(a) admixing at least an inorganic filler and/or aggregate and a polysulphide-containing organosilane that is bis(3-triethoxysilylpropyl)tetrasulphide and allowing the polysulphide-containing organosilane to react with the inorganic filler and/or aggregate;

(b) admixing during or after step (a) elemental sulphur with the inorganic filler and/or aggregate at a temperature at which sulphur is liquid to obtain an admixture comprising molten sulphur and inorganic filler and/or aggregate; and

(c) solidifying the admixture to obtain the sulphur concrete.

16. A process comprising:

(a) admixing an inorganic ingredient with an organosilane that is bis(3-triethoxysilylpropyl)tetrasulphide, (TESPT) under conditions such that said organosilane is allowed to react with said inorganic ingredient to thereby form a first admixture;

(b) admixing elemental sulphur with said first admixture at a first temperature at which sulphur is liquid to obtain a second admixture comprising molten sulphur and said inorganic ingredient; and

(c) solidifying said second admixture by cooling said second admixture to a second temperature below the melting temperature of sulphur.

17. A process as recited in claim 16 , wherein the amount of organosilane admixed with said inorganic ingredient is in the range of from 0.01 to 0.2 wt % based on the weight of said inorganic ingredient.

18. A process as recited in claim 17 , wherein said admixing step (a) is conducted at a temperature in the range of from 120 to 150° C.

19. A process as recited in claim 18 , wherein said admixing step (b) is conducted at a temperature in the range of from 120 to 180° C.

20. A process as recited in claim 19 , wherein said inorganic ingredient is an inorganic filler or an inorganic aggregate or both.

21. A process as recited in claim 20 , wherein said inorganic ingredient has an oxide or an hydroxyl group on its surface.

22. A process as recited in claim 21 , wherein said organosilane is dissolved in a solvent when admixed with said inorganic ingredient.

23. A process as recited in claim 22 , wherein said solvent has a boiling temperature less than the temperature at which admixing step (a) is conducted in order to allow said solvent to evaporate during said admixing step (a).

24. A process comprising: mixing an inorganic ingredient, an organosilane bis(3-triethoxysilylpropyl)tetrasulphide, and sulphur at a first temperature at which said sulphur is liquid and under conditions such that said organosilane reacts with said inorganic material to form an admixture; and cooling said admixture to a second temperature below the melting temperature of sulphur to thereby solidify said admixture.

25. A process as recited in claim 24 , wherein the amount of organosilane mixed with said inorganic ingredient and said sulphur is in the range of from 0.02 to 0.1 wt % based on the weight of said inorganic ingredient.

26. A process as recited in claim 25 , wherein said first temperature is above 120° C.

27. A process as recited in claim 26 , wherein said inorganic ingredient is an inorganic filler or an inorganic aggregate or both.

28. A process as recited in claim 27 , wherein said inorganic ingredient has an oxide or an hydroxyl group on its surface.

29. A process as recited in claim 28 , wherein said organosilane is dissolved in a solvent when admixed with said inorganic ingredient.

30. A process as recited in claim 29 , wherein said solvent has a boiling temperature less than the temperature at which said mixing step is conducted in order to allow said solvent to evaporate during said mixing step.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 23, 2007
From: VAN TRIER, ROB ALOYSIUS MARIA; VERBIST, GUY LODE MAGDA MARIA
To: SHELL OIL COMPANY
Reel/Frame 019214/0025 →