Non-petroleum based rejuvenating agent

Abstract

The invention provides a non-petroleum based rejuvenating agent to improve the performance of the recycled asphalt, and accordingly extend the service life of the recycled pavement.

Claims

1. A non-petroleum based rejuvenating agent applied to hot recycling asphalt concrete, characterized by comprising the following components in percentage: 40 to 80 percent of treated edible recovered oil, 10 to 50 percent of matrix asphalt, 0.1 to 5 percent of stabilizer, and 0.1 to 5 percent of antioxidant; wherein the treated edible recovered oil is obtained from edible recovered oil treated by dehydration, slag removal, color removal and flavor removal, and colloid removal processes.

2. The non-petroleum based rejuvenating agent according to claim 1, wherein the matrix asphalt is No. 90 road petroleum asphalt or No. 70 road petroleum asphalt.

3. The non-petroleum based rejuvenating agent according to claim 1, wherein the stabilizer is diaryl disulfide.

4. The non-petroleum based rejuvenating agent according to claim 1, where the antioxidant is Tetra [3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid] pentaerythyl alcohol ester, or tri(2,4-di-tert-butylphenyl) phosphite ester, or both.

5. The non-petroleum based rejuvenating agent according to claim 1, wherein the colloid removal process is treatment by one of: membrane separation, hydration, acid refining and mildew degelation.

Description

4. EMBODIMENTS

(1) The invention provides a non-petroleum based rejuvenating agent. In order to make the purpose of the invention, the technical proposal and the effect more clear and definite, the invention is further described in detail below. It should be understood that, the specific embodiments described herein are used only to explain, but not to limit the invention.

(2) This invention provides a kind of non-petroleum based rejuvenating agent, comprising 40 to 80 percent of treated edible recovered oil, 10 to 50 percent of matrix asphalt, 0.1 to 5 percent of stabilizer and 0.1 to 5 percent of antioxidant.

(3) Further, the matrix asphalt as above-mentioned is either No. 90 or No. 70 road petroleum asphalt. The stabilizer as above-mentioned is diaryl disulfide. The antioxidant as above-mentioned is Tetra [3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid]pentaerythyl alcohol ester, or tri(2,4-di-tert-butylphenyl) phosphite ester, or the both.

(4) Further, the treated edible recovered oil as above-mentioned is obtained from the edible recovered oil by dehydration, slag removal, color removal and flavor removal, and colloid removal processes. Colloid removal process refers to treatment by one of the following methods: membrane separation, hydration, acid refining and mildew degelation.

(5) To further describe the invention, the specific process of preparing the non-petroleum based rejuvenating agent in the invention is as follows:

(6) The edible recovered oil was placed and heated in the reactor in proportion, and continuously stirred in the heating process. When the temperature rose to 80° C.-120° C., the road petroleum asphalt at 100° C.-120° C. was added, and the stirring continued at constant temperature of 100° C.-120° C. for 10-20 minutes. Then, antioxidant was added and stirred constant temperature for 10-20 minutes. After that, stabilizer was added proportionately, continuously stirred and mixed at constant temperature for 60-90 minutes. Finally, the mixture was gradually cooled to room temperature to get the said non-petroleum based rejuvenating agent.

(7) Specifically, the details are explained by the examples below.

Example 1

(8) 65% edible recovered oil was placed in the reactor, stirred and preheated to 80° C. No. 90 road petroleum asphalt was preheated to 100° C. 31% No. 90 road petroleum asphalt was added to the reactor, and continuously stirred at constant temperature of 100° C. for 10 min. 2% Tetra [3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid]pentaerythyl alcohol ester and 1.5% tri(2,4-di-tert-butylphenyl) phosphite ester were added to the reactor, and continuously stirred at constant temperature for 10 min. Then, 0.5% diaryl disulfide was added, stirred and mixed at constant temperature for 65 min. The mixture was gradually cooled down to get the said non-petroleum based rejuvenating agent.

Example 2

(9) 76% edible recovered oil was placed in the reactor, stirred and preheated to 100° C. No. 90 road petroleum asphalt was preheated to 110° C. 21% No. 90 road petroleum asphalt was added to the reactor, and continuously stirred at constant temperature of 110° C. for 15 min. 1% Tetra [3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid]pentaerythyl alcohol ester and 0.5% tri (2,4-di-tert-butylphenyl) phosphite ester were added to the reactor, and continuously stirred at constant temperature for 15 min. Then, 1.5% diaryl disulfide was added, stirred and mixed at constant temperature for 80 min. The mixture was gradually cooled down to get the said non-petroleum based rejuvenating agent.

Example 3

(10) 61% edible recovered oil was placed in the reactor, stirred and preheated to 80° C. No. 70 road petroleum asphalt was preheated to 120° C. 32% No. 90 road petroleum asphalt was added to the reactor, and continuously stirred at constant temperature of 120° C. for 20 min. 3% Tetra [3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid]pentaerythyl alcohol ester and 2% tri(2,4-di-tert-butylphenyl) phosphite ester were added to the reactor, and continuously stirred at constant temperature for 20 min. Then, 2% diaryl disulfide was added, stirred and mixed at constant temperature for 70 min. The mixture was gradually cooled down to get the said non-petroleum based rejuvenating agent.

(11) To demonstrate the compliance of the non-petroleum based rejuvenating agent in the invention with the specification and standard for rejuvenating agents, the measured indicators of the non-petroleum based rejuvenating agent in the invention are listed below, as shown in Table 1.

(12) TABLE-US-00001 TABLE 1 Normative Item standards Example 1 Example 2 Example 3 60° C. Viscosity cSt Type RA-1: 71 68 70 50-175 Flash Point (° C.) ≥220  276 281 278 Saturated Content (%) ≤30 15.4 15.9 15.5 Aromatic Content (%) Actually 34 36 32 measured Ratio of Viscosity  ≤3 1.2 1.1 1.2 Before and After Thin-Film Oven Test Change of Mass ≤4, ≥−4 −0.8 −0.9 −0.8 Before and After Thin-Film Oven Test (%) 15° C. Density Actually 0.940 0.942 0.941 measured

(13) To further express the advanced nature of the non-petroleum based rejuvenating agent in the invention, the results of examples 1, 2 and 3 are compared with that of the petroleum-based rejuvenating agent before and after the recycling of aged asphalt, as shown in Table 2.

(14) TABLE-US-00002 TABLE 2 Penetration Ductility Softening Point Asphalt Index (mm) (cm) (° C.) Criteria of Recycled Asphalt 60-80 Actually ≥46 measured Undisturbed Aged Asphalt 13.1 0 70.4 Undisturbed Petroleum 32.1 11.2 56.7 Aged Asphalt Based Mixing Rejuvenating Ratio 12% Agent Example 1 79.4 >100 49.7 Example 2 80.9 >100 49.7 Example 3 79.2 98.0 49.6

(15) By the comparison, it is shown that that the reduction ability of the non-petroleum based rejuvenating agent in the invention is about 50% higher than that of the petroleum-based rejuvenating agent, which is a great progress of existing technology.

(16) No matter in the hot in-place recycling project or in the central plant hot recycling project, the production of non-petroleum based rejuvenating agent can be completed without limitation of site, personnel or other factors, provided that an reactor with heating and stirring function, all kinds of raw materials mixed in given proportion, sufficient heating temperature and stirring time are guaranteed.

(17) As for the hot in-place recycling, the prepared non-petroleum based rejuvenating agent is only required to be filled into the recycling unit in advance; and during the central plant hot recycling, the non-petroleum based rejuvenating agent may be delivered to the mixing cylinder through the pipeline for blending.

(18) In the invention, the adjustment of the blending proportion for the raw materials and the selection of the matrix asphalt depend on the service life and design of the original pavement, and the design criteria of new pavement. According to the technical standard desired in different pavement designs, the blending ratio of raw materials for the non-petroleum based rejuvenating agent in the patent is adjusted, so that the reduction of non-petroleum based rejuvenating agent is more targeted and purposeful, suitable for the heat recycling projects of different regions.

(19) Of course, the above descriptions are only better embodiments of the invention, and this invention is not limited to the above-listed embodiments. It should be stated that, all equivalent alternatives and obvious variants made by any technician familiar with the field under the instruction of this specification will fall within the substantive scope of this specification, which should be protected by the invention.