Enhancement of the Byproducts of a Regeneration Process of Exhaust Oils

Abstract

A process for the enhancement of the byproducts of a process for the regeneration of exhaust oils is described, wherein said process for the regeneration of exhaust oils which includes at least one of the following steps: a) passing of the oil to be regenerated into one or more centrifuges, b) storage of the oil, before treatment, in suitable containers, c) desiloxanation and d) filtering. The byproducts of one or more of steps a) to d) are treated, gathered and mixed with one another and added to the bitumen coming out as tail of a fractioned distillation step of the above-said regeneration process of exhaust oils.

A plant for the carrying out of a process according to any one of the preceding claims is also described, comprising a processing unit for each of the byproducts coming from steps a) to d) and a mixer (6) with stirring (7).

Claims

1. A process for the enhancement of the by-products of a process for the regeneration of exhaust oils, wherein said process for the regeneration of exhaust oils comprises at least one of the following steps: a) passing of the oil to be regenerated into one or more centrifuges, b) storage of the oil, before the treatment, in suitable containers, c) desiloxanation and d) filtering, characterised in that the by-products of one or more of the steps a) to d) are treated, gathered and mixed with one another and added to the bituminous material exiting from the exhaust oil regeneration plant.

2. The process as in claim 1 characterised in that the by-products coming from step a) undergo a decanting step, to reduce the water contents thereof.

3. The process as in claim 2, characterised in that the solid material coming out of decanting is mixed with a strongly dehydrating agent.

4. The process as in claim 3, characterised in that said strongly dehydrating agent is CaO.

5. The process as in claim 1 characterised in that the by-products coming from step b) and/or from step c) are mixed directly with one another and with any other possibly treated by-products.

6. The process as in claim 1 characterised in that the by-products coming from step c) are micronised.

7. A plant for carrying out a process according to claim 1 characterised in that it comprises a processing unit for each of the byproducts coming from steps a) to d) and a mixer (6) with stirring (7).

8. The plant as in claim 7, characterised in that it furthermore comprises a decanter (2) for the by-products of step a).

9. The plant as in claim 8, characterised in that it furthermore comprises a reactor-decanter (10) within which, through a pipe (9), the products coming from the decanter (2) are supplied, and through a pipe (12) a strong dehydrating agent, such as CaO, is supplied.

10. The plant as in claim 7 characterised in that it comprises a micronisation unit for the by-products coming from step c).

11. Bitumen, characterised in that it is obtained through a process according to claim 1.

Description

[0027] Decanter 2 provides an outlet 8 - preferably located far away from pipe 1, so that the suspension supplied by pipe 1 does not become cloudy and pollutes with solids the waste water coming out of 8 - and a drain pipe 9 which leads to a reactor-decanter 10, equipped with stirring 11 and, preferably, with a cooling device, known per se. Reactor-decanter 10 is fed, as well as by the pipe 9 coming from decanter 2, also by a pipe 12, coming from a container 13, containing quicklime, generally under nitrogen flow, to avoid undesired hydration thereof, with the risk of an excessive development of heat and of making the lime unsuitable for the aimed objects.

[0028] A pipe 14 connects reactor-decanter 10 to mixer 6, while the wastes are removed as waste water by pipe 15.

[0029] Moving on to the micronisation unit, it is connected to mixer 6 through a pipe 16.

[0030] Moving on to mixer 6 itself, it comprises two outlets, a waste water outlet 17 and a product outlet 18.

[0031] In the following, the enhancement process of the byproducts is illustrated.

[0032] If the regeneration process of exhaust oils provides a centrifugation step, the solid residue is removed in a known manner from the centrifuge and is stored. It is then sent, through pipe 1, to decanter 2. That is, any byproducts coming from step a) undergo a decanting step to reduce the water contents thereof. For such operation a supply pump is generally provided. Although “solid residue” has been mentioned, supply 1 in actual fact consists of a slurry of solid particles in oil and water and forms something between a liquid and a paste, so that it is a material which can be easily pumped. This step can be performed continuously or batchwise. If it is a continuous supply, it will have to be relatively small with respect to the mass contained in decanter 2, while if it is operated batchwise, after supply in 2, the material will have to be left to sit for a certain length of time. In any case, the mass contained in 2 must be able to lie virtually unperturbed, so as to allow the solid material to go downwards and the liquid to rise to the surface. A certain degree of separation is thus obtained: the liquid, mostly (polluted) waste water, on the surface, is removed through pipe 8 and sent to a waste water treatment step, to then be disposed of in the sewage; the solid is instead made to go through pipe 9, to then end up in reactor-decanter 10. Simultaneously, quicklime (CaO or calcium oxide) is supplied, passing through container 13 (where it is contained, as stated, under nitrogen to prevent the quenching reaction thereof by air moisture), through pipe 12, in the same reactor-decanter 10. In practice, the solid material coming out of decanting is mixed with a heavily dehydrating substance and, preferably, said heavily dehydrating substance is CaO, easily available and cheap. The reaction is strongly exothermic and this is the reason why reactor-decanter 10 is preferably coated by a heat exchanger, of a type known per se, containing a coolant. A stirrer 11 causes the solid coming from decanter 2 and the CaO coming from container 13 to be mixed intimately, creating wide contact surfaces between the two solids, so as to greatly increase the reaction yield. In addition to the removal of any acids, the CaO reacts with the water still imbibing the solid, according to the reaction:

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[0033] From the bottom of reactor-decanter 10 a solid mixture comes out containing the initial solids, coming from centrifugation, dehydrated and hydrated lime [Ca(OH).sub.2]. This mixture, through pipe 14, is transported into mixer 6. Any waste liquid is sent by pipe 15 to the waste water disposal plant, possibly after a thermal oxidation step of the substances therein contained.

[0034] In case a desiloxanation unit is present in the exhaust oil regeneration plant, comprising an alumina bed, when said alumina has been saturated, it must be removed, possibly after undergoing some regeneration cycle, in a manner known per se. Normally, such removal occurs periodically, after a certain number of regeneration cycles and/or after a usage time which compensates the opposite needs of not replacing the alumina too often and of having still sufficiently removal yields. Alternatively, it is possible to measure desiloxanation efficiency by replacing the alumina when the silica contents in the oil being regenerated exceeds a preset threshold.

[0035] In any case, the exhaust alumina is supplied, through pipe 3, to micronisation unit 4, wherein the particles are unbundled and the average size thereof is reduced. The solid, micronised alumina is transported by pipe 16 to mixer 6.

[0036] If there is a filtration unit comprising celite, it is sent directly to mixer 6 from supply 5. Supply 5 carries to mixer 6 also the sludge of the storage tanks of the oil to be treated. In practice, the byproducts coming from step b) and possibly from step c) are mixed directly with one another and with any other byproducts, treated as seen.

[0037] In mixer 6 the supplied substances are mixed by stirrer 7. Thereby the solids, coming from pipes 14, 16 and 5, are mixed with the oily material, coming from the sludge, coming from pipe 5. Pipe 17 removes any waste substances, after a thermal oxidation step, while the tail material, through pipe 18, is sent to the final use.

[0038] It has thus been discovered, in a fully surprising manner, that the material which is transported by pipe 18 can - due to simple treatments illustrated earlier - be easily and advantageously mixed with the bituminous material which comes out of the exhaust oil regeneration plant and which, unlike what was thought, contributes to remarkably improving the physical and chemical properties of the produced bitumen; only the treatments provided according to the present invention allow to obtain such a result. In particular, if this material is added to a higher-quality bitumen, for example like the one which can be obtained according to EP 3 098 291, it imparts the bitumen such properties as to make it solid or almost solid at room temperature, which is highly desirable for some processes.

[0039] It must be considered that the different supplies of this process consist of byproducts which, up until the present patent application, were not reused and were thus turned into waste upon removal from the plant. This type of waste, containing different polluting substances, was furthermore to be classified as special waste, which require burdensome storage conditions and expensive processes for the disposal thereof, in any case ending up impacting on the environment. Thereby, these byproducts, instead of becoming wate, become instead part of one of the products of these processes which are sold. On the contrary, the addition thereof to these products even increases the value thereof, making it possible to increase the gain for whoever implements the process, given that they have - fully unexpectedly -greater amounts of a product having a very likely higher unitary cost. The present invention hence makes up an excellent example of circular economy, achieving advantages both in economic and environmental terms.

[0040] It must also be taken into account that, up until today, there was no indication in the art which enabled the skilled person to understand that a process like the one just described could lead to the actually achieved result, while in actual fact it was believed that these byproducts could only negatively affect the bitumen and could hence not be mixed therewith.

[0041] However, it is understood that the invention must not be considered limited to the special arrangement illustrated above, which makes up only an examplary embodiment thereof, but that different variants are possible, all within the reach of a skilled person, without departing from the scope of protection of the invention, as defined by the following claims.

[0042] In particular, although the process and the plant have been described starting from the assumption that all the byproducts were employed, it must be clear that, remaining in the scope of the present invention, there is an enhancement even if one or more of the byproducts should lack, although probably the value of the bitumen obtained at the end can be lower than that containing all the byproducts; in any case, even in these cases the bitumen would reach a greater value than that currently on the market.

[0043] Moreover, the process subject of the present application would be implemented with alumina and/or celite of a different origin than exhaust oil regeneration.

[0044] Some actuation examples of the process according to the present invention are reported in the following.

[0045] From 1-2 tons of alumina, 1-2 tons of product obtained in 14 and from 5 tons of celite 21 tons of high-quality bitumen were obtained, sold by the Applicant under the trademark Visco-flex 1000.

[0046] From 2 tons of alumina 28 tons of bitumen were obtained, sold by the Applicant under the name Itelplus 2.

[0047] From 2 tons of material transported in 14, 28 tons of bitumen were obtained, sold under the name Viscoplus 1.

[0048] Finally, from 5 tons of celite, 25 tons of bitumen were obtained, sold under the trade name Viscoplus 2.

TABLE-US-00001 1 Supply centrifuge residues 2 Decanter 3 Alumina supply pipe 4 Micronisation unit 5 Celite and tank sludge supply 6 Mixer 7 Stirrer (of 6) 8 Output (of 2) 9 Product drain pipe (of 2) 10 Reactor-decanter 11 Stirrer (of 10) 12 Pipe 13 Container 14 Pipe 15 Waste drain 16 Pipe 17 Waste drain 18 Product drain