EMERGENCY DISTILLATION COLUMN AND USE THEREOF

Abstract

An emergency distillation column is disclosed, connected to a plant wherein a main distillation column is present. Such connection occurs by means of by-pass of the pipes which supply said main column, which by-pass has stopping means of the liquid which allow the supply of said emergency column when the pressure drops downstream of the main column exceed a preset threshold value. Preferably, said stopping means are shut-off valves. A process of using the emergency is involves continuously measuring a pressure different between inflow and outflow of liquid being distilled and comparing the measured pressure against a dedicated threshold. A plant for the regeneration of waste oils is disclosed, comprising a distillation column, which furthermore comprises the emergency distillation column as disclosed herein.

Claims

1. An emergency distillation column connected to a plant having a main distillation column present, wherein such connection occurs by means of by-pass of pipes that supply said main distillation column, wherein the by-pass pipes have a liquid stopping means which allow a supply of said emergency column when a pressure drop downstream of the main column exceeds a preset threshold value.

2. The emergency distillation column as recited in claim 1, wherein the emergency distillation column is sized having a volume that is smaller than a volume of the main distillation column.

3. The emergency distillation column as recited in claim 1, wherein the liquid stopping means are shut-off valves.

4. The emergency distillation column as recited in claim 2, wherein the liquid stopping means are shut-off valves.

5. A thermal deasphaltation column for regenerating waste oils comprising two separate fractionating segments, wherein the two separate fractionating segments comprise a first fractionating segment comprising the main distillation column, and a second fractionating segment comprising the emergency column as recited in claim 1, wherein the thermal deasphaltation column is under vacuum, and wherein said two fractionating segments operate in a complementary way supporting one another.

6. The thermal deasphaltation column as recited in claim 5 further comprising a number of trays, wherein the number of trays can vary depending on a quality of the waste oil to be regenerated.

7. A process for using the emergency column recited in claim 1, wherein a pressure difference between an inflow and an outflow of liquid being distilled is measured continuously and compared against a dedicated threshold.

8. The process as recited in claim 7, wherein the dedicated threshold has a range of between 2 and 100 torr (266.64 to 13,332.2 Pa).

9. The process as recited in claim 7, wherein the dedicated threshold has a range of between 5 and 50 torr (666.61 to 6,666.1 Pa).

10. The process as recited in claim 7, wherein the dedicated threshold has a range of between 7 and 15 torr (933.25 to 1,999.83 Pa).

11. The process as recited in claim 7, wherein the process is a regeneration process of waste oils.

12. A plant for the regeneration of waste oils comprising the distillation column and comprising the emergency distillation column as recited in claim 1.

13. The plant as recited in claim 12 comprising a liquid loop pump associated with emergency distillation column for maintaining a vacuum within said column.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0018] These and other features and advantages of an emergency distillation column as disclosed herein will be appreciated as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawing wherein:

[0019] FIG. 1 is schematic diagram of an example distillation column as disclosed herein.

DETAILED DESCRIPTION

[0020] FIG. 1 represents a portion of a generic chemical or petrochemical plant. Based on such representation, the plant comprises a distillation column 1 and, according to the present invention, an emergency distillation column 2; based on a preferred embodiment, column 2 has a smaller volume than that of main distillation column 1, since the intervention thereof is expected to be temporary. A mixture to be separated is supplied to column 1 in flow 3. Column 1 can be a column of any type: tray column, flash column, packed column. Preferably, it is a packed column or a tray column, the latter making it easier to measure and assess pressure drops.

[0021] Various flows 4, 5, 6, 7 come out from column 1 and, at the head of the column, a discharge of head product 8 comes out.

[0022] Flows 4-6 are managed by means of respective pumps or compressors 9-12.

[0023] Analysing the individual flows, the paths are as described in the following.

[0024] Flow 4 is supplied to a pump or compressor 9. outflow 13 from pump 9 undergoes a by-pass with a flow 14, which provides on its path a shut-off valve 15, which opens to flow 14 a recycling on the bottom of column 1. Flow 13 goes to the further process steps, relating to the product contained in the same flow 13.

[0025] Flow 5 is supplied to a pump or to a compressor 10. Flow 16 coming out of pump 10 is supplied to emergency column 2.

[0026] Flow 6 is split into two flows, 17 and 18, respectively. Flow 17 is supplied to a pump or compressor 11, which has an outflow 19, which goes back in as recycling into column 1. Flow 18 is supplied to a pump or compressor 12, which supplies it to a heat exchanger 20. From heat exchanger 20 two flows come out. The first flow 21 goes back into column 1 directly, at the temperature obtained due to the heat exchange with heat exchanger 20. The second flow 22 is supplied to a second heat exchanger 23 which brings it to a higher temperature and recycles it to column 1, in a higher position than flow 21. Going back to flow 19, coming out of pump 11, it is split and, in addition to flow 19, recycled, as seen, in column 1, a second flow 24 is obtained. Flow 24 is split into two flows 25 and 26, provided with a shut-off valve 27 and 28, respectively. Flow 26 is recovered as product, while flow 25 is supplied to column 2. Column 2 is preferably of the same type as column 1 (so as not to require a recalibration of the operating parameters) and implies outflows 29, 30 and 31. Another outflow 32 provides a shut-off valve 33 and joins flow 13. Finally, an outflow 34, controlled by a shut-off valve 35, sends a flow coming out from column 2 to join flow 4. From the above, it is easily inferred that said liquid stopping means are shut-off valves 28, 33 and 35.

[0027] During standard operation, the oil to be regenerated is supplied in 3 to column 1. The fractioned distillation leads to a series of fractions having different weight and hence with different boiling point, partly directed to the recovery as more or less noble product, partly recycled. Normally, column 1 is capable of distilling, in a known manner, the oil fractions in a standard manner.

[0028] According to the present invention, the pressure difference between inflow and outflow of the liquid being distilled is measured continuously and compared against a dedicated threshold. Preferably, said threshold ranges between 2 and 100 torr (from 266.64 to 13, 332.2 Pa), more preferably between 5 and 50 torr (from 666.61 to 6,666.1 Pa), in the most preferred ways from 7 to 15 torr (from 933.25 to 1,999.83 Pa); thereby, the quality of the products is not worsened, due to the clogging of column 1. The measuring of said pressure difference can be done at different locations, for example at the inflow of column 1 and in correspondence of one of the outflows, or on one of the trays of column 1 or at any other reference location.

[0029] As long as the measured pressure difference is below said threshold, column 1 works independently to continue distillation and emergency column 2 remains inactive. When the pressure difference rises above the preset threshold, sign of a progressing clogging, emergency column 2 comes into action, so as to be able to maintain the plant in full operation. Valves 27, 33 and 35 open and column 2 is activated. Flow 16 and flow 25 enter column 2 and the separation by distillation thereof is started. From column 2 flows 29, 30 and 31 come out, which are sent directly to product recovery. Flow 32 joins instead flow 13, while flow 34 joins flow 4, to give flows 13 and 14. Advantageously, emergency column 2 operates at a pressure of 2,000-3,500 Pa.

[0030] Column 1 is thus deactivated and it can be provided to the regeneration thereof, in a way known per se, removing all the clogging material, while column 2 continues for this time the desired separation for the process.

[0031] Based on a preferred embodiment of the present invention, a liquid loop pump is associated with emergency column 2, apt to keep the vacuum at the head of column 2, without increasing excessively overall energy consumption.

[0032] Once regeneration has been carried out, column 1 is restarted and the measuring of the pressure difference will give a value below the threshold one. Thereby, valves 27, 33 and 35 are closed and column 2 stops working, leaving the task to column 1 only.

[0033] At this point, it can be suitable to clean column 2, so as to keep it ready for any new interventions, without the risk of finding it too clogged and to have to still stop the plant, impairing the extraordinary effects of the present invention.

[0034] Thereby, it is possible to avoid to forcedly stop the plant, thus reducing losses of energy and material, always operating in optimal flow and energy consumption conditions and maintaining unchanged product quality. Column 2, as can be seen, can be sized smaller, since the work is normally carried out for very short periods of time. A good arrangement of the connections between emergency column 2 and the rest of the plant allows to minimise the increase of consumption linked to the operation of column 2, using the ancillary produced energy in the various stages of the process or exploiting for its own functioning apparatuses already in use.

[0035] In another alternative embodiment, a thermal deasphaltation column is provided for the regeneration of waste oils, consisting of two separate fractionating segments, one consisting of a main distillation column 1 and the other consisting of an emergency column 2, as seen before. The column is preferably under vacuum. Based on this embodiment, the two segments operate in a complementary way and one supporting the other.

[0036] Based on this embodiment, the thermal deasphaltation column thus formed in two segments has a varying number of trays, depending on the quality of the waste oil to be regenerated.

[0037] However, it is understood that the invention must not be considered limited to the particular arrangement illustrated above, which makes up only an exemplifying embodiment thereof, but that different variants are possible, all within the reach of a person skilled in the field, without departing from the scope of protection of the invention, as defined by the following claims.

LIST OF REFERENCE CHARACTERS

[0038] 1 Primary distillation column [0039] 2 Emergency distillation column [0040] 3 Supply flow (of 1) [0041] 4 Outgoing flow (from 1) [0042] 5 Outgoing flow (from 1) [0043] 6 Outgoing flow (from 1) [0044] 7 Outgoing flow (from 1) [0045] 8 Flow produced at the head (from 1) [0046] 9 Pump or compressor [0047] 10 Pump or compressor [0048] 11 Pump or compressor [0049] 12 Pump or compressor [0050] 13 Outgoing flow (from 9) [0051] 14 Flow [0052] 15 Shut-off valve (of 14) [0053] 16 Outgoing flow (from 10) [0054] 17 Flow [0055] 18 Flow [0056] 19 Outgoing flow (from 11) [0057] 20 Heat exchanger [0058] 21 Recycling point (in 1) [0059] 22 Outgoing flow (from 20) [0060] 23 Heat exchanger [0061] 24 Flow [0062] 25 Flow [0063] 26 Flow [0064] 27 Shut-off valve (of 25) [0065] 28 Shut-off valve (of 26) [0066] 29 Outgoing flow (from 2) [0067] 30 Outgoing flow (from 2) [0068] 31 Outgoing flow (from 2) [0069] 32 Flow [0070] 33 Shut-off valve (of 32) [0071] 34 Outgoing flow (from 2) [0072] 35 Shut-off valve (of 34)