FIELD OF THE INVENTION

This invention relates to a system for conversion of a hydrocarbonaceous feed wherein an amount of the converted feed may solidify, and specifically a system for removing halides from a hydrocarbon stream comprising one or more hal ides.

BACKGROUND OF THE INVENTION

Refinery processes comprise a plurality of treatments of hydrocarbon rich streams in order to provide products in the form of gasoline, diesel, etc. Such treatments comprise hydro-treatment, hydro-cracking, fractionation and strip ping, as well as intermediate heat exchange and removal of impurities.

Some of the hydrocarbon rich streams to be processed in the refinery com prises halides, e.g. comprising chlorine. Halides are unwanted in the product(s) and are also disadvantageous within the refinery plant due to corrosion issues within the units of the plant.

In addition to halides, other heteroatoms are also present in the treated hydro carbons, e.g. nitrogen. During hydrotreatment organically bound nitrogen may be released as ammonia. Ammonia and halides may react to form salts, e.g. ammonium chloride, which is a solid at temperatures below 270 °C. Precipita tion of such salts may result in partial or complete blocking of process lines and must therefore be avoided. Therefore, it is important to ensure the process tem perature to be above 270°C. Typically, the hydrotreatment reactions are exothermal, and therefore it is possi ble to optimize the energy consumption of the process, by heat exchange be tween feed and effluent. If ammonia and halides are present a problem in this respect is however that in a feed/effluent heat exchanger feed temperatures be low 270°C may result in cold zones in the heat exchanger, where e.g. ammo nium chloride may precipitate.

According to the present invention a halides removal washing system is de scribed, which is able to absorb halides from a process gas stream with a wash water injected into the process gas stream by means of an injector pipe and - nozzle.

WO 2015/050635 relates to a process for removing sulfur and halides from a hydrocarbon stream by hydrotreatment. The document is silent on the presence of nitrogen in the intermediate stream, and contrary to the present disclosure it explicitly recommends recuperation of heat from the hydrotreated product by heat exchange with chilled water, which is highly likely to cause precipitation of salts, if nitrogen was present.

BRIEF SUMMARY OF THE INVENTION

The halides removal washing system of the invention comprises a process gas duct suited for conduction of a process gas comprising halides. The system also comprises an injector pipe extending into the process gas duct. The injector pipe has a wash water inlet in a first end arranged outside the process gas duct and a wash water outlet with an injector nozzle in a second end of the injector pipe arranged within the process gas duct. The injector nozzle is adapted to spray the wash water into the process gas in the process gas duct downstream of the injector nozzle to absorb halides from the process gas. The halides removal washing system of this invention when used in a process gas duct with process gas comprising halides has the advantages that it en sures that NH4CI will not precipitate on any surfaces when operated properly. Thermal stress on pressure bearing parts at injection is avoided by the mechan ical design as it will be explained in more details in relation to the figures. The mixing of wash water and feed ensures washout of HCI above 99.9 %.

In an embodiment of the invention the system comprises anti-precipitation means arranged around at least a part of the injector pipe which extends into the process gas duct. It is to be understood that anti-precipitation means are means which helps ensure that the surface of the injector pipe will not be cold relative to the process gas. If the surface of the injector pipe is relative cold compared to the process gas around it, there is a risk that parts of the process gas will precipitate on the surface of the injector pipe, which may lead to corro sion. The anti-precipitation means may for example be heating means or insula tion.

In a further embodiment anti-precipitation means are arranged around at least a part of the injector nozzle. It is especially beneficial to provide the injector pipe and the injector nozzle with anti-precipitation means, since these members may otherwise provide relative cold surfaces on which there is a high risk of precipi tation of parts of the process gas.

The anti-precipitation means may be in form of heat insulation. In a further em bodiment the anti-precipitation means may be an injector purge channel adapted to provide a relative hot purge fluid compared to the temperature of the wash water. In a further embodiment, the anti-precipitation means may be a heat tracing, e.g. electrical heating wiring, an electrical wiring which can heat up the surfaces of the injector nozzle and the injector pipe when an electrical cur rent is sent through the electrical wiring. The effects of the heat insulation, the purge channel, heat tracing and further anti-precipitation means is avoidance of precipitation on surfaces which other wise would be relative cold as compared to the process gas.

In an embodiment of the invention, the process gas duct has an anti-corrosion liner arranged on the inside surface of the process gas duct downstream of the injector nozzle. In an embodiment, this anti-corrosion liner may be arranged ad jacent to the inside surface of the process gas duct, leaving a gap between the inside surface of the process gas duct and the anti-corrosion liner. This gap al lows for a purge fluid to flow between the anti-corrosion liner and the process gas duct. The gap may in one embodiment be in the range of 0.2 - 50 mm. Fur thermore, a sealing may be provided between the anti-corrosion liner and the process gas duct for the process gas not to enter the gap and for controlled flow of the purge gas. Also, a purge fluid connection to the process gas duct down stream of the injector nozzle may be provided, which is adapted to purge fluid into the gap.

In an embodiment of the invention one or more mixers are arranged within the process gas duct downstream of the injector nozzle to provide mixing of the pro cess gas.

In a further embodiment of the invention, not only one but a plurality of injector pipes and a plurality of injector nozzles are provided. The plurality of injector pipes and -nozzles may be arranged within a single process gas duct or there may also be a plurality of process gas ducts, each with one or more injector pipes and -nozzles. The plurality of process gas ducts may all be connected to a common process gas duct upstream of the injector nozzles in a manifold setup.

As mentioned in the above, the described halides removal washing system may be used in a hydrotreatment process. Throughout this text, the term “Organic halides” are chemical compounds in which one or more carbon atoms are linked by covalent bonds with one or more halogen atoms (fluorine, chlorine, bromine, iodine or astatine - group 17 in cur- rent lUPAC terminology). “Inorganic halides” are chemical compounds between a halogen atom and an element or radical that is less electronegative (or more electropositive) than the halogen, to make a fluoride, chloride, bromide, iodide, or astatine compound, with the further limitation that carbon is not part of the compound.

The term “removing halides” is meant to include situations where either some of the halides present or all of the halides present is removed. The term is thus not limited to situation where a certain percentage of the halides present are re moved.

The system disclosed may be found useful where the feed is a waste product comprising halides, such as direct hydrotreatment of waste plastic or hydrotreat ment of the product from pyrolysis of waste plastic. The feed may also originate from algae lipids, grown in salt water, or other biological feeds comprising hy- drocarbons and chloride.

An example of the halides removal washing system will be explained in more detail in the following with reference to the figures.

BRIEF DESCRIPTION OF THE FIGURES

Figure 1 shows an overview of a halides removal washing system. Figure 2 shows a detailed view of a part of a halides removal system.

POSITION NUMBERS

01. Process gas duct.

02. Injector pipe. 03. Injector nozzle.

04. Injector connection flange.

05. Heat insulation.

06. Injector purge channel.

07. Heat tracing. 08. Duct liner.

09. Duct sealing.

10. Mixing element.

11. Duct purge.

DETAILED DESCRIPTION OF THE FIGURES

Fig. 1 shows an overview of a halides removal washing system according to an embodiment of the invention. In this embodiment a manifold solution is used, with a plurality, in this case four process gas ducts 01 connected to a common process gas duct. For simplicity, only one of the process gas ducts has position numbering, it is to be understood, that the other three process gas ducts com prise similar components with the like position numbers. Within each of the pro cess gas ducts an injector pipe 02 is arranged through the common process gas duct, upstream and within the process gas duct downstream of the common process gas duct. At a first end of the injector pipe, an injector connection flange 04 provides for a wash water inlet. At the second end of the injector pipe an injector nozzle 03 is arranged in fluid connection to the injector pipe and the injector connection flange. The injector nozzle is adapted to spray a wash water into the process gas stream flowing in the process gas duct. Downstream the injector nozzle and within the process gas duct a number of mixing elements 10 are arranged in series to provide mixing of the process gas.

In Fig. 2 the part of the halides removal washing system with the injector pipe and -nozzle is shown in more detail. In this larger view, it can be seen that injec tor pipe is provided with both a heat insulation 05 and a heat tracing 07 to pre vent any precipitation of the relative hot process gas on the injector pipe with the relative cold wash water. Also, the injector nozzle has a heat tracing and it further has an injector purge channel 06 around the nozzle also to prevent pre cipitation of the relative hot process gas. The process gas duct has a duct liner 08 arranged within, adjacent to the inner surface of the process gas duct, starting a little upstream of the injector nozzle and stretching downstream of the injector nozzle. The liner is arranged with a gap between the liner ant the inner surface of the process gas duct, thereby al- lowing for a duct purge 11 fluid flow. To control this purge fluid flow, a duct seal ing 09 is arranged at the start of the liner upstream, between the liner and the inner surface of the process gas duct.