Method for the hydroprocessing of renewable feeds

Abstract

In a method for the hydroprocessing of renewable feeds in a hydroprocessing unit (unit A), comprising the use of sour waste water from the same or another unit (unit B), which is processing feeds containing sulfur and nitrogen, as wash water in unit A, thereby changing the pH of the waste water from unit A to lower the risk of carbonic acid corrosion of corrodible steel parts in unit A, the renewable material in unit A is directed to contact a material that is catalytically active in hydrogenating the renewable material in the presence of hydrogen, and the effluent is combined with the wash water stream which contains hydrogen sulfide and/or ammonia.

Claims

1. A method for the hydroprocessing of renewable feeds in a hydroprocessing unit (unit A), said method comprising: using sour waste water from another unit (unit B), which is processing feeds containing sulfur and nitrogen, as wash water in the unit A, thereby changing a pH of waste water from the unit A to lower the risk of carbonic acid corrosion of corrodible steel parts in the unit A, wherein the renewable feeds in the unit A is directed to contact a material that is catalytically active in hydrogenating the renewable feeds in the presence of hydrogen and the wash water, and an effluent from the unit A is combined with the wash water, which contains hydrogen sulfide and ammonia, and wherein the unit B, which is processing feeds containing sulfur and nitrogen and produces the sour waste water, is a hydroprocessing unit treating petroleum-based feeds.

2. The method according to claim 1, wherein chemicals containing nitrogen and/or sulfur are injected into the wash water to control the pH thereof.

3. The method according to claim 2, wherein ammonia is injected into the wash water.

4. The method according to claim 1, wherein the pH of the waste water from the unit A is raised to a value of 7.0 or above.

5. The method according to claim 4, wherein the pH of the waste water from the unit A is raised to a value of 8.0 or above.

6. The method according to claim 1, wherein the sour waste water contains more than 100 ppm hydrogen sulfide.

7. The method according to claim 1, wherein the sour waste water contains more than 100 ppm ammonia.

8. The method according to claim 1, wherein the wash water which contains hydrogen sulfide and ammonia creates an iron sulfide film capable of protecting the surface of carbon steel in at least one of the hydroprocessing units.

Description

(1) The present invention relates to a method for the hydroprocessing of renewable feeds in a hydroprocessing unit (unit A), said method comprising the use of sour waste water from the same or another unit (unit B), which is processing feeds containing sulfur and nitrogen, as wash water in unit A, thereby changing the pH of the waste water from unit A to lower the risk of carbonic acid corrosion of corrodible steel parts in unit A,

(2) wherein the renewable material in unit A is directed to contact a material that is catalytically active in hydrogenating the renewable material in the presence of hydrogen and the wash water, and the effluent is combined with a water stream which contains hydrogen sulfide and/or ammonia.

(3) WO 98/17743 describes a method and an apparatus for the treatment of fluid catalytic cracking (FCC) product gases. The method de-acidifies the wet gas from the FCC fractionation column before it is compressed for further processing, thereby reducing the volume and the corrosive nature of the gas stream as it is processed. In a preferred process for de-acidification, a gas-liquid contact surface is used to interact the gas stream with an ammonia solution to bind and remove the acid gases from the gas stream before the gas stream enters the main compressor. Specifically, an acid-containing (CO.sub.2 and H.sub.2S) hydrocarbon stream is de-acidified using an ammonia solution, and a sour water stream is generated and subsequently stripped.

(4) The WO document mentioned above does not disclose the use of sour waste water obtained from a unit which processes feeds containing nitrogen (NH.sub.3) and sulfur (H.sub.2S) as washing water for a hydroprocessing unit that is treating renewable feeds containing carbonic acid (CO.sub.2). Even though the de-acidifying step disclosed in the WO document is similar to that of the present invention, i.e. acid+base.fwdarw.salt+water, the process of the present invention involves the use of sour waste water as an active component in a hydroprocessing unit, whereas in the WO document, the generated sour water stream is just stripped.

(5) In the prior art, sour waste water from hydroprocessing units is typically routed to the sour water stripper for subsequent treatment. According to the method of the present invention, some of the sour waste water will bypass the sour water stripper and be pumped to the wash water surge drum of a hydroprocessing unit treating renewable feeds, with the purpose of being used as wash water.

(6) As a second embodiment of the method according to the invention, chemicals containing nitrogen and/or sulfur, such as ammonia and/or hydrogen sulfide, can be added to the wash water to control the pH thereof.

(7) The ammonia in the waste water from other hydroprocessing units will raise the pH of the waste water from the unit treating renewable feeds. The risk of carbonic acid corrosion of carbon steel is completely eliminated for pH>8.5, but in many cases the risk will be insignificant already at pH>7.5 to 8.

(8) The hydrogen sulfide in the waste water from other hydroprocessing units can also create an iron sulfide (FeS) film that may protect the surface of carbon steel from further corrosion from CO.sub.2 and H.sub.2S. Even in low concentrations where a sulfide film may not form, some benefit from CO.sub.2 corrosion is expected.

(9) Using the method of the present invention, the volume of sour water requiring treatment in the sour water stripper is reduced. The sour wash water can also release some H.sub.2S into the recycle gas to help keeping the recycle gas sour, thus reducing the amount of DMDS (dimethyl disulfide) that may be needed to keep the catalyst sulfided.

(10) In the method of the invention, the pH of the waste water from unit A is preferably raised to a value of 7.0 or above. More preferably, the pH of the waste water from unit A is raised to a value of 8.0 or above, whereby the risk of carbonic acid corrosion of corrodible steel parts is eliminated.

(11) The unit that produces sour water (unit B) is preferably a hydroprocessing unit that is treating petroleum-based feed stocks.