Process, method, and system for removing heavy metals from fluids

Patent metadata

Field	Value
Publication number	US-2016304791-A1
Application number	US-201514923514-A
Country	US
Kind code	A1
Filing date	Oct 27, 2015
Priority date	Oct 31, 2014
Publication date	Oct 20, 2016
Grant date	—

Abstract

A process for removing non-volatile, particulate mercury from crudes and condensates is disclosed. Particulate mercury in crudes can be removed by a process of first adding a halogen, such as I 2 . The halogen converts at least 10% of the particulate mercury into an oil-soluble mercury compound that cannot be removed by filtration or centrifugation. This oil-soluble mercury compound can then be removed by adsorption onto a solid adsorbent. The process can operate at near ambient conditions. The adsorption step can be carried out by mixing a particulate adsorbent in the halogen-treated crude and then removing it by centrifugation, desalting, filtration, hydrocyclone or by settling.

First claim

What is claimed is:

1 . A non-aqueous process to remove mercury from a crude, the process comprising:
mixing the crude containing particulate mercury with a halogen to form a digested crude to covert at least 10% of the particulate mercury into an oil-soluble mercury complex in the oil phase, contacting the digested crude with an adsorbent to remove at least 50% of the total mercury from the digested crude.

2 . The process of claim 1 , wherein the oil-soluble mercury complex comprises HgI 2 .

3 . The process of claim 1 , wherein the digested crude contains less than 2% total water as measured by Karl Fischer method.

4 . The process of claim 1 , wherein the halogen is selected from the group consisting of bromine, iodine and combinations thereof.

5 . The process of claim 1 , wherein the halogen is in the form of an organic solution.

6 . The process of claim 1 , wherein the mixing and the contacting are under conditions to maintain the crude essentially in the liquid state.

7 . The process of claim 6 , wherein the conditions comprise temperature and pressure for the crude to be below its bubble point.

8 . The process of claim 1 , wherein the halogen comprises iodine and bromine, and wherein the iodine and bromine are present at a I 2 :Br 2 molar ratio of greater than or equal to 0.1 and less than or equal to 1000.

9 . The process of claim 8 , wherein the I 2 :Br 2 molar ratio is greater than or equal to 5 and less than or equal to 100.

10 . The process of claim 8 , wherein the I 2 :Br 2 molar ratio is greater than or equal to 10 and less than or equal to 50.

11 . The process of claim 1 , wherein the adsorbent is selected from the group consisting of sulfur-containing polymers, anion exchange resins, molecular sieves, zeolites, metal organic framework (MOF) materials, metal oxides treated with sulfur compounds, carbon treated with sulfur compounds, clays, synthetic layered materials, sulfur-treated MOFs, self-assembled monolayers on mesoporous supports, selenium modified adsorbents, and combinations thereof.

12 . The process of claim 1 , wherein the adsorbent is a sulfur-treated metal oxides and carbon treated with sulfur compounds and the sulfur compounds are selected from the group consisting of thiosulfates, polysulfides and combinations thereof.

13 . The process of claim 1 , wherein the adsorbent is selected from the group consisting of thiosulfate-impregnated silica, polysulfide impregnated alumina, and combinations thereof.

14 . The process of claim 1 , wherein the adsorbent is essentially non-leachable.

15 . The process of claim 1 , wherein the contacting the digested crude with the adsorbent is in a process selected from the group consisting of a fixed bed, a fluidized bed, an ebullated bed, and expanded bed, and combinations thereof.

16 . The process of claim 1 , wherein the adsorbent is in the form of a powder and the powder is separated from the digested crude by processes selected from the group consisting of settling, filtration, centrifugation, hydrocyclones and combinations thereof.

17 . The process of claim 1 , wherein the crude is a fine-particulate high-mercury crude or condensate.

18 . The process of claim 1 , wherein the crude is predominantly non-volatile.

19 . The process of claim 1 , wherein the crude has a particulate mercury content of 10% or more.

20 . The process of claim 1 , further comprising recovery of the adsorbent and wherein the adsorbent to be recovered has a total mercury content of 100 ppm or more.

21 . The process of claim 20 , wherein the halogen is iodine and wherein at least a portion of the iodine and iodide that is adsorbed on the recovered adsorbent is recycled and mixed with a crude to form a digested crude.

Assignees

• Chevron Usa Inc

Inventors

• O'Rear Dennis John
• Wang Wei
• Malekzadeh Nga

Classifications

• C10G25/003

  Specific sorbent material, not covered by C10G25/02 or C10G25/03 · CPC title

• C10G29/02 Primary

  Non-metals · CPC title

• C10G25/12

  Recovery of used adsorbent · CPC title

• C10G2300/205

  Metal content · CPC title

• C10G57/00

  Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process · CPC title