Arsenic removal method

• US 4,454,027 A
• Filed: 08/16/1982
• Issued: 06/12/1984
• Est. Priority Date: 08/16/1982
• Status: Expired due to Fees

• Current Assignee: GA Technologies Incorporated
• Original Assignee: Union Oil Company of California (Chevron Corp.)
• Inventors: Fenton, Donald M.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): MCFARLANE, ANTHONY R
• Application Number:
  US06/408,078
• Time in Patent Office: 666 Days
• Field of Search: 208/253, 208/251 R, 208/11 R
• US Class Current: 208/253
• CPC Class Codes: C10G 25/003 Specific sorbent material, not covered by C10G25/02 or C10G25/03

Abstract

Aqueous and organic fluids which contain arsenic are contacted with spent oil shale from an oil shale retorting operation and separated therefrom, yielding a fluid of reduced arsenic content. In one embodiment, shale oil is placed in contact with spent oil shale under conditions of elevated temperature and pressure to reduce the arsenic content of the oil.

Claims

1. A method for removing arsenic from a substantially liquid hydrocarbon fluid which comprises reacting the arsenic with spent oil shale, by passing the fluid through a bed of spent oil shale particles and separating a fluid having a reduced arsenic content.

2. The method defined in claim 1 wherein the fluid is shale oil.

3. The method defined in claim 1 wherein the fluid is reacted with spent oil shale in the presence of water.

4. The method defined in claim 1 wherein reacting is conducted at a temperature up to about 400°

C.

5. The method defined in claim 4 wherein reacting is conducted at a temperature between about 250°

C. and about 350°

C.

6. The method defined in claim 4, wherein reacting is conducted under a superatmospheric pressure sufficient to maintain the fluid in a substantially liquid state, up to about 4,000 p.s.i.a.

7. A method for removing arsenic from a substantially liquid hydrocarbon fluid which comprises reacting the fluid with spent oil shale, by passing the fluid through a bed of spent oil shale particles at a temperature between the freezing point of the fluid and about 400°

C., and at a pressure between atmospheric pressure and about 4,000 p.s.i.a., and separating a fluid having a reduced arsenic content.

8. The method defined in claim 7 wherein the temperature is between about 250°

C. and about 350°

C.

9. The method defined in claim 7 wherein the fluid is reacted with spent oil shale in the presence of water.

10. A method for removing arsenic from substantially liquid shale oil which comprises reacting the oil with spent oil shale, by passing the oil through a bed of spent oil shale particles at a temperature between about 250°

C. and about 350°

C., in the presence of water and under a superatmospheric pressure sufficient to maintain the water and oil in a substantially liquid state, up to about 4,000 p.s.i.a., and separating a shale oil having a reduced arsenic content.