Process for improved water wash in FCC gas concentration units

• US 5,858,206 A
• Filed: 05/20/1997
• Issued: 01/12/1999
• Est. Priority Date: 05/20/1997
• Status: Expired due to Fees

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Castillo, Ricardo
• Primary Examiner(s): GRIFFIN, WALTER DEAN
• Application Number:
  US08/859,298
• Time in Patent Office: 602 Days
• Field of Search: 208/47, 208/48 R, 208/95, 208/101, 208/113
• US Class Current: 208/101
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: C10G 11/18 according to the "fluidised-bed" technique

Abstract

Wash water is used to remove impurities such as hydrogen sulfide, ammonia, and hydrogen cyanide from light hydrocarbons and gases derived from refinery fluid catalytic cracking operations. The present invention is a process of low pressure recirculation of wash water combined with low pressure removal of waste water which results in the efficient removal of the above impurities at significantly reduced wash water rates.

Claims

1. A process for water washing an overhead stream withdrawn from an FCC main fractionator of an FCC unit processing an FCC feedstock to remove impurities from the overhead stream, said process comprising:

a) admixing said overhead stream with a first portion of a first water recycle stream at a low pressure ranging from about 140 to about 350 kPa to provide a combined overhead stream;

b) cooling and at least partially condensing the combined overhead stream to provide a cooled overhead stream and passing the cooled overhead stream to a low pressure separator to provide a low pressure vapor stream, a low pressure liquid stream, and a low pressure aqueous stream;

c) raising the low pressure vapor stream to an intermediate pressure ranging from about 525 to about 800 kPa to provide an intermediate vapor stream and admixing the intermediate vapor stream with a wash water stream and a second portion of the first water recycle stream to provide an intermediate pressure admixture;

d) raising the intermediate pressure admixture to a high pressure ranging from about 1155 to about 1575 kPa to provide a high pressure stream and cooling and at least partially condensing the high pressure stream to provide a cooled high pressure stream and passing the cooled high pressure stream to a high pressure separator to provide a high pressure vapor stream, a high pressure liquid stream and a high pressure aqueous stream; and

,

e) recycling at least a portion of the high pressure aqueous stream as the first water recycle stream, and withdrawing a portion of the low pressure aqueous stream as a sour water stream.

2. The process of claim 1 wherein the wash water is selected from the group consisting of fresh water, a refinery condensate, a treated sour water stream, and mixtures thereof.

3. The process of claim 1 wherein the impurities are selected from the group consisting of hydrogen sulfide, hydrogen cyanide, ammonia, nitrogen compounds, and mixtures thereof.

4. The process of claim 1 wherein the overhead stream comprises C₁ -C₅ hydrocarbons, water, and impurities.

5. The process of claim 1 wherein a volumetric percentage of the first water recycle stream admixed with the intermediate vapor stream comprises between about 0.1 and 10 percent of the FCC feedstock.

6. The process of claim 1 further comprising admixing a portion of the low pressure aqueous stream with the overhead stream.

7. The process of claim 6 wherein a ratio of the portion of the low pressure aqueous stream admixed with the overhead stream to the portion of the low pressure aqueous stream withdrawn as the sour water stream ranges from about 0.40 to about 0.60 volume fraction.