Pyrolysis tar conversion

Patent metadata

Field	Value
Publication number	US-11530361-B2
Application number	US-202117495948-A
Country	US
Kind code	B2
Filing date	Oct 7, 2021
Priority date	Dec 16, 2016
Publication date	Dec 20, 2022
Grant date	Dec 20, 2022

Abstract

This invention relates to a process for determining the suitability of pyrolysis tar, such as steam cracker tar, for upgrading using hydroprocessing without excessive fouling of the hydroprocessing reactor. A pyrolysis tar is sampled, the sample is analyzed to determine one or more characteristics of the tar related to tar reactivity, and the analysis is used to determine conditions under which the tar can be blended, pre-treated, and/or hydroprocessed.

First claim

The invention claimed is:

1. A process for producing a hydroprocessed steam cracker tar (“SCT”), the process comprising:
(a) providing an SCT having a temperature T 1 ≤350° C. and a reactivity R T ≥28 Bromine Number units (“BN”), the SCT having a density at 15° C. ≥1.10 g/cm 3 and viscosity at 50° C. ≥1000 cSt, wherein at least 70 wt. % of the SCT has a normal boiling point of at least 290° C.;
(b) establishing a predetermined reference reactivity R Ref ≤18 BN;
(c) carrying out either
(i) conducting away at least a portion of the SCT or hydroprocessing at least a portion of the SCT under Mild Hydroprocessing Conditions, or
(ii) producing a treated SCT by carrying out one or more of
(A) one or more thermal treatments of at least a portion of the SCT by heating from T 1 to a temperature T HS , and maintaining the SCT at a temperature of at least T HS for a time t HS of at least 10 minutes to produce a treated SCT, wherein T HS is at least 10° C. greater than T 1 and T HS is in the range of 300° C. to 360° C. and t HS of ≥5 minutes, and
(B) combining at least a portion of the SCT with a second SCT; and
following steps (A) and/or (B) determining an R T of the treated SCT, and comparing R Ref and the R T of the treated SCT, and
(I) when R T of the treated SCT exceeds 12 BN, carrying out step (c)(i) or repeating steps (c)(ii)(A) and/or step (c)(ii)(B), or
(II) when R T of the treated SCT does not exceed R Ref , then conducting the treated SCT to step (d); and

(d) hydroprocessing the treated SCT, the hydroprocessing being carried out under Standard Hydroproces sing Conditions in the presence of (i) a utility fluid, (ii) at least one catalyst, and (iii) a treatment gas comprising molecular hydrogen to produce a hydroprocessor effluent comprising hydroprocessed SCT, wherein the Standard Hydroprocessing Conditions include a temperature ≥200° C., a pressure ≥8 MPa, a weight hourly space velocity (“WHSV”, tar basis) ≥0.3 hr −1 , and a molecular hydrogen consumption rate (tar basis) in the range of from 270 S m 3 /m 3 to about 534 S m 3 /m 3 .

2. The process of claim 1 , wherein (i) R T and R Ref are determined by a Bromine Number measurement and expressed in BN units, (ii) R Ref is ≤10 BN, and (iii) ≥90 wt. % of the SCT has a normal boiling point ≥290° C., (iv) the SCT has a viscosity at 15° C.≥1×10 4 cSt, and (v) the SCT has a density ≥1.1 g/cm 3 .

3. The process of claim 1 , wherein the utility fluid comprises two-ring and three-ring aromatics.

4. The process of claim 1 , wherein hydroprocessing of step (d) exhibits a 566° C.+ conversion of at least 20 wt. % continuously for at least ten days.

5. The process of claim 1 , wherein hydroprocessed SCT has a density measured at 15° C. that is at least 0.12 g/cm 3 less than that of the SCT.

6. The process of claim 1 , wherein the catalyst is a supported hydroprocessing catalyst which includes at least one metal selected from any of Groups 5 to 10 of the Periodic Table.

7. The process of claim 1 , wherein t HS is >20 minutes.

8. The process of claim 1 , wherein T HS <300° C.

9. The process of claim 1 , wherein T HS <250° C.

10. The process of claim 1 , wherein t HS is <70 minutes.

11. The process of claim 1 , wherein R T and R Ref are determined by one or more of electrochemical titration, colorimetric titration, and coulometric Karl Fischer titration.

12. The process of claim 1 wherein the reactivity R T of treated SCT conducted to step (d) is ≤18 BN.

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Kandel Kapil
• Heeter Glenn A
• Xu Teng
• Contello Giovanni S
• Emanuele Krystle J

Classifications

• C10G2300/302

  Viscosity · CPC title

• C10G2300/301

  Boiling range · CPC title

• C10G47/36 Primary

  Controlling or regulating · CPC title

• C10C1/19

  by thermal treatment not involving distillation · CPC title

• C10G1/00

  Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal (mechanical winning of oil from oil-shales, oil-sand, or the like B03B) · CPC title