Systems and methods for pyrolysis of feedstock in chemical furnaces

Patent metadata

Field	Value
Publication number	US-2020199459-A1
Application number	US-201816621321-A
Country	US
Kind code	A1
Filing date	Jun 25, 2018
Priority date	Jun 29, 2017
Publication date	Jun 25, 2020
Grant date	—

Abstract

A furnace having a convection section with convection tubes in a convection compartment is disclosed. The convection tubes receive and preheat hydrocarbon feed primarily by convection of heat from hot flue gas that flows into in the convection section. The convection section additionally includes a perforated distributor plate that prevents flow channeling of the hot flue gas as it flows into the convection section. The furnace also includes a radiant section having radiant tubes in a radiant compartment. The radiant tubes are in fluid communication with the convection tubes so that preheated hydrocarbon feed flows from the convection section to the radiant section. The radiant section burns fuel and heats the preheated hydrocarbon feed primarily by radiation and from the hot flue gas, which flows from the radiant section into the convection section.

First claim

1 . A furnace comprising:
a convection section that comprises convection tubes disposed in a convection compartment, the convection tubes adapted to receive hydrocarbon feed and to preheat the hydrocarbon feed primarily by convection of heat from hot flue gas that flows into the convection section, the convection section comprising a perforated distributor plate adapted to prevent flow channeling of the hot flue gas as it flows into the convection section; and a radiant section that comprises radiant tubes disposed in a radiant compartment, the radiant tubes in fluid communication with the convection tubes so that preheated hydrocarbon feed flows from the convection section to the radiant section, the radiant section adapted to burn fuel and heat the preheated hydrocarbon feed primarily by radiation and from the hot flue gas, wherein the furnace is adapted so that the hot flue gas flows from the radiant section into the convection section.

2 . The furnace as claimed in claim 1 , further comprising a stack section for receiving cooled flue gas from the convection section and discharging the cooled flue gas to the atmosphere.

3 . The furnace as claimed in claim 1 , wherein the perforated distributor plate is located in a lower ¼ of the convection section.

4 . The furnace as claimed in claim 1 , wherein the perforated distributor plate has a plurality of holes that form a free open area in a range from 0.1% to 5.5%.

5 . The furnace as claimed in claim 1 , wherein a difference in temperature between tube areas on each side of the convection tubes is not greater than 5% of average temperature.

6 . The furnace as claimed in claim 1 , wherein the perforated distributor plate is configured to provide a uniform flow distribution such that no flue gas flow channeling is evident by velocity or mass flow distribution in an area immediately below the convection tubes after passing of the hot flue gas through the perforated distributor plate.

7 . The furnace as claimed in claim 1 , wherein the perforated distributor plate has a thickness of 3 to 13 mm.

8 . The furnace as claimed in claim 1 , wherein the hot flue gas enters the convection section and passes through the distributor plate before encountering the convection tubes.

9 . The furnace as claimed in claim 1 , wherein the hot flue gas enters the convection section from one side and passes upwardly through the distributor plate.

10 . The furnace as claimed in claim 1 , wherein the convection section is adapted so that the hot flue gas also preheats at least one of fuel or steam.

11 . An apparatus comprising:
means for preheating hydrocarbon feed by convection of heat from hot flue gas; means for preventing flow channeling of the hot flue gas as it flows into proximity with the hydrocarbon feed; and means for heating the preheated hydrocarbon feed and producing the hot flue gas.

12 . The apparatus as claimed in claim 11 , further comprising:
means for receiving cooled flue gas and discharging the cooled flue gas to the atmosphere.

13 . The apparatus as claimed in claim 11 , wherein the means for preventing flow channeling is configured to provide a uniform flow distribution such that no flue gas flow channeling is evident by velocity or mass flow distribution in an area immediately below the means for preheating hydrocarbon feed after passing of the hot flue gas through the means for preventing flow channeling.

14 . The apparatus as claimed in claim 11 , further comprising means for receiving the hot flue gas from one side and directing the hot flue gas to pass upwardly through the means for preventing flow channeling before the hot flue gas encounters the means for preheating hydrocarbon feed.

15 . The apparatus as claimed in claim 11 , further comprising: means for preheating at least one of fuel or steam by convection of heat from hot flue gas.

16 . A method comprising:
preheating hydrocarbon feed by convection of heat from hot flue gas; preventing flow channeling of the hot flue gas as it flows into proximity with the hydrocarbon feed; and heating the preheated hydrocarbon feed and producing the hot flue gas.

17 . The method as claimed in claim 16 , further comprising receiving cooled flue gas and discharging the cooled flue gas to the atmosphere.

18 . The method as claimed in claim 16 , wherein the preventing flow channeling includes providing a uniform flow distribution such that no flue gas flow channeling is evident by velocity or mass flow distribution immediately prior to preheating the hydrocarbon feed after the preventing flow channeling.

19 . The method as claimed in claim 16 , further comprising:
receiving the hot flue gas from one side; and directing the hot flue gas to pass upwardly for the preventing flow channeling before the hot flue gas is used for the preheating hydrocarbon feed.

20 . The method as claimed in claim 16 , further comprising preheating at least one of fuel or steam by convection of heat from hot flue gas.

Assignees

• Sabic Global Technologies Bv

Inventors

• Rampure Mohanrao
• Bunama Ramsey

Classifications

• F27D17/10

  Arrangements for using waste heat · CPC title

• F27D17/17

  for preheating fluids, e.g. air or gases · CPC title

• F27B1/22

  Arrangements of heat-exchange apparatus · CPC title

• F27B9/3005

  arrangements for circulating gases · CPC title

• F27B9/10

  heated by hot air or gas · CPC title