Process for increasing process furnaces energy efficiency

US10190060B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10190060-B2
Application numberUS-201415120701-A
CountryUS
Kind codeB2
Filing dateDec 23, 2014
Priority dateFeb 25, 2014
Publication dateJan 29, 2019
Grant dateJan 29, 2019

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A process for increasing furnace energy efficiency through gas turbine integration by using turbine exhaust gas, wherein a hydrocarbon feed is heated in a furnace.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for increasing process furnaces energy efficiency through gas turbine integration by using turbine exhaust gas, wherein a hydrocarbon feed is heated in a furnace, said process comprising the following steps: i) feeding furnace combustion air to burners of said furnace together with furnace fuel to provide high temperature heat to said furnace; ii) cooling the hydrocarbon feed thus processed by using water from a steam drum under the formation of water vapour from some of the water; iii) returning the mixture of water and water vapour thus formed to said steam drum; iv) withdrawing saturated high-pressure steam from said steam drum and feeding said saturated high-pressure steam to a heat recovery unit; and v) feeding said turbine exhaust gas to said heat recovery unit for converting said high-pressure steam into super heated high pressure steam, thereby decoupling the gas turbine from the process furnace. 2. The process according to claim 1 , wherein said furnace is from the group including a steam cracker furnace, a propane dehydrogenation furnace, and a butane dehydrogenation furnace. 3. The process according to claim 1 , wherein said furnace is a steam cracker furnace and wherein in step i) high temperature heat is provided to a radiant section of said cracking furnace for pyrolysis of the hydrocarbon feed present in said radiant section under cracking conditions. 4. The process according to claim 1 , further comprising preheating furnace combustion air through hot flue gasses from said furnace and/or hot flue gasses from said heat recovery unit. 5. The process according to claim 1 further comprising preheating boiler water through hot flue gasses from said heat recovery unit and feeding the boiler feed water thus preheated to said steam drum. 6. The process according to claim 1 , further comprising preheating boiler water through hot flue gasses from a furnace and feeding the boiler feed water thus preheated to said steam drum. 7. The process according to claim 1 , wherein step ii) is carried out using a transfer line exchanger (TLE). 8. The process according to claim 1 , wherein said heat recovery unit further comprises an evaporator and/or a steam generator. 9. The process according to claim 1 , wherein said heat recovery unit comprises one or more duct burners for providing additional heating capacity for providing super heated high pressure steam. 10. The process according to claim 9 , further comprising one or more fresh air suppliers for providing air to said one or more burners. 11. The process according to claim 1 , further comprising one or more economizers, steam generators, steam drums and super heaters, operated at lower pressures to produce heat medium and/or low pressure steam. 12. The process according to claim 1 , further comprising heating process liquids or gasses by feeding said process liquids or gasses to said heat recovery unit.

Assignees

Inventors

Classifications

  • C10G9/002Primary

    Cooling of cracked gases · CPC title

  • Formation of non-aromatic carbon-to-carbon double bonds only · CPC title

  • using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants (using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10) · CPC title

  • C10G9/36Primary

    with heated gases or vapours · CPC title

  • in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US10190060B2 cover?
A process for increasing furnace energy efficiency through gas turbine integration by using turbine exhaust gas, wherein a hydrocarbon feed is heated in a furnace.
Who is the assignee on this patent?
Saudi Basic Ind Corp, Sabic Global Technologies Bv
What technology area does this patent fall under?
Primary CPC classification C10G9/002. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jan 29 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 4 related publications on this page (citations in our corpus or others sharing the same primary CPC).