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Position: Chinese Standard in English/SH/T 3045-2003
SH/T 3045-2003   Calculation of the thermal efficiency for petrochemical tubular heaters (English Version)
Standard No.: SH/T 3045-2003 Status:superseded remind me the status change

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Implemented on:2004-7-1 Delivery: via email in 1 business day

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,2024-10-1,2004-7-1,141137413041913E6D1AE6F9CDCB6
Standard No.: SH/T 3045-2003
English Name: Calculation of the thermal efficiency for petrochemical tubular heaters
Chinese Name: 石油化工管式炉热效率设计计算
Chinese Classification: P72    Petrochemical and chemical industry engineering
Professional Classification: SH    Professional Standard - Petrochemical
Source Content Issued by: NDRC
Issued on: 2004-3-10
Implemented on: 2004-7-1
Status: superseded
Superseded by:SH/T 3045-2024
Superseded on:2024-10-1
Superseding:SH 3045-1992
Target Language: English
File Format: PDF
Word Count: 6000 words
Translation Price(USD): 180.0
Delivery: via email in 1 business day
1 Scope This standard specifies the design and calculation method of thermal efficiency of gas-fired and oil-fired petrochemical tubular heaters. This standard is applicable to the design and calculation of thermal efficiency of gas-fired and oil-fired petrochemical tubular heaters. 2 Terms and definitions For the purposes of this document, the following terms and definitions apply. 2.1 thermal efficiency total heat absorbed divided by total heat input, or difference of total heat input minus total heat loss divided by total heat input 2.2 system object whose thermal efficiency is calculated by thermal balance The objects outside the boundary of the system are all referred to as the external environment 2.3 total heat absorbed sum of the used heat output from the system to the external environment 2.4 total heat input sum of heat from the external environment to the system 2.5 total heat loss sum of the unused parts of heat from the external environment to the system 2.6 lower heating value heat of reaction when the water vapor in the combustion products still exists in gaseous state after the fuel is completely burned, based on 15°C 2.7 sensible heat heat absorbed or released by a substance along change in temperature. Generally, it refers to the sensible heat under specified pressure 2.8 datum temperature reference temperature that measures the heat brought in or out by objects crossing the boundary of the system, entering the system, or leaving the system, under which, it is assumed that the enthalpy values of all objects are zero 3 Design and calculation of thermal efficiency 3.1 The thermal efficiency shall be calculated using Equations (1) and (2):
Foreword i 1 Scope 2 Terms and definitions 3 Design and calculation of thermal efficiency Annex A (Informative) Design and calculation chart Explanation of wording in this standard
Code of China
Standard
SH/T 3045-2003  Calculation of the thermal efficiency for petrochemical tubular heaters (English Version)
Standard No.SH/T 3045-2003
Statussuperseded
LanguageEnglish
File FormatPDF
Word Count6000 words
Price(USD)180.0
Implemented on2004-7-1
Deliveryvia email in 1 business day
Detail of SH/T 3045-2003
Standard No.
SH/T 3045-2003
English Name
Calculation of the thermal efficiency for petrochemical tubular heaters
Chinese Name
石油化工管式炉热效率设计计算
Chinese Classification
P72
Professional Classification
SH
ICS Classification
Issued by
NDRC
Issued on
2004-3-10
Implemented on
2004-7-1
Status
superseded
Superseded by
SH/T 3045-2024
Superseded on
2024-10-1
Abolished on
Superseding
SH 3045-1992
Language
English
File Format
PDF
Word Count
6000 words
Price(USD)
180.0
Keywords
SH/T 3045-2003, SH 3045-2003, SHT 3045-2003, SH/T3045-2003, SH/T 3045, SH/T3045, SH3045-2003, SH 3045, SH3045, SHT3045-2003, SHT 3045, SHT3045
Introduction of SH/T 3045-2003
1 Scope This standard specifies the design and calculation method of thermal efficiency of gas-fired and oil-fired petrochemical tubular heaters. This standard is applicable to the design and calculation of thermal efficiency of gas-fired and oil-fired petrochemical tubular heaters. 2 Terms and definitions For the purposes of this document, the following terms and definitions apply. 2.1 thermal efficiency total heat absorbed divided by total heat input, or difference of total heat input minus total heat loss divided by total heat input 2.2 system object whose thermal efficiency is calculated by thermal balance The objects outside the boundary of the system are all referred to as the external environment 2.3 total heat absorbed sum of the used heat output from the system to the external environment 2.4 total heat input sum of heat from the external environment to the system 2.5 total heat loss sum of the unused parts of heat from the external environment to the system 2.6 lower heating value heat of reaction when the water vapor in the combustion products still exists in gaseous state after the fuel is completely burned, based on 15°C 2.7 sensible heat heat absorbed or released by a substance along change in temperature. Generally, it refers to the sensible heat under specified pressure 2.8 datum temperature reference temperature that measures the heat brought in or out by objects crossing the boundary of the system, entering the system, or leaving the system, under which, it is assumed that the enthalpy values of all objects are zero 3 Design and calculation of thermal efficiency 3.1 The thermal efficiency shall be calculated using Equations (1) and (2):
Contents of SH/T 3045-2003
Foreword i 1 Scope 2 Terms and definitions 3 Design and calculation of thermal efficiency Annex A (Informative) Design and calculation chart Explanation of wording in this standard
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Keywords:
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