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JB/T 5910-1997 Electrostatic precipitator

Basic Information

Standard: JB/T 5910-1997

tandard name: Electrostatic precipitator

Standard category:Machinery Industry Standard (JB)

state:Abolished

release date:1997-04-15

Implementation date:1998-01-01

Expiration date:2005-09-01

standard classification number

Standard Classification Number:Machinery>>General Machinery and Equipment>>J88 Environmental Protection Equipment

associated standards

alternative situation:ZB J88001.2-1988 JB/T 5910-1991; replaced by JB/T 5910-2005

Publication information

other information

Introduction to standards:

Replaced by JB/T 5910-2005 JB/T 5910-1997 Electrostatic precipitator JB/T5910-1997 Standard download and decompression password: www.bzxz.net

Some standard content:

J88 | | tt | | JB | ||Ministry of Machinery Industry of the People's Republic of China
Published
Implemented on 1998-01-01
JB/T5910—1997
Foreword
This standard is for Revision of ZBJ88001.2-88 Electrostatic Precipitator Types and Basic Parameters and JB/T5910-.914 Electrostatic Precipitator Technical Conditions.
This standard will replace 2BJ88001.2-88 and JB/T5910-91 from the effective date. This standard was proposed and centralized by the Electrostatic Precipitator Sub-Technical Committee of the Environmental Protection Machinery Standardization Technical Committee of the Ministry of Machinery. The drafting unit of this standard: Jianjiang Feida Mechanical and Electrical Group Co., Ltd. The main drafter of this standard: Chen Jianguo.
This standard is entrusted to the Electrostatic Precipitator Sub-Technical Committee of the Environmental Protection Machinery Standardization Technical Committee of the Ministry of Machinery to be responsible for interpretation. 1 Scope
Machinery Industry Standard of the People's Republic of China
Electric Precipitator
JB/T5910-1997
Police Agent ZBJ88001.2-88
JB/ T 591091 | . This standard is applicable to the following ranges:
a) Flue gas treatment capacity %4.5×10°m/h (in standard state): b) Flue gas temperature ≤400C (>250C is high temperature type): c) Same-pole spacing 250~600mms
d) withstand allowable pressure -4.0×10*~0Pa (of which -1.0×10°~0Pa is the conventional type: -4.0×10*~1.010*Pa is the high-pressure type) :
e) The dust concentration of the inlet flue gas is ≤100g/m (under standard conditions). This standard does not apply to the treatment of flammable and explosive smoke (special treatment should be carried out for flammable and explosive smoke). When the designed working conditions exceed the applicable scope of this standard, the quality indicators should be specified in the product's technical documents (such as technical agreement).
2 Referenced Standards
The provisions contained in the following standards constitute provisions of this standard through reference in this standard. At the time of publication, the editions indicated were valid. All international standards are subject to revision. Parties using this standard should explore the possibility of using the following minor revisions of the standard. GB 10880-89
GB/T 1393192
JB/T 59061997
IB 5908-91
JB/T 5913-1997
JB6407-91
JB/T85361997
ZB K46 008. 188
3 structure
Electrostatic precipitator air leakage tightness test method
Electrostatic precipitator performance test method|| tt||Electrostatic precipitator anode plate
Sampling inspection of main parts of electrostatic precipitator and packaging, transportation, storage specifications electrostatic precipitator electrode line
Electrostatic precipitator debugging, operation, accurate repair, safety Technical Specifications Technical Conditions for Mechanical Installation of Electrostatic Precipitator
Rectifier Equipment for High-voltage Electrostatic Precipitator
3.1 The electrostatic precipitator is composed of mechanical and electrical parts. The mechanical part consists of anode system (including anode operating device), cathode system (including cathode vibration device), shell structural parts, air flow distribution device and other components. The electrical part consists of high-voltage power supply (including rectifier transformer and its control system), It is composed of high-voltage isolation and shutdown and low-voltage control systems. 3.2 The anode plate of the electrostatic precipitator should comply with the requirements of JB/T5906. 3.3 The cathode wire of the electrostatic precipitator should comply with the requirements of JB/T5913. 3.4 The high-voltage DC power supply of the electrostatic precipitator should comply with the requirements of ZBK46008.1. 3.5 Large-scale thermal power generation units are equipped with electrostatic precipitators and electrostatic precipitators for metallurgical cement that meet special requirements. According to needs, the wear-out control machinery industry department approved on 1997-04-15
Implemented on 1998-01.01||tt ||1
system and intelligent management system,
4 code notation
NXL
K×B-
JB/T5910-1997| |tt||H
Effective height of anode plate, m
Effective width of single electric field, m
Number of wide chambers
Effective length of single electric field, m)|| tt||Electric field number
Use code (expressed by the first letter of Wenyu pinyin, such as "D\" for thermal power, \S\ for sintering, etc.) For example: D3×4-1×10.4-10.0 It is a plate type. Electrostatic precipitator for dry thermal power plants. The number of electric fields is 3. The effective length of a single electric field is 4m. The effective width of a single electric field is 10.4m. The effective height of the anode plate is 10m. Basic parameters
5.
5.1 The flue gas circulation area of ??the single-chamber electrostatic precipitator is calculated according to formula (1): S-HB
1
where S-
a single-chamber electrostatic precipitator Flue gas circulation area.m: H——effective height of anode plate.m;
B--effective width of electric field in single chamber.m
5.2 The total dust collection area is calculated according to formula (2):
In the formula: A - total dust collection area.m
N electric field number:
L——effective length of single electric field m;
H
Effective height of anode plate, m:
Effective width of electric field in a single chamber, m:
B-
-Number of chambers:
d
Same pole Spacing, mm.
42000NLHBK
d
An electric field can be divided into one or more power supply zones. A high-voltage power supply generally supplies power to one power supply zone, :5.3||tt| |5.4 The rated output voltage and rated output current level of the high-voltage power supply are selected according to the values ??specified in 2.2 of ZBK46008.1-88, 6
Technical requirements
6.1 Dust removal efficiency
6.1.1 The dust emission concentration must comply with the relevant national standards, and its guaranteed efficiency shall be specified in the technical agreement between the supplier and the buyer. 2
JB/T5910-1997
6.1.2 Dust Removal. For the correction and evaluation of efficiency, see Appendix A (standard appendix), 6.2 Pressure drop
Determined according to the working conditions, the pressure drop of the electrostatic precipitator body is not greater than 250Pa6.3 Air leakage rate
Electrostatic precipitator The air leakage rate of the main body is not greater than 5%. The test method wwW.bzxz.Net
The dust removal efficiency and main body pressure drop of the electrostatic precipitator are determined according to the provisions of GB/T13931. The air regulation rate is measured according to the provisions of GB10880. Inspection rules
8.
Inspection is in accordance with JB5908.
9
Packaging, transportation and storage specifications
Packaging, transportation and storage are in accordance with the provisions of JB5908. Installation specifications
10
Installation is in accordance with JB/T8536.
11 Technical specifications for debugging, operation, maintenance and safety of electrostatic precipitator. According to the provisions of JB6407, there are two ways to correct the dust removal efficiency.
JB/T5910-1997
Appendix A
(standard appendix)
Correction method and evaluation of dust removal efficiency
The first method: The actual efficiency during the assessment is corrected from the working conditions to the design conditions, and the evaluation is made under the design conditions = (1-e) × 100%
Ke Kic.
K二ln(||tt| |100
100
C=C |C, C, C,.~ are the correction coefficients of flue gas volume, gas humidity, vegetable content, etc. If additional tests are required, it indicates that the dust collector efficiency assessment has passed. The second method is the guaranteed efficiency under the design conditions. : Correct the guaranteed efficiency from the design conditions to the working conditions, and evaluate it under the working conditions %=(1-)×100
KKrC
Kg=ln1%
100. | |tt |regardless of whether or not it has been corrected for efficiency
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