CN107763436A - A kind of coking desulfurization regenerator exhaust treatment system pipeline - Google Patents
A kind of coking desulfurization regenerator exhaust treatment system pipeline Download PDFInfo
- Publication number
- CN107763436A CN107763436A CN201711243606.8A CN201711243606A CN107763436A CN 107763436 A CN107763436 A CN 107763436A CN 201711243606 A CN201711243606 A CN 201711243606A CN 107763436 A CN107763436 A CN 107763436A
- Authority
- CN
- China
- Prior art keywords
- gas
- regenerator
- air blower
- gas piping
- connecting pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000004939 coking Methods 0.000 title claims abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 9
- 230000023556 desulfurization Effects 0.000 title claims abstract description 9
- 239000007789 gas Substances 0.000 claims abstract description 65
- 238000007664 blowing Methods 0.000 claims abstract description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000001301 oxygen Substances 0.000 claims abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 8
- 239000003245 coal Substances 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 230000003647 oxidation Effects 0.000 abstract description 3
- 238000007254 oxidation reaction Methods 0.000 abstract description 3
- 239000000571 coke Substances 0.000 abstract description 2
- 238000010276 construction Methods 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000012855 volatile organic compound Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/02—Pipe-line systems for gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1425—Regeneration of liquid absorbents
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/12—Arrangements for supervising or controlling working operations for injecting a composition into the line
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A kind of coking desulfurization regenerator exhaust treatment system pipeline, belongs to tail gas disposal technique field.Including regenerator, diffuse channel, the first rapidly opened and closed valve, connecting pipe, the second rapidly opened and closed valve, gas-blowing engine, oxygen conten analyser, gas piping after gas piping, air blower before air blower.The regenerator tail gas of discharge at the top of regenerator, gas piping before air blower is entered by connecting pipe, after mix with the coke-stove gas introduced by gas piping, by gas-blowing engine pressurization into gas piping after air blower.Advantage is, regenerator tail gas is passed through into coke oven gas pipe before connecting pipe introducing air blower, together handled with coke-stove gas, air is not discharged, thoroughly solve the atmosphere polluting problem of tail gas at the top of coal chemical enterprise Wet-type oxidation sweetening technique regenerator, have that simple in construction, easy to use, environmental benefit is good.
Description
Technical field
The invention belongs to tail gas disposal technique field, has been provided in particular in a kind of coking desulfurization regenerator exhaust treatment system
Pipeline.
Background technology
Domestic many coal chemical enterprises use Wet-type oxidation sweetening technique at present, and the regeneration supporting with it uses regenerator work
Skill, reduced investment is characterized in, regeneration efficiency is high, and tail gas is directly discharged into air by way of high altitude discharge at the top of its regenerator.
But the tail gas amount of this regenerator is larger, the impurity component in tail gas is more complicated (mainly containing NH3、H2S, VOCs etc.), its content
Also higher, intractability is larger.There is part coal chemical enterprise to absorb the NH in tail gas respectively using the method for multistage absorption3、H2S、
After the pollutant components such as VOCs, by the processing method of exhaust emissions air, but, operating cost uneven in the prevalence of absorption efficiency
Height, the problems such as execute-in-place complexity.And it is increasingly strict with national environmental protection regulation, the requirement to pollutant emission limit is also got over
Come higher, this just proposes higher requirement for the processing of regenerator tail gas.
The content of the invention
Object of the present invention is to provide a kind of coking desulfurization regenerator exhaust treatment system pipeline, solve and generally deposit
Uneven in absorption efficiency, operating cost is high, the problems such as execute-in-place complexity;By gas pipe before regenerator tail gas introducing air blower
Coke-stove gas in road, with pipeline is together handled, and is accomplished that regenerator tail gas is not completely outer and is arranged.
The present invention includes regenerator 1, diffuse channel 2, the first rapidly opened and closed valve 3, connecting pipe 4, the second rapidly opened and closed valve
5th, gas-blowing engine 6, oxygen conten analyser 7, gas piping 9 after gas piping 8, air blower before air blower.Regenerator 1 passes through company
Thread a pipe and 4 connected with gas piping before air blower 8, diffuse channel 2 connects with connecting pipe 4, and gas-blowing engine 6 connects air blower
Preceding gas piping 8 and gas piping 9 after air blower;First rapidly opened and closed valve 3 is arranged on diffuse channel 2, and second is rapidly opened and closed
Valve 5 is arranged on connecting pipe 4, and oxygen conten analyser 7 is connected with gas piping after air blower 9.The discharge of the top of regenerator 1 is again
Raw tower tail gas, by connecting pipe 4 into gas piping 8 before air blower, is mixed with the coke-stove gas introduced by gas piping 8
Afterwards, the gas piping 9 after the pressurization of gas-blowing engine 6 enters air blower.
Connecting pipe 4 is provided with tracing thermal-insulating, and its heat tracing form is steam tracing or electric tracing.
The invention provides a kind of coking desulfurization regenerator exhaust treatment system pipeline, and regenerator tail gas is introduced into air blower
Preceding coke oven gas pipe, together handled with coke-stove gas, air is not discharged, thoroughly solve coal chemical enterprise Wet-type oxidation sweetening
Pollution problem of the tail gas to air, has the advantages that simple in construction, easy to use, environmental benefit is good at the top of technique regenerator.
Brief description of the drawings
Fig. 1 is coking desulfurization regenerator exhaust treatment system pipeline configuration schematic diagram.Wherein:Regenerator 1, diffuse channel 2,
First rapidly opened and closed valve 3, connecting pipe 4, the second rapidly opened and closed valve 5, gas-blowing engine 6, oxygen conten analyser 7, before air blower
Gas piping 9 after gas piping 8, air blower.
Embodiment
The present invention includes regenerator 1, diffuse channel 2, the first rapidly opened and closed valve 3, connecting pipe 4, the second rapidly opened and closed valve
5th, gas-blowing engine 6, oxygen conten analyser 7, gas piping 9 after gas piping 8, air blower before air blower.Regenerator 1 passes through company
Thread a pipe and 4 connected with gas piping before air blower 8, diffuse channel 2 connects with connecting pipe 4, and gas-blowing engine 6 connects air blower
Preceding gas piping 8 and gas piping 9 after air blower;First rapidly opened and closed valve 3 is arranged on diffuse channel 2, and second is rapidly opened and closed
Valve 5 is arranged on connecting pipe 4, and oxygen conten analyser 7 is connected with gas piping after air blower 9.The discharge of the top of regenerator 1 is again
Raw tower tail gas, by connecting pipe 4 into gas piping 8 before air blower, is mixed with the coke-stove gas introduced by gas piping 8
Afterwards, the gas piping 9 after the pressurization of gas-blowing engine 6 enters air blower.
Connecting pipe 4 is provided with tracing thermal-insulating, and its heat tracing form is steam tracing or electric tracing.
As shown in figure 1, the regenerator tail gas of the top of regenerator 1 discharge, passes through gas pipe before the entrance air blower of connecting pipe 4
Road 8, after being mixed with the coke-stove gas introduced by gas piping 8, the gas piping after the pressurization of gas-blowing engine 6 enters air blower
9。
Claims (2)
1. a kind of coking desulfurization regenerator exhaust treatment system pipeline, it is characterised in that including regenerator (1), diffuse channel
(2), the first rapidly opened and closed valve (3), connecting pipe (4), the second rapidly opened and closed valve (5), gas-blowing engine (6), oxygen analysis
Instrument (7), gas piping (9) after gas piping (8), air blower before air blower;Regenerator (1) passes through connecting pipe (4) and air blast
Gas piping (8) connects before machine, and diffuse channel (2) connects with connecting pipe (4), coal before gas-blowing engine (6) connection air blower
Feed channel (8) and gas piping (9) after air blower;First rapidly opened and closed valve (3) is arranged on diffuse channel (2), and second is quick
Open and close valve (5) is arranged on connecting pipe (4), and oxygen conten analyser (7) is connected with gas piping after air blower (9);Regenerator
(1) the regenerator tail gas of top discharge, gas piping (8) before air blower is entered by connecting pipe (4), and by gas piping
(8) after the coke-stove gas mixing introduced, the gas piping (9) after gas-blowing engine (6) pressurization enters air blower.
A kind of 2. coking desulfurization regenerator exhaust treatment system pipeline according to claim 1, it is characterised in that:Communicating pipe
Road (4) is provided with tracing thermal-insulating, and its heat tracing form is steam tracing or electric tracing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711243606.8A CN107763436A (en) | 2017-11-30 | 2017-11-30 | A kind of coking desulfurization regenerator exhaust treatment system pipeline |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711243606.8A CN107763436A (en) | 2017-11-30 | 2017-11-30 | A kind of coking desulfurization regenerator exhaust treatment system pipeline |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107763436A true CN107763436A (en) | 2018-03-06 |
Family
ID=61277200
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711243606.8A Pending CN107763436A (en) | 2017-11-30 | 2017-11-30 | A kind of coking desulfurization regenerator exhaust treatment system pipeline |
Country Status (1)
Country | Link |
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CN (1) | CN107763436A (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980042981U (en) * | 1996-12-24 | 1998-09-25 | 김종진 | Deoiler for refining coke oven gas with improved sulfur dissolution rate |
CN1807558A (en) * | 2006-01-26 | 2006-07-26 | 济南钢铁股份有限公司 | Coke-oven gas desulfurization process |
CN201807283U (en) * | 2010-09-13 | 2011-04-27 | 太原煤气化股份有限公司焦化厂 | Treatment device for sodium salt-containing desulfuration waste liquid in coking industry |
CN102381688A (en) * | 2011-09-06 | 2012-03-21 | 武汉科技大学 | Concentrated sulfuric acid preparation method using hydrogen sulfide in manufactured gas |
CN202187023U (en) * | 2011-06-30 | 2012-04-11 | 首钢总公司 | Recycling device for converter coal gas diffused in steelmaking |
CN103343022A (en) * | 2013-07-26 | 2013-10-09 | 济南冶金化工设备有限公司 | Negative-pressure desulfurization technology and equipment for coke gas |
CN105505480A (en) * | 2015-12-23 | 2016-04-20 | 四川中航超高分子量管业有限公司 | Desulfurization purification system applicable to coke oven gas |
-
2017
- 2017-11-30 CN CN201711243606.8A patent/CN107763436A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980042981U (en) * | 1996-12-24 | 1998-09-25 | 김종진 | Deoiler for refining coke oven gas with improved sulfur dissolution rate |
CN1807558A (en) * | 2006-01-26 | 2006-07-26 | 济南钢铁股份有限公司 | Coke-oven gas desulfurization process |
CN201807283U (en) * | 2010-09-13 | 2011-04-27 | 太原煤气化股份有限公司焦化厂 | Treatment device for sodium salt-containing desulfuration waste liquid in coking industry |
CN202187023U (en) * | 2011-06-30 | 2012-04-11 | 首钢总公司 | Recycling device for converter coal gas diffused in steelmaking |
CN102381688A (en) * | 2011-09-06 | 2012-03-21 | 武汉科技大学 | Concentrated sulfuric acid preparation method using hydrogen sulfide in manufactured gas |
CN103343022A (en) * | 2013-07-26 | 2013-10-09 | 济南冶金化工设备有限公司 | Negative-pressure desulfurization technology and equipment for coke gas |
CN105505480A (en) * | 2015-12-23 | 2016-04-20 | 四川中航超高分子量管业有限公司 | Desulfurization purification system applicable to coke oven gas |
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Application publication date: 20180306 |