CN203090729U - Desulfurization device convenient for automatic control - Google Patents

Desulfurization device convenient for automatic control Download PDF

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Publication number
CN203090729U
CN203090729U CN 201320115082 CN201320115082U CN203090729U CN 203090729 U CN203090729 U CN 203090729U CN 201320115082 CN201320115082 CN 201320115082 CN 201320115082 U CN201320115082 U CN 201320115082U CN 203090729 U CN203090729 U CN 203090729U
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CN
China
Prior art keywords
gas
pipeline
oxygen
control
desulfurizing tower
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.)
Expired - Fee Related
Application number
CN 201320115082
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Chinese (zh)
Inventor
党勇
甄玉科
王同彦
翟玉铎
陈庆
张满
卞新亮
李先涛
张述爽
魏东方
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jinan Iron and Steel Group Co Ltd
Original Assignee
Jinan Iron and Steel Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jinan Iron and Steel Group Co Ltd filed Critical Jinan Iron and Steel Group Co Ltd
Priority to CN 201320115082 priority Critical patent/CN203090729U/en
Application granted granted Critical
Publication of CN203090729U publication Critical patent/CN203090729U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a desulfurization device convenient for automatic control. The desulfurization device comprises a desulfurization tower, wherein a gas mixture pipeline is arranged at one side of the desulfurization tower; a first online laser oxygen meter is arranged on the gas mixture pipeline; an oxygen gas tube and a nitrogen gas tube are arranged at the outer side of the gas mixture pipeline by a tee joint, respectively; an adjusting valve and a stop valve are arranged in the oxygen gas tube and the nitrogen gas tube, respectively, and are used for mixing two pipeline gases before the two gases enter the desulfurization tower; the gas mixing proportion is controlled by controlling opening-closing degree of the two gas adjusting valves; a tail gas pipeline connected with the top of the desulfurization tower is communicated to a coal gas outlet pipeline by a tower-top absorption adjusting valve; a second online laser oxygen meter is arranged in the tail gas pipeline; meanwhile, an emergency blow-off valve branch is arranged. The desulfurization device convenient for automatic control can be used for realizing essentially safe coal gas desulfurization effect by utilizing the principle that the nitrogen gas does not participate in combustion, mixing the oxygen gas with nitrogen gas and utilizing the laser detecting technology to control the mixing proportion and the reaction concentration in a combined manner.

Description

A kind of desulfurizer of being convenient to automation control
Technical field
The utility model relates to a kind of sulfur removal technology of coke gas, especially the safety automation control technology in the desulfurization oxygenation program.
Background technology
At present, the known coke gas desulfurization difficult problem that is the coal gas process field.Particularly a large amount of waste gas in coal gas and compressed air reaction back directly discharges, and is the important environomental pollution source of coking process.Therefore, the part coal chemical industry enterprises has been taked the novel process of pure oxygen desulfurization in order to reduce the generating capacity of waste gas.This technological effect is good, and it is few to produce tail gas (waste gas) amount, and can directly incorporate gas piping into, and to the protection effect of environment, negative effect is little.But because the particularity of chemical enterprise, the conveying of pure oxygen, desulphurization reaction process etc. all exists great potential safety hazard, particularly pure oxygen and sulphur can produce chemical reaction, even spontaneous combustion or detonation, and unpredictable consequence takes place.
The utility model content
In order to overcome that pure oxygen enters behind the desulfurizing tower because too high oxygen level causes sulphur spontaneous combustion or ill effect more, the utility model provides a kind of automatic control technology of essential safety, this technology is not only carried out the automatic control of overall process to the pure oxygen desulfurization on principle, provide guarantee from the essential safety aspect simultaneously, on the basis that guarantees desulfurized effect, fundamentally solved the insecurity factor that the pure oxygen desulfurization is brought.
The technical scheme that its technical problem that solves the utility model adopts is:
A kind of desulfurizer of being convenient to automation control, comprise desulfurizing tower, coal gas enters from the bottom of desulfurizing tower then and discharges from the middle and upper part of desulfurizing tower, it is characterized in that, side at desulfurizing tower is provided with the mist pipeline, the first online laser oxygen analyser is set on the mist pipeline, and connect oxygen hose and nitrogen tube respectively by threeway in the outside of mist pipeline, and control valve and stop valve are set respectively in oxygen hose and nitrogen tube, being used for two kinds of gases, two pipeline gas before entering desulfurizing tower mixes, and by controlling the folding extent control gas mixture ratio example of two control valves, the exhaust pipe that is connected with the desulfurizing tower top is communicated on the coal gas discharge line by the cat head suction control valve, the second online laser oxygen analyser is set in exhaust pipe, simultaneously, emergency diffusion valve branch road is set in exhaust pipe.
All control valves, stop valve and online laser oxygen analyser move under the control of center control device.
The beneficial effects of the utility model are: the utility model utilizes nitrogen not participate in the principle of burning, and by nitrogen and oxygen mix, and in conjunction with utilizing laser measuring technology control mixed proportion and reaction density, realizes the coal gas desulfurization effect of Essential Safety.Need transform pipeline, when realizing the environmental protection desulfurization, the oxygen content of control conveying guarantees desulfurized effect safely, and the safety in the desulfurization production technology, and principle is simple, and control is reliable.Oxygen, nitrogen and tail gas automatic disconnecting device are set simultaneously, from the angle realization essential safety of apparatus body safety.
Description of drawings
Fig. 1 is a schematic diagram of the present utility model;
Among the figure: 1 from desulfurizing tower, 21 coal gas to be desulfurization, 22 coal gas discharge lines, 31 mist pipelines, 32 first online laser oxygen analysers, 33 oxygen hoses, 34 nitrogen tube, 41 exhaust pipes, 42 cat head suction control valves, 43 second online laser oxygen analysers, 44 emergency diffusion valves, A1 control valve, A2 stop valve.
The specific embodiment
As Fig. 1, a kind of desulfurizer of being convenient to automation control comprises desulfurizing tower 1, online laser oxygen analyser, by-pass valve control and associated conduit.
Desulfurizing tower is a prior art, adopts the pure oxygen sulfur removal technology to carry out desulfurization.
Coal gas 21 to be desulfurization enters desulfurizing tower and discharges from the middle and upper part of desulfurizing tower one side then from the bottom of desulfurizing tower 1, the sulfur-bearing composition in the inside of desulfurizing tower oxygen and coal gas reacts, and generates new material, and the consumption that directly translates into oxygen reduces.Side at desulfurizing tower 1 is provided with mist pipeline 31, the first online laser oxygen analyser 32 is set on the mist pipeline, and connect oxygen hose 33 and nitrogen tube 34 respectively by threeway in the outside of mist pipeline, and control valve A1 and stop valve A2 are set respectively in oxygen hose and nitrogen tube, comprise two respectively, wherein control valve A1 is used for two kinds of gases, two pipeline gas before entering desulfurizing tower and mixes, and by controlling the folding extent control gas mixture ratio example of two control valves, stop valve is used for the cut-out of oxygen pipeline in emergency circumstances, prevents from that oxygen content is too high to cause blast.An exhaust pipe 41 is set at the top of desulfurizing tower 1, the oxygen content that is used for auxiliary detection tail gas, and between exhaust pipe and coal gas discharge line, cat head suction control valve 42 is set, the exhaust pipe 41 that is connected with the desulfurizing tower top is communicated on the coal gas discharge line 22 by the cat head suction control valve, the second online laser oxygen analyser 43 is set in exhaust pipe, be used for detecting the content of tail gas oxygen, simultaneously, emergency diffusion valve 44 is set in exhaust pipe, forms an emergency diffusion branch road.
Below in conjunction with this device sulfur method and process are described in detail:
When going into operation, oxygen pipeline is in closed condition, at first open nitrogen pipeline, nitrogen will be full of in the desulfurizing tower, burn with the sulfur generation chemical reaction of avoiding producing in pure oxygen and the sweetening process, utilize the control valve in the oxygen pipeline to control then, slowly control the unlatching of oxygen, utilize the first online laser oxygen analyser to analyze the ratio of nitrogen and oxygen in the mist, and utilize the opening degree of regulating two control valves to implement control automatically, oxygen content in the control mist, make its purpose that meets stopping reaction, simultaneously, utilize the second online laser oxygen analyser on the exhaust pipe to detect contained oxygen composition in the tail gas, to judge desulfurized effect, it is generally acknowledged that oxygen content is that safety is suitable in the tail gas in scope.Because oxygen oxygen content controlled (can realize) in the mixing duct by the control valve folding degree of regulating oxygen channel, therefore, can guarantee that into the tower Control for Oxygen Content is in certain safe range, in case generation anomaly, the oxygen content that tail gas detects exceeds technology and allows maximum, to control the oxygen cutting valve, directly cut off oxygen, thereby guarantee the safety of system.Can regulate the desulfurizing tower internal pressure by diffusing valve simultaneously, can diffuse automatically, prevent blast in case reach dangerous values.
Embodiment recited above is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; under the prerequisite that does not break away from the utility model design spirit; this area person skilled all should expand as in the determined protection domain of the utility model claims various distortion of the present utility model and improvement.

Claims (2)

1. be convenient to the desulfurizer that automation is controlled for one kind, comprise desulfurizing tower, coal gas enters from the bottom of desulfurizing tower then and discharges from the middle and upper part of desulfurizing tower, it is characterized in that, side at desulfurizing tower is provided with the mist pipeline, the first online laser oxygen analyser is set on the mist pipeline, and connect oxygen hose and nitrogen tube respectively by threeway in the outside of mist pipeline, and control valve and stop valve are set respectively in oxygen hose and nitrogen tube, being used for two kinds of gases, two pipeline gas before entering desulfurizing tower mixes, and by controlling the folding extent control gas mixture ratio example of two control valves, the exhaust pipe that is connected with the desulfurizing tower top is communicated on the coal gas discharge line by the cat head suction control valve, the second online laser oxygen analyser is set in exhaust pipe, simultaneously, emergency diffusion valve branch road is set in exhaust pipe.
2. a kind of desulfurizer of being convenient to automation control according to claim 1 is characterized in that all control valves, stop valve and online laser oxygen analyser move under the control of center control device.
CN 201320115082 2013-03-14 2013-03-14 Desulfurization device convenient for automatic control Expired - Fee Related CN203090729U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320115082 CN203090729U (en) 2013-03-14 2013-03-14 Desulfurization device convenient for automatic control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320115082 CN203090729U (en) 2013-03-14 2013-03-14 Desulfurization device convenient for automatic control

Publications (1)

Publication Number Publication Date
CN203090729U true CN203090729U (en) 2013-07-31

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CN 201320115082 Expired - Fee Related CN203090729U (en) 2013-03-14 2013-03-14 Desulfurization device convenient for automatic control

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111169A (en) * 2013-03-14 2013-05-22 济钢集团有限公司 Gas desulfurization method and automatically controlled desulfurization device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111169A (en) * 2013-03-14 2013-05-22 济钢集团有限公司 Gas desulfurization method and automatically controlled desulfurization device

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130731

Termination date: 20170314