CN104226101A - Slurry circulation process based on SDA process desulfurization system - Google Patents

Slurry circulation process based on SDA process desulfurization system Download PDF

Info

Publication number
CN104226101A
CN104226101A CN201410459139.2A CN201410459139A CN104226101A CN 104226101 A CN104226101 A CN 104226101A CN 201410459139 A CN201410459139 A CN 201410459139A CN 104226101 A CN104226101 A CN 104226101A
Authority
CN
China
Prior art keywords
slurry
slurries
desulphurization
tank
circulation
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
Application number
CN201410459139.2A
Other languages
Chinese (zh)
Inventor
张庆文
周航
常治铁
刘莉
李腾渊
刘立刚
孙凤军
李修梅
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.)
Ansteel Engineering Technology Corp Ltd
Original Assignee
Ansteel Engineering Technology Corp 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 Ansteel Engineering Technology Corp Ltd filed Critical Ansteel Engineering Technology Corp Ltd
Priority to CN201410459139.2A priority Critical patent/CN104226101A/en
Publication of CN104226101A publication Critical patent/CN104226101A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The invention relates to a slurry circulation process based on an SDA (Spray Drying Absorption) process desulfurization system. The slurry circulation process comprises the steps that (1) desulfurized fly ash of a desulfurization tower enters an accident pool, is mixed and stirred together with digestive water to prepare circulation slurry, the circulation slurry enters a slurry top tank after being filtered, and finally the filtered circulation slurry enters an atomizer to participate in desulfurization reaction; (2) when the desulfurization system fails or is maintained, slurry which overflows from or is discharged from the top tank, a digestion tank and a slurry tank is discharged into the accident pool; and (3) when the desulfurization system recovers to normally work, the slurry is re-circulated. Compared with the prior art, the slurry circulation process has the beneficial effects that (1) the desulfurized fly ash directly enters the accident pool, a dust producing point caused by fly ash discharging and transporting of the desulfurized tower is eliminated, and the environment quality of a desulfurization island is effectively improved; (2) the accident pool in an original desulfurization system is combined with a mixing tank and a circulation slurry tank in a circulation slurry system into a whole, the functions of the accident pool, the mixing tank and the circulation slurry tank are integrated, the quantity of equipment and the occupation area are reduced, and the input cost is lowered; (3) the process route is shortened, the structure is simple, and the operation and the maintenance are convenient.

Description

A kind of loop slurry technique based on SDA method desulphurization system
Technical field
The present invention relates to SDA method technical field of desulfurization, particularly relate to a kind of loop slurry technique based on SDA method desulphurization system.
Background technology
For controlling sulfur dioxide and Acid Rain Pollution, country increases the management of sintering gas flue gas sulfuric dioxide, requires must carry out desulfurization to sinter fume, weakens the impact of sulfur dioxide on ecological environment to the full extent.
Ansteel Engineering Technology Corporation Limited based on rotary spraying and drying technology, Self-Integration SDA sintering flue gas desulfurization technology, and took the lead in being applied to Anshan iron and steel plant and Sha Gang in 2009.On this basis by summing up and improving; this technology is become better and approaching perfection day by day; now one of primary solutions becoming flue gas of sintering machine; in " steel industry prevention and cure of pollution best practicable technology directive/guide---sintering and the pelletizing process " issued by national environmental protection portion, SDA method is recommended as one of flue gas of sintering machine optimum process technology method to enterprise.
For improving the utilization rate of desulfurizing agent, reduce the generation of desulfurizing byproduct, embody circular economy concept, current SDA sulfur removal technology adopts circulation technology mostly, partial desulfurization ash enters loop slurry preparation system, namely Desulphurization enters blending tank and makes loop slurry, and loop slurry enters recycle slurry flow container, top tank successively, finally enters atomizer and participates in desulphurization reaction.
Except loop slurry system, SDA technique need establish accident set pond, collecting-tank is entered by pushing up overflow and emptying slurries in tank, digester, serum pot when accident condition and overhaul of the equipments, by Pulp pump, slurries are promoted to vibratory sieve after recovering normal operation, continue to utilize, thus avoid slurries to arrange, and reduce desulfurizing agent waste outward.(as shown in Figure 1)
Summary of the invention
The invention provides a kind of loop slurry technique based on SDA method desulphurization system, include the emergency pool in desulphurization system in loop slurry system, the Desulphurization that desulfurizing tower produces directly enters emergency pool and makes loop slurry and uses, not only reduce equipment quantity and floor space, shorten process route, reduce input cost, also eliminate one simultaneously and produce dirt pits.
In order to achieve the above object, the present invention realizes by the following technical solutions:
Based on a loop slurry technique for SDA method desulphurization system, the emergency pool of desulphurization system is double does blending tank in serum recycle system and recycle slurry flow container, comprises the steps:
1) Desulphurization unloaded from desulfurizing tower ash bucket enters emergency pool by Desulphurization receiving opening, with digest the digestion water that water pipe transports from technique and mix, loop slurry is made under the abundant stirring action of mixer, be transported on vibratory sieve by Pulp pump, enter slurries top tank after filtration, finally enter atomizer and participate in desulphurization reaction;
2) when desulphurization system breaks down or be in inspecting state, overflow and emptying slurries in the tank of top, enter emergency pool by slurry feed pipe, starts mixer simultaneously and avoid slurries to deposit;
3) when desulphurization system is recovered normally to work, by Pulp pump, the slurries in emergency pool are delivered on vibratory sieve by slurries feed back pipe, re-start circulation.
Described desulfurizing tower is rotary spraying and drying absorption tower.
Slurries amount in described emergency pool is shown by liquid level gauge, and is regulated by control system control grout control valve.
Described technique digestion water pipe is provided with the flowmeter, flow control valve and the flow stop valve that are connected with control system, regulates pushing quantity according to Desulphurization discharge quantity.
Described Pulp pump adopts a-worker-a-backup, and the slurries feed back pipe after Pulp pump is provided with residual cake valve.
For realizing a kind of device of the loop slurry technique based on SDA method desulphurization system, comprise the emergency pool, Pulp pump and the vibratory sieve that are connected successively by slurries feed back pipe, the other Joining Technology digestion water pipe of described emergency pool and slurry feed pipe, the other end of slurry feed pipe connects overfall and the evacuation port of slurries top tank, digester and serum pot, and the Desulphurization receiving opening at emergency pool top connects desulfurizing tower cinder-discharging port by pipeline.
Compared with prior art, the invention has the beneficial effects as follows:
1) Desulphurization directly enters emergency pool by pipeline, eliminates " desulfurizing tower unloads ash and transport " this product dirt pits, effectively improves desulfurization island and environmental quality around;
2) emergency pool in former desulphurization system and the blending tank in loop slurry system, recycle slurry flow container are integrated, and have the function of three concurrently, decrease equipment quantity and floor space, reduce input cost;
3) shorten process route, and structure is simple, operation maintenance is convenient.
Accompanying drawing explanation
Fig. 1 is serum recycle system process figure conventional at present.
Fig. 2 is process chart of the present invention.
In figure: 1. emergency pool 2. mixer 3. slurry feed pipe 4. slurries feed back pipe 5. Pulp pump 6. residual cake valve 7. vibratory sieve 8. technique digestion water pipe 9. flow stop valve 10. flowmeter 11. flow control valve 12. Desulphurization receiving opening
Detailed description of the invention
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described further:
Seeing Fig. 2, is process chart of the present invention, a kind of loop slurry technique based on SDA method desulphurization system of the present invention, and the emergency pool 1 of desulphurization system is double does blending tank in serum recycle system and recycle slurry flow container, comprises the steps:
1) Desulphurization unloaded from desulfurizing tower ash bucket enters emergency pool 1 by Desulphurization receiving opening 12, with digest the digestion water that water pipe 8 transports from technique and mix, loop slurry is made under the abundant stirring action of mixer 2, be transported on vibratory sieve 7 by Pulp pump 5, enter slurries top tank after filtration, finally enter atomizer and participate in desulphurization reaction;
2) when desulphurization system breaks down or be in inspecting state, overflow and emptying slurries in the tank of top, enter emergency pool 1 by slurry feed pipe 3, starts mixer 2 simultaneously and avoid slurries to deposit;
3) when desulphurization system is recovered normally to work, by Pulp pump 5, the slurries in emergency pool 1 are delivered on vibratory sieve 7 by slurries feed back pipe 4, re-start circulation.
Described desulfurizing tower is rotary spraying and drying absorption tower.
Slurries amount in described emergency pool 1 is shown by liquid level gauge, and is regulated by control system control grout control valve.
On described technique digestion water pipe, 8 are provided with the flowmeter 10, flow control valve 11 and the flow stop valve 9 that are connected with control system, regulate pushing quantity according to Desulphurization discharge quantity.
Described Pulp pump 5 adopts a-worker-a-backup, and the slurries feed back pipe 4 after Pulp pump 5 is provided with residual cake valve 6.
For realizing a kind of device of the loop slurry technique based on SDA method desulphurization system, comprise the emergency pool 1, Pulp pump 5 and the vibratory sieve 7 that are connected successively by slurries feed back pipe 4, described emergency pool 1 is Joining Technology digestion water pipe 8 and slurry feed pipe 3 in addition, the other end of slurry feed pipe 3 connects overfall and the evacuation port of slurries top tank, digester and serum pot, and the Desulphurization receiving opening 12 at emergency pool 1 top connects desulfurizing tower cinder-discharging port by pipeline.
Technique digestion water pipe 8 arranges flowmeter 10 and technique digestion Water flow adjusting valve 11, technique digestion discharge stop valve 9, is to reach flexible modulation loop slurry concentration object, regulating according to Desulphurization discharge quantity to fresh water (FW) pushing quantity.
In emergency pool 1, liquid level gauge is installed, the liquid level of loop slurry in emergency pool 1 can be shown, and control the object of slurries amount in Desulphurization discharge quantity and technique digestion water yield realization control emergency pool 1 by control system.
Be provided with mixer 2 in emergency pool 1, ensure that the slurry agitation in pond is even, avoid alluvial.
Pulp pump 5 adopts a-worker-a-backup to design, and under guaranteeing that accident conditions appear in a Pulp pump 5, another Pulp pump 5 can complete function loop slurry being promoted to vibratory sieve 7.Be provided with residual cake valve 6 after Pulp pump 5, to facilitate the impurity got rid of in slurries, prevent silting.
The Desulphurization charging aperture 12 at emergency pool 1 top, is closely connected with desulfurizing tower ash-discharging device by pipeline, ensures that Desulphurization directly enters emergency pool 1, avoids dust to produce.Present invention eliminates the ash conveying device under desulfurizing tower in former desulphurization system, not only reduce investment outlay, and decrease a product dirt pits, effectively improve desulfurization island and environment around.

Claims (6)

1., based on a loop slurry technique for SDA method desulphurization system, the emergency pool of desulphurization system is double does blending tank in serum recycle system and recycle slurry flow container, it is characterized in that, comprises the steps:
1) Desulphurization unloaded from desulfurizing tower ash bucket enters emergency pool by Desulphurization receiving opening, with digest the digestion water that water pipe transports from technique and mix, loop slurry is made under the abundant stirring action of mixer, be transported on vibratory sieve by Pulp pump, enter slurries top tank after filtration, finally enter atomizer and participate in desulphurization reaction;
2) when desulphurization system breaks down or be in inspecting state, overflow and emptying slurries in the tank of top, enter emergency pool by slurry feed pipe, starts mixer simultaneously and avoid slurries to deposit;
3) when desulphurization system is recovered normally to work, by Pulp pump, the slurries in emergency pool are delivered on vibratory sieve by slurries feed back pipe, re-start circulation.
2. a kind of loop slurry technique based on SDA method desulphurization system according to claim 1, it is characterized in that, described desulfurizing tower is rotary spraying and drying absorption tower.
3. a kind of loop slurry technique based on SDA method desulphurization system according to claim 1, it is characterized in that, the slurries amount in described emergency pool is shown by liquid level gauge, and is regulated by control system control grout control valve.
4. a kind of loop slurry technique based on SDA method desulphurization system according to claim 1, it is characterized in that, described technique digestion water pipe is provided with the flowmeter, flow control valve and the flow stop valve that are connected with control system, regulates pushing quantity according to Desulphurization discharge quantity.
5. a kind of loop slurry technique based on SDA method desulphurization system according to claim 1, is characterized in that, described Pulp pump adopts a-worker-a-backup, and the slurries feed back pipe after Pulp pump is provided with residual cake valve.
6. for realizing the device of a kind of loop slurry technique based on SDA method desulphurization system according to claim 1, it is characterized in that, comprise the emergency pool, Pulp pump and the vibratory sieve that are connected successively by slurries feed back pipe, the other Joining Technology digestion water pipe of described emergency pool and slurry feed pipe, the other end of slurry feed pipe connects overfall and the evacuation port of slurries top tank, digester and serum pot, and the Desulphurization receiving opening at emergency pool top connects desulfurizing tower cinder-discharging port by pipeline.
CN201410459139.2A 2014-09-10 2014-09-10 Slurry circulation process based on SDA process desulfurization system Pending CN104226101A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410459139.2A CN104226101A (en) 2014-09-10 2014-09-10 Slurry circulation process based on SDA process desulfurization system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410459139.2A CN104226101A (en) 2014-09-10 2014-09-10 Slurry circulation process based on SDA process desulfurization system

Publications (1)

Publication Number Publication Date
CN104226101A true CN104226101A (en) 2014-12-24

Family

ID=52215533

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410459139.2A Pending CN104226101A (en) 2014-09-10 2014-09-10 Slurry circulation process based on SDA process desulfurization system

Country Status (1)

Country Link
CN (1) CN104226101A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709586A (en) * 2016-04-13 2016-06-29 中冶焦耐工程技术有限公司 Solution preparation and supplying method and device for coking furnace flue gas desulfurization system
CN106110867A (en) * 2016-08-12 2016-11-16 攀枝花市九鼎智远知识产权运营有限公司 A kind of heat-engine plant desulfurized fuming device
CN115156240A (en) * 2022-07-22 2022-10-11 广东同创科鑫环保有限公司 Method for resource utilization of desulfurized fly ash

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101468289A (en) * 2007-12-24 2009-07-01 同方环境股份有限公司 Desulfurizer suitable for sulfuric dioxide of large-scope change and control method thereof
CN102266716A (en) * 2011-07-04 2011-12-07 中电投远达环保工程有限公司 Simplified flue gas desulfurization device
CN202143816U (en) * 2011-07-04 2012-02-15 中电投远达环保工程有限公司 Accident discharge system of flue gas desulfurization device
CN102380308A (en) * 2010-09-03 2012-03-21 鞍钢集团工程技术有限公司 Sintering flue gas desulfurization and purification method and equipment
CN202289800U (en) * 2011-10-28 2012-07-04 鞍钢集团工程技术有限公司 Novel emergency pool for sintering flue gas desulfurization systems
CN202369507U (en) * 2011-11-03 2012-08-08 鞍钢集团工程技术有限公司 Sintering flue gas desulfurization digestion tank
CN204134471U (en) * 2014-09-10 2015-02-04 鞍钢集团工程技术有限公司 A kind of slurry circulation device based on SDA method desulphurization system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101468289A (en) * 2007-12-24 2009-07-01 同方环境股份有限公司 Desulfurizer suitable for sulfuric dioxide of large-scope change and control method thereof
CN102380308A (en) * 2010-09-03 2012-03-21 鞍钢集团工程技术有限公司 Sintering flue gas desulfurization and purification method and equipment
CN102266716A (en) * 2011-07-04 2011-12-07 中电投远达环保工程有限公司 Simplified flue gas desulfurization device
CN202143816U (en) * 2011-07-04 2012-02-15 中电投远达环保工程有限公司 Accident discharge system of flue gas desulfurization device
CN202289800U (en) * 2011-10-28 2012-07-04 鞍钢集团工程技术有限公司 Novel emergency pool for sintering flue gas desulfurization systems
CN202369507U (en) * 2011-11-03 2012-08-08 鞍钢集团工程技术有限公司 Sintering flue gas desulfurization digestion tank
CN204134471U (en) * 2014-09-10 2015-02-04 鞍钢集团工程技术有限公司 A kind of slurry circulation device based on SDA method desulphurization system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
顾兵等: "SDA脱硫工艺在烧结烟气脱硫中的应用", 《环境工程》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709586A (en) * 2016-04-13 2016-06-29 中冶焦耐工程技术有限公司 Solution preparation and supplying method and device for coking furnace flue gas desulfurization system
CN105709586B (en) * 2016-04-13 2018-10-26 中冶焦耐(大连)工程技术有限公司 A kind of flue gases of cock oven desulphurization system matches liquid, feed liquid method and device
CN106110867A (en) * 2016-08-12 2016-11-16 攀枝花市九鼎智远知识产权运营有限公司 A kind of heat-engine plant desulfurized fuming device
CN115156240A (en) * 2022-07-22 2022-10-11 广东同创科鑫环保有限公司 Method for resource utilization of desulfurized fly ash

Similar Documents

Publication Publication Date Title
CN102389705B (en) Zinc oxide desulphurization system
CN101723604A (en) Continuous preparation system for lime slurry having fixed concentration
CN204134471U (en) A kind of slurry circulation device based on SDA method desulphurization system
CN104226101A (en) Slurry circulation process based on SDA process desulfurization system
CN102423622A (en) Zinc oxide desulfuration technology
CN103418303B (en) Device and method for stably adding sludge in sintering
CN204447715U (en) Magnesium oxide method desulphurization system
CN102512938B (en) Limestone pulping and long-distance conveying device and using method thereof
CN204134458U (en) A kind of emergency pool that doublely can do loop slurry system blending tank and recycle slurry flow container
CN211688622U (en) Commercial concrete mixing plant transportation tank car washs and station sewage purification system
CN204800850U (en) Novel dry -mixed mortar jar
CN207628572U (en) Sandstone detaches and waste water recovery system
CN203512422U (en) Sintering flue gas desulfurized fly ash bin
CN209934147U (en) Gypsum slurry concentration and separation system
CN108744943A (en) A kind of desulphurization plant and its sulfur removal technology
CN204447716U (en) Limestone-based process desulphurization system
CN201643976U (en) Double-loop vertical jet wet-method desulfurization device used for preparing desulfurizing agent by utilizing carbide slag
CN202590609U (en) Slurry preparation device for limestone-gypsum wet desulphurization
CN111054207B (en) Carbide slag-gypsum flue gas desulfurization device and method applied to multi-pipe water bed
CN208717125U (en) A kind of high-efficiency oxy-hydrogen nickel filter cake discharging and pulp clean integrated apparatus
CN107012319A (en) One kind is used to sinter digestion steel-smelting sewage sludge system and method
CN202289862U (en) Zinc oxide desulfurization system
CN203944288U (en) A kind of tower outer circulation adds independent oxidation lime-gypsum method desulfurizer
CN204911217U (en) Papermaking desulfurization system
CN103937916B (en) Slag granulating system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20141224