CN101033060A - Sulfur prepared by coal gas wet-type oxidation sweetening process and device for preparing sulfuric acid from waste liquor - Google Patents
Sulfur prepared by coal gas wet-type oxidation sweetening process and device for preparing sulfuric acid from waste liquor Download PDFInfo
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- CN101033060A CN101033060A CNA2007100109697A CN200710010969A CN101033060A CN 101033060 A CN101033060 A CN 101033060A CN A2007100109697 A CNA2007100109697 A CN A2007100109697A CN 200710010969 A CN200710010969 A CN 200710010969A CN 101033060 A CN101033060 A CN 101033060A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract
This invention relates to equipment preparing H2SO4 with sulfur and its liquid waste grown by a gas humid oxidation and desulfurization technology including an incinerator, a heat waste recovery boiler, a converter and a H2SO4 mid groove, and composed of the following equipment units: firing unit: a burning stove, a liquid-supply pump, a gas pressing machine, an atomized air fan and a burnt air fan, a heat-waste recovery unit: a water-pipe heat waste boiler of forced circulation, a dry purification unit and a dry high temperature purified dust remover, a humid contact transforming unit: a converter with a cooler and set with a humid transforming vanadium accelerant catalyst, and a condensation unit: a sour gas condenser set with a glass tube vertical film-falling condensation tube.
Description
Technical field
The present invention relates to coal gas desulfurization and produce the sulfate technology field, particularly a kind of sulphur and waste liquid that generates with coal gas wet oxidation and desulfurization technology produced vitriolic equipment.
Background technology
The hydrogen sulfide that contains in the coal gas is a kind of objectionable impurities.Be used for steel-making and civil time without the coal gas of desulfurization, not only can reduce the quality of steel, and the sulfurous gas that burning produces can destroy environment, influence people's health.Therefore, for satisfying the needs of metallurgical industry, to atmospheric pollution, must the hydrogen sulfide in the coal gas be removed after the minimizing gas-fired.
With quinone ferro-cobalt class composite catalysts such as HPF, PDS, ZL is the Wet-type oxidation sweetening technology of representative, is China's coking industry oneself exploitation, the coal gas desulfurization novel process with complete independent intellectual property right; Remarkable advantages such as this technology has the desulfuration efficiency height, does not need exogenously added alkali unit, and investment and working cost are low, thereby obtained widespread use at China's coking industry.But from integral body, this technology is imperfection still: the first, and the product sulfur purity that generates after the desulfurization is low, of poor quality, sales difficulty; The second, the waste liquid that produces in the sweetening process is not taked suitable treatment process, and waste liquid effluxes and caused new environmental pollution.More than 2 restricted this sulfur removal technology The Application of Technology and development, need to be resolved hurrily and perfect.
Summary of the invention
The purpose of this invention is to provide a kind of sulphur and waste liquid that generates with coal gas wet oxidation and desulfurization technology and produce vitriolic equipment.
The objective of the invention is to realize by following technical proposals.
Produce vitriolic equipment according to sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology of the present invention, comprise liquid waste incinerator, heat recovery boiler, convertor, product sulfuric acid medial launder is characterized in that being made up of following unit:
1) burns the unit: comprise the roasting kiln formed by two incineration section, the combustion fluid liquid-feeding pump that is connected of the atomizing nozzle of roasting kiln, atomizing air gas blower, the gas compressor, the combustion air gas blower that are connected of the burner of roasting kiln therewith therewith respectively
2) waste heat recovery unit: this is a kind of forced circulation type waterpipe type waste heat boiler, is connected with above-mentioned roasting kiln, and is connected with boiler water circulating pump, and its vapour outlet is connected with drum, and boiler internal is provided with soot blower, and is provided with time controller,
3) dry purification unit: this is the dry type high temperature purification fly-ash separator that is connected with above-mentioned waste heat boiler that is provided with high temperature resistant fine filtering element, wherein is provided with pressurized air automatic back blow device,
4) wet type contact conversion unit: this is the convertor that has water cooler that is connected with the pneumatic outlet of above-mentioned high temperature purification fly-ash separator, the wet type with greater activity is housed in convertor transforms the vanadium catalyst catalyzer,
5) condensing unit: this is the acid gas condenser that is connected with above-mentioned convertor, in establish Glass tubing vertically moving membrane prolong, the outlet of condenser sulfuric acid links to each other with sour medial launder, the outlet of acid medial launder sulfuric acid links to each other with acid circulating pump, the acid circulating pump outlet links to each other with acid cooler, the acid cooler outlet links to each other with condenser sulfuric acid outlet conduit and product sulfuric acid line of pipes, and the top waste gas outlet is connected with chimney.
Described drum is connected with boiler feedpump, and this boiler feedpump is connected with the oiler feed groove, and this oiler feed groove is connected with oiler feed pipeline, compound pump, and compound pump is connected with pharmacy slot.
Described high temperature purification fly-ash separator is that high temperature resistant fine filtering element in the shell portion and automatic back blow device three parts that are arranged on this high temperature resistant fine filtering element top are formed by the refractory metal housing that comprises top exhaust chest, filtration chamber, middle part, lower taper ash bucket, the filtration chamber, middle part that is arranged on this refractory metal housing.
Described high temperature resistant fine filtering element is made up of diameter 40～200mm, the metal of long 1000～4000mm or the chimney filter that non-metallic material are made, vertical arranged vertical in housing, fixed by upper tube sheet, the exhaust chest top, top of described refractory metal housing is provided with the filtering gas outlet, filtration chamber, the middle part lower side of described refractory metal housing is provided with process gas import and manhole, is provided with the electromagnetism ash-valve in the exit of described lower taper ash bucket.
Adopt sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology of the present invention to produce vitriolic equipment, to be atomized the back with the mixing tank that the sulphur and the waste liquid of the generation of coal gas wet oxidation and desulfurization technology are sent into roasting kiln burns with pressing gas, the process gas that burns generation is through the waste heat boiler recovery waste heat, remove mine dust by dry type high temperature purification fly-ash separator, in convertor under the katalysis of highly active wet type vanadium catalyst, SO
2Be converted into SO
3, about 270～300 ℃ SO that contains that comes out from conversion unit
3Process gas enter the acid gas condenser of condensing unit, with freezing air it is cooled off indirectly, make the SO in the process gas
3Through hydration, condensation, concentrated about 90～98% the H that generates under about 230～260 ℃ temperature
2SO
4
Produce vitriolic equipment and compare to burn the sulphur that produces behind the coal gas wet oxidation and desulfurization and waste liquid with existing, it is short that the present invention has flow process, and running cost is low, and environment protecting waits remarkable advantage well; Significant to the coal gas wet oxidation and desulfurization equipment, protection environment and the resource circulation utilization that improve coking industry.
1) flow process is short
Existing sulphur and liquid waste incineration acid-producing apparatus are made up of liquid waste incineration, waste heat recovery, wet purification, drying, dry type contact conversion, absorption and tail gas seven unit of removing the evil usually;
Acid-producing apparatus of the present invention then by burning, waste heat recovery, dry purification, wet type contact transform, five unit equipments of condensation form, and have reduced drying and tail gas two unit of removing the evil.
In addition, the wet purification equipment flowsheet in the existing acid-producing apparatus is long, equipment is many, need be made up of 3～4 major equipments such as conditioning tower, cooling tower, clean tower or electrostatic precipitators at least usually, also need dispose utility appliance such as a large amount of pumps; And dry purification equipment only is made up of a dry type high temperature purification fly-ash separator among the present invention, has simplified process gas purification process, has shortened flow process.
2) running cost is low
With the sulphur and the liquid waste incineration sulphuric acid plant of scale, adopt low-temperature cooling water, electricity that acid-producing apparatus of the present invention consumed, be respectively and adopt about 30%, 56% of existing acid-making process; Year operation total expenses only is about 33% of existing acid-making process
3) environment protecting is good
Compare with existing sulphur and liquid waste incineration acid-producing apparatus, acid-producing apparatus of the present invention does not have waste liquid and effluxes.Efflux SO in the tail gas
2And SO
3Acid mist content is lower than national environmental protection and allows discharge index, can directly enter atmosphere through chimney, and the tail gas facility of removing the evil need be set.
Description of drawings
Fig. 1 is an equipment flowsheet synoptic diagram of the present invention.
Fig. 2 is the structural representation of dry type high temperature purification fly-ash separator of the present invention.
Embodiment
Below in conjunction with accompanying drawing concrete enforcement of the present invention is elaborated.
As shown in Figure 1, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology of the present invention produced vitriolic equipment, comprises liquid waste incinerator, heat recovery boiler, convertor, product sulfuric acid medial launder, it is characterized in that being made up of following unit:
1) burns the unit: comprise the roasting kiln 9 formed by two incineration section, the combustion fluid liquid-feeding pump 1 that is connected of the atomizing nozzle 7 of roasting kiln, atomizing air gas blower 22, the gas compressor 3, the combustion air gas blower 21 that are connected of the burner of roasting kiln 9 therewith therewith respectively
2) waste heat recovery unit: this is a kind of forced circulation type waterpipe type waste heat boiler 11, is connected with above-mentioned roasting kiln 9, and is connected with boiler water circulating pump 20, and its vapour outlet is connected with drum 10, and boiler internal is provided with soot blower, and is provided with time controller,
Described drum 10 is connected with boiler feedpump 8, and this boiler feedpump 8 is connected with oiler feed groove 6, and this oiler feed groove is connected with oiler feed pipeline, compound pump 5, and compound pump is connected with pharmacy slot 4.
3) dry purification unit: this is a kind of dry type high temperature purification fly-ash separator 12 that is connected with above-mentioned waste heat boiler 11 that is provided with high temperature resistant fine filtering element, wherein is provided with pressurized air automatic back blow device,
4) wet type contact conversion unit: this is the convertor that has water cooler 13 that is connected with the pneumatic outlet of above-mentioned high temperature purification fly-ash separator, the wet type with greater activity is housed in convertor 13 transforms the vanadium catalyst catalyzer,
5) condensing unit: this is the condenser 14 that is connected with above-mentioned convertor 13, in establish Glass tubing vertically moving membrane prolong, the outlet of condenser 14 sulfuric acid links to each other with sour medial launder 18, the outlet of acid medial launder sulfuric acid links to each other with acid circulating pump 17, the acid circulating pump outlet links to each other with acid cooler 16, the acid cooler outlet links to each other with condenser 14 sulfuric acid outlet conduits and product sulfuric acid line of pipes, and the top waste gas outlet is connected with chimney 15.
As shown in Figure 2, described dry type high temperature purification fly-ash separator 12 is that high temperature resistant fine filtering element 127 in the shell portion and automatic back blow device 125 3 parts that are arranged on these high temperature resistant fine filtering element 127 tops are formed by the refractory metal housing that comprises top exhaust chest 124, filtration chamber, middle part 127, lower taper ash bucket 121, the filtration chamber, middle part 127 that is arranged on this refractory metal housing.
As shown in Figure 2, described high temperature resistant fine filtering element 127 is made up of diameter 40～200mm, the metal of long 1000～4000mm or the chimney filter that non-metallic material are made, vertical arranged vertical in housing, fixed by upper tube sheet 126, top exhaust chest 124 tops of described refractory metal housing are provided with the filtering gas outlet, filtration chamber, middle part 123 lower side of described refractory metal housing are provided with process gas import 122 and manhole 128, are provided with electromagnetism ash-valve 129 in the exit of described lower taper ash bucket 121.
Compare with existing acid-making process, the present invention has reduced drying and tail gas two unit of removing the evil.Dry purification technology only is made up of a dry type high temperature purification fly-ash separator among the present invention, has simplified process gas purification process, has shortened flow process.Compare with existing technology, a year operation total expenses only is 33%, and no waste liquid effluxes.
Claims (7)
1, a kind of sulphur and waste liquid that generates with coal gas wet oxidation and desulfurization technology produced vitriolic equipment, comprises liquid waste incinerator, heat recovery boiler, convertor, product sulfuric acid medial launder, it is characterized in that being made up of following unit:
1) burns the unit: comprise the roasting kiln formed by two incineration section, the combustion fluid liquid-feeding pump that is connected of the atomizing nozzle of roasting kiln, atomizing air gas blower, the gas compressor, the combustion air gas blower that are connected of the burner of roasting kiln therewith therewith respectively
2) waste heat recovery unit: this is a kind of forced circulation type waterpipe type waste heat boiler, is connected with above-mentioned roasting kiln, and is connected with boiler water circulating pump, and its vapour outlet is connected with drum, and boiler internal is provided with soot blower, and is provided with time controller,
3) the dry purification unit is the high temperature purification fly-ash separator that is connected with above-mentioned waste heat boiler that is provided with high temperature resistant fine filtering element, wherein is provided with pressurized air automatic back blow device,
4) wet type contact conversion unit: this is the convertor that has water cooler that the pneumatic outlet of a kind of and above-mentioned high temperature purification fly-ash separator is connected, and the wet type contact conversion vanadium catalyst catalyzer with greater activity is housed in convertor,
5) condensing unit: this is the acid gas condenser that a kind of and above-mentioned convertor is connected, in establish Glass tubing vertically moving membrane prolong, the outlet of condenser sulfuric acid links to each other with sour medial launder, the outlet of acid medial launder sulfuric acid links to each other with acid circulating pump, the acid circulating pump outlet links to each other with acid cooler, the acid cooler outlet links to each other with condenser sulfuric acid outlet conduit and product sulfuric acid line of pipes, and the top waste gas outlet is connected with chimney.
2, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 1 produced vitriolic equipment, it is characterized in that described drum is connected with boiler feedpump, this boiler feedpump is connected with the oiler feed groove, this oiler feed groove is connected with oiler feed pipeline, compound pump, and compound pump is connected with pharmacy slot.
3, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 1 produced vitriolic equipment, it is characterized in that described dry type high temperature purification fly-ash separator is by comprising that the refractory metal housing that top exhaust chest, filtration chamber, middle part, lower taper ash bucket are formed, the filtration chamber, middle part that is arranged on this refractory metal housing are that high temperature resistant fine filtering element in the shell portion and automatic back blow device three parts that are arranged on this high temperature resistant fine filtering element top are formed.
4, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 3 produced vitriolic equipment, it is characterized in that described high temperature resistant fine filtering element is made up of diameter 40～200mm, the metal of long 1000～4000mm or the chimney filter that non-metallic material are made, vertical arranged vertical is fixed by upper tube sheet in housing.
5, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 3 produced vitriolic equipment, it is characterized in that the exhaust chest top, top of described refractory metal housing is provided with the filtering gas outlet, and the centre is provided with manhole.
6, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 3 produced vitriolic equipment, filtration chamber, the middle part lower side that it is characterized in that described refractory metal housing is provided with process gas import and manhole, is provided with the electromagnetism ash-valve in the exit of described lower taper ash bucket.
7, sulphur and the waste liquid that generates with coal gas wet oxidation and desulfurization technology according to claim 3 produced vitriolic equipment, it is characterized in that being equipped with the wet type with greater activity and transform the vanadium catalyst catalyzer in described convertor.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100109697A CN100497165C (en) | 2007-04-16 | 2007-04-16 | Sulfur prepared by coal gas wet-type oxidation desulfurization process and device for preparing sulfuric acid from waste liquor |
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|---|---|---|---|
| CNB2007100109697A CN100497165C (en) | 2007-04-16 | 2007-04-16 | Sulfur prepared by coal gas wet-type oxidation desulfurization process and device for preparing sulfuric acid from waste liquor |
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| CN101033060A true CN101033060A (en) | 2007-09-12 |
| CN100497165C CN100497165C (en) | 2009-06-10 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102092688A (en) * | 2011-02-12 | 2011-06-15 | 李金山 | Technological process for producing acid with sulfur-containing gas |
| CN103043622A (en) * | 2012-12-17 | 2013-04-17 | 刘立文 | Equipment and process for producing sulfuric acid by using calcium sulfate with high temperature and high pressure |
| CN103072957A (en) * | 2013-01-24 | 2013-05-01 | 中冶焦耐工程技术有限公司 | Technology for preparing sulfuric acid |
| EP2942323A1 (en) | 2014-05-09 | 2015-11-11 | Haldor Topsøe A/S | Production of sulfuric acid from coke oven gas desulfurisation product |
| CN107110600A (en) * | 2015-01-02 | 2017-08-29 | 韩国技术有限公司 | Utilize dust reducing apparatus caused by coal breakage supply in the coal drying unit of reheated steam |
-
2007
- 2007-04-16 CN CNB2007100109697A patent/CN100497165C/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102092688A (en) * | 2011-02-12 | 2011-06-15 | 李金山 | Technological process for producing acid with sulfur-containing gas |
| CN102381687A (en) * | 2011-02-12 | 2012-03-21 | 李金山 | Method for preparing acid by using sulfur containing waste material and wet method desulphurization process containing method thereof |
| CN102381687B (en) * | 2011-02-12 | 2013-08-14 | 李金山 | Method for preparing acid by using sulfur containing waste material and wet method desulphurization process containing method thereof |
| CN103043622A (en) * | 2012-12-17 | 2013-04-17 | 刘立文 | Equipment and process for producing sulfuric acid by using calcium sulfate with high temperature and high pressure |
| CN103043622B (en) * | 2012-12-17 | 2015-05-20 | 刘立文 | Equipment and process for producing sulfuric acid by using calcium sulfate with high temperature and high pressure |
| CN103072957A (en) * | 2013-01-24 | 2013-05-01 | 中冶焦耐工程技术有限公司 | Technology for preparing sulfuric acid |
| EP2942323A1 (en) | 2014-05-09 | 2015-11-11 | Haldor Topsøe A/S | Production of sulfuric acid from coke oven gas desulfurisation product |
| CN107110600A (en) * | 2015-01-02 | 2017-08-29 | 韩国技术有限公司 | Utilize dust reducing apparatus caused by coal breakage supply in the coal drying unit of reheated steam |
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| Publication number | Publication date |
|---|---|
| CN100497165C (en) | 2009-06-10 |
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Effective date of registration: 20180725 Address after: 116085 128 high energy street, Qixian Ling high tech Industrial Park, Dalian, Liaoning Patentee after: ACRE Coking And Refractory (Dalian) Engineering Consulting Corp., MCC Address before: No. 27, Shengnan Road, Dong Dong District, Anshan, Liaoning Province Patentee before: ACRE Coking and Refractory Engineering Consulting Corporation, MCC |