CN201209909Y - Acid and alkali neutralization type heating device utilizing low temperature exhaust heat of sulfuric acid production - Google Patents
Acid and alkali neutralization type heating device utilizing low temperature exhaust heat of sulfuric acid production Download PDFInfo
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- CN201209909Y CN201209909Y CNU2008200196568U CN200820019656U CN201209909Y CN 201209909 Y CN201209909 Y CN 201209909Y CN U2008200196568 U CNU2008200196568 U CN U2008200196568U CN 200820019656 U CN200820019656 U CN 200820019656U CN 201209909 Y CN201209909 Y CN 201209909Y
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- Prior art keywords
- acid
- pipeline
- heating device
- sulfuric acid
- waste heat
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- 239000002253 acid Substances 0.000 title claims abstract description 41
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 238000006386 neutralization reaction Methods 0.000 title claims abstract description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title claims description 22
- 239000003513 alkali Substances 0.000 title claims 3
- 238000010438 heat treatment Methods 0.000 title abstract description 12
- 239000007788 liquid Substances 0.000 claims description 3
- 239000002585 base Substances 0.000 claims 2
- 239000002918 waste heat Substances 0.000 abstract description 20
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000000034 method Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 2
- 229910052683 pyrite Inorganic materials 0.000 description 2
- 239000011028 pyrite Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
Description
技术领域 technical field
本实用新型属于废热利用技术领域,具体涉及一种酸碱中和式利用硫酸生产低温余热进行供暖的装置。The utility model belongs to the technical field of waste heat utilization, in particular to an acid-base neutralization device which utilizes sulfuric acid to produce low-temperature waste heat for heating.
背景技术 Background technique
在我国,硫酸生产包括硫磺制酸、硫铁矿制酸、冶炼烟气制酸,而上述制酸方法绝大多数都采用比较先进的两转两吸制酸工艺,制酸过程中,化学反应产生的热量是相当可观的,充分回收利用这些热量是硫酸制造工业的一项重要任务,在两转两吸制酸工艺中,通常把焙烧过程中800-1000℃的余热称为高温余热,约占余热总量的60%,转化过程中500℃左右的余热称为中温余热,约占余热总量的15%,干吸过程中100℃左右的余热称为低温余热,约占余热总量的25%,高温余热和中温余热由于温度高,因此回收利用比较容易,低温余热温度低,且酸温与酸的浓度有关,如硫铁矿制酸中,一吸酸和二吸酸的浓度为98%,酸温为100℃左右,干燥酸的浓度为93%,酸温为70℃左右;在硫磺制酸工艺中,一吸酸、二吸酸、干燥酸的浓度均为98%,酸温均为100℃左右。由于回收难度大,因此大多数硫酸生产厂家没有对低温余热进行回收,一般将生成的带有低温余热的酸流经酸冷器,与循环冷水进行换热降温,这样做不但低温余热得不到利用,而且为了降低酸的温度,还需要使用大量的冷水,既浪费了能源,又浪费了水源。为此,申请人于2007年5月30日申报了专利申请号为200710014486.4,名称为一种利用硫酸生产低温余热进行供暖的方法及装置的专利申请技术,利用硫酸生产中的低温余热进行供暖,取得了良好的经济效益。In China, sulfuric acid production includes sulfuric acid production, pyrite acid production, and smelting flue gas production of acid. Most of the above-mentioned acid production methods adopt relatively advanced two-turn and two-absorption acid production processes. During the acid production process, chemical reactions The heat generated is considerable, and fully recovering and utilizing this heat is an important task in the sulfuric acid manufacturing industry. In the two-rotation and two-suction acid production process, the waste heat at 800-1000°C during the roasting process is usually called high-temperature waste heat, about Accounting for 60% of the total waste heat, waste heat around 500°C in the conversion process is called medium-temperature waste heat, accounting for about 15% of the total waste heat, and waste heat around 100°C in the dry absorption process is called low-temperature waste heat, accounting for about 10% 25%, high-temperature waste heat and medium-temperature waste heat are relatively easy to recycle because of their high temperature, low-temperature waste heat has a low temperature, and the acid temperature is related to the concentration of acid, such as in pyrite acid production, the concentration of primary acid and secondary acid is 98%, the acid temperature is about 100°C, the concentration of dry acid is 93%, and the acid temperature is about 70°C; The temperature is about 100°C. Due to the difficulty of recovery, most sulfuric acid manufacturers do not recover low-temperature waste heat. Generally, the generated acid with low-temperature waste heat flows through the acid cooler to exchange heat with circulating cold water to cool down. This will not only prevent low-temperature waste heat from being obtained Utilize, and in order to reduce the temperature of acid, also need to use a large amount of cold water, both wasted energy, wasted water source again. For this reason, the applicant declared a patent application number of 200710014486.4 on May 30, 2007, which is a patent application technology for a method and device for heating by using sulfuric acid to produce low-temperature waste heat. Good economic benefits have been achieved.
发明内容 Contents of the invention
本实用新型的目的是提供一种安全、使用寿命长的酸碱中和式利用硫酸生产低温余热进行供暖的装置。The purpose of the utility model is to provide a safe and long service life acid-base neutralization device which uses sulfuric acid to produce low-temperature waste heat for heating.
本实用新型是通过以下技术方案来实现的:The utility model is achieved through the following technical solutions:
即一种酸碱中和式利用硫酸生产低温余热进行供暖的装置,包括酸冷器、用户管网,酸冷器分为管程和壳程,管程通过管路与用户管网连接形成循环管路,其特征在于还设有碱液罐通过管路与循环管路连接,循环管路与碱液罐之间的管路上设有碱液泵。That is, an acid-base neutralization device that uses sulfuric acid to produce low-temperature waste heat for heating, including an acid cooler and a user pipe network. The acid cooler is divided into a tube side and a shell side. The tube side is connected to the user pipe network through pipelines to form a cycle The pipeline is characterized in that a lye tank is connected to the circulation pipeline through the pipeline, and an lye pump is arranged on the pipeline between the circulation pipeline and the lye tank.
本实用新型具有安全、使用寿命长的优点。酸冷器一旦出现漏酸,通过隔离,对漏酸的酸冷器停车维修处理后,剩余的微量酸性环境,待酸冷器恢复使用连入循环管路以后,可以利用碱液泵从碱液罐中抽取一定量的30%浓度的NaOH碱液及时注入到循环管路中漏酸处理后的酸冷器或用户管网中的其他有关部位,使供暖循环水的PH值恢复到正常应用范围之内,防止对管道和设备造成腐蚀,延长使用寿命。The utility model has the advantages of safety and long service life. Once the acid cooler leaks acid, through isolation, after the leaking acid cooler is shut down and repaired, the remaining trace of acidic environment can be recovered from the lye by the lye pump after the acid cooler is resumed and connected to the circulation pipeline. Take a certain amount of 30% NaOH lye from the tank and inject it into the acid cooler after acid leakage treatment in the circulation pipeline or other relevant parts in the user pipe network in time to restore the PH value of the heating circulation water to the normal application range Within, to prevent corrosion of pipelines and equipment, prolong service life.
附图说明 Description of drawings
图1为本实用新型实施例1的示意图;Fig. 1 is the schematic diagram of the
图2为本实用新型实施例2的示意图。Fig. 2 is a schematic diagram of
如图中所示:1酸冷器,2碱液泵,3碱液罐,4用户管网,5热水罐,6温水罐。图中箭头为管路中液体的流动方向。As shown in the figure: 1 acid cooler, 2 lye pump, 3 lye tank, 4 user pipe network, 5 hot water tank, 6 warm water tank. The arrows in the figure indicate the flow direction of the liquid in the pipeline.
具体实施方式 Detailed ways
实施例1Example 1
如图1所示,酸冷器1分为管程和壳程,管程通过管路与用户管网4连接形成循环管路,碱液罐3通过管路与循环管路连接,碱液罐3与循环管路之间的管路上设有碱液泵2。As shown in Figure 1, the
在正常供暖时,当酸冷器发生漏酸,并对该酸冷器隔离、停车维修完毕投入运行以后,通过碱液泵2、碱液罐3向循环管路有关部位内注入一定量的30%浓度的NaOH碱液,使供暖循环水的PH值恢复到正常应用范围之内,即可有效防止漏酸对管路和设备进行腐蚀,延长使用寿命。During normal heating, when the acid cooler leaks acid, and after the acid cooler is isolated, shut down for maintenance and put into operation, a certain amount of 30 is injected into the relevant parts of the circulation pipeline through the
实施例2Example 2
如图2所示,酸冷器1分为管程和壳程,管程通过管路与用户管网4、热水罐5、温水罐6连接形成循环管路,碱液罐3通过管路与循环管路连接,碱液罐3与循环管路之间的管路上设有碱液泵2。As shown in Figure 2, the
在正常供暖时,当酸冷器发生漏酸,并对该酸冷器隔离、停车维修完毕投入运行以后,通过碱液泵2、碱液罐3向循环管路有关部位内注入一定量的30%浓度的NaOH碱液,使供暖循环水的PH值恢复到正常应用范围之内,即可有效防止漏酸对管路和设备进行腐蚀,延长使用寿命。During normal heating, when the acid cooler leaks acid, and after the acid cooler is isolated, shut down for maintenance and put into operation, a certain amount of 30 is injected into the relevant parts of the circulation pipeline through the
本实用新型不局限于以上实施例,循环管路上还可加设换热器、过滤器、补水罐等装置,本实用新型实施例中的NaOH碱液的浓度也是可以变化的。The utility model is not limited to the above embodiments, and heat exchangers, filters, water replenishment tanks and other devices can also be added on the circulation pipeline, and the concentration of the NaOH lye in the embodiments of the utility model can also be changed.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200196568U CN201209909Y (en) | 2008-04-01 | 2008-04-01 | Acid and alkali neutralization type heating device utilizing low temperature exhaust heat of sulfuric acid production |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200196568U CN201209909Y (en) | 2008-04-01 | 2008-04-01 | Acid and alkali neutralization type heating device utilizing low temperature exhaust heat of sulfuric acid production |
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| Publication Number | Publication Date |
|---|---|
| CN201209909Y true CN201209909Y (en) | 2009-03-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200196568U Expired - Fee Related CN201209909Y (en) | 2008-04-01 | 2008-04-01 | Acid and alkali neutralization type heating device utilizing low temperature exhaust heat of sulfuric acid production |
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| Country | Link |
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| CN (1) | CN201209909Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983298A (en) * | 2015-02-11 | 2016-10-05 | 上海长园电子材料有限公司 | Industrial flue gas cooling apparatus |
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2008
- 2008-04-01 CN CNU2008200196568U patent/CN201209909Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983298A (en) * | 2015-02-11 | 2016-10-05 | 上海长园电子材料有限公司 | Industrial flue gas cooling apparatus |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20090318 Termination date: 20170401 |