CN201074869Y - Device for supplying heat using sulfuric acid production low temperature waste heat - Google Patents
Device for supplying heat using sulfuric acid production low temperature waste heat Download PDFInfo
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- CN201074869Y CN201074869Y CNU2007200236147U CN200720023614U CN201074869Y CN 201074869 Y CN201074869 Y CN 201074869Y CN U2007200236147 U CNU2007200236147 U CN U2007200236147U CN 200720023614 U CN200720023614 U CN 200720023614U CN 201074869 Y CN201074869 Y CN 201074869Y
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- 239000002918 waste heat Substances 0.000 title claims abstract description 32
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title claims description 43
- 238000004519 manufacturing process Methods 0.000 title description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 137
- 238000010438 heat treatment Methods 0.000 claims abstract description 77
- 239000002253 acid Substances 0.000 claims abstract description 66
- 239000008236 heating water Substances 0.000 claims description 22
- 238000001816 cooling Methods 0.000 claims description 12
- 238000010792 warming Methods 0.000 claims description 5
- 230000017525 heat dissipation Effects 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 abstract description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract 4
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram 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
- 238000011084 recovery Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel 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
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002161 passivation Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000002407 reforming 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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Abstract
Description
技术领域 technical field
本实用新型属于废热利用设备领域,具体涉及一种利用硫酸生产低温余热进行供暖的装置。The utility model belongs to the field of waste heat utilization equipment, in particular to a device for heating by using sulfuric acid to produce low-temperature waste heat.
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。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, the 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 the waste heat around 100°C in the dry absorption process is called low-temperature waste heat, accounting for about 10% of the total waste heat. 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 around 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.
发明内容 Contents of the invention
本实用新型的目的是提供一种节能降耗的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 an energy-saving and consumption-reducing device that utilizes 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:即一种利用硫酸生产低温余热进行供暖的装置,包括酸冷器,酸冷器分为管程和壳程,壳程与进酸管、出酸管连接,管程与循环水进水管、循环水出水管连接,循环水进水管、循环水出水管上均设有阀门,其特征在于酸冷器的管程还通过管路与供暖装置连接。The utility model is realized through the following technical solutions: namely, a device for heating by using sulfuric acid to produce low-temperature waste heat, including an acid cooler, the acid cooler is divided into a tube side and a shell side, and the shell side is connected with the acid inlet pipe and the acid outlet pipe. The pipe is connected with the circulating water inlet pipe and the circulating water outlet pipe, and the circulating water inlet pipe and the circulating water outlet pipe are equipped with valves. It is characterized in that the pipe side of the acid cooler is also connected to the heating device through the pipeline.
所述的酸冷器为阳极保护管壳式酸冷器,所述的供暖系统包括热水塔、散热装置,温水塔;热水塔通过供暖水热水管与阳极保护管壳式酸冷器的管程连接,温水塔通过供暖水温水管与阳极保护管壳式酸冷器的管程连接,供暖水热水管、供暖水温水管上均设有阀门,热水塔与散热装置之间通过管路连接,管路上设有热水泵,散热装置与温水塔之间通过管路连接,供暖水温水管上设有温水泵,温水塔通过管路与供暖循环水补充塔连接。如利用低温余热提供给供暖循环水的热量等于供暖循环水散失的热量时,即可采用如上设置进行供暖,当供暖循环水出现损耗时,通过供暖循环水补充塔向温水塔内补充适量的供暖循环水即可。The acid cooler is an anode-protected shell-and-tube acid cooler, and the heating system includes a hot water tower, a cooling device, and a warm water tower; Tube side connection, the warm water tower is connected to the tube side of the anode protection shell-and-tube acid cooler through the heating water temperature pipe, the heating water hot water pipe and the heating water temperature water pipe are equipped with valves, and the hot water tower and the cooling device are connected through pipelines , a hot water pump is arranged on the pipeline, the cooling device and the warm water tower are connected through pipelines, a warm water pump is arranged on the heating water warm water pipe, and the warm water tower is connected with the heating circulating water replenishment tower through pipelines. If the heat supplied to the heating circulating water by low-temperature waste heat is equal to the heat lost by the heating circulating water, the above settings can be used for heating. When the heating circulating water is lost, an appropriate amount of heating can be added to the warm water tower through the heating circulating water replenishment tower Just circulate the water.
热水塔通过管路与供暖循环水增温装置连接,热水塔和温水塔之间设有连接管,连接管上设有阀门。当利用低温余热提供给供暖循环水的热量小于供暖循环水散失的热量时,或硫酸生产设备临时停车时,为保证供暖,可以通过供暖循环水增温装置加热供暖循环水,进行辅助性供暖。供暖循环水增温装置可以选用硫酸制造行业中常用的蒸汽锅炉,也可以采用其他可以产生高温蒸汽的设备。The hot water tower is connected with the heating circulating water warming device through pipelines, a connecting pipe is arranged between the hot water tower and the warm water tower, and a valve is arranged on the connecting pipe. When the heat supplied to the heating circulating water by low-temperature waste heat is less than the heat lost by the heating circulating water, or when the sulfuric acid production equipment is temporarily stopped, in order to ensure heating, the heating circulating water can be heated by the heating circulating water warming device for auxiliary heating. The heating circulating water heating device can be the steam boiler commonly used in the sulfuric acid manufacturing industry, or other equipment that can generate high-temperature steam.
本实用新型利用两转两吸制酸工艺中生成的浓度为98%的酸作为热源加热循环水进行供暖,既回收利用了硫酸生产中的低温余热,又节省了取暖所需要的能源和费用,具有节能降耗、便于维护、便于对现有技术进行改造的优点。本实用新型中的酸冷器可以采用阳极保护管壳式酸冷器,也可以采用其他类型的酸冷器。当使用阳极保护管壳式酸冷器时,因为阳极保护管壳式酸冷器一般采用316L不锈钢制造,而316L不锈钢在浓硫酸中的钝化效果与硫酸的浓度和温度有重要关系,浓度为98%酸在阳极保护管壳式酸冷器中的最高使用温度不能高于120℃,可正常工作在100℃左右;浓度为93%的酸在阳极保护管壳式酸冷器中的最高使用温度不能高于70℃,因此浓度为93%的酸不适合作为热源。冬季供暖只能选用浓度为98%的酸,供暖循环水采用中间水或脱盐水,不易结垢,有利于延长酸冷器和供暖系统的使用寿命。本实用新型不破坏原有硫酸生产设备,便于对现有技术的硫酸生产设备进行改造。在不需要供暖的春、夏、秋季节,通过关闭供暖水热水管、供暖水温水管上的阀门,打开循环水进水管、循环水出水管上的阀门即可。在需要供暖的冬季,关闭循环水进水管、循环水出水管上的阀门,打开供暖水热水管、供暖水温水管上的阀门即可使用。正常使用时,只需及时补充损耗的供暖循环水即可,便于维护。经试验,采用本实用新型加热的供暖循环水的温度稳定在65℃~80℃之间,完全可以满足冬季供暖的需要。本实用新型利用硫酸生产中的低温余热进行供暖,既有效解决了低温余热难以回收的难题,又为企业节省了大量的供暖费用,可广泛应用于硫酸生产企业中。The utility model uses the acid with a concentration of 98% generated in the two-turn and two-suction acid production process as a heat source to heat the circulating water for heating, which not only recycles the low-temperature waste heat in the production of sulfuric acid, but also saves the energy and cost required for heating. The utility model has the advantages of energy saving, consumption reduction, easy maintenance, and convenient modification of existing technologies. The acid cooler in the utility model can adopt an anode protection shell-and-tube type acid cooler, and also can adopt other types of acid coolers. When using an anodic protection shell-and-tube acid cooler, because the anode protection shell-and-tube acid cooler is generally made of 316L stainless steel, and the passivation effect of 316L stainless steel in concentrated sulfuric acid has an important relationship with the concentration and temperature of sulfuric acid, the concentration is The maximum operating temperature of 98% acid in the anode protection shell-and-tube acid cooler cannot be higher than 120°C, and it can work normally at about 100°C; the maximum use temperature of the acid with a concentration of 93% in the anode protection shell-and-tube acid cooler The temperature cannot be higher than 70°C, so acid with a concentration of 93% is not suitable as a heat source. Only acid with a concentration of 98% can be used for heating in winter, and intermediate water or desalinated water is used for heating circulating water, which is not easy to scale and is beneficial to prolong the service life of acid coolers and heating systems. The utility model does not destroy the original sulfuric acid production equipment, and is convenient for reforming the sulfuric acid production equipment in the prior art. In the seasons of spring, summer and autumn when heating is not needed, the valves on the circulating water inlet pipe and the circulating water outlet pipe can be opened by closing the valves on the heating water hot water pipe and the heating water temperature pipe. In winter when heating is required, close the valves on the circulating water inlet pipe and the circulating water outlet pipe, and open the valves on the heating water hot water pipe and the heating water warm water pipe to use. In normal use, it is only necessary to replenish the lost heating circulating water in time, which is convenient for maintenance. Through tests, the temperature of the heating circulating water heated by the utility model is stable between 65 DEG C and 80 DEG C, which can fully meet the needs of heating in winter. The utility model utilizes low-temperature waste heat in sulfuric acid production for heating, which not only effectively solves the difficult problem of low-temperature waste heat recovery, but also saves a lot of heating costs for enterprises, and can be widely used in sulfuric acid production enterprises.
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 the schematic diagram of the
如图中所示:1循环水出水管,2阀门,3阀门,4供暖水热水管,5阳极保护管壳式酸冷器,6供暖水温水管,7阀门,8阀门,9循环水进水管,10热水塔,11热水泵,12蒸汽锅炉,13阀门,14连接管,15温水塔,16散热装置,17供暖循环水补充塔,18温水泵。As shown in the picture: 1 circulating water outlet pipe, 2 valves, 3 valves, 4 heating water hot water pipes, 5 anode protection shell type acid cooler, 6 heating water temperature pipes, 7 valves, 8 valves, 9 circulating water inlet pipes , 10 hot water towers, 11 hot water pumps, 12 steam boilers, 13 valves, 14 connecting pipes, 15 warm water towers, 16 cooling devices, 17 heating circulating water replenishment towers, 18 warm water pumps.
具体实施方式 Detailed ways
实施例1Example 1
如图1所示:酸冷器为阳极保护管壳式酸冷器5,阳极保护管壳式酸冷器5的管程与循环水进水管9、循环水出水管1连接,阳极保护管壳式酸冷器5的壳程与进酸管、出酸管连接,循环水进水管9、循环水出水管1上分别设有阀门8、阀门2,热水塔10通过供暖水热水管4与阳极保护管壳式酸冷器5的管程连接,温水塔15通过供暖水温水管6与阳极保护管壳式酸冷器5的管程连接,供暖水热水管4上设有阀门3,供暖水温水管6设有阀门7,热水塔10与散热装置16之间的管路上设有热水泵11,供暖水温水管6上设有温水泵18,温水塔15通过管路与供暖循环水补充塔17连接。As shown in Figure 1: the acid cooler is an anode-protected shell-and-tube acid cooler 5, and the tube side of the anode-protected shell-and-tube acid cooler 5 is connected to the circulating water inlet pipe 9 and the circulating
本实用新型在不需要供暖的春、夏、秋季节时,阀门3、阀门7处于关闭状态,阀门2、阀门8处于打开状态,冷却循环水通过循环水进水管9、循环水出水管1流经阳极保护管壳式酸冷器5的管程,浓度为98%的酸通过进酸管、出酸管流经阳极保护管壳式酸冷器5的壳程。In the spring, summer and autumn seasons when heating is not required in the utility model, the
在需要供暖的冬季,在通过供暖循环水补充塔17向温水塔15中注入适量的供暖循环水,供暖循环水选用中间水,关闭阀门2、阀门8,同时打开阀门3、阀门7,在温水泵18的作用下,温水塔15中的供暖循环水通过供暖水温水管6流入阳极保护管壳式酸冷器5的管程,与壳程中流动的浓度为98%的酸进行热交换.加热后的供暖循环水从供暖水热水管4流入热水塔10,在热水泵11的作用下,进入散热装置16,散热装置16可以选用散热片,经过散热装置16的散热,供暖循环水的温度下降,流回温水塔15,重复上述过程,即可实现持续供暖,如果供暖循环水出现损耗,通过供暖循环水补充塔17向温水塔15注入适量的供暖循环水即可。In the winter when heating is required, inject an appropriate amount of heating circulating water into the
本实施例适用于所利用低温余热提供给供暖循环水的热量等于供暖循环水散失的热量时的情况。This embodiment is applicable to the situation when the heat supplied to the heating circulating water by the low-temperature waste heat is equal to the heat lost by the heating circulating water.
实施例2Example 2
如图2所示:热水塔10上设有供暖循环水增温装置,供暖循环水增温装置为蒸汽锅炉12,热水塔10和温水塔15之间设有连接管14,连接管14上设有阀门13,其他同图1。As shown in Figure 2: the hot water tower 10 is provided with a heating circulating water warming device, the heating circulating water warming device is a
在不需要供暖的春、夏、秋季节,本实施例同实施例1。In the seasons of spring, summer and autumn when heating is not needed, this embodiment is the same as
在需要供暖的冬季,正常供暖时本实施例与实施例1相同。In winter when heating is required, this embodiment is the same as
在需要供暖的冬季,当硫酸尘产设备临时停车时,为了不影响供暖,可以关停温水泵18,同时打开阀门13,使热水塔10与温水塔15连通,通过蒸汽锅炉12向热水塔10内输送少量高温低压蒸汽,维持热水塔10内供暖循环水的温度,在热水泵11的作用下,供暖循环水在热水塔10、散热装置16、温水塔15形成的循环回路中流动,进行辅助性供暖。In the winter when heating is required, when the sulfuric acid dust production equipment temporarily stops, in order not to affect the heating, the
在需要供暖的冬季,当所利用低温余热提供给供暖循环水的热量小于供暖循环水散失的热量时,供暖循环水的温度会逐渐降低,为了不影响供暖,可以通过蒸汽锅炉12向热水塔10内输送少量高温低压蒸汽,维持热水塔10内供暖循环水的温度,保证供暖。In the winter when heating is required, when the heat supplied by the low-temperature waste heat to the heating circulating water is less than the heat lost by the heating circulating water, the temperature of the heating circulating water will gradually decrease. A small amount of high-temperature and low-pressure steam is transported inside to maintain the temperature of the heating circulating water in the hot water tower 10 to ensure heating.
本实用新型不局限于以上实施例,供暖循环水也可以采用脱盐水或其他不易结垢的水,供暖循环水增温装置也可以采用本领域技术人员想到的其他的现有技术的装置。The utility model is not limited to the above embodiments. The heating circulating water can also use desalinated water or other water that is not easy to scale.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102778143A (en) * | 2012-07-04 | 2012-11-14 | 黑龙江建龙钢铁有限公司 | Circulating ammonia water waste heat utilizing system |
| CN104528662A (en) * | 2015-01-16 | 2015-04-22 | 中国瑞林工程技术有限公司 | System for generating hot water by recovering low-temperature waste heat in process of making acid by using smoke |
| CN105905873A (en) * | 2016-04-22 | 2016-08-31 | 中国瑞林工程技术有限公司 | Technology for producing water by using low temperature waste heat and for recycling low temperature waste heat |
| CN110054162A (en) * | 2019-04-25 | 2019-07-26 | 吉林隆源骐化工有限责任公司 | A kind of anodic protection acid cooler to heat |
| CN111520796A (en) * | 2020-04-09 | 2020-08-11 | 赤峰云铜有色金属有限公司 | Method for removing and utilizing heat of absorbed circulating acid in sulfuric acid process |
-
2007
- 2007-06-15 CN CNU2007200236147U patent/CN201074869Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102778143A (en) * | 2012-07-04 | 2012-11-14 | 黑龙江建龙钢铁有限公司 | Circulating ammonia water waste heat utilizing system |
| CN104528662A (en) * | 2015-01-16 | 2015-04-22 | 中国瑞林工程技术有限公司 | System for generating hot water by recovering low-temperature waste heat in process of making acid by using smoke |
| CN105905873A (en) * | 2016-04-22 | 2016-08-31 | 中国瑞林工程技术有限公司 | Technology for producing water by using low temperature waste heat and for recycling low temperature waste heat |
| CN110054162A (en) * | 2019-04-25 | 2019-07-26 | 吉林隆源骐化工有限责任公司 | A kind of anodic protection acid cooler to heat |
| CN111520796A (en) * | 2020-04-09 | 2020-08-11 | 赤峰云铜有色金属有限公司 | Method for removing and utilizing heat of absorbed circulating acid in sulfuric acid process |
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| C14 | Grant of patent or utility model | ||
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