CN204469688U - A kind of cooling device of high temperature ammonia-containing gas sampler - Google Patents
A kind of cooling device of high temperature ammonia-containing gas sampler Download PDFInfo
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- CN204469688U CN204469688U CN201520092119.6U CN201520092119U CN204469688U CN 204469688 U CN204469688 U CN 204469688U CN 201520092119 U CN201520092119 U CN 201520092119U CN 204469688 U CN204469688 U CN 204469688U
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Abstract
The cooling device of a kind of high temperature ammonia-containing gas of the utility model sampler, comprises the sampling pipe be connected on reactor gaseous phase outlet main pipeline, and the forecooler be connected in turn on sampling pipe and sampling cooler group; Sampling cooler group at least comprises a sampling cooler, sampling cooler is respectively arranged with the cooler sample gas inlet connecting forecooler sample export, connect sampling container cooler sample gas outlet, and for cooling medium circulation cooling medium inlet and cooling medium outlet; Cooling medium outlet connects forecooler cooling material inlet; The forecooler cooling material inlet that each sampling cooler is corresponding is connected respectively to after the cooling medium outlet of multiple sampling cooler gathers.Cooling medium cooler package got rid of by forecooler carries out secondary utilization, and realize the cooling in advance to gas sampled and process, the carrying out making full use of the cooling medium of discharge exchanges, and heat energy is realized enrichment better, carries out follow-up further utilization.
Description
Technical field
The utility model belongs to power plant's chemical technology field, relates to the cooling device in urea hydrolyser gaseous phase outlet sampler in flue gas denitrification system, is specially the cooling device of high temperature ammonia-containing gas sampler.
Background technology
Denitrification reducing agent ammonia (NH in domestic coal-burning power plant selective catalytic reduction (SCR) denitrification apparatus
3) be prepared as master with liquefied ammonia in early days, but liquefied ammonia is higher in link risks such as transport, storages.Urea technique for production of ammonia, due to higher security, is more and more subject to showing great attention to of vast SCR denitration user, has boundless market application foreground.
Utilize the hydrolysis of urea to produce ammonia, in hydrolysis reactor outlet gas phase, ammonia level is higher, the aqueous solution of urea of usual charging 50wt% percentage by weight, and hydrolyzer outlet gas phase contains ammonia 37.5v%.But hydrolysis actuator temperature higher (as 160 DEG C), High Temperature Gas phase mixture sampling under high-pressure reactor condition is very inconvenient, in addition in reactor outlet gas phase, moisture is higher, not only affect the inner member of subsequent analysis unit instrument, increase the unreliability of analysis result, also make follow-up assay add difficulty.
In order to ensure authenticity and the security of sampling, the sample of sample point don't fail to be delivered to sampler, one of them important step is exactly sample is introduced the cooling that cooler carries out to a certain degree, when ensureing certain flow, sample is cooled in the safe range of applicable assay (as sample is cooled to 30-40 DEG C, can guaranteed flow 500-700ml/min), People's Republic of China's power industry standard-water, vapour sampler DL/T457-91 could be met.
In prior art, the more employing cooling medium (as running water etc.) of cooling device carries out exchange heat, more commonly intake directly to cooling tube water inlet, after heat exchange, the water at low temperature of carrying heat is directly discharged from the delivery port of cooling tube, and cost is high, and it is slower to the cooldown rate of desired gas, the utilization rate of cooling medium is low, and cannot obtain the chemical composition of hydrolyzer outlet gas phase within the shortest time, efficiency is low.
Utility model content
For problems of the prior art, the utility model provides a kind of structure simple, efficient energy-saving, the cooling device of safe and reliable high temperature ammonia-containing gas sampler.
The utility model is achieved through the following technical solutions:
A cooling device for high temperature ammonia-containing gas sampler, comprises the sampling pipe be connected on reactor gaseous phase outlet main pipeline, and the forecooler be connected in turn on sampling pipe and sampling cooler group; Sampling cooler group at least comprises a sampling cooler, sampling cooler is respectively arranged with the cooler sample gas inlet connecting forecooler sample export, connect sampling container cooler sample gas outlet, and for cooling medium circulation cooling medium inlet and cooling medium outlet; Cooling medium outlet connects forecooler cooling material inlet; The forecooler cooling material inlet that each sampling cooler is corresponding is connected respectively to after the cooling medium outlet of multiple sampling cooler gathers.
Preferably, the multiple sampling coolers in sampling cooler group are arranged in parallel between forecooler sample export and sampling container.
Preferably, sampling pipe is disposed with sampling high temperature high pressure valve group and high temp. high pressure waterwater valve; The outlet of cooler sample gas sets gradually sampling container after pressure-reducing valve and sample valve.
Preferably, sampling cooler adopts shell and tube cooler, the inner coil pipe arranged adopts the two snakelike or continuous coil pipe of double helix of at least one deck, the two ends of coil pipe connect cooler sample gas inlet and the outlet of cooler sample gas respectively, flow in the cavity of cooling medium between coiled pipe cooler housing and coil pipe.
Preferably, sampling cooler adopts shell and tube cooler, inner straight pipe type heat exchanger tube two ends connect cooling medium inlet and cooling medium outlet respectively, the shell upper end of shell and tube cooler arranges cooler sample device entrance, lower end arranges the outlet of cooler sample gas, is filled with the GAS ABSORPTION filler of solid between shell and heat exchanger tube.
Further, two sampling coolers are arranged in parallel between forecooler sample export and sampling container, a sampling cooler adopts carbon dioxide solid absorbent to do GAS ABSORPTION filler, and another sampling cooler adopts ammonia solid absorbent to do GAS ABSORPTION filler.
Further, forecooler adopts shell-and-tube heat exchanger, and the two ends of internal heat exchange tubes connect cooling material inlet and outlet respectively.
Compared with prior art, the utility model has following useful technique effect:
The cooling medium that cooler package is got rid of by forecooler by the utility model carries out secondary utilization, realize the cooling in advance to gas sampled and process, the carrying out making full use of the cooling medium of discharge exchanges, heat energy is realized enrichment better, carry out follow-up further utilization, improve the product phase of enrichment energy; Article one, sampling line can corresponding multiple sampling cooler, and a corresponding forecooler of cooler, the mode of this arbitrarily combination as the case may be can make high temp samples gas be lowered the temperature timely and effectively in cooling link; The structure of sampling cooler group is simple, and assembling that can be random and cooperation, do not injure the instrument valve on sampling line, avoids sample temperature and spends the high instrument and meter damaging sampler and subsequent detection unit, improve and protect the security of personnel; Make the utility model safe and efficient, easy to use, flexible configuration, working stability is reliable.
Further, by the parallel connection of sampling cooler, the demand to large cardinal sampling can be met simultaneously, and ensure the cooling requirement that cooler sample export is discharged; Coordinate after the connection of the outlet of each sampling cooler is gathered, the cooling temperature difference between each sampling cooler can be eliminated, be passed into respectively again in forecooler after the intensification of each cooling medium is all closed, improve the efficiency of forecooler better, abundant make use of cooling medium.
Further, the high temperature high pressure valve arranged is utilized to realize master control to sampler, ensureing the normal work in hydrolysis of urea reactor when not sampling, wherein survival gas and moisture can be discharged in advance when sampling by blowoff valve, ensure the accuracy of each sampling; The pressure reduction making sample flow in sampling process can be regulated by the decompressor arranged in the outlet of cooler sample gas, ensure that the accuracy of sampling on the one hand, because of the sample of releasing at ambient pressure in container, portion of product component when moisture seriously evaporates, can not be carried away; Can carry out pressure adjustment to the sampling requirement under different condition on the other hand, adaptability is good, and operability is high.
Further, by the restriction of sampling cooler structure and optimization, can not only process and dismounting and change sampling cooler easily, not easily block; And can according to the sampling of gas with various and testing requirement, utilize the sampling cooler of different structure carry out combination and successively with the use of, the component test of sample gas can be carried out easily and fast.
Accompanying drawing explanation
Fig. 1 is the structural representation of cooling device described in the utility model example 1.
Fig. 2 is the syndeton schematic diagram of forecooler in the utility model example.
Fig. 3 is the structural representation of cooling device described in the utility model example 2.
Fig. 4 is the structural representation of sampling cooler group described in the utility model example 3.
In figure: 1-reactor gaseous phase outlet main pipeline; 2-sampling pipe; 3-samples high temperature high pressure valve; 4-high temp. high pressure waterwater valve; 5-forecooler; 6-cooling medium inlet; 7-cooling medium exports; 8-sampling cooler; 9-pressure-reducing valve; 10-sample valve; 11-sampling container; 12-forecooler cooling medium exports; 13-forecooler sample gas inlet; 14-cooler sample gas inlet; 15-cooler sample gas exports; 16-carbon dioxide solid absorbent; 17-ammonia solid absorbent.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described in further detail, described in be to explanation of the present utility model instead of restriction.
The sample gas of the required sampling of the utility model through being connected to sampling high temperature high pressure valve 3 on sampling pipe 2 and high temp. high pressure waterwater valve 4 emptying after, close the forecooler 5 that high temp. high pressure waterwater valve 4 enters sampling cooler 8 correspondence at different levels again, after preliminary precooling, enter multistage sampling cooler 8, running water can be adopted to enter sampling cooler 8 at different levels as cryogenic media respectively from water inlet, cryogenic media after effect is discharged from the cooling medium outlet 7 of sampling cooler 8 at different levels, hot water after gathering directly is not drained, but be divided into several road as the cryogenic media of forecooler 5 at different levels and enter forecooler 8 respectively, again the heat after enrichment is utilized after discharging sampler as waste water after playing a role.
Sampling cooler 8 is for the gas phase sampling refrigerating device of power plant's denitration hydrolysis of urea reactor, comprise housing and coil pipe, described housing tip arranges top cover, and bottom arranges base, on top cover, side arranges cooling medium inlet 6, and symmetrical opposite side arranges cooling medium outlet 7.
When to gas sample ammonia concentration, in lower or component, moisture is relatively little, enclosure interior arrange one or more groups heat exchanger effectiveness higher two snakelike/the continuous coil pipe of double-spiral structure, adopt single or multiple lift cooling tube arrangement architecture, concrete group of number is got by the calculating of required film-cooled heat, outermost layer cooling pipe orifice is arranged on Casing top eccentric position, be connected with cooler sample gas inlet 14, innermost layer cooling pipe orifice is arranged on the eccentric position of Casing top symmetry, exports 15 be connected with cooler sample gas.
And when for gas sample ammonia concentration, in higher or component, moisture is relatively high, the sampling cooler 8 adopted, in enclosure interior, the vertical parallel straight pipe type heat exchanger tube of many groups is set, cooling medium is walked in pipe, side, bottom arranges cooling medium inlet 6, and top opposite side arranges cooling medium outlet 7.Enclosure interior fills the solid gas sample process filler of certain altitude, and gas sample is after forecooler 5, and what be evenly distributed from top to bottom from cooler top flows through filler, discharges, enter subsequent pipeline from bottom.After filler is repeatedly flooded, toppled over by dismountable cooler top, can recycled for multiple times after process.Also corresponding liquid can being adopted as gas absorbent simultaneously, when adopting liquid to do gas absorbent, needing below cooler sample gas inlet 14 being arranged on sampling cooler 8, cooler sample gas outlet 15 is arranged on top.
Wherein, the conduit involved by sampling cooler 8 all adopts stainless steel, can avoid being corroded thus contaminated samples at long-term sampling process pipeline, makes institute's sample thief lose authenticity; It can be used in the on-line period of high temperature liquid-vapor mixture.The cold formation capable of being combined of removing device 8 of sampling in sampling cooler group, combined number primary condition per sample, cooling medium parameter and the design parameter such as mean temperature difference will be reached obtain.Sampling cooler 8 compact conformation, corrosion-resistant, heat transfer efficiency is high, the dismounting of pipeline valve and cleaning is simple, long service life.Forecooler adopts shell-and-tube heat exchanger, carries out simple heat exchange, and the secondary completing cooling medium utilizes; Concrete as below as described in three embodiments.
Example 1
The cooling device of a kind of high temperature ammonia-containing gas of the utility model sampler, as shown in Figure 1, comprises the sampling pipe 2 be connected on reactor gaseous phase outlet main pipeline 1, and the forecooler 5 be connected in turn on sampling pipe and sampling cooler 8; Sampling pipe 2 is disposed with high temperature high pressure valve group 3 and high temp. high pressure waterwater valve 4; The pipelines that cooler sample gas outlet 15 connects are disposed with pressure-reducing valve 9 and sample valve 10 and sampling container 11; As shown in Figure 2, the sampling cooler group in this preferred embodiment adopts a sampling cooler 8 to form, and is applicable to the situation that in or component lower to gas sample ammonia concentration, moisture is relatively little.A sampling cooler 8 arranges a forecooler 5, form one group of cooling device, first the sample gas that sampling pipe comes enters forecooler 5 through forecooler sample gas inlet 13, after precooling, 5 enter sampling cooler 8, sampling cooler side arranges cooling medium entrance 6, opposite side is cooling medium outlet 7, go device sample gas to export to enter follow-up instrument valve to sample further by cold through sampling cooler 8 sample gas out, cooling medium outlet 7 cryogenic media out of sampling cooler 8 is as the cooling medium entrance material of forecooler 5, after forecooler heat exchange, enter other unit from cooling medium outlet 12 discharge recycle.
Example 2
The cooling device of a kind of high temperature ammonia-containing gas of the utility model sampler, as shown in Figure 3, on the basis of example 1, one group of cooling device is increased in the sampling cooler group that sampling pipe 2 on reactor outlet gas phase main pipeline 1 connects, be arranged on after HTHP sample valve group, two-way is divided to enter two forecoolers 5 respectively, enter respective sampling cooler 8 more respectively, after heat exchange cooling process, enter the pipeline before pressure-reducing valve 9 from respective sampling cooler 8 out sample gas together and carry out subsequent samples work, cooling medium is external from unit, the water inlet 6 entering two groups of sampling coolers 8 is controlled respectively through ball valve, after heat exchange, cooling medium is discharged from respective sampling cooler, the forecooler 5 entering 2 groups of cooling devices after gathering respectively carries out the recycling of cooling medium, discharge from the cooling medium outlet of forecooler again, enter other unit recycling.
Example 3
The cooling device of a kind of high temperature ammonia-containing gas of the utility model sampler, as shown in Figure 4, the situation that in higher or component, moisture is relatively high for gas sample ammonia concentration, due to the difference of concentration of aqueous solution of urea, the ratio of the ammonia contained in gas phase, water, carbon dioxide is also different.If do not affect the constituent content of ammonia and carbon dioxide simultaneously, neutral drier can only be used, but the conventional neutral drier of major part is because reacting with gas product, generates other products, can not adopt.In order to the ammonia level in better test products gas, two special filler coolers can be set and carry out process test at twice, the sample gas that first time samples is merely through the sampling cooler of filling arbon dioxide solid absorbent 16, dry moisture and carbon dioxide, discharge the interference of moisture and carbon dioxide, test after final sampling and obtain ammonia concentration in gas sample, carbon dioxide solid absorbent 16 preferably can adopt solid sodium hydroxide; Then switch pipeline by Valve controlling and carry out second time sampling, sampling gas sample is merely through the sampling cooler 8 of filling ammonia solid absorbent 17, and first remove ammonia, sampling and testing obtains gas concentration lwevel in gas sample afterwards; The result of twice can calculate respectively and finally obtain each constituent content of gas product; Transfer sequence can be exchanged, thus can realize fast and accurately gathering targetedly and measuring.
Claims (7)
1. the cooling device of a high temperature ammonia-containing gas sampler, it is characterized in that, comprise the sampling pipe (2) be connected on reactor gaseous phase outlet main pipeline (1), and the forecooler (5) be connected in turn on sampling pipe and sampling cooler group; Described sampling cooler group at least comprises a sampling cooler (8), sampling cooler (8) is respectively arranged with the cooler sample gas inlet (14) connecting forecooler (5) sample export, connect sampling container (11) cooler sample gas outlet (15), and for cooling medium circulation cooling medium inlet (6) and cooling medium export (7); Cooling medium outlet (7) connects forecooler (5) cooling material inlet; The cooling medium of multiple sampling cooler (8) exports after (7) connection gathers and is connected respectively to forecooler (5) cooling material inlet corresponding to each sampling cooler (8).
2. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 1, it is characterized in that, the multiple sampling coolers (8) in described sampling cooler group are arranged in parallel between forecooler (5) sample export and sampling container (11).
3. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 1, it is characterized in that, described sampling pipe (2) is disposed with sampling high temperature high pressure valve group (3) and high temp. high pressure waterwater valve (4); Cooler sample gas outlet (15) sets gradually pressure-reducing valve (9) and sample valve (10) sampling container (11) afterwards.
4. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 1, it is characterized in that, sampling cooler (8) adopts shell and tube cooler, the inner coil pipe arranged adopts the two snakelike or continuous coil pipe of double helix of at least one deck, the two ends of coil pipe connect cooler sample gas inlet (14) and cooler sample gas outlet (15) respectively, flow in the cavity of cooling medium between coiled pipe cooler housing and coil pipe.
5. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 1, it is characterized in that, sampling cooler (8) adopts shell and tube cooler, inner straight pipe type heat exchanger tube two ends connect cooling medium inlet (6) and cooling medium outlet (7) respectively, the shell upper end of shell and tube cooler arranges cooler sample device entrance (14), lower end arranges cooler sample gas outlet (15), is filled with the GAS ABSORPTION filler of solid between shell and heat exchanger tube.
6. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 5, it is characterized in that, two sampling coolers (8) are arranged in parallel between forecooler (5) sample export and sampling container (11), a sampling cooler (8) adopts carbon dioxide solid absorbent (16) to do GAS ABSORPTION filler, and another sampling cooler (8) adopts ammonia solid absorbent (17) to do GAS ABSORPTION filler.
7. the cooling device of a kind of high temperature ammonia-containing gas sampler according to claim 4 or 5, is characterized in that, described forecooler (5) adopts shell-and-tube heat exchanger, and the two ends of internal heat exchange tubes connect cooling material inlet and outlet respectively.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520092119.6U CN204469688U (en) | 2015-02-09 | 2015-02-09 | A kind of cooling device of high temperature ammonia-containing gas sampler |
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| CN201520092119.6U CN204469688U (en) | 2015-02-09 | 2015-02-09 | A kind of cooling device of high temperature ammonia-containing gas sampler |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105372404A (en) * | 2015-11-03 | 2016-03-02 | 中煤科工集团重庆研究院有限公司 | Low-temperature gas explosion characteristic test method |
| CN109339279A (en) * | 2018-10-31 | 2019-02-15 | 东北石油大学 | A kind of suitable severe cold area has the agriculture residence of solar energy low-temperature thermal water phase-changing wall |
| CN112985900A (en) * | 2021-03-17 | 2021-06-18 | 西安热工研究院有限公司 | Chemical cleaning sampling cooling device and use method |
-
2015
- 2015-02-09 CN CN201520092119.6U patent/CN204469688U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105372404A (en) * | 2015-11-03 | 2016-03-02 | 中煤科工集团重庆研究院有限公司 | Low-temperature gas explosion characteristic test method |
| CN109339279A (en) * | 2018-10-31 | 2019-02-15 | 东北石油大学 | A kind of suitable severe cold area has the agriculture residence of solar energy low-temperature thermal water phase-changing wall |
| CN112985900A (en) * | 2021-03-17 | 2021-06-18 | 西安热工研究院有限公司 | Chemical cleaning sampling cooling device and use method |
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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: 20150715 Termination date: 20180209 |