CN205313486U - Novel skid -mounted equipment of hydrogen sulfide in desorption natural gas - Google Patents
Novel skid -mounted equipment of hydrogen sulfide in desorption natural gas Download PDFInfo
- Publication number
- CN205313486U CN205313486U CN201620054429.3U CN201620054429U CN205313486U CN 205313486 U CN205313486 U CN 205313486U CN 201620054429 U CN201620054429 U CN 201620054429U CN 205313486 U CN205313486 U CN 205313486U
- Authority
- CN
- China
- Prior art keywords
- natural gas
- hydrogen sulfide
- gas
- carried out
- skid
- 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.)
- Expired - Fee Related
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 104
- 239000003345 natural gas Substances 0.000 title claims abstract description 52
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229910000037 hydrogen sulfide Inorganic materials 0.000 title claims abstract description 28
- 238000003795 desorption Methods 0.000 title abstract 3
- 239000007789 gas Substances 0.000 claims abstract description 30
- 239000012528 membrane Substances 0.000 claims abstract description 11
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 6
- 239000000428 dust Substances 0.000 claims abstract description 6
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 6
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 6
- 238000000926 separation method Methods 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000008030 elimination Effects 0.000 claims description 11
- 238000003379 elimination reaction Methods 0.000 claims description 11
- 238000010926 purge Methods 0.000 claims description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 239000011593 sulfur Substances 0.000 claims description 5
- 238000004581 coalescence Methods 0.000 abstract description 6
- 238000012544 monitoring process Methods 0.000 abstract description 3
- 230000009467 reduction Effects 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000003009 desulfurizing effect Effects 0.000 description 3
- 230000032258 transport Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a novel skid -mounted equipment of hydrogen sulfide in desorption natural gas, including separating the above liquid drop of 5um and the coalescence -separation ware of solid, the realization is carried out compound heat to the natural gas and is heaied up, guarantee that gas temperature is higher than water, hydrocarbon dew point temperature's heater, carry out the hydrogen sulfide in the natural gas membrane separator of crude separation, the realization is to the torch of high sulfurous gas unloading burning or centralized processing, the digester of realization remaining a small amount of hydrogen sulfide readsorption desorption in to the natural gas, the flowmeter of monitoring is carried out in the realization to the natural gas throughput value after handling, the purified gas pipe network carried is carried out meet the standard's the natural gas, be provided with the differential gauge on the coalescence -separation ware, the natural gas export of digester bottom is provided with dust filter unit, the utility model has the advantages of high integrated sled dressization, the flow is simplified, and convenient transportation is moved, and the reduction running cost possesses monitor function simultaneously.
Description
Technical field
This utility model belongs to the purification apparatus technical field of natural gas, especially relates to the skid-mounted device of a kind of novel elimination hydrogen sulfide in natural gas.
Background technology
Natural gas is the energy of cleaning, environmental protection, safety, along with natural gas is by increasingly extensive use, makes people that the hydrogen sulfide in natural gas more to be paid close attention to. The natural gas of sulfur-bearing must could enter gas line network after desulfurization, a series of purification of dehydration and use. In the desulfurizer of prior art due in raw natural gas gas containing assorted many, after generally adopting more piece or multiple desulfurizing tower to can be only achieved desulfurization in parallel or series, sulfur content reaches requirement, and structure is complicated, and floor space is big, it has not been convenient to transport resettlement, operating cost is higher.
Utility model content
Problem to be solved in the utility model is to provide a kind of highly integrated skid, process simplification, conveniently transports resettlement, reduces operating cost, is provided simultaneously with the skid-mounted device of the novel elimination hydrogen sulfide in natural gas of monitoring function.
For solving above-mentioned technical problem, the technical solution adopted in the utility model is: the skid-mounted device of a kind of novel elimination hydrogen sulfide in natural gas, coalescing separator including the drop and solid that separate more than 5um, realize natural gas is carried out re-heat intensification, ensure that gas temperature is higher than water, the heater of hydrocarbon dew point temperature, hydrogen sulfide in natural gas is carried out the membrane separator of crude separation, realize torch high sulfur-containing gas emptying being burnt or focusing on, realize the digester to a small amount of hydrogen sulfide adsorbing and removing more remaining in natural gas, realize the natural gas after processing by measuring the effusion meter being monitored, the purge gas pipe network that standard compliant natural gas is carried.
Described coalescing separator is provided with differential manometer.
Bottom described digester, gas outlet is provided with dust filter unit.
Owing to adopting technique scheme, natural gas enters coalescing separator, separates drop and the solid of more than 5um, in order to blocking pipe valve instrument will not occur when running guarantee equipment. Coalescing filter arranges differential manometer, needs when pressure reduction is more than 50kpa to change Coalescence filter core, it is ensured that the separating effect of Coalescence filter core.The natural gas of elimination moisture enters back into heater, uses heater that natural gas is carried out re-heat intensification, it is ensured that gas temperature is higher than water, hydrocarbon dew point temperature 5~10 DEG C. Natural gas after heating enters membrane separator, and by the centrifugation of organic permeable membrane, the hydrogen sulfide of more than 90% is all saturated to enter arranges the torch entering emptying burning or focusing on outside infiltration gas. The natural gas of the hydrogen sulfide containing about 100~1000ppm enters digester as the tail gas of membrane separator, by a small amount of hydrogen sulfide in the desulfurizing agent adsorbed gas again of filling in digester, it is ensured that the hydrogen sulfide in natural gas content of output is less than 20ppm. Bottom digester, gas outlet filters out the desulfurizer powder being likely to carry through dust filter unit, enters effusion meter metering, controls valve through Self-operated pressure and controls desulfurization sledge pressure, and natural gas enters purge gas pipe network or local use afterwards.
The beneficial effects of the utility model are: highly integrated skid, process simplification, conveniently transport resettlement, reduce operating cost, the advantage being provided simultaneously with monitoring function.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is structural representation view of the present utility model
In figure:
1, coalescing separator 2, heater 3, membrane separator
4, torch 5, digester 6, effusion meter
7, purge gas pipe network
Detailed description of the invention
As shown in Figure 1, the skid-mounted device of a kind of novel elimination hydrogen sulfide in natural gas of this utility model, coalescing separator 1 including the drop and solid that separate more than 5um, realize natural gas is carried out re-heat intensification, ensure that gas temperature is higher than water, the heater 2 of hydrocarbon dew point temperature, hydrogen sulfide in natural gas is carried out the membrane separator 3 of crude separation, realize the torch 4 high sulfur-containing gas emptying being burnt or focusing on, realize the digester 5 to a small amount of hydrogen sulfide adsorbing and removing more remaining in natural gas, realize the natural gas after processing by measuring the effusion meter 6 being monitored, the purge gas pipe network 7 that standard compliant natural gas is carried. described coalescing separator 1 is provided with differential manometer. bottom described digester 5, gas outlet is provided with dust filter unit.
Natural gas enters coalescing separator 1, separates drop and the solid of more than 5um, in order to blocking pipe valve instrument will not occur when running guarantee equipment. Coalescing filter 1 arranges differential manometer, needs when pressure reduction is more than 50kpa to change Coalescence filter core, it is ensured that the separating effect of Coalescence filter core. The natural gas of elimination moisture enters back into heater 2, uses heater 2 that natural gas is carried out re-heat intensification, it is ensured that gas temperature is higher than water, hydrocarbon dew point temperature 5~10 DEG C. Natural gas after heating enters membrane separator 3, and by the centrifugation of organic permeable membrane, the hydrogen sulfide of more than 90% is all saturated to enter arranges the torch 4 entering emptying burning or focusing on outside infiltration gas. The natural gas of the hydrogen sulfide containing about 100~1000ppm enters digester 5 as the tail gas of membrane separator 3, by a small amount of hydrogen sulfide in the desulfurizing agent adsorbed gas again of filling in digester 5, it is ensured that the hydrogen sulfide in natural gas content of output is less than 20ppm.Bottom digester 5, gas outlet filters out the desulfurizer powder being likely to carry through dust filter unit, enters effusion meter 6 and measures, and controls valve through Self-operated pressure and controls desulfurization sledge pressure, and natural gas enters purge gas pipe network 7 or local use afterwards.
Above the skid-mounted device of a kind of novel elimination hydrogen sulfide in natural gas provided by the utility model is described in detail. Principle of the present utility model and embodiment are set forth by specific case used herein, and the explanation of above example is only intended to help to understand method of the present utility model and core concept thereof. Should be understood that the those of ordinary skill in art field, under the premise without departing from this utility model principle, it is also possible to this utility model carries out some improvement and modification, these improve and modification also falls in this utility model scope of the claims.
Claims (3)
1. the skid-mounted device of a novel elimination hydrogen sulfide in natural gas, it is characterized in that: include the coalescing separator of drop and the solid separating more than 5um, realize natural gas is carried out re-heat intensification, ensure that gas temperature is higher than water, the heater of hydrocarbon dew point temperature, hydrogen sulfide in natural gas is carried out the membrane separator of crude separation, realize torch high sulfur-containing gas emptying being burnt or focusing on, realize the digester to a small amount of hydrogen sulfide adsorbing and removing more remaining in natural gas, realize the natural gas after processing by measuring the effusion meter being monitored, the purge gas pipe network that standard compliant natural gas is carried.
2. the skid-mounted device of novel elimination hydrogen sulfide in natural gas according to claim 1, it is characterised in that: described coalescing separator is provided with differential manometer.
3. the skid-mounted device of novel elimination hydrogen sulfide in natural gas according to claim 1, it is characterised in that: bottom described digester, gas outlet is provided with dust filter unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620054429.3U CN205313486U (en) | 2016-01-20 | 2016-01-20 | Novel skid -mounted equipment of hydrogen sulfide in desorption natural gas |
Applications Claiming Priority (1)
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CN201620054429.3U CN205313486U (en) | 2016-01-20 | 2016-01-20 | Novel skid -mounted equipment of hydrogen sulfide in desorption natural gas |
Publications (1)
Publication Number | Publication Date |
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CN205313486U true CN205313486U (en) | 2016-06-15 |
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CN201620054429.3U Expired - Fee Related CN205313486U (en) | 2016-01-20 | 2016-01-20 | Novel skid -mounted equipment of hydrogen sulfide in desorption natural gas |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105505497A (en) * | 2016-01-20 | 2016-04-20 | 天津中油现代石油设备有限公司 | Novel skid-mounted equipment for removing hydrogen sulfide in natural gas |
CN106753646A (en) * | 2017-02-27 | 2017-05-31 | 西安长庆科技工程有限责任公司 | A kind of miniature liquid desulfurization skid-mounted unit containing metering and heating function |
CN107899390A (en) * | 2017-09-25 | 2018-04-13 | 江苏河海新能源股份有限公司 | A kind of de- hydrogen sulphide removing device |
CN109628185A (en) * | 2019-01-15 | 2019-04-16 | 西安长庆科技工程有限责任公司 | A kind of desulfurization integrated integrating device of intelligence well head and method |
-
2016
- 2016-01-20 CN CN201620054429.3U patent/CN205313486U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105505497A (en) * | 2016-01-20 | 2016-04-20 | 天津中油现代石油设备有限公司 | Novel skid-mounted equipment for removing hydrogen sulfide in natural gas |
CN106753646A (en) * | 2017-02-27 | 2017-05-31 | 西安长庆科技工程有限责任公司 | A kind of miniature liquid desulfurization skid-mounted unit containing metering and heating function |
CN107899390A (en) * | 2017-09-25 | 2018-04-13 | 江苏河海新能源股份有限公司 | A kind of de- hydrogen sulphide removing device |
CN109628185A (en) * | 2019-01-15 | 2019-04-16 | 西安长庆科技工程有限责任公司 | A kind of desulfurization integrated integrating device of intelligence well head and method |
CN109628185B (en) * | 2019-01-15 | 2024-08-02 | 西安长庆科技工程有限责任公司 | Intelligent wellhead desulfurization integrated device and method |
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Date | Code | Title | Description |
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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: 20160615 Termination date: 20190120 |