CN206214998U - A kind of heat-engine plant desulfurized compressed air drier - Google Patents

A kind of heat-engine plant desulfurized compressed air drier Download PDF

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Publication number
CN206214998U
CN206214998U CN201621145164.4U CN201621145164U CN206214998U CN 206214998 U CN206214998 U CN 206214998U CN 201621145164 U CN201621145164 U CN 201621145164U CN 206214998 U CN206214998 U CN 206214998U
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CN
China
Prior art keywords
compressed air
drier
main pipeline
oil
heat
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Expired - Fee Related
Application number
CN201621145164.4U
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Chinese (zh)
Inventor
聂鹏飞
张宏宇
王洋
王学斌
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Hebei Datang International Wangtan Power Generation Co Ltd
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Hebei Datang International Wangtan Power Generation Co Ltd
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Priority to CN201621145164.4U priority Critical patent/CN206214998U/en
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Publication of CN206214998U publication Critical patent/CN206214998U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

A kind of heat-engine plant desulfurized compressed air drier, belongs to heat-engine plant desulfurized equipment technical field, for the treatment to wet desulphurization compressed air.Its technical scheme is:Air compressor machine is connected with compressed air reservoir by main pipeline, compressed air reservoir is linked in sequence with oil strainer, drier, dirt filter by main pipeline, oil water separator is arranged on the main pipeline between compressed air reservoir delivery outlet and oil strainer, and drier inlet valve is installed on the main pipeline between oil water separator and compressed air reservoir.The utility model structure setting is scientific and reasonable, and compressed air first passes through compressed air reservoir, mitigates the live load of drying equipment thereafter, the equipment such as oil water separator and automatic water trap can be used for compressed air into the aqueous water before drier from.The utility model is stable, improves the drying effect of compressed air, effectively reduces compressed air dew-point temperature, reduces because of the excessive equipment fault for bringing of compressed air moisture.

Description

A kind of heat-engine plant desulfurized compressed air drier
Technical field
The utility model is related to a kind of heat-engine plant desulfurized compressed air drier, belongs to heat-engine plant desulfurized equipment and technology neck Domain.
Background technology
In heat-engine plant wet desulfurization, it is pneumatic that wet desulphurization device widely uses pneumatic control valve, flue gas analyzer etc. Part, hundreds of, its compressed air drying system uses traditional process mode to terminal gas point.But because part Drying device system design is unreasonable, compressed air drying effect on driving birds is not good, deep always to be stranded by compressed air for instrument entraining water problem Disturb, frequently, especially in the winter time, compressed air condensation water quantity is greatly increased the unit failure such as pneumatic control valve magnetic valve, cylinder, Compressed air table pipe even main pipeline icing phenomenon often occurs, and source of the gas off and on, causes outdoor atmospheric control basic It is in paralyzed state, have a strong impact on the using effects such as desulphurization plant, instrument.Current heat-engine plant desulfurized compressed air drier master The problem to be existed is:
(1)Compressed air design cycle not science, existing equipment mainly has air compressor machine, oil strainer, drier, dirt mistake Filter, compressed air reservoir, traditional flow are air compressor machine → oil strainer → drier → dirt filter → compressed airs Air accumulator, air compressor machine discharge compressed air first passes through drying and enters back into compressed air reservoir, but air compressor machine has just discharged compression Air do not have preliminary liquid qi leel from, lack aqueous water from equipment, be fitted without automatic water trap, be only provided with manually Draining valve, aqueous water can not be separated or discharged completely;
(2)Drier can only remove the gaseous state moisture content in compressed air, it is impossible to remove liquid moisture content, what compressed air was carried Liquid water content is exceeded, and it is abnormal that overload operation causes drier to work;
(3)Dry adsorbent proportioning unreasonable, cause adsorption capacity reduction or fail.
In order to improve the quality of desulfurization compressed air, the defect of pneumatic system is reduced, it is necessary to which existing thermal power plant is taken off Sulphur compressed air drier is improved.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of heat-engine plant desulfurized compressed air drier, this Device can improve the drying effect of compressed air, effectively reduce compressed air dew-point temperature, reduce because of Problem On Compressed Air With Water band The equipment fault for coming.
Solving the technical scheme of above-mentioned technical problem is:
A kind of heat-engine plant desulfurized compressed air drier, it includes air compressor machine, automatic water trap, oil strainer, drying Device, compressed air reservoir, dirt filter, air compressor machine are connected with compressed air reservoir by main pipeline, compressed air storage Gas tank is linked in sequence with oil strainer, drier, dirt filter by main pipeline, and its improvements is that it increased profit point From device, oil water separator is arranged on the main pipeline between compressed air reservoir delivery outlet and oil strainer, in water-oil separating Drier inlet valve is installed on the main pipeline between device and compressed air reservoir delivery outlet.
Above-mentioned heat-engine plant desulfurized compressed air drier, the bottom of the compressed air reservoir is provided with air accumulator row Water valve.
Above-mentioned heat-engine plant desulfurized compressed air drier, the compressed air reservoir, oil water separator, oil filtering Device, the low level of dirt filter have been respectively mounted drainpipe, and automatic water trap is provided with drainpipe.
The beneficial effects of the utility model are:
The utility model Structure and Process sets scientific and reasonable, changes the technological process of original compressed air drying so that Compressed air first passes through compressed air reservoir, obtains tentatively lowering the temperature, condenses, and then isolates the aqueous water in air, makes Part moisture and greasy dirt are deposited in compressed air reservoir bottom, mitigate the live load of drying equipment thereafter, increased profit The equipment such as separator and automatic water trap can be used for compressed air into the aqueous water before drier from
The utility model is stable, improves the drying effect of compressed air, significantly improves desulfurization compressed air Quality, effectively reduces compressed air dew-point temperature, reduces because of the excessive equipment fault for bringing of compressed air moisture.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Marked in figure as follows:Air compressor machine 1, automatic water trap 2, drainpipe 3, main pipeline 4, compressed air reservoir 5, gas storage Tank draining valve 6, drier inlet valve 7, oil water separator 8, oil strainer 9, drier 10, dirt filter 11.
Specific embodiment
The utility model is by air compressor machine 1, automatic water trap 2, drainpipe 3, main pipeline 4, compressed air reservoir 5, gas storage Tank draining valve 6, drier inlet valve 7, oil water separator 8, oil strainer 9, drier 10, dirt filter 11 are constituted.
Shown in figure, air compressor machine 1, compressed air reservoir 5, air accumulator draining valve 6, drier inlet valve 7, water-oil separating Device 8, oil strainer 9, drier 10, dirt filter 11 are connected by a compressed air main pipeline 4, and these unit Series are one Play the new compressed air drying system of composition.
Compressed air initially entered compressed air reservoir 5 before drier 10 is entered, it is necessary to the liquid for wherein carrying State water is removed completely, mitigates the grade load of oil water separator 8, and drier 10 is fully played desiccation.
Shown in figure, anterior setting air compressor machine 1 and compressed air reservoir 5 of the present utility model, air compressor machine 1 are empty with compression Gas air accumulator 5 is connected by main pipeline 4.The row of being provided with the connection main pipeline 4 of air compressor machine 1 and compressed air reservoir 5 Water pipe 3 and automatic water trap 2, the bottom of compressed air reservoir 5 set air accumulator draining valve 6.The compressed air of the discharge of air compressor machine 1 The aqueous water of middle carrying is periodically discharged by automatic water trap 2, air accumulator draining valve 6, can significantly be reduced into subsequently The aqueous water of drier.
Shown in figure, the compressed air of the discharge of compressed air reservoir 5 will be by drier inlet valve 7, drier air inlet State of the door 7 in opening, compressed air could enter drier 10.
Shown in figure, compressed air, be further across oil water separator 8, oil strainer 9 before drier 10 is entered Filtering, mainly filters out the impurity such as oil in compressed air, and oil water separator 8, oil strainer 9 are equipped with the and of drainpipe 3 Automatic water trap 2, periodically discharges the impurity being collected into.
Shown in figure, drier 10 is heatless regeneration formula drier, is provided with two adsorption tanks.In one cycle period, often Individual adsorption tower all have passed through three phases:Absorption --- regeneration --- pressurising.Each adsorption tanks places the oxygen of equal number respectively Change aluminium and molecular sieve, after the compressed air being adsorbed by drying of drier 10 is by dirt filter 11, eventually enter into terminal use Gas point.
The part-structure and model of one embodiment of the present utility model are as follows:
Main pipeline 4 is DN80 × 14000mm;
The internal diameter of compressed air reservoir draining valve 6 is DN50, model JL-500;
The model JYF-20N of oil water separator 8;
The model HF730B of oil strainer 9;
The model JWL-30 of drier 10;
The model HF530B of dirt filter 11;
The internal diameter of automatic water trap 2 is DN20, model AD-402;
Drainpipe 3 is DN20 × 500mm.

Claims (3)

1. a kind of heat-engine plant desulfurized compressed air drier, it includes air compressor machine(1), compressed air reservoir(5), oil filtering Device(9), drier(10), dirt filter(11), air compressor machine(1)With compressed air reservoir(5)By main pipeline(4)It is connected Connect, compressed air reservoir(5)With oil strainer(9), drier(10), dirt filter(11)By main pipeline(4)Order connects Connect, it is characterised in that:It increased oil water separator(8), oil water separator(8)Installed in compressed air reservoir(5)Output Mouth and oil strainer(9)Between main pipeline(4)On, in oil water separator(8)With compressed air reservoir(5)Between delivery outlet Main pipeline(4)On drier inlet valve is installed(7).
2. heat-engine plant desulfurized compressed air drier according to claim 1, it is characterised in that:The compressed air storage Gas tank(5)Bottom air accumulator draining valve is installed(6).
3. heat-engine plant desulfurized compressed air drier according to claim 1, it is characterised in that:The compressed air storage Gas tank(5), oil water separator(8), oil strainer(9), dirt filter(11)Low level be respectively mounted drainpipe(3), in draining Pipe(3)On automatic water trap is installed(2).
CN201621145164.4U 2016-10-21 2016-10-21 A kind of heat-engine plant desulfurized compressed air drier Expired - Fee Related CN206214998U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621145164.4U CN206214998U (en) 2016-10-21 2016-10-21 A kind of heat-engine plant desulfurized compressed air drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621145164.4U CN206214998U (en) 2016-10-21 2016-10-21 A kind of heat-engine plant desulfurized compressed air drier

Publications (1)

Publication Number Publication Date
CN206214998U true CN206214998U (en) 2017-06-06

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CN201621145164.4U Expired - Fee Related CN206214998U (en) 2016-10-21 2016-10-21 A kind of heat-engine plant desulfurized compressed air drier

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107575856A (en) * 2017-09-26 2018-01-12 北京泷涛环境科技有限公司 A kind of flue gas recirculation steam generator system
CN107934918A (en) * 2017-12-07 2018-04-20 湖南卓誉科技有限公司 A kind of oxygen control system processed of PSA oxygenerators

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107575856A (en) * 2017-09-26 2018-01-12 北京泷涛环境科技有限公司 A kind of flue gas recirculation steam generator system
CN107934918A (en) * 2017-12-07 2018-04-20 湖南卓誉科技有限公司 A kind of oxygen control system processed of PSA oxygenerators
CN107934918B (en) * 2017-12-07 2020-09-01 湖南卓誉科技有限公司 Oxygen generation control system of PSA oxygenerator

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GR01 Patent grant
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: 20170606

Termination date: 20191021