CN109179334A - A kind of submersible decompression chamber gas is without oil purification processes - Google Patents
A kind of submersible decompression chamber gas is without oil purification processes Download PDFInfo
- Publication number
- CN109179334A CN109179334A CN201811137749.5A CN201811137749A CN109179334A CN 109179334 A CN109179334 A CN 109179334A CN 201811137749 A CN201811137749 A CN 201811137749A CN 109179334 A CN109179334 A CN 109179334A
- Authority
- CN
- China
- Prior art keywords
- air
- compressed air
- oil
- stpe
- decompression chamber
- Prior art date
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- 230000006837 decompression Effects 0.000 title claims abstract description 18
- 238000000746 purification Methods 0.000 title claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 23
- 239000000203 mixture Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000001816 cooling Methods 0.000 claims abstract description 10
- 238000004140 cleaning Methods 0.000 claims abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 5
- 238000000926 separation method Methods 0.000 claims description 10
- 238000001914 filtration Methods 0.000 claims description 9
- 238000001179 sorption measurement Methods 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 238000005238 degreasing Methods 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 4
- 229910021536 Zeolite Inorganic materials 0.000 claims description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 3
- 239000002808 molecular sieve Substances 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 3
- 239000010457 zeolite Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 abstract description 8
- 239000002245 particle Substances 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 6
- 150000002430 hydrocarbons Chemical class 0.000 description 6
- 239000012535 impurity Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 210000005260 human cell Anatomy 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/047—Pressure swing adsorption
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
- C01B13/0262—Physical processing only by adsorption on solids characterised by the adsorbent
- C01B13/0266—Carbon based materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
- C01B13/0262—Physical processing only by adsorption on solids characterised by the adsorbent
- C01B13/027—Zeolites
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Materials Engineering (AREA)
- Drying Of Gases (AREA)
Abstract
The invention discloses a kind of submersible decompression chamber gases without oil purification processes, ten equipment relevant to air cleaning such as water cooling, water-oil separating, preposition air reservoir, high efficiency particle air filter, cooling driers, thick air filter, smart air filter, high-precision air filter, postposition air reservoir and active carbon adsorber are configured by the air supply system for submersible decompression chamber, the purpose removed and compress the liquid mixtures such as aerial oil, water is realized with this, ensures that submersible decompression chamber obtains oil-free gas supply effect with this.
Description
Technical field
The present invention relates to submersible decompression chamber field, specially a kind of submersible decompression chamber gas is without oil purification processes.
Background technique
Submersible decompression chamber mainly establishes pressure in cabin using compressed air and compressed air is used to carry out ventilation in cabin.
The air compressor machine that submersible decompression chamber uses is mostly to have oil lubrication type, and therefore, compressed air contains a large amount of oil vapour, especially uses
After a period of time, the oil vapour in compressed air can be more.Oil vapour is existed in the form of total hydrocarbon, under stress
Density will increase, and total hydrocarbon can generate a degree of damage to human body.
In the past, the total hydrocarbon content in diver's breathing gas as defined in national regulation was no more than 0.05mg/
m3, according to These parameters are difficult to realize at present for the gas supply cleaning equipment of submersible decompression chamber configuration, especially equipment operation is several
Realize that this index can be more difficult after time.According to measurement, the filtering element for air filter that a normal use period is 6000 hours,
Not pass through compressed air pretreatment system processing in the state of, when using 1000 it is small when after, the oil vapour of compressed air contains
Amount can reach every cubic metre of 0.1mg or more.Total hydrocarbon in compressed air can produce human cell membrane strong
Therefore toxicity damage realizes that oil-free gas supply has extremely important meaning to the health of diver.
Summary of the invention
The technical problem to be solved by the present invention is to overcome the existing defects, provides a kind of submersible decompression chamber gas without oil purification
Method comprises the steps of:
The pretreatment of Step.1 compressed air；Start air compressor machine, the compressed air of output is after water cooler by gas
Temperature is reduced to 35 DEG C hereinafter, then by oil water separator, separates to the mixture in compressed air, in compressed air
Mixtures of impurities by entering preposition air reservoir after initial gross separation, precipitate with separate after enter high-efficiency degreasing device；
The filtering of Stpe.2 multi-staged air；Enter cooling driers by the pretreated compressed air of compressed air system to carry out
After so that compressed air temperature is reduced to 2-3 DEG C, it is empty to enter back into thick air filter, smart air filter and superfinishing for low-temperature treatment
Air filter carries out gas deep purifying, then carries out precipitation and separation by postposition air reservoir.
Stpe.3 adsorption cleaning；Active carbon adsorber, purification need to be entered through postposition air reservoir treated compressed air
Compressed air afterwards can enter adsorption tower and implement oxygen separation for zeolite molecular sieve；
Stpe.4PSA oxygen；
The filtering material of high speed oil expeller in the Stpe.2 uses superfine fibre.
The volume of preposition air reservoir and postposition air reservoir in the Stpe.1 and Stpe.2 should be equal to PSA oxygenerator
Single-machine capacity is divided by 5 or 6.
Compared with prior art, the beneficial effects of the present invention are: by configuring water cooling for the air supply system of submersible decompression chamber
But, water-oil separating, preposition air reservoir, high efficiency particle air filter, cooling driers, thick air filter, smart air filter, high-precision
The equipment relevant to air cleaning of air filter, postposition air reservoir and active carbon adsorber etc. ten, realizes removing with this
The purpose of the liquid mixtures such as aerial oil, water is compressed, ensures that submersible decompression chamber obtains oil-free gas supply effect with this.
Detailed description of the invention
Fig. 1 is compressed air purifying flow diagram of the invention；
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.The present invention provides a kind of technical solution: as shown in Figure 1, a kind of submersible decompression chamber
Gas is comprised the steps of without oil purification processes:
The pretreatment of Step.1 compressed air；Start air compressor machine, the compressed air of output is after water cooler by gas
Temperature is reduced to 35 DEG C hereinafter, then by oil water separator, separates to the mixture in compressed air, in compressed air
Mixtures of impurities by entering preposition air reservoir after initial gross separation, precipitate with separate after enter high-efficiency degreasing device；Compression is empty
The degree of air cooling, compressed air temperature is lower, and the degree of water-oil separating will be better, conversely, will be poorer；In compressed air
Total hydrocarbon and compressed air in moisture content and dust granules mix to form liquid mixture, in compressed air
Temperature reduce, the easier precipitation and separation of these liquid mixtures.
PSA oxygenerator requires freeze drier air outlet temperature to be reduced to 2-3 DEG C, realizes that this temperature index need to will freeze
The air inlet temperature of drying machine can control at 45 DEG C or less.The air inlet temperature of freeze drier such as exceeds 45 DEG C, freeze-drying
The air outlet temperature of machine will increase therewith.Under standard state, freeze drier air inlet temperature is higher, the temperature of gas outlet
It will be higher.Minimum 80 DEG C of air compressor machine outlet temperature, the air inlet temperature of lyophilizer requires control at 45 DEG C hereinafter, temperature
If not can be carried out effective cooling processing for 80 DEG C of compressed airs, the liquid mixture in compressed air has been impossible to
Clear all, this is the normality phenomenon of current submersible decompression chamber gas supply purification system.Compressed air is being entered cooling driers by the present invention
It is pre-processed before, reduces compressed air temperature within 35 DEG C, and the mixtures such as oil, water in compressed air are reduced
To the level of 20-30%, in this way, laying the foundation for freeze drier and subsequent air filter, total hydrocarbon control can be made
Make the level for being no more than 1mg at every cubic metre.
The filtering of Stpe.2 multi-staged air；Enter cooling driers by the pretreated compressed air of compressed air system to carry out
After so that compressed air temperature is reduced to 2-3 DEG C, it is empty to enter back into thick air filter, smart air filter and superfinishing for low-temperature treatment
Air filter carries out gas deep purifying, then carries out precipitation and separation by postposition air reservoir.It is general main logical to intercept filtering
It crosses the prior art: directly intercepting, inertial collision, Blang's diffusion mechanism is good to tiny particles content collecting effect but windage is big, is
Acquisition high purification efficiency, filter core need fine and close simultaneously to regularly replace.Compressed air passes through air filter for liquid water, liquid
Oil droplet is separated, and filters off the dust in air and solid impurity.Particulate in air removal technology mainly have mechanical filter,
Absorption, electrostatic precipitation, anion and plasma method and the filtering of electrostatic electret etc..Mechanical Adsorption is the high surface area using material
And porous structure captures particulate pollutant, it is easy to it blocks, it is more significant for gas pollutant removal effect；Gas flow rate is got over
Fastly, the precipitated form of compressed air liquid mixture is poorer, otherwise better.Twice compression is arranged in the present invention in air supply system
Air cushion tank, with this ensure compressed air on stream can by the compressed air surge tank residence time as much as possible,
The effect for reducing flow velocity is played with this.High-efficiency degreasing device in the present invention is the filter material based on superfine fibre, has oil removing, removes
Dirt ability and certain dehumidification drying capacity；Air coarse filter can remove≤1 μm of dirt particle diameter；Under standard state, it can make
Level of the compressed air oil content processing to≤0.25ppm；Air fine filter can make dust-laden particle diameter≤0.1 μm；Oil content
≤0.001ppm；Air ultraprecise filter can make dust-laden particle diameter≤0.1 μm；Oil content≤0.0001ppm.
Stpe.3 adsorption cleaning；Active carbon adsorber, purification need to be entered through postposition air reservoir treated compressed air
Compressed air afterwards can enter adsorption tower and implement oxygen separation for zeolite molecular sieve；
Stpe.4PSA oxygen；
The filtering material of high speed oil expeller in the Stpe.2 uses superfine fibre.
The volume of preposition air reservoir and postposition air reservoir in the Stpe.1 and Stpe.2 should be equal to PSA oxygenerator
Single-machine capacity is divided by 5 or 6.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
A variety of variations, modification, replacement can be carried out to these embodiments without departing from the principles and spirit of the present invention by understanding
And modification, the scope of the present invention is defined by the appended.
Claims (3)
1. a kind of submersible decompression chamber gas is comprised the steps of without oil purification processes:
The pretreatment of Step.1 compressed air；Start air compressor machine, the compressed air of output is after water cooler by gas temperature
35 DEG C are reduced to hereinafter, separate then by oil water separator to the mixture in compressed air, it is miscellaneous in compressed air
Matter mixture pass through initial gross separation after enter preposition air reservoir, precipitate with separate after enter high-efficiency degreasing device；
The filtering of Stpe.2 multi-staged air；Enter cooling driers by the pretreated compressed air of compressed air system and carries out low temperature
Processing after so that compressed air temperature is reduced to 2-3 DEG C, enters back into thick air filter, smart air filter and superfinishing air mistake
Filter carries out gas deep purifying, then carries out precipitation and separation by postposition air reservoir；
Stpe.3 adsorption cleaning；Active carbon adsorber need to be entered through postposition air reservoir treated compressed air, it is purified
Compressed air can enter adsorption tower and implement oxygen separation for zeolite molecular sieve；
Stpe.4 PSA oxygen.
2. a kind of submersible decompression chamber gas according to claim 1 is without oil purification processes, it is characterised in that: the Stpe.2
In high speed oil expeller filtering material use superfine fibre.
3. a kind of submersible decompression chamber gas according to claim 1 is without oil purification processes, it is characterised in that: the Stpe.1
PSA oxygenerator single-machine capacity should be equal to divided by 5 or 6 with the volume of preposition air reservoir and postposition air reservoir in Stpe.2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811137749.5A CN109179334A (en) | 2018-09-28 | 2018-09-28 | A kind of submersible decompression chamber gas is without oil purification processes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811137749.5A CN109179334A (en) | 2018-09-28 | 2018-09-28 | A kind of submersible decompression chamber gas is without oil purification processes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109179334A true CN109179334A (en) | 2019-01-11 |
Family
ID=64907672
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811137749.5A Withdrawn CN109179334A (en) | 2018-09-28 | 2018-09-28 | A kind of submersible decompression chamber gas is without oil purification processes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109179334A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112100815A (en) * | 2020-08-14 | 2020-12-18 | 西安工程大学 | Surface air cooler series design method for air compressor air inlet pretreatment |
-
2018
- 2018-09-28 CN CN201811137749.5A patent/CN109179334A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112100815A (en) * | 2020-08-14 | 2020-12-18 | 西安工程大学 | Surface air cooler series design method for air compressor air inlet pretreatment |
| CN112100815B (en) * | 2020-08-14 | 2024-04-16 | 西安工程大学 | Surface cooler serialization design method for air compressor air inlet pretreatment |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190111 |
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| WW01 | Invention patent application withdrawn after publication |