CN108120506A - Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems - Google Patents
Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems Download PDFInfo
- Publication number
- CN108120506A CN108120506A CN201611056526.7A CN201611056526A CN108120506A CN 108120506 A CN108120506 A CN 108120506A CN 201611056526 A CN201611056526 A CN 201611056526A CN 108120506 A CN108120506 A CN 108120506A
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- double
- compressed air
- inlet pipe
- systems
- combination
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- 238000010926 purge Methods 0.000 title claims abstract description 32
- 238000005516 engineering process Methods 0.000 title claims abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000007921 spray Substances 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 2
- 238000000746 purification Methods 0.000 abstract description 7
- 230000007774 longterm Effects 0.000 abstract description 5
- 230000003068 static effect Effects 0.000 abstract description 3
- 239000003643 water by type Substances 0.000 abstract description 3
- 230000000903 blocking effect Effects 0.000 abstract description 2
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000790917 Dioxys <bee> Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000000038 chest Anatomy 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052594 sapphire Inorganic materials 0.000 description 1
- 239000010980 sapphire Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01J—MEASUREMENT OF INTENSITY, VELOCITY, SPECTRAL CONTENT, POLARISATION, PHASE OR PULSE CHARACTERISTICS OF INFRARED, VISIBLE OR ULTRAVIOLET LIGHT; COLORIMETRY; RADIATION PYROMETRY
- G01J5/00—Radiation pyrometry, e.g. infrared or optical thermometry
- G01J5/0044—Furnaces, ovens, kilns
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- 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
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01J—MEASUREMENT OF INTENSITY, VELOCITY, SPECTRAL CONTENT, POLARISATION, PHASE OR PULSE CHARACTERISTICS OF INFRARED, VISIBLE OR ULTRAVIOLET LIGHT; COLORIMETRY; RADIATION PYROMETRY
- G01J5/00—Radiation pyrometry, e.g. infrared or optical thermometry
- G01J5/02—Constructional details
- G01J5/06—Arrangements for eliminating effects of disturbing radiation; Arrangements for compensating changes in sensitivity
- G01J5/068—Arrangements for eliminating effects of disturbing radiation; Arrangements for compensating changes in sensitivity by controlling parameters other than temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Spectroscopy & Molecular Physics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Radiation Pyrometers (AREA)
Abstract
The invention discloses a kind of three non-compressed airs cooling and double purging technology type high-temperature high-pressure boiler temp measuring systems, including the double purge systems of double air water systems, oil and gas separating system and light path, double air water systems include the first compressed air inlet pipe, input port, delivery outlet, the second compressed air inlet pipe, valve, tracheae and burner hearth connector, first compressed air inlet pipe is connected to tracheae left end lower part, present invention design is reasonable, it is easy to use, double air waters and oil and gas separating system, purification cooling compressed air, and cooling system is avoided to generate and freezes or blocks；Double purge systems improve light path system static air pressure to more than 400Pa, effectively prevent light path system from blocking up ash and pollution, guarantee system is run steadily in the long term.
Description
Technical field
The present invention relates to burner hearth field of temperature measurement, and in particular to three non-compressed airs cool down and double purging technology type high-temperature high-pressure pots
Stove temp measuring system.
Background technology
The situation of domestic compressed air system：It is empty to be often present with cooling compression for existing service air system
Gas carries the problem of oil gas and steam.Contaminated compressed air, which enters light path system, can generate stifled ash and light path pollution, it is impossible to
Ensure that optics temp measuring system is run steadily in the long term.Due to the optics with IP65 degree of protection being operated under harsh environments
System needs to seal installation, causes the dismounting of temp measuring system and safeguards extremely difficult.Therefore it is above-mentioned to need proposition one kind that can solve
The novel blowing of problem, the technology of purification function ensure the measurement burner hearth key position of the long-term safety of temp measuring system, stabilization
Temperature.
The content of the invention
The purpose of the present invention is to solve above-mentioned deficiency, provide the cooling of three non-compressed airs and double purging technology type high-temperature high-pressures
Boiler temp measuring system.
The purpose of the present invention is what is be achieved through the following technical solutions：
Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems, including double air water systems, Oil-gas Separation
System and the double purge systems of light path, double air water systems include the first compressed air inlet pipe, input port, delivery outlet, the second compression
Air intake duct, valve, tracheae and burner hearth connector, the first compressed air inlet pipe are connected to tracheae left end lower part, valve peace
On the right side of the first compressed air inlet pipe, input port is arranged on the left of valve, and delivery outlet is arranged on the right side of valve, the second compression
Air intake duct is mounted on top, burner hearth connector in the middle part of tracheae and is arranged on the right end of tracheae, oil and gas separating system include housing,
Oil gas valve, timer two-way switch, filter, first outlet, second outlet, top tube and down tube, first outlet and second go out
Mouth is arranged on the right side of housing, and oil gas valve is arranged on the left end of upper tube, timer two-way switch be arranged on top tube and down tube it
Between, filter is arranged in down tube, and the double purge systems of light path include terminal box combination, sheath combination, connection B combinations, connection A groups
It closes and end flanges combination, terminal box combination is connected to sheath combination left side, connection B combinations are connected to the right side of sheath combination,
Connection A combinations are connected in sheath combination, and end flanges combination is connected to connection A combinations right side.
Silk plug is provided in the middle part of tracheae.
The double purge systems of light path are circular configuration, and circular surface is evenly arranged on front side of several around center of circle inner circumferential to blowing
Tapered injection orifice ring is swept around thermometric camera lens.
Divergent shape is in tilted layout each taper spray orifice at an angle.
The present invention has following beneficial effect：
Present invention design is reasonable, easy to use, double air waters and oil and gas separating system, purification cooling compressed air, and avoids cooling down
System, which generates, to be frozen or blocks；Double purge systems improve light path system static air pressure to more than 400Pa, effectively prevent light path system
The stifled ash of system and pollution, guarantee system are run steadily in the long term.
Description of the drawings
Fig. 1 is the double purge system structure diagrams of light path of the present invention；
Fig. 2 is the oil and gas separating system shell structure figure of the present invention；
Fig. 3 is the oil and gas separating system cut-away view of the present invention；
Fig. 4 is double air water system construction drawings of the present invention；
Fig. 5 is the double purge system top views of light path of the present invention；
Fig. 6 is the double purge system side views of light path of the present invention.
Specific embodiment
The present invention is further illustrated below in conjunction with the accompanying drawings：
As shown in Figure 1, the cooling of three non-compressed airs and double purging technology type high-temperature high-pressure boiler temp measuring systems, including double air water systems
System, the double purge systems of oil and gas separating system and light path, double air water systems include the first compressed air inlet pipe 12, input port 13,
Delivery outlet 14, the second compressed air inlet pipe 15, valve 19, tracheae 20 and burner hearth connector 18, the first compressed air inlet pipe
12 are connected to 20 left end lower part of tracheae, and valve 19 is mounted on 12 right side of the first compressed air inlet pipe, and input port 13 is arranged on valve
19 left side of door, delivery outlet 14 are arranged on 19 right side of valve, and the second compressed air inlet pipe 15 is mounted on 20 middle part top of tracheae, stove
Thorax connector 18 is arranged on the right end of tracheae 20, oil and gas separating system include housing 9, oil gas valve 6, timer two-way switch 7,
Filter 8, first outlet 11, second outlet 10, upper tube 21 and down tube 22, first outlet 11 and second outlet 10 are arranged on housing
9 right side, oil gas valve 6 are arranged on the left end of upper tube 21, and timer two-way switch 7 is arranged between upper tube 21 and down tube 22,
Filter 8 is arranged in down tube 22, and the double purge systems of light path include terminal box combination 1, sheath combination 2, connection B combinations 3, connection
A combinations 4 and end flanges combination 5, terminal box combination 1 are connected to 2 left side of sheath combination, and connection B combinations 3 are connected to sheath combination
2 right side, connection A combinations 4 are connected in sheath combination 2, and end flanges combination 5 is connected to 4 right side of connection A combinations.
20 middle part of tracheae is provided with silk plug 16.
The double purge systems of light path are circular configuration, and circular surface is evenly arranged with several tapered injection orifice rings around center of circle inner circumferential
Around thermometric camera lens 23.
Divergent shape is in tilted layout each taper spray orifice at an angle.
Double air waters and oil and gas separating system, purification cooling compressed air, and cooling system is avoided to generate and freezes or blocks；It is double
Purge system improves light path system static air pressure to more than 400Pa, effectively prevents light path system from blocking up ash and pollution, ensure system
Operation steady in a long-term；Flaring purge nozzle forms temperature probe vacuum auto purification using speedup fluidics is depressured, inlays dioxy
Change carbon gas infrared radiation wavelength narrowband window sapphire glass protection glass, exclusive combined type is conveniently detached system, installation dimension
Shield is extremely easy.
In the fine taper spray orifice that the double purge system centers of light path are arranged evenly around the center of circle, in a circle of divergence expression, this
Sample when gas by spray orifice at a high speed jet-like is blown over before camera lens when, a vacuum area is will result in camera lens near-surface region
Domain can provide the working environment of a purification for optics thermometric critical component and can take away the dust of attachment here,
This purging technology is referred to as self-purification function.
Gas purging can also completely cut off the high temperature from radiation of burner hearth, and optics temp measuring system is kept to be operated in 5-40 DEG C
Under the temperature environment of left and right.
The basic principles, main features and the advantages of the invention have been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (4)
1. three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems, including double air water systems, oil gas point
From system and the double purge systems of light path, it is characterised in that：Double air water systems include the first compressed air inlet pipe, input port, defeated
Outlet, the second compressed air inlet pipe, valve, tracheae and burner hearth connector, the first compressed air inlet pipe are connected to a tracheae left side
Lower part is held, valve is mounted on the right side of the first compressed air inlet pipe, and input port is arranged on the left of valve, and delivery outlet is arranged on valve
Right side, the second compressed air inlet pipe are mounted on top, burner hearth connector in the middle part of tracheae and are arranged on the right end of tracheae, Oil-gas Separation
System include housing, oil gas valve, timer two-way switch, filter, first outlet, second outlet, top tube and down tube, first
Outlet and second outlet are arranged on the right side of housing, and oil gas valve is arranged on the left end of upper tube, and timer two-way switch is arranged on
Between top tube and down tube, filter is arranged in down tube, and the double purge systems of light path include terminal box combination, sheath combination, connection B
Combination, connection A combinations and end flanges combination, terminal box combination are connected to sheath combination left side, and connection B combinations are connected to sheath
The right side of combination, connection A combinations are connected in sheath combination, and end flanges combination is connected to connection A combinations right side.
2. three non-compressed airs cooling according to claim 1 and double purging technology type high-temperature high-pressure boiler temp measuring systems,
It is characterized in that：Silk plug is provided in the middle part of the tracheae.
3. three non-compressed airs cooling according to claim 1 and double purging technology type high-temperature high-pressure boiler temp measuring systems,
It is characterized in that：The double purge systems of the light path are circular configuration, and circular surface is evenly arranged with several around center of circle inner circumferential
Front side is to purging tapered injection orifice ring around thermometric camera lens.
4. three non-compressed airs cooling according to claim 3 and double purging technology type high-temperature high-pressure boiler temp measuring systems,
It is characterized in that：Divergent shape is in tilted layout each taper spray orifice at an angle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611056526.7A CN108120506A (en) | 2016-11-26 | 2016-11-26 | Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611056526.7A CN108120506A (en) | 2016-11-26 | 2016-11-26 | Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108120506A true CN108120506A (en) | 2018-06-05 |
Family
ID=62223621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611056526.7A Pending CN108120506A (en) | 2016-11-26 | 2016-11-26 | Three non-compressed airs cool down and double purging technology type high-temperature high-pressure boiler temp measuring systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108120506A (en) |
-
2016
- 2016-11-26 CN CN201611056526.7A patent/CN108120506A/en active Pending
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