CN102029098B - Adsorption tower for testing - Google Patents
Adsorption tower for testing Download PDFInfo
- Publication number
- CN102029098B CN102029098B CN 201010527340 CN201010527340A CN102029098B CN 102029098 B CN102029098 B CN 102029098B CN 201010527340 CN201010527340 CN 201010527340 CN 201010527340 A CN201010527340 A CN 201010527340A CN 102029098 B CN102029098 B CN 102029098B
- Authority
- CN
- China
- Prior art keywords
- adsorption tower
- tank body
- gas
- support
- test
- 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
Images
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
The invention provides an adsorption tower for testing. The adsorption tower comprises a tank for containing an adsorbent, a bracket for supporting the tank and a gas flow control device, wherein the bracket is provided with a structure arranged on a working surface, and the tank is provided with a gas inlet and a gas outlet which are connected with gas pipelines. The flow of inlet gas can be controlled by a flowmeter, and the purifying effect of the adsorbent on coke oven gas can be determined by analyzing the coke oven gas at the gas inlet and the gas outlet after operating for a specific period of time, thereby providing an effective design reference and detailed data support of purification parameters for the construction of the adsorption tower.
Description
Technical field
The present invention relates to the gas turbine field, more specifically, relate to a kind of adsorption tower for test.
Background technology
Gas turbine is most of to adopt the coke-stove gas gas that acts as a fuel, but the impurity content in the coke-stove gas is a lot, such as solid-state dust, aqueous water, alkali metal, tar, element sulphur etc.After the gas turbine fuel system supercharging, be guaranteed the uptime of combustion machine (being gas turbine), just must process the objectionable impurities in the coke-stove gas, this processing is normally finished by adsorption tower.
At present, the design and use of adsorption tower are by rule of thumb, with reference to the behaviour in service of other similar adsorption towers.Because the pressure of the employed coal gas of each adsorption tower differs larger, it is larger that the component of coal gas and content also differ, if just simply with reference to the behaviour in service of other similar adsorption towers, then before adsorption tower uses, practical function and purification parameter to adsorption tower do not have detailed Data support, adsorption tower and the actual behaviour in service of design differ larger, therefore cause in the turbine power plant that has now moved, and the operational effect of a lot of gas turbines is unsatisfactory.
Adsorption tower is generally the equipment of large-scale complexity, and about 2 meters of diameters are high about 5 meters, needs the pipeline of various connections and a large amount of construction.If the adsorption tower after building up and actual requirement differ larger, the old adsorption tower and rebuild new adsorption tower and then can bring the raising of cost, the prolongation of duration of dismantling.And, adsorption tower is main equipment, the behaviour in service that relates to is complicated and changeable, not just can simulate by simple chemical test tube and simple chemical devices, therefore, how to measure adsorbent to the clean-up effect of coke-stove gas, so for the detailed Data support of building adsorption tower and effective design reference being provided and purifying parameter be a difficult problem of needing solution badly.
Secondly, existing adsorption tower also only rests on the adsorption tower that simple adsorbent is coke, and is undesirable for the clean-up effect of coke-stove gas.
Summary of the invention
The present invention aims to provide a kind of adsorption tower for test, is difficult to measure the clean-up effect of the coke-stove gas that adsorbent uses specific gas turbine and the problem of changing the adsorbent inconvenience to solve prior art.And then the detailed Data support that effective design reference is provided and purifies parameter for building adsorption tower.
According to the present invention, a kind of adsorption tower for test is provided, comprise: hold the tank body of adsorbent, support and the gas flow control device of support tank body, support has the structure that is arranged on the working face, and tank body is provided with fuel gas inlet and the gas outlet that is connected with fuel gas pipeline.
Further, the internal diameter of tank body greater than 50mm less than 200mm.Perhaps the height of tank body greater than 800mm less than 2000mm.
Further, the internal diameter of tank body greater than 60mm less than 100mm, the height of described tank body greater than 1000mm less than 1600mm.
Further, tank body is provided with the rotating shaft of relative support upset.
Further, also be provided with bearing pin or the bolt that tank body is located on the support.
Further, support has the structure that is arranged on movably on the working face.
Further, the structure that is arranged on movably on the working face of support is the castor of frame bottom, and castor has the structure of rolling at working face.
Further, also be provided with the brake that castor is located on the support.
Further, volume control device comprises Pressure gauge and stop valve.
Owing to adopt flowmeter control charge flow rate, after moving the specific time, measure adsorbent to the structure of the clean-up effect of coke-stove gas by the coke-stove gas analysis that combustion gas is imported and exported, and tank design becomes the structure of movable reversing, so overcome the clean-up effect problem that prior art is difficult to measure the coke-stove gas that adsorbent uses specific gas turbine, be convenient for changing simultaneously different adsorbents and test.
Description of drawings
Consist of this specification a part, be used for further understanding accompanying drawing of the present invention and show the preferred embodiments of the present invention, and be used for illustrating principle of the present invention with specification.Among the figure:
Fig. 1 shows the structure according to the adsorption tower for testing of the present invention.
Fig. 2 shows the structure according to the tank body of the adsorption tower for testing of the present invention, has wherein omitted part valve and instrument.
The specific embodiment
Need to prove that in the situation of not conflicting, embodiment and the feature among the embodiment among the application can make up mutually.Describe below with reference to the accompanying drawings and in conjunction with the embodiments the present invention in detail.
Fig. 1 shows the structure according to the adsorption tower for testing of the present invention, as shown in the figure, adsorption tower comprises: the tank body 5 that holds adsorbent, for example tank body is slender cylinder, support support 7 and the gas flow control device of tank body, support 7 has the structure that is arranged on the working face, for example is the cuboid framework, can directly or indirectly be supported on the working face, tank body 5 is provided with fuel gas inlet 1 and the gas outlet 6 that is connected with fuel gas pipeline.By flowmeter control charge flow rate, move the specific time and measure adsorbent to the clean-up effect of coke-stove gas.
Preferably, the internal diameter of tank body 5 of adsorption tower that is used for test greater than 50mm less than 200mm.So just can satisfy the condition of test.For example internal diameter is 60mm, 80mm, 100mm, 120mm, 140mm, 160mm, 180mm.
Preferably, the height of adsorption tower tank body 5 that is used for test greater than 800mm less than 2000mm.So just can satisfy the condition of test.For example highly be 900mm, 1100mm, 1300mm, 1500mm, 1700mm, 1900mm.
Preferably, the internal diameter of adsorption tower tank body 5 that is used for test greater than 60mm less than 100mm, the height of tank body 5 greater than 1000mm less than 1600mm.Internal diameter 60mm to 80mm for example, external diameter 90mm to 100mm, height 1000mm to 1300mm.Adsorbent can be better to the clean-up effect of coke-stove gas like this.
Preferably, the tank body 5 that is used for as shown in Figure 2 the adsorption tower of test is provided with the rotating shaft 4 that spins upside down for tank body 5.Support 7 is provided with the axis hole that holds rotating shaft 4, and for example rotating shaft is one section seamless steel pipe, can easily with tank body 5 reversings, pour out replacing to adsorbent.
Preferably, be used for also being provided with on the support 7 of adsorption tower of test bearing pin or bolt to tank body 5 location, bearing pin or bolt pass the locating hole that rotating shaft 4 is provided with to be come tank body 5 location, this simple for structure, is convenient to install.
Preferably, having the structure that is arranged on movably on the working face on the support 7 for the adsorption tower of testing, for example is carriage.The field condition that can adapt to like this coke-stove gas to be determined, mobile easy for installation.
Preferably, be the castor 8 of frame bottom for the structure that is arranged on movably on the working face on the support 7 of the adsorption tower of testing, castor 8 has the structure of rolling at working face.Convenient so mobile, simple for structure.
Preferably, also be provided with the brake that castor 8 is located on the support 7 for the adsorption tower of testing.After the adsorption tower of test moved to the working site, brake can lock castor 8, makes the duty of adsorption tower held stationary, worked when complete the locking of untiing brake, the again adsorption tower of easily mobile test.
Preferably, the volume control device that is used for the adsorption tower of test comprises Pressure gauge 2 and stop valve 3, with the control charge flow rate, move the specific time after, by the sample tap that combustion gas is imported and exported the survey combustion gas is taken a sample, then analyze and measure adsorbent to the clean-up effect of coke-stove gas.Certainly, the adsorption tower that is used for test can also comprise the determinator that the coke-stove gas of combustion gas import and export is analyzed, and the convenient content of measuring accurately the objectionable impurities in the coke-stove gas determines that adsorbent is to the clean-up effect of coke-stove gas.
The above is the preferred embodiments of the present invention only, is not limited to the present invention, and for a person skilled in the art, the present invention can have various modifications and variations.Within the spirit and principles in the present invention all, any modification of doing, be equal to replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (7)
1. an adsorption tower that is used for test is characterized in that, comprising: hold the support of tank body, gas flow control device and the described tank body of support of adsorbent, described tank body is provided with the rotating shaft of relative support upset; Described support has the structure that is arranged on the working face, and described tank body is provided with fuel gas inlet and the gas outlet that is connected with fuel gas pipeline; The internal diameter of described tank body greater than 50 mm less than 200 mm; The height of described tank body greater than 800 mm less than 2000 mm.
According to claim 1 for the test adsorption tower, it is characterized in that, the internal diameter of described tank body greater than 60 mm less than 100 mm, the height of described tank body greater than 1000 mm less than 1600 mm.
3. the adsorption tower for test according to claim 1 is characterized in that, also is provided with bearing pin or bolt to described tank body location on the described support.
4. the adsorption tower for test according to claim 1 is characterized in that described support has the structure that is arranged on movably on the working face.
5. the adsorption tower for test according to claim 4 is characterized in that the structure that is arranged on movably on the working face of described support is the castor of frame bottom, and described castor has the structure of rolling at working face.
6. the adsorption tower for test according to claim 5 is characterized in that, also is provided with the brake to described castor location on the described support.
7. the adsorption tower for test according to claim 1 is characterized in that described volume control device comprises Pressure gauge and stop valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010527340 CN102029098B (en) | 2010-10-29 | 2010-10-29 | Adsorption tower for testing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010527340 CN102029098B (en) | 2010-10-29 | 2010-10-29 | Adsorption tower for testing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102029098A CN102029098A (en) | 2011-04-27 |
| CN102029098B true CN102029098B (en) | 2013-01-02 |
Family
ID=43882888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010527340 Expired - Fee Related CN102029098B (en) | 2010-10-29 | 2010-10-29 | Adsorption tower for testing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102029098B (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2304461Y (en) * | 1997-07-16 | 1999-01-20 | 黄公连 | Two stage separate absorption tower for separating air to obtain richened nitrogen |
| US20040084793A1 (en) * | 2002-10-31 | 2004-05-06 | Martin Bulow | Method of forming a (CFx)n containing absorbent composition, intermediate materials employed in conducting the method and method of using the composition for preferential separation of a fluorine-containing gas from a gas stream containing the same |
| CA2732403A1 (en) * | 2008-07-30 | 2010-02-04 | Twister B.V. | System and method for removing hydrogen sulfide from a natural gas stream |
| JP5313737B2 (en) * | 2009-03-26 | 2013-10-09 | 東京瓦斯株式会社 | Mixed gas supply device and composition variation adjustment method in mixed gas supply device |
-
2010
- 2010-10-29 CN CN 201010527340 patent/CN102029098B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN102029098A (en) | 2011-04-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| MY163720A (en) | Apparatus and method for detecting and quantifying leakage in a pipe | |
| CN102029098B (en) | Adsorption tower for testing | |
| CN201281641Y (en) | Device for measuring pressure of glass kiln | |
| CN202066840U (en) | Active carboncoal absorbent absorption performance test device | |
| CN210639118U (en) | Online continuous monitoring device for hydrogen chloride in flue gas | |
| CN204782996U (en) | Stratum leakage analogue means | |
| CN204261502U (en) | A kind of blast furnace and coal gas of converter analyzer sample gas filter | |
| CN202869970U (en) | Novel ultraviolet-ray analyzer | |
| CN202144735U (en) | Non-power well head medicine-adding and gas-collecting device | |
| CN204522677U (en) | A kind of VOCs treatment NACF filter cylinder | |
| CN202794141U (en) | Device for testing adsorption effect of porous carbon on sewage | |
| CN202928844U (en) | Anti-pollution water taking device | |
| CN204170528U (en) | A kind of industrial waste-gas purifier | |
| CN104667703A (en) | Combination system for adsorbing sulfur dioxide in flue gas by virtue of activated carbon | |
| CN105842368A (en) | Air purifying device for gas chromatograph | |
| CN203148820U (en) | Reaction material sieving device for permeable reaction wall | |
| CN203562266U (en) | Oil conservator | |
| CN201150842Y (en) | Fume gas desulfurization fouling monitoring device | |
| CN204855451U (en) | Chemical plant toxic gas detection device | |
| CN204085989U (en) | Coke-oven gas device for filtering impurities | |
| CN203540124U (en) | Normal pressure airtight chromatography device | |
| CN204594870U (en) | A kind of diffusion-absorption device being applicable to mensuration AVS and SEM | |
| CN203938684U (en) | For the antiplugging apparatus of blast furnace gas sampling | |
| CN103234889A (en) | Screening device for permeable reactive material of reactive barrier | |
| CN204086229U (en) | A kind of transformer oil chromatographic on-line monitoring special-purpose air generator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130102 Termination date: 20171029 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |