CN201133567Y - Natural gas converter - Google Patents
Natural gas converter Download PDFInfo
- Publication number
- CN201133567Y CN201133567Y CNU2007203113223U CN200720311322U CN201133567Y CN 201133567 Y CN201133567 Y CN 201133567Y CN U2007203113223 U CNU2007203113223 U CN U2007203113223U CN 200720311322 U CN200720311322 U CN 200720311322U CN 201133567 Y CN201133567 Y CN 201133567Y
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- Prior art keywords
- valve
- pipeline
- steel cylinder
- auxiliary agent
- pressure cylinder
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Abstract
The utility model relates to a natural gas converter, which comprises an accessory ingredient pressure cylinder and a pressure cylinder. The middle of the upper part of the accessory ingredient pressure cylinder is provided with an accessory ingredient filling tube, and both sides of the upper part of the accessory ingredient pressure cylinder are provided with an inlet pipe I and an outlet pipe II. The middle of the lower part is provided with a raffinate discharge pipe I. Three barriers are distributed uniformly alternately upwards along the middle of the cylinder body inside the accessory ingredient pressure cylinder. Both sides of the upper part of the pressure cylinder are provided with an inlet pipe II and an outlet pipe II. The middle of the lower part of the pressure cylinder is provided with a raffinate discharge pipe II with three barriers distributed uniformly and alternately inside the pressure cylinder. The inlet pipe I is connected with an inlet pressure gauge through a valve, and is inserted in the accessory ingredient pressure cylinder. The accessory ingredient filling tube is provided with a valve. The inlet pipe II is inserted in the pressure cylinder, and is connected with the outlet pipe I through a valve. The outlet pipe is provided a valve outside the cylinder. The raffinate discharge pipe I and the raffinate discharge pipe II are connected with a raffinate discharge port through a valve. The utility model can improve the gas utilization efficiency.
Description
Technical field
The utility model relates to a kind of rock gas operative installations, particularly a kind of Natural Gas Conversion device.
Background technique
Rock gas is a kind of nontoxic, colourless, tasteless gas, and its Main Ingredients and Appearance is a methane, and its lower calorific value is 34.91MJ/Nm
3The density of rock gas (methane) is 0.7174Kg/Nm during 101.352KPa at 0 ℃
3, relative density (density of establishing air is 1) is 0.5548, than air approximately light half.Need a large amount of air for supporting combustions, 1m during rock gas perfect combustion
3Rock gas perfect combustion approximately needs 9.52m
3Air; If incomplete combustion then can produce the toxic gas carbon monoxide.
In order to give full play to the effect of rock gas cleaning, the safe energy, rock gas is fully burnt, reduce carbon monoxide emission, improve the combustion of natural gas calorific value simultaneously, in the hope of reaching the saving gas consumption, solve the purpose of rock gas imbalance between supply and demand, be badly in need of a kind of equipment that improves gas utilization efficient, and do not have this series products in the market.
The model utility content
Technical problem to be solved in the utility model provides a kind of Natural Gas Conversion device that can improve gas utilization efficient.
For addressing the above problem, a kind of Natural Gas Conversion device described in the utility model is characterized in that: it comprises auxiliary agent pressure steel cylinder (1) and pressure steel cylinder (2); Be provided with auxiliary agent in the middle of described auxiliary agent pressure steel cylinder (1) top and fill pipe (5), both sides are respectively equipped with input pipeline I (3) and output pipeline I (4), be provided with residual liquid discharge pipeline I (6) in the middle of the bottom, its inside even staggered floor that makes progress along the bottle middle part is distributed with three dividing plates (7); Described pressure steel cylinder (2) both sides, top are respectively equipped with input pipeline II (8) and output pipeline II (9), are provided with residual liquid discharge pipeline II (10) in the middle of the bottom, and its inner evenly staggered floor is distributed with three dividing plates (7); Described input pipeline I (3) links to each other with input air pressure power table (12) by valve (11), and inserts in the described auxiliary agent pressure steel cylinder (1); Described auxiliary agent fills pipe (5) and is provided with valve (11); Described input pipeline II (8) inserts in the described pressure steel cylinder (2) and with described output pipeline I (4) and links to each other by valve (11); Described output pipeline II (9) is provided with valve (11) outside bottle; Described residual liquid discharge pipeline I (6) links to each other with residual liquid discharge mouth (13) by valve (11) with residual liquid discharge pipeline II (10).
Described dividing plate is provided with 5% the gradient.
The utility model compared with prior art has the following advantages:
1, improved the natural gas burning flame temperature.Under the natural air state, the natural gas burning flame temperature is between 400～500 °, under oxygen hybrid working state, the natural gas burning flame temperature is between 1900～2100 °, and the combustion of natural gas flame temperature behind employing the utility model is respectively between 800～900 ° and between 3500～4300 °.
2, improved the natural gas burning calorific value.Under the natural air state, the combustion heat value of every cubic natural gas is between 8000～8700 kilocalories, under oxygen hybrid working state, the combustion heat value of every cubic natural gas is between 38000～45000 kilocalories, and the combustion of natural gas calorific value behind employing the utility model is respectively between 14000～17000 kilocalories and between 90000～110000 kilocalories.
3, the rock gas builder that the utility model adopted is a kind of nontoxic, and is tasteless, do not burn, inexplosive safe and reliable chemical assistant (liquid).Not free, not stratified after this auxiliary agent and rock gas fully react, in stable condition lasting, thus rock gas is fully burned, reduce noxious gas emission, improve explosion limit, guarantee the cleaning of natural gas and strengthened Security.
4, improve gas utilization efficient, save natural gas energy resource consumption.Owing to adopt combustion of natural gas temperature and calorific value behind the utility model all to be improved, thereby some operational sites that need the high-temperature higher calorific value all can be used, promptly saved cost, safe and reliable again, save natural gas energy resource consumption simultaneously, can solve the contradiction of the present natural gas supply deficiency of China.
5, because the dividing plate that the utility model is adopted in bottle has certain gradient, therefore not only can avoid auxiliary agent to remain on the dividing plate, but also can avoid in the auxiliary agent pressure steel cylinder because the moisture that gas-liquid reaction produced rising.
6, the utility model is simple in structure, need not electric energy and other power, only depends on rock gas self pressure, just can finish, and its throughput can reach per hour 20～800m
3
Description of drawings
Below in conjunction with accompanying drawing embodiment of the present utility model is described in further detail.
Fig. 1 is a structural representation of the present utility model.
1-auxiliary agent pressure steel cylinder 2-pressure steel cylinder 3-input pipeline I 4-output pipeline I
The 5-auxiliary agent fills pipe 6-residual liquid discharge pipeline I 7-dividing plate 8-input pipeline II
9-output pipeline II 10-residual liquid discharge pipeline II 11-valve 12-input air pressure power table
13-residual liquid discharge mouth
Embodiment
As shown in Figure 1, a kind of Natural Gas Conversion device, it comprises auxiliary agent pressure steel cylinder 1 and pressure steel cylinder 2.
Be provided with auxiliary agent in the middle of auxiliary agent pressure steel cylinder 1 top and fill pipe 5, both sides are respectively equipped with input pipeline I 3 and output pipeline I 4, are provided with residual liquid discharge pipeline I 6 in the middle of the bottom, and its inside even staggered floor that makes progress along the bottle middle part is distributed with three dividing plates 7.
Both sides, pressure steel cylinder 2 top are respectively equipped with input pipeline II 8 and output pipeline II 9, are provided with residual liquid discharge pipeline II 10 in the middle of the bottom, and its inner evenly staggered floor is distributed with three dividing plates 7.
Input pipeline I 3 links to each other with input air pressure power table 12 by valve 11, and inserts in the auxiliary agent pressure steel cylinder 1; Auxiliary agent fills pipe 5 and is provided with valve 11; Input pipeline II 8 inserts in the described pressure steel cylinder 2 and with described output pipeline I 4 and links to each other by valve 11; Output pipeline II 9 is provided with valve 11 outside bottle; Residual liquid discharge pipeline I 6 links to each other with residual liquid discharge mouth 13 by valve 11 with residual liquid discharge pipeline II 10.
All dividing plates 7 are equipped with 5% the gradient.
Input pipeline I 3 does not contact with bottle body bottom in bottle fully with input pipeline II 8.
During use, under passive state, open auxiliary agent and fill the valve 11 of pipe on 5, auxiliary agent is filled from auxiliary agent mouthful pour in the auxiliary agent pressure steel cylinder 1, at the bottom of auxiliary agent enters bottle by dividing plate 7, throttle down 11.Pipe natural gas or compressed natural gas are connected with rock gas synergy transducer by pipeline, with input air pressure power table 12 gas pressure is controlled in 0.1～0.6MPa scope, open the valve 11 that links to each other with pressure gauge 12, rock gas is input in the auxiliary agent pressure steel cylinder 1 by input pipeline I 3.
After rock gas entered, bottom at the bottom of gas utilization self pressure enters bottle was stirred and is fully reacted with builder in the steel cylinder.When liquid rolled upwards, minimum one deck dividing plate 7 barrier liquids upwards rolled in the steel cylinder; When the liquid that splashes makes progress, stopped by a middle faulted layer dividing plate 7 and last layer staggered floor dividing plate 7.After reaction was finished, gas was entered the pressure steel cylinder 2 by input pipeline II 8 from valve 11 by output pipeline I 4.
Owing to also containing small amount of moisture in the gas that enters pressure steel cylinder 2, by the prevention of three faulted layer dividing plates 7, moisture content is deposited to bottle body bottom; Gas then enters rock gas by valve 11 and uses main pipe from output pipeline II 9.
After the builder effective ingredient in the auxiliary agent pressure steel cylinder is fully used up, close input pipeline I valve 11 and output pipeline II valve 11, open auxiliary agent and fill the valve 11 of managing on 5, discharge residual air, there is not when pressure in the steel cylinder, open the valve 11 of residual liquid discharge pipeline I 6 and residual liquid discharge pipeline II 10, raffinate is discharged by residual liquid discharge mouth 13.
Working principle of the present utility model, be to utilize gas flow characteristic, after rock gas and builder are fully mixed, reach mutually dissolving fully, not free, not stratified, evenly gasify in company with rock gas, form new gaseous compound, combustion efficiency is stable, make rock gas under the natural air state and add under the oxygen condition, its flame temperature and combustion heat value double than raw natural gas.
The utility model can adopt gas chemical industry's auxiliary agent.
Auxiliary agent pressure steel cylinder 1 and pressure steel cylinder 2 in the utility model all adopt diameter 250～500mm, and height 1000～1800mm, carrying pressure maximum are the steel cylinder of 1.6MPa.Valve adopts can carry the Flange Ball Valves that pressure maximum is 1.6MPa.
The utility model can be used for rock gas is had the terminal use of user demand: steel-making, generating, industry cutting, heat supply, provide natural gas supply station etc. for oneself.
Claims (2)
1, a kind of Natural Gas Conversion device is characterized in that: it comprises auxiliary agent pressure steel cylinder (1) and pressure steel cylinder (2); Be provided with auxiliary agent in the middle of described auxiliary agent pressure steel cylinder (1) top and fill pipe (5), both sides are respectively equipped with input pipeline I (3) and output pipeline I (4), be provided with residual liquid discharge pipeline I (6) in the middle of the bottom, its inside even staggered floor that makes progress along the bottle middle part is distributed with three dividing plates (7); Described pressure steel cylinder (2) both sides, top are respectively equipped with input pipeline II (8) and output pipeline II (9), are provided with residual liquid discharge pipeline II (10) in the middle of the bottom, and its inner evenly staggered floor is distributed with three dividing plates (7); Described input pipeline I (3) links to each other with input air pressure power table (12) by valve (11), and inserts in the described auxiliary agent pressure steel cylinder (1); Described auxiliary agent fills pipe (5) and is provided with valve (11); Described input pipeline II (8) inserts in the described pressure steel cylinder (2) and with described output pipeline I (4) and links to each other by valve (11); Described output pipeline II (9) is provided with valve (11) outside bottle; Described residual liquid discharge pipeline I (6) links to each other with residual liquid discharge mouth (13) by valve (11) with residual liquid discharge pipeline II (10).
2, a kind of Natural Gas Conversion device as claimed in claim 1, it is characterized in that: described dividing plate (7) is provided with 5% the gradient.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007203113223U CN201133567Y (en) | 2007-12-07 | 2007-12-07 | Natural gas converter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007203113223U CN201133567Y (en) | 2007-12-07 | 2007-12-07 | Natural gas converter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201133567Y true CN201133567Y (en) | 2008-10-15 |
Family
ID=40061839
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007203113223U Expired - Fee Related CN201133567Y (en) | 2007-12-07 | 2007-12-07 | Natural gas converter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201133567Y (en) |
-
2007
- 2007-12-07 CN CNU2007203113223U patent/CN201133567Y/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081015 Termination date: 20131207 |