CN1940034A - Synergist for improving natural gas burning temperature and its apparatus - Google Patents
Synergist for improving natural gas burning temperature and its apparatus Download PDFInfo
- Publication number
- CN1940034A CN1940034A CN 200510107703 CN200510107703A CN1940034A CN 1940034 A CN1940034 A CN 1940034A CN 200510107703 CN200510107703 CN 200510107703 CN 200510107703 A CN200510107703 A CN 200510107703A CN 1940034 A CN1940034 A CN 1940034A
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- Prior art keywords
- natural gas
- pressure vessel
- gasoline
- synergistic agent
- combustion
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 239000003345 natural gas Substances 0.000 title claims abstract description 36
- 239000003502 gasoline Substances 0.000 claims abstract description 27
- KTWOOEGAPBSYNW-UHFFFAOYSA-N ferrocene Chemical compound [Fe+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KTWOOEGAPBSYNW-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000012747 synergistic agent Substances 0.000 claims description 29
- 238000002485 combustion reaction Methods 0.000 claims description 17
- 239000002994 raw material Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 abstract 1
- 235000011613 Pinus brutia Nutrition 0.000 abstract 1
- 241000018646 Pinus brutia Species 0.000 abstract 1
- 238000007664 blowing Methods 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 235000009508 confectionery Nutrition 0.000 description 13
- 239000000203 mixture Substances 0.000 description 13
- 239000000446 fuel Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000002585 base Substances 0.000 description 6
- 239000012467 final product Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000002360 explosive Substances 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- -1 ultraviolet ray Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 1
- SYWNIVZVLMPODI-UHFFFAOYSA-N C(=CC=CC)[Fe] Chemical compound C(=CC=CC)[Fe] SYWNIVZVLMPODI-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 241000723346 Cinnamomum camphora Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 239000001293 FEMA 3089 Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229960000583 acetic acid Drugs 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229960000846 camphor Drugs 0.000 description 1
- 229930008380 camphor Natural products 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000012362 glacial acetic acid Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
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Abstract
A synergist increased by natural-gas burning temperature and its apparatus are disclosed. The synergist consists of pine cone oil 45-55wt%, gasoline 40-50wt% and ferrocene 2-7wt%. The apparatus comprises pressure-proof container, which is set with air-inlet valve and outlet valve. The process is carried out by packing synergist into one device, blowing natural gas out from the bottom of device, mixing it with synergist, outputting while chemical and physical reacting and increasing burning temperature of natural gas.
Description
Technical field
The present invention relates to a kind of synergistic agent and device thereof, especially relate to a kind of synergistic agent and device thereof that the combustion of natural gas temperature is improved.
Background technology
The main ingredient of Sweet natural gas is a methane, accounts for usually more than 90%, also contains some ethane, propane, butane and pentane plus class, and non-hydrocarbons components such as a spot of carbonic acid gas, nitrogen, hydrogen sulfide, hydrogen are arranged.The relative density of Sweet natural gas: 0.55～0.75, flash-point :-218 ℃, spontaneous ignition temperature: 500～700 ℃ (typical dry gas), and Lower Explosive Limit: 3.6%～6.5%, upper explosive limit: 13%～17%, minimum ignition energy: 0.3～0.4mJ (typical dry gas); No matter industrial as industrial welding, combustion gas vehicle, still civilian, Sweet natural gas is very extensive as a kind of fuel applications, yet as welding, the natural gas burning temperature is 1900-2100 ℃ at present for industry, temperature of combustion is low, thereby the consumption of Sweet natural gas is big, and the combustion time that needs is long.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, a kind of synergistic agent that the combustion of natural gas temperature is improved is provided;
Another object of the present invention provides a kind of device that the combustion of natural gas temperature is improved.
The present invention realizes in the following way:
A kind of synergistic agent and device thereof that the combustion of natural gas temperature is improved is characterized in that: this synergistic agent is that the raw material by following volumn concentration mixes: turps 45-55%, gasoline 40-50%, ferrocene 2-7%;
The volumn concentration of described turps, gasoline, ferrocene is respectively 50%, 45%, 5%;
Described gasoline is 70# gasoline;
A kind of device that improves natural gas temperature is characterized in that: this device comprises a pressure vessel, and pressure vessel is provided with an intake valve and air outlet valve;
In described pressure vessel, be provided with an airway that links to each other with described intake valve;
The bottom of described pressure vessel is provided with a base;
Described intake valve and air outlet valve are located at the top of described pressure vessel;
Described pressure vessel is a spherical cylindrical shell.
The present invention has following effect:
In general, gasoline is divided into No. 70 and No. 85 two trades mark by motor-method octane number, be divided into No. 90, No. 93, No. 95 and four trades mark of No. 97 motor spirit by research octane number (RON), everybody classifies by research octane number (RON) by the gasoline trade mark of custom in the daily life at present.Gasoline is used as the fuel of gasoline automobile and petrol motor usually.Motor spirit is selected the gasoline of the different trades mark for use according to the height of engine compression ratio; Compression ratio is higher, can select the gasoline of higher board for use; Otherwise, then select the gasoline that hangs down the trade mark for use.Aviation spirit is then usually as piston aviation engine fuel, be divided into three trades mark No. 75, No. 95, No. 100 by research octane number (RON), only can be divided into fuel, solvent and industrial chemicals, lubricant and several big classes such as relevant product, wax, pitch, refinery coke according to production method and end-use at present at the outstanding petroleum products of blimp.Turps, English name Turpenitine; Turpentine oil is colourless extremely yellowish clear liquid; Smelly special, flavor is hot, stores for a long time or is exposed in the air, and is smelly cumulative strong, look gradual change Huang; This product is inflammable, and dense smoke takes place during burning.Easily molten in ethanol, with chloroform, ether or Glacial acetic acid can mix arbitrarily, and be molten in water.Relative density (water=1) 0.85～0.87; Relative density (air=1) 4.84; Boiling point: 154～170 ℃; Flash-point: 35 ℃; Hazard property: its steam and air form explosive mixture, and chance naked light, high heat energy cause combustion explosion.Play combustion-supporting effect among the present invention; Ferrocene: formal name used at school: biscyclo pentadienyl iron, molecular formula: (C5H5) 2Fe, ferrocene are a kind of organometallicss.Normal temperature for orange-yellow powder, has the camphor smell down.Fusing point 172 degree-174 degree, boiling point 249 degree, water insoluble, be soluble in organic solvents such as benzene, ether, gasoline, diesel oil.Do not have an effect with acid, alkali, ultraviolet ray, chemical property is stable, and 400 degree do not decompose with interior.(1) as the energy-saving and smoke-removing perfect combustion catalyzer: can be used for various fuel, as diesel oil, gasoline, heavy oil, coal etc.The ferrocene of adding 0.1% in the derv fuel oil, oily 10-14% capable of saving fuel, raising rate 10-13%, smoke intensity decline 30-80 ‰ in the tail gas.In addition, add 0.3 ‰ in heavy oil, add 0.2% ferrocene in the coal, fuel consumption is descended, simultaneously, smoke intensity descends 30%.(2) as the additive of synthetic gasoline, artificial liquefied gas: in synthetic gasoline, add ferrocene and the associated additives of 0.01-0.5%, can be made into the various artificially synthetic gasolines that are equivalent to 80#, 85#, 90#; Add 0.03% ferrocene in methyl alcohol, can be made into fuel value is the artificial liquefied gas of 3372-38656 KJ-KG; In methyl alcohol, alcoholic acid mixing solutions, add the 0.005%-0.008% ferrocene, can be made into new and effective domestic fuel.
The present invention utilizes the above-mentioned character of turps, gasoline, ferrocene, form by the intake valve and the air outlet valve that are provided with by a pressure vessel, earlier a kind of synergistic agent is gone in the pressure vessel by the intake valve jar during use, then Sweet natural gas is blown out from pressure vessel bottom with synergistic agent in it by airway by intake valve and mix, make Sweet natural gas generation physics, chemical reaction, combustion of natural gas intensity and the temperature of combustion exported from air outlet valve can improve about 35%.Sweet natural gas of the present invention is when this device and synergistic agent thorough mixing provided by the invention, under the effect of synergistic agent, combustion of natural gas is speeded up, because the effect that the dilution of terebinthine combustion-supporting effect, gasoline helps profit effect, ferrocene to improve combustionvelocity, make the natural gas burning temperature improve, the present invention improves more than the natural gas burning temperature to 3300 ℃, thus the needs of the Sweet natural gas combustion temperatures of can satisfying the demand.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Embodiment
Embodiment one: take off the raw material of stating volumn concentration and mix: turps 45%, 70# gasoline 50%, ferrocene 5%, mix and be mixed with synergistic agent, at first above-mentioned synergistic agent is poured in the device, the amount of pouring into is 1/2nd of a vessel content, then with Sweet natural gas from bottom of device blow out with install in synergistic agent mixes, export then and get final product.This device as shown in Figure 1, comprise a pressure vessel 1, pressure vessel 1 is provided with an intake valve 2 and air outlet valve 3, is provided with an airway 4 that links to each other with intake valve 2 in pressure vessel 1, the bottom of pressure vessel 1 is provided with a base 5, and intake valve 2 and air outlet valve 3 are located at the top of described pressure vessel 1.
Embodiment two: take off the raw material of stating volumn concentration and mix: turps 55%, 70# gasoline 40%, ferrocene 5%, mix and be mixed with synergistic agent, at first above-mentioned synergistic agent is poured in the device, the amount of pouring into is 1/2nd of a vessel content, then with Sweet natural gas from bottom of device blow out with install in synergistic agent mixes, export then and get final product.This device device as shown in Figure 1, comprise a pressure vessel 1, pressure vessel 1 is provided with an intake valve 2 and air outlet valve 3, in pressure vessel 1, be provided with an airway 4 that links to each other with intake valve 2, the bottom of pressure vessel 1 is provided with a base 5, and intake valve 2 and air outlet valve 3 are located at the top of described pressure vessel 1.
Embodiment three: take off the raw material of stating volumn concentration and mix: turps 50%, 70# gasoline 45%, ferrocene 5%, mix and be mixed with synergistic agent, at first above-mentioned synergistic agent is poured in the device, the amount of pouring into is 1/2nd of a vessel content, then with Sweet natural gas from bottom of device blow out with install in synergistic agent mixes, export then and get final product.This device device as shown in Figure 1, comprise a pressure vessel 1, pressure vessel 1 is provided with an intake valve 2 and air outlet valve 3, in pressure vessel 1, be provided with an airway 4 that links to each other with intake valve 2, the bottom of pressure vessel 1 is provided with a base 5, and intake valve 2 and air outlet valve 3 are located at the top of described pressure vessel 1.
Embodiment four: take off the raw material of stating volumn concentration and mix: turps 46%, 70# gasoline 48%, ferrocene 6%, mix and be mixed with synergistic agent, at first above-mentioned synergistic agent is poured in the device, the amount of pouring into is 1/2nd of a vessel content, then with Sweet natural gas from bottom of device blow out with install in synergistic agent mixes, export then and get final product.This device device as shown in Figure 1, comprise a pressure vessel 1, pressure vessel 1 is provided with an intake valve 2 and air outlet valve 3, in pressure vessel 1, be provided with an airway 4 that links to each other with intake valve 2, the bottom of pressure vessel 1 is provided with a base 5, and intake valve 2 and air outlet valve 3 are located at the top of described pressure vessel 1.
Embodiment five: take off the raw material of stating volumn concentration and mix: turps 54%, 70# gasoline 42%, ferrocene 4%, mix and be mixed with synergistic agent, at first above-mentioned synergistic agent is poured in the device, the amount of pouring into is 1/2nd of a vessel content, then with Sweet natural gas from bottom of device blow out with install in synergistic agent mixes, export then and get final product.This device device as shown in Figure 1, comprise a pressure vessel 1, pressure vessel 1 is provided with an intake valve 2 and air outlet valve 3, in pressure vessel 1, be provided with an airway 4 that links to each other with intake valve 2, the bottom of pressure vessel 1 is provided with a base 5, and intake valve 2 and air outlet valve 3 are located at the top of described pressure vessel 1.
Claims (8)
1. synergistic agent that the combustion of natural gas temperature is improved is characterized in that: this synergistic agent is that the raw material by following volumn concentration mixes: turps 45-55%, gasoline 40-50%, ferrocene 2-7%.
2. a kind of synergistic agent that the combustion of natural gas temperature is improved as claimed in claim 1, it is characterized in that: the volumn concentration of described turps, gasoline, ferrocene is respectively 50%, 45%, 5%.
3. a kind of synergistic agent that the combustion of natural gas temperature is improved as claimed in claim 1 or 2, it is characterized in that: described gasoline is 70# gasoline.
4. device that the combustion of natural gas temperature is improved, it is characterized in that: this device comprises a pressure vessel (1), pressure vessel (1) is provided with an intake valve (2) and air outlet valve (3).
5. the device of raising natural gas temperature as claimed in claim 4 is characterized in that: be provided with an airway (4) that links to each other with described intake valve (2) in described pressure vessel (1).
6. as the device of claim 4 or 5 described raising natural gas temperature, it is characterized in that: the bottom of institute's pressure vessel (1) is provided with a base (5).
7. as the device of claim 4 or 5 described raising natural gas temperature, it is characterized in that: described intake valve (2) and air outlet valve (3) are located at the top of described pressure vessel (1).
8. as the device of claim 4 or 5 described raising natural gas temperature, it is characterized in that: described pressure vessel (1) is a spherical cylindrical shell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200510107703A CN100577778C (en) | 2005-09-30 | 2005-09-30 | Synergist for improving natural gas burning temperature and its apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200510107703A CN100577778C (en) | 2005-09-30 | 2005-09-30 | Synergist for improving natural gas burning temperature and its apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1940034A true CN1940034A (en) | 2007-04-04 |
| CN100577778C CN100577778C (en) | 2010-01-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200510107703A Expired - Fee Related CN100577778C (en) | 2005-09-30 | 2005-09-30 | Synergist for improving natural gas burning temperature and its apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100577778C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102876414A (en) * | 2012-10-16 | 2013-01-16 | 陈衍芽 | Preparation process for synergistic industrial biogas |
| WO2014017185A1 (en) * | 2012-07-26 | 2014-01-30 | Bruce Briant Parsons | Body of molecular sized fuel additive |
| CN103710062A (en) * | 2014-01-02 | 2014-04-09 | 北京大通鸿业科技发展有限公司 | Efficient natural gas |
| CN104877722A (en) * | 2015-05-07 | 2015-09-02 | 王大力 | Natural gas metal cutting gas |
| CN112175682A (en) * | 2020-10-10 | 2021-01-05 | 辽宁华融富瑞新能源科技股份有限公司 | Industrial natural gas combustion-supporting synergist |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1058048C (en) * | 1998-08-18 | 2000-11-01 | 张云 | Formulation and prodn. method of gas light oil |
-
2005
- 2005-09-30 CN CN200510107703A patent/CN100577778C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014017185A1 (en) * | 2012-07-26 | 2014-01-30 | Bruce Briant Parsons | Body of molecular sized fuel additive |
| CN104640960A (en) * | 2012-07-26 | 2015-05-20 | 高效燃料解决方案有限责任公司 | Body of molecular sized fuel additive |
| US9879196B2 (en) | 2012-07-26 | 2018-01-30 | Efficient Fuel Solutions, Llc | Body of molecular sized fuel additive |
| AU2017251764B2 (en) * | 2012-07-26 | 2019-06-13 | Efficient Fuel Solutions, Llc | Body of molecular sized fuel additive |
| CN102876414A (en) * | 2012-10-16 | 2013-01-16 | 陈衍芽 | Preparation process for synergistic industrial biogas |
| CN102876414B (en) * | 2012-10-16 | 2014-01-22 | 陈衍芽 | Preparation process for synergistic industrial biogas |
| CN103710062A (en) * | 2014-01-02 | 2014-04-09 | 北京大通鸿业科技发展有限公司 | Efficient natural gas |
| CN103710062B (en) * | 2014-01-02 | 2015-02-04 | 北京大通鸿业科技发展有限公司 | Efficient natural gas |
| CN104877722A (en) * | 2015-05-07 | 2015-09-02 | 王大力 | Natural gas metal cutting gas |
| CN112175682A (en) * | 2020-10-10 | 2021-01-05 | 辽宁华融富瑞新能源科技股份有限公司 | Industrial natural gas combustion-supporting synergist |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100577778C (en) | 2010-01-06 |
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