子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 乙炔发生设备、乙炔发生设备的控制方法以及乙炔气体的制造方法 | CN201080048301.1 | 2010-11-15 | CN103189477B | 2016-06-15 | 大森博昭 |
| 本发明提供一种能够更高精度地对乙炔发生器进行供水控制的乙炔发生设备、乙炔发生设备的控制方法以及乙炔气体的制造方法。具有：使电石与水反应来产生乙炔气体的乙炔发生器1、向乙炔发生器1供应电石的供应罐2、向乙炔发生器1供应水的水供应单元3、检测从乙炔发生器1排出的乙炔气体的产生量的气体流量检测器4、检测从乙炔发生器1排出的乙炔气体的温度的气体温度检测器5、以及基于乙炔气体的产生量和乙炔气体的温度来控制供应给乙炔发生器1的水的流量的控制装置6。 | ||||||
| 2 | 乙炔发生设备、乙炔发生设备的控制方法以及乙炔气体的制造方法 | CN201080048301.1 | 2010-11-15 | CN103189477A | 2013-07-03 | 大森博昭 |
| 本发明提供一种能够更高精度地对乙炔发生器进行供水控制的乙炔发生设备、乙炔发生设备的控制方法以及乙炔气体的制造方法。具有：使电石与水反应来产生乙炔气体的乙炔发生器1、向乙炔发生器1供应电石的供应罐2、向乙炔发生器1供应水的水供应单元3、检测从乙炔发生器1排出的乙炔气体的产生量的气体流量检测器4、检测从乙炔发生器1排出的乙炔气体的温度的气体温度检测器5、以及基于乙炔气体的产生量和乙炔气体的温度来控制供应给乙炔发生器1的水的流量的控制装置6。 | ||||||
| 3 | A process for the production of an acetylene base stable fuel gas, the products obtained by this process and the use of the produced acetylene base fuel gas | EP80301997.5 | 1980-06-13 | EP0021748B1 | 1984-10-03 | Hayes, Edward O. |
| 4 | A process for the production of an acetylene base stable fuel gas, the products obtained by this process and the use of the produced acetylene base fuel gas | EP80301997.5 | 1980-06-13 | EP0021748A1 | 1981-01-07 | Hayes, Edward O. |
A relatively safe and stable acetylene base fuel gas of enhanced BTU output is prepared, without formation of undesirable by-products, through the reaction of a carbide, such as calcium carbide, with a liquid activator comprised of water, a water-soluble rate-controlling-substance, and a strong inorganic acid. The resulting fuel gas includes a composition which acts as a top cylinder lubricant for an internal combustion engine and thus is suitable for powering such an engine or a power plant. Preferably, the calcium carbide employed is provided with an air and moisture impermeable coating, which is degraded upon contact by the activator. |
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| 5 | アセチレン発生設備、アセチレン発生設備の制御方法及びアセチレンガスの製造方法 | JP2012506036 | 2010-11-15 | JPWO2012066611A1 | 2014-05-12 | 大森 博昭; 博昭 大森 |
| アセチレン発生機への給水制御をより高精度に行うことが可能なアセチレン発生設備、アセチレン発生設備の制御方法及びアセチレンガスの製造方法を提供する。カルシウムカーバイドと水とを反応させてアセチレンガスを発生させるアセチレン発生機1と、アセチレン発生機1にカルシウムカーバイドを供給する供給タンク2と、アセチレン発生機1に水を供給する水供給部3と、アセチレン発生機1から排出されるアセチレンガスの発生量を検出するガス流量検出器4と、アセチレン発生機1から排出されるアセチレンガスの温度を検出するガス温度検出器5と、アセチレンガスの発生量とアセチレンガスの温度とに基づいて、アセチレン発生機1に供給する水の流量を制御する制御装置6とを備える。 | ||||||
| 6 | Acetylene generating facility, a manufacturing method of the control method, and acetylene gas acetylene generating facility | JP2012506036 | 2010-11-15 | JP5101749B2 | 2012-12-19 | 博昭 大森 |
| 7 | Loop-Route Production Method and System for Polyvinyl Chloride | US14904499 | 2013-12-19 | US20160168297A1 | 2016-06-16 | Weimin Yang; Hua Yan; Dongsheng Liu; Jinguang Zhong |
| The present invention relates to a loop-route production method and system for polyvinyl chloride, and belongs to the intersecting fields of coal chemicals, polymer materials and chemical machinery. Limestone and carbon materials such as coal are reacted in an oxygen-enriched high temperature furnace to obtain calcium carbide and carbon monoxide, and then acetylene and carbon monoxide are respectively produced from calcium carbide and dichloroethane (obtaining ethylene, etc., through methanol or ethanol); both of the end products are combined to form a closed-loop; acetylene and dichloroethane are reacted to produce a vinyl chloride monomer, which is polymerized to obtain polyvinyl chloride. The system of the present invention mainly includes a device for pulverizing and mixing solid raw materials, a device for conveying solid materials, an oxygen-enriched calcium carbide furnace, an oxygen-enriched air-blowing device, a tube-shell thermostatic reactor, a fixed bed tubular reactor, a fluidized bed reactor, an acetylene generator having a heat exchanger, a fixed bed reactor and a polymerization reactor, The present invention has the advantages of not only removing the dependence on oil resources during the production of polyvinyl chlorides, but also totally eliminating the mercury pollution. | ||||||
| 8 | Power generation system | US11504201 | 2006-08-15 | US20080044323A1 | 2008-02-21 | Pete Rosas |
| A modular system for generation of acetylene gas, in a reactor suitable for the controlled reaction of calcium carbide and water, is disclosed. In this system, a self-container reactor module is provided which is suitable for coupling to an acetylene gas reservoir. In one of the preferred embodiments of this invention, this reactor module can include a primary and a secondary charge of calcium carbide, and a stoichiometric excess of water. Acetylene gas is formed by initial contact of a primary calcium carbide charge with water in the reactor reservoir. Upon essentially complete reaction of the primary charge and the water in the reservoir, the pressure within the reactor is monitored, as such gas is drawn off to fuel the operation of an internal combustion engine. Where such pressure drops to, or below a pre-determined level, a secondary charge of calcium carbide is contacted with the remaining water in the reactor reservoir, so as to prevent interruption in the fueling of the internal combustion engine. These modules can also be “daisy chained” together, and thereafter sequentially activated, to provide essentially continuous operation of an internal combustion engine. | ||||||
| 9 | Integrated apparatus and process for high recovery of acetylene from the reaction of calcium carbide with water | US880933 | 1997-06-23 | US5955040A | 1999-09-21 | James W. Bunger; Christopher P. Russell; Jerald W. Wiser; Jesse C. Tsai |
| An apparatus for the manufacture of acetylene and hydrated lime from the reaction of calcium carbide and an excess of water is disclosed. A primary reactor for the initial reaction of the calcium carbide and water is disposed concentrically within a secondary reactor. Hydrated lime and unreacted calcium carbide flow directly from the primary reactor to the secondary reactor, where the carbide lime settles from the water and is removed. | ||||||
| 10 | Acetylene-gas generator. | US1912709947 | 1912-07-17 | US1070355A | 1913-08-12 | RICHARDSON JEROME L |
| 11 | Acetylene-gas generator. | US1908462491 | 1908-11-13 | US940384A | 1909-11-16 | FERREL ZIBA A |
| 12 | Acetylene-gas apparatus. | US1899717271 | 1899-05-18 | US649981A | 1900-05-22 | FULTON JAMES E |
| 13 | Acetylene-gas apparatus. | US1899722684 | 1899-07-03 | US639188A | 1899-12-12 | TALLMADGE JAMES W |
| 14 | Acetylene-gas generator | US612753D | US612753A | 1898-10-18 | ||
| 15 | Acetylene-gas generator | US605398D | US605398A | 1898-06-07 | ||
| 16 | raymond | US603205D | US603205A | 1898-04-26 | ||
| 17 | Acetylene-gas generator | US578847D | US578847A | 1897-03-16 | ||
| 18 | Loop-route production method and system for polyvinyl chloride | US14904499 | 2013-12-19 | US09783629B2 | 2017-10-10 | Weimin Yang; Hua Yan; Dongsheng Liu; Jinguang Zhong |
| The present invention relates to a loop-route production method and system for polyvinyl chloride, and belongs to the intersecting fields of coal chemicals, polymer materials and chemical machinery. Limestone and carbon materials such as coal are reacted in an oxygen-enriched high temperature furnace to obtain calcium carbide and carbon monoxide, and then acetylene and carbon monoxide are respectively produced from calcium carbide and dichloroethane (obtaining ethylene, etc., through methanol or ethanol); both of the end products are combined to form a closed-loop; acetylene and dichloroethane are reacted to produce a vinyl chloride monomer, which is polymerized to obtain polyvinyl chloride. The system of the present invention mainly includes a device for pulverizing and mixing solid raw materials, a device for conveying solid materials, an oxygen-enriched calcium carbide furnace, an oxygen-enriched air-blowing device, a tube-shell thermostatic reactor, a fixed bed tubular reactor, a fluidized bed reactor, an acetylene generator having a heat exchanger, a fixed bed reactor and a polymerization reactor. The present invention has the advantages of not only removing the dependence on oil resources during the production of polyvinyl chlorides, but also totally eliminating the mercury pollution. | ||||||
| 19 | Process for high recovery of acetylene and lime from the reaction of calcium carbide with water | US09399564 | 1999-09-20 | US06294148B1 | 2001-09-25 | James W. Bunger; Christopher P. Russell; Jerald W. Wiser; Jesse C. Tsai |
| A process for controlling the continuous production of acetylene and hydrated lime from the reaction of water with calcium carbide is disclosed where the hydrated lime is withdrawn at a desired mass ratio of the hydrated lime to the calcium carbide feed. The process is also controlled by regulating the temperature so that it is independent of the variations in the production of acetylene by regulating heat transfer to the environment at a rate to maintain a constant temperature in the reactor. Preferably, the reaction is controlled by withdrawing the hydrated lime slurry product at a rate low enough to maintain a slurry concentration of hydrated lime above about 14 weight percent. | ||||||
| 20 | Acetylene-gas generator. | US1910573680 | 1910-07-25 | US1025352A | 1912-05-07 | WHITE FRANCIS H |
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