| 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 | 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。 | ||||||
| 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 | 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。 | ||||||
| 3 | 副产品熟石灰排出装置 | CN201080066564.5 | 2010-11-12 | CN103189478B | 2014-12-10 | 大森博昭 |
| 提供一种结构简单，维护次数少的副产品熟石灰排出装置。副产品熟石灰排出装置包括：与乙炔发生机的副产品熟石灰排出口直接或间接连接，上部有入口，下部有出口的保留好从乙炔发生机出来的副产品熟石灰的密封罐；用于从所述罐的出口将副产品熟石灰取出的排出机；用于对所述罐以及所述排出机进行加热的加热装置；对所述罐的重量进行计测的秤量器；用于根据所述秤量器计测出的所述罐的重量，对副产品熟石灰的取出速度进行控制的控制机构。 | ||||||
| 4 | 副产品熟石灰排出装置 | CN201080066564.5 | 2010-11-12 | CN103189478A | 2013-07-03 | 大森博昭 |
| 本发明提供一种结构简单，维护次数少的副产品熟石灰排出装置。副产品熟石灰排出装置包括：与乙炔发生机的副产品熟石灰排出口直接或间接连接，上部有入口，下部有出口的保留好从乙炔发生机出来的副产品熟石灰的密封罐；用于从所述罐的出口将副产品熟石灰取出的排出机；用于对所述罐以及所述排出机进行加热的加热装置；对所述罐的重量进行计测的秤量器；用于根据所述秤量器计测出的所述罐的重量，对副产品熟石灰的取出速度进行控制的控制机构。 | ||||||
| 5 | Apparatus for production of acetylene | US775214 | 1991-10-11 | US5284630A | 1994-02-08 | James W. Bunger; Hoil Ryu; Prasad A. V. Devineni |
| A two-stage process for producing acetylene and calcium chloride from calcium carbide and water has two successive reaction steps. In step Number 1, calcium carbide is charged into an entrained flow-type reactor vessel containing water. The reaction which follows proceeds to about 60-90% completion. The entrained reaction products and the unreacted feed material are carried over to a secondary reactor to complete the reaction, and the acetylene gas is drawn off. Calcium hydroxide product is removed from the reactor and reacted with hydrogen chloride to form calcium chloride. Heat generated by the exothermic reactions of water with calcium carbide and HCl with calcium hydroxide is used to dry the calcium chloride product and improve its value. In the presence of excess water, the calcium carbide-water reaction is effectively a first order, irreversible reaction. | ||||||
| 6 | Apparatus and process for the production of acetylene | US704713 | 1991-05-17 | US5082644A | 1992-01-21 | James W. Bunger; Hoil Ryu; Prasad A. V. Devineni |
| A two-stage process for producing acetylene and calcium chloride from calcium carbide and water has two successive reaction steps. In step Number 1, calcium carbide is charged into an entrained flow-type reactor vessel containing water. The reaction which follows proceeds to about 60-90% completion. The entrained reaction products and the unreacted feed material are carried over to a secondary reactor to complete the reaction, and the acetylene gas is drawn off. Calcium hydroxide product is removed from the reactor and reacted with hydrogen chloride to form calcium chloride. Heat generated by the exothermic reactions of water with calcium carbide and HCl with calcium hydroxide is used to dry the calcium chloride product and improve its value. In the presence of excess water, the calcium carbide-water reaction is effectively a first order, irreversible reaction. | ||||||
| 7 | CARBIDE SUPERCELL FOR DRY ACETYLENE GENERATION AND AN INTERNAL COMBUSTION ENGINE USING THE SAME | US11767335 | 2007-06-22 | US20070295288A1 | 2007-12-27 | Joseph W. Wulff; Harry J. Wulff |
| Novel carbide supercells for dry acetylene generation are disclosed herein, along with methods of use and internal combustion engines incorporating the carbide supercells. A carbide supercell according to one embodiment includes an outer shell defining an interior gas chamber and a rotating basket positioned in the gas chamber. The basket defines a plurality of holes and is configured to contain at least one calcium carbide rock. An injector is adjacent the basket for spraying a liquid into the basket, and a controller is in data communication with the injector for actuating the injector. A chamber outlet is adjacent an upper end of the gas chamber. | ||||||
| 8 | 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. | ||||||
| 9 | TWO-STAGE PROCESS FOR PRODUCTION OF CALCIUM CHLORIDE AND ACETYLENE | EP90916963 | 1990-10-25 | EP0498844A4 | 1993-01-20 | BUNGER, JAMES, W.; RYU, HOIL; DEVINENI, PRASAD, A., V. |
| A two-staged process for producing acetylene and calcium chloride from calcium carbide (12) and water (12) has two successive reaction steps. In step Number 1, calcium carbide is charged into an entrained flow-type reactor (10) vessel containing water. The reaction which follows proceeds to about 60-90 % completion. The entrained reaction products and the unreacted feed material are carried over to a secondary reactor (16) to complete the reaction, and the acetylene gas is drawn off (26). Calcium hydroxide product is removed from the reactor (23) and reacted with hydrogen chloride to form calcium chloride. Heat generated by the exothermic reactions of water with calcium carbide and HCl with calcium hydroxide is used to dry the calcium chloride product and improve its value. In the presence of excess of water, the calcium carbide-water reaction is effectively a first order, irreversible reaction. | ||||||
| 10 | Carbide supercell for dry acetylene generation and an internal combustion engine using the same | US11767335 | 2007-06-22 | US07607409B2 | 2009-10-27 | Joseph W. Wulff; Harry J. Wulff |
| Novel carbide supercells for dry acetylene generation are disclosed herein, along with methods of use and internal combustion engines incorporating the carbide supercells. A carbide supercell according to one embodiment includes an outer shell defining an interior gas chamber and a rotating basket positioned in the gas chamber. The basket defines a plurality of holes and is configured to contain at least one calcium carbide rock. An injector is adjacent the basket for spraying a liquid into the basket, and a controller is in data communication with the injector for actuating the injector. A chamber outlet is adjacent an upper end of the gas chamber. | ||||||
| 11 | 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. | ||||||
| 12 | Dry acetylene generator | US428486 | 1982-09-29 | US4451268A | 1984-05-29 | John A. Lerch |
| A multi-stage generator for generating dry acetylene gas from calcium carbide while leaving a residue of dry lime has a generator housing including a plurality of vertically spaced shelves, each shelf and its associated components providing a stage of the generator. Each shelf has an exit slot and a water spray zone circumferentially spaced therefrom. A deposit zone is formed intermediate the water spray zone and the exit slot. Stirring arms are rotatably mounted to cooperate with each shelf to sweep the calcium carbide mixture received in the deposit zone into the wetting zone and thereafter into the exit slot. The exit slot of each shelf is offset angularly relative to the exit slot of the preceeding shelf so that the calcium carbide mixture is swept about each shelf through a substantial angle prior to exiting to the next shelf. | ||||||
| 13 | Acetylene-gas generator. | US1898673509 | 1898-03-11 | US638459A | 1899-12-05 | HOLT RAY W; ROSE HOWARD A |
| 14 | Acetylene-generating lamp | US621230D | US621230A | 1899-03-14 | ||
| 15 | Byproduct slaked lime discharge device | JP2012512099 | 2010-11-12 | JP5066632B2 | 2012-11-07 | 博昭 大森 |
| 16 | JPH05500941A - | JP51565590 | 1990-10-25 | JPH05500941A | 1993-02-25 | |
| 17 | Apparatus and process for the production of acetylene. | EP90916963.3 | 1990-10-25 | EP0498844B1 | 1994-08-31 | BUNGER, James, W.; RYU, Hoil; DEVINENI, Prasad, A., V. |
| A two-staged process for producing acetylene and calcium chloride from calcium carbide (12) and water (12) has two successive reaction steps. In step Number 1, calcium carbide is charged into an entrained flow-type reactor (10) vessel containing water. The reaction which follows proceeds to about 60-90 % completion. The entrained reaction products and the unreacted feed material are carried over to a secondary reactor (16) to complete the reaction, and the acetylene gas is drawn off (26). Calcium hydroxide product is removed from the reactor (23) and reacted with hydrogen chloride to form calcium chloride. Heat generated by the exothermic reactions of water with calcium carbide and HCl with calcium hydroxide is used to dry the calcium chloride product and improve its value. In the presence of excess of water, the calcium carbide-water reaction is effectively a first order, irreversible reaction. | ||||||
| 18 | TWO-STAGE PROCESS FOR PRODUCTION OF CALCIUM CHLORIDE AND ACETYLENE | EP90916963.0 | 1990-10-25 | EP0498844A1 | 1992-08-19 | BUNGER, James, W.; RYU, Hoil; DEVINENI, Prasad, A., V. |
| Un procédé en deux étapes de production d'acétylène et de chlorure de calcium à partir de carbure de calcium (12) et d'eau (12) comprend deux étapes de réaction successives. Dans l'étape numéro 1, du carbure de calcium est chargé dans un réacteur du type à écoulement entraîné (10) contenant de l'eau. La réaction qui suit se poursuit jusqu'à environ 60 à 90 % de la réaction complète. Les produits de réaction entraînés et la matière d'alimentation n'ayant pas réagis sont transportés vers un réacteur secondaire (16) pour terminer la réaction, puis du gaz acétylène est soutiré (26). Un produit d'hydroxyde de calcium est extrait du réacteur (23) puis réagit avec du chlorure d'hydrogène pour former du chlorure de calcium. De la chaleur générée par des réaction exothermiques d'eau avec du carbure de calcium et d'HCl avec de l'hydroxyde de calcium est utilisée pour sécher le produit de chlorure de calcium et améliorer sa valeur. En présence d'un excès d'eau, la réaction carbure de calcium-eau est en réalité une réaction de premier ordre irréversible. | ||||||
| 19 | 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。 | ||||||
| 20 | 副生消石灰排出装置 | JP2012512099 | 2010-11-12 | JPWO2012063366A1 | 2014-05-12 | 大森 博昭; 博昭 大森 |
| 機構が簡単であり、メンテナンス頻度の少ない副生消石灰排出装置を提供する。アセチレン発生機の副生消石灰排出口に直接又は間接的に連結され、上部に入口、下部に出口を有しており、アセチレン発生機からの副生消石灰を保持するシールタンクと、該タンクの出口から副生消石灰を抜き出すための排出機と、該タンク及び該排出機を加熱するための加熱装置と、該タンクの重量を計測する秤量器と、該秤量器で計測された該タンクの重量に応じて副生消石灰を抜き出す速度を制御する制御機構と、を備えた副生消石灰排出装置。 | ||||||
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