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序号	专利名	申请号	申请日	公开（公告）号	公开（公告）日	发明人
181		IT4809078	1978-02-17	IT7848090A0	1978-02-17

182	Operating method for a fill schraegkammerverkokungsofens and schraegkammerverkokungsofen for implementing this method	DE2559118	1975-12-30	DE2559118B1	1977-06-02	WAGENER DIETRICH DR-ING

183	Schraegkammerkoksofen	DE2559131	1975-12-30	DE2559131B1	1977-03-10	PRANGE KURT; ISERMANN FRIEDRICH; HASENAECKER ERNST; BLASE MANFRED

184		BR654774	1974-08-08	BR7406547A	1976-03-30	CUNHA R

185		NO752301	1975-06-26	NO752301L	1975-12-30	DERUELLE J; PENET O

186		SE7507333	1975-06-26	SE7507333L	1975-12-29	DERUELLE J; PENET O

187	Oven carbonization and semi-carbonization to achieve a predetermined heating pattern	FR984453D	1943-09-28	FR984453A	1951-07-06

188	A method for generating karburiertem water gas in Schraegkammeroefen	DEO0020678		DE608044C	1935-01-17

189	Coke oven battery with schraegliegenden retorts	DEB0109280	1923-04-15	DE445450C	1927-06-11

190	Improvements in or relating to coking or carbonizing ovens	GB3232526	1926-12-21	GB263801A	1927-03-17
263,801. Stettiner Chamotte-Fabrik Akt.-Ges. vorm. Didier. Dec. 24, 1925, [Convention date]. Coke ovens; charging and discharging.-In an inclined coke oven a, the sole h is extended upwardly to the charging-bench f and a discharging ram m is mounted on the truck d carrying the charging-hopper e, the distance between the centres of the ram m and hopper e being such that one oven may be charged simultaneously with the discharge of the next oven in the setting. The pusher-rod m is so supported in guides k that the ram head moves parallel to and in contact with the oven sole h and is formed on the upper surface with teeth which are engaged by a pinion connected through gearing with an operating-handle. In the modification shown in Fig .3, the upper part s<2> of the oven sole is more steeply inclined than the lower part s<1> this arrangement permitting the charging aperture t to be of reduced size and also the charging throat u of the gas generator q to be extended upwardly to the bench f where a separate charging device w is provided.
191	Heating for Destillationskammeroefen	DED0047636	1925-03-25	DE433849C	1926-09-07

192	Process and apparatus for the internal distillation of solid combustibles	GB1099524	1924-05-05	GB237369A	1925-07-30
237,369. Lencauchez, J. A. May 5, 1924. Air.heating furnaces.-Solid combustibles are distilled by the passage therethrough of a heated gas, which is heated by heat accumulators disposed immediately beneath the floor. The material is heated in a pair of chambers, each chamber 1 having a floor composed of overlapping elements 2 with spaces between them. A heat accumulator consisting of three chambers 12, 13, 14 containing brickwork is heated by combustion of gas from a burner 18, the combustion products escaping through a passage 21 and flue 30, serving to heat the air admitted through a passage 19. On moving the damper 31 to the position shown, opening the register 15 and cutting off the gas to the burner, the heating gas from a main 46 is heated on the accumulators and passes into the material through the openings in the floor.
193	Schraegkammerofen	DEB0104827	1922-05-06	DE416317C	1925-07-11

194	Distillation fuel	FR576776D	1924-02-05	FR576776A	1924-08-26

195	Schraegkammerofen for distilling carbon material	DES0052541		DE385545C	1923-11-27

196	Methods and apparatus for the treatment of coal	FR522941D	1919-04-02	FR522941A	1921-08-09	SMITH CHARLES HOWARD

197	Improvements in and relating to Briquet-carbonizing Furnaces.	GB844519	1919-04-03	GB125381A	1920-05-27	SMITH CHARLES HOWARD
125,381. Smith, C. H. April 3, 1918, [Convention date]. Retort furnaces; charging and discharging.-A furnace for carbonizing briquettes comprises a series of inclined chambers or retorts 6 divided into compartments 6b by partitions 6, the chambers being heated by means of heating flues 18, 18, Fig. 10, in which fuel, preferably gas supplied by pipes 19, is burned with air heated in a recuperator 7 comprising a number of flues 20, down which the hot gases from the furnace pass as shown in Fig. 6, alternating with flues 22 up which the air passes, as shown in Fig. 5. The hot air leaves the recuperator by the flue 23 leading to the heating flues 18, 18, and the heat of the carbonizing chambers is controlled by dampers at both ends of the heating flues. The chambers and flues of the furnace and recuperator are arranged as shown in Fig. 10, the flues being disposed so as to heat the chambers effectively in the neighbourhood of the partitions 6a. The apparatus is charged by a car 27, Fig. 11, divided into compartments and provided with a telescopic shoot which bridges the space between the car and the compartments. After carbonizing, the charge passes out to a dumping-car 30.
198	Four regenerative gasifier with management remaining constant heating flames	FR445344D	1912-06-24	FR445344A	1912-11-08

199	A Regenerative Gas-generating Furnace with Constant Direction of the Heating Flames.	GB191214702D	1912-06-24	GB191214702A	1912-09-12
14,702. Stettiner Chamotte-Fabrik Akt.-Ges. vorm. Didier. July 10,1911, [Convention date]. Retort furnaces.-The waste gases from gasretort furnaces, in which the heating-flame has a constant direction, are first passed through recuperators and then through reversible regenerators, rapid wear of the change-over valves &c. being thus obviated owing to the preliminary cooling of the gases in the recuperators. An inclined retort fornace is shown in the Figures, of which Fig. 3 shows sections on the lines E F, G H, I K of Fig. 1, Fig. 4 a horizontal section on the line L M of Fig. 1, and Fig. 7 a vertical section showing part of the reversing arrangements. The waste gases from the heating-conduits 3 pass through the vertical passages 5 to the conduits 6 of the recuperator, in which the gas for combustion is heated by passing upwards through the conduits 8, whence it is led by passages 15, 18 to vertical passages 4 at the ends of the heating- conduits 3. The waste gases, after leaving the recuperators, are collected in a chamber 11, from which, in the position of the slides 29, 30 shown in Fig. 7, they pass by the passage 25 to the regenerator 20, which they leave by the outlet passages 42, 43 connecting to the flue. Air for combustion enters the regenerator 19 through the passage 39 and thence passes by way of the passages 22, chamber 16, and conduits 17, to the ends of the heating conduits. On reversal, the waste gases from the chamber 11 pass to the regenerator 19, which they leave by the conduit 34, and air for combustion enters the regenerator 20 by the conduit 47, passing thence to the chamber 16. The outlets 34, 43 of the regenerators are provided with slides for regulating their area, in addition to the cut-off slides 36, 48.
200	Oven with inclined chambers, intended more especially for the production of coke	FR425472D	1910-04-05	FR425472A	1911-06-12	KLOENNE AUGUST

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