公开(公告)号：WO2008064660A3

公开(公告)日：2009-06-11

申请号：PCT/DE2007002148

申请日：2007-11-28

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: F01D1/22 ,  C02F1/461 ,  F02C3/05 ,  F02C3/28 ,  F02C3/30 ,  F23G5/46

CPC classification number: F02C3/305 ,  C02F1/4672 ,  C02F2201/46165 ,  C02F2201/4617 ,  F01D1/22 ,  F02C3/05 ,  F02C3/22 ,  F02C3/28 ,  F02C6/006 ,  F02C6/18 ,  F05D2220/762 ,  F05D2220/768

Abstract: Disclosed are a method and a device for operating a generator (4) by means of hot gas, particularly hot gas obtained from the gasifier of a waste reprocessing plant, said hot gas being conducted across a double turbine rotor (13). In said method and device, steam (44) is introduced or generated upstream of the turbine (3) such that a hot gas-steam mixture (45) is introduced via a tapering turbine inlet (11) at an elevated density and a high speed, causing a preliminary reaction in the mixture. The hot gas-steam mixture (45) is then first expanded and once again compressed by means of the double turbine rotor (13) and is introduced in an expanding manner into a widening diffuser section (16) of the discharge pipe (15) in which a negative pressure prevails.

Abstract translation: 本发明公开了用于操作由从气化器到热气体的废物处理设备得到的热气体，特别是所描述的双涡轮机转子（13）的被引导的发电机（4），其特征在于，所述涡轮机的水蒸汽的上游（44）引入或（3）的方法和装置 被引入。生产，从而在更高的密度，并在上变窄涡轮机入口（11）高速热气体 - 蒸汽混合物（45），在该混合物的预反应导致。 热气体 - 蒸汽混合物（45）然后在双涡轮机转子（13）的第一和然后再压缩，并在流出管的扩口扩压器部分（16）再膨胀膨胀（15）被引入，其中所述排泄管（15） 真空为准。

公开(公告)号：WO2008064661A2

公开(公告)日：2008-06-05

申请号：PCT/DE2007002149

申请日：2007-11-28

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

CPC classification number: F02C3/22 ,  C10J3/20 ,  C10J3/84 ,  C10J2200/156 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0966 ,  C10J2300/1223 ,  C10J2300/1634 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1684 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10K1/101 ,  F02C6/10 ,  F23G5/006 ,  F23G5/02 ,  F23G5/24 ,  F23G5/46 ,  F23G2201/301 ,  F23G2201/40 ,  F23G2201/603 ,  F23G2201/702 ,  F23G2201/80 ,  F23G2206/202 ,  F23G2206/203 ,  F23J15/006 ,  F23J2217/102 ,  F23J2217/50 ,  F23J2219/40 ,  F23L7/005 ,  Y02E20/12

Abstract: Disclosed are a method and an installation for generating effective energy by gasifying waste. In said method and installation, waste such as garbage is introduced into a shaft-type melting gasifier, is dried in a reverse flow, is degassed, and is gasified while the solid residue is melted. The hot crude gases that are withdrawn from the melting gasifier (15) are fed to a hot gas steam generator (18) in which steam is admixed to the hot gas and said hot gas-steam mixture is conducted across the double turbine rotor (18.13) of a turbine (18.3) that drives a power generator (18.4), a preliminary reaction taking place at the same time. The pre-purified hot gas-steam mixture is then introduced into a downflow device (38) in which the mixture is cooled and pre-purified using sprayed water mixed with reactant and by repeatedly expanding, compressing, and foaming the mixture, the pre-purified gas being withdrawn and the liquid being collected. The pre-purified gas is fed to a gas purification process (40) in which the pre-purified gas is foamed with reactant and is defoamed again. The purified gases are finally further utilized for generating power, e.g. by being burned in an engine (41).

Abstract translation: 在的方法以及通过废物气化为Nutzenergieerzeugung植物在废物被引入如在轴熔融气化炉城市废物，在逆流干燥，脱气等，而根据固体残渣熔融气化从熔融气化器被发送（15）被抽出的热原料气的热气体的蒸汽发生器 （18）提供的混合，其中所述热气体的水蒸汽，并通过涡轮机的双涡轮机转子（18点13分）此热气体 - 蒸汽混合物（18.3）被引导，其驱动发电机（18.4），同时进行预反应。 此后，预纯化的热气体 - 蒸汽混合物被引入降流装置（38），使用eingedüstem其中，用试剂水并通过反复延伸和压缩与发泡偏移，被冷却时，它们的混合物和预清洗，其中，所述预纯化的气体抽出并 收集液体。 将预纯化的气体送入气体净化器（40），在该净化器中气体与试剂一起发泡并再次消泡。 最后，另一种能量回收的净化气体z。 B.在供应的电动机（41）中燃烧。

公开(公告)号：WO03011775A3

公开(公告)日：2003-08-07

申请号：PCT/DE0202748

申请日：2002-07-26

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: C02F1/00 ,  C02F1/24 ,  C02F1/44 ,  C02F1/467 ,  C02F1/66 ,  C02F1/72 ,  C02F1/74 ,  C02F9/00 ,  C02F9/08 ,  B01J10/00 ,  C02F1/20

CPC classification number: C02F1/72 ,  C02F1/001 ,  C02F1/24 ,  C02F1/444 ,  C02F1/4672 ,  C02F1/66 ,  C02F1/74 ,  C02F9/00 ,  C02F2001/007 ,  C02F2101/301 ,  C02F2103/44 ,  C02F2209/06 ,  C02F2209/42 ,  C02F2303/12

Abstract: The invention relates to a method and an installation for treating liquids, especially for purifying contaminated water. Said method consists of the following steps: the raw water is pre-purified by adding a foam-forming reaction agent; the pre-purified water undergoes a main purification process by foaming the water with ionising radicals contained in the exhaust from the subsequent steps, in a known perforated cylinder washer (21); the foam formed is eliminated; the de-foamed water is ionised; and the impurities in the purified water are sedimented. The purified water is then additionally purified, the mud consisting of impurities from the pre-purification and the main purification process is physically separated, and the transformation of raw water into purified water is carried out continuously.

Abstract translation: 它是一种方法和用于净化污染水说明用于液体处理的植物，特别地，其特征在于，第一前处理的原水通过添加泡沫形成的试剂，然后将这样的预纯化水的主清扫的通过水的与包含在排气lonisierungsradikalen一起发泡 在一个已知的刺辊涤气器（21）的后续阶段的，消泡形成的泡沫，电离杂质的脱泡的水和沉淀在纯净水中，净化水的再一个物理后纯化，然后，最后，从预清洗和主清洗取出的物理分离 杂质污泥进行，并且其中的粗的连续纯化携带到纯净水。

公开(公告)号：CZ286864B6

公开(公告)日：2000-07-12

申请号：CZ304690

申请日：1990-06-19

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: B01D47/04 ,  B01D53/74

Abstract: Combustion fumes are cleaned, prior to emission by contact with foam produced by turbulence in cleaning liq. The turbulence is produced by freely working rollers (13) dipping below the surface of a bath (15) of the liq. and with peripheral indentations for gas energising into a prim. reaction chamber (11a). The internal roller cavity forms a secondary reactor chamber (11b) assymetrically bounded by the roller surface. Used foam is taken by a conduit (16) to be broken down, e.g. by a motor-driven radial fan producing regenerated cleaning liq. in a collector (18) while cleaned gas leaves from a pipe (25).

公开(公告)号：ES2111642T3

公开(公告)日：1998-03-16

申请号：ES92914227

申请日：1992-07-03

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: B01D47/04 ,  B01D47/06 ,  B01D53/34 ,  B01D53/74 ,  B01D53/77

Abstract: A gas cleaning process esp. for flue gases, involves contacting a foam-forming reactant with the gas in a reaction chamber, destroying the foam after reaction, separately collecting recovered reactant and sludge and releasing the cleaned gas. When cleaning gases at below 60 deg. C, (a) foam destruction is carried out in the reaction chamber to form a dense foam and an underlying reactant layer mixed with water and gases; (b) the dense foam and surface sludge are withdrawn from the reaction chamber by suction and are temporarily stored for gravity sepn., and (c) material layer-spen. is carried out in a settling phase, the individualy layers being successively sepd. When the gases are at above 60 deg. C the settled sludge is dried in a dryer by stepwise vertically downward transport of the sludge in contact with dirty gas fed to the dryer. Also claimed is a plant for carrying out the process, including a reaction chamber contg. rotating rolls for contacting the gases with the reactant.

公开(公告)号：LT3485B

公开(公告)日：1995-11-27

申请号：LTIP503

申请日：1993-04-30

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: B01D47/06 ,  B01D47/04

公开(公告)号：HU9300439D0

公开(公告)日：1993-05-28

申请号：HU9300439

申请日：1992-07-03

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: B01D47/04 ,  B01D47/06 ,  B01D53/34 ,  B01D53/74 ,  B01D53/77

Abstract: A gas cleaning process esp. for flue gases, involves contacting a foam-forming reactant with the gas in a reaction chamber, destroying the foam after reaction, separately collecting recovered reactant and sludge and releasing the cleaned gas. When cleaning gases at below 60 deg. C, (a) foam destruction is carried out in the reaction chamber to form a dense foam and an underlying reactant layer mixed with water and gases; (b) the dense foam and surface sludge are withdrawn from the reaction chamber by suction and are temporarily stored for gravity sepn., and (c) material layer-spen. is carried out in a settling phase, the individualy layers being successively sepd. When the gases are at above 60 deg. C the settled sludge is dried in a dryer by stepwise vertically downward transport of the sludge in contact with dirty gas fed to the dryer. Also claimed is a plant for carrying out the process, including a reaction chamber contg. rotating rolls for contacting the gases with the reactant.

公开(公告)号：AT502861B1

公开(公告)日：2007-06-15

申请号：AT93012002

申请日：2002-07-26

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: C02F1/00 ,  C02F1/24 ,  C02F1/44 ,  C02F1/467 ,  C02F1/66 ,  C02F1/72 ,  C02F1/74 ,  C02F9/00 ,  C02F9/08 ,  B01J10/00 ,  C02F1/20

Abstract: In continual process to treat effluent wash water, in a first stage a foam-building reactant is admixed to the water with air in a rotating perforated drum. The reactant forms bubbles in water containing ionized radicals introduced from subsequent stages. Foam is skimmed off and the water ionized, driving sedimentation. Sludge is then physically removed from the first-stage treated water and the foam-treated water. Foam generation and removal, oxidation, ionization and collection of treated water takes place in a vertical gravity-driven sequence within the same assembly. Gases liberated with radicals by the ionization process are returned to the foam generation reaction stage and are recycled within a closed system. Also claimed is a commensurate assembly with a pre-cleaning tank (10) into which foam generating agent is admixed and the pH is regulated (13, 14). The assembly has a main treatment block (20) with vertically stacked drum station (21), foam generation station (23), ionization station (24), clean water tank (25), sludge separator (30) and sumps (11, 26). The assembly further has a filter (40) and a clean water discharge (43).

公开(公告)号：CZ20040868A3

公开(公告)日：2005-03-16

申请号：CZ20040868

申请日：2002-07-26

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: C02F1/00 ,  C02F1/24 ,  C02F1/44 ,  C02F1/467 ,  C02F1/66 ,  C02F1/72 ,  C02F1/74 ,  C02F9/00 ,  C02F9/08 ,  B01J10/00 ,  C02F1/20

CPC classification number: C02F1/72 ,  C02F1/001 ,  C02F1/24 ,  C02F1/444 ,  C02F1/4672 ,  C02F1/66 ,  C02F1/74 ,  C02F9/00 ,  C02F2001/007 ,  C02F2101/301 ,  C02F2103/44 ,  C02F2209/06 ,  C02F2209/42 ,  C02F2303/12

公开(公告)号：CZ9003046A3

公开(公告)日：2000-05-17

申请号：CZ304690

申请日：1990-06-19

Applicant: BERTHOLD HERMANN

Inventor： BERTHOLD HERMANN

IPC: B01D47/04 ,  B01D53/74