Werner & Pfleiderer Gmbh

Klaus-Jurgen Hinger

Johannes Werner

An extruder drivable for displacement by moving devices is provided for sewer pipe reconstruction and has a radial nozzle applying by extrusion a thermoplastic tube to the inside wall of a sewer pipe to be reconstructed. The thermoplastic tube is pressed against the inside wall by pressurized air and cooled down to form a lining pipe.

Apparatus for lining an inside wall of a sewer pipe

A plurality of reactors, which can all be interconnected selectively by way of pipes, are used for the hydrolytic separation of a cellulose-containing substrate so that a stepwise pressure reduction in one reactor is made possible and thus a stepwise pressure build-up in all the other reactors. The steam entering and leaving the reactors is used to produce a fluidized bed of the substrate. A high output with a low specific expenditure of energy is achieved by these measures.

Method and apparatus for the hydrolytic separation of cellulose

The invention relates to an apparatus for converting sewage-sludge filter cakes into oil, gas and coke by pyrolysis. The apparatus has two dewatering stages--a preliminary evaporating stage and a residual evaporating stage, a conversion stage and a cooling stage. Each of the evaporating, converting and cooling stages are constructed with at least one module. Each module has a housing divided by walls into a transfer chamber at one end and a second chamber at the other end. The second chamber is divided between a feed chamber and a delivery chamber. Between the transfer chamber and the second chamber is a heat transfer chamber. In the heat transfer chamber there are a plurality of first tubes connecting the feed chamber to the transfer chamber and a plurality of second tubes connecting the transfer chamber to the delivery chamber. Conveyors are provided in each of the tubes to deliver solid feed material from the feed chamber to the first tubes into the transfer chamber and then from the transfer chamber to the delivery chamber where the matter is then fed to another module according to the desired treatment. The tubes are spaced apart from each other to permit a heat transfer medium to be fed into and out of the heat transfer chamber.

Apparatus for converting sewage sludge filter cake by pyrolysis

A method for acid-catalyzed hydrolytic splitting of cellulose to give a high yield in sugar with a minimal expenditure in energy, in particular, with the smallest possible charge of live steam. Admission of steam is performed in a plurality of successive, discrete reaction stages having in each case defined temperature and pressure values in such a manner that the temperature rises from one stage to the next while the reaction time decreases and a rapid expansion takes place subsequently to the last reaction stage. A high pressure poured bed reactor is used for performing this method.

Method the hydrolytic splitting of acid treated comminuted crude

A process for the hydrolysis of cellulose from vegetable raw materials to glucose, particularly using wood as the raw material, comprises conveying the raw material through a hydrolysis zone in finely comminuted form, the raw material being impregnated with dilute acid and at a sufficiently high hydrolysis temperature. The raw material impregnated with dilute acid is supplied in portions and continuously through the hydrolysis zone where it is heated to a hydrolysis temperature of above 250.degree. C. by means of high pressure steam. This takes place in an extremely short time accompanied by a sudden pressure rise. Apparatus for performing this process comprises a tubular reactor having at least one straight pipe through which can be conveyed an endless piston chain. The pistons of this chain form a leakage gap opposite the inner wall of the pipe and, in each case, two adjacent pistons define a piston chamber. A high pressure steam line is arranged to issue approximately into the center of the pipe.

Process for the hydrolysis of cellulose from vegetable raw materials to

In a procedure and an installation for the incinerating of sludge, predried sludge is dried to residual moisture by the addition of heat in a first processing step and then pyrolized by the continued addition of heat and the exclusion of air in a second processing step, with the pyrolysis gas obtained being used at least partially to generate the hot fumes required for heat input. To incinerate sludge in a way which is compatible with the environment, saves energy and is inexpensive, the predried sludge is carried co-current with the hot fumes in the first processing step and the so-dried sludge is then, in the second step, carried in countercurrent flow to those same fumes. An evaporation worm-gear machine (1) with a worm shaft (9) capable of being driven by rotation, with at least one spiral coil (14), which is placed in a housing (3) serves to carry out the first processing step, while a pyrolysis rotation cylindrical reactor (2) with an opposite direction of movement of the material which is in the hollow-built worm shaft (9) serves to effect the second processing step.

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Stuttgart, Germany

Klaus-Jurgen Hinger