Abstract: A plate type heat exchanger includes a plurality of laminated plates 11 each having a resin-covered gasket 15 mounted in a gasket groove 13 therein surrounding a heat transfer surface 12. The resin-covered gasket includes a core 15a of elastic material whose liquid-contacted side surface is covered with a corrosion-resistant resin cover 15b. In this plate type heat exchanger, the liquid-noncontacted side of the core 15a is integrally formed with a fixing element 16, while the outer peripheral surface of the plate 11 is formed with a recess 14 adapted to fit on the fixing element 16. Thus, the resin-covered gasket 15 can be mounted in the gasket groove 13 without using any adhesive agent.

Abstract: The invention presents a method, apparatus and container for sterilizing solid matter or liquid matter containing solid matter efficiently in a short time, while preventing deterioration of quality or decline of flavor.In this method, solid matter (a) and liquid matter (b) are separately heated and sterilized, and both are mixed after being sterilized, and put and sealed in a bag (c) or container. When heating and sterilizing the solid matter independently, the solid matter is weight and dispensed in each retainer (c) by the portion of one pack each, and sterilized, and is transferred, after being sterilized, from the retainer (d) into a bag (c) or container, and sealed. Sterilization is executed by rotating the retainer (d) and inducing an agitating action on the inside solid matter.

Abstract: A plurality of stacked trays 2 are accommodated within a rotary housing 3 rotatably supported in a sterilization vessel 1 (FIG. 7a). A medium support port 42a is sealingly engaged with an inlet port 25. Then, a flow of hot water is supplied to the inlet port 25. Thus, a spray hot water is ejected from spray nozzle 23 for heat sterilizing products on the trays 2. Thereafter, a spray of cooling water is ejected from the spray nozzle 23 for cooling the products. The rotary housing 3 is rotated to a position in which inclination of the trays 2 exceeds 90 degrees. Then, the rotary housing 3 is counter-rotated to a position in which the trays 2 are inclined at a vertical orientation (FIG. 7b). A hot gas supply port 37a is sealingly engaged with the inlet port 25 so as to supply a flow of hot air into the inlet port 25, whereby the products may be dried.

Abstract: An object of the present invention is to mass-produce fried food of high quality having no unevenly fried spots by making uniform the amount of cooking oil for frying food fed to food and the temperature distribution of the oil. A plurality of stacked pan-like trays (10) are received in a closable processing tank (1) and heated cooking oil is rapidly fed into the trays (10) through the side wall thereof by oil feed nozzles (41) so that the oil flows on the bottoms of the trays (10) at a given flow rate, the excess oil being allowed to overflow from the side opposite to the oil feed side to flow downwardly of the trays (10). The stacked trays (10) are individually fed with oil by the oil feed nozzles (41) so that none of the oil flowing from upper trays enters lower trays. The oil feed nozzles (41) are slidable back and forth relative to the trays (10), and the processing tank (1) is pressurized or evacuated according to the cooking conditions for articles of food a.

Abstract: A thin film flow-down type concentrating apparatus for concentrating a heat susceptible raw liquid with heated steam to high concentration without spoiling the flavor or deteriorating the quality by alternately laminating raw liquid plates and steam plates 20, in which the width of the raw liquid heating passage 18 is gradually narrowed from the raw liquid inlet to the concentrate outlet. As a result, if the volume of the raw liquid decreases due to evaporation and separation of the moisture in the raw liquid, scorching is prevented. Besides, by the steam generated from the raw liquid, in order to prevent increase of the flow velocity of the concentrate going toward the concentrate exit, the plate intervals of the raw liquid heating passage is gradually widened from the raw liquid inlet toward the concentrate outlet.

Abstract: This invention relates to a spray type retort sterilizer which preforms various types of high-pressure sterilization. Sterilization is achieved through the use of non-atomized hot water droplets. The sterilized comprises a retort that is capable of receiving multiple trays of materials, a pressurized air intake system for introducing pressurized air into the retort, an exhaust system and multiple spray units capable of spraying liquid such that at least one spray unit is disposed adjacent to each tray of material. The invention is further defined to include a heat exchanger and a pump for removing the liquid from the retort, passing it through the heat exchanger and delivering the liquid to the spray units. The invention is further defined to include spray units that are rotatable.

Abstract: A wood treating method and apparatus whereby a wood which is thin or bent, such as a soft wood or wood removed during growth or a wood from thinning, is strengthened, straightened and molded in any desired shape, wherein after the wood is heated and softened in a high temperature high pressure atmosphere, mechanical compressive forces are applied to the wood to minimize the voids in the wood; thus, the wood is hardened, strengthened and the bent wood is corrected, making it possible to form the wood in any desired shape without lumbering the same.

Abstract: A wood treating method and apparatus in which a wood which is thin or bent, such as a soft wood or wood removed during growth or a wood from thinning, is strengthened, straightened and molded in any desired shape, wherein after the wood is heated and softened in a high temperature high pressure atmosphere, mechanical compressive forces are applied to the wood to minimize the voids in the wood; thus, the wood is hardened, strengthened and the bent wood is corrected, making it possible to form the wood in any desired shape without lumbering the same.

Abstract: A plate-type heat exchanger comprises a plurality of plates laminated through gaskets fixed in gasket grooves formed in the entire peripheral edges thereof without using any adhesive agent. The liquid-noncontacted peripheral side surface of the gasket body of the gasket is integrally formed with suitably spaced fixing tabs each comprising a plurality of projecting pieces projecting from the gasket body, and at least a fixing piece extending parallel with the gasket body. The plate is formed with gasket fixing portions associated with the fixing tabs of the gasket for fixing the fixing tabs by force-fitting the fixing pieces of the fixing tabs in slits extending parallel with the gasket groove.

Abstract: A thin film downward flow type plate concentrator suitable for concentration of liquids which are highly heat-sensitive, wherein preheating channels (19), distributing portions (23), pool portions (24) and heating channels (18) which are formed in heat transfer plates (10) are improved to provide efficient concentration of a raw liquid in one-pass. These various portions are given respective channel shapes most suitable for their respective roles with respect to the raw liquid; thus, the total heat transfer performance is improved.

Abstract: An evaporating apparatus includes an evaporator (E) for converting a liquid into vapor and a preheater (2) for heating the liquid before it is fed to the evaporator (E). A pump (6) for feeding the liquid to the preheater (2) and another pump (8) for pressurizing the liquid passing from the preheater (2) to the evaporator (E) are provided, where the former maintains the liquid at a saturation pressure with respect to a temperature slightly higher than a saturation temperature (t.sub.o) at the preheater outlet, and the latter serves to raise the liquid pressure to a saturation pressure with respect to a desired evaporation temperature (t.sub.2). Rate of flow of a heating medium for the preheater (2) is controlled so that its temperature (t.sub.w3) is slightly higher than a liquid preheater outlet temperature (t.sub.ex). Thus, in the preheater (2), the liquid temperature (t.sub.ex) is maintained lower than saturation temperature (t.sub.o), ensuring a greater amount of heat transfer by subcool boiling.

Abstract: A heat recovery system including a closed working fluid loop constituted by connecting an evaporating apparatus supplied with warm waste water, a steam turbine having an output shaft to be coupled to the load, and a condensing apparatus supplied with cooling water, works on the basis of a Rankine cycle and utilize non-azeotropic mixture as the working fluid.

Abstract: A heat recovery system including a closed working fluid loop constituted by connecting an evaporating apparatus supplied with warm waste water, a steam turbine having an output shaft to be coupled to the load, and a condensing apparatus supplied with cooling water, works on the basis of a Rankine cycle and is adapted to utilize a non-azeotropic mixture as the working fluid.

Abstract: A heat recovery system including a closed working fluid loop constituted by connecting an evaporating apparatus supplied with warm waste water, a steam turbine having an output shaft to be coupled to the load, and a condensing apparatus supplied with cooling water, works on the basis of a Rankine cycle and utilize a non-azeotropic mixture as the working fluid.

Abstract: An evaporating apparatus comprising a high temperature side evaporator and a low temperature side evaporator connected in series in a flowing direction of a heat source, a first and second pipe line for directing fluid being evaporated therethrough, and an ejector having a suction inlet and a discharge outlet of drive steam and an induction port of steam being sucked, wherein the first pipe line is linked through the high temperature side evaporator to the suction inlet of the ejector, and the second pipe line is branched from the first pipe line at the upstream side of the hot temperature side evaporator, and linked through the low temperature side evaporator to the induction port of the ejector.

Abstract: A plate type evaporator comprising a plurality of vertically extending plate elements assembled face-to-face to define therebetween alternate channels for a heating medium and for a liquid to be evaporated. The plate elements have porous layers formed on their opposed heat transfer surfaces functioning as the channels for the liquid to be evaporated. The porous layers are utilized as nuclear boiling accelerating members to improve the capability of evaporating liquid on the boiling heat transfer surfaces.

Abstract: A plate type evaporator comprising a plurality of vertically extending plate elements assembled face-to-face to define therebetween alternate channels for a heating medium and for a liquid to be evaporated. In order to accelerate the nuclear boiling of the liquid in the liquid channels, the heat transfer surface of each plate element has a plurality of vertically extending transversely spaced ridges projecting toward the associated liquid channel, such ridges being in contact with the heat transfer surface of the opposed plate element to provide areas of contact assisting in the evolution of vapor bubbles and divide the liquid channel into narrow sections assisting in the generation of vapor, such sections also assuring that even in deeper places in the liquid channel, vapor bubbles will be generated without yielding to the liquid pressure; alternatively, each plate element has a porous layer formed on its heat transfer surface facing the liquid channel.

Abstract: A cross-current type plate heat exchanger comprising a plurality of vertically disposed heat transfer plates arranged side by side to define fluid passageways through which two fluids to be heat exchanged flow in a cross-current fashion. Each heat transfer plate is formed with a plurality of juxtaposed vertical grooves extending from the top to the bottom of the heat transfer surface of the heat transfer plate, and a plurality of substantially horizontal projections are formed between the vertical grooves to divide the heat transfer area into a plurality of sections. Vertically extending short projections which are lower than the vertical grooves are formed between the substantially horizontal projections in such a manner that the number of such short projections provided in the vertically separated sections is progressively increased so that the bottommost section has the greatest number of short projections.

Abstract: A structure of fluid condensing and heat conducting surface of the condenser characterized in that completely recessed grooves for collecting fluid are provided on said surface integrally therewith, wherein the distance between the centers of radii of rounded corners of said groove is made less than 3 mm.

Abstract: A plate heat exchanger comprises a laterally arranged cylindrical container having an inlet and outlet for one of both media and those for the other medium and opening at one end, a plurality of heat exchange units each including a pair of opposite frames and a pack of plate elements therebetween and being inserted in sequence into the container, and a press lid attached to said one opening end of container under condition of thrusting said plurality of heat exchange units. The plate elements are clamped face to face through surrounding sealing surrounding sealing strips respectively to form between the plates interspaces through which the media flow. Every second interspace among the interspaces is closed with respect to the space within the container and communicates with said inlet and outlet for said one medium.