| Document |
Document Title |
|
JPS5959241A |
PURPOSE: To increase the quantity of heat supplied to a waste heat utilizing installation and to enhnace the heat utilization efficiency thereof to a large extent, by a method wherein a part of hot gas in the upstream side of a heat exch...
|
|
JPS5955340A |
In reheating and conveying a granular heat carrier, such as sand, using a carrier gas, where the heat carrier may be utilized for desorption by heating a charged lumpy adsorbent, the heat carrier is circulated through a vertically arrang...
|
|
JPS5913459B2 |
|
|
JPS5952523A |
PURPOSE: To make it possible to automatically control the operation of the titled apparatus, by a method wherein a chinker layer is always monitored by an infrared ray imaging apparatus and the temp. distribution of said clinker layer is...
|
|
JPS5912338B2 |
|
|
JPS5912339B2 |
|
|
JPS5911335B2 |
|
|
JPS5911334B2 |
|
|
JPS5911336B2 |
|
|
JPS5911333B2 |
|
|
JPS5927444U |
|
|
JPS596828B2 |
|
|
JPS5923522U |
|
|
JPS594744Y2 |
|
|
JPS594793Y2 |
|
|
JPS596172B2 |
|
|
JPS596170B2 |
|
|
JPS596169B2 |
PURPOSE:Air from the cooler and exhaust gas from the firing furnace are adjusted to a selected temperature and introduced into the dryer so that the hot gas to the electric dust collector can be maintained over the dew point and that the...
|
|
JPS596171B2 |
|
|
JPS596168B2 |
PURPOSE:Dried material is distributedly charged into a floating type heat exchanger, thereby adjusting the temperature of introduced exhaust gas from the heat exchanger into the dryer to a selected temperature, whereby the resultant effe...
|
|
JPS595541B2 |
|
|
JPS595338B2 |
PURPOSE:To carry out calcining with high efficiency by setting up a high wind velocity zone at the lower part of the dense suspension layer, on occasion of calcining raw material of cement or alumina and heating the pulverulent and granu...
|
|
JPS595008B2 |
|
|
JPS594393B2 |
|
|
JPS594394B2 |
Fine-grained material adapted to be fired in a furnace is discharged from a preheater into a gas conduit extending from the furnace to the preheater and through which a stream of hot gases pass. The conduit is shaped to deflect the gas s...
|
|
JPS593951B2 |
A method is disclosed for heat treating pulverulent or granular raw material such as cement meal. Raw material is directed to at least two multi-stage preheater strings, the first string communicating with the kiln by a smoke riser pipe ...
|
|
JPS5912746A |
PURPOSE: To attain to lower the irregularity in the quality of a product, in a Dwight- Lloyd sintering machine, a slit almost at right angles relative to the advance direction of a pallet is formed to the surface layer of a sintering sto...
|
|
JPS593167B2 |
|
|
JPS5912747A |
PURPOSE: To carry out the preheating of a stock powder and the heating of a fluid in a heating pipe simultaneously in good efficiency, by a metod wherein a heat exchanger part having a heat recovering heating pipe provided therein is pro...
|
|
JPS591992Y2 |
|
|
JPS59251B2 |
|
|
JPS59250B2 |
1531458 Utilizing waste heat in calcining process ASSOCIATED PORTLAND CEMENT MFRS Ltd 12 March 1976 [12 March 1975] 10303 /75 Heading F4B In a calcination process comprising an endothermic stage and an exothermic stage, at least part of ...
|
|
JPS59252B2 |
PURPOSE:To carry out the stable roasting with a cheap cost of equipment and moreover with a small heat consumption, by circulating a part of the raw material with the sequence of the dryer, the separator of dried raw material and the sup...
|
|
JPS59326A |
(57) [Abstract] Since this gazette is application data in front of an electronic application, the data of an abstract is not recorded.
|
|
JPS5857382B2 |
|
|
JPS5857381B2 |
|
|
JPS5855215Y2 |
|
|
JPS58186845U |
|
|
JPS5855091B2 |
|
|
JPS5854105B2 |
|
|
JPS5852694B2 |
|
|
JPS58199036A |
PURPOSE: To improve the enriching efficiency of oxygen by subjecting a calcined material to heat exchange with air having an increase oxygen concn. then using nearly the entire quantity of said air as secondary air for combustion. CONSTI...
|
|
JPS58196837A |
A method and apparatus for reducing the sulfur content and/or the SO2 emission in a system for calcining fine grained materials such as in the manufacture of cement utilizing a pre-calcining and a final calcining stage. The sulfur conten...
|
|
JPS5846462B2 |
|
|
JPS5842873Y2 |
|
|
JPS58163545A |
The main characteristic lies in the fact that the fumes leaving the calcining furnace (22) are used to heat a current of air which is then used, in its turn, to heat the sand to be treated at its inlet to the calcining furnace, and in th...
|
|
JPS5843334B2 |
Glass is tempered by contact with solid particles fluidised with a gas to ensure that transfer from the glass the glass to the particles. The fluidised material is kept in a steady state of uniform fluidisation. Pref. the fluidised bed i...
|
|
JPS58141731U |
|
|
JPS58156338A |
For liquefying hot melt adhesive, a hopper is provided at its lower region with one or more discrete upwards projections (for example a single, fluted cone), with means for heating the projection(s). In use, a unitary mass of hot melt ad...
|
|
JPS5837463Y2 |
|
