US 4,802,341 AGrant
Adsorption Apparatus Test as an Electro-Heating Storage
Issue Date:1989-02-07
•10 Claims
•1 Drawing Sheets
Abstract
Periodic absorption apparatus with the substance pair zeolite/water being used as electro-head storage devices. Due to the heat pumping effect there can be a 30% savings of power.
Metadata
Inventors
- Peter Maier-Laxhuber
- Fritz Kaubek
Application Information
Application Number:US 6954847
Filing Date:1985-01-28
Priority Date:1984-04-09
Art Unit:344
Classifications
IPC:
F25B 2700
Field of Search:
237622192 B238.3;238.5;477;235.1;476;477;478;479378
Patent Drawings (1 sheets)
Description
Background of the Invention
The invention relates to an adsorption apparatus with hear pumping effect used as as electro-heating storage.
In order to smooth the severely fluctuating current use, electro-heat storages are employed. During tariff-favorable current a storage material, like ceramic, cast iron, oil or water is heated, for example, during the charge phase. The stored heat is fed to the consumer via suitable heat removing systems during the subsequent discharging phase. Night time current storages are in use for heating individual rooms and central heat storages which supply a plurality of consumers from one location through a heat distribution system. In order to keep the space requirement for the electro-heat storages as low as possible, the storage materials are partially heated to a temperature above 900.degree. C. Undesirable heat losses must be prevented with expensive insulation measures. A heat pumping effect with a corresponding energy saving is not possible with these devices.
Zeolites are solid alumini-silicates with a uniform crystal structure. Adsorption zeolites have the characteristics of being able to adsorb a considerable amount of water in its crystal structure. Heat is released during this adsorption. In order to again desorb the water, heat must be used.
Heat storage installations with the adsorption pair of zeolite/water are suggested in German laid open patent applications Nos. P 32 07 656 and P 32 12 608. By means of low-tariff current steam is desorbed from the adsorption zeolith and liquified in a condenser. The condensated steam is again evaporated at a later time by absorbing ambient heat and adsorbed in the adsorption substance by releasing heat at high temperatures. The control of such installations is only possible by a plurality of valves or check valves with corresponding control units. This control effort is not economical with small electro-heat storages despite a 30% saving of energy.
Summary of the Invention
It is, therefore, an object of the invention to use periodic adsorption processes as electro-heat storages and to save energy by means of available pump effect.
The adsorption electro-heat storage in accordance with the invention consists of the conventional parts electro heating, heat removal system and control, on the one hand, and the adsorption part, on the other hand. The adsorption part consists of two containers which are connected by means of a steam line; namely the adsorption substance container which in the conventional part of the electro-heat storage replaces the storage material and the collecting container for condensate. A steam line leads from the containers to a condenser and a water cycle leads to a heat collector. The water cycle contains a pump. The mode of operation is divided into two phases;
(a) charging phase - the adsorption substance container is heated to 200.degree.-300.degree. C. by means of the electro-heater. Thereby, steam is desorbed from the adsorption substance which is liquified in the condenser and flows as a condensate into the collecting container. The condensation heat is discharged as an operating heat at temperatures up to 100.degree. C.;
(b) discharge phase - the electro-heater is out of operation. Heat is removed from the adsorption substance container through the conventional heat removal system. Condensate evaporates in the collecting container during lower steam pressures and cools the remaining water. The steam is exothermically adsorbed by the adsorption substance at high temperatures. The adsorption heat can be removed through the heat removal system if so desired. The pump of the water cycle feeds cooled residue condensate through the heat collector. So that the water cycle does not dissipate heat to the heat collector, a control unit actuates the pump only when the temperature in the heat collector is higher than the condensation temperature in the collecting container. Moreover, the operation of the pump may be made dependent from other criteria through this control unit. For example, the pump may only be operated after a certain temperature had been exceeded in the heat collector.
This process can be advantageously used for safety against frost or for maintaining a certain temperature of the exhaust heat (for example, waste water, cooling air).
The possibility exists in conventional electro-heat storages for room heating to aftercharge the heating storage with current during the daytime on extremely cold days. Since during these very cold days the heat reception through the heat collector may be limited, an aftercharge is advantageously transmitted to the system through an electrical heater in the collecting container. Thereby, the heat dissipation capacity from the adsorption electro-heating storage increases by about 30% with respect to the aftercharge capacity, since the adsorption of the steam in the adsorption substance releases the chemically stored adsorption heat.
The adsorption electro-heat storage in accordance with the invention can be advantageously integrated into a tile hearth. In this case, hot combustion gases take over the desorption operation from case to case. In this manner, the tile hearth can store more heat and recover additional heat through the heat collector. The cooling time of the tiled hearth is prolonged.
A further advantageous possibility of use is the coupling of an adsorption electro-heat storage with a hot water storage. The adsorption part recovers additional heat through the heat pumping effect from the air or the waste water and permits a small structural size of the water storage. The use of night current is also advantageous for the utility company during the summer time.
Adsorption apparatuses operate at least partially under vacuum conditions. A sufficient tightness of the system is the basic requirement for a smooth operation. It is therefore suggested to assemble the adsorption part as a compact, finished apparatus part by the manufacturer. When using the heat collector as an outside adsorber, it must be pushed through the building wall to the outside, while the remainder of the device components remain within the building. For this purpose, a wall box is built into the building wall which is closed with a suitable insulation element during the installation of the device. This insulation element fixed the heat collector to the outside and leaves room on the inside for the flexible condensation lines to the collecting container.
In a further advantageous development the insulation element is provided with a ventilation system which feeds hot exhaust air from the building to the outside positioned heat collector for recovery.
The zeolite types Na-A, Mg-A, Na-Y, H-Y and Na-X have been shown to be useful as adsorption substances. They have very good adsorption characteristics for water in addition to a sufficient temperature and cycle stability.
The condensate in the collecting container may freeze due to the evaporation operation. The latent heat which is thereby released can be additionally used for the adsorption heat in the adsorption substance during increased temperatures. In a sufficiently large dimensioned collecting container, the total evaporation enthalphy may be supplied by the latent conversion heat. The ice which is generated in the discharge phase is again molten during the condensation heat. About 1.3 Kilogram water is required per Kilogram of adsorption substance.
If no conversion heat is to be used and when heat is coupled in through the heat collector from the environment at temperatures below 0.degree. C., an antifreeze agent may be added to the water. Suitable substances are salts or lyes which have a low steam pressure.
If only ambient heat is collected above 0.degree. C., no antifreeze agents are required. The heat collector may be installed above the maximum water level in the collecting container, so that the heat collector does not freeze during the frosty weather. The water would then return into the collecting container when the pump is in the rest position. A water syphon in the water cycle prevents a condensation of steam in the heat collector during the charge phases and also prevents a loss of heat to the outside.
The described adsorption electro-heat storage does not contain any valves and requires only a small control effort for the control of the pump. The costs for power are lower by about 30% with respect to the conventional systems. The electrical connecting line is reduced by about one third.
Ventilation heat losses can be reduced by a simple heat recovery of the exhaust air. Since all components of a conventional electro-heat storage can be used, with the exception of the storage material, only a small amount of additional cost is incurred. A heat pumping installation with heat recovery possibilities is obtained from a pure heat storage device with a favorable control. During the discharge phase the new system is always ready to absorb ambient heat, in contrast to other heat pumping systems, no matter how high the temperatures and amounts are. Even the smallest heat amounts can be used without limitation.
Brief Description of the Drawings
Exemplified embodiments of the invention are illustrated in the drawing and are described in more detail in the following. In the drawings:
FIG. 1 - an adsorption electro-heat storage for room heating; and
FIG. 2 - an adsorption electro-heat storage in combination with a hot water storage.
Detailed Description of the Preferred Embodiments
FIG. 1 shows an adsorption substance container 1 on which a small collecting container 2 is connected. From there, a steam line 3 leads to a condenser (4) and two flexible liquid lines 5 lead to a heat collector 6. The associated water cycle contains a pump 7. The operation is divided into two phases:
a. Charge Phase
The adsorption substance container is heated to a temperature of 250.degree.-300.degree. C. by means of electric heating rods 8. During this time water is evaporated from the adsorption substance. The steam can condense in condensator 4 and dissipate heat to the room air. The condensate flows into the collecting container 2 and remains there until the discharge phase.
b. Discharge Phase
The adsorption substance container is cooled by the air flow. During a lowering of the adsorption substance temperature there is also a lowering of the steam pressure in the containers. Water from the collecting container gets cold and the adsorption substance hot. Whenever the water temperature in the collecting container 2 falls below the outer temperature pump 7 pumps water through the heat collector. The cold water absorbs heat from the outer air and transfers it to the evaporating water in the collecting container 2.
FIG. 2 shows a combination of an adsorption electro-heat storage with a hot water storage. Condenser 24 is mounted within the hot water storage 28. During the charging phase the condenser dissipates the condensation heat to the water storage 28. During the discharge phase the operating heat is transferred from the adsorption substance container 21 through a water-steam-system to the water. When the storage water is too cold, the valve 29 opens. Water flows from container 30 to the evaporator 31 and evaporates therein. The steam dissipates the condensation heat in the liquefier 32. The condensate again collects in container 30.
Thus, the several aforementioned objects and advantages are most effectively attained. Although several somewhat preferred embodiments have been disclosed and described in detail herein, it should be understood that his invention is in no sense limited thereby and its scope to be determined by that of the appended claims.
Claims
We claim:
1. Adsorption apparatus for use as electro-heat storage by using the heat pumping effect, comprising: an adsorption substance container containing an adsorption substance, said adsorption substance being capable of adsorbing water and being heatable by an electric heating system as to desorb steam from said adsorption substance; a condenser for liquifying said steam to form a condensate; a collecting container for collecting said condensate, said adsorption substance container being in vapor communication with said collecting container by a steam line, said condenser being in vapor communication with said collecting container so that desorbed steam from said adsorption substance can be liquified by said condenser to form said condensate and said condensate collects in said collecting container; a heat collector for collecting ambient heat; a water cycle connected between said collecting container and said heat collector; and a circulation pump installed in said water cycle for circulating said condensate.
2. Adsorption apparatus in accordance with claim 1 wherein said apparatus further comprises, a control device for comparing the temperature of said heat collector with the temperature of said condensate in said collecting container.
3. Adsorption apparatus in accordance with claim 1 wherein zeolite selected fro the group consisting of type Na-A, Mg-A, Na-Y, H-Y and Na-X is used as adsorption substance.
4. Adsorption apparatus in accordance with claim 1 wherein an additional electrical heating unit is installed in the lower part of said collecting container.
5. Adsorption apparatus in accordance with claim 1 wherein an antifreeze agent having a low boiling point is admixed with the water in said water cycle.
6. Adsorption apparatus in accordance with claim 1 wherein the lines of said water cycle are slightly bendable at certain segments, so that position changes are made possible during the installation of the heating collector with respect to the collecting container without opening said water cycle.
7. Adsorption apparatus in accordance with claim 1 wherein said heat collector is positioned higher than the maximum water level in said collecting container, so that the water in said heat collector can run from said heat collector back into said collecting container under the force of gravity.
8. Adsorption apparatus in accordance with claim 1 wherein the lines of said water cycle extend through an insulation element which closes the installation opening for the installation of said heat collector.
9. Adsorption apparatus in accordance with claim 8 wherein a ventilation system is integrated in said insulation element which feeds hot exhaust air to said heat collector.
10. Adsorption apparatus in accordance with claim 1 wherein the water level in said collecting container is dimensioned sufficiently large that the latent heat which is released during icing is sufficient to replace the heat amount which said heat collector cannot feed.