Zeolite, method for production thereof, adsorbent comprising said zeolite, heat utilization system, adsorption heat pump, heating and cooling storage system and humidity controlling air-conditioning a
An adsorbent and zeolite technology, applied in the field of air conditioning devices, can solve the problems of deprivation of zeolite adsorption capacity and zeolite instability, and achieve the effects of excellent durability and high adsorption capacity
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[0200] Next, the calcining step in the method for preparing zeolite of the present invention will be explained.
[0201] The calcination step is a process of heat-treating the zeolite precursor that has been hydrothermally synthesized in the above-mentioned manner and separated under a given condition in a nitrogen-diluted air stream or the like or under vacuum. As a result, the zeolite of the present invention was produced.
[0202] In this calcination step, the calcination conditions are adjusted to control the removal of the nitrogen-containing organic template to thereby produce a zeolite containing at least a given amount of carbon or at least a given amount of nitrogen and carbon. A method may be employed in which, after the organic template is completely removed by calcination, a nitrogen-containing compound such as an organic compound, for example an organic amine such as methylamine or ethylamine is adsorbed onto the pore wall to thereby produce a compound containing ...
Embodiment 1-1
[0316] Hydrothermal synthesis and calcination were performed in the following manner to produce nitrogen-containing zeolites.
[0317] First 11.53g of 85% phosphoric acid was added to 28.05g of water. Thereto was gradually added 5.44 g of pseudo-boehmite (containing 25% of water, produced by Condea). The resulting mixture was stirred. This mixture is referred to as Liquid A. In addition to Liquid A, a liquid was prepared by mixing 5.56 g of ferrous sulfate heptahydrate, 4.35 g of morpholine, 5.06 g of triethylamine and 29 g of water. This liquid was gradually added to Liquid A and the resulting mixture was stirred for 3 hours to obtain a gel-like starting reactant material having the following composition.
[0318] 0.4FeSO 4 : 0.8Al 2 o 3 :P 2 o 5 : 1.0 Morpholine: 1.0 Triethylamine: 70H 2 o
[0319] The resulting starting reactant material was introduced into a 200-cc stainless steel autoclave equipped with a Teflon (trade mark) inner cylinder. The starting materia...
Embodiment 1-2
[0327] A roasted product as a nitrogen-containing zeolite was obtained in the same manner as in Example 1-1, except that the roasting temperature and the oxygen concentration in the passing gas were changed to 340° C. and 5% by volume, respectively.
[0328] The obtained calcined product had a nitrogen content of 1.7 wt%, a carbon content of 3.1 wt%, and a C / N weight ratio of 1.83. From the XRD pattern obtained in the same manner as in Example 1, it was found that the calcined product had a pure CHA structure (FD, 14.5 T / nm3).
[0329] Its water vapor adsorption capacity (25°C) was 27 wt%. The pore utilization factor determined using Equation 3 was 0.9. Durability Test 1 was carried out, as a result, no decrease in adsorption was observed and the degree of crystallinity remained unchanged. The weight loss (g1) and weight loss (g2) of the roasted product were further measured. The results are shown in Table 1.
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Abstract
Description
Claims
Application Information
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