Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
402 words
Process for adsorptive separation of crude gas mixtures by vacuum swing adsorption in two containers filled with adsorbent said containers being adsorbers A and B which are provided with a bottom and top inlet and discharge end, the gas content which is adsorbed less strongly, if at all, (raffinate) being obtained under reduced pressure, said process comprising (F1) operating the two adsorbers A and B alternately so that the crude gas fed into the adsorbers is not stopped at any time during the course of the process, a vacuum pump remaining continuously connected to the adsorbent packing, (a) at time t 1 depressurizing adsorber A at the top end, the gas released in this way flowing into the top end of an evacuated adsorber B, adsorber A being connected at the bottom end to a vacuum pump and adsorber B being filled at the bottom end with crude gas, (b) at time t 2 evacuating adsorber A and filling adsorber B at the top end with raffinate from a raffinate reservoir R, adsorber B being filled at the bottom end under reduced pressure with crude gas, (c) at time t 3 , evacuating adsorber A at the bottom end and filling adsorber B the bottom end with crude gas, or crude gas flows through adsorber B at the bottom end, starting at a pressure of 1 bar, and stripping off the gas content which is adsorbed less strongly as the product at the top end of adsorber B, (d) proceeding further with the process by repeating the times t 1 , t 2 and t 3 adsorbers A/B being changed over, or alternatively in a two-adsorber VSA process (e) at time t 1 depressurizing adsorber A at the top end, the gas released in this way flows into the top end of the adsorber B, which is operated under reduced pressure, charging adsorber A at the bottom end with crude gas, adsorber B is connected at the bottom end to a vacuum pump, but the pressure in adsorber B rises here due to the entry of gas from adsorber A, and the pressure in adsorber A falls, (f) at time t 2 the process proceeding analogously to (1b), (g) at time t 3 the process proceeding analogously to (1c), (h) the process proceeding further by repeating the times t 1 , t 2 and t 3 , adsorbers A/B being changed over.
Claim 2
Dependent Claim
402 words
Process for adsorptive separation of crude gas mixtures by vacuum swing adsorption in two containers filled with adsorbent said containers being adsorbers A and B which are provided with a bottom and top inlet and discharge end, the gas content which is adsorbed less strongly, if at all, (raffinate) being obtained under reduced pressure, said process comprising (F1) operating the two adsorbers A and B alternately so that the crude gas fed into the adsorbers is not stopped at any time during the course of the process, a vacuum pump remaining continuously connected to the adsorbent packing, (a) at time t 1 depressurizing adsorber A at the top end, the gas released in this way flowing into the top end of an evacuated adsorber B, adsorber A being connected at the bottom end to a vacuum pump and adsorber B being filled at the bottom end with crude gas, (b) at time t 2 evacuating adsorber A and filling adsorber B at the top end with raffinate from a raffinate reservoir R, adsorber B being filled at the bottom end under reduced pressure with crude gas, (c) at time t 3 , evacuating adsorber A at the bottom end and filling adsorber B the bottom end with crude gas, or crude gas flows through adsorber B at the bottom end, starting at a pressure of 1 bar, and stripping off the gas content which is adsorbed less strongly as the product at the top end of adsorber B, (d) proceeding further with the process by repeating the times t 1 , t 2 and t 3 adsorbers A/B being changed over, or alternatively in a two-adsorber VSA process (e) at time t 1 depressurizing adsorber A at the top end, the gas released in this way flows into the top end of the adsorber B, which is operated under reduced pressure, charging adsorber A at the bottom end with crude gas, adsorber B is connected at the bottom end to a vacuum pump, but the pressure in adsorber B rises here due to the entry of gas from adsorber A, and the pressure in adsorber A falls, (f) at time t 2 the process proceeding analogously to (1b), (g) at time t 3 the process proceeding analogously to (1c), (h) the process proceeding further by repeating the times t 1 , t 2 and t 3 , adsorbers A/B being changed over.
Claim 3
Dependent Claim
29 words
Process according to claim 1, wherein the release of the gas content adsorbed less strongly, if at all, takes place under 1 bar or 1 bar to 3 bar.
Claim 4
Dependent Claim
21 words
Process according to claim 1, wherein the entire cycle time t 1 +t 2 +t 3 is 10 to 120 seconds.
Claim 5
Dependent Claim
23 words
Process according to claim 1, wherein the pressure at time t 1 of the adsorber to be depressurized drops to below 1 bar.
Claim 6
Dependent Claim
21 words
Process according to claim 1, wherein (a) oxygen is obtained adsorptively from air or (b) argon is obtained adsorptively from nitrogen.
Claim 7
Dependent Claim
57 words
A VSA separation process based on three beds, two beds of which operate according to the process of claim 1, said separation process based on three beds being changed over automatically to said two bed process in the event of malfunction of a valve of an adsorber unit, so that operation is maintained only with two adsorbers.
Claim 8
Dependent Claim
82 words
A VSA separation process based on three adsorber units, two of which operate according to the process of claim 1, the three adsorber units being chosen so that one adsorber is connected to a vacuum pump within time t 1 +t 2 +t 3 and two adsorbers are charged with crude gas with a time lag, the time lag being t 1 +t 2 +t 3 , and the adsorption time of an adsorber is 2×(t 1 +t 2 +t 3 ).