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    • 1. 发明专利
    • CONTROL METHOD OF AIR SEPARATOR
    • JPH04359786A
    • 1992-12-14
    • JP13260291
    • 1991-06-04
    • HITACHI LTDHITACHI TECHNO ENG
    • SHIRACHI KENZOUKAWATANI TADAHISATAHARA TOSHIYUKIHASHIMOTO KENICHITASAKA YASUO
    • F25J3/04
    • PURPOSE:To enhance the collection rate by installing a concentration controller for a specific component contained in a feed gas supplied to a coarse argon tower from the top of a main refining tower and controlling an outlet bypass valve based on its concentration in a low temperature air separator which collects argon. CONSTITUTION:Air in an air heat exchanger 1 exchanges heat with return gas from a main refining tower A. After it is cooled, it is blown into a lower tower 2 of the main refining tower A, where it is refined and separated into liquid nitrogen at the top and liquid air at the bottom. The liquid nitrogen and liquid air are supplied to an upper tower 3, but a part of the liquid air is supplied to a concentrator of a coarse Argon tower 4 where the feed gas from the upper tower 3 is liquefied. An expansion turbine 5 is driven by a part of the raw material air cooled by the air heat exchanger 1. The air from the expansion turbine 5 is blown into the upper tower 3 where it is refined and separated. A part of the air flows through an outlet bypass valve 7 and made to enter a waste nitrogen piping line from the upper tower 3. The outlet bypass valve 7 is automatically controlled according to the outlet of a concentration controller 9 which monitors the concentration of argon.
    • 5. 发明专利
    • CONTROL METHOD OF NITROGEN MANUFACTURING DEVICE
    • JPH051881A
    • 1993-01-08
    • JP15293291
    • 1991-06-25
    • HITACHI LTDHITACHI TECHNO ENG
    • KAWATANI TADAHISATASAKA YASUOYANAGII TOSHIAKIFURUYA MITSUHIROKOYAMA SHOJI
    • F25J3/04
    • PURPOSE:To make the control operation of an operator unnecessary and an efficiently optimum operation by a method wherein the amount of liquid nitrogen, collected from the title device, is controlled by the opening degree of an automatic valve provided in a waste gas main tube or the flow rate of waste gas, flowing through the waste gas main tube. CONSTITUTION:When cold heat is excessive, the load of a turbine 7 is reduced by the operation of a liquid surface regulator 38 and the amount of waste gas is increased whereby the opening degree of an automatic valve is increased. On the contrary, when the cold heat is insufficient, the load of the turbine 7 is increased by the operation of the liquid surface regulator 38 and the amount of waste gas is reduced whereby the opening degree of the automatic valve is reduced. According to this method, the inlet pressure of the turbine is controlled in constant at all times. The opening degree of the bypass valve 15 of the turbine 7 is inputted into the opening degree regulator 36 to effect cascade control, in which the set value of a liquid nitrogen flow rate regulator 37 is changed by the output of the opening degree regulator 36. The output of the opening degree regulator 36 is set so as not to exceed the maximum collectable amount of liquid nitrogen whereby the amount of liquid nitrogen in accordance with the excessive degree of the generating amount of cold heat can be collected at all times.
    • 6. 发明专利
    • METHOD FOR OPERATING PRE-TREATMENT DEVICE FOR AIR-SEPARATOR
    • JPH04139375A
    • 1992-05-13
    • JP26058390
    • 1990-10-01
    • HITACHI LTDHITACHI TECHNO ENG
    • YANAGII TOSHIAKITASAKA YASUOKAWATANI TADATAKA
    • F25J3/04
    • PURPOSE:To enable a smooth energization of a device to be carried out by a method wherein a pressure removing valve of an adsorption column is opened when an energization is started and an amount of air more than a limited amount of reduction in a freezer is assured. CONSTITUTION:If a pre-treatment device for an air separator is being energized or the separator is being planned to be stopped and a degree of opening of an air releasing valve 14 is larger than its specified value, either a pressure releasing valve 12 or 13 of an adsorption column 6 or 7 being used is opened, a part of an air volume released from an air releasing valve 14 is released from the pressure reducing valve 12 or 13 so as to keep an amount of air. In addition, in case that the planned stopping is being carried out and a degree of opening of the air releasing valve 14 is more than its specified value or during the time in which the separator is ranged from its rectifying operation to its normal operation, either the pressure reducing valve 12 or 13 is opened only when the pressure is being decreased and it is not opened in other occasions. In this case, since the main body of the separator requires a rated amount of air, the rated amount of air can be assured and so it does not lower a limited amount of reduct of the freezer.
    • 10. 发明专利
    • CONTROL OF FLOW RATE OF PURIFIED GAS OF TSA ADSORBING TOWER
    • JPH05223A
    • 1993-01-08
    • JP15293391
    • 1991-06-25
    • HITACHI LTDHITACHI TECHNO ENG
    • NAKAMURA HIROHIKOTASAKA YASUOTSUSHIMA HIROSHI
    • B01D53/04
    • PURPOSE:To reduce the fluctuation of the flow rate on the downstream side of a TSA adsorbing tower and to make the flow rate and pressure of purified air constant by preliminarily increasing the inlet flow rate of the TSA adsorbing tower corresponding to the change-over time of the TSA adsorbing tower before the TSA adsorbing tower enters a pressurizing process. CONSTITUTION:The inlet guide blade 11 of an air compressor 12 is preliminarily operated by a control unit 12 a definite time before a TSA adsorbing tower 2 enters a pressurizing process at the time of the completion of a cooling process and the air compressor 1 is subjected to incremental operation. Next, the TSA adsorbing tower 2 enters the pressurizing process and a part of purified air is sent to the TSA adsorbing tower 2 through a pressure gas inlet change- over valve 10. Whereupon, the purified air is increased in quantity to be capable of being sent out in the same amount as the purified air before pressurization. By this constitution, the flow rate of the purified gas of the TSA adsorbing tower is always kept constant and the pressure of purified gas is kept almost constant to always perform stable operation.