Air Conditioning System, Compression System with Gas Secondary Injection and Judgment and Control Method Thereof
US-2018363954-A1 · Dec 20, 2018 · US
US2018356136A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018356136-A1 |
| Application number | US-201615775476-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 5, 2016 |
| Priority date | Dec 11, 2015 |
| Publication date | Dec 13, 2018 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided are a gas-replenishing and enthalpy-increasing control method, device and apparatus for a two-stage compressor. The method includes: when a gas-replenishing electronic expansion valve needs to be opened, gradually increasing, by a controller, an opening degree of the gas-replenishing electronic expansion valve in a time sequence; after the gas-replenishing electronic expansion valve is opened, acquiring a detected gas-replenishing superheat degree of a two-stage compressor; and adjusting, based on the gas-replenishing superheat degree of the two-stage compressor, the opening degree of the gas-replenishing electronic expansion valve, wherein the gas-replenishing electronic expansion valve is disposed between a medium-pressure liquid storage tank and the two-stage compressor, and when the opening degree of the gas-replenishing electronic expansion valve is not zero, a gaseous refrigerant in the medium-pressure liquid storage tank replenishes gas and increases enthalpy for the two-stage compressor,.
Opening claim text (preview).
1 . A gas-replenishing and enthalpy-increasing control method for a two-stage compressor, comprising: when a gas-replenishing electronic expansion valve needs to be opened, gradually increasing, by a controller, an opening degree of the gas-replenishing electronic expansion valve in a time sequence; after the gas-replenishing electronic expansion valve is opened, acquiring a detected gas-replenishing superheat degree of a two-stage compressor; and adjusting, based on the gas-replenishing superheat degree of the two-stage compressor, the opening degree of the gas-replenishing electronic expansion valve, wherein the gas-replenishing electronic expansion valve is disposed between a medium-pressure liquid storage tank and the two-stage compressor, and when the opening degree of the gas-replenishing electronic expansion valve is not zero, a gaseous refrigerant in the medium-pressure liquid storage tank replenishes gas and increases enthalpy for the two-stage compressor. 2 . The method as claimed in claim 1 , wherein gradually increasing, by a controller, an opening degree of the gas-replenishing electronic expansion valve in a time sequence when a gas-replenishing electronic expansion valve needs to be opened comprises: after the two-stage compressor is opened and operates for a first preset time period, controlling, by the controller, the opening degree of the gas-replenishing electronic expansion valve to be a first preset opening degree; when the opening degree of the gas-replenishing electronic expansion valve is the first preset opening degree, after the gas-replenishing expansion valve operates for a second preset time period, increasing the opening degree of the gas-replenishing electronic expansion valve to a second preset opening degree; and when the opening degree of the gas-replenishing electronic expansion valve is a second preset opening degree, after the gas-replenishing expansion valve operates for a third preset time period, fully opening the gas-replenishing electronic expansion valve. 3 . The method as claimed in claim 1 , wherein acquiring a detected gas-replenishing superheat degree of a two-stage compressor comprises: collecting a gas-replenishing temperature and a gas-replenishing pressure of the two-stage compressor; acquiring a saturation temperature corresponding to the gas-replenishing pressure; and taking a difference between the gas-replenishing temperature and the saturation temperature as the gas-replenishing superheat degree of the two-stage compressor. 4 . The method as claimed in claim 3 , wherein adjusting, based on the gas-replenishing superheat degree of the two-stage compressor, the opening degree of the gas-replenishing electronic expansion valve comprises: judging whether the gas-replenishing superheat degree of the two-stage compressor is greater than a preset superheat degree at predetermined intervals; when the gas-replenishing superheat degree of the two-stage compressor is greater than the preset superheat degree, determining that the replenished gas of the two-stage compressor entrains liquid; when the gas-replenishing superheat degree of the two-stage compressor is not greater than the preset superheat degree, determining that the replenished gas of the two-stage compressor does not entrain liquid; and adjusting the opening degree of the gas-replenishing electronic expansion valve according to the situation that the replenished gas of the two-stage compressor entrains liquid. 5 . The as claimed in claim 4 , wherein adjusting the opening degree of the gas-replenishing electronic expansion valve according to the situation that the replenished gas of the two-stage compressor entrains liquid comprises: when the replenished gas of the two-stage compressor entrains liquid, reducing the current opening degree of the gas-replenishing electronic expansion valve to a preset opening degree, wherein the preset opening degree is an opening degree preset based on a full opening degree of the gas-replenishing electronic expansion valve, and the full opening degree is an opening degree when the gas-replenishing electronic expansion valve is fully opened; and when the replenished gas of the two-stage compressor does not entrain liquid, keeping the current opening degree of the gas-replenishing electronic expansion valve unchanged or increasing the current opening degree. 6 . The method as claimed in claim 5 , wherein keeping the current opening degree of the gas-replenishing electronic expansion valve unchanged or increasing the current opening degree comprises: when it is determined that the replenished gas of the two-stage compressor does not entrain liquid, if the operations of reducing the current opening degree of the gas-replenishing electronic expansion valve and keeping the current opening degree of the gas-replenishing electronic expansion valve are executed respectively after it was judged previously twice whether the gas-replenishing superheat degree is greater than the preset opening degrees, executing the operation of increasing the current opening degree of the gas-replenishing electronic expansion valve, and otherwise, executing the operation of keeping the current opening degree of the gas-replenishing electronic expansion valve. 7 . A gas-replenishing and enthalpy-increasing control device for a two-stage compressor, comprising: a gas-replenishing electronic expansion valve, disposed between a medium-pressure liquid storage tank and a two-stage compressor; and a controller, connected to the gas-replenishing electronic expansion valve, and configured to gradually increase an opening degree of the gas-replenishing electronic expansion valve in a time sequence when the gas-replenishing electronic expansion valve needs to be opened, acquire a gas-replenishing superheat degree of the two-stage compressor after the gas-replenishing electronic expansion valve is opened, and adjust the opening degree of the gas-replenishing electronic expansion valve based on the gas-replenishing superheat degree of the two-stage compressor. 8 . The device as claimed in claim 7 , further comprising: a detection apparatus, connected to the controller, and configured to collect a gas-replenishing temperature and a gas-replenishing pressure of the two-stage compressor, wherein the controller comprises: a reading apparatus, connected to the detection apparatus, and configured to read a saturation temperature corresponding to the gas-replenishing pressure; and a calculator, connected to the detection apparatus and the reading apparatus, and configured to calculate a difference between the gas-replenishing temperature and the saturation temperature, so as to obtain the gas-replenishing superheat degree. 9 . The device as claimed in claim 8 , wherein the detection apparatus further comprises: a pressure sensor, disposed at a gas-replenishing port of the two-stage compressor, and configured to collect the gas-replenishing pressure; and a temperature-sensing package, disposed at the gas-replenishing port of the two-stage compressor, and configured to collect the gas-replenishing temperature. 10 . The device as claimed in claim 7 , further comprising: a four-way valve, a first end being connected to the two-stage compressor; a gas-liquid separator, a first end being connected to a second end of the four-way valve, and a second end being connected to the two-stage compressor; an outdoor heat exchanger, a first end being connected to a third end of the four-way valve; and an indoor heat exchanger, a first end being connected to a fourth end of the four-way valve, and a second end being connected to the medium-pressure liquid storage tank. 11 . The de
Expansion valves · CPC title
Suction pressures · CPC title
Timing · CPC title
at the suction side of the compressor · CPC title
at the discharge side of the compressor · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.