Abstract:
A novel heat pump system capable of carrying out a cooling (refrigerating) operation or a heating (room heating) operation with ammonia and carbon dioxide, natural media, utilized in a combined state. The heat pump system (1) comprises a combination of an ammonia cycle (2), and a carbon dioxide cycle (3), and is characterized in that a carbon dioxide medium is circulated in the carbon dioxide cycle (3) by heating or cooling a part of the cycle, in addition to utilizing a natural circulation phenomenon in which a liquid head difference is formed in a carbon dioxide medium in the cycle without incorporating a compressor in the cycle, structural members of the ammonia cycle (2) being installed in a place isolated from a machine for cooling and heating an object material.
Abstract:
A refrigerator, comprising a low stage side refrigerant circuit (2) formed by connecting in order a low stage side compressor (4), a cascade condenser (5), a low stage side receiver (6), a low stage side expansion valve (7) formed of a temperature sensitive expansion valve, and an evaporator (8); and a high stage side refrigerant circuit (3) formed by connecting in order a high stage side compressor (9), a condenser (10), a high stage side receiver (11), a high stage side expansion valve (12) formed of a motor-driven expansion valve, and the cascade condenser (5); wherein the opening of the high stage side expansion valve (12) is adjusted so that a pressure detected by a high pressure sensor (SPH2) detecting the high pressure of the low stage side refrigerant circuit (2) agrees with a specified target high pressure.
Abstract:
This invention relates to a method of refrigeration purification and power generation of industrial waste gas and apparatus therefor. The apparatus is composed of two parts, the first of which is constituted by a multistage phase changeable refrigeration cycle for phase-changeable non heating refrigeration technique for obtaining effectually cool quantity; the second of which makes use of the feature of the harmful gas in the waste gas having the higher boiling point, condenses, liquifies and separates the harmful gas; the purified liquid and the liquid refrigeration medium of last stage absorbe heat from waste gas in order to be evaporated into steam; two steams drive respectively turbines to apply wark, collecting a mechanical power in a negative pression region and adding a mechanical energy loss of cooling waste gas during pressing. The invention can remedy the effect of industrial waste gas on the atmosphere and generate effectually power.
Abstract:
This invention relates to a non-heat refrigeration method and a cycle system thereof, the system composes a first stage, one or more median stage(s) and a last stage. The first stage is known refrigerative technique, the other stages condense evapor of self-stage by using cool quantity in lower temperature of preceding stage to effect refrigeration cycle. The first stage provides a cool quantity, the last stage cools a load, the median stage(s) amplify the cool quantity of preceding stage. The temperature of the respective stage rise gradually in connective order, the first stage has lowest temperature and the last stage has highest temperature. This system hasn't heat leaking outside, provides a cool quantity having a lower temperature and ameliorates efficiency.
Abstract:
Provided is a cascade refrigeration system (100) for a transport unit (10). The cascade refrigeration system (100) has a first refrigeration cycle (101) comprising a first compressor (120) and a first expansion valve (140), a second refrigeration cycle (102) comprising a second compressor (220) and a second expansion valve (240), and a cascade heat exchanger (150). The cascade heat exchanger (150) comprises a condenser side (151) fluidically coupled downstream of the first compressor (120) and upstream of the first expansion valve (140), and an evaporator side (152) fluidically coupled downstream of the second expansion valve (240) and upstream of the second compressor (220). The cascade refrigeration system (100) also comprises a pre-cooler (180) comprising a first side (181) and a second side (182). The first side (181) is fluidically coupled downstream of the first compressor (120) and upstream of the condenser side (151) of the cascade heat exchanger (150), and the pre-cooler (180) is configured to transfer heat between refrigerant in the first side (181) and refrigerant in the second side (182).
Abstract:
The present invention relates to a refrigerant composition comprising 75 - 80% by weight of HFO-1234ze(E), 6% to not greater than 12% by weight of HFC-134a and from 11% to about 17% by weight of HFO1336mzz(E), and to the use of the refrigerant in a heat exchange systems, including electronic cooling, low and medium temperature refrigeration and to the use of such compositions as a replacement of the refrigerant R-410A for heating and cooling applications.
Abstract:
A system includes a pressure exchanger (PX). The PX is coupled to a motor that controls an operating speed of the PX. The system further includes a first pressure gauge configured to generate first pressure data indicative of a pressure of a fluid of a condenser. A first controller is to generate a first control signal based on the first pressure data. The motor of the PX is configured to adjust the operating speed of the PX based on the first control signal. The system further includes a pump. The system further includes a fluid density sensor for generating fluid density data associated with a first output fluid of the PX. A second controller is to generate a second control signal based on at least the fluid density data. The pump is to adjust an operating speed of the pump based on the second control signal.