[go: up one dir, main page]

CN212274317U - System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system - Google Patents

System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system Download PDF

Info

Publication number
CN212274317U
CN212274317U CN202020851817.0U CN202020851817U CN212274317U CN 212274317 U CN212274317 U CN 212274317U CN 202020851817 U CN202020851817 U CN 202020851817U CN 212274317 U CN212274317 U CN 212274317U
Authority
CN
China
Prior art keywords
outlets
pipelines
inlets
compressors
waste heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202020851817.0U
Other languages
Chinese (zh)
Inventor
谭垒
韩兴旺
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuhan Wanton Huazhong Cold Chain Port Co ltd
Original Assignee
Wantontong Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wantontong Technology Co ltd filed Critical Wantontong Technology Co ltd
Priority to CN202020851817.0U priority Critical patent/CN212274317U/en
Application granted granted Critical
Publication of CN212274317U publication Critical patent/CN212274317U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

A high-temperature hot water preparation system by utilizing waste heat recovery in a refrigeration system. The traditional refrigerating system adopting Freon as a refrigerant is subjected to the thermodynamic property of the refrigerant, and the temperature of water cannot be too high when heat recovery is carried out on condensation waste heat. The utility model discloses the constitution includes: an R134a refrigeration working medium circulating system and an R744 refrigeration working medium circulating system; the R134a refrigerant circulating system comprises a group of R134a compressors (1), the outlets of the group of R134a compressors are respectively connected with the inlets of the R134a oil separators (2) through pipelines, the outlets of the R134a oil separators are connected with the inlets of the evaporative condensers (3) through pipelines, the outlets of the evaporative condensers are connected with the inlets of the condensing evaporators (4) through pipelines, and the outlets of the condensing evaporators are communicated with the inlets of the R134a liquid reservoirs (5). The utility model is used for utilize waste heat recovery to prepare high temperature hot water among the refrigerating system.

Description

System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system
The technical field is as follows:
the utility model relates to a utilize waste heat recovery to prepare high temperature hot water system among refrigerating system.
Background art:
when the refrigeration system is used for preparing low temperature, a large amount of heat can be released from the condensation side of the system, so that the efficiency of the whole system can be improved by applying the refrigeration system to waste heat recovery, and the purposes of energy conservation and environmental protection are achieved. The traditional refrigerating system adopting Freon as a refrigerant is subjected to the thermodynamic property of the refrigerant, and the temperature of water cannot be too high when heat recovery is carried out on condensation waste heat.
The utility model has the following contents:
the utility model aims at solving the problem of above-mentioned existence, provide an utilize waste heat recovery to prepare high temperature hot water system among the refrigerating system of R134a refrigerant cycle system and R744 refrigerant cycle system.
The above purpose is realized by the following technical scheme:
a system for preparing high-temperature hot water by utilizing waste heat recovery in a refrigeration system comprises an R134a refrigeration working medium circulation system and an R744 refrigeration working medium circulation system;
the R134a refrigerant cycle system comprises a group of R134a compressors, the outlets of the group of R134a compressors are respectively connected with the inlets of the R134a oil separators through pipelines, the outlets of the R134a oil separators are connected with the inlets of the evaporative condensers through pipelines, the outlets of the evaporative condensers are connected with the inlets of the condensing evaporators through pipelines, the outlets of the condensing evaporators are communicated with the inlet of the R134a liquid storage tank, the outlets of the R134a liquid storage tank are communicated with a group of economizers through pipelines, the outlets of the economizers are communicated with the end evaporators through a liquid supply pipe, and the end evaporators are communicated with the suction port of the R134a compressor through a gas return pipe;
the R744 refrigeration working medium circulating system comprises a group of R744 compressors, the outlets of the R744 compressors are respectively connected with the inlets of the R744 oil separators through pipelines, the outlets of the R744 oil separators are connected with the inlets of the gas coolers through pipelines, the outlets of the gas coolers are connected with the inlets of the R744 liquid reservoirs through pipelines, the outlets of the R744 liquid reservoirs are connected with the inlets of the condensing evaporators through pipelines and the pipelines are provided with expansion valves, the outlets of the condensing evaporators are connected with the inlets of the R744 gas-liquid separators through pipelines, and the outlets of the R744 gas-liquid separators are communicated with the inlets of the R744 compressors.
Has the advantages that:
1. the utility model discloses increase carbon dioxide and stride critical compressor, absorb the waste heat of freon refrigerant side, utilize the high characteristics of carbon dioxide exhaust temperature to prepare high temperature hot water.
The utility model discloses the proper super-cooled degree that increases liquid after the condensation among the refrigerating system can improve refrigerating system's refrigerating output to improve whole refrigerating system's refrigeration efficiency.
The utility model discloses use carbon dioxide as the refrigerant, carbon dioxide is as pure natural refrigerant, and ozone layer destroys the latent energy and is 0, and global warming latent energy is 1, has superior thermodynamic properties.
The utility model discloses increase carbon dioxide and stride critical circulation, and carbon dioxide is higher at the exhaust temperature of transcritical circulation in-process, and the gas cooling process can have fine heat transfer with water, obtains the hot water of higher temperature, prepares 40~95 ℃ of high temperature hot water when increasing R134a refrigeration cycle super-cooled rate.
The utility model discloses can set up the water supply leaving water temperature automatically, the water supply temperature range is 40~95 ℃.
Description of the drawings:
FIG. 1 is a schematic diagram of the present invention;
in the figure: 1. r134a compressor; 2. an R134a oil separator; 3. an evaporative condenser; 4. a condensing evaporator; 5. r134a reservoir; 6. an economizer; 7. a terminal evaporator; 8. an R744 compressor; 9. an R744 oil separator; 10. a gas cooler; 11. a reservoir of R744; 12. an expansion valve; 13. a gas-liquid separator of R744; 14. and (4) an air return pipe.
The specific implementation mode is as follows:
example 1:
a system for preparing high-temperature hot water by utilizing waste heat recovery in a refrigeration system comprises an R134a refrigeration working medium circulation system and an R744 refrigeration working medium circulation system;
the R134a refrigerant cycle system comprises a group of R134a compressors 1, the outlets of the group of R134a compressors are respectively connected with the inlets of the R134a oil separators 2 through pipelines, the outlets of the R134a oil separators are connected with the inlets of the evaporative condensers 3 through pipelines, the outlets of the evaporative condensers are connected with the inlets of the condensing evaporators 4 through pipelines, the outlets of the condensing evaporators are communicated with the inlet of the R134a liquid accumulator 5, the outlets of the R134a liquid accumulator are communicated with a group of economizers 6 through pipelines, the outlets of the economizers are communicated with a terminal evaporator 7 through a liquid supply pipe, and the terminal evaporator is communicated with the suction port of the R134a compressor through a gas return pipe 14;
the R744 refrigeration working medium circulating system comprises a group of R744 compressors 8, outlets of the group of R744 compressors are respectively connected with inlets of R744 oil separators 9 through pipelines, outlets of the R744 oil separators are connected with inlets of gas coolers 10 through pipelines, outlets of the gas coolers are connected with inlets of R744 liquid reservoirs 11 through pipelines, outlets of the R744 liquid reservoirs are connected with inlets of condensing evaporators through pipelines and are provided with expansion valves 12, outlets of the condensing evaporators are connected with inlets of R744 gas-liquid separators 13 through pipelines, and outlets of the R744 gas-liquid separators are communicated with inlets of the R744 compressors.
Example 2:
a preparation method of a system for preparing high-temperature hot water by utilizing waste heat recovery in a refrigeration system comprises the following steps:
r134a is used as the circulating part of the refrigerant: r134a is compressed by a compressor, enters an evaporative condenser through an oil separator for condensation, after condensation, R134a enters a condensation evaporator for continuous supercooling, after supercooling, R134a enters a liquid storage device and then enters an economizer, R134a is sent to a tail end evaporator after secondary supercooling, after evaporation, the gas state is changed to the gas state and returns to an air suction port of the R134a compressor, and the circulation is completed;
r744 is used as the circulating part of the refrigeration working medium: after being compressed by the compressor, the R744 enters the gas cooler through the oil separator to exchange heat with water to prepare high-temperature hot water, the R744 enters the R744 liquid storage device after being cooled, then enters the condensation evaporator through the expansion valve to be subcooled for R134a, and the R744 changes into a gas state and returns to the suction port of the R744 compressor through the gas-liquid separator to finish circulation.

Claims (1)

1. A system for preparing high-temperature hot water by recovering waste heat in a refrigerating system is characterized in that: the system for preparing high-temperature hot water by utilizing waste heat recovery in the refrigeration system comprises an R134a refrigeration working medium circulation system and an R744 refrigeration working medium circulation system;
the R134a refrigerant cycle system comprises a group of R134a compressors, the outlets of the group of R134a compressors are respectively connected with the inlets of the R134a oil separators through pipelines, the outlets of the R134a oil separators are connected with the inlets of the evaporative condensers through pipelines, the outlets of the evaporative condensers are connected with the inlets of the condensing evaporators through pipelines, the outlets of the condensing evaporators are communicated with the inlet of the R134a liquid storage tank, the outlets of the R134a liquid storage tank are communicated with a group of economizers through pipelines, the outlets of the economizers are communicated with the end evaporators through a liquid supply pipe, and the end evaporators are communicated with the suction port of the R134a compressor through a gas return pipe;
the R744 refrigeration working medium circulating system comprises a group of R744 compressors, the outlets of the R744 compressors are respectively connected with the inlets of the R744 oil separators through pipelines, the outlets of the R744 oil separators are connected with the inlets of the gas coolers through pipelines, the outlets of the gas coolers are connected with the inlets of the R744 liquid reservoirs through pipelines, the outlets of the R744 liquid reservoirs are connected with the inlets of the condensing evaporators through pipelines and the pipelines are provided with expansion valves, the outlets of the condensing evaporators are connected with the inlets of the R744 gas-liquid separators through pipelines, and the outlets of the R744 gas-liquid separators are communicated with the inlets of the R744 compressors.
CN202020851817.0U 2020-05-20 2020-05-20 System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system Active CN212274317U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020851817.0U CN212274317U (en) 2020-05-20 2020-05-20 System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020851817.0U CN212274317U (en) 2020-05-20 2020-05-20 System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system

Publications (1)

Publication Number Publication Date
CN212274317U true CN212274317U (en) 2021-01-01

Family

ID=73878566

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020851817.0U Active CN212274317U (en) 2020-05-20 2020-05-20 System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system

Country Status (1)

Country Link
CN (1) CN212274317U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111473545A (en) * 2020-05-20 2020-07-31 万吨通科技有限公司 System and method for preparing high-temperature hot water by recovering waste heat in refrigeration system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111473545A (en) * 2020-05-20 2020-07-31 万吨通科技有限公司 System and method for preparing high-temperature hot water by recovering waste heat in refrigeration system

Similar Documents

Publication Publication Date Title
CN109724293A (en) Solar-driven absorption subcooled CO2 transcritical two-stage compression refrigeration system
CN105135749B (en) Carbon dioxide cold-hot combined supply system
CN107323217B (en) Waste heat driven absorption refrigeration auxiliary supercooling CO 2 Automobile air conditioner
Gao et al. System principles and applications of hybrid sorption–compression heat pump–A review
CN110500824A (en) A non-azeotropic working medium supercooled CO2 transcritical refrigeration system
CN111141062B (en) A solar energy absorption and emission composite transcritical CO2 refrigeration system
CN209371421U (en) A kind of magnetic suspension centrifugal power heat pipe combined air conditioners all-in-one machine
CN212274317U (en) System for preparing high-temperature hot water by utilizing waste heat recovery in refrigeration system
CN102410664A (en) Novel air energy refrigerating device
CN105371516B (en) Carbon dioxide twin-stage cold-hot combined supply system
CN111141047A (en) A solar energy absorption cascade carbon dioxide two-stage compression refrigeration system
CN204202062U (en) With the water-cooled cooling water air conditioner unit of ice-reserving function
CN211823239U (en) Ultra-low temperature transcritical cascade refrigeration system
CN105352213A (en) Steam and air cascade refrigerating system
CN109163470A (en) A kind of ultralow temperature carbon dioxide water chiller-heater unit
CN211060438U (en) Parallel compression machinery supercooling double-condenser combined supply system
CN205783983U (en) The heat high efficiente callback device of air source handpiece Water Chilling Units
CN109282397B (en) Novel energy storage air conditioner and method based on air compression refrigeration cycle
CN208720562U (en) A kind of low circumstance temperature air source heat pump system
CN111322781A (en) Refrigerator centralized cold source carbon dioxide cascade refrigeration system and refrigeration method
CN105783331A (en) Heat efficient recovery device for air source water chilling unit
CN206637882U (en) Switchable type double evaporators CO2 trans critical cycle refrigeration systems
CN211977298U (en) Heat recovery system in CO2 cascade refrigeration system
CN207146964U (en) A kind of refrigeration system
CN205090654U (en) Cold and hot antithetical couplet of carbon dioxide doublestage supplies system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20231107

Address after: 436032 No.1 Donghu Road, Gedian Economic and Technological Development Zone, Ezhou City, Hubei Province

Patentee after: Wuhan Wanton Huazhong Cold Chain Port Co.,Ltd.

Address before: 436070 office building of Shangkong Huading Industrial Park, east of Chuangye Avenue, Gedian Development Zone, Ezhou City, Hubei Province

Patentee before: Wantontong Technology Co.,Ltd.

TR01 Transfer of patent right