CN202562126U - Recovered-adsorption-heat based heating and booster system device - Google Patents
Recovered-adsorption-heat based heating and booster system device Download PDFInfo
- Publication number
- CN202562126U CN202562126U CN201220194564XU CN201220194564U CN202562126U CN 202562126 U CN202562126 U CN 202562126U CN 201220194564X U CN201220194564X U CN 201220194564XU CN 201220194564 U CN201220194564 U CN 201220194564U CN 202562126 U CN202562126 U CN 202562126U
- Authority
- CN
- China
- Prior art keywords
- tube
- heat
- pressure
- low
- valve
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
The utility model relates to a recovered-adsorption-heat based heating and booster system device, which is characterized by comprising a hot water pump, a low-temperature heating cylinder, a low-pressure valve, an adsorbent cylinder, a blade pipe, a composite adsorbent, a high-pressure valve I, a heat-storage water tank, a circulating hot water pipe, a high-pressure water pump, a high-pressure heating cylinder, a heating pipe, a steam pipe, an analyzing cylinder, a high-pressure valve II, a condensing heat-exchanging cylinder, a throttling valve and an ammonia pipeline, wherein the high-pressure heating cylinder is internally provided with a heating pipe, and the front end of the high-pressure water pump is provided with a nozzle; and the composite adsorbent is prepared by sintering or pressing activated carbon fiber cloth and a composite adsorbent together and is distributed in the middle of the blade pipe. According to the utility model, a chemical reaction heat principle is utilized, the heat energy of recovered adsorption heat is used to convert a low-temperature heat source into a high-temperature heat source to carry out heating and working, and when the adsorbent cylinder and the analyzing cylinder continuously work in an alternative circulation manner, heat supply, power generation and refrigeration are realized; and the recovered-adsorption-heat based heating and booster system device is simple in structure, low in manufacture cost, high in heat efficiency and easy for realizing industrial production.
Description
Technical field
The utility model relates to a kind of chemical heat pump equipment technical field, particularly a kind of recovery heat of adsorption increasing temperature and pressure system and device.
Background technology
At present, domestic applied solar energy in the prior art, waste thermal energy, geothermal water source and natural air thermal source thermal-arrest heat up, and adopt following several kinds of forms: solar thermal collector, mechanical heat pump, chemical heat pump.They exist jointly: the huge heat energy efficiency of equipment volume is low, function singleness problem such as can only thermal-arrest can not boost.The applicant's patent of invention 200810011718.5; A kind of adsorption refrigerating device technology that adopts the liquid storage cartridge heater is provided; Be a kind of chemisorbed principle of utilizing, the heat energy of external heat and the heat energy of chemisorbed generation are mutually combined, carry out the heat refrigeration plant; Exist: the adsorbent heat conductivility is poor, and production technology is numerous and diverse to be difficult to realize industrialization production.
Summary of the invention
The utility model has overcome the defective of above-mentioned existence; Purpose provides a kind of chemical reaction heat principle of utilizing, and transfers low-temperature heat source to chemical heat energy and combines to produce the recovery heat of adsorption increasing temperature and pressure system and device that HTHP heat energy carries out heating, heating and cooling and heating generating with heating source.
[0004] the utility model reclaims heat of adsorption increasing temperature and pressure system and device content Description:
The utility model reclaims heat of adsorption increasing temperature and pressure system and device; It is characterized in that: be to constitute by: heat-exchanger pump, low-temperature heat tube, low pressure valve, sorbent tube, blade pipe, compound adsorbent, hyperbar valve I, thermal storage water tank, circulating hot water pipe, high-pressure hydraulic pump, high pressure cartridge heater, heating tube, steam pipe, parsing tube, hyperbar valve II, condensing heat-exchange tube, choke valve, nozzle and ammonia pipeline; Heat-exchanger pump is connected with the low-temperature heat tube; The low-temperature heat tube is connected with sorbent tube through gas pipeline; On gas pipeline, be provided with the low pressure valve, in sorbent tube, be provided with blade pipe and compound adsorbent, resolve tube top and be connected with condensing heat-exchange tube top through gas pipeline; On gas pipeline, be provided with the air valve II; Thermal storage water tank's top is connected with sorbent tube top, parsing tube top respectively, and the bottom of sorbent tube is connected high-pressure hydraulic pump through waterpipe with high pressure cartridge heater bottom, on waterpipe, be provided with penstock III, penstock VI; The top of the top of sorbent tube and parsing tube is connected with condensing heat-exchange tube top through the ammonia pipeline; On the ammonia pipeline, be provided with hyperbar valve II, the bottom of condensing heat-exchange tube is connected with the low-temperature heat tube through feed channel, on feed channel, is provided with choke valve.
The top of sorbent tube is connected with the thermal storage water tank through waterpipe, on waterpipe, is provided with the penstock I, and thermal storage water tank's top is connected with parsing tube top through waterpipe, on waterpipe, is provided with the penstock II.
Thermal storage water tank's bottom is connected last penstock IV and the penstock V of being respectively equipped with of circulating hot water pipe with sorbent tube, a parsing tube bottom respectively through the circulating hot water pipe.
The top of sorbent tube is connected with high pressure cartridge heater top through gas pipeline, and gas pipeline is provided with the air valve I.
The low-temperature heat tube is connected with a parsing tube bottom through gas pipeline, on gas pipeline, is provided with the air valve III.
In the high pressure cartridge heater, be provided with heating tube.
Be provided with nozzle at the high-pressure hydraulic pump front end.
Compound adsorbent is by active carbon fiber fabrics and compound adsorbent sintering together or compressed together processing, and is arranged in the middle of the blade pipe.
[0005] the utility model reclaims heat of adsorption increasing temperature and pressure device; Utilize the chemical reaction heat principle; Adopt the heat energy that reclaims heat of adsorption to convert low-temperature heat source into the elevated temperature heat energy and heat acting; When sorbent tube carries out with a parsing tube continuous operation alternate cycles, can realize heating, generating and refrigeration.It is simple in structure, cost is low, the thermal efficiency is high, is easy to realize industrialization production.
[0006]
Description of drawings
Fig. 1 reclaims heat of adsorption increasing temperature and pressure system and device structural representation;
Among the figure: the 1st, heat-exchanger pump; The 2nd, the low-temperature heat tube; The 3rd, the low pressure valve; The 4th, sorbent tube; The 5th, the blade pipe; The 6th, compound adsorbent; The 7th, hyperbar valve I; The 8th, the thermal storage water tank; The 9th, the circulating hot water pipe; The 10th, high-pressure hydraulic pump; The 11st, the high pressure cartridge heater; The 12nd, heating tube; The 13rd, steam pipe; The 14th, resolve tube; The 15th, hyperbar valve II; The 16th, the condensing heat-exchange tube; The 17th, choke valve; The 18th, nozzle; The 19th, the ammonia pipeline; The 20th, the air valve I; The 21st, the penstock I; The 22nd, the penstock II; The 23rd, the air valve II; The 24th, the penstock III; The 25th, the penstock IV; The 26th, the air valve III; The 27th, the penstock V; The 28th, the penstock VI.
[0007]
The specific embodiment
The utility model reclaims heat of adsorption increasing temperature and pressure system and device and is achieved in that below in conjunction with the accompanying drawing work bright specifically.See Fig. 1; The utility model reclaims heat of adsorption increasing temperature and pressure system and device; Be by: heat-exchanger pump 1, low-temperature heat tube 2, low pressure valve 3, sorbent tube 4, blade pipe 5, compound adsorbent 6, hyperbar valve I 7, thermal storage water tank 8, circulating hot water pipe 9, high-pressure hydraulic pump 10, high pressure cartridge heater 11, heating tube 12, steam pipe 13, resolve tube 14, hyperbar valve II 15, condensing heat-exchange tube 16, choke valve 17, nozzle 18 and ammonia pipeline 19 and constitute; Heat-exchanger pump 1 is connected with low-temperature heat tube 2; Low-temperature heat tube 2 is connected with sorbent tube 4 through gas pipeline; On gas pipeline, be provided with low pressure valve 3, in sorbent tube 4, be provided with blade pipe 5 and compound adsorbent 6, resolve tube 14 tops and be connected with condensing heat-exchange tube 16 tops through gas pipeline; On gas pipeline, be provided with air valve II 23; Thermal storage water tank 8 top is connected with sorbent tube 4 tops, parsing tube 14 tops respectively, and the bottom of sorbent tube 4 is connected high-pressure hydraulic pump 10 through waterpipe with high pressure cartridge heater 11 bottoms, on waterpipe, be provided with penstock III 24, penstock VI 28; The top of the top of sorbent tube 4 and parsing tube 14 is connected with condensing heat-exchange tube 16 tops through ammonia pipeline 19; On ammonia pipeline 19, be provided with hyperbar valve II 15, the bottom of condensing heat-exchange tube 16 is connected with low-temperature heat tube 2 through feed channel, on feed channel, is provided with choke valve 17.
The top of sorbent tube 4 is connected with thermal storage water tank 8 through waterpipe, on waterpipe, is provided with penstock I 21, and thermal storage water tank 8 top is connected with parsing tube 14 tops through waterpipe, on waterpipe, is provided with penstock II 22.
Thermal storage water tank 8 bottom is connected with sorbent tube 4, parsing tube 14 bottoms respectively through circulating hot water pipe 9, is respectively equipped with penstock IV 25 and penstock V 27 on the circulating hot water pipe 9.
The top of sorbent tube 4 is connected with high pressure cartridge heater 11 tops through gas pipeline, and gas pipeline is provided with air valve I 20.
Low-temperature heat tube 2 is connected with parsing tube 14 bottoms through gas pipeline, on gas pipeline, is provided with air valve III 26.
In high pressure cartridge heater 11, be provided with heating tube 12.
Be provided with nozzle 18 at high-pressure hydraulic pump 10 front ends.
Compound adsorbent 6 is by active carbon fiber fabrics and compound adsorbent sintering together or compressed together processing, and is arranged in the middle of the blade pipe 5.
[0008] the utility model reclaims the course of work of heat of adsorption increasing temperature and pressure system and device:
After at first sorbent tube 4 and parsing tube 14 being assembled, in condensing heat-exchange tube 16, be full of 2/3 ammoniacal liquor.Heat-exchanger pump 1 is drawn up 25 ℃ next underground water, send in the ring pipe in the low-temperature heat tube 2, make the low temperature ammonia be heated to be 25 ℃; Pressure is the ammonia of 1.0 Mpa, will be heated to be 25 ℃ again, and pressure is that the ammonia of 1.0 Mpa is sent in the sorbent tube 4; Through ammonia pipeline 19 ammonia is sent in the sorbent tube 4; Ammonia and adsorbents adsorb, the heat of adsorption of generation is transformed into 80 ℃ hot water with the cold water in the blade pipe 5, sprays into high pressure cartridge heater 11 through the nozzle 18 of high-pressure hydraulic pump 10 front ends; Through heating tube 12 the water temperature heating is generated 120 ℃ steam; Steam is in the blade pipe 5 of steam pipe 13 input sorbent tubes 4, and blade pipe 5 is resolved the heating of adsorbent ammonia, and the air pressure of the ammonia of parsing is 1.4 Mpa; Temperature is 120 ℃, and temperature is that 120 ℃ of air pressure ammonia that is 1.4 Mpa converts cold water temperature into 55 ℃～65 ℃ after via condensing heat-exchange tube 16 and sends into the heating heat supply.If the air pressure of the ammonia of resolving is risen to 2.3 Mpa, temperature is 160 ℃ of purposes that can reach generating work.
Through reclaiming heat of adsorption increasing temperature and pressure system and device when sorbent tube 4 carries out with parsing tube 14 continuous operation alternate cycles, can realize heating, generating and refrigeration.
Claims (8)
1. one kind is reclaimed heat of adsorption increasing temperature and pressure system and device; It is characterized in that: be by heat-exchanger pump (1), low-temperature heat tube (2), low pressure valve (3), sorbent tube (4), blade pipe (5), compound adsorbent (6), hyperbar valve I (7), thermal storage water tank (8), circulating hot water pipe (9), high-pressure hydraulic pump (10), high pressure cartridge heater (11), heating tube (12), steam pipe (13), resolve tube (14), hyperbar valve II (15), condensing heat-exchange tube (16), choke valve (17), nozzle (18) and ammonia pipeline (19) formation; Heat-exchanger pump (1) is connected with low-temperature heat tube (2); Low-temperature heat tube (2) is connected with sorbent tube (4) through gas pipeline; On gas pipeline, be provided with low pressure valve (3); In sorbent tube (4), be provided with blade pipe (5) and compound adsorbent (6); Resolving tube (14) top is connected with condensing heat-exchange tube (16) top through gas pipeline; On gas pipeline, be provided with air valve II (23); Thermal storage water tank's (8) top is connected with sorbent tube (4) top, parsing tube (14) top respectively, and the bottom of sorbent tube (4) is connected high-pressure hydraulic pump (10) through waterpipe with high pressure cartridge heater (11) bottom, on waterpipe, be provided with penstock III (24), penstock VI (28); The top of the top of sorbent tube (4) and parsing tube (14) is connected with condensing heat-exchange tube (16) top through ammonia pipeline (19); On ammonia pipeline (19), be provided with hyperbar valve II (15), the bottom of condensing heat-exchange tube (16) is connected with low-temperature heat tube (2) through feed channel, on feed channel, is provided with choke valve (17).
2. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1; It is characterized in that: the top of sorbent tube (4) is connected with thermal storage water tank (8) through waterpipe; On waterpipe, be provided with penstock I (21); Thermal storage water tank's (8) top is connected with parsing tube (14) top through waterpipe, on waterpipe, is provided with penstock II (22).
3. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1; It is characterized in that: thermal storage water tank's (8) bottom is connected with sorbent tube (4), parsing tube (a 14) bottom respectively through circulating hot water pipe (9), is respectively equipped with penstock IV (25) and penstock V (27) on the circulating hot water pipe (9).
4. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1 is characterized in that: the top of sorbent tube (4) is connected with high pressure cartridge heater (11) top through gas pipeline, and gas pipeline is provided with air valve I (20).
5. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1 is characterized in that: low-temperature heat tube (2) is connected with parsing tube (a 14) bottom through gas pipeline, on gas pipeline, is provided with air valve III (26).
6. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1 is characterized in that: in high pressure cartridge heater (11), be provided with heating tube (12).
7. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1 is characterized in that: be provided with nozzle (18) at high-pressure hydraulic pump (10) front end.
8. recovery heat of adsorption increasing temperature and pressure system and device according to claim 1 is characterized in that: compound adsorbent (6) is by active carbon fiber fabrics and compound adsorbent sintering together or compressed together processing, and is arranged in the middle of the blade pipe (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220194564XU CN202562126U (en) | 2012-05-03 | 2012-05-03 | Recovered-adsorption-heat based heating and booster system device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220194564XU CN202562126U (en) | 2012-05-03 | 2012-05-03 | Recovered-adsorption-heat based heating and booster system device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202562126U true CN202562126U (en) | 2012-11-28 |
Family
ID=47211776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220194564XU Expired - Fee Related CN202562126U (en) | 2012-05-03 | 2012-05-03 | Recovered-adsorption-heat based heating and booster system device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202562126U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102628625A (en) * | 2012-05-03 | 2012-08-08 | 金继伟 | Recovered and absorbed heat warming and boosting system device |
-
2012
- 2012-05-03 CN CN201220194564XU patent/CN202562126U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102628625A (en) * | 2012-05-03 | 2012-08-08 | 金继伟 | Recovered and absorbed heat warming and boosting system device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202501664U (en) | Photoelectric and photothermal solar energy heat pump system | |
| CN203476414U (en) | Waste heat recovery energy storage low-temperature power generating system and heat pump unit | |
| CN102182655B (en) | Low-temperature Rankine dual-cycle power generating unit | |
| CN104061710A (en) | Method for providing steam power and device thereof | |
| KR20170044182A (en) | Solar water heating auxiliary heat storage device and power plant boiler solar water heating supply system formed thereof | |
| CN102758690A (en) | Efficient high-pressure liquid air energy storage/release system | |
| CN112554984A (en) | Constant-pressure water-pumping compressed air energy storage system with heat storage function and operation method | |
| CN201909484U (en) | Aqueous ammonia-applicable system for obtaining heat from medium-temperature and low-temperature geothermal wells | |
| CN202811079U (en) | High-efficiency and high-pressure liquid air energy storage/ release system | |
| CN202048721U (en) | Heating device utilizing low grade heat source | |
| CN108771950A (en) | A kind of carbon dioxide recycle electricity generation system and method being pressurized using chemical absorbing | |
| CN203190713U (en) | Pressurization type three-phase absorption energy storage device | |
| CN202562126U (en) | Recovered-adsorption-heat based heating and booster system device | |
| CN103090582A (en) | Supercharged three-phase absorbing type energy storage device | |
| CN102628625A (en) | Recovered and absorbed heat warming and boosting system device | |
| CN201917228U (en) | Power generation system with residual heat of fume | |
| CN216240842U (en) | Low-temperature circulating power generation system using carbon dioxide gas as working medium | |
| WO2020029422A1 (en) | Disk type solar photothermal gradient utilization system | |
| CN103256848A (en) | Self-warming type thermochemical heat accumulating device and application | |
| CN102191958A (en) | Low-temperature air source generating device | |
| CN102230687B (en) | Heating device using low-grade heat source | |
| CN212339398U (en) | Life hot water supply device based on solar energy and trans-critical carbon dioxide heat pump | |
| CN206094279U (en) | Slaughterhouse is with multistage full heat recovery hot water system of refrigerating unit | |
| CN111750419B (en) | Domestic hot water supply system based on solar energy and transcritical carbon dioxide heat pump | |
| CN113882921A (en) | Low-temperature circulating power generation system and method using carbon dioxide gas as working medium |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121128 Termination date: 20140503 |