CN1268210A - Parallel multistage type hot water pump using water evaporation and condensation principle - Google Patents

Parallel multistage type hot water pump using water evaporation and condensation principle Download PDF

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Publication number
CN1268210A
CN1268210A CN98808556.9A CN98808556A CN1268210A CN 1268210 A CN1268210 A CN 1268210A CN 98808556 A CN98808556 A CN 98808556A CN 1268210 A CN1268210 A CN 1268210A
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China
Prior art keywords
chamber
water
steam
condensation
suction
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CN98808556.9A
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Chinese (zh)
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CN1131943C (en
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田炯贵
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04FPUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F1/00Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
    • F04F1/02Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped using both positively and negatively pressurised fluid medium, e.g. alternating
    • F04F1/04Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped using both positively and negatively pressurised fluid medium, e.g. alternating generated by vaporising and condensing

Abstract

Steam generated in a steam generating chamber (10) by heat from a combustion chamber (31) passes through a connection steam pipe (17) to act in a pumping chamber (8) to discharge water in the pumping chamber (8) to the outside as a hot water via the steam generating chamber (10), a discharge water check valve (12), a discharge water connection passage (13) and a discharge water reheating chamber (14-1, 14-2) and through a discharge pipe (15) and a discharge port (16). Meanwhile, steam in the pumping chamber (8) is fed to a condensation chamber (5) to be brought into contact with cold water to undergo rapid condensation, so that negative pressure generates in the condensation chamber (5) to permit water to be sucked into the condensation chamber (5) via a suction port (1), a suction water passage (3) and a suction water check valve (4). The water sucked is further fed to the pumping chamber (8) via a connection suction downcomer (7).

Description

Utilize the parallel multistage heat pump of evaporation of water and condensation principle
The background of invention
1, FIELD OF THE INVENTION
The present invention relates to a kind of heat pump, relate in particular to the parallel multistage heat pump that utilizes evaporation of water and condensation principle.
2, description of related art
Be not to use intergrade steamer or recycle pump suction hot water or use other pump suction/supply cold water according to heat pump of the present invention, but aspirate hot water: produce calory burning by a parallel multistage heat pump by following steps, by calory burning evaporable water that produces and the water of condensation evaporation (steam) once more.
Also have, the present invention pays attention to the heating of hot water more and bigger pumping action is provided.The present invention is used for jumbo hot water and produces equipment, specifically, and than the water-heating boiler little 1/2 or 1/4 of a routine.
Above conventional water-heating boiler (or hot water generation equipment) necessarily requires recycle pump and water pump that cold water is provided of a circulating hot water, and can not clean-burning fuel when the fuel that provides is a lot, therefore the crock accumulation phenomenon of each link of burning can't be solved, the poison gas (for example hot NO) that is lower than 50ppm can not be produced.
The accompanying drawing summary
When understanding preferably when of the present invention in conjunction with the following drawings and with reference to following detailed description, will be conspicuous to more comprehensively understanding of the present invention and its advantage, in the accompanying drawing similarly label represent identical or similar component, wherein:
Fig. 1 is the longitudinal sectional drawing of expression a preferred embodiment of the present invention;
Fig. 2 is the sectional drawing of the 100-100 line of presentation graphs 1;
Fig. 3 is the sectional drawing of the 200-200 line of presentation graphs 1;
Fig. 4 is the sectional drawing of the 300-300 line of presentation graphs 1;
The sectional drawing of the 400-400 line of Fig. 5 presentation graphs 1;
Fig. 6 is the flow chart of expression a preferred embodiment of the present invention.
The general introduction of invention
Therefore, an object of the present invention is to address the above problem, a kind of parallel multistage heat pump that utilizes evaporation of water and condensation principle is provided, be used for circulating hot water and suction cold water, do not use other recycle pump or water pump, therefore can not produce the crock accumulation phenomenon of the link of respectively burning, greatly reduce the generation speed of toxic gas.
Can realize above-mentioned purpose according to the present invention by means of the said parallel multistage heat pump of evaporation of water and condensation principle that utilizes, said heat pump comprises: a chamber structure, it is more than two-stage, be connected with a columniform steam generating chamber, have one and connect discharge pipe, a high temperature smoke pipe, the water passage of a channel change, with a discharge water non-return side, wherein constitute a firing chamber, a front surface discharge water in the both sides of said firing chamber repeats heating chamber and a rear surface discharge water repeats heating chamber, a burner inserts opening, one the 3rd air flue, an opening that runs through, a front surface reverse burning plate and a rear surface reverse burning plate, whereby, after ignitable fuel contacts five times with air, the combustion gas of discharging bottom in said firing chamber; A pump structure, it has a pump chamber, a condensation chamber and a kind of thermoinsulation material; Pump chamber comprises: connection suction pipe, one connect steam tube, outer steam discharge pipe and at the interior steam discharge pipe on the top of each steam generating chamber of formation firing chamber; Condensation chamber comprises: suction water non-return side, one connect water pipe, "+" type burst buffer plate, first de-noising network, second de-noising network, porose separating plate and at an exhaust port of its outside; Thermoinsulation material is used to stop moving of between pump chamber and condensation chamber heat; An economizer, it has the separating plate that a low temperature smoke pipe and change passage, be positioned at said pump structure around and and to be connected water pipe continuous; With a structure, be used to connect a suction water passage, a discharge water connecting path, a discharge pipe, and be connected air and outer loop link with a chimney by a suction opening, an exhaust openings.
Detailed description of preferred embodiment
Describe a preferred embodiment of the present invention with reference to the accompanying drawings in detail.In addition, in the following description, provide the description of understanding necessity of the present invention, so that more in depth understand the present invention.Be noted that for clarity sake, in the following description, omitted unnecessary meeting and made theme of the present invention ambiguous the known function and the detailed description of structure.
As shown in Figure 2, the structure of pumping unit is adopted on the top of a columniform steam generating chamber 10, the bottom of this pumping unit is a pump chamber 8, on the top of this pumping unit is a condensation chamber 5, said steam generating chamber 10 includes one and connects discharge pipe 9 and a smoke pipe 32, wherein forms one by firing chamber 31 of the present invention.As shown in Figure 1, said structure is used for the parallel longitudinal structure more than two-stage, and economizer 2 must exist in multistage pump equipment near, said energy saving device 2 includes a low temperature smoke pipe 33 that promotes waste gas.Shown in the flow chart of Fig. 6, according to the present invention, in filling according to the order water of the arrow shown in the solid line and during outer heat-exchanger (radiator), the air in the equipment is discharged into the outside of equipment by an exhaust port side 24, and each link that circulates all has been full of water.As previously discussed, after equipment and each circulation link all are full of water, at the fuel such as coal gas or oil in case when in firing chamber 31, burning, the calory burning of high temperature at first run to firing chamber 31 around and high temperature smoke pipe 32, thereby in steam generating chamber 10, evaporate the water.The vapor collection of the above generation is arrived the top of pump chamber 8 by steam connection tube 17, by connecting discharge pipe 9 water in the pump chamber 8 is added to steam generating chamber 10 simultaneously, thereby can change the flow direction of the water in the water passage 11, in steam generating chamber 10, store.Therefore, above-mentioned steam is by draining non-return side 12 and draining connecting path 13, arrives discharge water and repeats heating chamber 14-1 and 14-2, is discharged into the outside of equipment by discharge pipe 15 and floss hole 16, the heat energy that in radiator, leaves, and taken out to gravity tank.Subsequent, in the separating surface of collecting a certain amount of steam and water and air in the bottom of interior steam discharge pipe 19 arrives during the bottom of steam discharge pipe 19, the steam that should surpass the hydraulic pressure corresponding with the mobile hydraulic head in the bottom of interior steam discharge pipe 19 is by outer steam discharge pipe 18 and the interior steam discharge pipe 19 instantaneous bottoms that are discharged into condensation chamber 5.
At this moment, when the instantaneous discharging of steam because steam flows fast, and because when steam directly contacts with cold water in a single day rapid condensation taking place will produce fierce vibration and noise, so and a spot of water of discharging together of steam will produce fierce cracked.In order to eliminate above-described cracked sound, the damping of shocks plate 20 of "+" type is installed, and the first de-noising network 21 and the second de-noising network 22 that constitutes the taper network is installed, so that eliminate vibration and the noise that directly contacts generation owing to steam and water.Be condensed into water as the above-mentioned most of water vapor of having eliminated vibration and noise in the bottom of condensation chamber 5, the steam that does not condense has been finished its condensation operation when passing porose separating plate 23, said separating plate is provided with little intensive hole at the center of condensation chamber 5.When the condensation number of steam during greater than the evaporation of water amount, vacuum phenomenon appears in the inside at equipment, produce negative pressure, thus from the water of gravity tank suction successively to the top of suction mouth 1, economizer 2, suction water passage 3, suction water non-return side 4, condensation chamber 5, the bottom that connects water pipe 6, condensation chamber 5, connection suction pipe 7 and pump chamber 8.By repeating following operation continuously: by continuous calory burning produce steam, collect the steam that produces on the top of pump 8, to the instantaneous discharged steam in the bottom of condensation chamber 5, condensing steam is water once more, just can aspirate under the situation of the recycle unit that is not subjected to the external force effect according to equipment of the present invention.
In operation period of the present invention, the air that produces in the inside of equipment is discharged in the air by air vents side 24 during at emissions operation, and the non-return side becomes by negative pressure and produce the suction operation, thereby can prevent that suction from keeping side 24 to carry out.The step that adds hot water is as follows: force in the following order under the current: the suction water reverse side 4 of combuster 31 between suction water route 3 and draining connecting path 13, condensation chamber 5, connect water pipe 6, connect discharge pipe 7, pump chamber 8, connect discharge pipe 9, steam raising chamber 10, the water passage 11 that passage changes, discharge water non-return side 13, and be discharged into the residual steam in the water in condensation process in the air according to the following steps: the condensation/recovery of water makes water rising and mobile simultaneously: steam connection tube 17 in the following order, the top of steam connecting plate 20, the first de-noising network 21, the second de-noising network 22, the bottom of condensation chamber 5, porose separating plate 23, with discharge orifice side 24.In addition, be used for as previously discussed that the equipment of suction and draining is parallel to be equipped with multistagely, thereby can reduce the vibration of link that circulates, and strengthen level and smooth driving.
The difference of reverse burning of the present invention and conventional reverse burning is: the energy that is obtained by the speed of fluid has produced negative pressure, and the front and rear of firing chamber carries out two-way reverse, therefore fuel and air can be in contact with one another 5 times, therefore might realize perfect combustion.
Attempt fuel combination and air to obtain rotating force according to burner of the present invention, allow the first portion's air that produces by blower pass through closure simultaneously, allow 31 the anterior reverse burning of second portion air in the firing chamber, and allow the third part air in the firing chamber burning of 31 rear portion and conventional burner similar.As shown in Figure 1, the first and second part air that enter in the burner insertion opening 25 rotate, fuel burns in firing chamber 31, and repeat to have produced negative pressure between the heating chamber 14-1 at front surface reverse burning plate 29 and front surface discharge water, allow the first and second part air pass the center of front surface reverse burning plate 29 apace simultaneously, suction and the unburnt gas that the inside of steam generating chamber 10 contacts whereby makes great efforts to make it to rekindle with the contact of second portion air and with the second portion air.After this, allow at the third part air of the 3rd air connecting tube 26 and the heating of the 3rd air flue 27 center by a relevant opening 28 and rear surface reverse burning plate 30 fast, thereby repeat to produce negative pressure between the heating chamber 14-2 at rear surface reverse burning plate 30 and rear surface discharge water, whereby suction in the firing chamber collect and the unburnt gas that contact with third part gas in 31 top so that make its perfect combustion.Collect through the above the combusted gas generant cigarette ash that burn on 31 top in the firing chamber, promptly relative lighter non-combustion gas, and it is become burn when reverse under the effect of reverse burning plate.Also have, the combustion gas of perfect combustion are after the high temperature smoke pipe 32 of steam generating chamber 10 and the foot by being connected firing chamber 31 transfers out most of calory burning, all the other heats of discharging from the top of steam generating chamber 10 rise along waste gas rising path 39, bottom at the separating plate 35 that is made of thermoinsulation material descends, and raises once more along the low temperature smoke pipe 33 of economizer 2.After this, successively after pump chamber 8, economizer 2 and condensation chamber 5 transmission after-heats and simultaneously said after-heat descend once more along the space that forms between condensation chamber 5 and economizer 2, by chimney gaseous emission to atmosphere.In other words, the direction that flows of the flow direction of combustion gas and water is opposite, can improve the thermal efficiency whereby, makes it reach best.
From the above obviously as can be seen, the present invention has useful effect: by using a general burner without the change firing unit, employing is according to thermal losses structure of the present invention and combustion method, just can obtain perfect combustion greatly by less heat loss, and under the situation of not using other recycle pump or water pump, just can produce hot water continuously, the hot water that has fundamentally changed prior art whereby produces the implication of equipment or water-heating boiler, and can produce hot water at an easy rate by the most cheap cost.
Though represented and described to be considered to the preferred embodiments of the present invention, one of ordinary skill in the art will appreciate that to produce various changes and modifications, and available equivalents is replaced each parts and can not departed from scope of the present invention.In addition, can carry out many improvement with the particular case of the instruction that adapts to the present invention and provide and don't depart from center range of the present invention.Therefore expectation the invention is not restricted to implementing the disclosed certain embodiments of best mode of the present invention, but expectation the present invention includes all embodiments in the scope that falls into appending claims.

Claims (1)

1. parallel multistage heat pump that utilizes evaporation of water and condensation principle comprises:
A chamber structure, it is more than two-stage, be connected with a columniform steam generating chamber, have one and connect discharge pipe, a high temperature smoke pipe, the water passage of a channel change, with a discharge water non-return side, wherein constitute a firing chamber, a front surface discharge water in the both sides of said firing chamber repeats heating chamber and a rear surface discharge water repeats heating chamber, a burner inserts opening, one the 3rd air flue, an opening that runs through, a front surface reverse burning plate, with a rear surface reverse burning plate, whereby, after ignitable fuel contacts five times with air, the combustion gas of discharging bottom in said firing chamber;
A pump structure, it has a pump chamber, a condensation chamber and a kind of thermoinsulation material; Pump chamber comprises: connection suction pipe, one connect steam tube, outer steam discharge pipe and at the interior steam discharge pipe on the top of the said steam of each of the said firing chamber of formation generating chamber; Condensation chamber comprises: suction water non-return side, one connect water pipe, "+" type burst buffer plate, first de-noising network, second de-noising network, porose separating plate and at an exhaust port of its outside; Thermoinsulation material is used to stop moving of between said pump chamber and said condensation chamber heat;
An economizer, it has a low temperature smoke pipe and a channel change separating plate, be positioned at said pump structure around and and to be connected water pipe continuous; With
A structure is used to connect a suction water passage, a discharge water connecting path, a discharge pipe, and is connected air and outer loop link by a suction opening, an exhaust openings with a chimney.
CN988085569A 1998-05-06 1998-05-06 Parallel multistage type hot water pump using water evaporation and condensation principle Expired - Fee Related CN1131943C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/KR1998/000113 WO1999057442A1 (en) 1998-05-06 1998-05-06 Parallel multistage type hot water pump using water evaporation and condensation principle

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CN1268210A true CN1268210A (en) 2000-09-27
CN1131943C CN1131943C (en) 2003-12-24

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CN (1) CN1131943C (en)
AU (1) AU7084298A (en)
RU (1) RU2195585C2 (en)
WO (1) WO1999057442A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108889921A (en) * 2018-07-05 2018-11-27 宁波北仑益鸣企业管理服务有限公司 Mold vacuum evacuation device and the technique for vacuumizing operation accordingly

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2511328C2 (en) * 2012-08-20 2014-04-10 Федеральное государственное автономное образовательное учреждение высшего профессионального образования "Белгородский государственный национальный исследовательский университет" (НИУ "БелГУ") Method for pumpless fluid pumping-out

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Publication number Priority date Publication date Assignee Title
JPS4977003A (en) * 1972-11-29 1974-07-25
JPS6030485A (en) * 1983-07-30 1985-02-16 Noriaki Wakao Piston driven temperature difference pump

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108889921A (en) * 2018-07-05 2018-11-27 宁波北仑益鸣企业管理服务有限公司 Mold vacuum evacuation device and the technique for vacuumizing operation accordingly

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WO1999057442A1 (en) 1999-11-11
CN1131943C (en) 2003-12-24
RU2195585C2 (en) 2002-12-27
AU7084298A (en) 1999-11-23

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