CN103868126B - The fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water is provided simultaneously - Google Patents
The fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water is provided simultaneously Download PDFInfo
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- CN103868126B CN103868126B CN201410071224.1A CN201410071224A CN103868126B CN 103868126 B CN103868126 B CN 103868126B CN 201410071224 A CN201410071224 A CN 201410071224A CN 103868126 B CN103868126 B CN 103868126B
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Abstract
The present invention relates to a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously, including a secondary net hot water tube system (1), first via secondary network hot water tube system (2), second road secondary network hot water tube system (3), First Heat Exchanger (4), second heat exchanger (5), hot water lithium bromide absorbing unit (6) and direct-burning type lithium bromide absorption type unit (7), the secondary net hot water going out a secondary net hot water tube system (1) is introduced into first generator (604) of hot water lithium bromide absorbing unit (6), after out, series connection enters First Heat Exchanger (4) and the second heat exchanger (5) again, after passing through second vaporizer (701) of direct-burning type lithium bromide absorption type unit (7), flow out through a secondary net hot water tube system (1).The present invention can realize when reducing secondary net hot water backwater's temperature, increasing by the effective heat release temperature difference of secondary net hot water, central heating system spike heating demand can also be undertaken, and two-way hot water can be provided simultaneously, two-way hot water is separate, and temperature and pressure can be different.
Description
Technical field
The present invention relates to a kind of suction-type lithium bromide heat-exchange system.Belong to air conditioner technical field.
Background technology
In conventional central heating system, a secondary net hot water is after the heated intensification in thermal source place, is sent to each heat user by heating network, after passing through heat exchanger heat exchange cooling at each heat user place with secondary network hot water, returns thermal source place heat temperature raising again through heating network.
The ordinary heat exchanger (being water-water heat exchanger in diagram) as shown in Figure 1 that each heat user place uses, one secondary net hot water and secondary network hot water carry out heat exchange by heat exchanger tube (shell-and-tube heat exchanger) or heat-transfer surface (plate type heat exchanger), heat in one secondary net hot water is delivered in secondary network hot water, one secondary net hot water temperature declines, secondary network hot water temperature raises, completing secondary network hot water process of heat-obtaining from a secondary net hot water, secondary network hot water is transported to thermal field for producing or life, heating again.By configuring multiple heat exchanger, the different hot water demands (different pressures or different temperatures) at same heat user place can be met.
For reducing heating network construction cost and heat conveying cost, it is necessary to increase the supply water temperature of a secondary net hot water or reduce its return water temperature, to increase supply backwater temperature difference, thus reducing required flow when carrying identical heat as far as possible.But owing to the heatproof of heating network limits, the supply water temperature of a secondary net hot water can not be too high.And the ordinary heat exchanger adopted, a secondary net hot water and secondary network hot water need certain heat transfer temperature difference could realize effective heat exchange, so the return water temperature of a secondary net hot water needs to be higher than the inlet temperature of secondary network hot water in theory.After the temperature of secondary network hot water is determined, the return water temperature of a secondary net hot water is restricted, and the available temperature difference of a secondary net hot water is by the restriction of secondary network hot water temperature.If new flow process and system can be adopted, when ensureing secondary network hot water temperature, reduce the return water temperature of a secondary net hot water, break through its restriction bottleneck higher than secondary network hot water inlet temperature, then can realize aforementioned minimizing heating network construction cost and the purpose of heat conveying cost.
Additionally, because central heating system needs to meet heat demand during most cold snap, thus heating network is all the design and construction that carry out according to maximum heating demand, but in actual moving process, the heating system overwhelming majority time is all run under part heating demand, and this has resulted in the waste of heating network heat capacity.If new flow process and system can be adopted, the peakload of heat supply peak period is undertaken by the equipment of heat user, central heating network is made only to undertake a degree of basic load, then under identical central heating ability, the construction cost of heating network can reduce, the oepration at full load time lengthening of heating network, the investment utilization ratio of heating network can get a promotion.
Summary of the invention
It is an object of the invention to overcome above-mentioned deficiency, a kind of return water temperature reducing a secondary net hot water in original technical foundation is provided, to realize increasing by the effective heat release temperature difference of secondary net hot water, and central heating system spike heating demand can be undertaken, and the suction-type lithium bromide heat-exchange system of two-way hot water can be provided simultaneously, two-way hot water is separate, and temperature and pressure can be different.
nullThe object of the present invention is achieved like this: a kind of fuel supplementing type suction-type lithium bromide heat-exchange system simultaneously providing two-way hot water,Including a secondary net hot water tube system、First via secondary network hot water tube system and First Heat Exchanger,Described system also has additional the second road secondary network hot water tube system、Second heat exchanger、Hot water lithium bromide absorbing unit and direct-burning type lithium bromide absorption type unit,Hot water lithium bromide absorbing unit includes the first vaporizer、First absorber、First condenser and the first generator,Direct-burning type lithium bromide absorption type unit includes the second vaporizer、Second absorber、Second condenser and the second generator,The secondary net hot water going out a described secondary net hot water tube system is introduced into the first generator of hot water lithium bromide absorbing unit,After out, series connection enters First Heat Exchanger and the second heat exchanger again,After passing through the second vaporizer of direct-burning type lithium bromide absorption type unit,Flow out through a secondary net hot water tube system;Go out all or part of first vaporizer flowing through hot water lithium bromide absorbing unit of the hot water backwater of described second road secondary network hot water tube system, enter back into the second heat exchanger, the remainder going out the hot water backwater of described second road secondary network hot water tube system and the hot water backwater going out first via secondary network hot water tube system then each flow through the first absorber of hot water lithium bromide absorbing unit, second absorber of the first condenser and direct-burning type lithium bromide absorption type unit, different parts in second condenser and First Heat Exchanger, flow out then through respective secondary network hot water tube system.
A kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention, the hot water backwater going out described second road secondary network hot water tube system first flows through the first vaporizer of hot water lithium bromide absorbing unit, enter back into the second heat exchanger after cooling and a secondary net hot water heat exchange heats up, finally flow out then through the second road secondary network hot water tube system;The hot water backwater going out described first via secondary network hot water tube system is divided into two strands, one series connection flows through the first absorber of hot water lithium bromide absorbing unit, the first condenser, after another burst of series connection flows through the second absorber of direct-burning type lithium bromide absorption type unit, the second condenser intensification, after the hot water backwater that two strands of first via secondary network hot water tube systems come converges, last series connection again flows through First Heat Exchanger and a secondary net hot water heat exchange heats up, and finally flows out then through first via secondary network hot water tube system.
A kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention, the hot water backwater going out described second road secondary network hot water tube system is that all series connection flows through the first vaporizer and second heat exchanger of hot water lithium bromide absorbing unit, and the hot water going out described first via secondary network hot water tube system then flows through the second absorber in the first absorber of hot water lithium bromide absorbing unit, the first condenser and direct-burning type lithium bromide absorption type unit, the second condenser and First Heat Exchanger.
A kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention, the hot water backwater going out described second road secondary network hot water tube system is divided into two strands, one series connection flows through the first vaporizer and second heat exchanger of hot water lithium bromide absorbing unit, another strand then flows through the first absorber of hot water lithium bromide absorbing unit, second absorber of the first condenser and direct-burning type lithium bromide absorption type unit, any one or more in second condenser, the hot water backwater going out described first via secondary network hot water tube system then only flows through the first absorber of hot water lithium bromide absorbing unit, second absorber of the first condenser and direct-burning type lithium bromide absorption type unit, remainder in second condenser and First Heat Exchanger.
nullA kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention,The hot water backwater going out described second road secondary network hot water tube system is divided into two strands,One series connection flows through the first vaporizer and second heat exchanger of hot water lithium bromide absorbing unit,Another strand then flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、After any one or more in second condenser,Two strands of water converge,Pass through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、In second condenser, remainder is any one or more,The hot water backwater going out described first via secondary network hot water tube system then only flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、Remainder in second condenser and First Heat Exchanger.
nullA kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention,The hot water backwater going out described second road secondary network hot water tube system is divided into two strands,After one series connection flows through the first vaporizer and second heat exchanger of hot water lithium bromide absorbing unit,In parallel again or random order is connected、Connection in series-parallel flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、Any one or more in second condenser,Another strand then flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、In second condenser, remaining is any one or more,The hot water backwater going out described first via secondary network hot water tube system then only flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、Remainder in second condenser and First Heat Exchanger.
nullA kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention,Go out the hot water backwater that described second road secondary network hot water tube system comes and be divided into two strands,After one series connection flows through the first vaporizer and second heat exchanger of hot water lithium bromide absorbing unit,In parallel again or random order is connected、Connection in series-parallel flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、Any one in second condenser,And another strand also flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、In second condenser remaining any one,After two strands of water converge,Pass through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、In second condenser remainder any one,The hot water backwater that first via secondary network hot water tube system comes then only flows through the first absorber of hot water lithium bromide absorbing unit、Second absorber of the first condenser and direct-burning type lithium bromide absorption type unit、Residue in second condenser that and First Heat Exchanger.
nullA kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously of the present invention,Including a secondary net hot water tube system、First via secondary network hot water tube system and First Heat Exchanger,Described system also has additional the second road secondary network hot water tube system、Second heat exchanger、Hot water lithium bromide absorbing unit and direct-burning type lithium bromide absorption type unit,Hot water lithium bromide absorbing unit includes the first vaporizer、First absorber、First condenser and the first generator,Direct-burning type lithium bromide absorption type unit includes the second vaporizer、Second absorber、Second condenser and the second generator,The secondary net hot water going out a described secondary net hot water tube system is introduced into the first generator of hot water lithium bromide absorbing unit,After out, series connection enters First Heat Exchanger and the second heat exchanger again,After passing through the second vaporizer of direct-burning type lithium bromide absorption type unit,Flow out through a secondary net hot water tube system;The hot water backwater's parallel connection going out described second road secondary network hot water tube system is divided into two strands, one first flows through the first vaporizer of hot water lithium bromide absorbing unit, enter back into the second heat exchanger, another plume is through the first absorber of hot water lithium bromide absorbing unit, two strands of secondary network hot water are supplied water after converging and are flowed out by secondary network hot water tube system, the hot water backwater going out described first via secondary network hot water tube system first flows through the second absorber of direct-burning type lithium bromide absorption type unit, parallel connection flows through the first condenser of hot water lithium bromide absorbing unit and the second condenser of direct-burning type lithium bromide absorption type unit again, last series connection again flows through First Heat Exchanger, last then through the outflow of first via secondary network hot water tube system.
The present invention is by arranging hot water lithium bromide absorbing unit, direct-burning type lithium bromide absorption type unit and two heat exchangers, all or part of of second road secondary network hot water is first flowed through the vaporizer of hot water lithium bromide absorbing unit, enter back into after cooling in the second heat exchanger with a secondary net hot water heat exchange, the temperature that once net hot water goes out heat exchanger can be made to drop lower than secondary network return water temperature, finally a secondary net hot water is allowed to flow through the vaporizer of direct-burning type lithium bromide absorption type unit again, it is possible to be even lower by the return water temperature of a secondary net further.Additionally, remainder and the first via secondary network hot water tube system hot water backwater of the second road secondary network hot water tube system hot water backwater then each flow through the different parts in hot water lithium bromide absorbing unit absorber, condenser and direct-burning type lithium bromide absorption type unit absorber, condenser and (or) First Heat Exchanger, it is possible to obtain heat and temperature raise.The direct-burning type lithium bromide absorption type unit of the present invention does not need when part heating demand to run, and is only heated secondary network hot water by a secondary net hot water liberated heat;When the heat of a secondary net hot water can not meet heat demand, restart direct-burning type lithium bromide absorption type unit, the return water temperature of a secondary net hot water can be reduced on the one hand further, extract more heat in secondary network hot water, on the other hand, the heat that fuel combustion produces can supply the breach between a secondary net hot water thermal amount and heating demand, bears spike heating demand.Compared with conventional art, the present invention can be implemented in reduction by one secondary net hot water backwater's temperature, when increasing by the effective heat release temperature difference of secondary net hot water, central heating system spike heating demand can also be undertaken, and the suction-type lithium bromide heat-exchange system of two-way hot water can be provided simultaneously, two-way hot water is separate, and temperature and pressure can be different.
The invention has the beneficial effects as follows:
1, when a secondary net hot water flow is fixing, adopts unit of the present invention can reduce its return water temperature, improve and effectively utilize the temperature difference, it is possible to increase the extraction of heat and utilize quantity, improve the heat capacity of system.
2, during identical heating demand, afterburning fuel can undertake spike heating demand, and heating network only needs to undertake a degree of basic load, thus reducing the flow of a secondary net hot water, reduces the construction cost of its conveying cost and heating network, thermal source place.
3, the two-way hot water that temperature is different, pressure is different can be provided, it is possible to meet two kinds of different heat demand of the same area simultaneously simultaneously.
Accompanying drawing explanation
Fig. 1 is the fundamental diagram of conventional ordinary heat exchanger multichannel heat supply.
Fig. 2 is one of application example of fuel supplementing type suction-type lithium bromide heat-exchange system that present invention simultaneously provides two-way hot water.
Fig. 3 is the two of the application example of the fuel supplementing type suction-type lithium bromide heat-exchange system that present invention simultaneously provides two-way hot water.
Accompanying drawing labelling in figure:
One secondary net hot water tube system 1, first via secondary network hot water tube system the 2, second road secondary network hot water tube system 3, First Heat Exchanger the 4, second heat exchanger 5, hot water lithium bromide absorbing unit 6, direct-burning type lithium bromide absorption type unit 7, first vaporizer the 601, first absorber the 602, first condenser 603 and the first generator 604 of hot water lithium bromide absorbing unit 6, the second vaporizer the 701, second absorber the 702, second condenser 703 and the second generator 704 of direct-burning type lithium bromide absorption type unit 7.
One secondary net hot water enters A1, a secondary net hot water goes out A2, first via secondary network hot water backwater enters B1, first via secondary network hot water backwater goes out B2, the second road secondary network hot water backwater enters C1, the second road secondary network hot water backwater goes out C2.
Detailed description of the invention
Fig. 2 is for providing a kind of application example figure of the fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water while involved in the present invention.This system is made up of a secondary net hot water tube system 1, first via secondary network hot water tube system the 2, second road secondary network hot water tube system 3, First Heat Exchanger the 4, second heat exchanger 5, hot water lithium bromide absorbing unit 6 and direct-burning type lithium bromide absorption type unit 7.Hot water lithium bromide absorbing unit 6 includes the first vaporizer the 601, first absorber the 602, first condenser 603 and the first generator 604.Direct-burning type lithium bromide absorption type unit 7 includes the second vaporizer the 701, second absorber the 702, second condenser 703 and the second generator 704.The secondary net hot water that one secondary net hot water tube system 1 comes is introduced into after the first generator 604 of hot water lithium bromide absorbing unit 6 once lowers the temperature as driving heat source, series connection entrance First Heat Exchanger 4 and the second heat exchanger 5 are lowered the temperature again, after passing through the second vaporizer 701 of direct-burning type lithium bromide absorption type unit 7, flow out through a secondary net hot water tube system 1;The hot water backwater that first via secondary network hot water tube system 2 comes is divided into two strands, one series connection flows through first absorber the 602, first condenser 603 of hot water lithium bromide absorbing unit 6, after another burst of series connection flows through second absorber the 702, second condenser 703 intensification of direct-burning type lithium bromide absorption type unit 7, after the hot water backwater that two strands of first via secondary network hot water tube systems 2 come converges, last series connection again flows through First Heat Exchanger 4 and a secondary net hot water heat exchange heats up, and finally flows out then through first via secondary network hot water tube system 2;The hot water backwater that second road secondary network hot water tube system 3 comes first flows through the first vaporizer 601 of hot water lithium bromide absorbing unit 6, enter back into the second heat exchanger 5 after cooling and a secondary net hot water heat exchange heats up, finally flow out then through the second road secondary network hot water tube system 3.
There is provided in the fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water while shown in Fig. 2, the hot water backwater that second road secondary network hot water tube system 3 comes is that all series connection flows through the first vaporizer 601 and the second heat exchanger 5 of hot water lithium bromide absorbing unit 6, and the hot water that first via secondary network hot water tube system 2 comes then flows through the second absorber the 702, second condenser 703 and the first heat exchanger 4 in first absorber the 602, first condenser 603 of hot water lithium bromide absorbing unit 6 and direct-burning type lithium bromide absorption type unit 7.It can also be that the hot water backwater that the second road secondary network hot water tube system 3 comes is divided into two strands, one series connection flows through the first vaporizer 601 and the second heat exchanger 5 of hot water lithium bromide absorbing unit 6, another strand then flows through the first absorber 602 of hot water lithium bromide absorbing unit 6, second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7, any one or more in second condenser 703, the hot water backwater that first via secondary network hot water tube system 2 comes then only flows through the first absorber 602 of hot water lithium bromide absorbing unit 6, second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7, remainder in second condenser 703 and First Heat Exchanger 4;nullIt can also is that the hot water backwater that the second road secondary network hot water tube system 3 comes is divided into two strands,One series connection flows through the first vaporizer 601 and the second heat exchanger 5 of hot water lithium bromide absorbing unit 6,Another strand then flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、After any one or more in second condenser 703,Two strands of water converge,Pass through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、In second condenser 703, remainder is any one or more,The hot water backwater that first via secondary network hot water tube system 2 comes then only flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、Remainder in second condenser 703 and First Heat Exchanger 4;nullOr second the hot water backwater that comes of road secondary network hot water tube system 3 be divided into two strands,After one series connection flows through the first vaporizer 601 and second heat exchanger 5 of hot water lithium bromide absorbing unit 6,In parallel again or random order is connected、Connection in series-parallel flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、Any one or more in second condenser 703,Another strand then flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、In second condenser 703, remaining is any one or more,The hot water backwater that first via secondary network hot water tube system 2 comes then only flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、Remainder in second condenser 703 and First Heat Exchanger 4;nullOr second the hot water backwater that comes of road secondary network hot water tube system 3 be divided into two strands,After one series connection flows through the first vaporizer 601 and second heat exchanger 5 of hot water lithium bromide absorbing unit 6,In parallel again or random order is connected、Connection in series-parallel flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、Any one in second condenser 703,And another strand also flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、In second condenser 703 remaining any one,After two strands of water converge,Pass through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、In second condenser 703 remainder any one,The hot water backwater that first via secondary network hot water tube system 2 comes then only flows through the first absorber 602 of hot water lithium bromide absorbing unit 6、Second absorber 702 of the first condenser 603 and direct-burning type lithium bromide absorption type unit 7、Residue in second condenser 703 that and First Heat Exchanger 4.
Thering is provided the hot water lithium bromide absorbing unit in the fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water and direct-burning type lithium bromide absorption type unit while shown in Fig. 2 can be single-action, economic benefits and social benefits or diarcs unit.One secondary net hot-water heating system and secondary network hot-water heating system can be closed circulation systems, it is also possible to be open system.
Fig. 3 is for providing the two of all the other application examples figure of the fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water while involved in the present invention.This system is made up of a secondary net hot water tube system 1, first via secondary network hot water tube system the 2, second road secondary network hot water tube system 3, First Heat Exchanger the 4, second heat exchanger 5, hot water lithium bromide absorbing unit 6 and direct-burning type lithium bromide absorption type unit 7.Hot water lithium bromide absorbing unit 6 includes the first vaporizer the 601, first absorber the 602, first condenser 603 and the first generator 604.Direct-burning type lithium bromide absorption type unit 7 includes the second vaporizer the 701, second absorber the 702, second condenser 703 and the second generator 704.The secondary net hot water that one secondary net hot water tube system 1 comes is introduced into after the first generator 604 of hot water lithium bromide absorbing unit 6 once lowers the temperature as driving heat source, series connection enters cooling in First Heat Exchanger 4 and the second heat exchanger 5 again, after passing through the second vaporizer 701 of direct-burning type lithium bromide absorption type unit 7, flow out through a secondary net hot water tube system 1;The hot water backwater that first via secondary network hot water tube system 2 comes first flows through the second absorber 702 of direct-burning type lithium bromide absorption type unit 7, after second condenser 703 of the first condenser 603 flowing through hot water lithium bromide absorbing unit 6 in parallel and direct-burning type lithium bromide absorption type unit 7 heats up again, last series connection again flows through First Heat Exchanger 4 and a secondary net hot water heat exchange heats up, and finally flows out then through first via secondary network hot water tube system 2;Hot water backwater's parallel connection that second road secondary network hot water tube system 3 comes is divided into two strands, one first flows through the first vaporizer 601 of hot water lithium bromide absorbing unit 6, enter back into the second heat exchanger 5 after cooling and a secondary net hot water heat exchange heats up, another plume heats up through the first absorber 602 of hot water lithium bromide absorbing unit 6, and two strands of secondary network hot water are supplied water after converging and flowed out by secondary network hot water tube system 3.
Claims (10)
- null1. the fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously,Including a secondary net hot water tube system (1)、First via secondary network hot water tube system (2) and First Heat Exchanger (4),It is characterized in that described system also has additional the second road secondary network hot water tube system (3)、Second heat exchanger (5)、Hot water lithium bromide absorbing unit (6) and direct-burning type lithium bromide absorption type unit (7),Hot water lithium bromide absorbing unit (6) includes the first vaporizer (601)、First absorber (602)、First condenser (603) and the first generator (604),Direct-burning type lithium bromide absorption type unit (7) includes the second vaporizer (701)、Second absorber (702)、Second condenser (703) and the second generator (704),The secondary net hot water going out a described secondary net hot water tube system (1) is introduced into first generator (604) of hot water lithium bromide absorbing unit (6),After out, series connection enters First Heat Exchanger (4) and the second heat exchanger (5) again,After passing through second vaporizer (701) of direct-burning type lithium bromide absorption type unit (7),Flow out through a secondary net hot water tube system (1);Go out all or part of first vaporizer (601) flowing through hot water lithium bromide absorbing unit (6) of the hot water backwater on described second road secondary network hot water tube system (3), enter back into the second heat exchanger (5), the remainder going out the hot water backwater on described second road secondary network hot water tube system (3) and the hot water backwater going out first via secondary network hot water tube system (2) then each flow through first absorber (602) of hot water lithium bromide absorbing unit (6), second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7), different parts in second condenser (703) and First Heat Exchanger (4), flow out then through respective secondary network hot water tube system.
- 2. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1, the hot water backwater that it is characterized in that described second road secondary network hot water tube system (3) first flows through first vaporizer (601) of hot water lithium bromide absorbing unit (6), enter back into the second heat exchanger (5) after cooling to heat up with a secondary net hot water heat exchange, finally flow out then through the second road secondary network hot water tube system (3);The hot water backwater going out described first via secondary network hot water tube system (2) is divided into two strands, one series connection flows through first absorber (602) of hot water lithium bromide absorbing unit (6), first condenser (603), another burst of series connection flows through second absorber (702) of direct-burning type lithium bromide absorption type unit (7), after second condenser (703) heats up, after the hot water backwater that two bursts of first via secondary network hot water tube system (2) come converges, last series connection again flows through First Heat Exchanger (4) and heats up with a secondary net hot water heat exchange, last then through first via secondary network hot water tube system (2) outflow.
- 3. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1, it is characterized in that the hot water backwater described second road secondary network hot water tube system (3) is that all series connection flows through the first vaporizer (601) and second heat exchanger (5) of hot water lithium bromide absorbing unit (6), the hot water going out described first via secondary network hot water tube system (2) then flows through first absorber (602) of hot water lithium bromide absorbing unit (6), the second absorber (702) in first condenser (603) and direct-burning type lithium bromide absorption type unit (7), second condenser (703) and First Heat Exchanger (4).
- null4. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1,It is characterized in that the hot water backwater described second road secondary network hot water tube system (3) is divided into two strands,One series connection flows through the first vaporizer (601) and second heat exchanger (5) of hot water lithium bromide absorbing unit (6),Another stock then flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Any one or more in second condenser (703),The hot water backwater going out described first via secondary network hot water tube system (2) then only flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Remainder in second condenser (703) and First Heat Exchanger (4).
- null5. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1,It is characterized in that the hot water backwater described second road secondary network hot water tube system (3) is divided into two strands,One series connection flows through the first vaporizer (601) and second heat exchanger (5) of hot water lithium bromide absorbing unit (6),Another stock then flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、After any one or more in second condenser (703),Two strands of water converge,Pass through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、In second condenser (703), remainder is any one or more,The hot water backwater going out described first via secondary network hot water tube system (2) then only flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Remainder in second condenser (703) and First Heat Exchanger (4).
- null6. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1,It is characterized in that the hot water backwater described second road secondary network hot water tube system (3) is divided into two strands,After one series connection flows through the first vaporizer (601) and second heat exchanger (5) of hot water lithium bromide absorbing unit (6),In parallel again or random order is connected、Connection in series-parallel flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Any one or more in second condenser (703),Another stock then flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、In second condenser (703), remaining is any one or more,The hot water backwater going out described first via secondary network hot water tube system (2) then only flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Remainder in second condenser (703) and First Heat Exchanger (4).
- null7. a kind of fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously according to claim 1,It is characterized in that the hot water backwater that described second road secondary network hot water tube system (3) comes and be divided into two strands,After one series connection flows through the first vaporizer (601) and second heat exchanger (5) of hot water lithium bromide absorbing unit (6),In parallel again or random order is connected、Connection in series-parallel flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Any one in second condenser (703),And another stock also flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、In second condenser (703) remaining any one,After two strands of water converge,Pass through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、In second condenser (703) remainder any one,The hot water backwater that first via secondary network hot water tube system (2) comes then only flows through first absorber (602) of hot water lithium bromide absorbing unit (6)、Second absorber (702) of the first condenser (603) and direct-burning type lithium bromide absorption type unit (7)、Residue in second condenser (703) that and First Heat Exchanger (4).
- null8. the fuel supplementing type suction-type lithium bromide heat-exchange system that two-way hot water is provided simultaneously,Including a secondary net hot water tube system (1)、First via secondary network hot water tube system (2) and First Heat Exchanger (4),It is characterized in that described system also has additional the second road secondary network hot water tube system (3)、Second heat exchanger (5)、Hot water lithium bromide absorbing unit (6) and direct-burning type lithium bromide absorption type unit (7),Hot water lithium bromide absorbing unit (6) includes the first vaporizer (601)、First absorber (602)、First condenser (603) and the first generator (604),Direct-burning type lithium bromide absorption type unit (7) includes the second vaporizer (701)、Second absorber (702)、Second condenser (703) and the second generator (704),The secondary net hot water going out a described secondary net hot water tube system (1) is introduced into first generator (604) of hot water lithium bromide absorbing unit (6),After out, series connection enters First Heat Exchanger (4) and the second heat exchanger (5) again,After passing through second vaporizer (701) of direct-burning type lithium bromide absorption type unit (7),Flow out through a secondary net hot water tube system (1);nullThe hot water backwater's parallel connection going out described second road secondary network hot water tube system (3) is divided into two strands,One first flows through first vaporizer (601) of hot water lithium bromide absorbing unit (6),Enter back into the second heat exchanger (5),Another plume is through first absorber (602) of hot water lithium bromide absorbing unit (6),Two strands of secondary network hot water are supplied water after converging and are flowed out by secondary network hot water tube system,The hot water backwater going out described first via secondary network hot water tube system (2) first flows through second absorber (702) of direct-burning type lithium bromide absorption type unit (7),Parallel connection flows through first condenser (603) of hot water lithium bromide absorbing unit (6) and second condenser (703) of direct-burning type lithium bromide absorption type unit (7) again,Last series connection again flows through First Heat Exchanger (4),Last then through first via secondary network hot water tube system (2) outflow.
- 9. according to one of them described a kind of fuel supplementing type suction-type lithium bromide heat-exchange system providing two-way hot water of claim 1 ~ 8 simultaneously, it is characterised in that hot water lithium bromide absorbing unit (6) and direct-burning type lithium bromide absorption type unit (7) in described system are single-action, economic benefits and social benefits or diarcs unit.
- 10. according to one of them described a kind of fuel supplementing type suction-type lithium bromide heat-exchange system providing two-way hot water of claim 1 ~ 8 simultaneously, it is characterized in that the secondary net hot water tube system (1) in described system, first via secondary network hot water tube system (2) and the second road secondary network hot water tube system (3) they are closed circulation systems, or open system.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1189598A (en) * | 1998-01-08 | 1998-08-05 | 江苏双良集团公司 | Two-section or multi-section hot water lithium bromide absorbing refrigerating unit |
CN101329117A (en) * | 2008-07-23 | 2008-12-24 | 北京环能瑞通科技发展有限公司 | Integral type absorption type heat exchange machine unit |
CN202119157U (en) * | 2011-06-25 | 2012-01-18 | 双良节能系统股份有限公司 | Steam type lithium bromide absorption type heat pump capable of efficiently utilizing working steam water condensation heat |
CN204141672U (en) * | 2014-03-01 | 2015-02-04 | 双良节能系统股份有限公司 | The fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water is provided simultaneously |
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JP3900098B2 (en) * | 2003-03-20 | 2007-04-04 | 株式会社デンソー | Water heater |
JP5457163B2 (en) * | 2009-12-21 | 2014-04-02 | 川重冷熱工業株式会社 | Control method and apparatus for absorption chiller / heater using exhaust gas of distributed power generation system |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1189598A (en) * | 1998-01-08 | 1998-08-05 | 江苏双良集团公司 | Two-section or multi-section hot water lithium bromide absorbing refrigerating unit |
CN101329117A (en) * | 2008-07-23 | 2008-12-24 | 北京环能瑞通科技发展有限公司 | Integral type absorption type heat exchange machine unit |
CN202119157U (en) * | 2011-06-25 | 2012-01-18 | 双良节能系统股份有限公司 | Steam type lithium bromide absorption type heat pump capable of efficiently utilizing working steam water condensation heat |
CN204141672U (en) * | 2014-03-01 | 2015-02-04 | 双良节能系统股份有限公司 | The fuel supplementing type suction-type lithium bromide heat-exchange system of two-way hot water is provided simultaneously |
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