CN201340135Y - Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set - Google Patents
Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set Download PDFInfo
- Publication number
- CN201340135Y CN201340135Y CNU2009200379760U CN200920037976U CN201340135Y CN 201340135 Y CN201340135 Y CN 201340135Y CN U2009200379760 U CNU2009200379760 U CN U2009200379760U CN 200920037976 U CN200920037976 U CN 200920037976U CN 201340135 Y CN201340135 Y CN 201340135Y
- Authority
- CN
- China
- Prior art keywords
- solution
- hot water
- heat exchanger
- generator
- hot
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 113
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 title claims abstract description 35
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 21
- 230000000694 effects Effects 0.000 title claims description 8
- 238000002485 combustion reaction Methods 0.000 title description 16
- 239000002131 composite material Substances 0.000 title description 7
- 239000006096 absorbing agent Substances 0.000 claims abstract description 21
- 239000003507 refrigerant Substances 0.000 claims abstract description 14
- 150000001875 compounds Chemical class 0.000 claims 4
- 239000012530 fluid Substances 0.000 claims 1
- 239000003517 fume Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 12
- -1 compound lithium bromide Chemical class 0.000 abstract description 5
- 238000005192 partition Methods 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 description 16
- 239000000446 fuel Substances 0.000 description 15
- 239000007788 liquid Substances 0.000 description 13
- 238000004378 air conditioning Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000295 complement effect Effects 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
本实用新型涉及一种热水直燃单双效复合型溴化锂吸收式冷水、冷热水机组,包括直燃型高压发生器(7)、蒸发器(22)、吸收器(1)、低压发生器、冷凝器(21)、溶液热交换器、溶液泵和冷剂泵(24),所述低压发生器包括热水发生器(15)和蒸汽发生器(17),热水换热管束(18)和蒸汽换热管束(19)设置在同一筒体(20)内,热水换热管束(18)和蒸汽换热管束(19)之间设置有分隔板(16);溶液热交换器包括高温热交换器(6)、低温热交换器(4)和单效溶液热交换器(5);溶液泵包括单效溶液泵(23)和双效溶液泵(25);单效溶液泵(23)和单效溶液热交换器(5)设置在吸收器(1)和热水发生器(15)之间的连接管路上,组成单效溶液循环流程系统。本实用新型机组能实现单效溶液循环量、双效溶液循环量与加热负荷之间的良好匹配。
The utility model relates to a hot water direct-fired single-double-effect compound lithium bromide absorption chiller and hot water unit, comprising a direct-fired high-voltage generator (7), an evaporator (22), an absorber (1), a low-pressure generator Condenser, condenser (21), solution heat exchanger, solution pump and refrigerant pump (24), described low pressure generator comprises hot water generator (15) and steam generator (17), hot water heat exchange tube bundle ( 18) and the steam heat exchange tube bundle (19) are arranged in the same cylinder (20), and a partition plate (16) is arranged between the hot water heat exchange tube bundle (18) and the steam heat exchange tube bundle (19); the solution heat exchange The device includes a high-temperature heat exchanger (6), a low-temperature heat exchanger (4) and a single-effect solution heat exchanger (5); the solution pump includes a single-effect solution pump (23) and a double-effect solution pump (25); the single-effect solution The pump (23) and the single-effect solution heat exchanger (5) are arranged on the connecting pipeline between the absorber (1) and the hot water generator (15), forming a single-effect solution circulation process system. The unit of the utility model can realize good matching between the single-effect solution circulation volume, the double-effect solution circulation volume and the heating load.
Description
(一)技术领域 (1) Technical field
本实用新型涉及一种溴化锂吸收式冷水、冷热水机组。属空调设备技术领域。The utility model relates to a lithium bromide absorption type cold water, cold and hot water unit. It belongs to the technical field of air conditioning equipment.
(二)背景技术 (2) Background technology
以往的直燃型溴化锂吸收式冷热水机组如图1所示,该机组由直燃型高压发生器7、蒸发器22、吸收器1、低压发生器27、冷凝器21、高温热交换器6、低温热交换器4、控制系统(图中未示出)及连接各部件的管路、阀所组成。直燃型溴化锂吸收式冷热水机组只能用直接燃烧燃料产生的热量驱动运行。The previous direct-fired lithium bromide absorption chiller and hot water unit is shown in Figure 1. The unit consists of a direct-fired high-
以往可同时或分别以热水(如太阳能热水、地热热水、各种生产工艺环节产生的废热水等)热量和直接燃烧燃料产生的热量驱动进行制冷运行、以直接燃烧燃料产生的热量驱动进行制热运行,用于提供空调用冷(热)水的热水直燃二用型溴化锂吸收式冷热水机组如图2所示,该机组的低压发生器37采用热水蒸汽复合型发生器结构,低温热交换器4与低压发生器之间的稀溶液联通管29上设有电动调节阀31,在高发进液管32上设有电磁阀31,使机组能同时或分别利用热水或直接燃烧燃料产生的热量驱动进行制冷运行。但这种机组存在下列不足之处:In the past, cooling operation could be driven by hot water (such as solar hot water, geothermal hot water, waste hot water generated in various production processes, etc.) and heat generated by direct combustion of fuel at the same time or separately, and heat generated by direct combustion of fuel Driven for heating operation, the hot water direct-fired dual-purpose lithium bromide absorption chiller and hot water unit used to provide cold (hot) water for air conditioning is shown in Figure 2. The low-pressure generator 37 of this unit is a hot water steam composite type Generator structure, the dilute solution communication pipe 29 between the low-
1、电动调节阀和电磁阀必须采用高气密性、高可靠性的阀门,给外购件选型带来难度(市场上可选用的阀门要么价格昂贵,要么性能不能满足要求);1. Electric control valves and solenoid valves must use high air-tightness and high reliability valves, which brings difficulties to the selection of purchased parts (the available valves on the market are either expensive or their performance cannot meet the requirements);
2、机组同时利用热水热量和直接燃烧燃料产生的热量驱动制冷运行时,溶液泵28的运行频率根据直燃高压发生器7的压力自动控制,同时还要对电动调节阀的开度进行调节控制,以减少进入低压发生器的稀溶液量,控制难度大,难以实现溶液循环量分配与加热量互补之间的良好匹配。2. When the unit uses the heat of hot water and the heat generated by direct combustion of fuel to drive cooling operation, the operating frequency of the solution pump 28 is automatically controlled according to the pressure of the direct combustion high-
(三)发明内容 (3) Contents of the invention
本实用新型的目的在于克服上述不足,提供一种使机组成为能同时或分别利用热水或直接燃烧燃料产生的热量驱动进行制冷运行、利用直接燃烧燃料产生的热量驱动进行供热运行的热水直燃单双效复合型溴化锂吸收式冷水、冷热水机组。The purpose of this utility model is to overcome the above disadvantages and provide a hot water unit that can simultaneously or separately use the heat generated by hot water or direct combustion fuel to drive for cooling operation, and use the heat generated by direct combustion fuel to drive for heating operation. Direct-fired single- and double-effect composite lithium bromide absorption chillers, cold and hot water units.
本实用新型的目的在是这样实现的:一种热水直燃单双效复合型溴化锂吸收式冷水、冷热水机组,包括直燃型高压发生器、蒸发器、吸收器、低压发生器、冷凝器、溶液热交换器、溶液泵、冷剂泵、及连接各部件的管路和阀,其特征在于:The purpose of this utility model is achieved in this way: a hot water direct-fired single-double-effect composite lithium bromide absorption chiller, hot and cold water unit, including a direct-fired high-pressure generator, evaporator, absorber, low-pressure generator, The condenser, the solution heat exchanger, the solution pump, the refrigerant pump, and the pipelines and valves connecting the components are characterized in that:
所述低压发生器包括热水发生器和蒸汽发生器,所述热水发生器的热水换热管束和蒸汽发生器的蒸汽换热管束设置在同一筒体内,热水换热管束和蒸汽换热管束之间设置有分隔板,The low pressure generator includes a hot water generator and a steam generator, the hot water heat exchange tube bundle of the hot water generator and the steam heat exchange tube bundle of the steam generator are arranged in the same cylinder, the hot water heat exchange tube bundle and the steam heat exchange tube bundle A partition plate is arranged between the heat pipe bundles,
所述溶液热交换器包括高温热交换器、低温热交换器和单效溶液热交换器,The solution heat exchanger includes a high-temperature heat exchanger, a low-temperature heat exchanger and a single-effect solution heat exchanger,
所述溶液泵包括单效溶液泵和双效溶液泵,The solution pump includes a single-effect solution pump and a double-effect solution pump,
所述单效溶液泵和单效溶液热交换器设置在吸收器和热水发生器之间的连接管路上,组成单效溶液循环流程系统;所述双效溶液泵、低温热交换器和高温热交换器设置在吸收器、直燃型高压发生器和蒸汽发生器之间的连接管路上,组成双效溶液循环流程系统,这样就形成了单双效复合型溶液循环流程系统,The single-effect solution pump and the single-effect solution heat exchanger are arranged on the connecting pipeline between the absorber and the hot water generator to form a single-effect solution circulation flow system; the double-effect solution pump, the low-temperature heat exchanger and the high-temperature The heat exchanger is set on the connecting pipeline between the absorber, the direct-fired high-pressure generator and the steam generator to form a double-effect solution circulation process system, thus forming a single-double-effect composite solution circulation process system,
本实用新型在以往的直燃型溴化锂吸收式冷热水基础上,通过增设单效溶液泵、单效溶液热交换器和热水发生器,组成单效溶液循环系统,使机组成为能同时或分别利用热水或直接燃烧燃料产生的热量驱动进行制冷运行、利用直接燃烧燃料产生的热量驱动进行供热运行的热水直燃单双效复合型溴化锂吸收式冷热水机组,克服了采用电动调节阀和电磁阀的不足之处。机组同时利用热水热量和直接燃烧燃料产生的热量驱动制冷运行时,易于进行溶液循环量分配与加热量互补之间的匹配控制。机组运行时,充分利用废热水或低廉热水的热能,只有当热水制冷量(供热量)不能满足空调需求时,才启动燃烧器进行补充加热。On the basis of the previous direct-fired lithium bromide absorption type hot and cold water, the utility model forms a single-effect solution circulation system by adding a single-effect solution pump, a single-effect solution heat exchanger and a hot water generator, so that the unit can simultaneously or The hot water direct-fired single-effect compound lithium bromide absorption chiller and hot water unit is driven by hot water or the heat generated by direct combustion of fuel for cooling operation, and the heat generated by direct combustion of fuel is used for heating operation. Disadvantages of regulating valves and solenoid valves. When the unit utilizes the heat of hot water and the heat generated by direct combustion of fuel to drive cooling operation, it is easy to perform matching control between the distribution of solution circulation and the complementary heating. When the unit is running, the thermal energy of waste hot water or low-cost hot water is fully utilized. Only when the cooling capacity (heat supply) of hot water cannot meet the demand of air conditioning, the burner is started for supplementary heating.
(四)附图说明 (4) Description of drawings
图1为以往的直燃型溴化锂吸收式冷热水机组示意图。Figure 1 is a schematic diagram of a conventional direct-fired lithium bromide absorption chiller.
图2为以往的热水直燃二用型溴化锂吸收式冷热水机组示意图。Fig. 2 is a schematic diagram of a conventional hot water direct-fired dual-purpose lithium bromide absorption chiller.
图3为本实用新型热水直燃单双效复合型溴化锂吸收式冷水、冷热水机组的一实施例示意图(冷却水流程采用并联流程)。Fig. 3 is a schematic diagram of an embodiment of the hot water direct combustion single-double-effect compound lithium bromide absorption chiller and hot water unit of the utility model (the cooling water flow adopts a parallel flow).
图4为本实用新型热水直燃单双效复合型溴化锂吸收式冷水、冷热水机组的另一实施例示意图(冷却水流程采用并联流程)。Fig. 4 is a schematic diagram of another embodiment of the utility model hot water direct-fired single-double-effect compound lithium bromide absorption chiller and hot water unit (the cooling water flow adopts a parallel flow).
图5为本实用新型用于单独制冷的热水直燃型溴化锂吸收式冷水机组。Fig. 5 is the hot water direct-fired lithium bromide absorption chiller used for independent refrigeration of the utility model.
图中附图标记:Reference signs in the figure:
吸收器1、吸收器进液管2、溶液切换阀3、低温热交换器4、单效溶液热交换器5、高温热交换器6、直燃型高压发生器7、高发出液管8、热水发生器进液管9、热水发生器出液管10、蒸汽发生器出液管11、冷剂蒸汽管12、蒸汽切换阀13、蒸汽发生器进液管14、热水发生器15、分隔板16、蒸汽发生器17、热水换热管束18、蒸汽换热管束19、筒体20、冷凝器21、蒸发器22、单效溶液泵23、冷剂泵24、双效溶液泵25、燃烧器26、低压发生器27、溶液泵28、稀溶液连通管29、低发出液管30、电磁阀31、高发进液管32、电动调节阀33、冷剂蒸汽管34、热水进口35、热水出口36、复合型低压发生器37、中间溶液布液管38、冷剂水出口管39。
(五)具体实施方式 (5) Specific implementation methods
本实用新型如图3所示机组,该机组是由直燃型高压发生器7、蒸发器22、吸收器1、热水发生器15、蒸汽发生器17、冷凝器21、高温热交换器6、低温热交换器4、单效溶液热交换器5、双效溶液泵25、单效溶液泵23、冷剂泵24、控制系统(图中未示出)及连接各部件的管路、阀所构成的热水直燃单双效复合型溴化锂吸收式冷热水机组。热水发生器15的热水换热管束18和蒸汽发生器17的蒸汽换热管束19以上下结构方式设置在同一筒体20内(热水发生器和蒸汽发生器均为低压发生器),两换热管束之间设置有分隔板16;单效溶液热交换器5的稀溶液出液管作为热水发生器进液管9接到热水发生器15顶部;热水发生器出液管10作为单效溶液热交换器的浓溶液进液管接到单效溶液热交换器5的浓溶液进液联箱上;高温热交换器6的中间溶液出液管作为蒸汽发生器进液管14接到蒸汽发生器17顶部;蒸汽发生器出液管11即为低温热交换器4的浓溶液进液管;单效溶液热交换器5和低温热交换器4的浓溶液出液管都接到吸收器进液管2上;在高发出液管8与吸收器1之间的管路上装有溶液切换阀3;在冷剂蒸汽管12与蒸发器22之间的管路上装有蒸汽切换阀13。The unit of the utility model is shown in Figure 3, and the unit is composed of a direct-fired high-
机组同时利用热水和燃烧燃料产生的热量制冷运行时,溶液切换阀和蒸汽切换阀关闭,由单效溶液泵从吸收器中输出的稀溶液经单效溶液热交换器换热升温后经热水发生器进液管进入热水发生器并被均匀分布在热水换热管束上,被来自外部装置(或系统)的热水加热浓缩成浓溶液后进入热水发生器底部,然后经热水发生器出液管进入单效溶液热交换器换热降温后经吸收器进液管进入吸收器,形成单效溶液循环流程。由双效溶液泵从吸收器中输出的稀溶液经低温热交换器、高温热交换器换热升温后进入直燃型高压发生器,被燃烧器26燃烧燃料产生的热量加热浓缩成中间溶液,中间溶液经高发出液管进入高温热交换器换热降温后,经蒸汽发生器进液管进入蒸汽发生器并被均匀分布在蒸汽换热管束上,被管内冷剂蒸汽(来自直燃型高压发生器)进一步加热浓缩成浓溶液,然后进入蒸汽发生器底部;进入蒸汽发生器底部的浓溶液经蒸汽发生器出液管进入低温热交换器换热降温后,经吸收器进液管进入吸收器,形成双效溶液循环流程。蒸汽换热管束内的冷剂蒸汽加热管外溶液放热后凝结成冷剂水(又称为高发冷剂水),然后进入冷凝器;热水换热管束及蒸汽换热管束的管外溶液被加热所产生的蒸汽进入冷凝器换热管束,被冷凝成冷剂水,该冷剂水与高发冷剂水一同进入蒸发器,被喷淋到蒸发器管外进行蒸发制冷,从而实现同时利用热水和直接燃烧燃料产生的热量来制冷。单效溶液泵的运行由机组的控制系统根据热水热量进行变频控制,以控制单效溶液循环量;双效溶液泵的运行由机组的控制系统根据直燃型高压发生器的压力进行变频控制,以控制双效溶液循环量,燃烧器的燃料燃烧量越大,高发压力越高,双效溶液泵的运行频率越高,双效溶液循环量越大,从而实现单效溶液循环量、双效溶液循环量与加热负荷之间的良好匹配,机组按单双效复合溶液循环流程运行。When the unit uses hot water and the heat generated by burning fuel for cooling operation at the same time, the solution switching valve and the steam switching valve are closed, and the dilute solution output from the absorber by the single-effect solution pump passes through the single-effect solution heat exchanger and then heats up. The liquid inlet pipe of the water generator enters the hot water generator and is evenly distributed on the hot water heat exchange tube bundle. It is heated by the hot water from an external device (or system) and concentrated into a concentrated solution, then enters the bottom of the hot water generator, and then passes through the hot water. The liquid outlet pipe of the water generator enters the single-effect solution heat exchanger for heat exchange and cooling, and then enters the absorber through the liquid inlet pipe of the absorber to form a single-effect solution circulation process. The dilute solution output from the absorber by the double-effect solution pump passes through the low-temperature heat exchanger and the high-temperature heat exchanger, and then enters the direct-fired high-pressure generator, and is heated and concentrated by the heat generated by the
机组单独利用热水热量制冷运行时,溶液切换阀、蒸汽切换阀关闭,燃烧器和双效溶液泵停转,低温热交换器、高温热交换器、直燃型高压发生器和蒸汽发生器不工作,机组按单效溶液循环流程运行。When the unit uses hot water heat for cooling operation alone, the solution switching valve and steam switching valve are closed, the burner and double-effect solution pump stop, and the low-temperature heat exchanger, high-temperature heat exchanger, direct-fired high-pressure generator and steam generator do not operate. Working, the unit operates according to the single-effect solution circulation process.
机组单独利用燃烧燃料产生的热量制冷运行时,溶液切换阀、蒸汽切换阀关闭,热水发生器换热管内无热水流通,单效溶液泵停转,单效溶液热交换器和热水发生器不工作,机组按双效溶液循环流程运行。When the unit uses the heat generated by burning fuel for cooling operation, the solution switching valve and steam switching valve are closed, there is no hot water circulation in the heat exchange tube of the hot water generator, the single-effect solution pump stops, and the single-effect solution heat exchanger and hot water generate If the device does not work, the unit operates according to the double-effect solution circulation process.
机组供热运行时,溶液切换阀、蒸汽切换阀开启,热水发生器管内无热水流通(外部热源热水直接送入空调系统供热,或送入热交换器换热后提供空调热水),单效溶液泵停转。When the unit is running for heating, the solution switching valve and the steam switching valve are opened, and there is no hot water circulation in the hot water generator pipe (hot water from an external heat source is directly sent to the air conditioning system for heating, or sent to the heat exchanger to provide hot water for air conditioning ), the single-effect solution pump stops.
燃烧器的燃料燃烧量由机组的控制系统根据空调负荷所需加热量自动调节控制,当热源热水为废热水或低廉热水时,机组充分利用废热水或低廉热水的热能,只有当热水制冷量(供热量)不能满足空调需求时,才启动燃烧器进行补充加热。The fuel combustion volume of the burner is automatically adjusted and controlled by the control system of the unit according to the heating capacity required by the air-conditioning load. When the heat source hot water is waste hot water or low-cost hot water, the unit makes full use of the heat energy of waste hot water or low-cost hot water, only When the cooling capacity (heat supply) of hot water cannot meet the demand of air conditioning, the burner is started for supplementary heating.
机组的冷却水流程可是并联流程(如图3所示),也可是串联流程(如图4所示)。The cooling water process of the unit can be a parallel process (as shown in Figure 3) or a series process (as shown in Figure 4).
取消图3、图4机组中的溶液切换阀、蒸汽切换阀及其连接管,机组即成为用于单独制冷的热水直燃型溴化锂吸收式冷水机组(如图5所示)。Cancel the solution switching valve, steam switching valve and connecting pipes in the unit shown in Figure 3 and Figure 4, and the unit becomes a hot water direct-fired lithium bromide absorption chiller for separate refrigeration (as shown in Figure 5).
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200379760U CN201340135Y (en) | 2009-01-08 | 2009-01-08 | Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009200379760U CN201340135Y (en) | 2009-01-08 | 2009-01-08 | Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201340135Y true CN201340135Y (en) | 2009-11-04 |
Family
ID=41235679
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2009200379760U Expired - Lifetime CN201340135Y (en) | 2009-01-08 | 2009-01-08 | Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201340135Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103868131A (en) * | 2014-03-01 | 2014-06-18 | 双良节能系统股份有限公司 | After-burning lithium bromide absorption type heat exchange system |
| CN105953459A (en) * | 2016-06-22 | 2016-09-21 | 烟台荏原空调设备有限公司 | Single and double effect compound type absorption refrigerating unit |
| CN110173925A (en) * | 2019-06-24 | 2019-08-27 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorption type cold water unit with single-action heat pump heat-production functions |
-
2009
- 2009-01-08 CN CNU2009200379760U patent/CN201340135Y/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103868131A (en) * | 2014-03-01 | 2014-06-18 | 双良节能系统股份有限公司 | After-burning lithium bromide absorption type heat exchange system |
| CN103868131B (en) * | 2014-03-01 | 2016-08-17 | 双良节能系统股份有限公司 | Fuel supplementing type suction-type lithium bromide heat-exchange system |
| CN105953459A (en) * | 2016-06-22 | 2016-09-21 | 烟台荏原空调设备有限公司 | Single and double effect compound type absorption refrigerating unit |
| CN110173925A (en) * | 2019-06-24 | 2019-08-27 | 双良节能系统股份有限公司 | Direct-fired lithium bromide absorption type cold water unit with single-action heat pump heat-production functions |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103983042B (en) | The indoor cold-hot integrated system of a kind of solar energy | |
| CN102914079A (en) | Two-stage type hot water direct-fired single-double effect composite lithium bromide absorption refrigeration unit | |
| CN102116539B (en) | Adsorption and compression composite heat pump system driven by multiple heat sources | |
| CN102914080A (en) | Two-stage single-effect and double-effect lithium bromide absorption refrigerating unit with smoke and hot water afterburning | |
| CN101876496B (en) | Double-evaporator direct-fired absorption refrigerating and heating unit | |
| CN110173927B (en) | Direct-fired lithium bromide absorption refrigerator with single-effect heat pump heating function | |
| CN102914081A (en) | Two-section flue gas hot-water single/double-effect composite lithium bromide absorption type refrigerating unit | |
| CN101526282B (en) | Hot-water direct-fired single-double effect compound type lithium bromide absorption type cold water and cold-hot water unit | |
| CN101526283B (en) | Fume hot-water single-double effect compound type lithium bromide absorption type cold water and cold-hot water unit | |
| CN201340135Y (en) | Hot water direct combustion single/double effect composite type lithium bromide absorption cold water/hot and cold water set | |
| CN109269143B (en) | Novel absorption heat pump and application method thereof | |
| CN102997481A (en) | Hot water direct-fired single-double effect composite type lithium bromide absorption refrigerating unit | |
| CN202915597U (en) | Two-section flue gas hot-water single-effect and double-effect composite lithium bromide absorption type refrigerating unit | |
| CN202973646U (en) | Flue gas hot water afterburning single/double-effect composite lithium bromide absorption refrigerating unit | |
| CN110173926B (en) | Double-generator direct-fired lithium bromide absorption heat pump unit with double-effect refrigeration function | |
| CN110307665B (en) | Direct-fired lithium bromide absorption type cold water and heat pump unit | |
| CN103512271B (en) | Direct-fired three-purpose-type lithium bromide absorption-type cold and hot water unit with flue gas heat exchanger | |
| CN202915598U (en) | Two-stage smoke and hot water afterburning single-effect and double-effect composite lithium bromide absorption refrigerating unit | |
| CN103123181A (en) | Single-effect and double-effect compound-type lithium bromide absorption refrigerating device with smoke and hot water afterburning | |
| CN201340137Y (en) | Double high pressure generator direct combustion type lithium bromide absorption cold water/hot and cold water set | |
| CN201340136Y (en) | Smoke hot water single/double effect composite type lithium bromide absorption cold water/hot and cold water set | |
| CN211177497U (en) | Double-generator direct-combustion lithium bromide absorption heat pump unit with double-effect refrigeration function | |
| CN202973645U (en) | Hot water direct combustion single-effect and double-effect combined type lithium bromide absorption type refrigerating set | |
| CN2826307Y (en) | Hot water direct combustion dual-purpose type lithium bromide absorption type water chilling, water chilling/heating unit | |
| CN203501546U (en) | Direct-fired triple-purpose lithium bromide absorption cold and hot water set with dual-energy-saving device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20091104 Effective date of abandoning: 20090108 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20091104 Effective date of abandoning: 20090108 |