WO2011095123A1 - 一种梯次利用冷凝冷却热量的集中供热系统 - Google Patents

一种梯次利用冷凝冷却热量的集中供热系统 Download PDF

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Publication number
WO2011095123A1
WO2011095123A1 PCT/CN2011/070801 CN2011070801W WO2011095123A1 WO 2011095123 A1 WO2011095123 A1 WO 2011095123A1 CN 2011070801 W CN2011070801 W CN 2011070801W WO 2011095123 A1 WO2011095123 A1 WO 2011095123A1
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heat
cooling
circulating water
heating system
line
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PCT/CN2011/070801
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English (en)
French (fr)
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陈连祥
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Chen Lianxiang
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D12/00Other central heating systems
    • F24D12/02Other central heating systems having more than one heat source
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/16Waste heat
    • F24D2200/18Flue gas recuperation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24DDOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D2200/00Heat sources or energy sources
    • F24D2200/16Waste heat
    • F24D2200/24Refrigeration
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]

Definitions

  • the present invention relates to a centralized heating system utilizing petrochemicals and low-temperature heat discarded by enterprises with condensation and cooling heat. Specifically, it is a centralized heating system that uses condensation to cool heat. Background technique
  • the object of the present invention is to provide a centralized heating system that utilizes condensing and cooling heat in a stepwise manner, which is a condensing and cooling system that is inevitably produced in a production process by a petrochemical company and cannot be directly utilized by an enterprise.
  • the heat replaces the heat produced by other heating methods, realizes the huge environment of "heat and enterprise joint production", benefits the human beings, thereby saving energy, lowering the cost, protecting the environment, and generating enormous economic and social benefits.
  • a ladder using a condensing and cooling heat central heating system comprising: a higher temperature cooling circulating water inflow line, a standard cooling circulating water return line, the higher temperature Cooling circulating water line and reaching the standard cooling circulating water return line
  • the front replacement heat device, the reheat device, the heat utilization device, and the recooling device are sequentially connected.
  • the secondary heat utilization device and the low temperature heat compensation device are sequentially connected from the heat utilization device to the front heat replacement device, and the low temperature heat compensation device is respectively connected to the cooling circulating water inlet pipeline and the cooling circulating water return pipeline. .
  • the front heat exchanger is a heat exchanger at the beginning of the water line of the higher temperature cooling circulating water.
  • the reheating device is a peaking heat source.
  • the invention adopts a condensing and cooling heat centralized heating system for the ladder, so that the condensing cooling heat of the higher temperature in the production process can be partially or completely reused, the condensation and cooling load required by the process are replaced by the former heat device, and the heat is utilized.
  • the device, the recooling device is co-cooled to process requirements. It not only reduces the process cooling load, reduces thermal pollution, reduces the consumption of resources such as water resources, electric energy, and chemicals, but also saves energy consumption of the heat utilization device.
  • the system can also provide the refrigeration device with the driving heat source required for the refrigerator. It realizes the huge environment of "heat-management joint production" for the benefit of centuries, thus saving energy, lowering costs, protecting the environment, and generating huge economic and social benefits.
  • Figure 1 is a schematic view of the structure of the present invention.
  • Ty is the return water temperature required for the cooling process
  • T h when the process requires temperature Ty, corresponds to the heating return water temperature.
  • a step-by-step condensing and cooling heat centralized heating system includes: a higher temperature cooling circulating water incoming water pipeline 1, a cooling circulating water incoming water main pipeline or a cooling device, and a standard cooling circulating water return water pipeline device 13.
  • the higher temperature cooling circulating water inflow water line 1 is connected to the pre-displacement heat device 5, and the front replacement heat device 5 is passed through the heating hot water line 3 to the reheating device 8, and the outlet of the reheating device 8 is connected to the heat utilization.
  • the device 6 and the heat utilization device 6 are sequentially connected to the secondary heat utilization device 9 and the low temperature thermal compensation device 10 by the heating and returning water pipeline 4, and the low temperature thermal compensation device 10 respectively communicates with the cooling circulating water inlet pipeline 11 and the cooling circulating water returning pipeline. 12; the low temperature thermal compensation device 10 returns to the front replacement heat device 5, the front replacement heat device 5 passes the higher temperature cooling circulating water return water line 2 to the recooling device 7, and the recooling device 7 to the standard cooling circulating water return water line device 13.
  • the front heat exchanger 5 can also be used to heat the circulating water from the higher temperature to the heat exchanger at the beginning of the water line 1.
  • the recooling device 7 may also be an original cooling device or a cooling circulating water summary line and its secondary line.
  • the heat source of the reheating device is provided by an air cooler or an oil gas cooler or a water cooler, a heat pipe, a heat pump, a boiler, etc.; in the existing higher temperature cooling circulating water decooling device or cooling circulating water to water summary A peaking heat source can also be used.
  • the front replacement heat device 5 is composed of a heat exchanger valve pump control device and a pipeline.
  • the heat utilization device 6 is composed of a heat exchanger valve pump control device, and is composed of a hot device and a pipeline.
  • the recooling device 7 is composed of a cooling device, a heat exchange device, a valve pump, a control device, and a pipeline.
  • the recooling device can be newly built or retrofitted using the original cooling system device.
  • the reheating device 8 is composed of a condensing, cooling device, a control device, a valve, a pump, and a pipeline.
  • the secondary heat utilization device 9 is composed of a heat exchanger, using heat equipment, valves, pumps and pipelines.
  • the low temperature thermal compensation device 10 is composed of a heat exchanger, a control device, a valve, a pump and a pipeline.
  • a pre-displacement heat device 5, a heat supply water supply line 3, a reheating device 8, and a heat utilization device are installed between the higher temperature cooling circulating water inflow line 1 and the standard cooling circulating water return line device 13. 6.
  • the higher temperature cooling circulating water that needs to be cooled passes through the higher temperature cooling circulating water to release the relatively high cooling heat between the water line 1 and the front heat replacing device 5, and the higher temperature cooling cycle on the side of the front heat replacing device 5
  • the water return line 2 to the recooling device 7 continue to release heat, and after reaching the required cooling temperature Ty of the process, the cooling water return line device 13 on the side of the recooling device 7 is returned to the process device to complete the cooling cycle.
  • the recooling device 7 can be realized by utilizing a modified original cooling system.
  • the water from the front heat exchanger 5 is further heated by the heating water supply line 3 to the reheating device 8, and then the heat is released through the heating water supply line 3 to the heat utilization device 6, and the heat is cooled after the cooling.
  • the return water passes through the heating and returning water line 4 to the front heat replacing device 5 to complete the cycle of heat extraction and discharge.
  • the heat utilization device 6 and the heating and returning water pipeline 4 are connected in series with the secondary heat utilization device 9 and the low temperature compensation device 10, and the circulation process is from the heat utilization device 6 to supply heat back to the water through the heating and return water pipeline. 4 to the secondary heat utilization device 9 further reduces the temperature level, to provide a heat source for the thermal energy device, and the cooled heat supply back to the low temperature thermal compensation device 10, the low temperature thermal compensation device 10 It cools the circulating water to heat the heat source to the temperature of T h , and then completes the thermal cycle through the heating return line 4 to the former heat exchanger 5.
  • the secondary heat utilization device 9 can provide a low temperature heat source for low temperature thermal energy equipment such as aquaculture and water source heat pumps.
  • the main purpose of the low temperature thermal compensation device 10 is that the temperature of the heat supply back from the secondary heat utilization device 9 is very low (possibly as low as 0 ° C), which is lower than the temperature requirement T y of the process cooling, in order to ensure the process requirements. , using other heat sources through the low temperature thermal compensation device 10 to heat the heating back to T h
  • the ladder uses the condensation and cooling heat centralized heating system to make the condensation heat of the higher temperature in the production process partially or completely reused, and the condensation and cooling load required by the process are replaced by the former heat exchanger.
  • the heat utilization device and the recooling device are jointly cooled to the process requirements. It not only reduces the process cooling load, reduces thermal pollution, reduces the resource consumption of water resources, electric energy, chemicals, etc., but also saves the energy consumption of the heat utilization device.
  • the system can also provide the cooling heat source required by the refrigerator for the refrigeration equipment if there is a cooling demand on the side of the heat utilization device. It realizes the huge environment of "heat-management joint production" for the benefit of centuries, thus saving energy, lowering costs, protecting the environment, and generating huge economic and social benefits.

Description

说 明 书 一种梯次利用冷凝冷却热量的集中供热系统 技术领域
本发明涉及一种利用石油化工及具有冷凝、 冷却热量企业废弃的低温 热量的集中供热系统。 具体是一种梯次利用冷凝冷却热量的集中供热系统。 背景技术
目前, 石油化工等企业生产过程中, 产生许多冷凝、 冷却热量在生产 生活中可直接利用的温位却排放到环境中, 造成环境污染, 同时还浪费了 大量水、 电、 药剂等资源。 在其周边的热量用户却在利用常规的加热方式 生产品质相同的热能, 如何合理的利用冷凝、 冷却热量, 置换其它加热方 式生产的热量, 实现 "热企联产"一定会产生巨大的环境, 经济效益, 造 福人类, 成为人类的期望。
发明内容 本发明目的在于: 为了克服上述的不足, 提供一种梯次利用冷凝冷却 热量的集中供热系统,它是利用石油化工等企业,生产过程中必然产生而 企业却无法直接利用的冷凝、 冷却热量置换其它加热方式生产的热量, 实 现 "热企联产" 巨大的环境, 造福人类, 从而, 节约能源, 降底成本, 保 护环境, 产生巨大的经济效益和社会效益。
本发明的目的是通过这样的技术方案实现的: 一种梯次利用冷凝、 冷 却热量集中供热系统, 包括: 较高温冷却循环水来水管线、 达标冷却循环 水回水管线, 所述的较高温冷却循环水管线与达标冷却循环水回水管线之 间, 依次连通前置换热装置、 再热装置、 热量利用装置、 再冷装置。
所述的从热量利用装置至前置换热装置之间依次连通次级热量利用装 置和低温热补偿装置, 所述的低温热补偿装置分别连通冷却循环水进水管 线、 冷却循环水回水管线。
所述的前置换热装置为较高温冷却循环水来水管线始端的换热器。 所述的再热装置为调峰热源。
本发明一种梯次利用冷凝、 冷却热量集中供热系统, 使生产工艺中较 高温度的冷凝冷却热量能部份或全部再次利用, 工艺要求的冷凝、 冷却负 荷由前置换热装置, 热量利用装置, 再冷却装置共同冷却至工艺要求。 既 降低了工艺冷却负荷, 减少热污染, 降低水资源、 电能、 药剂等资源消耗, 又节约了热利用装置能源消耗。 在热量利用装置侧如有制冷需求时, 本系 统还可以为制冷设备提供制冷机所需驱动热源。 它实现了 "热企联产" 巨 大的环境, 造福人类, 从而, 节约能源, 降底成本, 保护环境, 产生巨大 的经济效益和社会效益。
附图说明
图 1是本发明结构示意图。
编号说明:
1、 较高温冷却循环水来水管线 2、 较高温冷却循环水回水管线,
3、 供热热水 4、 供热回水
7、 再冷装置
Figure imgf000004_0001
10、 低温热补偿装置
11、 冷却循环水进水 12、 冷却循环水回水 13、 达标冷却循环水回水管线装置
Ty、 是冷却工艺要求的回水温度,
Th、 是工艺要求温度 Ty时, 对应供热回水温度。
具体实施方式
实施例
一种梯次利用冷凝、冷却热量集中供热系统, 如图 1所示, 包括: 较高 温冷却循环水来水管线 1、冷却循环水来水总管线或冷却装置、达标冷却循 环水回水管线装置 13, 所述的较高温冷却循环水来水管线 1连通前置换热 装置 5, 前置换热装置 5通过供热热水管线 3至再热装置 8, 再热装置 8的 出口连通热量利用装置 6,热量利用装置 6由供热回水管线 4依次连通次级 热量利用装置 9、 低温热补偿装置 10, 低温热补偿装置 10分别连通冷却循 环水进水管线 11、 冷却循环水回水管线 12; 低温热补偿装置 10返回前置 换热装置 5,前置换热装置 5通过较高温冷却循环水回水管线 2至再冷装置 7, 再冷装置 7至达标冷却循环水回水管线装置 13。
所述的前置换热装置 5也可以采用较高温冷却循环水来水管线 1始端 的换热器。
所述的再冷装置 7 也可以为原有冷却装置或冷却循环水汇总管线及其 次级管线。
所述的再热装置的热源是由空冷器或油气冷却器或水冷器、 热管、 热 泵、 锅炉等装置提供;在现有的较高温度的冷却循环水去冷却装置或冷却循 环水来水汇总也可以采用调峰热源。
所述的前置换热装置 5由换热器阀泵控制设备, 管道组成装置。 所述的热量利用装置 6 由换热器阀泵控制设备, 用热的设备及管线组 成。
所述的再冷装置 7 由冷却设备、 换热设备、 阀泵、 控制设备及管线构 成。 再冷装置可以新建或改造利用原冷却系统装置。
所述的再热装置 8由冷凝、 冷却设备、 控制设备、 阀、 泵及管线组成。 所述的次级热量利用装置 9由换热器, 用热设备、 阀、 泵及管线组成。 所述的低温热补偿装置 10由换热器、 控制设备, 阀、 泵及管线组成。 本供热系统, 在较高温冷却循环水来水管线 1 与达标冷却循环水回水 管线装置 13间加装了前置换热装置 5, 供热供水管线 3, 再热装置 8, 热量 利用装置 6, 再冷装置 7, 供热回水管线 4。 这样, 需要冷却的较高温冷却 循环水经过较高温冷却循环水来水管线 1至前置换热装置 5之间要释放相 对高位的冷却热量, 经前置换热装置 5 侧的较高温冷却循环水回水管线 2 至再冷装置 7继续释放热量, 达到工艺要求的冷却温位 Ty后, 经再冷装置 7侧的达标冷却循环水回水管线装置 13回至工艺装置完成冷却循环。 再冷 装置 7可通过利用改造原冷却系统实现。
所述的前置换热装置 5出来的水由供热供水经管线 3至再热装置 8进 一步的提升温位, 然后经供热供水管线 3至热量利用装置 6释放热量, 降 温后的供热回水经供热回水管线 4至前置换热装置 5完成取放热能的循环。
所述的热量利用装置 6与供热回水管线 4间串接次级热量利用装置 9 和低温补偿装置 10, 这样的循环流程是从热量利用装置 6出来供热回水经 供热回水管线 4至次级热量利用装置 9进一步降低温位, 为用热能设备提 供热源, 降温后的供热回水至低温热补偿装置 10, 低温热补偿装置 10以其 它冷却循环水为热源换热加热至 Th温位, 然后, 经供热回水管线 4至前置 换热装置 5完成用热循环过程。 在此工况下, 从前置换热装置 5出来的冷 却循环水回水已冷至工艺要求温位 Ty, 不再进入再冷装置 7, 而是直接旁 路至达标冷却循环水回水管线装置 13回用。 所述的次级热量利用装置 9可 为养殖种植及水源热泵等低温用热能设备提供低温热源。
低温热补偿装置 10的主要目的是, 从次级热量利用装置 9出来的供热 回水温度很低 (可能低至 0°C),低于工艺冷却要求温位 Ty时, 为保证工艺要 求, 通过低温热补偿装置 10利用其它需热源使供热回水升温至 Th
在实施过程中, 也可能将前置换热装置 5 中供回水管线与较高温位冷 却循环水起始端的换热器直接串接, 以换取更高温度的热量。
实验证明: 本发明一种梯次利用冷凝、冷却热量集中供热系统, 使生产 工艺中较高温度的冷凝冷却热量能部份或全部再次利用, 工艺要求的冷凝、 冷却负荷由前置换热装置, 热量利用装置, 再冷却装置共同冷却至工艺要 求。 既降低了工艺冷却负荷, 减少热污染, 降低水资源、 电能、 药剂等资 源消耗, 又节约了热利用装置能源消耗。 在热量利用装置侧如有制冷需求 时, 本系统还可以为制冷设备提供制冷机所需驱动热源。 它实现了 "热企 联产" 巨大的环境, 造福人类, 从而, 节约能源, 降底成本, 保护环境, 产生巨大的经济效益和社会效益。

Claims

权 利 要 求 书
1、 一种梯次利用冷凝冷却热量的集中供热系统, 包括: 较高温冷却循 环水来水管线 (1 )、 达标冷却循环水回水管线(13), 其特征在于: 所述的 较高温冷却循环水管线 (1 ) 与达标冷却循环水回水管线(13)之间, 依次连 通前置换热装置 (5)、 再热装置 (8)、 热量利用装置 (6)、 再冷装置 (7)。
2、根据权利要求 1所述的一种梯次利用冷凝冷却热量的集中供热系统, 其特征在于: 所述的从热量利用装置 (6 ) 至前置换热装置 (5 ) 之间依次 连通次级热量利用装置 (9) 和低温热补偿装置 (10 ) , 所述的低温热补偿 装置(10)分别连通冷却循环水进水管线(11 )、冷却循环水回水管线(12)。
3、根据权利要求 2所述的一种梯次利用冷凝冷却热量的集中供热系统, 其特征在于: 所述的前置换热装置 (5) 为较高温冷却循环水来水管线 (1 ) 始端的换热器。
4、根据权利要求 1所述的一种梯次利用冷凝冷却热量的集中供热系统, 所述的再热装置 (5) 为调峰热源。
PCT/CN2011/070801 2010-02-04 2011-01-30 一种梯次利用冷凝冷却热量的集中供热系统 WO2011095123A1 (zh)

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