CN104075585A - Hydrogen chloride synthesis thermal energy comprehensive utilization device and method - Google Patents
Hydrogen chloride synthesis thermal energy comprehensive utilization device and method Download PDFInfo
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- CN104075585A CN104075585A CN201410348143.1A CN201410348143A CN104075585A CN 104075585 A CN104075585 A CN 104075585A CN 201410348143 A CN201410348143 A CN 201410348143A CN 104075585 A CN104075585 A CN 104075585A
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- lithium bromide
- tube connector
- hydrogen chloride
- heat
- hot
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- 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
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
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- 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
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to the field of ionic membrane caustic soda production, particularly to a hydrogen chloride synthesis thermal energy comprehensive utilization device and method. The hydrogen chloride synthesis thermal energy comprehensive utilization device comprises a caustic soda synthetic furnace, a lithium bromide hot water tank, a hot water pump and a polymerization heat exchanger, wherein the caustic soda synthetic furnace is connected with a venturi heater through a first connecting pipe; the venturi heater is connected with the lithium bromide hot water tank through a third connecting pipe; the lithium bromide hot water tank is connected with the hot water pump through a fourth connecting pipe; the hot water pump is connected with the inlet of the venturi heater and a lithium bromide refrigerating unit through a sixth connecting pipe and a seventh connecting pipe respectively; the lithium bromide hot water tank is connected with the lithium bromide refrigerating unit through a fifth connecting pipe; the lithium bromide refrigerating unit is connected with a piece of cold equipment through an eighth connecting pipe. The hydrogen chloride synthesis thermal energy comprehensive utilization device and method can recycle the thermal energy and ensure steady operation of the hydrogen chloride synthesis.
Description
Technical field
the present invention relates to ion film caustic soda production field, particularly the synthetic heat energy comprehensive utilization device of a kind of hydrogen chloride and method.
Background technology
along with the development of caustic soda technology, traditional hot-water type synthetic furnace thermal waste phenomenon is serious, adopts middle pressure steam synthetic furnace, utilize venturi heating, make heat energy effectively pass to lithium bromide unit, utilize its Conversion of Energy function, cold water is provided, recycles for cool equipment.
Summary of the invention
patent of the present invention is intended to solve the serious problem of traditional hot-water type synthetic furnace thermal waste in above-mentioned caustic soda production, and the synthetic heat energy comprehensive utilization device of a kind of hydrogen chloride is provided and utilizes method.
the technical scheme that the present invention solves described problem employing is:
the synthetic heat energy comprehensive utilization device of a kind of hydrogen chloride, comprises caustic soda synthetic furnace, lithium bromide hot-water cylinder, heat-exchanger pump, lithium bromide hot-water cylinder, polymerization heat exchanger; Caustic soda synthetic furnace is connected with venturi heater by the first tube connector, venturi heater is connected with lithium bromide hot-water cylinder by the 3rd tube connector, lithium bromide hot-water cylinder is connected with heat-exchanger pump by the 4th tube connector, heat-exchanger pump is connected with lithium bromide refrigerating unit with the entrance of venturi heater with the 7th tube connector by the 6th tube connector respectively, lithium bromide hot-water cylinder is connected with lithium bromide refrigerating unit by the 5th tube connector, lithium bromide refrigerating unit by the 8th tube connector be connected with cool equipment.
technique scheme can be recycled heat energy, can ensure again the synthetic synthesizing stable operation of hydrogen chloride.
the synthetic utilization method of heat of a kind of hydrogen chloride, the steam that caustic soda synthetic furnace produces is by venturi heater spray heating lithium bromide unit circulation hot-water system, lithium bromide hot water circuit enters lithium bromide unit, used heat conducts to lithium bromide unit, be converted into cold water through lithium bromide unit, recycle for cool equipment, unnecessary heat is for polymeric plate heat exchanger.
preferred version of the present invention is:
pass through the 11 tube connector with cool equipment and be connected with cold water tank, cold water tank is connected with water supply pump by the tenth tube connector, and water supply pump is connected with lithium bromide refrigerating unit by the 9th tube connector.
the first tube connector is connected with polymerization heat exchanger by the second tube connector.
Brief description of the drawings
fig. 1 is structural representation of the present invention.
Detailed description of the invention
the synthetic heat energy comprehensive utilization device of a kind of hydrogen chloride, referring to accompanying drawing 1, in figure: caustic soda synthetic furnace 1, the first tube connector 2, the second tube connector 3, polymerization heat exchanger 4, venturi heater 5, the three tube connectors 6, lithium bromide hot-water cylinder 7, the four tube connectors 8, heat-exchanger pump 9, the six tube connectors 10, the 7th tube connector 11, the five tube connectors 12, lithium bromide refrigerating unit 13, the eight tube connectors 14, with cool equipment 15, the 11 tube connectors 16, cold water tank 17, the tenth tube connector 18, water supply pump 19, the nine tube connectors 20.
caustic soda synthetic furnace 1 is connected with venturi heater 5 by the first tube connector 2, venturi heater 5 is connected with lithium bromide hot-water cylinder 7 by the 3rd tube connector 6, lithium bromide hot-water cylinder 7 is connected with heat-exchanger pump 9 by the 4th tube connector 8, hot water 9 pumps are connected with lithium bromide refrigerating unit 13 with the entrance of venturi heater 5 with the 7th tube connector 11 by the 6th tube connector 10 respectively, lithium bromide hot-water cylinder 7 is connected with lithium bromide refrigerating unit 13 by the 5th tube connector 12, lithium bromide refrigerating unit 13 by the 8th tube connector 14 be connected with cool equipment 15.
pass through the 11 tube connector 16 with cool equipment 15 and be connected with cold water tank 17, cold water tank 17 is connected with water supply pump 19 by the tenth tube connector 18, and water supply pump 19 is connected with lithium bromide refrigerating unit 13 by the 9th tube connector 20.
the first tube connector 2 is connected with polymerization heat exchanger 4 by the second tube connector 3.
the steam that caustic soda synthetic furnace 1 produces sprays heating lithium bromide unit circulation hot-water system by venturi heater 5, lithium bromide hot water circuit enters lithium bromide unit 13, used heat conducts to lithium bromide unit, be converted into cold water through lithium bromide unit, recycle for cool equipment 15, unnecessary heat is for polymeric plate heat exchanger 4.
this technology solves the serious problem of traditional hot-water type synthetic furnace thermal waste in caustic soda production, and provides one can recycle heat energy, can ensure again the device of hydrogen chloride synthesizing stable operation.
Claims (4)
1. the synthetic heat energy comprehensive utilization device of hydrogen chloride, comprises caustic soda synthetic furnace, lithium bromide hot-water cylinder, heat-exchanger pump, lithium bromide hot-water cylinder, polymerization heat exchanger; It is characterized in that: caustic soda synthetic furnace is connected with venturi heater by the first tube connector, venturi heater is connected with lithium bromide hot-water cylinder by the 3rd tube connector, lithium bromide hot-water cylinder is connected with heat-exchanger pump by the 4th tube connector, heat-exchanger pump is connected with lithium bromide refrigerating unit with the entrance of venturi heater with the 7th tube connector by the 6th tube connector respectively, lithium bromide hot-water cylinder is connected with lithium bromide refrigerating unit by the 5th tube connector, lithium bromide refrigerating unit by the 8th tube connector be connected with cool equipment.
2. want 1 to ask the described synthetic heat energy comprehensive utilization device of hydrogen chloride according to right, it is characterized in that: pass through the 11 tube connector with cool equipment and be connected with cold water tank, cold water tank is connected with water supply pump by the tenth tube connector, and water supply pump is connected with lithium bromide refrigerating unit by the 9th tube connector.
3. the synthetic heat energy comprehensive utilization device of hydrogen chloride according to claim 1, is characterized in that: the first tube connector is connected with polymerization heat exchanger by the second tube connector.
4. the synthetic utilization method of heat of hydrogen chloride as claimed in claim 1, it is characterized in that: the steam that caustic soda synthetic furnace produces is by venturi heater spray heating lithium bromide unit circulation hot-water system, lithium bromide hot water circuit enters lithium bromide unit, used heat conducts to lithium bromide unit, be converted into cold water through lithium bromide unit, recycle for cool equipment, unnecessary heat is for polymeric plate heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410348143.1A CN104075585A (en) | 2014-07-22 | 2014-07-22 | Hydrogen chloride synthesis thermal energy comprehensive utilization device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410348143.1A CN104075585A (en) | 2014-07-22 | 2014-07-22 | Hydrogen chloride synthesis thermal energy comprehensive utilization device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104075585A true CN104075585A (en) | 2014-10-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410348143.1A Pending CN104075585A (en) | 2014-07-22 | 2014-07-22 | Hydrogen chloride synthesis thermal energy comprehensive utilization device and method |
Country Status (1)
| Country | Link |
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| CN (1) | CN104075585A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114072622A (en) * | 2019-07-10 | 2022-02-18 | 睿特维亚有限公司 | Bernoulli heat pump with laminar flow refrigerant |
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| JPH1019375A (en) * | 1996-07-05 | 1998-01-23 | Matsushita Electric Ind Co Ltd | Heat pump type bath hot water heating system |
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| CN1865813A (en) * | 2006-05-10 | 2006-11-22 | 江苏双良空调设备股份有限公司 | Second lithium bromide absorption type heat pump for preparing steam by using vertical double-side falling-film absorber |
| CN201281489Y (en) * | 2008-09-28 | 2009-07-29 | 江苏双良空调设备股份有限公司 | Thermal water vapor concurrent heating type lithium bromide absorption type water chilling unit |
| CN201795634U (en) * | 2010-07-29 | 2011-04-13 | 青岛瑞德新能源工程技术有限公司 | Waste heat recovery energy saving apparatus for cooling |
| CN202007132U (en) * | 2011-04-26 | 2011-10-12 | 安徽中企能源管理有限公司 | Hydrogen chlorine synthesizing afterheat utilizing device |
| CN202598942U (en) * | 2012-05-05 | 2012-12-12 | 四川科伦药业股份有限公司 | Lithium bromide refrigerating unit for steam condensate waste heat recovery system |
| CN203240835U (en) * | 2013-04-27 | 2013-10-16 | 上海东智屏科贸有限公司 | Device for recycling waste heat of hydrochloric acid furnace |
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2014
- 2014-07-22 CN CN201410348143.1A patent/CN104075585A/en active Pending
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| JPH1019375A (en) * | 1996-07-05 | 1998-01-23 | Matsushita Electric Ind Co Ltd | Heat pump type bath hot water heating system |
| JP2003035454A (en) * | 2001-07-23 | 2003-02-07 | Matsushita Electric Ind Co Ltd | Heat pump hot water supply apparatus |
| JP3855695B2 (en) * | 2001-07-23 | 2006-12-13 | 松下電器産業株式会社 | Heat pump water heater |
| CN1865813A (en) * | 2006-05-10 | 2006-11-22 | 江苏双良空调设备股份有限公司 | Second lithium bromide absorption type heat pump for preparing steam by using vertical double-side falling-film absorber |
| CN201281489Y (en) * | 2008-09-28 | 2009-07-29 | 江苏双良空调设备股份有限公司 | Thermal water vapor concurrent heating type lithium bromide absorption type water chilling unit |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114072622A (en) * | 2019-07-10 | 2022-02-18 | 睿特维亚有限公司 | Bernoulli heat pump with laminar flow refrigerant |
| CN114072622B (en) * | 2019-07-10 | 2023-10-31 | 睿特维亚有限公司 | Bernoulli heat pump with laminar flow refrigerant |
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Application publication date: 20141001 |