CN106608619A - Sulfuric acid HRS low-pressure saturated steam heat exchanger - Google Patents

Sulfuric acid HRS low-pressure saturated steam heat exchanger Download PDF

Info

Publication number
CN106608619A
CN106608619A CN201510703666.8A CN201510703666A CN106608619A CN 106608619 A CN106608619 A CN 106608619A CN 201510703666 A CN201510703666 A CN 201510703666A CN 106608619 A CN106608619 A CN 106608619A
Authority
CN
China
Prior art keywords
air inlet
inlet pipe
heat exchanger
appendix
pressure saturated
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.)
Pending
Application number
CN201510703666.8A
Other languages
Chinese (zh)
Inventor
吴澳洲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Huaertai Chemical Industry Co Ltd
Original Assignee
Anhui Huaertai Chemical Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Anhui Huaertai Chemical Industry Co Ltd filed Critical Anhui Huaertai Chemical Industry Co Ltd
Priority to CN201510703666.8A priority Critical patent/CN106608619A/en
Publication of CN106608619A publication Critical patent/CN106608619A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention discloses a sulfuric acid HRS low-pressure saturated steam heat exchanger. The heat exchanger comprises a heat exchanger, a first air inlet pipe, a first electric valve, a second air inlet pipe, a second electric valve, an exhaust pipe and a thermometer. Compared with the existing device, the sulfuric acid HRS low-pressure saturated steam heat exchanger has a simple structure and strong functions, can realize recycle of the used steam for devices after the used steam is heated through heat exchange, prevents direct discharge of the steam into air, saves resources and reduces a production cost.

Description

A kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs
Technical field
The present invention relates to a kind of heat-exchanger rig, more particularly to a kind of sulphuric acid HRS low-pressure saturated steams Heat-exchanger rig.
Background technology
Chemical company's sulfuric acid plant HRS boiler by-product low-pressure saturated steams, and unnecessary steam is thought It is sent to and reuses elsewhere, but because feed-line is longer, causes vapor (steam) temperature low, Cause steam quality low, thus resulting in steam cannot use, so it is big by the steam to have to Amount emptying, causes the wasting of resources, in view of disadvantages described above, is necessary to design a kind of sulphuric acid HRS in fact Low-pressure saturated steam heat-exchanger rig.
The content of the invention
The technical problem to be solved is:There is provided a kind of sulphuric acid HRS low pressure saturation to steam Vapour heat-exchanger rig is directly discharged in air solving steam of the sulfuric acid plant HRS boilers using after Cause the problem of the wasting of resources.
To solve above-mentioned technical problem, the technical scheme is that:A kind of sulphuric acid HRS low pressure Saturated vapor heat-exchanger rig, including heat exchanger, the first air inlet pipe, the first electrodynamic valve, second Air inlet pipe, the second electrodynamic valve, exhaustor, thermometer, described heat exchanger is cylindrical drum, The first described air inlet pipe runs through heat exchanger, described the first air inlet pipe and heat exchanger close-fitting Be connected, described the first electrodynamic valve is located at the first air inlet pipe left end, described the first electrodynamic valve with First air inlet pipe screw thread is connected, and the second described air inlet pipe is located at heat exchanger bottom right, institute The second air inlet pipe and the heat exchanger stated is weldingly connected, and the second described electrodynamic valve enters positioned at second Trachea bottom, the second described electrodynamic valve is connected with the second air inlet pipe screw thread, described exhaustor Positioned at heat exchanger top left side, described exhaustor is weldingly connected with heat exchanger, described Thermometer is exhaustor top right-hand member, and described thermometer is connected with aerofluxuss pipe screw thread.
Further, described exhaustor contains the first appendix, three electrodynamic valves, second defeated Trachea, the 3rd appendix.
Further, the first described appendix be located at heat exchanger top left side, described first Appendix is weldingly connected with heat exchanger.
Further, three described electrodynamic valves are located at the first appendix right-hand member, three described electricity Dynamic valve is connected with the first gas transmission pipe screw thread.
Further, the second described appendix is located at three electrodynamic valve right-hand members, and described second is defeated Trachea is connected with three electrodynamic valve screw threads.
Further, the 3rd described appendix is located at three electrodynamic valve bottoms, and described the 3rd is defeated Trachea is connected with three electrodynamic valves and the second air inlet pipe screw thread.
Further, sealing ring is additionally provided with the middle of the first described air inlet pipe and heat exchanger, it is described Sealing ring be connected with heat exchanger and the first air inlet pipe close-fitting.
Compared with prior art, sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs, are first turned on First electrodynamic valve so that the high-temperature steam of sulphuric acid back pressure is input into the first air inlet pipe, the first air inlet pipe High-temperature steam is input in heat exchanger, and supply is discharged from the right-hand member outlet of the first air inlet pipe Sulphuric acid plant is used, then by opening the second electrodynamic valve so that after steam enter from second Trachea is entered in heat exchanger, then in heat exchanger, high-temperature steam in the first air inlet pipe and the Steam heat transmission in two air inlet pipe so that the temperature of steam and first in heat exchanger Temperature in air inlet pipe reaches gas washing in SA production and sets required steam simultaneously, so as to the second air inlet pipe Vapor (steam) temperature in middle entrance heat exchanger passes through in the first appendix after raising, defeated into first The temperature of steam is detected after trachea by thermometer, if the temperature of steam reaches qualified three afterwards Electrodynamic valve opens one end of the second appendix so that steam is discharged from the second appendix, if temperature During less than qualified temperature, three electrodynamic valves open one end of the 3rd appendix so that steam is from the Three appendixs are transmitted back in the second air inlet pipe, hence in so that vapor (steam) temperature reaches and qualified can be defeated by Sulphuric acid device is used, and the apparatus structure is simple, powerful, can realize that the steam after use leads to Cross continuation supply arrangement after heat exchange heats up to use, instead of steam and be directly discharged in air, from Resource has been saved, production cost has been reduced.
Description of the drawings
Fig. 1 is the sectional view of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs
Fig. 2 is the sectional view of heat exchanger
Fig. 3 is the front view of exhaustor
The air inlet pipe 2 of heat exchanger 1 first
The air inlet pipe 4 of first electrodynamic valve 3 second
The exhaustor 6 of second electrodynamic valve 5
The sealing ring 101 of thermometer 7
First electrodynamic valve 602 of appendix 601 3
The appendix 604 of second appendix 603 the 3rd
Specific embodiment
Hereinafter, various specific details are elaborated, to provide to constituting described embodiment The thorough understanding of the concept on basis.However, it will be apparent to those skilled in the art that institute The embodiment of description can be in the case of without some or all in these specific details To put into practice.In other cases, well-known process step is not specifically described.
As shown in Figure 1, Figure 2, Figure 3 shows, including heat exchanger 1, the first air inlet pipe 2, first Electrodynamic valve 3, the second air inlet pipe 4, the second electrodynamic valve 5, exhaustor 6, thermometer 7, sealing The 101, first appendix of circle, 601, three electrodynamic valves 602, the second appendixs the 603, the 3rd Appendix 604, described heat exchanger 1 is cylindrical drum, and the first described air inlet pipe 2 runs through Heat exchanger 1, the first described air inlet pipe 2 is connected with the close-fitting of heat exchanger 1, and described One electrodynamic valve 3 is located at the left end of the first air inlet pipe 2, described the first electrodynamic valve 3 and the first air inlet The screw thread of pipe 2 is connected, and the second described air inlet pipe 4 is located at the bottom right of heat exchanger 1, described The second air inlet pipe 4 be weldingly connected with heat exchanger 1, described second electrodynamic valve 5 is located at the The bottom of two air inlet pipe 4, the second described electrodynamic valve 5 is connected with the screw thread of the second air inlet pipe 4, institute The exhaustor 6 stated is located at the top left side of heat exchanger 1, described exhaustor 6 and heat exchanger 1 is weldingly connected, and described thermometer 7 is the top right-hand member of exhaustor 6, described thermometer 7 It is connected with the screw thread of exhaustor 6, described exhaustor 6 contains the first appendix 601, three Electrodynamic valve 602, the second appendix 603, the 3rd appendix 604, the first described appendix 601 are located at the top left side of heat exchanger 1, described first appendix 601 and heat exchanger 1 It is weldingly connected, three described electrodynamic valves 602 are located at the right-hand member of the first appendix 601, described Three electrodynamic valves 602 are connected with the screw thread of the first appendix 601, the second described appendix 603 Positioned at three right-hand members of electrodynamic valve 602, described the second appendix 603 and three electrodynamic valves 602 Screw thread is connected, and the 3rd described appendix 604 is located at three bottoms of electrodynamic valve 602, described 3rd appendix 604 is connected with three screw threads of 602 and second air inlet pipe of electrodynamic valve 4, described Sealing ring 101, described sealing ring 101 are additionally provided with the middle of first air inlet pipe 2 and heat exchanger 1 It is connected with the close-fitting of 1 and first air inlet pipe of heat exchanger 2, sulphuric acid HRS low-pressure saturated steams are changed Thermal, is first turned on the first electrodynamic valve 3 so that the high-temperature steam input first of sulphuric acid back pressure Air inlet pipe 2, the first air inlet pipe 2 is input into high-temperature steam in heat exchanger 1, and from first The right-hand member outlet of air inlet pipe 1 is discharged supply sulphuric acid plant and is used, then electric by opening second Dynamic valve 5 so that after steam enter in heat exchanger 1 from the second air inlet pipe 4, then heat exchange Steam heat in high-temperature steam and the second air inlet pipe 4 in machine 1 in first air inlet pipe 2 is passed Pass so that the temperature in heat exchanger 1 in the temperature and the first air inlet pipe of steam reaches simultaneously Required steam is set to gas washing in SA production, so as to enter in heat exchanger 1 in the second air inlet pipe 4 Vapor (steam) temperature raise after by the first appendix 601, leading to into after the first appendix 601 Excess temperature table 7 detects the temperature of steam, if the temperature of steam reaches qualified rear three electrodynamic valves 602 one end for opening the second appendix 603 so that steam is discharged from the second appendix 603, If temperature is less than qualified temperature, three electrodynamic valves make a call to 602 one end for opening the 3rd appendix 604, So that steam is transmitted back in the second air inlet pipe from the 3rd appendix 604, hence in so that vapor (steam) temperature Reach the qualified sulphuric acid device that can be defeated by use, wherein heat exchanger 1 is located at closed cylinder, from And steam heat exchange is reached, sealing ring 101 is to prevent steam from the first air inlet pipe 2 and heat friendship The gap changed planes in the middle of 1 is discharged, so as to reach sealing function.
Embodiment described above is only that the preferred embodiment of the present invention is described, and It is non-that the spirit and scope of the present invention are defined.In the premise without departing from design concept of the present invention Under, various modifications and improvement that this area ordinary person makes to technical scheme, Protection scope of the present invention should be dropped into.

Claims (7)

1. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs, it is characterised in that including heat exchange Machine, the first air inlet pipe, the first electrodynamic valve, the second air inlet pipe, the second electrodynamic valve, exhaustor, Thermometer, described heat exchanger is cylindrical drum, and the first described air inlet pipe runs through heat exchanger, The first described air inlet pipe is connected with heat exchanger close-fitting, and the first described electrodynamic valve is located at first Air inlet pipe left end, the first described electrodynamic valve is connected with the first air inlet pipe screw thread, and described second Air inlet pipe is located at heat exchanger bottom right, and the second described air inlet pipe welds phase with heat exchanger Even, the second described electrodynamic valve is located at the second air inlet pipe bottom, described the second electrodynamic valve and the Two air inlet pipe screw threads are connected, and described exhaustor is located at heat exchanger top left side, described row Trachea is weldingly connected with heat exchanger, and described thermometer is exhaustor top right-hand member, described Thermometer is connected with aerofluxuss pipe screw thread.
2. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 1, its Be characterised by described exhaustor contain the first appendix, three electrodynamic valves, the second appendix, 3rd appendix.
3. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 2, It is characterized in that the first described appendix is located at heat exchanger top left side, described first is defeated Trachea is weldingly connected with heat exchanger.
4. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 3, It is characterized in that three described electrodynamic valves are located at the first appendix right-hand member, described three are electronic Valve is connected with the first gas transmission pipe screw thread.
5. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 4, It is characterized in that the second described appendix is located at three electrodynamic valve right-hand members, the second described gas transmission Guan Yusan item electrodynamic valves screw thread is connected.
6. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 5, It is characterized in that the 3rd described appendix is located at three electrodynamic valve bottoms, the 3rd described gas transmission Guan Yusan items electrodynamic valve and the second air inlet pipe screw thread are connected.
7. a kind of sulphuric acid HRS low-pressure saturated steam heat-exchanger rigs as claimed in claim 6, It is characterized in that sealing ring is additionally provided with the middle of the first described air inlet pipe and heat exchanger, it is described Sealing ring is connected with heat exchanger and the first air inlet pipe close-fitting.
CN201510703666.8A 2015-10-26 2015-10-26 Sulfuric acid HRS low-pressure saturated steam heat exchanger Pending CN106608619A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510703666.8A CN106608619A (en) 2015-10-26 2015-10-26 Sulfuric acid HRS low-pressure saturated steam heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510703666.8A CN106608619A (en) 2015-10-26 2015-10-26 Sulfuric acid HRS low-pressure saturated steam heat exchanger

Publications (1)

Publication Number Publication Date
CN106608619A true CN106608619A (en) 2017-05-03

Family

ID=58613970

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510703666.8A Pending CN106608619A (en) 2015-10-26 2015-10-26 Sulfuric acid HRS low-pressure saturated steam heat exchanger

Country Status (1)

Country Link
CN (1) CN106608619A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5130112A (en) * 1990-03-23 1992-07-14 Monsanto Company Method for recovering high grade process energy from a contact sulfuric acid process
CN2816602Y (en) * 2005-04-28 2006-09-13 南京圣诺热管有限公司 High-temperature steam generator for recovering after heat from sulfuric acid
CN202072471U (en) * 2011-04-02 2011-12-14 中冶焦耐(大连)工程技术有限公司 Heat exchange device for high-temperature process gases and low-temperature process gases in acid making process
CN104567493A (en) * 2013-10-16 2015-04-29 朱力 Heat exchanger
CN104727181A (en) * 2015-02-11 2015-06-24 浙江荣晟环保纸业股份有限公司 Tail gas heat recycling structure used for paper making machine drying cylinder
CN205222695U (en) * 2015-10-26 2016-05-11 安徽华尔泰化工股份有限公司 Sulphuric acid HRS low pressure saturated steam heat transfer device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5130112A (en) * 1990-03-23 1992-07-14 Monsanto Company Method for recovering high grade process energy from a contact sulfuric acid process
CN2816602Y (en) * 2005-04-28 2006-09-13 南京圣诺热管有限公司 High-temperature steam generator for recovering after heat from sulfuric acid
CN202072471U (en) * 2011-04-02 2011-12-14 中冶焦耐(大连)工程技术有限公司 Heat exchange device for high-temperature process gases and low-temperature process gases in acid making process
CN104567493A (en) * 2013-10-16 2015-04-29 朱力 Heat exchanger
CN104727181A (en) * 2015-02-11 2015-06-24 浙江荣晟环保纸业股份有限公司 Tail gas heat recycling structure used for paper making machine drying cylinder
CN205222695U (en) * 2015-10-26 2016-05-11 安徽华尔泰化工股份有限公司 Sulphuric acid HRS low pressure saturated steam heat transfer device

Similar Documents

Publication Publication Date Title
CN204080417U (en) A kind of energy saving and environment friendly guide roll type rapid steamer
CN104089513B (en) A kind of heat energy recycling system
CN204187926U (en) A kind of medicine vacuum drying constant temperature system
CN106608619A (en) Sulfuric acid HRS low-pressure saturated steam heat exchanger
CN105271324B (en) A kind of low pressure exhaust steam recycling system
CN205222695U (en) Sulphuric acid HRS low pressure saturated steam heat transfer device
CN204521663U (en) High/low temperature sterilizing cabinet
CN207627953U (en) A kind of distilling apparatus of chemical field
CN204026622U (en) Steam boiler
CN206903698U (en) Back pressure turbine system with attemperator
CN204730734U (en) The segmented heat exchanger of temperature-controllable
CN204569884U (en) A kind of Wort boiling system of reusable edible secondary steam
CN106287655B (en) A kind of steam heat recovery technique
CN103330260A (en) Energy integration loop control system
CN104019637A (en) Steam heating type drying device and drying technology thereof
CN210736961U (en) Heating system of polymer melt spinning processing equipment
CN208887412U (en) Vapour emission reduction device more than a kind of hot-water cylinder
CN109612318A (en) A kind of waste-heat recovery device
CN217187911U (en) Evaporator pipeline device
CN204027394U (en) A kind of heat energy recycling system
CN211794155U (en) Tunnel type steam box inlet and outlet steam self-circulation and exhaust steam recycling system
CN204829871U (en) Boiler room returns water circulating system
CN209847914U (en) Instantaneous inactivation device of biological waste liquid
CN209960957U (en) Drying box condensate recovery system
CN203949475U (en) The recycling system of the dry waste heat of a kind of corn wet milling separator tube bank

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170503