CN114887343A - Chemical industry equipment is with safe type retort - Google Patents

Chemical industry equipment is with safe type retort Download PDF

Info

Publication number
CN114887343A
CN114887343A CN202210533729.XA CN202210533729A CN114887343A CN 114887343 A CN114887343 A CN 114887343A CN 202210533729 A CN202210533729 A CN 202210533729A CN 114887343 A CN114887343 A CN 114887343A
Authority
CN
China
Prior art keywords
tank
sleeve
distillation
tank body
heating
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.)
Granted
Application number
CN202210533729.XA
Other languages
Chinese (zh)
Other versions
CN114887343B (en
Inventor
赵志强
赵新杰
蒋国涛
赵江涛
张迎迎
赵应应
赵淘淘
韩凤鑫
许佳鹏
史朝朝
王冬丽
李向阳
王帅
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.)
Henan Longbai Intelligent Equipment Manufacturing Co ltd
Original Assignee
Henan Longbai Intelligent Equipment Manufacturing 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 Henan Longbai Intelligent Equipment Manufacturing Co ltd filed Critical Henan Longbai Intelligent Equipment Manufacturing Co ltd
Priority to CN202210533729.XA priority Critical patent/CN114887343B/en
Publication of CN114887343A publication Critical patent/CN114887343A/en
Application granted granted Critical
Publication of CN114887343B publication Critical patent/CN114887343B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/02Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in boilers or stills
    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The invention relates to a safety distillation retort for chemical equipment, which comprises a retort body, a cover body and a heating sleeve, wherein the cover body is connected with the retort body through a sealing end face; the upper end of the annular sleeve is hermetically connected with the outer circumference of the cover body, the lower part of the outer side wall of the tank body is provided with a circle of supporting seat, the supporting seat is provided with a plurality of stand columns, the outer wall of the annular sleeve body is provided with a circle of compression ring, the compression ring is sleeved on the stand columns, and the stand columns are provided with compression springs; the tank body and the cover body are connected through explosion venting bolts. When the pressure of the distillation tank exceeds the standard, the distillation tank can reduce the pressure in a mode of expanding the volume of the tank body, and avoid the leakage of combustible gas or toxic gas in the tank or the overflow of external air into the tank to cause explosion or poisoning accidents, so the distillation tank has the advantages of safety and reliability.

Description

Chemical industry equipment is with safe type retort
Technical Field
The invention relates to a safety distillation tank for chemical equipment, and belongs to the technical field of chemical equipment.
Background
The distillation tank is a device for separating homogeneous liquid mixture, is one of the most commonly used devices in chemical industry, and is also a device with high risk and easy leakage and fire explosion accidents. The materials in the distillation tank are mostly flammable and explosive dangerous chemicals, once the materials are leaked, the materials and air form explosive mixtures, and fire explosion can be caused when the materials meet open fire. If the material is a toxic chemical, the leakage may result in poisoning of personnel.
Specifically, in the working process of the distillation tank, the material is heated, when the temperature reaches the boiling point of a certain component, the component is converted from a liquid state into a gas state, and the gas is discharged from the distillation pipe and condensed and collected. In the process, the problem of ultrahigh pressure in the tank caused by temperature fluctuation, material fluctuation, blockage of a distillation pipe or other reasons can occur, and the tank body can be cracked, so that inflammable or toxic gas is leaked, and further explosion or toxic accidents are caused. In the prior art, a tank body is generally provided with an explosion venting port, when the pressure exceeds a limit value, the explosion venting port is opened to release the pressure, and the pressure in the tank is reduced, so that the tank body is prevented from being broken. However, after the explosion venting port is opened, gas leakage still exists, and if open fire or a power supply exists on the site, fire accidents are easily caused. If toxic gas exists during explosion venting, the health of field workers can be harmed.
Disclosure of Invention
Aiming at the problems, the invention provides a safe distillation retort for chemical equipment, which has the specific scheme that:
a safety distillation tank for chemical equipment comprises a tank body, a cover body and a heating sleeve, wherein the cover body is connected with the tank body through a sealing end face; the upper end of the annular sleeve is hermetically connected with the outer circumference of the cover body, the lower part of the outer side wall of the tank body is provided with a circle of supporting seat, the supporting seat is provided with a plurality of stand columns, the outer wall of the annular sleeve body is provided with a circle of compression ring, the compression ring is sleeved on the stand columns, and the stand columns are provided with compression springs; the tank body and the cover body are connected through explosion venting bolts.
Furthermore, the feed pipe and the distillation pipe are provided with a vertical sliding sleeve section, and the cover body is connected with the sliding sleeve section in a sliding and sealing manner; the internal mount that is equipped with of jar, the lower part and the mount fixed connection of inlet pipe and distillation tube.
Furthermore, the heating sleeve also comprises a bottom sleeve which is arranged at the bottom of the tank body; the upper end of the bottom sleeve is connected with the lower part of the supporting seat through an explosion venting bolt; the bottom of annular cover is equipped with medium joint, goes up the lower part that medium joint runs through to the supporting seat, and the bottom cover is equipped with down medium joint, and lower medium joint is connected with last medium joint plug.
Further, jar body bottom is equipped with the landing leg, and the bottom cover is equipped with the groove of stepping down, and the upper portion opening in the groove of stepping down, landing leg are arranged in the groove of stepping down.
Furthermore, an annular sealing slip ring is arranged between the inner wall of the annular sleeve and the outer wall of the tank body.
Furthermore, the junction of the feed pipe, the distillation pipe and the cover body is provided with an annular sliding sleeve.
Furthermore, a heating sleeve connecting seat is arranged on one side of the tank body, and a heat exchange medium inlet and outlet pipe is arranged on one side of the annular sleeve, which faces the heating sleeve connecting seat; a vertical sliding groove is formed in the inner side of the heating sleeve connecting seat, and a sliding block is arranged in the sliding groove; the inlet pipe and the outlet pipe are connected with the sliding block; the upper part of the sliding chute is provided with a cooling medium inlet and a cooling medium outlet, and the lower part of the sliding chute is provided with a heating medium inlet and a heating medium outlet; when the slide block is positioned at the lower limit, the heat exchange medium inlet and outlet pipe is in butt joint with the heating medium inlet and outlet, and when the slide block is positioned at the upper limit, the heat exchange medium inlet and outlet pipe is in butt joint with the cooling medium inlet and outlet.
Further, the cover body is provided with a stirring motor, a stirring shaft of the stirring motor penetrates into the tank body, a nut is connected to the stirring shaft in a threaded manner, a clamping column is arranged on the outer side wall of the nut, the support is provided with a shaped hole, and the shaped hole is provided with an L-shaped clamping groove; the profile hole can restrict the nut from rotating after the nut enters the profile hole.
When the pressure of the distillation tank exceeds the standard, the distillation tank can reduce the pressure in a mode of expanding the volume of the tank body, and avoid the leakage of combustible gas or toxic gas in the tank or the overflow of external air into the tank to cause explosion or poisoning accidents, so the distillation tank has the advantages of safety and reliability.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of the connection structure of the bottom cover;
FIG. 3 is a schematic view of the structure of the stirring shaft;
FIG. 4 is a schematic cross-sectional view of the stirring shaft;
fig. 5 is a schematic structural view of a heating jacket connecting seat.
Detailed Description
Example 1
As shown in fig. 1 to 5, the safety distillation retort for chemical equipment comprises a retort body 1, a cover body 2 and a heating jacket, wherein a heat exchange coil is arranged in the heating jacket, the retort body is heated by injecting a heat exchange medium into the heat exchange coil, and the heat exchange medium generally adopts steam and molten salt. The cover body is connected with the tank body through a sealing end face, the heating sleeve is arranged outside the tank body, the cover body is provided with a feeding pipe 3 and a distillation pipe 4, the heating sleeve comprises an annular sleeve 5, and the annular sleeve is in sliding connection with the side wall of the tank body; the upper end of the annular sleeve 5 is hermetically connected with the outer circumference of the cover body 2, the lower part of the outer side wall of the tank body is provided with a circle of supporting seat 6, the supporting seat 6 is provided with a plurality of stand columns 7, the outer wall of the annular sleeve body is provided with a circle of pressing ring 8, the pressing ring is sleeved on the stand columns 7, and the stand columns are provided with pressure springs 8; the tank body and the cover body are connected through explosion venting bolts 10. When the pressure in the tank exceeds the limit value, the explosion venting bolt falls off, and the sealing end faces of the tank body and the cover body are disconnected. Under the effect of the pressure in the tank and the pressure spring, the annular sleeve moves upwards along the tank body, the volume of the tank body is increased, and the pressure in the tank can be reduced. At the moment, the annular sleeve still forms a seal with the side wall of the tank body, so that gas in the tank body is prevented from leaking. In addition, after the annular sleeve is moved on, the lower part of the tank body is exposed, the annular sleeve does not heat the materials in the tank body, the heat dissipation of the tank body after being exposed is accelerated, the temperature of the materials is rapidly reduced, the materials can be prevented from continuously evaporating, and the pressure in the tank body is favorably reduced.
In the scheme, the cover body and the annular sleeve adopt an integrated structure, so that the cover body and the annular sleeve form sealing. Because the distillation pipe and the feeding pipe are arranged on the cover body, when the annular sleeve moves upwards, the distillation pipe and the feeding pipe cannot interfere with the annular sleeve to move upwards. The distillation tube and the feed tube may be provided as a hose connection structure.
The strength of the hose connection is not as strong as the fixed steel pipe connection. This embodiment provides a structure, and inlet pipe and distillation tube adopt fixed knot to construct, and do not influence the upshift of ring sheath when letting out the explosion. The specific structure is that the feed pipe and the distillation pipe are provided with a vertical sliding sleeve section, and the cover body is connected with the sliding sleeve section in a sliding and sealing way; the tank body is internally provided with a fixed frame 13, and the lower parts of the feeding pipe and the distillation pipe are fixedly connected with the fixed frame 13. When the annular sleeve and the cover body move upwards, the cover body can slide along the sliding sleeve section.
In order to ensure that the sealing performance is kept among the cover body, the annular sleeve and the tank body after explosion venting. An annular sealing slip ring 9 is arranged between the inner wall of the annular sleeve and the outer wall of the tank body. And an annular sliding sleeve 11 is arranged at the joint of the feed pipe, the distillation pipe and the cover body. The sliding ring and the sliding sleeve are both made of temperature-resistant and corrosion-resistant sealing elements, such as fluororubber.
In the scheme, the annular sleeve can only heat the side wall of the tank body, and in order to ensure the heating effect on materials during distillation, the heating sleeve also comprises a bottom sleeve 12 which is arranged at the bottom of the tank body and used for heating the bottom of the tank body; the upper end of the bottom sleeve is connected with the lower part of the supporting seat through an explosion venting bolt 10, after explosion venting, the bottom sleeve falls off, heating of the bottom of the tank body is stopped, and meanwhile, the bottom of the tank body can be exposed for cooling; referring to fig. 2, the bottom of the annular sleeve is provided with an upper medium joint 14, the upper medium joint penetrates through the lower part of the supporting seat, the bottom of the annular sleeve is sleeved with a lower medium joint 15, and the lower medium joint is connected with the upper medium joint in an inserting manner. The connection between the bottom sleeve and the medium circulation pipeline is realized through the upper medium joint and the lower medium joint, and the upper medium joint and the lower medium joint are disconnected simultaneously after the bottom sleeve falls off.
The bottom of the tank body is provided with a supporting leg 16, the bottom of the tank body is provided with a yielding groove in a sleeved mode, the upper portion of the yielding groove is open, and the supporting leg is located in the yielding groove. The landing leg can make a jar body liftoff a section height, does benefit to the droing of bottom cover.
Referring to fig. 1 and 5, a heating jacket connecting seat 17 is arranged on one side of the tank body, and a heat exchange medium inlet and outlet pipe 18 is arranged on one side of the annular jacket facing the heating jacket connecting seat; a vertical sliding groove is arranged on the inner side of the heating sleeve connecting seat, and a sliding block 19 is arranged in the sliding groove; the inlet pipe and the outlet pipe are connected with the sliding block; the upper part of the sliding chute is provided with a cooling medium inlet and outlet 20, and the lower part of the sliding chute is provided with a heating medium inlet and outlet 21; when the slide block is positioned at the lower limit, the heat exchange medium inlet and outlet pipe is in butt joint with the heating medium inlet and outlet, and when the slide block is positioned at the upper limit, the heat exchange medium inlet and outlet pipe is in butt joint with the cooling medium inlet and outlet. After explosion venting, the annular sleeve moves upwards, the sliding block moves upwards along with the annular sleeve, the heat exchange medium inlet and outlet pipe is disconnected with the heating medium inlet and outlet, and the heat medium is stopped to be introduced. When the heat exchange medium is moved upwards to the upper limit, the heat exchange medium inlet and outlet pipe is in butt joint with the cooling medium inlet and outlet, and the cooling medium is introduced to carry out forced cooling, wherein the cooling medium can adopt cold air.
The cover body is provided with a stirring motor, a stirring shaft 26 of the stirring motor penetrates into the tank body, referring to fig. 3-4, a nut 22 is connected to the stirring shaft in a threaded manner, a clamping column 23 is arranged on the outer side wall of the nut, a shaped hole 24 is formed in the support, and an L-shaped clamping groove 25 is formed in the shaped hole; the profile hole can restrict the nut from rotating after the nut enters the profile hole. The structure considers that the reset capacity of the pressure spring is limited, in order to enable the annular sleeve to move upwards quickly, the inner volume of the tank body is increased to realize pressure reduction, and the tank body is cooled quickly. At the initial stage, the cover body drives the stirring shaft to rise under the action of the pressure spring, the nut enters the molded hole, the clamping column slides into the L-shaped clamping groove, then the stirring shaft continues to rotate, the stirring shaft moves up under the pushing of the nut, the cover body and the annular sleeve are driven to move up until the upper limit is reached, and the upper limit can be realized by arranging the limit on the control accessible stand column.

Claims (8)

1. The utility model provides a chemical industry equipment is with safe type retort, includes a jar body, lid and heating jacket, and the lid passes through the seal end face with a jar body to be connected, and the heating jacket is established at a jar external portion, and the lid is equipped with inlet pipe and distillation column, its characterized in that: the heating sleeve comprises an annular sleeve, and the annular sleeve is connected with the side wall of the tank body in a sliding manner; the upper end of the annular sleeve is hermetically connected with the outer circumference of the cover body, the lower part of the outer side wall of the tank body is provided with a circle of supporting seat, the supporting seat is provided with a plurality of stand columns, the outer wall of the annular sleeve body is provided with a circle of compression ring, the compression ring is sleeved on the stand columns, and the stand columns are provided with compression springs; the tank body and the cover body are connected through explosion venting bolts.
2. The safety distillation tank for chemical equipment according to claim 1, wherein: the feeding pipe and the distillation pipe are provided with a vertical sliding sleeve section, and the cover body is connected with the sliding sleeve section in a sliding and sealing manner; the internal mount that is equipped with of jar, the lower part and the mount fixed connection of inlet pipe and distillation tube.
3. The safety distillation tank for chemical equipment according to claim 1, wherein: the heating sleeve also comprises a bottom sleeve which is arranged at the bottom of the tank body; the upper end of the bottom sleeve is connected with the lower part of the supporting seat through an explosion venting bolt; the bottom of annular cover is equipped with medium joint, goes up the lower part that medium joint runs through to the supporting seat, and the bottom cover is equipped with down medium joint, and lower medium joint is connected with last medium joint plug.
4. The safety distillation tank for chemical equipment as claimed in claim 3, wherein: the bottom of the tank body is provided with a supporting leg, the bottom of the tank body is provided with a yielding groove in a sleeved mode, the upper portion of the yielding groove is open, and the supporting leg is located in the yielding groove.
5. The safety distillation tank for chemical equipment according to claim 1, wherein: and an annular sealing slip ring is arranged between the inner wall of the annular sleeve and the outer wall of the tank body.
6. The safety distillation tank for chemical equipment as claimed in claim 2, wherein: the junction of the feed pipe and the distillation pipe with the cover body is provided with an annular sliding sleeve.
7. The safety distillation tank for chemical equipment according to claim 1, wherein: a heating sleeve connecting seat is arranged on one side of the tank body, and a heat exchange medium inlet and outlet pipe is arranged on one side of the annular sleeve facing the heating sleeve connecting seat; a vertical sliding groove is formed in the inner side of the heating sleeve connecting seat, and a sliding block is arranged in the sliding groove; the inlet pipe and the outlet pipe are connected with the sliding block; the upper part of the sliding chute is provided with a cooling medium inlet and a cooling medium outlet, and the lower part of the sliding chute is provided with a heating medium inlet and a heating medium outlet; when the slide block is positioned at the lower limit, the heat exchange medium inlet and outlet pipe is in butt joint with the heating medium inlet and outlet, and when the slide block is positioned at the upper limit, the heat exchange medium inlet and outlet pipe is in butt joint with the cooling medium inlet and outlet.
8. The safety distillation tank for chemical equipment according to claim 1, wherein: the cover body is provided with a stirring motor, a stirring shaft of the stirring motor penetrates into the tank body, a nut is connected to the stirring shaft in a threaded manner, a clamping column is arranged on the outer side wall of the nut, the support is provided with a shaped hole, and the shaped hole is provided with an L-shaped clamping groove; the profile hole can restrict the nut from rotating after the nut enters the profile hole.
CN202210533729.XA 2022-05-17 2022-05-17 Safe type retort for chemical industry equipment Active CN114887343B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210533729.XA CN114887343B (en) 2022-05-17 2022-05-17 Safe type retort for chemical industry equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210533729.XA CN114887343B (en) 2022-05-17 2022-05-17 Safe type retort for chemical industry equipment

Publications (2)

Publication Number Publication Date
CN114887343A true CN114887343A (en) 2022-08-12
CN114887343B CN114887343B (en) 2023-09-12

Family

ID=82722869

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210533729.XA Active CN114887343B (en) 2022-05-17 2022-05-17 Safe type retort for chemical industry equipment

Country Status (1)

Country Link
CN (1) CN114887343B (en)

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1488550A (en) * 1974-11-22 1977-10-12 Mikropul Ges Fuer Mahl U Staub Apparatus for relief of explosion pressure in vessels
DE10121211A1 (en) * 2001-04-30 2002-11-14 Andreas Grasl Thermic release and valve device for pressure gas cartridges comprises valve body with screw-in aperture into which pressure gas cartridge can be screwed, insert bolt displaceable in valve body and cap connected with valve body
US20040055866A1 (en) * 2002-09-20 2004-03-25 Levine Michael R. Desalinization still
US20050178648A1 (en) * 2002-09-20 2005-08-18 Levine Michael R. Low energy vacuum distillation method and apparatus
CN204637624U (en) * 2015-05-14 2015-09-16 山东豪迈化工技术有限公司 Novel distillation tower
CN205549645U (en) * 2016-02-19 2016-09-07 濮阳市联众兴业化工有限公司 Material shifts and prevents flashing device between rectifying column
CN208761373U (en) * 2018-07-25 2019-04-19 贵州中矿基业安全技术有限公司 Explosion-proof fluid reservoir
WO2020242428A1 (en) * 2019-05-29 2020-12-03 Леонид Нисонович КОНТОРОВИЧ Explosion and fire prevention system for high-voltage electrical equipment
CN112483694A (en) * 2019-09-11 2021-03-12 江苏泛亚微透科技股份有限公司 Explosion-proof valve capable of managing humidity and application thereof
CN114344929A (en) * 2022-01-19 2022-04-15 石家庄职业技术学院 Explosion-proof distillation retort is used in chemical production

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1488550A (en) * 1974-11-22 1977-10-12 Mikropul Ges Fuer Mahl U Staub Apparatus for relief of explosion pressure in vessels
DE10121211A1 (en) * 2001-04-30 2002-11-14 Andreas Grasl Thermic release and valve device for pressure gas cartridges comprises valve body with screw-in aperture into which pressure gas cartridge can be screwed, insert bolt displaceable in valve body and cap connected with valve body
US20040055866A1 (en) * 2002-09-20 2004-03-25 Levine Michael R. Desalinization still
US20050178648A1 (en) * 2002-09-20 2005-08-18 Levine Michael R. Low energy vacuum distillation method and apparatus
CN204637624U (en) * 2015-05-14 2015-09-16 山东豪迈化工技术有限公司 Novel distillation tower
CN205549645U (en) * 2016-02-19 2016-09-07 濮阳市联众兴业化工有限公司 Material shifts and prevents flashing device between rectifying column
CN208761373U (en) * 2018-07-25 2019-04-19 贵州中矿基业安全技术有限公司 Explosion-proof fluid reservoir
WO2020242428A1 (en) * 2019-05-29 2020-12-03 Леонид Нисонович КОНТОРОВИЧ Explosion and fire prevention system for high-voltage electrical equipment
CN112483694A (en) * 2019-09-11 2021-03-12 江苏泛亚微透科技股份有限公司 Explosion-proof valve capable of managing humidity and application thereof
CN114344929A (en) * 2022-01-19 2022-04-15 石家庄职业技术学院 Explosion-proof distillation retort is used in chemical production

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李建华;黄郑华;: "液化石油气储罐泄漏的消防安全设计", 油气储运, no. 11, pages 54 - 56 *

Also Published As

Publication number Publication date
CN114887343B (en) 2023-09-12

Similar Documents

Publication Publication Date Title
US20200208777A1 (en) Liquid oxygen storage tank
CN114887343A (en) Chemical industry equipment is with safe type retort
CN105080428B (en) High-temperature and high-pressure reaction kettle for supercritical CO2 core damage
CN109870350A (en) A kind of liquid-leakage preventing high temperature and pressure hydraulic pressure fracturing system and test method
HUE033333T2 (en) Method of fuel for energetics production
CN112556405A (en) Sintering furnace dewaxing structure and sintering furnace
CN205872947U (en) Pressure release interlock system bleeds
CN213196081U (en) Pressurizing device for diffusion welding equipment and diffusion welding equipment
CN112098261B (en) Device for evaporating liquid metal sodium at high temperature and high pressure and operation method
CN205199023U (en) Carbon dioxide extraction device
CN103035305B (en) Hydrogen elimination test device
CN210385780U (en) Small-sized high-pressure reaction kettle
CN210434505U (en) Sealed heating reaction device of lithium hydride reaction kettle
CN208919705U (en) A kind of explosion-protection equipment of butane spherical tank
CN109847669B (en) Overtemperature control system and control method for tubular reactor of supercritical water oxidation device
US4577488A (en) Apparatus and method for inspecting welds
CN207576344U (en) A kind of high pressure tank body convenient-opening fluid pressure type reaction kettle
CN113525944A (en) Petroleum storage device
CN207738706U (en) A kind of waste oil regeneration high temperature distillation catalytic unit
CN208554259U (en) A kind of high pressure gas heating heating device
US3833056A (en) High temperature cooling process and system
CN209085378U (en) A kind of cooling tank for vitamin production
CN210571895U (en) Internal corrosion test stand
US2449738A (en) Oil emulsion treater
CN215677912U (en) Hydraulic test device for vertical cylindrical pressure container

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
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Zhao Zhiqiang

Inventor after: Xu Jiapeng

Inventor after: Shi Chaochao

Inventor after: Wang Dongli

Inventor after: Li Xiangyang

Inventor after: Wang Shuai

Inventor after: Zhao Xinjie

Inventor after: Jiang Guotao

Inventor after: Zhao Jiangtao

Inventor after: Zhang Yingying

Inventor after: Zhao Yingying

Inventor after: Zhao Taotao

Inventor after: Han Fengxin

Inventor after: Chen Yi

Inventor before: Zhao Zhiqiang

Inventor before: Shi Chaochao

Inventor before: Wang Dongli

Inventor before: Li Xiangyang

Inventor before: Wang Shuai

Inventor before: Zhao Xinjie

Inventor before: Jiang Guotao

Inventor before: Zhao Jiangtao

Inventor before: Zhang Yingying

Inventor before: Zhao Yingying

Inventor before: Zhao Taotao

Inventor before: Han Fengxin

Inventor before: Xu Jiapeng

GR01 Patent grant
GR01 Patent grant