CN106269798B - A kind of low temperature pressurized hydrolysis tank - Google Patents

A kind of low temperature pressurized hydrolysis tank Download PDF

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Publication number
CN106269798B
CN106269798B CN201610739302.XA CN201610739302A CN106269798B CN 106269798 B CN106269798 B CN 106269798B CN 201610739302 A CN201610739302 A CN 201610739302A CN 106269798 B CN106269798 B CN 106269798B
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CN
China
Prior art keywords
tube assembly
valve tube
pipe
outlet valve
saturation
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 - Fee Related
Application number
CN201610739302.XA
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Chinese (zh)
Other versions
CN106269798A (en
Inventor
刘文治
黄道德
赵春霞
胡长庆
陈新桥
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.)
Ningbo Baolinong Environment Technology Co ltd
Original Assignee
Ningbo Li Li Nong Environmental Technology Development 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 Ningbo Li Li Nong Environmental Technology Development Co Ltd filed Critical Ningbo Li Li Nong Environmental Technology Development Co Ltd
Priority to CN201610739302.XA priority Critical patent/CN106269798B/en
Publication of CN106269798A publication Critical patent/CN106269798A/en
Priority to PCT/CN2017/098942 priority patent/WO2018036552A1/en
Application granted granted Critical
Publication of CN106269798B publication Critical patent/CN106269798B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

A kind of low temperature pressurized hydrolysis tank disclosed by the invention, including tank body, outer coil pipe, insulating layer, supporting leg, outlet valve tube assembly, intake valve tube assembly, drain valve tube assembly, into saturation water valve tube assembly, go out saturation water valve tube assembly, screw rod feeding device, air outlet valve tube assembly, external disk pipe dish is wound on tank body, and insulating layer is coated on outer coil pipe;Saturated water, the exit port of outer coil pipe are connect with into and out of saturation water valve tube assembly respectively, and top of the tank is provided with screw rod feeding device, manhole, air outlet valve tube assembly, pressure gauge, safety valve, thermometer and temperature sensor;Discharge port connection outlet valve tube assembly, drain valve tube assembly and the intake valve tube assembly of tank base.Low temperature pressurized hydrolysis tank saturated water indirect heating of the invention, it is ensured that temperature of charge is no more than 120 DEG C in hydrolytic decomposition pot.It is pressurizeed with air compressor machine, more than the correlation pressure of steam direct heating, had not only reached hydrolysis purpose, but also do not generate volatile organic contaminant, and do not generated stink and peculiar smell.

Description

A kind of low temperature pressurized hydrolysis tank
Technical field
The present invention relates to the field of environment protection equipment of organic waste chemical hydrolysis processing, in particular to a kind of low temperature pressure (hydraulic) waters Solve tank.
Background technique
Traditional hydrolytic decomposition pot is the high-temperature steam that logical Boiler Steam directly generates 120 DEG C~180 DEG C, directly heats and produces therewith Raw steam correlation pressure generates organic waste more than 120 DEG C, the vapor (steam) temperature of 0.2MPa for 0.2MPa~0.8MPa Mixed type volatile organic acids, such as formic acid, acetic acid, propionic acid, butyric acid etc..One kind is generated therewith is charred taste pollution environment.Such as Add cooling recycling volatile organic acids to make complex technical process, increases technological equipment investment.
Summary of the invention
Technical problem to be solved by the present invention lies in provide a kind of structure for the problems of existing hydrolytic decomposition pot Low temperature pressurized hydrolysis tank simplified, at low cost.
The technical problems to be solved by the invention can be realized by the following technical programs:
A kind of low temperature pressurized hydrolysis tank, including tank body, outer coil pipe, insulating layer, supporting leg, outlet valve tube assembly, intake valve pipe Component, drain valve tube assembly, into saturation water valve tube assembly, go out saturation water valve tube assembly, screw rod feeding device, air outlet valve pipe group Part, the tank body are mounted on the supporting leg, and the external disk pipe dish is wound on the outer wall of the tank body, and the insulating layer is coated on On the outer coil pipe;The saturation water inlet of the outer coil pipe is connect with described into saturation water valve tube assembly, and the outer coil pipe is satisfied It is connect with water out with the water valve tube assembly of saturation out, screw rod conveying dress is provided in the upper capping of the top of the tank It sets, manhole, air outlet valve tube assembly, pressure gauge, safety valve, thermometer and temperature sensor, the discharging of the screw rod feeding device Pipe enters in tank body across the upper capping of the top of the tank;The discharge port of the tank base connects the outlet valve tube assembly With drain valve tube assembly, the intake valve tube assembly is connected in the outlet valve tube assembly.
In a preferred embodiment of the invention, it is described into saturation water valve tube assembly include water pipe and being connected on into saturation It is described on saturation water pipe into saturated water shut-off valve, it is described go out saturation water valve tube assembly include saturation water pipe and being connected on institute It states out and goes out saturated water shut-off valve, described to connect into saturation water pipe with the saturation water inlet of the outer coil pipe, institute on saturation water pipe Saturation water pipe is stated out to connect with the saturation water out of the outer coil pipe.
In a preferred embodiment of the invention, the outlet valve tube assembly includes discharge nozzle and is connected on the discharging The first outlet valve and the second outlet valve on pipe, the intake valve tube assembly include air inlet pipe and are connected in the air inlet pipe Intake valve, the air inlet pipe are connected on the discharge nozzle between first outlet valve and the second outlet valve.
Due to using technical solution as above, when organic materials is hydrolyzed in the present invention, with the saturation more than 100 DEG C Water is heated, and is controlled organic materials temperature in tank body and is no more than 120 DEG C, pressure is the pressure that air compressor generates, and is 0.7MPa~1.0MPa, compressed air temperature are no more than 100 DEG C.Not only hydrolysis purpose had been reached, but also has not discharged volatile organic acids, done To odorless, without being charred taste and other peculiar smell.Simplify hydrolysis system and do not generate volatile organic acids again, reduces investment.
Detailed description of the invention
Fig. 1 is low temperature pressurized hydrolysis jar structure schematic diagram of the invention.
Fig. 2 is the top view of Fig. 1.
Specific embodiment
In conjunction with attached drawing, the solution of the present invention is specifically described by embodiment.
Referring to Fig. 1 and Fig. 2, a kind of low temperature pressurized hydrolysis tank shown in figure, including tank body 1, outer coil pipe 2, insulating layer 3, Supporting leg 4, outlet valve tube assembly 5, intake valve tube assembly 6, drain valve tube assembly 7, into saturation water valve tube assembly 8, go out saturation water valve Tube assembly 9, screw rod feeding device 12, air outlet valve tube assembly 10.
Tank body 1 is mounted on supporting leg 4, and outer coil pipe 2 is coiled on the outer wall of tank body 1, and insulating layer 3 is coated on outer coil pipe 2.
It include into saturation water pipe 17 and being connected on into ending on saturation water pipe 17 into saturated water into saturation water valve tube assembly 8 Valve 18, being saturated water valve tube assembly 9 out includes saturation water pipe 19 and being connected on out on saturation water pipe 19 to go out saturated water shut-off valve 20, it is connect into saturation water pipe 17 with the saturation water inlet of outer coil pipe 2, the saturation water out for being saturated water pipe 19 and outer coil pipe 2 out connects It connects.
Screw rod feeding device 12, manhole 11, air outlet valve tube assembly 10, pressure are provided in the upper capping 21 at 1 top of tank body Power table 13, safety valve 14, thermometer 15 and temperature sensor 16, the discharge nozzle 22 of screw rod feeding device 12 pass through 1 top of tank body Upper capping 21 enter tank body 1 in.Manhole 11 is located at the center of upper capping 21.
The bottom of tank body 1 is tapered, and the bottom of taper is that discharge port 23 connects outlet valve tube assembly 5 and drain valve tube assembly 7, drain valve tube assembly 7 includes drainpipe 24 and the drain valve 25 being connected on drainpipe 24, and drainpipe 24 and discharge port 23 connect It connects.
Outlet valve tube assembly 5 includes discharge nozzle 26 and the outlet valve 27,28 that is connected on discharge nozzle 26, outlet valve 27 with go out Material mouth 23 connects.
Intake valve tube assembly 6 includes air inlet pipe 29 and the intake valve 30 being connected in air inlet pipe 29, and air inlet pipe 29 is connected to On discharge nozzle 26 between outlet valve 27,28 and the second outlet valve.

Claims (3)

1. a kind of low temperature pressurized hydrolysis tank, which is characterized in that including tank body, outer coil pipe, insulating layer, supporting leg, outlet valve tube assembly, Intake valve tube assembly, drain valve tube assembly, into saturation water valve tube assembly, go out saturation water valve tube assembly, screw rod feeding device, outlet Valve tube assembly, the tank body are mounted on the supporting leg, and the external disk pipe dish is wound on the outer wall of the tank body, the insulating layer It is coated on the outer coil pipe;The saturation water inlet of the outer coil pipe is connect with described into saturation water valve tube assembly, the external disk The saturation water out of pipe is connect with the water valve tube assembly of saturation out, and it is defeated to be provided with screw rod in the upper capping of the top of the tank Expect device, manhole, air outlet valve tube assembly, pressure gauge, safety valve, thermometer and temperature sensor, the screw rod feeding device The upper capping that discharge nozzle passes through the top of the tank enters in tank body;The discharge port of the tank base connects the outlet valve pipe Component and drain valve tube assembly, the intake valve tube assembly are connected in the outlet valve tube assembly.
2. a kind of low temperature pressurized hydrolysis tank as described in claim 1, which is characterized in that described to include into saturation water valve tube assembly Into saturation water pipe and it is connected on described into, into saturated water shut-off valve, the water valve tube assembly of saturation out includes on saturation water pipe Saturation water pipe and be connected on it is described go out saturation water pipe on go out saturated water shut-off valve, it is described into saturation water pipe and the outer coil pipe It is saturated water inlet connection, the water pipe of saturation out is connect with the saturation water out of the outer coil pipe.
3. a kind of low temperature pressurized hydrolysis tank as described in claim 1, which is characterized in that the outlet valve tube assembly includes discharging The first outlet valve and the second outlet valve on the discharge nozzle are managed and are connected on, the intake valve tube assembly includes air inlet pipe and string The intake valve being associated in the air inlet pipe, the air inlet pipe are connected to the discharging between first outlet valve and the second outlet valve Guan Shang.
CN201610739302.XA 2016-08-26 2016-08-26 A kind of low temperature pressurized hydrolysis tank Expired - Fee Related CN106269798B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201610739302.XA CN106269798B (en) 2016-08-26 2016-08-26 A kind of low temperature pressurized hydrolysis tank
PCT/CN2017/098942 WO2018036552A1 (en) 2016-08-26 2017-08-25 Low-temperature pressurized hydrolysis tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610739302.XA CN106269798B (en) 2016-08-26 2016-08-26 A kind of low temperature pressurized hydrolysis tank

Publications (2)

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CN106269798A CN106269798A (en) 2017-01-04
CN106269798B true CN106269798B (en) 2019-03-19

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CN (1) CN106269798B (en)
WO (1) WO2018036552A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106269798B (en) * 2016-08-26 2019-03-19 宁波宝力农环境技术开发有限公司 A kind of low temperature pressurized hydrolysis tank
CN107971328A (en) * 2017-12-28 2018-05-01 宁波宝力农环境技术开发有限公司 Low Temperature Thermal hydrolytic decomposition pot

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CN201632261U (en) * 2010-04-12 2010-11-17 杨辉 Hydrolytic-hydrothermal oxidizing reaction kettle for agriculture and animal husbandry wastes and household refuses
CN201692979U (en) * 2010-06-13 2011-01-05 烟台润达垃圾处理环保股份有限公司 Digestion tank for hydrothermal treatment of municipal domestic waste
CN201871374U (en) * 2010-11-24 2011-06-22 杨健 Pyrolytic oxidizing reaction kettle for household garbage
CN102247974A (en) * 2011-05-13 2011-11-23 北京加朗传奇新能源科技有限责任公司 Method and device for hydrolyzing organic waste
KR101088095B1 (en) * 2011-04-18 2011-11-29 주식회사 에코그린텍 Equipment for decomposition of organic matter and method for decomposition of organic matter using the same
CN203184326U (en) * 2013-03-28 2013-09-11 云南天远生态环保科技有限责任公司 Professional hydrolysis tank for domestic waste organic matters
CN103570206A (en) * 2012-07-21 2014-02-12 宁波互联聚能环保技术有限公司 Thermal hydrolysis reactor dedicated for low dryness of wet steam, multiple discharge system and dehydration method (L.M.D method)
CN206009402U (en) * 2016-08-26 2017-03-15 宁波宝硕美机械设备工程有限公司 A kind of low temperature pressurized hydrolysis tank

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CN201415124Y (en) * 2009-04-16 2010-03-03 刘文治 Chemical catalytic hydrolysis tank
CN102603370A (en) * 2012-03-27 2012-07-25 河南农业大学 Treatment technology for producing organic fertilizer by tobacco field waste and fermentation tank thereof
CN202519170U (en) * 2012-03-27 2012-11-07 河南农业大学 Fermentation tank utilizing tobacco field wastes to produce organic fertilizer
CN204939488U (en) * 2015-08-05 2016-01-06 天紫环保装备制造(天津)有限公司 A kind of Methane Resources treatment system
CN204939314U (en) * 2015-08-05 2016-01-06 天紫再生资源加工(天津)有限公司 Convection agitation formula rubbish mineralising fermentation unit
CN205133453U (en) * 2015-10-31 2016-04-06 孙明杰 Big -arch shelter bacterial manure generator
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CN205164716U (en) * 2015-11-05 2016-04-20 四川高博环保工程有限公司 High temperature high pressure device of hydrolysising
CN205275474U (en) * 2015-12-23 2016-06-01 北京中源创能工程技术有限公司 Aerobic fermentation equipment
CN106269798B (en) * 2016-08-26 2019-03-19 宁波宝力农环境技术开发有限公司 A kind of low temperature pressurized hydrolysis tank

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101448581A (en) * 2006-09-28 2009-06-03 Eco原料株式会社 Processing system for organic waste
CN201632261U (en) * 2010-04-12 2010-11-17 杨辉 Hydrolytic-hydrothermal oxidizing reaction kettle for agriculture and animal husbandry wastes and household refuses
CN201692979U (en) * 2010-06-13 2011-01-05 烟台润达垃圾处理环保股份有限公司 Digestion tank for hydrothermal treatment of municipal domestic waste
CN201871374U (en) * 2010-11-24 2011-06-22 杨健 Pyrolytic oxidizing reaction kettle for household garbage
KR101088095B1 (en) * 2011-04-18 2011-11-29 주식회사 에코그린텍 Equipment for decomposition of organic matter and method for decomposition of organic matter using the same
CN102247974A (en) * 2011-05-13 2011-11-23 北京加朗传奇新能源科技有限责任公司 Method and device for hydrolyzing organic waste
CN103570206A (en) * 2012-07-21 2014-02-12 宁波互联聚能环保技术有限公司 Thermal hydrolysis reactor dedicated for low dryness of wet steam, multiple discharge system and dehydration method (L.M.D method)
CN203184326U (en) * 2013-03-28 2013-09-11 云南天远生态环保科技有限责任公司 Professional hydrolysis tank for domestic waste organic matters
CN206009402U (en) * 2016-08-26 2017-03-15 宁波宝硕美机械设备工程有限公司 A kind of low temperature pressurized hydrolysis tank

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WO2018036552A1 (en) 2018-03-01

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Effective date of registration: 20170814

Address after: Zhenning Zhenhai District Jiaochuan streets Road 315221 Zhejiang city of Ningbo province No. 123

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Address before: 315192 Zhejiang city of Ningbo province Yinzhou District South Road No. 1288

Applicant before: NINGBO BAOSHUOMEI MACHINERY EQUIPMENT ENGINEERING CO.,LTD.

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