CN212719772U - Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator - Google Patents

Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator Download PDF

Info

Publication number
CN212719772U
CN212719772U CN202021218624.8U CN202021218624U CN212719772U CN 212719772 U CN212719772 U CN 212719772U CN 202021218624 U CN202021218624 U CN 202021218624U CN 212719772 U CN212719772 U CN 212719772U
Authority
CN
China
Prior art keywords
furnace body
waste
waste liquid
chlorine
furnace
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
CN202021218624.8U
Other languages
Chinese (zh)
Inventor
程光明
王军
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.)
Jiangsu Liyu Environmental Technology Co ltd
Original Assignee
Jiangsu Liyu Environmental Technology 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 Jiangsu Liyu Environmental Technology Co ltd filed Critical Jiangsu Liyu Environmental Technology Co ltd
Priority to CN202021218624.8U priority Critical patent/CN212719772U/en
Application granted granted Critical
Publication of CN212719772U publication Critical patent/CN212719772U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Incineration Of Waste (AREA)

Abstract

The utility model discloses an improved eddy current type fluorine-chlorine-containing waste liquid and waste gas incinerator, which relates to a waste liquid and waste gas incinerator, comprising a furnace body with a hollow furnace chamber, wherein the upper part of the furnace body is provided with a waste gas inlet, an air inlet and an atomizing spray gun externally connected with a waste liquid pipeline along the tangential direction of the furnace chamber, an arc baffle is arranged in the furnace chamber, a mist guide channel is formed between the arc baffle and the inner wall of the furnace body, and the mist guide channel is in a gradually expanding structure along the mist outlet direction of the atomizing spray gun; an auxiliary burner for spraying fire into the furnace cavity is arranged on one side wall of the furnace body, and a layer of rectifying grating is arranged in the furnace body; a circular truncated cone-shaped baffle is arranged in the furnace body, and the large opening end of the circular truncated cone-shaped baffle covers the flue gas outlet. The utility model provides a waste gas waste liquid mix abundant even and influence combustion efficiency's problem inadequately, and can effectively reduce the export flue gas velocity of flow, reduce the loss of follow-up equipment.

Description

Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator
Technical Field
The utility model relates to a waste liquid waste gas burns device, concretely relates to improved generation eddy current type fluorine chlorine waste liquid waste gas burns burning furnace.
Background
With the rapid development of fluorine chemical industry in China, the disposal of waste liquid and waste gas containing fluorine and chlorine becomes a problem which is urgently needed to be solved by the industry. The waste gas containing the fluorine-chlorine waste liquid has complex components, belongs to industrial waste with high boiling point, high toxicity and high corrosion property, and is suitable for being treated by a vortex incinerator. However, when the existing vortex incinerator is used for treating waste gas containing fluorine and chlorine, the waste gas and the waste liquid are incinerated simultaneously, so that the defects of insufficient mixing, easy generation of harmful incomplete combustion products, influence on the safety of the operation of the incinerator and the like exist.
In addition, the flue gas that current burning furnace burns the production need let in follow-up treatment facility and carry out further processing, but the flue gas velocity of flow is fast, easily leads to the fact the impact to follow-up equipment, influences its life, causes unnecessary loss.
Disclosure of Invention
An object of the utility model is to overcome the not enough of above-mentioned technique, provide an improved generation vortex type fluorine chlorine waste liquid waste gas burns burning furnace, solved waste gas waste liquid mix abundant even and influence combustion efficiency's problem inadequately, and can effectively reduce the export flue gas velocity of flow, reduce the loss of follow-up equipment.
In order to realize the purpose of the utility model, the utility model adopts the technical scheme that: an improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator comprises a furnace body with a hollow furnace chamber, and is characterized in that a waste gas inlet, an air inlet and an atomizing spray gun externally connected with a waste liquid pipeline are arranged at the upper part of the furnace body along the tangential direction of the furnace chamber, an arc-shaped baffle is installed in the furnace chamber, a mist guide channel is formed between the arc-shaped baffle and the inner wall of the furnace body, the mist guide channel is of a gradually-expanding structure along the mist outlet direction of the atomizing spray gun, and a mist outlet of the atomizing spray gun is positioned between the arc-shaped baffle and the inner wall of; an auxiliary burner for spraying fire into the furnace cavity is arranged on one side wall of the furnace body, a layer of rectifying grating is arranged in the furnace body, and the auxiliary burner and the rectifying grating are positioned below the waste gas inlet, the air inlet and the atomizing spray gun; a flue gas outlet is formed in one side of the lower part of the furnace body, and a waste residue outlet is formed in the bottom of the furnace body; a circular truncated cone-shaped baffle is installed in the furnace body, and the large opening end of the circular truncated cone-shaped baffle covers the flue gas outlet.
Furthermore, the waste gas inlet, the air inlet and the atomizing spray gun are positioned on the same horizontal plane and are uniformly distributed at intervals along the periphery of the furnace body.
Furthermore, the side walls of the upper part, the middle part and the lower part of the furnace body are respectively provided with a temperature monitoring port, so that the burning condition in the furnace body can be observed at any time.
Furthermore, the atomizing spray guns are provided with two groups which are distributed up and down.
Furthermore, the waste residue outlet is of a conical structure with a large top and a small bottom, so that slag can be discharged conveniently.
Furthermore, the auxiliary burner is provided with two groups which are distributed up and down.
Further, the flow straightening grid is located between two sets of auxiliary burners.
The utility model has the advantages that: the waste gas, the air and the waste liquid are fed into the furnace chamber by adopting a tangential feeding design, a flame cylinder can be formed in the furnace chamber and is spirally discharged from a flue gas outlet at one side of the lower part, the waste gas and the waste liquid can be fully and uniformly mixed with air for combustion assistance in the spiral process and can be completely combusted, the heat retention time is also prolonged due to the existence of the flame cylinder, the waste heat effect is utilized, the waste liquid and the waste gas are completely decomposed, and meanwhile, the energy consumption is saved, and the furnace is economical and practical; meanwhile, the rectification grating is adopted, so that the smoke is uniformly distributed, the flow velocity of a smoke outlet can be effectively reduced by using the truncated cone-shaped baffle, the loss of subsequent equipment is reduced, and the service life is prolonged.
Drawings
Fig. 1 is a front view of the present invention.
Fig. 2 is a top view of the present invention.
In the figure: the device comprises a furnace body 1, a waste gas inlet 2, an air inlet 3, a waste liquid pipeline 4, an atomizing spray gun 5, an arc-shaped baffle 6, an auxiliary burner 7, a flue gas outlet 8, a waste residue outlet 9, a temperature monitoring port 10, a mist guide channel 11, a rectifying grid 12 and a truncated cone-shaped baffle 13.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings.
Example 1
As shown in fig. 1-2, an improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator comprises a furnace body 1 with a hollow furnace chamber, wherein a waste gas inlet 2, an air inlet 3 and an atomizing spray gun 5 externally connected with a waste liquid pipeline 4 are arranged at the upper part of the furnace body 1 along the tangential direction of the furnace chamber, an arc-shaped baffle 6 is installed in the furnace chamber, a mist guide channel 11 is formed between the arc-shaped baffle 6 and the inner wall of the furnace body 1, the mist guide channel 11 is in a gradually expanding structure along the mist outlet direction of the atomizing spray gun 5, and a mist outlet of the atomizing spray gun 5 is positioned between the arc-shaped baffle 6 and the inner; an auxiliary burner 7 for spraying fire into the furnace cavity is arranged on one side wall of the furnace body 1, a layer of rectifying grating 12 is arranged in the furnace body 1, and the auxiliary burner 7 and the rectifying grating 12 are positioned below the waste gas inlet 2, the air inlet 3 and the atomizing spray gun 5; a flue gas outlet 8 is formed in one side of the lower part of the furnace body 1, and a waste residue outlet 9 is formed in the bottom of the furnace body; a truncated cone-shaped baffle 13 is arranged in the furnace body 1, and the large opening end of the truncated cone-shaped baffle 13 covers the flue gas outlet 8; the waste gas inlet 2, the air inlet 3 and the atomizing spray gun 5 are positioned on the same horizontal plane and are uniformly distributed along the periphery of the furnace body 1 at intervals; temperature monitoring ports 10 are respectively arranged on the side walls of the upper part, the middle part and the lower part of the furnace body 1, so that the burning condition in the furnace body 1 can be observed at any time; the atomizing spray guns 5 are provided with two groups which are distributed up and down; the waste residue outlet 9 is of a conical structure with a large upper part and a small lower part, so that slag can be discharged conveniently; the auxiliary burners 7 are provided with two groups which are distributed up and down; the rectifying grid 12 is located between the two groups of auxiliary burners 7.
The described embodiments are only some, but not all embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

Claims (7)

1. An improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator comprises a furnace body with a hollow furnace chamber, and is characterized in that a waste gas inlet, an air inlet and an atomizing spray gun externally connected with a waste liquid pipeline are arranged at the upper part of the furnace body along the tangential direction of the furnace chamber, an arc-shaped baffle is installed in the furnace chamber, a mist guide channel is formed between the arc-shaped baffle and the inner wall of the furnace body, the mist guide channel is of a gradually-expanding structure along the mist outlet direction of the atomizing spray gun, and a mist outlet of the atomizing spray gun is positioned between the arc-shaped baffle and the inner wall of; an auxiliary burner for spraying fire into the furnace cavity is arranged on one side wall of the furnace body, a layer of rectifying grating is arranged in the furnace body, and the auxiliary burner and the rectifying grating are positioned below the waste gas inlet, the air inlet and the atomizing spray gun; a flue gas outlet is formed in one side of the lower part of the furnace body, and a waste residue outlet is formed in the bottom of the furnace body; a circular truncated cone-shaped baffle is installed in the furnace body, and the large opening end of the circular truncated cone-shaped baffle covers the flue gas outlet.
2. The improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator according to claim 1, wherein said waste gas inlet, air inlet and atomizing spray gun are located on the same horizontal plane and are uniformly spaced along the periphery of the incinerator body.
3. The improved vortex type incinerator for waste liquid and gas containing fluorine and chlorine according to claim 1, wherein temperature monitoring ports are respectively arranged on the side walls of the upper, middle and lower parts of the incinerator body, so that the incineration conditions in the incinerator body can be observed at any time.
4. The improved vortex type waste liquid and gas incinerator containing fluorine and chlorine as claimed in claim 1, wherein said spray lances are provided in two groups which are distributed up and down.
5. The improved vortex type fluorine-chlorine-containing waste liquid and gas incinerator according to claim 1, wherein said waste residue outlet is a tapered structure with a large top and a small bottom for facilitating slag discharge.
6. The improved vortex type waste fluorine-containing chlorine gas incinerator according to claim 1, wherein said auxiliary burners are arranged in two groups distributed up and down.
7. The improved vortex type waste fluorine-containing chlorine gas incinerator according to claim 6, wherein said rectifying grid is located between two sets of auxiliary burners.
CN202021218624.8U 2020-06-29 2020-06-29 Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator Expired - Fee Related CN212719772U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202021218624.8U CN212719772U (en) 2020-06-29 2020-06-29 Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202021218624.8U CN212719772U (en) 2020-06-29 2020-06-29 Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator

Publications (1)

Publication Number Publication Date
CN212719772U true CN212719772U (en) 2021-03-16

Family

ID=74962634

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202021218624.8U Expired - Fee Related CN212719772U (en) 2020-06-29 2020-06-29 Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator

Country Status (1)

Country Link
CN (1) CN212719772U (en)

Similar Documents

Publication Publication Date Title
CN102644922B (en) Incineration treatment device for nitrogen-containing organic wastes and incineration treatment process
CN106402905B (en) A kind of fractional combustion flare tip device
CN201827897U (en) Environment-friendly chemical saliferous waste water incinerator
CN103836632A (en) Waste adhesive incineration disposal device
CN102605136A (en) Soft sealing device for converter mouth and fume hood
CN212719772U (en) Improved vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator
CN203131843U (en) Waste gas burning device
CN218510911U (en) High-concentration salt-containing waste liquid incinerator
CN212777390U (en) Vortex type fluorine-chlorine-containing waste liquid and waste gas incinerator
CN110296433A (en) Combustion chamber high temperature burning zone temprature control method and device
CN207527602U (en) A kind of burner for handling High water cut low heat value organic wastewater
CN102798129B (en) Efficient thermal oxidation furnace for low afterburning-amount smoke constant-speed grading reaction
CN206904987U (en) A kind of three wastes comprehensive incinerator
CN203464291U (en) Burning device for processing waste gas and waste liquid in methionine process production
CN213983592U (en) Sludge waste liquid spray gun combustor
CN208871646U (en) A kind of sulfur recovery facility tail gas burning furnace
CN204141592U (en) A kind of incinerator processing solid waste liquid
CN113881460A (en) Multi-arc plasma gasification furnace
CN210638010U (en) Steam supply boiler
CN106949485A (en) A kind of environmental protection and energy saving incinerator
CN205710615U (en) The pulverized coal gasification furnace that a kind of preheated air enters with eddy flow
CN214664477U (en) High-temperature air burner system for waste heat type solid waste treatment device
CN218787561U (en) Waste gas incinerator capable of treating waste rubber
CN110657437A (en) Multiple whirl waste gas waste liquid combustor
CN208967806U (en) A kind of waste gas and waste liquid burner

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20210316