CN215439680U - Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank - Google Patents

Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank Download PDF

Info

Publication number
CN215439680U
CN215439680U CN202121751744.9U CN202121751744U CN215439680U CN 215439680 U CN215439680 U CN 215439680U CN 202121751744 U CN202121751744 U CN 202121751744U CN 215439680 U CN215439680 U CN 215439680U
Authority
CN
China
Prior art keywords
section
sulfuric acid
dry
circulating
acid tank
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.)
Active
Application number
CN202121751744.9U
Other languages
Chinese (zh)
Inventor
王志强
杜子益
丁重云
栾喜波
王再光
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.)
Yantai City Jin'ao Environmental Protection Technology Co ltd
Original Assignee
Yantai City Jin'ao Environmental Protection 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 Yantai City Jin'ao Environmental Protection Technology Co ltd filed Critical Yantai City Jin'ao Environmental Protection Technology Co ltd
Priority to CN202121751744.9U priority Critical patent/CN215439680U/en
Application granted granted Critical
Publication of CN215439680U publication Critical patent/CN215439680U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The utility model discloses a dry-absorption workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, and relates to the field of dry absorption of sulfuric acid. The absorption tower is connected with a converter through a surface cooling pipe, the surface cooling pipe comprises a vertical ascending section and a vertical descending section, and the ascending section is connected with the descending section through an arc section. The traditional equipment is assisted, and the effect of reducing the temperature of sulfuric acid in the circulating acid tank is realized. Thereby realizing the effect of ensuring the quality of the sulfuric acid product.

Description

Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank
Technical Field
The utility model relates to the field of sulfuric acid dry absorption, in particular to a dry absorption section device for reducing the temperature of sulfuric acid in a circulating acid tank.
Background
Flue gas enters a purification, conversion and dry absorption section for acid production after passing through a bag-type dust collector, 93 percent or 98 percent concentrated sulfuric acid is produced, but the flue gas temperature is too high due to changes of ore feeding amount and process conditions in the process, the temperature of dry acid and acid absorption is very high, and all heat cannot be taken away only by cooling a circulating acid tank by a plate-type heat exchanger, so that qualified sulfuric acid products cannot be produced.
Disclosure of Invention
The utility model discloses a dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, which assists traditional equipment and realizes the effect of reducing the temperature of the sulfuric acid in the circulating acid tank. Thereby realizing the effect of ensuring the quality of the sulfuric acid product.
In order to realize the technical effect, the application discloses dry-absorption workshop section device for reducing sulfuric acid temperature in a circulating acid tank, including the first absorption tower that is connected with the circulating acid tank, first absorption tower passes through the cold union coupling of table with the converter, the cold pipe of table includes vertically ascending section and descending segment, ascending section and descending segment pass through the segmental arc and link to each other.
Furthermore, the ascending section, the descending section and the arc-shaped section are all tubular structures with circular sections, and the diameters of the sections are the same.
Furthermore, a spray head is arranged at the upper part of the first absorption tower, an acid outlet is arranged at the bottom of the first absorption tower, the spray head is connected with an outlet of the circulating acid tank, and the acid outlet is connected with an inlet of the circulating acid tank.
Furthermore, the meter cooling pipes are arranged in one or more numbers, and the meter cooling pipes are connected in series or in parallel.
Further, the surface cooling pipe is an iron pipe.
The beneficial effects of the utility model include:
through set up the cold pipe of table between converter and first order absorption tower, realize the natural heat dissipation through the cold pipe of table, cool down the flue gas in advance, reduce the temperature of flue gas, thereby reduce the temperature of flue gas when getting into the one-level absorption tower, the temperature that has reduced the circulation acid is more favorable to producing qualified sour product, the cold pipe simple manufacture of above-mentioned table, it is simple and convenient to change the step on the basis of former equipment, and later stage production need not management and maintenance, and does not consume the energy of electric energy or other forms.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It is obvious that the drawings in the following description are some embodiments of the utility model, and that for a person skilled in the art, other drawings can be derived from them without inventive effort.
FIG. 1 is a block diagram of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention. It is to be understood that the embodiments described are only a few embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The first embodiment is as follows:
the dry absorption section device for reducing the temperature of sulfuric acid in a circulating acid tank, as shown in figure 1, comprises a first absorption tower 2 connected with the circulating acid tank 1, wherein the first absorption tower is connected with a converter 3 through a surface cooling pipe 4, the surface cooling pipe comprises a vertical ascending section 41 and a vertical descending section 42, and the ascending section and the descending section are connected through an arc-shaped section 43.
Example two:
on the basis of the technical scheme of the first embodiment, the ascending section, the descending section and the arc-shaped section are all tubular structures with circular sections, and the diameters of all the sections are the same. The upper part of the first absorption tower is provided with a spray header 21, the bottom of the first absorption tower is provided with an acid outlet 22, the spray header is connected with an outlet of the circulating acid tank, and the acid outlet is connected with an inlet of the circulating acid tank. The surface cooling pipes are arranged in a plurality of numbers and are used in series. The surface cooling pipe is an iron pipe.
The above-mentioned embodiments are merely illustrative of the preferred embodiments of the present invention, and do not limit the scope of the present invention, and various modifications and improvements of the technical solution of the present invention by those skilled in the art without departing from the spirit of the present invention should fall within the protection scope defined by the claims of the present invention.

Claims (5)

1. A dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank is characterized in that: the absorption tower is characterized by comprising a first absorption tower (2) connected with a circulating acid tank (1), wherein the first absorption tower is connected with a converter (3) through a surface cooling pipe (4), the surface cooling pipe comprises a vertical ascending section (41) and a vertical descending section (42), and the ascending section and the descending section are connected through an arc-shaped section (43).
2. The dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, which is characterized in that: the ascending section, the descending section and the arc-shaped section are all tubular structures with circular sections, and the diameters of the sections are the same.
3. The dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, which is characterized in that: the upper part of the first absorption tower is provided with a spray header (21), the bottom of the first absorption tower is provided with an acid outlet (22), the spray header is connected with an outlet of the circulating acid tank, and the acid outlet is connected with an inlet of the circulating acid tank.
4. The dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, which is characterized in that: one or more surface cooling pipes are arranged, and the surface cooling pipes are connected in series or in parallel for use.
5. The dry-suction workshop section device for reducing the temperature of sulfuric acid in a circulating acid tank, which is characterized in that: the surface cooling pipe is an iron pipe.
CN202121751744.9U 2021-07-30 2021-07-30 Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank Active CN215439680U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202121751744.9U CN215439680U (en) 2021-07-30 2021-07-30 Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202121751744.9U CN215439680U (en) 2021-07-30 2021-07-30 Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank

Publications (1)

Publication Number Publication Date
CN215439680U true CN215439680U (en) 2022-01-07

Family

ID=79685615

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202121751744.9U Active CN215439680U (en) 2021-07-30 2021-07-30 Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank

Country Status (1)

Country Link
CN (1) CN215439680U (en)

Similar Documents

Publication Publication Date Title
WO2019019205A1 (en) Gas-gas high-temperature heat exchanger
CN215439680U (en) Dry-suction workshop section device for reducing temperature of sulfuric acid in circulating acid tank
CN201476626U (en) Tubular heat exchanger inside decomposer
CN201944825U (en) Flue gas and low temperature corrosion resistance heating medium coal economizer
CN201032405Y (en) Air condenser
CN203923124U (en) The wash-out benzene device washing oil recycle system
CN209588742U (en) A kind of hydrogen manufacturing condensation and generation device
CN202339122U (en) Gas cooling device
CN208955517U (en) A kind of dedusting radiator structure of electrical cabinet
CN208829265U (en) A kind of purification sulfur trioxide process units
CN111268653A (en) Energy-saving conversion device and process for preparing sulfuric acid from sulfur-containing flue gas
CN2524196Y (en) High performance anodic protecting shell concentrated sulfuric acid cooler
CN205299577U (en) Remove dioxin device
CN217083414U (en) Combined type cold-heat exchanger for sulfuric acid conversion
CN205300282U (en) Novel horizontal rapid cooling device
CN206055582U (en) A kind of synthesis ammonia plug-in type waste heat boiler
CN202382618U (en) Anodic-protection plate-and-shell acid cooler
CN203605202U (en) Efficient waste heat boiler
CN206113678U (en) Light oil schizolysis burner gas waste heat utilization equipment
CN202881132U (en) Crude naphthalene single-furnace and double-tower device
CN220170048U (en) System for improve polycrystalline silicon reduction tail gas and retrieve lean rich solution heat exchange
CN203479028U (en) Reformer device using product gas waste heat
CN215540718U (en) Reactor for small skid-mounted ammonia synthesis device
CN214693332U (en) Circulating water cooling device for dilute nitric acid by double-pressurization method
CN203513615U (en) Efficient combined type shift gas-semiwater gas heat exchanger

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant