CN206444985U - Offal treatment reutilization system - Google Patents

Abstract

The utility model discloses a kind of offal treatment reutilization system, the system handles solid waste and liquid debris by solid and liquid debris crematory system, and harmful dust-collector and bottom ash produced by after incineration are handled using high Warm Melt processing system with output melting regenerative granular material, recycle the harmless dust-collector and bottom ash that incinerate output and melting regenerative granular material, output high pressure concrete product or other cement products are processed through cement products system, and the waste heat energy produced by the waste combustion processing system is linked to cogeneration system with output steam and electric power, whereby, output steam while enterprise's waste disposal issues are solved, electric power, melt regenerative granular material, high pressure concrete product or other cement products, and then reach effect of changing rejected material to useful resource.

Description

Offal treatment reutilization system

Technical field

The utility model is related to a kind of offal treatment reutilization system, and more particularly to one kind can be by solid waste, liquid Body discarded object and hazardous industrial waste are after processing, and steam, electric power, melting regenerative granular material and high pressure concrete system is made in production The system of product or other cement products.

Background technology

Counted according to Ministry of Economic Affaris, the annual output value of domestic other cement products class products is grown to by 3,200,000,000 in 95 years yuan 5,200,000,000 yuan of 104 years, wherein, concrete brick product accounts for more than 50% ratio, and obvious concrete brick has been conventional at present One of construction material.Concrete brick primary raw material includes cement, natural pellet (such as sandstone) ... at this stage, because sandstone is day Right product, and TaiWan, China various regions sandstone is because of relation that geology is distributed thus source rock is different, in addition, in the sand of wet season or dry season Stone quality is also variant, therefore, and sandstone product cut size levels at different levels differ with distribution with fineness, cause sandstone to originate and matter Amount is unstable.

In addition, rapid economic development causes the exhaustive exploitation and discarded object of natural resources growing day by day, particularly textile industry, The enterprise such as photoelectric panel industry and paper-making industry is in the solid waste produced by procedure for producing, semiconductor Ye Deng enterprises in procedure for producing Produced liquid debris and other industries are in the hazardous industrial waste produced by procedure for producing, and current government is except product Pole is promoted outside Sources decreasing, is also directed to recycling of recycling the waste, it is desirable to by dealing carefully with technology, reaches reduction discarded The purpose of produce output.And in recent years, with the renewal of public work specification, change blast furnace stone, combustion matchmaker's generating flying dust etc. Composition and the close industrial process discarded object of cement are learned, is gradually used to replace natural pellet, therefore, the present inventor endeavours While how thinking is in demand of the reduction to environment natural resources, flying ash of incinerators, the final place of bottom ash are effectively solved Problem is put, and can stable raw material quality, the not enough awkward situation of the domestic processing of trade waste at this stage energy of releiving.

Utility model content

It is unstable in view of the primary raw material quality for making concrete brick at this stage, and each industry is produced by procedure for producing Offal treatment energy it is not enough, and the missing still having much room for improvement.

Therefore, the purpose of this utility model is by solid waste combustion processing system, liquid debris incineration After reason system and high Warm Melt processing system processing solid waste, liquid debris and hazardous industrial waste, it will be produced It is high pressure concrete brick or other cement products that raw bottom ash, dust-collector are recycled through cement products system, and can be by discarded object Waste heat energy connection cogeneration system produced by crematory system is supplied in factory outside personal and factory with producing steam and electric power Sale, so as to output high pressure concrete brick or other cement products while enterprise's waste disposal issues are solved.

To reach object defined above, the utility model provides a kind of offal treatment reutilization system, and system Bao Han ︰ mono- consolidate Body waste combustion processing system, to handle comprising the general industry discarded object except sludge class and sludge class, the sludge class The general industry discarded object that general industry discarded object is dried for dewatered sludge except sludge class through sludge drying apparatus is set through broken It is standby to carry out after crushing, pre-treatment is carried out by separation equipment and carried out by feeding apparatus into solid waste combustion processing equipment As the raw material needed for cement products equipment or importing after produced harmless bottom ash can be crushed through jaw crusher after incineration, and incineration High Warm Melt processing equipment carries out incineration process, and the waste gas produced by after incinerating then sequentially enters the non-catalyst of first choice Reduce denitrating system (SNCR), whirlwind separator, precipitator, first choice media reductive denitrating system (SCR), work Property carbon adsorption equipment, the first bag collector and scrubbing tower, and having precipitator and the first bag collector output Evil dust-collector imports high Warm Melt processing equipment, the waste gas after processing is emitted into air, and passes through cyclone type point Used heat from device is reclaimed by the first boiler heat-exchange apparatus, and the high-temperature steam feeding steam-electric accreting of institute's output is set It is standby, and the middle temperature waste gas by first choice media reductive denitrating system (SCR) is heated in advance with extraneous air system by air Hot equipment carries out indirectly heat, and the preheated air of institute's output is sent into solid waste combustion processing equipment, the solid is given up Gurry incineration process equipment can carry out incineration burning with preheated air and outer solid, liquid or gaseous fuel；One liquid waste Thing crematory system, to treatment liquid discarded object, the liquid debris is given up after pre-treatment by apparatus for feeding into liquid Gurry incineration process equipment is incinerated, and harmful bottom ash produced by after incineration is imported into high Warm Melt processing equipment, and Waste gas produced by after incineration then sequentially enters the second non-media reductive denitrating system (SNCR) of selectivity, the second selective catalyst Reduce denitrating system (SCR), active carbon adsorption equipment, the second bag collector and the scrubbing tower, and by the second pocket type dust Harmful dust-collector of device output imports high Warm Melt processing equipment, the waste gas after processing is emitted into air, and warp The used heat for crossing the second non-media reductive denitrating system (SNCR) of selectivity is reclaimed by the second boiler heat-exchange apparatus, and will The high-temperature steam feeding steam-electric accreting equipment of institute's output；One high Warm Melt processing system, to handle hazardous industrial waste, The bottom ash and dust-collector of solid waste combustion processing system and liquid debris crematory system, and melting tail gas is imported Liquid debris incineration process equipment, and then water quenching melts regenerative granular material to fused mass with output；One cogeneration system, comprising even The steam-electric accreting equipment of pure water equipment is connected to, to reclaim the first boiler heat-exchange apparatus and the second boiler heat-exchange apparatus High-temperature steam, and used in being converted into after Low Temperature Steam for the sludge drying apparatus in factory, steam curing room, flue gas heater, And use the boiler blow-down water of institute's output for the first boiler heat-exchange apparatus and the second boiler heat-exchange apparatus；And a water Mud product system, the fused mass of the high Warm Melt processing system, the incinerator bottom slag of solid waste combustion processing system with After useless fire proofed wood is handled through jaw crusher, puddled and be press-formed into mould by cement products equipment with existing raw material, and supported through steam After raw room health processing output high pressure concrete product or mold forming is filled with the other cement products of output after puddling.

Brief description of the drawings

Fig. 1 is the Organization Chart of the utility model system；

Fig. 2 is the flow chart of the utility model system.

1 offal treatment reutilization system

20 solid waste combustion processing systems

200 solid waste combustion processing equipments

201 sludge storage facilities

202 sludge drying apparatus

203 disintegrating apparatus

204 separation equipments

205 feeding apparatus

The non-media reductive denitrating system (SNCR) of 206 first choices

207 whirlwind separators

208 precipitators

209 first choice media reductive denitrating systems (SCR)

210 first bag collectors

211 first boiler heat-exchange apparatus

212 air heat pre-heating device

213 scrubbing towers

30 liquid debris crematory systems

300 liquid debris incineration process equipment

301 solvent slop storage facilities

302 apparatuss for feeding

The 303 second non-media reductive denitrating systems (SNCR) of selectivity

304 second boiler heat-exchange apparatus

305 second selective media reductive denitrating systems (SCR)

306 second bag collectors

40 high Warm Melt processing systems

400 high Warm Melt processing equipments

50 cogeneration systems

500 steam-electric accreting equipment

501 pure water equipments

502 flue gas heaters

60 cement products systems

600 cement products equipment

601 jaw crushers

602 steam curing rooms

A solid waste

A-1 general industries discarded object (sludge class)

A-1-1 dewatered sludges

A-1-2 wet muds

A-2 general industries discarded object (except sludge class)

B liquid debris

C hazardous industrial wastes

The harmless bottom ash of D-1

D-2 is harmful to bottom ash

F active carbon adsorption equipment

G steam

H air

I-1 solids, liquid or gaseous fuel

I-2 liquid or gaseous fuel

The harmless dust-collectors of J-1

J-2 is harmful to dust-collector

K melts tail gas

L melts regenerative granular material

M electric power

O running water

P condensed waters

Q gives up fire proofed wood

The existing raw materials of R

S high pressure concretes product or other cement products

T fused mass

Embodiment

To make skilled in the art realises that the utility model is intended to reached purpose technology, means and effect for being used, under Face will coordinate schema, enumerate a preferred embodiment, and describe Ru Hou ︰ in detail

First, refer to Fig. 1 and coordinate shown in Fig. 2, the offal treatment reutilization system 1 is burnt comprising a solid waste Change processing system 20, a liquid debris crematory system 30, a high Warm Melt processing system 40, a cogeneration system 50 and a cement products system 60.And Industry Waste of the solid waste combustion processing system 20 to handle solid waste A Gurry (sludge class) A-1 and trade waste (except sludge class) A-2, and it is linked to high Warm Melt processing system 40, vapour Electric cogeneration system 50 and cement products system 60, in an embodiment of the present utility model, trade waste (the sludge class) A- 1 includes Organic sludge, inorganic nature sludge, non-harmful greasy filth, mud mixture, slurry paper sludge, weaving sludge one or its group Close, the useless tree of solid-states of trade waste (except the sludge class) A-2 comprising waste ion-exchang resin, in addition to waste ion-exchang resin Fat, waste plastic mixture, scrap rubber mixture, culled wood pallet, culled wood mixture, useless dust arrester filter bag one or its group Close；Liquid debris crematory system 30 be used to treatment liquid discarded object B, and be linked to high Warm Melt processing system 40 and Cogeneration system 50, in an embodiment of the present utility model, liquid debris B is comprising useless in addition to waste ion-exchang resin Resin, non-harmful organic liquid waste or solvent slop, non-harmful mixed waste liquor, waste oil mixture, useless medicine, arsenic and its compound its One or its combination；High Warm Melt processing system 40 is to handle hazardous industrial waste C and be handled through solid waste combustion The bottom ash produced after being handled with liquid debris crematory system 30 of system 20 and dust-collector, it is real in of the present utility model one Apply in example, and hazardous industrial waste C is included using the dust-collector produced by heat treating process processing hazardous industrial waste, waste material Reclaim the residue produced or sludge, the wastewater treatment sludge of electroplating process, arsenic and its compound, copper and its compound, the copper And its compound only limits Induction refining, dust-collector, waste liquid, sludge, filter material, incinerated flying ash or bottom ash.

Secondly, please referring still to shown in Fig. 1~2, solid waste A trade waste (sludge class) A-1 deposits in dirt Mud storage facility 201, wherein, it is aqueous that wet mud A-1-2, which need to be introduced into sludge drying apparatus 202 using steam heating, drying, Rate is less than 60% dry sludge A -1-1, and trade waste (except sludge class) A-2 need to be introduced into disintegrating apparatus 203 and handle Afterwards, dry sludge A -1-1 and trade waste (except sludge class) A-2 is entered separation equipment 204 and carry out pre-treatment and by throwing Material equipment 205 enters solid waste combustion processing equipment 200 and incinerated, in an embodiment of the present utility model, solid Waste combustion processing equipment 200 is cyclone type incinerator, vertical fluidized pool furnace, horizontal type fluidized-bed stove or cyclone type fluid bed Stove；And harmless bottom ash D-1 produced after incineration is imported into high Warm Melt processing equipment 400 or led after jaw crusher 601 Enter cement products equipment 600.And the waste gas produced by after incinerating contains shot-like particle, oxysulfide, nitrogen oxides, lead, cadmium, mercury etc. Heavy metal and dioxin, therefore need to sequentially enter the non-media reductive denitrating system (SNCR) 206 of first choice, whirlwind separator 207th, precipitator 208, the bag collector 210 of first choice media reductive denitrating system (SCR) 209, first and wash Wash tower 213, make waste gas by the non-media reductive denitrating system (SNCR) 206 of first choice by nitrogen oxides be converted to nitrogen and After water, the particulate contaminant of different-grain diameter is removed using whirlwind separator 207 and precipitator 208, and by harmless dust Grey J-1 (harmless high temperature ash) can import high Warm Melt processing equipment 400 and melt processing or as cement products according to its demand Raw material needed for equipment 600, remaining waste gas passes through first choice media reductive denitrating system (SCR) 209 to be catalyzed by means of catalyst Nitrogen oxides in waste gas is converted to nitrogen and water by effect again, and in by active carbon adsorption equipment F, such as fixed absorption Bed, spraying apparatus etc., to adsorb the dioxin and other compounds in waste gas, then, are filtered by the first bag collector 210 The activated carbon after being adsorbed is collected, then harmful dust-collector J-2 (harmful Low Temperature Ash) is imported into high Warm Melt processing equipment 400 burn, and remaining harmless exhaust gases enables waste gas to be emitted into after scrubbing tower 213 carries out desulfurization carrying out washing treatment with liquid caustic soda In air, and the waste water of scrubbing tower 213 is then disposed by sewage treatment equipment.In addition, in whirlwind separator 207 and electrostatic Between dust arrester 208 be provided with the first boiler heat-exchange apparatus 211, in first choice media reductive denitrating system (SCR) 209 with Pre-heating device 212 is heated provided with air between first bag collector 210, makes the middle temperature used heat by whirlwind separator 207 It can be reclaimed by the first boiler heat-exchange apparatus 211, and the high-temperature steam G of institute's output is sent into steam-electric accreting equipment 500, And extraneous air H can then be heated pre-heating device 212 by air and carry out indirectly heat, and the preheated air H of institute's output is sent into Solid waste combustion processing equipment 200, enable solid waste combustion processing equipment 200 with preheated air H and outer solid, Liquid or gaseous fuel I-1 are the burning energy.

Liquid debris B systems deposit in solvent slop storage facility 301, and are entered in after pre-treatment by apparatus for feeding 302 Liquid debris incineration process equipment 300 is incinerated, and harmful bottom ash D-2 produced by after incineration is imported into high temperature hot melt Melt processing equipment 400 to burn, because liquid debris incineration process equipment 300 is with outside liquid or gaseous fuel I-2, outer Portion air H, the escaping gas or gas with foreign flavor extracted out by solvent slop storage facility 301 and high Warm Melt processing equipment 400 melting tail gas K is the burning energy, therefore, and the weight such as shot-like particle, oxysulfide, nitrogen oxides, lead, cadmium, mercury is contained in waste gas Metal and dioxin, therefore the waste gas produced by after incinerating need to sequentially enter the second non-media reductive denitrating system (SNCR) of selectivity 303rd, second 304, second selective media reductive denitrating system (SCR) 305, second bag collector 30 of boiler heat-exchange apparatus 6 and scrubbing tower 213, waste gas is carried out preliminary denitration work by the second non-media reductive denitrating system (SNCR) 303 of selectivity Industry, and carry out Waste Heat Recovery to reduce EGT by the second boiler heat-exchange apparatus 304, then by the high-temperature steam of institute's output G feeding steam-electric accretings equipment 500, then, is catalyzed using the second selective media reductive denitrating system (SCR) 305 and by catalyst Effect is with ammoniacal liquor nitrogen oxides reduction, and the waste gas after denitration is in by active carbon adsorption equipment F, such as fixed adsorbent bed, spray Mist equipment etc., to adsorb after dioxin and other compounds in waste gas, progress is collected by filtration by the second bag collector 306 Activated carbon after absorption, then the high Warm Melt processing equipment 400 of harmful dust-collector J-2 (harmful Low Temperature Ash) importings is burnt, and Remaining harmless exhaust gases enables waste gas through smoke stack emission to air after scrubbing tower 213 carries out desulfurization carrying out washing treatment with liquid caustic soda In, and the waste water of scrubbing tower 213 is then disposed by sewage treatment equipment.

Hazardous industrial waste C is handled by high Warm Melt processing equipment 400, is implemented in of the present utility model one Example in, high Warm Melt processing equipment 400 be electric arc furnaces, plasma-based melting furnace, resistance melting furnace, lure electrical heating melting furnace, revolution Melt surface stove, internal combustion fixation surface melting furnace, flux melting furnace, coke beds shaft furnace inner molten stove one or its Combination；Hazardous industrial waste C is set, under the operating environment of anaerobic, to utilize high-temperature fusion through high Warm Melt processing system 400 Organic cracking contained in above-mentioned discarded object is micro-molecular gas by technology, then by the melting tail gas produced by operation K imports liquid debris incineration process equipment 300 and carries out aerobic burning to remove chemical toxicity, and after above-mentioned offal treatment Fused mass T in contained inorganic moieties enter jaw crusher 601, another part is then melted as liquid, is then converted into lava, and Vitrified water quenching melting regenerative granular material L is produced using water quenching method when molten slurry discharge, and melting regenerative granular material L can directly work as Commodity are in cement products equipment 600 in sale outside factory, or importing factory for high pressure concrete product or other cement products S processing procedure Use.

Cogeneration system 50 includes the steam-electric accreting equipment 500 for being connected with pure water equipment 501, and the first boiler is reclaimed in decapacitation Outside the high-temperature steam G of the boiler heat-exchange apparatus 304 of heat-exchange apparatus 211 and second, moreover it is possible to be converted into low temperature in high-temperature steam G and steam After vapour G, directly work as commodity in sale outside factory, or import in factory for sludge drying apparatus 202, steam curing room 602, flue gas Device 502 is used, and is available for selling or provide outside factory the electric power M that uses of each system in factory while producing, and by steam-electric accreting equipment 500 The boiler blow-down water P of institute's output is used for the first boiler heat-exchange apparatus 211 and the second boiler heat-exchange apparatus 304.And pure water Equipment 501 is with outside running water O, the clean steam condensate (SC) P of 202 outputs of sludge drying apparatus and by steam-electric accreting The Low Temperature Steam G of the output of equipment 500 steam condensate (SC) P of institute's output after the heating of flue gas heater 502 originate for supply.

And through high Warm Melt processing equipment 400 handle after fused mass T, through solid waste combustion processing equipment 200 Harmless bottom ash D-1 and useless fire proofed wood Q after incineration can make water in entering cement products system 60 after the processing of jaw crusher 601 Mud product equipment 600 is in the existing raw material R of addition (the useless dust-collector of such as cement, natural pellet, toner, non-harmful or its mixture ... Deng) and water, puddle into mould extrusion forming after allotment ratio, and output high pressure concrete after being handled through the health of steam curing room 602 Product, or mold forming is filled after puddling with the other cement products of output, wherein, high pressure concrete product is comprising chain high pressure Brick, grass-planting brick, hollow brick, continent common brick, floor tile and building block ... etc., and other cement products comprising plate, watt, pipe, case and Wave-dissipating block ... etc., for enclosure wall, waterfront or hillside bank protection, parking place, people's row or garage's water permeable pavement, kerbstone, wave absorption Block and sewage pipe ..., which are waited, to be used.

Therefore following Gong Xiao ︰ obviously can be reached using offal treatment reutilization system of the present utility model

1. offal treatment reutilization system of the present utility model passes through solid waste combustion processing system and liquid respectively Body waste combustion processing system is located to handle solid waste and liquid debris using high Warm Melt processing system Manage the harmful or harmless bottom ash and dust of hazardous industrial waste, solid waste and liquid debris produced by after incineration Ash melts regenerative granular material with output, and the melting regenerative granular material can be directly when commodity outside factory in selling, or through cement products system Output high pressure concrete product or other cement products are processed, thereby output can while enterprise's waste disposal issues are solved Directly in the melting regenerative granular material, high pressure concrete product or other cement products sold outside factory, and then reach waste material Effect of change.

2. offal treatment reutilization system of the present utility model reclaims solid waste by setting cogeneration system The high-temperature steam of thing crematory system and liquid debris crematory system institute output, and in being converted into factory needed for processing procedure Steam while, output is available for the electric power that each system is used in factory, and will can be sold outside steam and electric power, to reduce the manufacturing Cost.

3. offal treatment reutilization system system of the present utility model is by solid waste, liquid debris and noxious industry Discarded object output after processing melts regenerative granular material, therefore can replace the natural pellet in part, reduces the need for environment natural resources The amount of asking and harm.

Embodiment described above, preferred embodiment only of the present utility model, is not limited to reality of the present utility model Scope is applied, all changes and modification without departing from carried out by the utility model technical spirit are all that the utility model the scope of the claims is contained Lid.

Claims (12)

1. a kind of offal treatment reutilization system, Bao Han ︰

One solid waste combustion processing system, is connected to high Warm Melt processing system, cogeneration system and cement system Strain is united, with bottom ash, high-temperature steam and the dust-collector produced by handling respectively after the solid waste combustion processing system is incinerated；

One liquid debris crematory system, is connected to the high Warm Melt processing system and the cogeneration system, to locate Manage the bottom ash and high-temperature steam produced by after the liquid debris crematory system is incinerated；

One high Warm Melt processing system, is connected to the solid waste combustion processing system, the liquid debris incineration process System and the cement products system, to melt the bottom ash and the dust-collector and raw material needed for providing the cement products system；

One cogeneration system, be connected to the solid waste combustion processing system, the liquid debris crematory system and The cement products system, to reclaim and convert the solid waste combustion processing system and the liquid debris incineration process system The high-temperature steam for output of uniting, and electric power needed for the cement products system is provided；And

One cement products system, is connected to the solid waste combustion processing system, the high Warm Melt processing system and the vapour Electric cogeneration system, to output high pressure concrete product or other cement products.

2. offal treatment reutilization system as claimed in claim 1, wherein, the solid waste combustion processing system is used to Processing includes the trade waste except sludge class and sludge class, and the solid waste combustion processing system includes solid waste Thing incineration process equipment, sludge storage facility, disintegrating apparatus, separation equipment, feeding apparatus, whirlwind separator, the first boiler Heat-exchange apparatus, precipitator, air heating pre-heating device, the first bag collector and scrubbing tower.

3. offal treatment reutilization system as claimed in claim 2, wherein, the sludge class trade waste includes Organic Sludge, inorganic nature sludge, non-harmful greasy filth, mud mixture, slurry paper sludge, weaving sludge one or its combination, and the sludge Trade waste except class is mixed comprising waste ion-exchang resin, the solid-state spent resin in addition to waste ion-exchang resin, waste plastics Compound, scrap rubber mixture, culled wood pallet, culled wood mixture, useless dust arrester filter bag one or its combination.

4. offal treatment reutilization system as claimed in claim 2, wherein, the solid waste combustion processing equipment is rotation Wind formula incinerator, vertical fluidized pool furnace, horizontal type fluidized-bed stove or cyclone type fluid bed furnace.

5. offal treatment reutilization system as claimed in claim 1, wherein, the liquid debris crematory system is used to Treatment liquid discarded object, and the liquid debris crematory system includes liquid debris incineration process equipment, solvent slop storage Cryopreservation device, apparatus for feeding, the second boiler heat-exchange apparatus, the second bag collector and scrubbing tower.

6. offal treatment reutilization system as claimed in claim 5, wherein, the liquid debris is included except useless ion exchange Spent resin, non-harmful organic liquid waste or solvent slop, non-harmful mixed waste liquor, waste oil mixture outside resin, useless medicine, arsenic and Its compound one or its combination.

7. offal treatment reutilization system as claimed in claim 1, wherein, the high Warm Melt processing system is used to handle The bottom ash and dust of hazardous industrial waste, the solid waste combustion processing system and the liquid debris crematory system Ash, and the high Warm Melt processing system includes high Warm Melt processing equipment.

8. offal treatment reutilization system as claimed in claim 7, wherein, the high Warm Melt processing equipment is electric arc Stove, plasma-based melting furnace, resistance melting furnace, lure electrical heating melting furnace, rotary surface melting furnace, internal combustion fixation surface melting Stove, flux melting furnace, coke beds shaft furnace inner molten stove one or its combination.

9. offal treatment reutilization system as claimed in claim 7, wherein, the hazardous industrial waste is included using at heat Residue or sludge, the waste water of electroplating process that dust-collector, waste recovery produced by logos processing hazardous industrial waste are produced Handle sludge, arsenic and its compound, copper and its compound, described copper and its compound only limit Induction refining, dust-collector, waste liquid, Sludge, filter material, incinerated flying ash or bottom ash.

10. offal treatment reutilization system as claimed in claim 1, wherein, the cogeneration system is pure comprising being connected with The steam-electric accreting equipment and flue gas heater of wetting system.

11. offal treatment reutilization system as claimed in claim 1, wherein, the cement products system includes cement products Equipment, jaw crusher and steam curing room.

12. offal treatment reutilization system as claimed in claim 1, wherein, the high pressure concrete product includes chain height Press floor tile, grass-planting brick, hollow brick, continent common brick, floor tile and building block, other cement products comprising plate, watt, pipe, case and disappear Ripple block.