Building on its phthalic anhydride process and downstream equipment capabilities, Tianjin Huabang also provides EPC-based engineering for phthalic anhydride-derived plasticizer production units, including the core reaction, finishing, storage, utility, and packaging sections. These projects are typically developed for clients requiring reliable esterification technology, consistent product quality, efficient heat management, and practical plant automation.
Pulse-Jet Cleaning Principle
Compressed air is released through pulse valves into the filter-bag system, rapidly expanding the bags and dislodging accumulated dust, ensuring stable, long-term operation.
Modular Filter-Bag Architecture
The HB-FMC family is organized in standardized bag-count increments, simplifying selection and scaling.
Stable Filtration Efficiency
The series is intended for high dust-removal efficiency in dry-service applications, with filtration performance dependent on media choice, air-to-cloth ratio, and process conditions.
Adaptable Discharge Arrangement
Depending on project need, the baghouse may be supplied with a hopper, butterfly valve, ash discharge, or screw-conveyor configuration.
Safety and Monitoring Options
The system may include differential-pressure monitoring, dust-concentration monitoring, an explosion-relief interface, and automatic pulse-sequence control.
Tianjin Huabang provides EPC-based tail-gas treatment packages for phthalic anhydride production units, integrating catalytic oxidation, heat recovery, process control, and utility integration into a complete engineered environmental and energy-recovery system. This package is not treated as an isolated add-on, but as an essential process-support unit that must operate in balance with the main PA plant.
Huabang supplies catalytic oxidation units utilizing BASF catalysts and affirms its position as the exclusive equipment partner with BASF in Asia Pacific for PA tail-gas catalysts, having jointly delivered over 20 units to date.
The PA tail-gas EPC basis can include:
The esterification section must maintain stable stoichiometry, residence time, and temperature profile to achieve high conversion and consistent acid value. Reactor design, agitation, heat transfer, and alcohol circulation all strongly influence final product quality.
Because esterification is an equilibrium-limited process, efficient removal of reaction water is essential. The EPC basis, therefore, places strong emphasis on overhead condensation, phase separation, reflux control, and, where applicable, vacuum-assisted finishing.
Plasticizer production is heat-intensive but highly amenable to optimization. Integrated heating, condensation, and cooling utility design can improve both operating cost and product stability.
The plant must manage combustible organics, hot liquids, and esterification off-gas in a controlled way. Vent recovery, scrubbers, condensers, flame-safe routing, and electrical-area classification are therefore part of the engineering basis.

Huabang can develop the reactor train around jacketed or coil-equipped vessels, selected agitation patterns, staged feed logic, and controlled overhead removal. Reactor sizing and internals are adapted to the conversion target, viscosity profile, and selected alcohol system.
The overhead system may include a condenser, a phase separator, a reflux arrangement, and a water draw-off logic to maintain reaction progress and protect product quality.
Where lower residual volatiles, better odor profile, or higher product stability are required, the line can incorporate vacuum finishing, stripping, and polishing steps.
The EPC basis includes alcohol storage, intermediate circulation, finished-product tankage, pumping and loading arrangements with instrumentation and interlocks.
The package can incorporate scrubbers, condensers, and VOC management sections for reactor vents, tank breathing, and product finishing services.

The core duty is stable destruction of VOCs and CO without introducing excessive pressure drop or causing catalyst damage under changing gas composition.
Where tail-gas composition permits, the oxidation section can be designed to recover sufficient reaction heat to support steam generation and reduce net utility burden.
Tail-gas units must handle warm-up, low-load operation, and composition fluctuation without thermal shock or unstable reactor conditions. Start-up heaters, bypasses, and interlocks are therefore part of the engineering basis.
Temperature control, contaminant management, flow distribution, and emergency logic must all be designed to extend catalyst life and avoid overheating or localized hot spots.
The tail-gas unit must be engineered so it does not disturb upstream oxidation and recovery sections. Hydraulic balance, backpressure stability, and control logic are therefore essential.
The reactor section is engineered around catalyst performance, gas distribution, thermal uniformity, and maintainability.
Recovered heat can be directed into steam generation and utility integration, turning the environmental unit into an energy-contributing process asset.
Multi-point monitoring and interlocks are used to manage bed temperature, protect the catalyst, and maintain a safe operating range.
The package can be delivered with process, mechanical, piping, electrical, automation, and structural scopes on a coordinated-execution basis.
Huabang provides EPC and process-package capabilities for fumaric acid production units, including reaction, conversion, concentration, crystallization support, evaporation, solids finishing, and utility integration. In these projects, the engineering challenge extends beyond equipment supply; it lies in integrating liquid-phase process control, impurity management, evaporation efficiency, and downstream solid handling into a stable, cost-effective plant design.
The fumaric-acid EPC basis can include:
Evaporation and Concentration Efficiency
Fumaric-acid projects often depend heavily on the economics and operability of the evaporation section. The number of stages, recirculation logic, and fouling tolerance must be balanced against utility cost and capital cost.
Crystallization and Solid Recovery
Downstream recovery must be engineered to obtain product yield, manageable crystal habit, and practical separation performance without excessive fines generation.
Impurity and Product-Grade Control
Product quality may be affected by metal ions, color bodies, organic carryover, and impurities from recycling. The process basis, therefore, includes impurity-path analysis and purge / polishing logic where needed.
Liquor Handling and Fouling Management
Because fumaric-acid systems can be solids-forming and concentration-sensitive, line routing, circulation rate, and cleaning philosophy are important parts of the EPC scope.
Downstream Dry Solids Integration
Drying, cooling, conveying, and packaging must be matched to the product’s crystalline behavior and the final customer specifications.
Integrated Crystallization and Separation Basis
The process package can include the interface between concentration, crystallization, solid recovery, and recycle balance rather than treating each section independently.
Impurity-Control Engineering
The EPC basis can incorporate feed-quality control, metallurgy selection, filtration logic, and purge strategy to protect final product quality.
Strong Solids-Handling Continuity
The line can extend directly into cooling, conveying, and packaging for a complete production-to-dispatch route.

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