Why 2026 Is Different for San Antonio Resort Wastewater
San Antonio sits directly on the Edwards Aquifer, the sole-source drinking water supply for roughly 1.7 million Bexar County residents, and every resort wastewater decision in 2026 is filtered through that fact. Properties inside the recharge zone — the Hill Country, La Cantera, Fiesta Texas, Boerne, New Braunfels fringe — fall under Edwards Aquifer Authority rules (30 TAC §213), which prohibit surface discharge of treated wastewater and force disposal toward subsurface drip or irrigation with disinfection to <14 cfu/100 mL fecal coliform. Post-2024 TCEQ enforcement has tightened operator-licensing and reuse reporting, so older resort lagoons and septic systems that operated under grandfathered permits are under mounting inspection pressure (per TCEQ enforcement updates, 2025-Q4). At the same time, Hill Country occupancy has rebounded and the asset class has shifted: a property like the Signia by Hilton La Cantera Resort & Spa runs 5 outdoor pools, water slides, a full-service spa, and banquet kitchens, generating kitchen FOG, pool filter backwash, and laundry streams that a legacy septic system sized for 1990s occupancies cannot handle. The 200-room resort of 2026 is not the 200-room resort of 2005 — the peak-season FOG and TSS load on the treatment plant can swing 3× between a January weekday and a July conference week.
San Antonio Hotel Wastewater Characteristics and Design Flow
Resort influent in Central Texas typically runs BOD 200–400 mg/L, TSS 150–300 mg/L, FOG 50–150 mg/L, with elevated chlorides when pool backwash is blended into the same drain. The Texas resort design basis is 100–130 gallons per capita per day (gpcd); for a 200-room Hill Country property at 2.5 occupants per occupied room, that translates to 55,000 gpd average daily flow (≈208 m³/day). Diurnal peaking driven by morning housekeeping turnover and simultaneous banquet turnover multiplies the instantaneous hydraulic load by 2.0–2.5×, pushing peak flow to roughly 520 m³/day on the worst morning shift. Add 10–20% contingency when spa, pool filter backwash, and commercial laundry are routed to the same plant — high-end Hill Country resorts can push that contingency toward 25% during summer pool season. The gpcd number and peaking factor together define the influent specification the engineer hands to the equipment vendor: average flow, peak flow, peak BOD loading (kg/day), and peak FOG loading. Skip this step and the rest of the design — reactor volume, equalization, membrane area — is guesswork.
| Parameter | Typical Resort Range (2026) | Design Basis for a 200-Room Hill Country Property |
|---|---|---|
| Influent BOD | 200–400 mg/L | 300 mg/L |
| Influent TSS | 150–300 mg/L | 250 mg/L |
| Influent FOG | 50–150 mg/L | 100 mg/L |
| Per-capita flow | 100–130 gpcd | 110 gpcd |
| Diurnal peaking factor | 2.0–2.5× | 2.5× |
| Average daily flow (200 keys × 2.5 occ × 110 gpcd) | — | 55,000 gpd (208 m³/day) |
| Peak instantaneous flow | — | ≈520 m³/day |
TCEQ, SAWS, and Edwards Aquifer Rules a Resort Must Clear

Three overlapping rule sets govern a San Antonio resort plant, and the equipment must be selected to satisfy all three simultaneously. SAWS commercial pretreatment limits set the floor for anything discharging to the municipal collection system: TSS ≤250 mg/L, BOD ≤250 mg/L, FOG ≤100 mg/L, pH 6.0–9.0 (per SAWS Sewer Use Ordinance, current 2025 revision). TCEQ 30 TAC §285 covers on-site sewage facilities (OSSF) for flows under 5,000 gpd, while TCEQ 30 TAC Chapter 317 governs conventional collection and treatment works above that threshold — Chapter 317 is the design criteria your engineer will cite for the basis-of-design report. Edwards Aquifer Authority rules (30 TAC §213) prohibit surface discharge within the recharge/contributing zones and require subsurface disposal plus disinfection to <14 cfu/100 mL fecal coliform. Reclaimed water for landscape irrigation or cooling-tower makeup must meet TCEQ Type I or Type II reuse standards with continuous disinfection — UV or chlorine dioxide, not chlorination alone — because chlorination alone does not satisfy reuse criteria when the holding time before reuse is short (per TCEQ 30 TAC §210 reuse rules, 2025).
| Authority / Rule | Applies To | Key Threshold | Engineering Implication |
|---|---|---|---|
| SAWS Sewer Use Ordinance | Discharge to SAWS collection | TSS ≤250 mg/L, BOD ≤250 mg/L, FOG ≤100 mg/L, pH 6.0–9.0 | Biological plant with FOG removal at headworks |
| TCEQ 30 TAC §285 | OSSF < 5,000 gpd | Aerobic treatment, subsurface disposal | Package plant + drip irrigation |
| TCEQ 30 TAC Chapter 317 | Conventional works > 5,000 gpd | Design criteria, operator licensing | Engineered basis-of-design report, Class C/D operator |
| Edwards Aquifer Authority 30 TAC §213 | Recharge / contributing zones | No surface discharge, <14 cfu/100 mL fecal coliform | Subsurface drip or reuse with continuous disinfection |
| TCEQ 30 TAC §210 | Reclaimed water for reuse | Type I/II reuse, UV or ClO₂ | MBR + UV, or SBR + ClO₂ for reuse-quality effluent |
Three Process Trains That Work for a San Antonio Resort
Three credible biological process trains cover the 2026 San Antonio resort market; the right pick depends on flow, site footprint, reuse intent, and operator availability. The WSZ buried package sewage treatment plant runs an A/O biological contact oxidation process in a single buried unit, 1–80 m³/h, requires no full-time operator, and can be installed under landscaping in a Hill Country service yard without breaking the visual envelope. The MBR membrane bioreactor system couples activated sludge with submerged PVDF ultrafiltration (0.1 μm nominal pore size), producing near-reuse effluent with TSS <10 mg/L and BOD <5 mg/L in roughly 60% of the footprint of a conventional activated-sludge plant. The SBR sequencing batch reactor runs timed fill/react/settle/decant cycles with a biological selector, has a well-proven track record at 50–500 m³/day, easier operator interface, and zero membrane replacement cost; the trade-off is larger equalization volume and tank footprint. For resorts with full-service kitchens, banquet halls, or on-site laundry, a DAF pre-treatment unit upstream of the biological stage drops TSS by 80–95% and removes the bulk of the FOG before it hits the biology — without DAF, free-floating grease coats the media in a WSZ or fouls the membrane in an MBR.
| Criterion | WSZ Package Plant | MBR | SBR |
|---|---|---|---|
| Flow range | 1–80 m³/h (≈25–1,900 m³/day) | 10–500+ m³/day | 50–500 m³/day |
| Effluent TSS / BOD | ≤30 / ≤30 mg/L | <10 / <5 mg/L | ≤20 / ≤20 mg/L |
| Reuse-ready effluent | No (needs tertiary) | Yes (UV/ClO₂ polish only) | Partial (needs tertiary) |
| Footprint | Smallest (buried) | ~60% of CAS footprint | Largest (batch tanks) |
| Operator skill | None full-time | Class C/D, membrane care | Class C/D, batch tuning |
| Best fit | <50 m³/day, tight site, no reuse | Reuse, Edwards Aquifier, tight sites | 50–500 m³/day, room for tanks, no reuse |
Sizing a 200-Room Hill Country Resort: Worked Example

For a 200-room Hill Country resort at 2.5 occupancy and 110 gpcd, the design average is 55,000 gpd (208 m³/day) with a 2.5× peak of 520 m³/day. With a 20% contingency for spa, pool backwash, and on-site laundry, the engineering specification rises to roughly 250 m³/day nominal and 600+ m³/day peak. A 220 m³/day MBR paired with a 4 m³ equalization basin absorbs the diurnal swing; a 30 m³/h DAF pre-treatment unit (ZSQ-30) drops the FOG and TSS load on the membrane to keep cleaning intervals reasonable. For disinfection, an on-site chlorine dioxide generator sized to the irrigation holding tank provides the residual needed for TCEQ Type II reuse without the THM formation risk of free chlorine. Sludge handling runs through a lamella clarifier thickener followed by a 5 m² plate-and-frame filter press — the plate-and-frame filter press produces a 22–28% dry-solids cake that can be hauled off-site as Class B biosolids. Total plant footprint is approximately 180 m² including the DAF skid, MBR tankage, sludge room, and disinfection contact basin, which fits inside a typical Hill Country service-yard enclosure with a 65 dB(A) sound-attenuation package. For engineers cross-checking against the Turkish market, the same MBR + DAF + ClO₂ topology is documented in our hotel wastewater system design in Ankara reference design, and the DAF sizing math is walked through in our DAF system process flow walkthrough.
Reuse or Dispose: The 2026 Economic Decision
San Antonio potable water rates are among the highest in Texas, and the reuse math for a 200-room resort is straightforward. Landscape irrigation on a Hill Country golf-view property can consume 30–50% of total resort water demand, and diverting MBR effluent to that irrigation loop recovers the offset directly on the SAWS bill. At 2026 commercial rates, the MBR CAPEX premium over an SBR or WSZ of the same nominal capacity pays back in 3–6 years at 200-room scale, before counting laundry reuse and cooling-tower makeup (Zhongsheng field data, 2026). The MBR membrane bioreactor system is the only process among the three that reliably produces reuse-quality water without a separate RO or advanced polishing step; the OPEX delta is roughly 0.3–0.5 kWh/m³ higher electricity for membrane aeration and backwash, partially offset by lower chemical consumption because biomass stays in the reactor longer. WSZ and SBR still meet SAWS disposal limits economically when the resort has no on-site landscape demand and prefers simpler operations. For Edwards Aquifer projects, the question is not really reuse vs disposal — it is MBR-with-UV vs SBR-with-ClO₂-and-subsurface-drip. Both are compliant; MBR is more compact and reuse-ready. Engineers weighing UV against ClO₂ for either path can compare residence time, residual stability, and THM formation in our ozone vs UV disinfection comparison.
Decision Framework: Picking the Right System for Your Property

Use the following four-question filter to converge on a process train in a single meeting with your engineer. Question one: average daily flow. Question two: reuse target (yes/no). Question three: site footprint and operator availability. Question four: Edwards Aquifer or standard SAWS discharge. Under 50 m³/day, tight site, no reuse target, the WSZ buried package plant is the lowest-CAPEX, lowest-operational-burden option and is fully automatic. Between 50 and 500 m³/day with a reuse target or an Edwards Aquifer constraint, the MBR with DAF pre-treatment and UV or ClO₂ disinfection is the engineering consensus choice. Between 50 and 500 m³/day with no reuse target and room for tanks, the SBR with DAF pre-treatment and chlorination is the lower-CAPEX path. Always pair the biological stage with an automatic chemical dosing skid for pH adjustment and coagulant, and a rotary mechanical bar screen at the headworks to protect downstream equipment from the rag and wipe load typical of resort plumbing. Engineers working on tropical or high-rainfall resort sites can compare similar process trains in our Costa Rica hotel wastewater engineering guide.
| Property Profile | Process Train | Pre-treatment | Disinfection | Notes |
|---|---|---|---|---|
| <50 m³/day, no reuse, tight site | WSZ buried package plant | Bar screen | Chlorination (disposal only) | Fully automatic, no full-time operator |
| 50–500 m³/day, reuse target or Edwards Aquifer | MBR | DAF + bar screen | UV or on-site ClO₂ | Reuse-ready effluent, ~180 m² footprint |
| 50–500 m³/day, no reuse, room for tanks | SBR | DAF + bar screen | Chlorination | Lower CAPEX, larger equalization volume |
| All configurations | — | Rotary bar screen + auto chemical dosing | — | Mandatory headworks for Texas resort loading |
Frequently Asked Questions
What design flow per room should a San Antonio resort use in 2026?
Use 110 gallons per capita per day (gpcd) at 2.5 occupants per occupied room, which yields 275 gpcd per occupied key; apply a 2.5× peaking factor for the instantaneous hydraulic load and add 10–20% contingency for spa, pool backwash, and laundry. This per TCEQ Chapter 317 design basis.
Which SAWS pretreatment limits apply to a commercial resort discharge?
Discharge to the SAWS collection system must meet TSS ≤250 mg/L, BOD ≤250 mg/L, FOG ≤100 mg/L, and pH 6.0–9.0 (per SAWS Sewer Use Ordinance, 2025 revision). A DAF pre-treatment unit is the standard way to bring FOG under the 100 mg/L ceiling.
Is an MBR required for reuse at a Hill Country resort?
An MBR is the only process among the three credible 2026 trains (WSZ, MBR, SBR) that produces reuse-quality effluent without a separate RO polishing step — typical MBR effluent is TSS <10 mg/L and BOD <5 mg/L, which meets TCEQ Type II reuse after UV or ClO₂ disinfection.
What TCEQ chapter governs a 200-room resort wastewater system?
30 TAC Chapter 317 governs conventional collection and treatment works above 5,000 gpd, which covers virtually every 200-room resort. Properties inside the Edwards Aquifer recharge or contributing zones also fall under 30 TAC §213, which mandates subsurface disposal and <14 cfu/100 mL fecal coliform.